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Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


1

Process for production of synthesis gas with reduced sulfur content  

DOE Patents [OSTI]

A process for the partial oxidation of a sulfur- and silicate-containing carbonaceous fuel to produce a synthesis gas with reduced sulfur content which comprises partially oxidizing said fuel at a temperature in the range of 1800.degree.-2200.degree. F. in the presence of a temperature moderator, an oxygen-containing gas and a sulfur capture additive which comprises an iron-containing compound portion and a sodium-containing compound portion to produce a synthesis gas comprising H.sub.2 and CO with a reduced sulfur content and a molten slag which comprises (i) a sulfur-containing sodium-iron silicate phase and (ii) a sodium-iron sulfide phase. The sulfur capture additive may optionally comprise a copper-containing compound portion.

Najjar, Mitri S. (Hopewell Junction, NY); Corbeels, Roger J. (Wappingers Falls, NY); Kokturk, Uygur (Wappingers Falls, NY)

1989-01-01T23:59:59.000Z

2

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales...  

Gasoline and Diesel Fuel Update (EIA)

200 Energy Information AdministrationPetroleum Marketing Annual 1998 Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District (Cents per Gallon...

3

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales...  

Gasoline and Diesel Fuel Update (EIA)

200 Energy Information AdministrationPetroleum Marketing Annual 1999 Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District (Cents per Gallon...

4

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales...  

Gasoline and Diesel Fuel Update (EIA)

Energy Information Administration Petroleum Marketing Annual 1995 Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District (Cents per Gallon...

5

The sulfur content of volcanic gases on Mars Fabrice Gaillard, a  

E-Print Network [OSTI]

principles, we model here the likely sulfur contents of (1) the martian and terrestrial mantles and (2 a denser atmosphere are shown to be dominated by CO ± CO2 and H2 ± H2O species, depending on fO2, sulfur by H2S, which should have favored the acidification of any persistent water layer. The calculated

Boyer, Edmond

6

Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities  

U.S. Energy Information Administration (EIA) Indexed Site

(Percent) (Percent) Type: Sulfur Content API Gravity Period: Monthly Annual Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Show Data By: Type Area Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 View History U.S. 1.43 1.38 1.41 1.43 1.47 1.42 1985-2013 PADD 1 0.75 0.73 0.69 0.68 0.73 0.68 1985-2013 East Coast 0.67 0.66 0.61 0.63 0.66 0.57 1985-2013 Appalachian No. 1 2.0 1.72 1.52 1.40 1.55 1.74 1985-2013 PADD 2 1.42 1.34 1.44 1.46 1.61 1.49 1985-2013 Ind., Ill. and Ky. 1.45 1.36 1.47 1.56 1.75 1.67 1985-2013 Minn., Wis., N. Dak., S. Dak. 2.33 2.11 2.18 2.03 2.01 1.69 1985-2013 Okla., Kans., Mo. 0.89 0.89 0.92 0.82 0.87 0.85 1985-2013 PADD 3 1.54 1.48 1.51 1.52 1.54 1.48 1985-2013

7

Table 17. U.S. No. 2 Diesel Fuel Prices by Sulfur Content and...  

Gasoline and Diesel Fuel Update (EIA)

EIA-782B, "Resellers'Retailers' Monthly Petroleum Product Sales Report." 17. U.S. No. 2 Diesel Fuel Prices by Sulfur Content and Sales Type Energy Information Administration ...

8

,"Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities"  

U.S. Energy Information Administration (EIA) Indexed Site

Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities" Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Sulfur Content, Weighted Average Refinery Crude Oil Input Qualities",16,"Monthly","9/2013","1/15/1985" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_pnp_crq_a_epc0_ycs_pct_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_crq_a_epc0_ycs_pct_m.htm" ,"Source:","Energy Information Administration"

9

U.S. Coal Reserves: An Update by Heat and Sulfur Content  

Gasoline and Diesel Fuel Update (EIA)

2) 2) Distribution Category UC-98 U.S. Coal Reserves: An Update by Heat and Sulfur Content February 1993 Energy Information Administration Office of Coal, Nuclear, Electric and Alternate Fuels U.S. Department of Energy Washington, DC 20585 Energy Information Administration/ U.S. Coal Reserves: An Update by Heat and Sulfur Content ii This report was prepared by the Energy Information Administration, the independent statistical and analytical agency within the Department of Energy. The information contained herein should not be construed as advocating or reflecting any policy position of the Department of Energy or of any other organization. Energy Information Administration/ U.S. Coal Reserves: An Update by Heat and Sulfur Content iii Contacts This report was prepared by the staff of the Energy

10

Effects of Fuel Sulfur Content and Diesel Oxidation Catalyst on PM Emitted from Light-Duty Diesel Engine  

Science Journals Connector (OSTI)

This work aims at the particle number concentrations and size distributions, sulfate and trace metals emitted from a diesel engine fueled with three different sulfur content fuels, operating with and without DOC. ... Figure 2. Sulfate emission rate and fuel consumption as a function of sulfur content at engine speed of 2690 rpm. ... Thus, the use of low metal fuels and lubricating oil is as important to the environment and human health as low sulfur fuels, especially for engines with after-treatment devices. ...

Hong Zhao; Yunshan Ge; Xiaochen Wang; Jianwei Tan; Aijuan Wang; Kewei You

2010-01-05T23:59:59.000Z

11

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales...  

Gasoline and Diesel Fuel Update (EIA)

80.8 75.7 76.2 67.5 71.8 77.4 83.7 75.0 64.4 See footnotes at end of table. 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District 242 Energy Information...

12

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales...  

Annual Energy Outlook 2013 [U.S. Energy Information Administration (EIA)]

74.4 73.3 70.4 60.5 69.0 71.9 77.8 71.0 60.5 See footnotes at end of table. 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District 242 Energy Information...

13

Microchannel Distillation of JP-8 Jet Fuel for Sulfur Content Reduction  

SciTech Connect (OSTI)

In microchannel based distillation processes, thin vapor and liquid films are contacted in small channels where mass transfer is diffusion-limited. The microchannel architecture enables improvements in distillation processes. A shorter height equivalent of a theoretical plate (HETP) and therefore a more compact distillation unit can be achieved. A microchannel distillation unit was used to produce a light fraction of JP-8 fuel with reduced sulfur content for use as feed to produce fuel-cell grade hydrogen. The HETP of the microchannel unit is discussed, as well as the effects of process conditions such as feed temperature, flow rate, and reflux ratio.

Zheng, Feng; Stenkamp, Victoria S.; TeGrotenhuis, Ward E.; Huang, Xiwen; King, David L.

2006-09-16T23:59:59.000Z

14

Estimates of central Appalachian coal reserves by cost of production and sulfur content  

SciTech Connect (OSTI)

This study provides information on the quantity, quality, and production costs for all minable coal reserves in the major coal-producing counties of central Appalachia, a region that contains the large majority of low-sulfur and compliance coal reserves in the eastern US. Presently, the best source of detailed reserve information in the Appalachian region is the estimates produced by the mining and land holding companies that control the reserves. The authors have been able to obtain overall reserve estimates based on the detailed geological and engineering studies conducted by these companies. In areas where this information does not exist, the authors have relied on published estimates of reserves and modified these estimates based on known conditions on surrounding properties. This reserve information has been combined with data on coal quality and mining costs to produce cost curves for all minable coal reserves by sulfur content. Results to date indicate that most of the major coal-producing counties in central Appalachia will be able to increase production levels significantly on a sustainable basis for at least the next 20 years, without major real increases in coal prices.

Watkins, J.

1988-08-01T23:59:59.000Z

15

Process for alternately steam reforming sulfur containing hydrocarbons that vary in oxygen content  

SciTech Connect (OSTI)

In the hydrotreating and steam reforming of an oxygen and sulfur bearing hydrocarbon fuel, the oxygen is first removed in an oxidizer containing a bed of platinum catalyst, the inlet temperature being well below 1000/sup 0/F and preferably on the order of 300/sup 0/F. The sulfur in the fuel does not harm the oxidizer catalyst and may be removed downstream by known hydrodesulfurization techniques prior to reforming. A process is described for removing oxygen from an oxygen and sulfur bearing hydrocarbon fuel, such as peak shared natural gas, upstream in the process so that sulfur can be removed later. The fuel and some hydrogen are introduced into an oxidizer at a temperature of 350/sup 0/F or less down to the minimum ignition temperature. The oxidizer consists of a platinum bed catalyst which catalyzes the oxidation of the oxygen to water with accompanying heat release to raise the exit gas temperature to less than 650/sup 0/F. The temperature desorbs the sulfur from the catalyst, and the exit gases are passed downstream to nickel subsulfide or molybdenum desfulfide catalysts where the hydrosulfurization process takes place. (BLM)

Lesieur, R.R.; Setzer, H.J.; Hawkins, J.R.

1980-01-01T23:59:59.000Z

16

Extension of an Artificial Neural Network Algorithm for Estimating Sulfur Content of Sour Gases at Elevated Temperatures and Pressures  

Science Journals Connector (OSTI)

Extension of an Artificial Neural Network Algorithm for Estimating Sulfur Content of Sour Gases at Elevated Temperatures and Pressures ... (1, 39) The i neuron within the hidden k layer performs the following tasks: summation of the arriving weighted inputs and propagations of the resulting summation through an activation function, f, to the adjacent neurons of the next hidden layer or to the output neuron(s). ... This work deals with the potential application of artificial neural networks (ANN) to represent PVT data within their exptl. ...

Mehdi Mehrpooya; Amir H. Mohammadi; Dominique Richon

2009-11-19T23:59:59.000Z

17

Direct Determination of Pyrite Content in Argonne Premium Coals by the Use of Sulfur X-ray Near Edge Absorption Spectroscopy (S-XANES)  

Science Journals Connector (OSTI)

Direct Determination of Pyrite Content in Argonne Premium Coals by the Use of Sulfur X-ray Near Edge Absorption Spectroscopy (S-XANES) ... Argonne National Laboratory, Argonne, Illinois 60439 ... Argonne premium coal samples are used by researchers worldwide as standards in coal research. ...

Trudy B. Bolin

2010-10-01T23:59:59.000Z

18

Phosphorothioate Oligonucleotides with Low Phosphate Diester Content:? Greater than 99.9% Sulfurization Efficiency with Aged Solutions of Phenylacetyl Disulfide (PADS)  

Science Journals Connector (OSTI)

Phosphorothioate Oligonucleotides with Low Phosphate Diester Content:? Greater than 99.9% Sulfurization Efficiency with Aged Solutions of Phenylacetyl Disulfide (PADS) ... Modified oligonucleotides as modulators of gene expression are currently under intense investigation as novel therapeutic agents of high specificity through antisense mechanisms of action.1 Among the oligonucleotide modifications reported to date, phosphorothioate (PS) oligonucleotides, where one nonbridging oxygen of the internucleotide linkage is replaced by a sulfur atom, are the first class of antisense therapeutics to get marketing approval by regulatory agencies. ... Incomplete sulfurization during solid-phase synthesis of PS-oligonucleotides using phosphoramidite chemistry was identified as the cause of formation of two new classes of process-related oligonucleotide impurities containing a DMTr-C-phosphonate moiety. ...

Achim H. Krotz; Dennis Gorman; Paul Mataruse; Craig Foster; James D. Godbout; Christopher C. Coffin; Anthony N. Scozzari

2004-10-20T23:59:59.000Z

19

Assessment of the impacts on health due to the emissions of Cuban power plants that use fossil fuel oils with high content of sulfur. Estimation of external costs  

Science Journals Connector (OSTI)

Fossil fuel electricity generation has been demonstrated to be a main source of atmospheric pollution. The necessity of finding out a balance between the costs of achieving a lower level of environmental and health injury and the benefits of providing electricity at a reasonable cost have lead to the process of estimating the external costs derived from these impacts and not included in the electricity prices as a quantitative measure of it that, even when there are large uncertainties involved, can be used by decision makers in the process of achieving a global sustainable development. The external costs of the electricity generation in three Cuban power plants that use fossil fuel oils with high sulfur content have been assessed. With that purpose a specific implementation of the Impact Pathways Methodology for atmospheric emissions was developed. Dispersion of atmospheric pollutants is modeled at local and regional scales in a detailed way. Health impacts include mortality and those morbidity effects that showed relation with the increment of selected pollutant concentration in national studies. The external cost assessed for the three plants was 40,588,309USDyr?1 (min./max.: 10,194,833/169,013,252), representing 1.06USDCentkWh?1. Costs derived from sulfur species (SO2 and sulfate aerosol) stand for 93% of the total costs.

L. Turts Carbonell; E. Meneses Ruiz; M. Snchez Gcita; J. Rivero Oliva; N. Daz Rivero

2007-01-01T23:59:59.000Z

20

Two stage sorption of sulfur compounds  

DOE Patents [OSTI]

A two stage method for reducing the sulfur content of exhaust gases is disclosed. Alkali- or alkaline-earth-based sorbent is totally or partially vaporized and introduced into a sulfur-containing gas stream. The activated sorbent can be introduced in the reaction zone or the exhaust gases of a combustor or a gasifier. High efficiencies of sulfur removal can be achieved.

Moore, William E. (Manassas, VA)

1992-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


21

Sulfur capture in combination bark boilers  

SciTech Connect (OSTI)

A review of sulfur dioxide emission data for eight combination bark boilers in conjunction with the sulfur contents of the fuels reveals significant sulfur capture ranging from 10% to over 80% within the solid ash phase. Wood ash characteristics similar to activated carbon as well as the significant wood ash alkali oxide and carbonate fractions are believed responsible for the sulfur capture. Sulfur emissions from combination bark-fossil fuel firing are correlated to the sulfur input per ton of bark or wood residue fired.

Someshwar, A.V.; Jain, A.K. (National Council of the Paper Industry for Air and Stream Improvement, Gainesville, FL (United States))

1993-07-01T23:59:59.000Z

22

SULFUR-TOLERANT CATALYST FOR THE SOLID OXIDE FUEL CELL.  

E-Print Network [OSTI]

??JP-8 fuel is easily accessible, transportable, and has hydrogen content essential to solid oxide fuel cell (SOFC) operation. However, this syngas has sulfur content which (more)

Bozeman, Joe Frank, III

2010-01-01T23:59:59.000Z

23

Using ISC & GIS to predict sulfur deposition from coal-fired power plants  

E-Print Network [OSTI]

The goal of this research project was to determine if atmospheric sources have the potential of contributing significantly to the sulfur content of grazed forage. Sulfur deposition resulting from sulfur dioxide emissions from coal- fired power...

Lopez, Jose Ignacio

2012-06-07T23:59:59.000Z

24

CONTENTS  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Operations Office RPD relative percent difference RSD relative standard deviation TIC tentatively identified compound DOERL-96-68, HASQARD Table of Contents, Rev. 3 Volume...

25

CONTENTS  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

3.0 - CRITICAL, SPECIAL, & ENGINEERED LIFTS March 21, 2013 Rev 1 Page 1 CHAPTER 3.0 TABLE OF CONTENTS 3.0 CRITICAL LIFTS ......

26

CONTENTS  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

assurancecontrol) 3. Responsible operations manager 4. Equipment custodian 5. Cognizant engineer. *Reviewapproval is mandatory. 18.3.3 Hostile Environment Plan Contents The plan...

27

CONTENTS  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

CONTENTS CONTENTS Introduction ........................................................................................................3 ON THE HORIZON: Promising Research Efforts Currently Underway A Smarter Charge .........................................................................................4 Unlocking Fire Ice .........................................................................................5 CRISP Crunches Cyber Threats ....................................................................6 Gel Zeroes in on Cancer ...............................................................................7 Liquid Solvent: A Solid Solution for CO 2 .....................................................8 Real-time Grid Stability ................................................................................9

28

Graphene-wrapped sulfur nanospheres with ultra-high sulfur loading for high energy density lithiumsulfur batteries  

Science Journals Connector (OSTI)

Abstract Lithiumsulfur (LiS) battery with high theoretical energy density is one of the most promising energy storage systems for electric vehicles and intermittent renewable energy. However, due to the poor conductivity of the active material, considerable weight of the electrode is occupied by the conductive additives. Here we report a graphene-wrapped sulfur nanospheres composite (S-nanosphere@G) with sulfur content up to 91wt% as the high energy density cathode material for LiS battery. The sulfur nanospheres with diameter of 400500nm are synthesized through a solution-based approach with the existence of polyvinylpyrrolidone (PVP). Then the sulfur nanospheres are uniformly wrapped by conductive graphene sheets through the electrostatic interaction between graphene oxide and PVP, followed by reducing of graphene oxide with hydrazine. The design of graphene wrapped sulfur nanoarchitecture provides flexible conductive graphene coating with void space to accommodate the volume expansion of sulfur and to minimize polysulfide dissolution. As a result, the S-nanosphere@G nanocomposite with 91wt% sulfur shows a reversible initial capacity of 970mAhg?1 and an average columbic efficiency>96% over 100 cycles at a rate of 0.2C. Taking the total mass of electrode into account, the S-nanosphere@G composite is a promising cathode material for high energy density LiS batteries.

Ya Liu; Jinxin Guo; Jun Zhang; Qingmei Su; Gaohui Du

2015-01-01T23:59:59.000Z

29

System for adding sulfur to a fuel cell stack system for improved fuel cell stability  

DOE Patents [OSTI]

A system for adding sulfur to a reformate stream feeding a fuel cell stack, having a sulfur source for providing sulfur to the reformate stream and a metering device in fluid connection with the sulfur source and the reformate stream. The metering device injects sulfur from the sulfur source to the reformate stream at a predetermined rate, thereby providing a conditioned reformate stream to the fuel cell stack. The system provides a conditioned reformate stream having a predetermined sulfur concentration that gives an acceptable balance of minimal drop in initial power with the desired maximum stability of operation over prolonged periods for the fuel cell stack.

Mukerjee, Subhasish; Haltiner, Jr., Karl J; Weissman, Jeffrey G

2013-08-13T23:59:59.000Z

30

Offshore Sulfur Comes In  

Science Journals Connector (OSTI)

Offshore Sulfur Comes In ... "The deposit is a major new source of sulfur," say Hines H. Baker, president of Humble Oil, and Langbourne M. Williams, president of Freeport Sulphur. ... Humble's deposit, known as Grand Isle (Block 18), was discovered in the course of offshore oil exploration and it ranks among the most important sulfur discoveries of recent years. ...

1956-10-01T23:59:59.000Z

31

The reaction kinetics of gasoline sulfur compounds: Catalytic mechanisms for sulfur reduction  

SciTech Connect (OSTI)

One of the key elements of reformulated gasoline is the reduction of the sulfur compounds produced by fluid catalytic cracking. This paper probes the reaction kinetics of refractory gasoline-range thiophene derivatives (thiophene, tetrahydrothiophene, and alkylthiophenes) in an effort to determine the mechanisms of sulfur compound cracking in the FCC unit. The gasoline-range sulfur compounds were analyzed using gas chromatography with an atomic emission detector. The authors` results show that the FCC catalysts affects the cracking of sulfur compounds through both hydrogen transfer and zeolite pore restriction mechanisms. An experimental FCC catalyst is shown to reduce gasoline sulfur content in the Davidson Circulating Riser (DCR{sup TM}) pilot unit. Model compound tests show that the activity of the catalyst is due to both its catalytic and adsorptive properties. Tetrahydrothiophene, which is produced from thiophenes by hydrogen transfer, is completely removed by the experimental catalyst.

Harding, R.H.; Gatte, R.R.; Albro, T.G.; Wormsbecher, R.F. [W.R. Grace & Co. Conn, Columbia, MD (United States)

1993-12-31T23:59:59.000Z

32

Abatement of Air Pollution: Control of Sulfur Compound Emissions  

Broader source: Energy.gov (indexed) [DOE]

Abatement of Air Pollution: Control of Sulfur Compound Emissions Abatement of Air Pollution: Control of Sulfur Compound Emissions (Connecticut) Abatement of Air Pollution: Control of Sulfur Compound Emissions (Connecticut) < Back Eligibility Agricultural Commercial Construction Fed. Government Fuel Distributor General Public/Consumer Industrial Installer/Contractor Institutional Investor-Owned Utility Local Government Low-Income Residential Multi-Family Residential Municipal/Public Utility Nonprofit Residential Retail Supplier Rural Electric Cooperative Schools State/Provincial Govt Systems Integrator Transportation Tribal Government Utility Program Info State Connecticut Program Type Environmental Regulations Provider Department of Energy and Environmental Protection These regulations set limits on the sulfur content of allowable fuels (1.0%

33

ADVANCED SULFUR CONTROL CONCEPTS  

SciTech Connect (OSTI)

Conventional sulfur removal in integrated gasification combined cycle (IGCC) power plants involves numerous steps: COS (carbonyl sulfide) hydrolysis, amine scrubbing/regeneration, Claus process, and tail-gas treatment. Advanced sulfur removal in IGCC systems involves typically the use of zinc oxide-based sorbents. The sulfides sorbent is regenerated using dilute air to produce a dilute SO{sub 2} (sulfur dioxide) tail gas. Under previous contracts the highly effective first generation Direct Sulfur Recovery Process (DSRP) for catalytic reduction of this SO{sub 2} tail gas to elemental sulfur was developed. This process is currently undergoing field-testing. In this project, advanced concepts were evaluated to reduce the number of unit operations in sulfur removal and recovery. Substantial effort was directed towards developing sorbents that could be directly regenerated to elemental sulfur in an Advanced Hot Gas Process (AHGP). Development of this process has been described in detail in Appendices A-F. RTI began the development of the Single-step Sulfur Recovery Process (SSRP) to eliminate the use of sorbents and multiple reactors in sulfur removal and recovery. This process showed promising preliminary results and thus further process development of AHGP was abandoned in favor of SSRP. The SSRP is a direct Claus process that consists of injecting SO{sub 2} directly into the quenched coal gas from a coal gasifier, and reacting the H{sub 2}S-SO{sub 2} mixture over a selective catalyst to both remove and recover sulfur in a single step. The process is conducted at gasifier pressure and 125 to 160 C. The proposed commercial embodiment of the SSRP involves a liquid phase of molten sulfur with dispersed catalyst in a slurry bubble-column reactor (SBCR).

Apostolos A. Nikolopoulos; Santosh K. Gangwal; William J. McMichael; Jeffrey W. Portzer

2003-01-01T23:59:59.000Z

34

Sulfur@Carbon Cathodes for Lithium Sulfur Batteries > Research...  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Electrode Channel Flow DEMS Cell Sulfur@Carbon Cathodes for Lithium Sulfur Batteries Better Ham & Cheese: Enhanced Anodes and Cathodes for Fuel Cells Epitaxial Single...

35

Sulfur-Graphene Oxide Nanocomposite Cathodes for Lithium/Sulfur...  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Advanced Materials Advanced Materials Find More Like This Return to Search Sulfur-Graphene Oxide Nanocomposite Cathodes for LithiumSulfur Cells Lawrence Berkeley National...

36

Elemental sulfur recovery process  

DOE Patents [OSTI]

An improved catalytic reduction process for the direct recovery of elemental sulfur from various SO[sub 2]-containing industrial gas streams. The catalytic process provides combined high activity and selectivity for the reduction of SO[sub 2] to elemental sulfur product with carbon monoxide or other reducing gases. The reaction of sulfur dioxide and reducing gas takes place over certain catalyst formulations based on cerium oxide. The process is a single-stage, catalytic sulfur recovery process in conjunction with regenerators, such as those used in dry, regenerative flue gas desulfurization or other processes, involving direct reduction of the SO[sub 2] in the regenerator off gas stream to elemental sulfur in the presence of a catalyst. 4 figures.

Flytzani-Stephanopoulos, M.; Zhicheng Hu.

1993-09-07T23:59:59.000Z

37

Chapter 11 - Sulfur Recovery  

Science Journals Connector (OSTI)

Abstract Sulfur is present in many raw industrial gases and in natural gas in the form of hydrogen sulfide. Sulfur removal facilities are located at the majority of oil and gas processing facilities throughout the world. The sulfur recovery unit does not make a profit for the operator but it is an essential processing step to allow the overall facility to operate, as the discharge of sulfur compounds to the atmosphere is severely restricted by environmental regulations. Concentration levels of H2S vary significantly depending upon their source. H2S produced from absorption processes, such as amine treating of natural gas or refinery gas, can contain 5075% H2S by volume or higher. This chapter provides information about fundamentals of sulfur removal facilities in the natural gas industry.

Alireza Bahadori

2014-01-01T23:59:59.000Z

38

Bacterial Sulfur Storage Globules  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

by I. J. Pickering and G. N. George by I. J. Pickering and G. N. George Sulfur is essential for all life, but it plays a particularly central role in the metabolism of many anaerobic microorganisms. Prominent among these are the sulfide-oxidizing bacteria that oxidize sulfide (S2-) to sulfate (SO42-). Many of these organisms can store elemental sulfur (S0) in "globules" for use when food is in short supply (Fig. 1). The chemical nature of the sulfur in these globules has been an enigma since they were first described as far back as 1887 (1); all known forms (or allotropes) of elemental sulfur are solid at room temperature, but globule sulfur has been described as "liquid", and it apparently has a low density – 1.3 compared to 2.1 for the common yellow allotrope a-sulfur. Various exotic forms of sulfur have been proposed to explain these properties, including micelles (small bubble-like structures) formed from long-chain polythionates, but all of these deductions have been based upon indirect evidence (for example the density was estimated by flotation of intact cells), and many questions remained.

39

System for adding sulfur to a fuel cell stack system for improved fuel cell stability  

DOE Patents [OSTI]

A system for adding sulfur to a fuel cell stack, having a reformer adapted to reform a hydrocarbon fuel stream containing sulfur contaminants, thereby providing a reformate stream having sulfur; a sulfur trap fluidly coupled downstream of the reformer for removing sulfur from the reformate stream, thereby providing a desulfurized reformate stream; and a metering device in fluid communication with the reformate stream upstream of the sulfur trap and with the desulfurized reformate stream downstream of the sulfur trap. The metering device is adapted to bypass a portion of the reformate stream to mix with the desulfurized reformate stream, thereby producing a conditioned reformate stream having a predetermined sulfur concentration that gives an acceptable balance of minimal drop in initial power with the desired maximum stability of operation over prolonged periods for the fuel cell stack.

Mukerjee, Subhasish (Pittsford, NY); Haltiner, Jr., Karl J (Fairport, NY); Weissman, Jeffrey G. (West Henrietta, NY)

2012-03-06T23:59:59.000Z

40

Demand, Supply, and Price Outlook for Low-Sulfur Diesel Fuel  

Gasoline and Diesel Fuel Update (EIA)

To help ensure that sulfates in engine exhaust do not To help ensure that sulfates in engine exhaust do not prevent manufacturers of heavy-duty diesel engines from meeting new particulate emissions standards for 1994 and later model years, 1 the Clean Air Act Amend- ments of 1990 (CAAA90) require refiners to reduce the sulfur content of on-highway diesel fuel from current average levels of 0.30 percent by weight to no more than 0.05 percent by weight. The new standard, which goes into effect October 1, 1993, also requires that on-highway diesel fuel have a minimum cetane index of 40 or a maximum aromatic content of 35 percent by volume. 2 (See list of terms and definitions on the fol- lowing page.) This provision is designed to prevent any future rises in aromatics levels. 3 Since the direct mea- surement of aromatics is complex, a minimum cetane

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


41

Low temperature fracture evaluation of plasticized sulfur paving mixtures  

E-Print Network [OSTI]

May 1985 Major Subject: Civil Engineering LOW TEMPERATURE FRACTURE EVALUATION OF PLASTICIZED SULFUR PAVING MIXTURES A Thesis by KAMYAR MAHBOUB Approved as to style and content by: Dallas N. Li tie (Chai rman of Committee) Ro e . Lytto Member... modifications to the standard ASTM procedure. These modifications were required due to the nature of plasticized sulfur mixtures and asphalt cement mixtures. The J-integral version of Paris ' law was successfully used to characterize the fatigue...

Mahboub, Kamyar

2012-06-07T23:59:59.000Z

42

Freeport Begins Offshore Sulfur Plant  

Science Journals Connector (OSTI)

Freeport Begins Offshore Sulfur Plant ... Discovered by Humble Oil & Refining, the sulfur deposit off Grand Isle is believed by industry observers to be one of the largest discovered in recent years. ...

1958-07-07T23:59:59.000Z

43

An Aerosol Condensation Model for Sulfur Trioxide  

SciTech Connect (OSTI)

This document describes a model for condensation of sulfuric acid aerosol given an initial concentration and/or source of gaseous sulfur trioxide (e.g. fuming from oleum). The model includes the thermochemical effects on aerosol condensation and air parcel buoyancy. Condensation is assumed to occur heterogeneously onto a preexisting background aerosol distribution. The model development is both a revisiting of research initially presented at the Fall 2001 American Geophysical Union Meeting [1] and a further extension to provide new capabilities for current atmospheric dispersion modeling efforts [2]. Sulfuric acid is one of the most widely used of all industrial chemicals. In 1992, world consumption of sulfuric acid was 145 million metric tons, with 42.4 Mt (mega-tons) consumed in the United States [10]. In 2001, of 37.5 Mt consumed in the U.S., 74% went into producing phosphate fertilizers [11]. Another significant use is in mining industries. Lawuyi and Fingas [7] estimate that, in 1996, 68% of use was for fertilizers and 5.8% was for mining. They note that H{sub 2}SO{sub 4} use has been and should continue to be very stable. In the United States, the elimination of MTBE (methyl tertiary-butyl ether) and the use of ethanol for gasoline production are further increasing the demand for petroleum alkylate. Alkylate producers have a choice of either a hydrofluoric acid or sulfuric acid process. Both processes are widely used today. Concerns, however, over the safety or potential regulation of hydrofluoric acid are likely to result in most of the growth being for the sulfuric acid process, further increasing demand [11]. The implication of sulfuric acid being a pervasive industrial chemical is that transport is also pervasive. Often, this is in the form of oleum tankers, having around 30% free sulfur trioxide. Although sulfuric acid itself is not a volatile substance, fuming sulfuric acid (referred to as oleum) is [7], the volatile product being sulfur trioxide. Sulfate aerosols and mist may form in the atmosphere on tank rupture. From chemical spill data from 1990-1996, Lawuyi02 and Fingas [7] prioritize sulfuric acid as sixth most serious. During this period, they note 155 spills totaling 13 Mt, out of a supply volume of 3700 Mt. Lawuyi and Fingas [7] summarize information on three major sulfuric acid spills. On 12 February 1984, 93 tons of sulfuric acid were spilled when 14 railroad cars derailed near MacTier, Parry Sound, Ontario. On 13 December 1978, 51 railroad cars derailed near Springhill, Nova Scotia. One car, containing 93% sulfuric acid, ruptured, spilling nearly its entire contents. In July 1993, 20 to 50 tons of fuming sulfuric acid spilled at the General Chemical Corp. plant in Richmond, California, a major industrial center near San Francisco. The release occurred when oleum was being loaded into a nonfuming acid railroad tank car that contained only a rupture disk as a safety device. The tank car was overheated and this rupture disk blew. The resulting cloud of sulfuric acid drifted northeast with prevailing winds over a number of populated areas. More than 3,000 people subsequently sought medical attention for burning eyes, coughing, headaches, and nausea. Almost all were treated and released on the day of the spill. By the day after the release, another 5,000 people had sought medical attention. The spill forced the closure of five freeways in the region as well as some Bay Area Rapid Transit System stations. Apart from corrosive toxicity, there is the additional hazard that the reactions of sulfur trioxide and sulfuric acid vapors with water are extremely exothermic [10, 11]. While the vapors are intrinsically denser than air, there is thus the likelihood of strong, warming-induced buoyancy from reactions with ambient water vapor, water-containing aerosol droplets, and wet environmental surface. Nordin [12] relates just such an occurrence following the Richmond, CA spill, with the plume observed to rise to 300 m. For all practical purposes, sulfur trioxide was the constituent released from the heated tank

Grant, K E

2008-02-07T23:59:59.000Z

44

SULFUR POLYMER ENCAPSULATION.  

SciTech Connect (OSTI)

Sulfur polymer cement (SPC) is a thermoplastic polymer consisting of 95 wt% elemental sulfur and 5 wt% organic modifiers to enhance long-term durability. SPC was originally developed by the U.S. Bureau of Mines as an alternative to hydraulic cement for construction applications. Previous attempts to use elemental sulfur as a construction material in the chemical industry failed due to premature degradation. These failures were caused by the internal stresses that result from changes in crystalline structure upon cooling of the material. By reacting elemental sulfur with organic polymers, the Bureau of Mines developed a product that successfully suppresses the solid phase transition and significantly improves the stability of the product. SPC, originally named modified sulfur cement, is produced from readily available, inexpensive waste sulfur derived from desulfurization of both flue gases and petroleum. The commercial production of SPC is licensed in the United States by Martin Resources (Odessa, Texas) and is marketed under the trade name Chement 2000. It is sold in granular form and is relatively inexpensive ({approx}$0.10 to 0.12/lb). Application of SPC for the treatment of radioactive, hazardous, and mixed wastes was initially developed and patented by Brookhaven National Laboratory (BNL) in the mid-1980s (Kalb and Colombo, 1985; Colombo et al., 1997). The process was subsequently investigated by the Commission of the European Communities (Van Dalen and Rijpkema, 1989), Idaho National Engineering Laboratory (Darnell, 1991), and Oak Ridge National Laboratory (Mattus and Mattus, 1994). SPC has been used primarily in microencapsulation applications but can also be used for macroencapsulation of waste. SPC microencapsulation has been demonstrated to be an effective treatment for a wide variety of wastes, including incinerator hearth and fly ash; aqueous concentrates such as sulfates, borates, and chlorides; blowdown solutions; soils; and sludges. It is not recommended for treatment of wastes containing high concentrations of nitrates because of potentially dangerous reactions between sulfur, nitrate, and trace quantities of organics. Recently, the process has been adapted for the treatment of liquid elemental mercury and mercury contaminated soil and debris.

KALB, P.

2001-08-22T23:59:59.000Z

45

Why sequence Alkaliphilic sulfur oxidizing bacteria for sulfur pollution  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Alkaliphilic sulfur oxidizing Alkaliphilic sulfur oxidizing bacteria for sulfur pollution remediation? Burning sulfur-containing fuels, such as coal, oil, and natural gas, contributes significantly to global environmental problems, such as air pollution and acid rain, besides contributing to the loss of the ozone layer. One method of managing sulfur compounds released as byproducts from industrial processes is to scrub them out using chemical treatments and activated charcoal beds. A lower-cost solution relies on incorporating alkaliphic sulfur-oxidizing bacteria into biofilters to convert the volatile and toxic compounds into insoluble sulfur for easier removal. Discovered in the last decade, these bacteria have been found to thrive in habitats that span the full pH range. The bacteria could have applications

46

It's Elemental - The Element Sulfur  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Phosphorus Phosphorus Previous Element (Phosphorus) The Periodic Table of Elements Next Element (Chlorine) Chlorine The Element Sulfur [Click for Isotope Data] 16 S Sulfur 32.065 Atomic Number: 16 Atomic Weight: 32.065 Melting Point: 388.36 K (115.21°C or 239.38°F) Boiling Point: 717.75 K (444.60°C or 832.28°F) Density: 2.067 grams per cubic centimeter Phase at Room Temperature: Solid Element Classification: Non-metal Period Number: 3 Group Number: 16 Group Name: Chalcogen What's in a name? From the Sanskrit word sulvere and the Latin word sulphurium. Say what? Sulfur is pronounced as SUL-fer. History and Uses: Sulfur, the tenth most abundant element in the universe, has been known since ancient times. Sometime around 1777, Antoine Lavoisier convinced the rest of the scientific community that sulfur was an element. Sulfur is a

47

Why sequence purple sulfur bacteria?  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

purple sulfur bacteria? purple sulfur bacteria? The process by which plants and some bacteria can convert light energy to sugar, or photosynthesis, is crucial to global food webs, and complicated. Very little is known about the photosynthetic bacteria in the purple sulfur bacteria group, which may represent one of the most primitive photosynthetic organisms and are capable of carbon fixation and sequestration in both light and dark conditions with the help of sulfur compounds. Purple sulfur bacteria are autotrophic and can synthesize organic compounds from inorganic sources. Researchers hope to learn more by sequencing nine type strains of purple sulfur bacteria that are found in freshwater, brackish and marine systems. The information would lead to a better understanding of the process of photosynthesis as well as the global

48

Microbial transformations of sulfur compounds  

Science Journals Connector (OSTI)

Oct 13, 1978 ... tains a large part of the chemical energy transferred ... ical energy is partly preserved in the bio- mass of .... ethanol to remove elemental sulfur.

2000-01-10T23:59:59.000Z

49

Sulfur dioxide oxidation and plume formation at cement kilns  

SciTech Connect (OSTI)

Results of source sampling at the Glens Falls cement kiln in Glens Falls, N.Y., are reported for sulfur oxides, ammonia, hydrochloric acid, oxygen, and moisture content. The origin of a detached, high-opacity, persistent plume originating from the cement kiln stack is investigated. It is proposed that this plume is due to ammonium salts of SOx and sulfuric acid that have been formed in condensed water droplets in the plume by the pseudocatalytic action of ammonia. (1 diagram, 1 graph, 22 references, 7 tables)

Dellinger, B.; Grotecloss, G.; Fortune, C.R.; Cheney, J.L.; Homolya, J.B.

1980-10-01T23:59:59.000Z

50

Assessing Potential Acidification of Marine Archaeological Wood Based on Concentration of Sulfur Species  

SciTech Connect (OSTI)

The presence of sulfur in marine archaeological wood presents a challenge to conservation. Upon exposure to oxygen, sulfur compounds in waterlogged wooden artifacts are being oxidized, producing sulfuric acid. This speeds the degradation of the wood, potentially damaging specimens beyond repair. Sulfur K-edge x-ray absorption spectroscopy was used to identify the species of sulfur present in samples from the timbers of the Mary Rose, a preserved 16th century warship known to undergo degradation through acidification. The results presented here show that sulfur content varied significantly on a local scale. Only certain species of sulfur have the potential to produce sulfuric acid by contact with oxygen and seawater in situ, such as iron sulfides and elemental sulfur. Organic sulfurs, such as the amino acids cysteine and methionine, may produce acid but are integral parts of the wood's structure and may not be released from the organic matrix. The sulfur species contained in the sample reflect the exposure to oxygen while submerged, and this exposure can differ greatly over time and position. A better understanding of the species pathway to acidifications required, along with its location, in order to suggest a more customized and effective preservation strategy. Waterlogged archaeological wood, frequently in the form of shipwrecks, is being excavated for historical purposes in many countries around the world. Even after extensive efforts towards preservation, scientists are discovering that accumulation of sulfate salts results in acidic conditions on the surfaces of the artifacts. Sulfuric acid degrades structural fibers in the wood by acid hydrolysis of cellulose, accelerating the decomposition of the ship timbers. Determining the sulfur content of waterlogged wood is now of great importance in maritime archaeology. Artifact preservation is often more time consuming and expensive than the original excavation; but it is key to the availability of objects for future study as well as maintaining the integrity of historical data and preserving the value of museum pieces. Sulfur occurs in a wide number of oxidation states from -2 to +6, and appears in numerous organic and inorganic compounds in nature. However, it is a very minor component of wood. Sulfur K-edge x-ray absorption spectroscopy (XAS) is a valuable technique because it has the ability to detect very low concentrations of sulfur in the specimen. XAS is also sensitive to differences in oxidation states, as well as long and short range order in molecules.

Not Available

2011-06-22T23:59:59.000Z

51

Graphene-sulfur nanocomposites for rechargeable lithium-sulfur battery electrodes  

SciTech Connect (OSTI)

Rechargeable lithium-sulfur batteries having a cathode that includes a graphene-sulfur nanocomposite can exhibit improved characteristics. The graphene-sulfur nanocomposite can be characterized by graphene sheets with particles of sulfur adsorbed to the graphene sheets. The sulfur particles have an average diameter less than 50 nm..

Liu, Jun; Lemmon, John P; Yang, Zhenguo; Cao, Yuiliang; Li, Xiaolin

2014-06-17T23:59:59.000Z

52

Sulfur minimization in bacterial leaching  

SciTech Connect (OSTI)

The production of sewage biosolids in Ontario in 1989 was estimated to be 7 million m{sup 3} of wet sludge per year. Of this amount, land application accounts for between 20 and 30% of the total. Unfortunately, the use of sewage biosolids on agricultural land is often prohibited because of heavy metal contamination of the biosolids. High cost and operational problems have made chemical methods of metal extraction unattractive. Consequently, microbiological methods of leaching of heavy metals have been studied for over a decade. A relatively simple microbiological process has been investigated in recent years in flask level experiments and recently in a semicontinuous system. The process exploits nonacidophilic and acidophilic indigenous thiobacilli to extract heavy metals from sewage biosolids. These thiobacilli use elemental sulfur as the energy source, producing sulfuric acid. However, the resulting decontaminated biosolids can cause environmental problems like acidification of the soil, when acid is generated from the residual sulfur in the biosolids. The present study examines the possibility of reducing the amount of sulfur added in batch and semicontinuous bacterial leaching systems, and maximizing sulfur oxidation efficiency, thereby reducing the residual sulfur in leached biosolids.

Seth, R.; Prasad, D.; Henry, J.G. [Univ. of Toronto, Ontario (Canada). Dept. of Civil Engineering

1996-11-01T23:59:59.000Z

53

Diesel Emission Control -- Sulfur Effects (DECSE) Program; Phase I Interim Data Report No. 1  

SciTech Connect (OSTI)

The Diesel Emission Control-Sulfur Effects (DECSE) is a joint government/industry program to determine the impact of diesel fuel sulfur levels on emission control systems whose use could lower emissions of nitrogen oxides (NO{sub x}) and particulate matter (PM) from on-highway trucks in the 2002--2004 model years. Phase 1 of the program was developed with the following objectives in mind: (1) evaluate the effects of varying the level of sulfur content in the fuel on the emission reduction performance of four emission control technologies; and (2) measure and compare the effects of up to 250 hours of aging on selected devices for multiple levels of fuel sulfur content. This interim data report summarizes results as of August, 1999, on the status of the test programs being conducted on three technologies: lean-NO{sub x} catalysts, diesel particulate filters and diesel oxidation catalysts.

DOE; ORNL; NREL; EMA; MECA

1999-08-15T23:59:59.000Z

54

Molecular Structures of Polymer/Sulfur Composites for Lithium...  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Structures of PolymerSulfur Composites for Lithium-Sulfur Batteries with Long Cycle Life. Molecular Structures of PolymerSulfur Composites for Lithium-Sulfur Batteries with Long...

55

Amylopectin Wrapped Graphene Oxide/Sulfur for Improved Cyclability of LithiumSulfur Battery  

Science Journals Connector (OSTI)

Amylopectin Wrapped Graphene Oxide/Sulfur for Improved Cyclability of LithiumSulfur Battery ... An amylopectin wrapped graphene oxide-sulfur composite was prepared to construct a 3-dimensionally cross-linked structure through the interaction between amylopectin and graphene oxide, for stabilizing lithium sulfur batteries. ...

Weidong Zhou; Hao Chen; Yingchao Yu; Deli Wang; Zhiming Cui; Francis J. DiSalvo; Hctor D. Abrua

2013-09-05T23:59:59.000Z

56

Sulfur: its clinical and toxicologic aspects  

Science Journals Connector (OSTI)

Although there is no known dietary requirement for inorganic sulfur, it is an essential element for all animal species in as much as they all require the sulfur-containing amino acid methionine. There are three predominate forms of organic sulfur in animals and humans: 1) the thiomethyl of methionine residues in protein; 2) the sulfhydryl disulfides of protein; and 3) the compounds containing ester or amide bound sulfates of glycosaminoglycans, steroids, and many xenobiotic metabolites. Thus, sulfur becomes an important constituent of amino acids, proteins, enzymes, vitamins and other biomolecules. Unlike mammalian species, plants can use inorganic sulfur and synthesize methionine from which are synthesized all the other important sulfur compounds. Hence, sulfur deficiency occurs mainly when plants are grown in sulfur-depleted soils and when humans and animals consume low-protein diets. In recent times, however, the increasing prevalence of refining petroleum and smelting sulfur compounds of metallic minerals into free metals are having a large impact on the balance of sulfur in the environment. Sulfur toxicity is associated mainly with high levels of the element and its toxic volatile substances in the environment. Sulfur dioxide (SO2), a major air pollutant, may adversely affect animal and human health by causing bronchitis, bronchoconstriction, and increased pulmonary resistance.

Lioudmila A Komarnisky; Robert J Christopherson; Tapan K Basu

2003-01-01T23:59:59.000Z

57

Why Sequence Sulfur-Oxidizing Bacteria?  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Sulfur-Oxidizing Bacteria? Sulfur-Oxidizing Bacteria? Several environmental problems, such as acid rain, biocorrosion, etc., are caused by sulfur compounds, such as sulfur dioxide (SO2) and hydrogen sulfide (H2S). A sustainable process to remove these sulfur compounds is the production of elemental sulfur from H2S-containing gas streams by the use of sulfide-oxidizing bacteria. In this process, H2S is absorbed into the alkaline solution in the scrubber unit, followed by the biological oxidation of H2S to elemental sulfur and the recycling of water. With this two-step process, a variety of gas streams (i.e., natural gas, synthesis gas, biogas, and refinery gas) can be treated. For the treatment of sulfate-containing waste streams, an extra step has to be introduced: the transformation of sulfate into H2S by sulfate-reducing bacteria. In

58

Availability of heavy fuel oils by sulfur level, September 1981  

SciTech Connect (OSTI)

A narrative analysis of the status of the United States' total new supply of heavy fuel oils, is given with emphasis on sulfur levels. Tables detail refinery production, stocks, and imports of residual fuel oil and No. 4 fuel oil by sulfur content. All data except stock figures are reported on a monthly and on a year-to-date basis; stock data are reported on an end-of-current-month basis. Units of measure are thousands of barrels. Stocks held, refineries and bulk terminals and refinery production are given by Petroleum Administration for Defense (PAD) and refinery Districts. Imports are given by PAD District, by country of origin, and by importing State. Waterborne movements from PAD District III to other districts are detailed for the most recent month only. This report was previously published by the Bureau of Mines in the Minerals Industries Surveys Series under the same title. Publication was discontinued with the December 1981 issue. 2 figures, 13 tables.

Wolfrey, J.

1981-01-01T23:59:59.000Z

59

Nonlinear optics at maximum coherence  

Science Journals Connector (OSTI)

...D. Walls Nonlinear optics at maximum coherence S. E. Harris G. Y. Yin M. Jain H...optical processes which utilize maximum coherence of a non-allowed transition. The nonlinear...frequency. Nonlinear optics at maximum coherence B y S. E. Harris, G. Y. Yin, M...

1997-01-01T23:59:59.000Z

60

Carbon/Sulfur Nanocomposites and Additives for High-Energy Lithium...  

Broader source: Energy.gov (indexed) [DOE]

CarbonSulfur Nanocomposites and Additives for High-Energy Lithium Sulfur Batteries CarbonSulfur Nanocomposites and Additives for High-Energy Lithium Sulfur Batteries 2011 DOE...

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


61

Improve reformer operation with trace sulfur removal  

SciTech Connect (OSTI)

Modern bimetallic reforming catalysts typically have feed specifications for sulfur of 0.5 to 1 wppm in the reformer naphtha carge. Sulfur in the raw naphtha is reduced to this level by naphtha hydrotreating. While most naphtha hydrotreating operations can usually obtain these levels without substantial problems. It is difficult to obtain levels much below 0.5 to 1 wppm with this process. Revamp of a constrained existing hydrotreater to reduce product sulfur slightly can be extremely costly typically entailing replacement or addition of a new reactor. At Engelhard the authors demonstrated that if the last traces of sulfur remaining from hydrotreating can be removed, the resulting ultra-low sulfur feed greatly improves the reformer operation and provides substantial economic benefit to the refiner. Removal of the remaining trace sulfur is accomplished in a simple manner with a special adsorbent bed, without adding complexity to the reforming operation.

McClung, R.G.; Novak, W.J.

1987-01-01T23:59:59.000Z

62

Sulfur transformations in early diagenetic sediments from the Bay of Concepcion, off Chile  

SciTech Connect (OSTI)

Despite the recognition that both organic sulfur and pyrite form during the very early stages of diagenesis, and that the amount of H{sub 2}S generated in bacterial sulfate reduction primarily limits their formation, the mechanisms and the active species involved still are not clear. In this study, we quantified the major forms of sulfur distributed in sediments to assess the geochemical mechanisms involved in these transformations. XANES spectroscopy, together with elemental analysis, were used to measure sulfur speciation in the organic-rich sediments from the Bay of Concepcion, Chile. Organic polysulfides constituted the major fraction of the organic sulfur, and occurred maximally just below the sediment surface (1--3 cm), where intermediates from H{sub 2}S oxidation were likely to be generated most abundantly. Sulfonates, which could be formed through the reactions of sulfate and thiosulfate, also showed a sub-surface maximum in the vicinity of the ``oxic-anoxic interface``. These results strongly suggest a geochemical origin for organic polysulfides and sulfonates, and illustrate that intermediates from H{sub 2}S oxidation play a dominant role in incorporating sulfur into organic matter. Pyrite was absent in the surficial layer, and first appeared just below the H{sub 2}S maximum, where organic polysulfides began to decrease in abundance. From these results, we argue, that an iron monosulfide precursor formed first from reactions with H{sub 2}S, and then reacts with organic polysulfides, completing the synthesis of pyrite in the sediment column.

Vairavamurth, M.A.; Wang, Shengke; Khandelwal, B.; Manowitz, B. [Brookhaven National Lab., Upton, NY (United States); Ferdelman, T.; Fossing, H. [Max Plank Institute for Marine Microbiology, Bremen (Germany). Dept. of Biogeochemistry

1995-04-01T23:59:59.000Z

63

Contribution of isotopologue self-shielding to sulfur mass-independent fractionation during sulfur dioxide photolysis  

E-Print Network [OSTI]

Signatures of sulfur mass-independent fractionation (S-MIF) are observed for sulfur minerals in Archean rocks, and for modern stratospheric sulfate aerosols (SSA) deposited in polar ice. Ultraviolet light photolysis of ...

Lyons, J. R.

64

HYDROCARBON AND SULFUR SENSORS FOR SOFC SYSTEMS  

SciTech Connect (OSTI)

The following report summarizes work conducted during the Phase I program Hydrocarbon and Sulfur Sensors for SOFC Systems under contract No. DE-FC26-02NT41576. For the SOFC application, sensors are required to monitor hydrocarbons and sulfur in order to increase the operation life of SOFC components. This report discusses the development of two such sensors, one based on thick film approach for sulfur monitoring and the second galvanic based for hydrocarbon monitoring.

A.M. Azad; Chris Holt; Todd Lesousky; Scott Swartz

2003-11-01T23:59:59.000Z

65

Sulfur-Free Selective Pulping  

E-Print Network [OSTI]

Technoeconomic Appraisal," December 1991. 5. DOE Annual Report on Contract No. AC02-83CH10093, Bozell, J. J., Hames, B., Chum, H. L., Dimmel, D. R, Althen, E., Caldwell, P. L., Daube, Oxidation ;; Diels-Alder .. I I -Methanol .. ~ 5 I 3 (C~O) OCH... - Hydrogen 3 (Q-IP) # Q-I 3 o o ~ o 1 2 ~ (H) Lignin DMBQ =two OCH3 groups Anthraquinone MMBQ =one OCH3 group A. K, and Kuroda, K-I.,"Sulfur-free Selective Pulping," March 1992. 6. DOE Annual Report on Contrac No. DE-AC02-83CH10093, Bozell, J. J...

Dimmel, D. R.; Bozell, J. J.

66

Sulfurization of a carbon surface for vapor phase mercury removal II: Sulfur forms and mercury uptake  

E-Print Network [OSTI]

promote the formation of organic sulfur and the presence of H2S during the cooling process increased in the presence of H2S was very effective towards Hg uptake in nitrogen. Corre- lation of mercury uptake capacitySulfurization of a carbon surface for vapor phase mercury removal ­ II: Sulfur forms and mercury

Borguet, Eric

67

Diesel Emission Control -- Sulfur Effects (DECSE) Program; Phase I Interim Data Report No. 2: NO{sub x} Adsorber Catalysts  

SciTech Connect (OSTI)

The Diesel Emission Control-Sulfur Effects (DECSE) is a joint government/industry program to determine the impact of diesel fuel sulfur levels on emission control systems whose use could lower emissions of nitrogen oxides (NOx) and particulate matter (PM) from on-highway trucks in the 2002--2004 model years. Phase 1 of the program was developed with the following objectives in mind: (1) evaluate the effects of varying the level of sulfur content in the fuel on the emission reduction performance of four emission control technologies; and (2) measure and compare the effects of up to 250 hours of aging on selected devices for multiple levels of fuel sulfur content. This interim report discusses the results of the DECSE test program that demonstrates the potential of NOx adsorber catalyst technology across the range of diesel engine operation with a fuel economy penalty less than 4%.

DOE; ORNL; NREL; EMA; MECA

1999-10-15T23:59:59.000Z

68

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

No. 2 Distillate Prices by Sales Type" No. 2 Distillate Prices by Sales Type" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","No. 2 Distillate",7,"Monthly","9/2013","1/15/1983" ,"Data 2","No. 2 Diesel Fuel",6,"Monthly","9/2013","1/15/1994" ,"Data 3","No. 2 Diesel Fuel, Ultra Low-Sulfur",6,"Monthly","9/2013","1/15/2007" ,"Data 4","No. 2 Diesel Fuel, Low-Sulfur",6,"Monthly","9/2013","1/15/1994" ,"Data 5","No. 2 Diesel Fuel, High-Sulfur",5,"Monthly","9/2013","1/15/1994"

69

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Diesel, Low-Sulfur Prices - Sales to End Users " Diesel, Low-Sulfur Prices - Sales to End Users " ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","No. 2 Diesel, Low-Sulfur Prices - Sales to End Users ",9,"Monthly","9/2013","1/15/1994" ,"Release Date:","12/2/2013" ,"Next Release Date:","1/2/2014" ,"Excel File Name:","pet_pri_dist_a_epd2dm10_pta_dpgal_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pri_dist_a_epd2dm10_pta_dpgal_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov"

70

MaximumLetThrough.PDF  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

9 9 Maximum Let-Through Currents in the APS Storage Ring Quadrupole, Sextupole, and Corrector Magnets J. Carwardine, D. McGhee, G. Markovich May 18, 1999 Abstract Limits are described for the maximum magnet currents, under specified fault conditions, for the storage ring quadrupole, sextupole, and corrector magnets. Introduction In computing the maximum let-through current for the magnets for the storage ring, several factors must be considered. In general, the maximum current likely to occur even under fault conditions is less than the maximum theoretical DC current given the magnet resistance and the maximum available DC voltage. The first level of protection against magnet current overloads is the over-current interlock that is built into the converter electronics package. The threshold is set to approximately 110% of

71

High-Sulfur Coal for Generating Electricity  

Science Journals Connector (OSTI)

High-Sulfur...FLUIDIZED-BED COMBUSTORS, COMBUSTION...MAY FLUE GAS DES S E...1971 ). High-sulfur...was brief. Natural gas became...overdependent on natural gas and oil to...elevated pressure with a downward...coals of high ash-fusion...

James T. Dunham; Carl Rampacek; T. A. Henrie

1974-04-19T23:59:59.000Z

72

The complete genome sequence of Staphylothermus marinus reveals differences in sulfur metabolism among heterotrophic Crenarchaeota  

SciTech Connect (OSTI)

Staphylothermus marinus is an anaerobic, sulfur-reducing peptide fermenter of the archaeal phylum Crenarchaeota. It is the third heterotrophic, obligate sulfur reducing crenarchaeote to be sequenced and provides an opportunity for comparative analysis of the three genomes. The 1.57 Mbp genome of the hyperthermophilic crenarchaeote Staphylothermus marinus has been completely sequenced. The main energy generating pathways likely involve 2-oxoacid:ferredoxin oxidoreductases and ADP-forming acetyl-CoA synthases. S. marinus possesses several enzymes not present in other crenarchaeotes including a sodium ion-translocating decarboxylase likely to be involved in amino acid degradation. S. marinus lacks sulfur-reducing enzymes present in the other two sulfur-reducing crenarchaeotes that have been sequenced - Thermofilum pendens and Hyperthermus butylicus. Instead it has three operons similar to the mbh and mbx operons of Pyrococcus furiosus, which may play a role in sulfur reduction and/or hydrogen production. The two marine organisms, S. marinus and H. butylicus, possess more sodium-dependent transporters than T. pendens and use symporters for potassium uptake while T. pendens uses an ATP-dependent potassium transporter. T. pendens has adapted to a nutrient-rich environment while H. butylicus is adapted to a nutrient-poor environment, and S. marinus lies between these two extremes. The three heterotrophic sulfur-reducing crenarchaeotes have adapted to their habitats, terrestrial vs. marine, via their transporter content, and they have also adapted to environments with differing levels of nutrients. Despite the fact that they all use sulfur as an electron acceptor, they are likely to have different pathways for sulfur reduction.

Anderson, iain J.; Dharmarajan, Lakshmi; Rodriguez, Jason; Hooper, Sean; Porat, Iris; Ulrich, Luke E.; Elkins, James G.; Mavromatis, Kostas; Sun, Hui; Land, Miriam; Lapidus, Alla; Lucas, Susan; Barry, Kerrie; Huber, Harald; Zhulin, Igor B.; Whitman, William B.; Mukhopadhyay, Biswarup; Woese, Carl; Bristow, James; Kyrpides, Nikos

2008-09-05T23:59:59.000Z

73

Analyzing organic sulfur in coal/char: Integrated mild degradation/XANES methods. Final technical report, September 1, 1993--November 30, 1994  

SciTech Connect (OSTI)

The overall goal of this study is to improve the understanding of sulfur in coals/chars via the use of combined advanced nondestructive and advanced destructive methods of sulfur analysis. This study combines selective oxidation, analytical pyrolysis, and sulfur X-ray Absorption Near Edge Structure Spectroscopy (XANES) analysis. Samples with a wide variety of sulfur contents, (0.63%--4.40%) have been prepared for use in this study. This includes steam gasification chars, oxidized coals and desulfurized coals as well of the original unaltered coals. Mild pyrolysis and XANES data shows that the sulfur chemistry of gasification chars is significantly different from that of the original coals. Mild pyrolysis of the samples that were oxidized with peroxyacetic acid showed that the level of simple thiophene structures observed in the pyrolysis products declines with increasing levels of oxidation. Sulfur XANES spectra of treated samples showed various effects depending on the treatment severity. The XANES spectra of less severely treated samples were similar, although not identical, to the untreated coal spectra. XANES of gasification chars indicated conversion of pyrite to pyrrhotite, removal of organic sulfide sulfur and dissolution of soluble inorganic sulfur species during gasification. Mild oxidation with peroxyacetic acid results in preferential oxidation of sulfide forms before thiophene forms but increasing oxidation severity leads to virtually all sulfur species being oxidized. Good agreement between W-band EPR and XANES data for aromatic sulfur contents were obtained. The TPR analysis of coal indicated that organic sulfur was present as alkyl-aryl sulfide, aryl-aryl sulfides, simple thiophenes and condensed thiophenes. TPR shows that non-thiophenic compounds are removed by PAA oxidation, and that the longer the oxidation is performed the greater is the removal of non-thiophenic sulfur structures.

Palmer, S.R. [Southern Illinois Univ., Carbondale, IL (United States); Huffman, G.P. [Univ. of Kentucky, Lexington, KY (United States)

1994-12-31T23:59:59.000Z

74

Method of removal of sulfur from coal and petroleum products  

DOE Patents [OSTI]

A method for the removal of sulfur from sulfur-bearing materials such as coal and petroleum products using organophosphine and organophosphite compounds is provided.

Verkade, John G. (Ames, IA); Mohan, Thyagarajan (Ames, IA); Angelici, Robert J. (Ames, IA)

1995-01-01T23:59:59.000Z

75

Investigation of Sulfur Deactivation on Cu/Zeolite SCR Catalysts...  

Broader source: Energy.gov (indexed) [DOE]

of Sulfur Deactivation on CuZeolite SCR Catalysts in Diesel Application Investigation of Sulfur Deactivation on CuZeolite SCR Catalysts in Diesel Application Investigation of...

76

Additives and Cathode Materials for High-Energy Lithium Sulfur...  

Broader source: Energy.gov (indexed) [DOE]

Additives and Cathode Materials for High-Energy Lithium Sulfur Batteries Additives and Cathode Materials for High-Energy Lithium Sulfur Batteries 2013 DOE Hydrogen and Fuel Cells...

77

Manipulating the Surface Reactions in Lithium Sulfur Batteries...  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Manipulating the Surface Reactions in Lithium Sulfur Batteries Using Hybrid Anode Structures. Manipulating the Surface Reactions in Lithium Sulfur Batteries Using Hybrid Anode...

78

Single ion heat engine with maximum efficiency at maximum power  

E-Print Network [OSTI]

We propose an experimental scheme to realize a nano heat engine with a single ion. An Otto cycle may be implemented by confining the ion in a linear Paul trap with tapered geometry and coupling it to engineered laser reservoirs. The quantum efficiency at maximum power is analytically determined in various regimes. Moreover, Monte Carlo simulations of the engine are performed that demonstrate its feasibility and its ability to operate at maximum efficiency of 30% under realistic conditions.

Obinna Abah; Johannes Rossnagel; Georg Jacob; Sebastian Deffner; Ferdinand Schmidt-Kaler; Kilian Singer; Eric Lutz

2012-05-07T23:59:59.000Z

79

Sulfur Behavior in the Sasol?Lurgi Fixed-Bed Dry-Bottom Gasification Process  

Science Journals Connector (OSTI)

This article reports on the findings of a study regarding the sulfur behavior across a Sasol?Lurgi gasifier. ... (2) This ash, referred to as coarse ash, is a combination of red and white to gray sintered clinkers with heterogeneous texture varying from fine material to large irregularly shaped aggregates of sizes ranging from 4 to 75 mm. ... South African coals that are used for the Sasol?Lurgi gasification process are normally low-grade medium rank C (bituminous) coal with a total sulfur content of approximately 1?2 wt %, on an as-received basis. ...

M. Pat Skhonde; R. Henry Matjie; J. Reginald Bunt; A. Christien Strydom; Herold Schobert

2008-12-05T23:59:59.000Z

80

Sulfur nanocrystals anchored graphene composite with highly improved electrochemical performance for lithiumsulfur batteries  

Science Journals Connector (OSTI)

Abstract Two kinds of graphenesulfur composites with 50wt% of sulfur are prepared using hydrothermal method and thermal mixing, respectively. Transmission Electron Microscopy (TEM) and Energy Dispersive X-ray Spectra mapping show that sulfur nanocrystals with size of ?5nm dispersed on graphene sheets homogeneously for the sample prepared by hydrothermal method (NanoS@G). While for the thermal mixed graphenesulfur composite (SG mixture), sulfur shows larger and uneven size (50200nm). X-ray Photoelectron Spectra (XPS) reveals the strong chemical bonding between the sulfur nanocrystals and graphene. Comparing with the SG mixture, the NanoS@G composite shows highly improved electrochemical performance as cathode for lithiumsulfur (LiS) battery. The NanoS@G composite delivers an initial capacity of 1400mAhg?1 with the sulfur utilization of 83.7% at a current density of 335mAg?1. The capacity keeps above 720mAhg?1 over 100 cycles. The strong adherence of the sulfur nanocrystals on graphene immobilizes sulfur and polysulfides species and suppressed the shuttle effect, resulting higher coulombic efficiency and better capacity retention. Electrochemical impedance also suggests that the strong bonding enabled rapid electronic/ionic transport and improved electrochemical kinetics, therefore good rate capability is obtained. These results demonstrate that the NanoS@G composite is a very promising candidate for high-performance LiS batteries.

Jun Zhang; Zimin Dong; Xiuli Wang; Xuyang Zhao; Jiangping Tu; Qingmei Su; Gaohui Du

2014-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


81

Catalyst for elemental sulfur recovery process  

DOE Patents [OSTI]

A catalytic reduction process is described for the direct recovery of elemental sulfur from various SO[sub 2]-containing industrial gas streams. The catalytic process provides high activity and selectivity, as well as stability in the reaction atmosphere, for the reduction of SO[sub 2] to elemental sulfur product with carbon monoxide or other reducing gases. The reaction of sulfur dioxide and reducing gas takes place over a metal oxide composite catalyst having one of the following empirical formulas: [(FO[sub 2])[sub 1[minus]n](RO)[sub n

Flytzani-Stephanopoulos, M.; Liu, W.

1995-01-24T23:59:59.000Z

82

Sulfur-graphene oxide material for lithium-sulfur battery cathodes  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Sulfur-graphene oxide material for lithium-sulfur battery cathodes Sulfur-graphene oxide material for lithium-sulfur battery cathodes Theoretical specific energy and theoretical energy density Scanning electron micrograph of the GO-S nanocomposite June 2013 Searching for a safer, less expensive alternative to today's lithium-ion batteries, scientists have turned to lithium-sulfur as a possible chemistry for next-generation batteries. Li/S batteries have several times the energy storage capacity of the best currently available rechargeable Li-ion battery, and sulfur is inexpensive and nontoxic. Current batteries using this chemistry, however, suffer from extremely short cycle life-they don't last through many charge-discharge cycles before they fail. A research team led by Elton Cairns and Yuegang Zhang has developed a new

83

Phosphazene groups modified sulfur composites as active cathode materials for rechargeable lithium/sulfur batteries  

Science Journals Connector (OSTI)

A novel phosphazene groups modified sulfur composites cathode [triphosphazene sulfide composite (PS) or nitroanilinetriphosphazene disulfide composite (NPS)] which can give good affinity with electrolytes was...

J. D. Liu; S. Q. Zhang; S. B. Yang; Z. F. Shi; S. T. Zhang; L. K. Wu

2013-11-01T23:59:59.000Z

84

Energy Levels in Sulfur Nuclei  

Science Journals Connector (OSTI)

A study has been made of the proton groups from the reaction of 3.22-Mev deuterons with sulfur in the form, primarily, of H2S gas. The following Q values have been assigned to the reaction S32(dp)S33:6.48,5.69,4.58,4.31,3.63,3.33,2.60,2.33,2.06,1.78,1.37,0.85,and0.18 Mev, corresponding to the ground state and twelve excited states of S33. Four of these groups have been investigated for proton gamma-ray coincidences to confirm this assignment. The yield as a function of deuteron energy has been observed for the six highest energy groups and indication of the presence of some broad resonances found. A qualitative measurement of the variation with angle of relative yields of the groups has indicated a proton intensity distribution that is symmetric for some groups and asymmetric for others. The cross section for the reaction for 90 observation has been found to be 1.2 barns. The mass difference S33-S32 has been calculated to be 0.99963 mass unit.Two low intensity, high energy groups have been assigned to the reaction S33(dp)S34 with Q values of 8.67 and 7.85 Mev. This, together with the above observation, leads to a value of 1.99691 for the mass difference S34-S32.

Perry W. Davison

1949-03-01T23:59:59.000Z

85

Steam reforming utilizing sulfur tolerant catalyst  

SciTech Connect (OSTI)

This patent describes a steam reforming process for converting hydrocarbon material to hydrogen gas in the presence of sulfur which consists of: adding steam to the hydrocarbon material and passing the steam and hydrocarbon material over catalyst material at elevated temperatures. The improvement comprises utilizing as a catalyst material high activity, sulfur tolerant catalyst of platinum supported on lanthanum stabilized alumina or magnesium promoted lanthanum stabilized alumina. It also describes a steam process for converting hydrocarbon material to hydrogen gas in the presence of sulfur which consists of steam to the hydrocarbon material over catalyst material at elevated temperatures. The improvement comprises utilizing as a catalyst material high activity, sulfur tolerant catalysts consisting essentially of iridium supported on lanthanum stabilized alumina or magnesium promoted lanthanum stabilized alumina. In addition a steam reforming process is described for converting hydrocarbon material to hydrogen gas in the presence of sulfur comprising adding steam to the hydrocarbon material and passing the steam and hydrocarbon material over catalyst material at elevated temperatures. The improvement comprises utilizing as a catalyst material high activity sulfur tolerant catalysts consisting essentially of palladium supported on lanthanum stabilized alumina or magnesium promoted lanthanum stabilized alumina.

Setzer, H.J.; Karavolis, S.; Bett, J.A.S.

1987-09-15T23:59:59.000Z

86

Development of a new FGD process that converts sulfur dioxide to salable ammonium phosphate fertilizer  

SciTech Connect (OSTI)

Rich mineral resources have enabled Chinese coal output and energy consumption to rank second and third in the world, respectively. In 1992, up to 70 percent of the country`s electric power was generated by the combustion of some 300 million tons of coal. Although the average sulfur content level in Chinese coals is only about 0.8 percent, the share of high- sulfur coals with 2 percent or more sulfur content is as high as 18 percent. As a result, air pollution accompanied by acid rain now occurs over most of the country, especially in southwestern China. Currently, the area comprising Guangdong, Guangxi, the Sichuan Basin, and the greater part of Gueizhou, where the sulfur content in coal is between 2 and 7 percent and the average pH values of rain water are between 4 and 5 per annum, has become one of the three biggest acid rain-affected areas in the world. In 1992, the national installed coal-fired electricity generation capacity exceeded 100,000 MWe. By the year 2000, it is expected to reach as much as 200,000 MWe, according to a new scheduled program. Environmental pollution caused by large-scale coal combustion is a very important issue that needs to be considered in the implementation of the program. To ensure that the effects of coal-fired power generation on the environment can be properly controlled in the near future, TPRI (Thermal Power Research Institute), the sole thermal power engineering research institution within the Ministry of Electric Power Industry (MOEPI), has conducted a long-term research program to develop sulfur emission control technologies suitable to the special conditions prevalent in China since the early 1970s. The details are summarized. The objective of this chapter is to describe the fundamental concept and major pilot test results and present an economic evaluation of a new process combining flue gas desulfurization (FGD) and ammonium phosphate fertilizer production.

Ji-lu Chen

1993-12-31T23:59:59.000Z

87

Alaska has 4. 0 trillion tons of low-sulfur coal: Is there a future for this resource  

SciTech Connect (OSTI)

The demand for and use of low-sulfur coal may increase because of concern with acid rain. Alaska's low-sulfur coal resources can only be described as enormous: 4.0 trillion tons of hypothetical onshore coal. Mean total sulfur content is 0.34% (range 0.06-6.6%, n = 262) with a mean apparent rank of subbituminous B. There are 50 coal fields in Alaska; the bulk of the resources are in six major fields or regions: Nenana, Cook Inlet, Matanuska, Chignik-Herendeen Bay, North Slope, and Bering River. For comparison, Carboniferous coals in the Appalachian region and Interior Province have a mean total sulfur content of 2.3% (range 0.1-19.0%, n = 5,497) with a mean apparent rank of high-volatile A bituminous coal, and Rocky Mountain and northern Great Plains Cretaceous and Tertiary coals have a mean total sulfur content of 0.86% (range 0.02-19.0%, n = 2,754) with a mean apparent rank of subbituminous B. Alaskan coal has two-fifths the total sulfur of western US coals and one-sixth that of Carboniferous US coals. Even though Alaska has large resources of low-sulfur coal, these resources have not been developed because of (1) remote locations and little infrastructure, (2) inhospitable climate, and (3) long distances to potential markets. These resources will not be used in the near future unless there are some major, and probably violent, changes in the world energy picture.

Stricker, G.D. (Geological Survey, Denver, CO (USA))

1990-05-01T23:59:59.000Z

88

Availability of heavy fuel oils by sulfur levels, February 1981  

SciTech Connect (OSTI)

This monthly report includes a narrative analysis of the status of the United States' total new supply of heavy fuel oils, with an emphasis on sulfur levels. Tables detail refinery production, stocks, and imports of residual fuel oil and No. 4 fuel oil by sulfur content. All data except stock figures are reported on a monthly and on a year-to-date basis; stock data are reported on an end-of-current-month basis. Units of measure are thousands of barrels. Stocks held at refineries and bulk terminals and refinery production are given by Petroleum Administration for Defense (PAD) and Refinery Districts. Imports are given by PAD District, by country or origin, and by importing state. Waterborne movements from PAD District III to other districts are detailed for the most recent month only. The December issue repeats the seven major tables with final data in all categories for the previous calendar year. This report was previously published by the Bureau of Mines in the Minerals Industries Surveys Series under the same title. 2 figs., 13 tabs.

Wolfrey, J.

1981-10-15T23:59:59.000Z

89

Availability of heavy fuel oils by sulfur levels, March 1981  

SciTech Connect (OSTI)

This monthly report includes a narrative analysis of the status of the United States' total new supply of heavy fuel oils, with an emphasis on sulfur levels. Tables detail refinery production, stocks, and imports of residual fuel oil and No. 4 fuel oil by sulfur content. All data except stock figures are reported on a monthly and on a year-to-date basis; stock data are reported on an end-of-current-month basis. Units of measure are thousands of barrels. Stocks held at refineries and bulk terminals and refinery production are given by Petroleum Administration for Defense (PAD) and Refinery Districts. Imports are given by PAD District, by country of origin, and by importing state. Waterborne movements from PAD District III to other districts are detailed for the most recent month only. The December issue repeats the seven major tables with final data in all categories for the previous calendar year. This report was previously published by the Bureau of Mines in the Minerals Industries Survey Series under the same title. 2 figs., 13 tabs.

Wolfrey, J.

1981-10-15T23:59:59.000Z

90

Availability of heavy fuel oils by sulfur level, August 1981  

SciTech Connect (OSTI)

A narrative analysis of the status of the United States' total new supply of heavy fuel oils, is given with emphasis on sulfur levels. Tables detail refinery production, stocks, and imports of residual fuel oil and No. 4 fuel oil by sulfur content. All data except stock figures are reported on a monthly and on a year-to-date basis; stock data are reported on an end-of-current-month basis. Units of measure are thousands of barrels. Stocks held at refineries and bulk terminals and refinery production are given by Petroleum Administration for Defense (PAD) and Refinery Districts. Imports are given by PAD District, by country of origin, and by importing State. Waterborne movements from PAD District III to other districts are detailed for the most recent month only. This report was previously published by the Bureau of Mines in the Minerals Industries Surveys Series under the same title. Publication was discontinued with the December 1981 issue. 1 figure, 14 tables.

Wolfrey, J.

1981-01-01T23:59:59.000Z

91

Availability of heavy fuel oils by sulfur level, October 1981  

SciTech Connect (OSTI)

A narrative analysis of the status of the United States' total new supply of heavy fuel oils, is given with emphasis on sulfur levels. Tables detail refinery production, stocks, and imports of residual fuel oil and No. 4 fuel oil by sulfur content. All data except stock figures are reported on a monthly and on a year-to-date basis; stock data are reported on an end-of-current-month basis. Units of measure are thousands of barrels. Stocks held at refineries and bulk terminals and refinery production are given by Petroleum Administration for Defense (PAD) and refinery Districts. Imports are given by PAD District, by country of origin, and by importing State. Waterbone movements from PAD District III to other districts are detailed for the most recent month only. This report was previously published by the Bureau of Mines in the Minerals Industries Surveys Series under the same title. Publication was discontinued with the December 1981 issue. 1 figure, 14 tables.

Wolfrey, J.

1981-01-01T23:59:59.000Z

92

Carbon/Sulfur Nanocomposites and Additives for High-Energy Lithium...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

& Publications Additives and Cathode Materials for High-Energy Lithium Sulfur Batteries CarbonSulfur Nanocomposites and Additives for High-Energy Lithium Sulfur Batteries...

93

IEP - Water-Energy Interface: Total Maximum Daily Load Page  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Total Maximum Daily Loads (TMDLs) Total Maximum Daily Loads (TMDLs) The overall goal of the Clean Water Act is to "restore and maintain the chemical, physical, and biological integrity of the Nation’s waters." In 1999, EPA proposed changes to Section 303(d), to establish Total Maximum Daily Loads (TMDLs) for watersheds that do not meet this goal. The TMDL is the highest amount of a given pollutant that is permissible in that body of water over a given period of time. TMDLs include both waste load allocation (WLA) for point sources and load allocations for non-point sources. In Appalachia, acid mine drainage (AMD) is the single most damaging non-point source. There is also particular concern of the atmospheric deposition of airborne sulfur, nitrogen, and mercury compounds. States are currently in the process of developing comprehensive lists of impaired waters and establishing TMDLs for those waters. EPA has recently proposed a final rule that will require states to develop TMDLs and implement plans for improving water quality within the next 10 years. Under the new rule, TMDL credits could be traded within a watershed.

94

SULFURIC ACID REMOVAL PROCESS EVALUATION: SHORT-TERM RESULTS  

SciTech Connect (OSTI)

The objective of this project is to demonstrate the use of alkaline reagents injected into the furnace of coal-fired boilers as a means of controlling sulfuric acid emissions. Sulfuric acid controls are becoming of increasing interest to utilities with coal-fired units for a number of reasons. Sulfuric acid is a Toxic Release Inventory species, a precursor to acid aerosol/condensable emissions, and can cause a variety of plant operation problems such as air heater plugging and fouling, back-end corrosion, and plume opacity. These issues will likely be exacerbated with the retrofit of SCR for NOX control on some coal-fired plants, as SCR catalysts are known to further oxidize a portion of the flue gas SO{sub 2} to SO{sub 3}. The project is testing the effectiveness of furnace injection of four different calcium- and/or magnesium-based alkaline sorbents on full-scale utility boilers. These reagents have been tested during four one- to two-week tests conducted on two FirstEnergy Bruce Mansfield Plant units. One of the sorbents tested was a magnesium hydroxide slurry produced from a wet flue gas desulfurization system waste stream, from a system that employs a Thiosorbic{reg_sign} Lime scrubbing process. The other three sorbents are available commercially and include dolomite, pressure-hydrated dolomitic lime, and commercial magnesium hydroxide. The dolomite reagent was injected as a dry powder through out-of-service burners, while the other three reagents were injected as slurries through air-atomizing nozzles into the front wall of upper furnace, either across from the nose of the furnace or across from the pendant superheater tubes. After completing the four one- to two-week tests, the most promising sorbents were selected for longer-term (approximately 25-day) full-scale tests. The longer-term tests are being conducted to confirm the effectiveness of the sorbents tested over extended operation and to determine balance-of-plant impacts. This reports presents the results of the short-term tests; the long-term test results will be reported in a later document. The short-term test results showed that three of the four reagents tested, dolomite powder, commercial magnesium hydroxide slurry, and byproduct magnesium hydroxide slurry, were able to achieve 90% or greater removal of sulfuric acid compared to baseline levels. The molar ratio of alkali to flue gas sulfuric acid content (under baseline conditions) required to achieve 90% sulfuric acid removal was lowest for the byproduct magnesium hydroxide slurry. However, this result may be confounded because this was the only one of the three slurries tested with injection near the top of the furnace across from the pendant superheater platens. Injection at the higher level was demonstrated to be advantageous for this reagent over injection lower in the furnace, where the other slurries were tested.

Gary M. Blythe; Richard McMillan

2002-03-04T23:59:59.000Z

95

SULFURIC ACID REMOVAL PROCESS EVALUATION: SHORT-TERM RESULTS  

SciTech Connect (OSTI)

The objective of this project is to demonstrate the use of alkaline reagents injected into the furnace of coal-fired boilers as a means of controlling sulfuric acid emissions. Sulfuric acid controls are becoming of increasing interest to utilities with coal-fired units for a number of reasons. Sulfuric acid is a Toxic Release Inventory species, a precursor to acid aerosol/condensable emissions, and can cause a variety of plant operation problems such as air heater plugging and fouling, back-end corrosion, and plume opacity. These issues will likely be exacerbated with the retrofit of SCR for NO{sub x} control on some coal-fired plants, as SCR catalysts are known to further oxidize a portion of the flue gas SO{sub 2} to SO{sub 3}. The project is testing the effectiveness of furnace injection of four different calcium- and/or magnesium-based alkaline sorbents on full-scale utility boilers. These reagents have been tested during four one- to two-week tests conducted on two First Energy Bruce Mansfield Plant units. One of the sorbents tested was a magnesium hydroxide slurry produced from a wet flue gas desulfurization system waste stream, from a system that employs a Thiosorbic{reg_sign} Lime scrubbing process. The other three sorbents are available commercially and include dolomite, pressure-hydrated dolomitic lime, and commercial magnesium hydroxide. The dolomite reagent was injected as a dry powder through out-of-service burners, while the other three reagents were injected as slurries through air-atomizing nozzles into the front wall of upper furnace, either across from the nose of the furnace or across from the pendant superheater tubes. After completing the four one- to two-week tests, the most promising sorbents were selected for longer-term (approximately 25-day) full-scale tests. The longer-term tests are being conducted to confirm the effectiveness of the sorbents tested over extended operation and to determine balance-of-plant impacts. This reports presents the results of the short-term tests; the long-term test results will be reported in a later document. The short-term test results showed that three of the four reagents tested, dolomite powder, commercial magnesium hydroxide slurry, and byproduct magnesium hydroxide slurry, were able to achieve 90% or greater removal of sulfuric acid compared to baseline levels. The molar ratio of alkali to flue gas sulfuric acid content (under baseline conditions) required to achieve 90% sulfuric acid removal was lowest for the byproduct magnesium hydroxide slurry. However, this result may be confounded because this was the only one of the three slurries tested with injection near the top of the furnace across from the pendant superheater platens. Injection at the higher level was demonstrated to be advantageous for this reagent over injection lower in the furnace, where the other slurries were tested.

Gary M. Blythe; Richard McMillan

2002-02-04T23:59:59.000Z

96

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Name","Description"," Of Series","Frequency","Latest Data for" ,"Data 1","New York Heat Content of Natural Gas Deliveries to Consumers (BTU per Cubic...

97

energy content  

Science Journals Connector (OSTI)

energy content, (weight) strength ? Arbeitsvermgen n (im ballistischen Mrser gemessen), Sprengenergie f (im ballistischen Mrser gemessen) [Mit 10 g Sprengstoff ermittelt

2014-08-01T23:59:59.000Z

98

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Heat Content of Natural Gas Deliveries to Consumers (BTU per Cubic Foot)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description"," Of...

99

Can Sulfur Spectroscopy the Vasa?  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Title Title by Magnus Sandström*, Farideh Jalilehvand, Ingmar Persson, Ulrik Gelius and Patrick Frank The famous 17th-century Swedish warship Vasa has been on display in the Vasa Museum since 1990 (Figure 1). The Vasa sank on its maiden voyage in 1628, and was recovered in 1961 after 333 years in the cold brackish water of Stockholm harbor. After extensive conservation treatment, the oaken Vasa appeared in good condition (1). Figure 1. The Vasa on display in the Vasa Museum, Stockholm, Sweden. Dimensions: length 61 m (69 m including bowsprit), maximum width 11.7 m, stern castle 19.3 m high, displacement 1210 tons. (photo by Hans Hammarskiöld at the Vasa Museum). Reproduced by permission, (http://www.nature.com/). However, high acidity and a rapid spread of sulfate salts and elemental

100

Effects of paleolatitude on coal quality - model for organic sulfur distribution in US coal  

SciTech Connect (OSTI)

In the conterminous US, most Carboniferous peats accumulated at latitudes of 0/degrees/-15/degrees/S, Cretaceous Rocky Mountain province peats at 30/degrees/-45/degrees/N, Tertiary northern Great Plains peats at 40/degrees/-55/degrees/N, and Tertiary Gulf Coast peats at 30/degrees/-40/degrees/N. Alaskan Cretaceous and Tertiary peats accumulated at latitudes above 70/degrees/N. A comparison of paleolatitudes calculated from paleomagnetic poles and organic sulfur contents for more than 7000 coal samples indicates that the higher the latitude in which a peat swamp developed, the lower the mean organic sulfur content of the subsequent coal (correlation coefficient - 0.4; significant at the 99% confidence level). Mean organic sulfur contents range from 0.90% (range = 0.01-5.08%, standard deviation = 0.56) in low-latitude Carboniferous coal to 0.25% (range = 0.01-1.41%, standard deviation = 0.23) in high-latitude Alaskan Cretaceous and Tertiary coal.

Affolter, R.H.; Stricker, G.D.

1989-03-01T23:59:59.000Z

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


101

Boiler Maximum Achievable Control Technology (MACT) Technical...  

Broader source: Energy.gov (indexed) [DOE]

Boiler Maximum Achievable Control Technology (MACT) Technical Assistance - Fact Sheet, May 2014 Boiler Maximum Achievable Control Technology (MACT) Technical Assistance - Fact...

102

Safety considerations for the use of sulfur in sulfur-modified pavement materials  

E-Print Network [OSTI]

on the surround1ng environment. As sulfur-modified paving materials were being developed, there was a corresponding concern for studying the amounts of gaseous emiss1ons that were generated. The Texas Trans- portat1on Inst1tute (TTI) was one of the first... organizations in the United States to become 1nvolved in the research and development of sulfur-modified pavements, Throughout 1ts laboratory stud1es TTI cont1nually mon1tored hydrogen sulf1de (H25) and sulfur d1oxide (502) em1ssions produced during mix...

Jacobs, Carolyn Yuriko

2012-06-07T23:59:59.000Z

103

Fact #824: June 9, 2014 EPA Sulfur Standards for Gasoline  

Broader source: Energy.gov [DOE]

Sulfur naturally occurs in gasoline and diesel fuel, contributing to pollution when the fuel is burned. Beginning in 2004, standards were set on the amount of sulfur in gasoline (Tier 2 standards)....

104

ORIGINAL ARTICLE Sulfur oxidizers dominate carbon fixation  

E-Print Network [OSTI]

). Methylotrophs and iron oxidizers were also active in plume waters and expressed key proteins for methane by bacteria (especially, alpha-, gamma- and epsilon-proteobacteria) that likely participate in the oxidationORIGINAL ARTICLE Sulfur oxidizers dominate carbon fixation at a biogeochemical hot spot in the dark

Hansell, Dennis

105

High-Sulfur Coal for Generating Electricity  

Science Journals Connector (OSTI)

...amounts of coal, because...Director-Mineral Re-sources...of Gas from Coal through a...on coals of high ash-fusion temperature...per ton of high-sulfur coal burned. Absorp-tion...particulate matter as well as...capable of remov-ing up to...

James T. Dunham; Carl Rampacek; T. A. Henrie

1974-04-19T23:59:59.000Z

106

NONEQUILIBRIUM SULFUR CAPTURE AND RETENTION IN AN AIR COOLED SLAGGING COAL COMBUSTOR  

SciTech Connect (OSTI)

Calcium oxide injected in a slagging combustor reacts with the sulfur from coal combustion to form sulfur-bearing particles. They are deposited on the liquid slag layer on the combustor wall. Due to the low solubility of sulfur in slag, slag must be rapidly drained from the combustor to limit sulfur gas re-evolution. Analysis indicated that slag mass flow rates in excess of 400 lb/hr should limit sulfur re-evolution. The objective of this 42-month project was to perform a series of tests to determine the factors that control the retention of the sulfur in the slag. 36 days of testing on the combustor were completed prior to the end of this reporting period, 12/31/98. This compares with 16 tests required in the original project plan. Combustor tests in early 1997 with high (37%) ash, Indian coal confirmed that high slag mass flow rates of about 500 lb/hr resulted in retention in the slag of up to 20% of the injected sulfur content mineral matter. To further increase the slag flow rate, rice husks, which contain 20% ash, and rice husk char, which contain 70% ash, were co-fired with coal in the combustor. A series of 13 combustor tests were performed in fourth quarter of 1997 and a further 6 tests were performed in January 1998 and in the summer of 1998. The test objective was to achieve slag flow rates between 500 and 1,000 lb/hr. Due to the very low bulk density of rice husk, compared to pulverized coal, almost the entire test effort focused on developing methods for feeding the rice husks into combustor. In the last test of December 1997, a peak mineral matter, injection rate of 592 lb/hr was briefly achieved by injection of coal, rice husk char, gypsum, and limestone into the combustor. However, no significant sulfur concentration was measured in the slag removed from the combustor. The peak injection rate reached with biomass in the 1997 tests was 310 lb/hr with rice husk, and 584 lb/hr with rice husk char.

Dr. Bert Zauderer

1999-03-15T23:59:59.000Z

107

Short communication Influence of molybdenum and sulfur on copper  

E-Print Network [OSTI]

Short communication Influence of molybdenum and sulfur on copper metabolism in sheep: comparison of molybdenum able to trigger the copper sulfur molybdenum interference in sheep was measured with either only) and 4 increasing molybdenum doses. The sulfur-molybdenum-copper interference was quantified

Paris-Sud XI, Université de

108

A novel lithium/sulfur battery based on sulfur/graphene nanosheet composite cathode and gel polymer electrolyte  

Science Journals Connector (OSTI)

A novel sulfur/graphene nanosheet (S/GNS) composite was prepared ... ball milling of sulfur with commercial multi-layer graphene nanosheet, followed by a heat treatment. ... of irregularly interlaced nanosheet-li...

Yongguang Zhang; Yan Zhao; Zhumabay Bakenov

2014-03-01T23:59:59.000Z

109

A simple approach to synthesize nanosized sulfur/graphene oxide materials for high-performance lithium/sulfur batteries  

Science Journals Connector (OSTI)

We report on a simple and facile synthesis route for the sulfur/graphene oxide composite via ultrasonic mixing of the nano-sulfur and graphene oxide aqueous suspensions followed by a low-temperature heat treat...

Yongguang Zhang; Yan Zhao; Zhumabay Bakenov

2014-07-01T23:59:59.000Z

110

Sulfur accumulation in pinewood (Pinus sylvestris) induced by bacteria in a simulated seabed environment: Implications for marine archaeological wood and fossil fuels  

Science Journals Connector (OSTI)

Fresh pinewood blocks were submerged in sulfate and iron(II) containing media, inoculated with bacterial consortia isolated from seawater, aiming to simulate the seabed conditions of the Vasa shipwreck (1628). The consortia contained erosion (EB) and sulfate-reducing bacteria (SRB). Sulfur K-edge X-ray absorption near edge structure (XANES) spectroscopy and scanning X-ray spectromicroscopy images showed that organic sulfur, mainly thiols (R-SH), had accumulated in the lignin-rich middle lamella in EB-degraded parts of the wood. The sulfur content in the wood increased more than 10 times in 2 years. In another series with active inoculums from marine archaeological wood, the sulfur XANES spectra showed, after 4 years of anaerobic treatment, considerable amounts also of inorganic iron sulfides, Fe1?xS, which oxidized at atmospheric exposure. A sediment sample from the Vasa's seabed was also rich in iron sulfides, including pyrite, FeS2. X-ray fluorescence mappings of sulfur and phosphorous distributions indicate that scavenging SRB penetration, producing hydrogen sulfide in situ, is restricted to EB-degraded parts of the wood structure. The sulfur isotope depletion of 34S from ?34S=21 in marine sulfate to ?34S=6 and 1.8 for fractions of reduced sulfur and sulfate separated from a Vasa wood sample, respectively, suggests bacterial transformation. A fuller understanding of the routes of sulfur accumulation, as reactive iron sulfides and as organic sulfur, has important implications for improving conservation methods of marine archaeological wood. Moreover, the biogenic accumulation of organically bound sulfur, specifically in lignin-rich parts of waterlogged wood, has wider geochemical significance for fossil fuels of marine origin, as lignin-rich humic matter is important for the diagenetic formation of kerogens from anoxic marine sediments.

Yvonne Fors; Thomas Nilsson; Emiliana Damian Risberg; Magnus Sandstrm; Peter Torssander

2008-01-01T23:59:59.000Z

111

Graphene-Wrapped Sulfur Particles as a Rechargeable LithiumSulfur Battery Cathode Material with High Capacity and Cycling Stability  

Science Journals Connector (OSTI)

Graphene-Wrapped Sulfur Particles as a Rechargeable LithiumSulfur Battery Cathode Material with High Capacity and Cycling Stability ... The resulting graphenesulfur composite showed high and stable specific capacities up to ?600 mAh/g over more than 100 cycles, representing a promising cathode material for rechargeable lithium batteries with high energy density. ...

Hailiang Wang; Yuan Yang; Yongye Liang; Joshua Tucker Robinson; Yanguang Li; Ariel Jackson; Yi Cui; Hongjie Dai

2011-06-24T23:59:59.000Z

112

Chapter 3 - Potential of Sodium-Sulfur Battery Energy Storage to Enable Further Integration of Wind  

Science Journals Connector (OSTI)

Abstract Wind generation is the leading alternative for environmentally responsible power generation and for energy independence in the future. However, wind power output cannot be controlled same as conventional generation, and wind is not necessarily available to serve peak load. In this chapter, the use of a Sodium Sulfur battery directly coupled with a wind farm to provide generation shifting for serving peak demand and for limiting the wind farm power output ramp-rate is discussed. Results from field operation of a 1 MW, 7.2 \\{MWh\\} Sodium Sulfur battery coupled with an 11.55 MW wind farm were provided to validate the batterys ability to successfully carry out both the tasks. It is shown that the two tasks could be combined to achieve maximum benefit. Value addition from shifting wind generation to on-peak is calculated and the optimal ratio storage to wind ratio is discussed.

Saurabh Tewari

2015-01-01T23:59:59.000Z

113

Sulfur in the Changuinola peat deposit, Panama, as an indicator of the environments of deposition of peat and coal  

SciTech Connect (OSTI)

The sulfur (S) content of coal is often used to infer aspects of paleoclimate, trophic state, and proximity to marine influence, of the mire in which it was deposited. In this study, the S content of peat in a large back-barrier mire complex on the Caribbean coast of Panama is related to climatic, biological, and tectonic factors of the depositional environment. The S content is in proportion to the degree of humidification of the peat, and both are independent of the pH of the groundwater. The distribution of forms of organic and inorganic sulfur in the tropical peats are found to be comparable to published values for temperate and subtropical peats, despite differences in vegetation and climate.The distribution of high-sulfur peats in the eastern part of the deposit and low-sulfur peats in the western part, and the SE-NW transgression parallel to the trend of the coastline, reflects the regional structural trend of coseismic subsidence greatest to the southeast.

Phillips, S.; Bustin, R.M. [Univ. of British Columbia, Vancouver, British Columbia (Canada). Dept. of Geological Sciences

1996-01-01T23:59:59.000Z

114

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222014 5:11:47 PM" "Back to Contents","Data 1: U.S. Gasoline and Diesel Retail Prices" "Sourcekey","EMMEPM0PTENUSDPG","EMMEPM0UPTENUSDPG","EMMEPM0RPTENUS...

115

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116

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117

Workbook Contents  

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PM" "Back to Contents","Data 1: Price of Liquefied U.S. Natural Gas Re-Exports to Russia (Dollars per Thousand Cubic Feet)" "Sourcekey","NGMEPG0ERENUS-NRSDMCF"...

118

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121

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:11:23 PM" "Back to Contents","Data 1:...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:04 PM" "Back to Contents","Data 1: Virginia...

124

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:26:30 PM" "Back to Contents","Data 1: Alabama...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:01 PM" "Back to Contents","Data 1: Rhode...

126

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:04:58 PM" "Back to Contents","Data 1: Natural...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:04:23 PM" "Back to Contents","Data 1: Vermont...

128

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:00 PM" "Back to Contents","Data 1: Oregon...

130

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:01:53 PM" "Back to Contents","Data 1: Utah...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:06:23 PM" "Back to Contents","Data 1: Michigan...

132

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:02 PM" "Back to Contents","Data 1: South...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:03 PM" "Back to Contents","Data 1: Tennessee...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:01:23 PM" "Back to Contents","Data 1: Montana...

139

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:01:32 PM" "Back to Contents","Data 1: New...

140

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141

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:04 PM" "Back to Contents","Data 1: Utah...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:04:31 PM" "Back to Contents","Data 1: Natural...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:00 PM" "Back to Contents","Data 1: Oklahoma...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:08:23 PM" "Back to Contents","Data 1: Illinois...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:06:23 PM" "Back to Contents","Data 1: Maryland...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:01:23 PM" "Back to Contents","Data 1: Percent...

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:08 PM" "Back to Contents","Data 1: U.S....

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:04:51 PM" "Back to Contents","Data 1: Natural...

151

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:05:23 PM" "Back to Contents","Data 1: Natural...

152

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153

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,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"1162014 3:23:07 PM" "Back to Contents","Data 1: Wyoming...

154

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159

CATALYST EVALUATION FOR A SULFUR DIOXIDE-DEPOLARIZED ELECTROLYZER  

SciTech Connect (OSTI)

Thermochemical processes are being developed to provide global-scale quantities of hydrogen. A variant on sulfur-based thermochemical cycles is the Hybrid Sulfur (HyS) Process which uses a sulfur dioxide depolarized electrolyzer (SDE) to produce the hydrogen. Testing examined the activity and stability of platinum and palladium as the electrocatalyst for the SDE in sulfuric acid solutions. Cyclic and linear sweep voltammetry revealed that platinum provided better catalytic activity with much lower potentials and higher currents than palladium. Testing also showed that the catalyst activity is strongly influenced by the concentration of the sulfuric acid electrolyte.

Hobbs, D; Hector Colon-Mercado, H

2007-01-31T23:59:59.000Z

160

Method to prevent sulfur accumulation in membrane electrode assembly  

DOE Patents [OSTI]

A method of operating a hybrid sulfur electrolyzer to generate hydrogen is provided that includes the steps of providing an anolyte with a concentration of sulfur dioxide, and applying a current. During steady state generation of hydrogen a plot of applied current density versus concentration of sulfur dioxide is below a boundary line. The boundary line may be linear and extend through the origin of the graph with a slope of 0.001 in which the current density is measured in mA/cm2 and the concentration of sulfur dioxide is measured in moles of sulfur dioxide per liter of anolyte.

Steimke, John L; Steeper, Timothy J; Herman, David T

2014-04-29T23:59:59.000Z

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161

TABLE OF CONTENTS  

National Nuclear Security Administration (NNSA)

AC05-00OR22800 AC05-00OR22800 TABLE OF CONTENTS Contents Page # TOC - i SECTION A - SOLICITATION/OFFER AND AWARD ......................................................................... A-i SECTION B - SUPPLIES OR SERVICES AND PRICES/COSTS ........................................................ B-i B.1 SERVICES BEING ACQUIRED ....................................................................................B-2 B.2 TRANSITION COST, ESTIMATED COST, MAXIMUM AVAILABLE FEE, AND AVAILABLE FEE (Modification 295, 290, 284, 280, 270, 257, 239, 238, 219, M201, M180, M162, M153, M150, M141, M132, M103, M092, M080, M055, M051, M049, M034, M022, M003, A002) ..........................................................B-2 SECTION C - DESCRIPTION/SPECIFICATION/WORK STATEMENT DESCRIPTION OF

162

sulfur dioxide emissions | OpenEI  

Open Energy Info (EERE)

sulfur dioxide emissions sulfur dioxide emissions Dataset Summary Description Emissions from energy use in buildings are usually estimated on an annual basis using annual average multipliers. Using annual numbers provides a reasonable estimation of emissions, but it provides no indication of the temporal nature of the emissions. Therefore, there is no way of understanding the impact on emissions from load shifting and peak shaving technologies such as thermal energy storage, on-site renewable energy, and demand control. Source NREL Date Released April 11th, 2011 (3 years ago) Date Updated April 11th, 2011 (3 years ago) Keywords buildings carbon dioxide emissions carbon footprinting CO2 commercial buildings electricity emission factors ERCOT hourly emission factors interconnect nitrogen oxides

163

CEDR Content  

Broader source: Energy.gov (indexed) [DOE]

CEDR Content" CEDR Content" "The Consolidated Energy Data Report (CEDR) consists of 27 worksheets that should be completed by each site, as applicable, and included as part each site's SSP in a MS Excel electronic format. The CEDR is due to the SPO no later than December 9th." "Worksheet",,"Overview","Action" 1.1,"Content","Stand-alone overview of the CEDR tabs.","None" 2.1,"Funds, Meters, Training","Collects information on energy and water spending, and metering status.","If applicable, complete cells highlighted in orange. Edited and new data cells should be highlighted in light blue." 3.1,"BTU & Gal Key","Reference tab containing all factors and dropdown menu information for all tabs starting with ""3"". If you need to divide up the CEDR, please keep all tabs starting with ""3"" together to ensure calculation links are not broken. ","None"

164

Sulfur incorporation into copper indium diselenide single crystals through annealing in hydrogen sulfide  

SciTech Connect (OSTI)

CuInSe{sub 2} crystals were sulfurized in a H{sub 2}S-Ar gas mixture at 575 deg. C. The focus was on the resulting mass transport, in particular, on the interdiffusion of Se and S. Experiments were done for various sulfurization times, and the resulting S distribution was measured by Auger electron spectroscopy sputter depth profiling and analyzed with the Boltzmann-Matano method. A one-dimensional diffusion process had shaped the S distribution in these crystals. The respective diffusion coefficient was on the order of 10{sup -16} cm{sup 2}/s, and it varied only slightly with the S content in CuIn(Se,S){sub 2}.

Titus, Jochen; Birkmire, Robert W.; Hack, Christina; Mueller, Georg; McKeown, Patrick [Institute of Energy Conversion, University of Delaware, Newark, Delaware 19716 (United States); Crystal Growth Laboratory, Department of Materials Science, University of Erlangen-Nuernberg (Germany); Evans East, Princeton, New Jersey 08520 (United States)

2006-02-15T23:59:59.000Z

165

Sulfur-isotope separation by distillation  

SciTech Connect (OSTI)

Sulfur-isotope separation by low-temperature distillation of hydrogen sulfide was studied in an 8-m, 25-mm diameter distillation column. Column temperature was controlled by a propane-propylene heat pipe. Column packing HETP was measured using nitric oxide in the column. The column was operated at pressures from 45 to 125 kPa. The relative volatility of S-32 vs. S-34 varied from 1.0008 to 1.0014.

Mills, T.R.

1982-01-01T23:59:59.000Z

166

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Workbook Contents" Workbook Contents" ,"U.S. State-to-State capacity" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","Units of Measurement","Frequency","Updated Date" ,"Pipeline State-to-State Capacity","State-to-State capacity","Million cubic feet per day (MMcf/d)","Quarterly","application/vnd.ms-excel" ,"State Inflow Capacity","Inflow capacity from other States","Million cubic feet per day (MMcf/d)","Quarterly","application/vnd.ms-excel" ,"State Outflow Capacity","Outflow capacity to other States","Million cubic feet per day (MMcf/d)","Quarterly","application/vnd.ms-excel"

167

Sulfur/three-dimensional graphene composite for high performance lithiumsulfur batteries  

Science Journals Connector (OSTI)

Abstract A sulfur/graphene composite is prepared by loading elemental sulfur into three-dimensional graphene (3D graphene), which is assembled using a metal ions assisted hydrothermal method. When used as cathode materials for lithiumsulfur (LiS) batteries, the sulfur/graphene composite (S@3D-graphene) with 73wt % sulfur shows a significantly enhanced cycling performance (>700mAhg?1 after 100 cycles at 0.1C rate with a Coulombic efficiency>96%) as well as high rate capability with a capacity up to 500mAhg?1 at 2C rate (3.35Ag?1). The superior electrochemical performance could be attributed to the highly porous structure of three-dimensional graphene that not only enables stable and continue pathway for rapid electron and ion transportation, but also restrain soluble polysulfides and suppress the shuttle effect. Moreover, the robust structure of 3D graphene can keep cathode integrity and accommodate the volume change during high-rate charge/discharge processes, making it a promising candidate as cathode for high performance LiS batteries.

Chunmei Xu; Yishan Wu; Xuyang Zhao; Xiuli Wang; Gaohui Du; Jun Zhang; Jiangping Tu

2015-01-01T23:59:59.000Z

168

Development of the Hybrid Sulfur Thermochemical Cycle  

SciTech Connect (OSTI)

The production of hydrogen via the thermochemical splitting of water is being considered as a primary means for utilizing the heat from advanced nuclear reactors to provide fuel for a hydrogen economy. The Hybrid Sulfur (HyS) Process is one of the baseline candidates identified by the U.S. Department of Energy [1] for this purpose. The HyS Process is a two-step hybrid thermochemical cycle that only involves sulfur, oxygen and hydrogen compounds. Recent work has resulted in an improved process design with a calculated overall thermal efficiency (nuclear heat to hydrogen, higher heating value basis) approaching 50%. Economic analyses indicate that a nuclear hydrogen plant employing the HyS Process in conjunction with an advanced gas-cooled nuclear reactor system can produce hydrogen at competitive prices. Experimental work has begun on the sulfur dioxide depolarized electrolyzer, the major developmental component in the cycle. Proof-of-concept tests have established proton-exchange-membrane cells (a state-of-the-art technology) as a viable approach for conducting this reaction. This is expected to lead to more efficient and economical cell designs than were previously available. Considerable development and scale-up issues remain to be resolved, but the development of a viable commercial-scale HyS Process should be feasible in time to meet the commercialization schedule for Generation IV gas-cooled nuclear reactors.

Summers, William A.; Steimke, John L

2005-09-23T23:59:59.000Z

169

Sulfide catalysts for reducing SO2 to elemental sulfur  

DOE Patents [OSTI]

A highly efficient sulfide catalyst for reducing sulfur dioxide to elemental sulfur, which maximizes the selectivity of elemental sulfur over byproducts and has a high conversion efficiency. Various feed stream contaminants, such as water vapor are well tolerated. Additionally, hydrogen, carbon monoxide, or hydrogen sulfides can be employed as the reducing gases while maintaining high conversion efficiency. This allows a much wider range of uses and higher level of feed stream contaminants than prior art catalysts.

Jin, Yun (Peking, CN); Yu, Qiquan (Peking, CN); Chang, Shih-Ger (El Cerrito, CA)

2001-01-01T23:59:59.000Z

170

In situ derivation of sulfur activated TiO{sub 2} nano porous layers through pulse-micro arc oxidation technology  

SciTech Connect (OSTI)

Highlights: {yields} S-TiO{sub 2} layers were grown by MAO technique under pulse current for the first time. {yields} Effect of growth parameters on chemical composition, topography, and morphology of the layers was studied. {yields} A correlation between photocatalytic performance and growth conditions was proposed. -- Abstract: Micro arc oxidation technique, as a facile and efficient process, was employed to grow sulfur doped titania porous layers. This research sheds light on the photocatalytic performance of the micro arc oxidized S-TiO{sub 2} nano-porous layers fabricated under pulse current. Morphological and topographical studies, performed by SEM and AFM techniques, revealed that increasing the frequency and/or decreasing the duty cycle resulted in formation of finer pores and smoother surfaces. XRD and XPS results showed that the layers consisted of anatase and rutile phases whose fraction was observed to change depending on the synthesis conditions. The highest anatase relative content was obtained at the frequency of 500 Hz and the duty cycle of 5%. Furthermore, photocatalytic activity of the layers was examined by measuring the decomposition rate of methylene blue under both ultraviolet and visible photo irradiations. Maximum photodegradation reaction rate constants over the pulse-grown S-TiO{sub 2} layers were respectively measured as 0.0202 and 0.0110 min{sup -1} for ultraviolet and visible irradiations.

Bayati, M.R., E-mail: mbayati@ncsu.edu [Department of Materials Science and Engineering, North Carolina State University, Raleigh, NC 27695 (United States); School of Metallurgy and Materials Engineering, Iran University of Science and Technology, P.O. Box 16845-161, Tehran (Iran, Islamic Republic of); Golestani-Fard, F. [School of Metallurgy and Materials Engineering, Iran University of Science and Technology, P.O. Box 16845-161, Tehran (Iran, Islamic Republic of) [School of Metallurgy and Materials Engineering, Iran University of Science and Technology, P.O. Box 16845-161, Tehran (Iran, Islamic Republic of); Center of Excellence for Advanced Materials, Iran University of Science and Technology, P.O. Box 16845-195, Tehran (Iran, Islamic Republic of); Moshfegh, A.Z. [Department of Physics, Sharif University of Technology, P.O. Box 11155-9161, Tehran (Iran, Islamic Republic of) [Department of Physics, Sharif University of Technology, P.O. Box 11155-9161, Tehran (Iran, Islamic Republic of); Institute for Nanoscience and Nanotechnology, Sharif University of Technology, P.O. Box 14588-89694, Tehran (Iran, Islamic Republic of); Molaei, Roya [School of Metallurgy and Materials Engineering, Iran University of Science and Technology, P.O. Box 16845-161, Tehran (Iran, Islamic Republic of)] [School of Metallurgy and Materials Engineering, Iran University of Science and Technology, P.O. Box 16845-161, Tehran (Iran, Islamic Republic of)

2011-10-15T23:59:59.000Z

171

Lithium/Sulfur Batteries Based on Doped Mesoporous Carbon - Energy...  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Materials Advanced Materials Find More Like This Return to Search LithiumSulfur Batteries Based on Doped Mesoporous Carbon Oak Ridge National Laboratory Contact ORNL About...

172

Analyses of sulfur-asphalt field trials in Texas  

E-Print Network [OSTI]

128 LIST OF FIGURES FIGURE PAGF Layout of SNPA sulfur bitumen binder pavem nt test ? U. S. Highway 69, Lufkin, Texas 15 Col 1oi d mi 1 1 furnished by SNPA for preparation of sul fur-asphalt emulsions View of mixing station showing sulfur... designed to investigate the advantage of using a colloid mill to prepare sulfur-asphalt binders as compared to comingling the asphalt and molten sulfur in a pipeline leading directly to the pug mill. After only six months of testing, the results...

Newcomb, David Edward

1979-01-01T23:59:59.000Z

173

Development of sulfur cathode material for Li-S batteries.  

E-Print Network [OSTI]

??M.S. Efforts were taken to fabricate a cathode material having Sulfur as the active material. First step is composed of identifying potential ways of fabricating (more)

Dharmasena, Ruchira Ravinath, 1984-

2014-01-01T23:59:59.000Z

174

Project Profile: Baseload CSP Generation Integrated with Sulfur...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

Related Links FAQs Contact Us Offices You are here Home Concentrating Solar Power Project Profile: Baseload CSP Generation Integrated with Sulfur-Based...

175

Fundamental Studies of Lithium-Sulfur Cell Chemistry  

Broader source: Energy.gov (indexed) [DOE]

Studies of Lithium-Sulfur Cell Chemistry PI: Nitash Balsara LBNL June 17, 2014 Project ID ESS224 This presentation does not contain any proprietary, confidential, or otherwise...

176

Sulfur removal and comminution of carbonaceous material  

DOE Patents [OSTI]

Finely divided, clean coal or other carbonaceous material is provided by forming a slurry of coarse coal in aqueous alkali solution and heating the slurry under pressure to above the critical conditions of steam. The supercritical fluid penetrates and is trapped in the porosity of the coal as it swells in a thermoplastic condition at elevated temperature. By a sudden, explosive release of pressure the coal is fractured into finely divided particles with release of sulfur-containing gases and minerals. The finely divided coal is recovered from the minerals for use as a clean coal product. 2 figs.

Narain, N.K.; Ruether, J.A.; Smith, D.N.

1987-10-07T23:59:59.000Z

177

Sulfur removal and comminution of carbonaceous material  

DOE Patents [OSTI]

Finely divided, clean coal or other carbonaceous material is provided by forming a slurry of coarse coal in aqueous alkali solution and heating the slurry under pressure to above the critical conditions of steam. The supercritical fluid penetrates and is trapped in the porosity of the coal as it swells in a thermoplastic condition at elevated temperature. By a sudden, explosive release of pressure the coal is fractured into finely divided particles with release of sulfur-containing gases and minerals. The finely divided coal is recovered from the minerals for use as a clean coal product.

Narain, Nand K. (Bethel Park, PA); Ruether, John A. (McMurray, PA); Smith, Dennis N. (Herminie, PA)

1988-01-01T23:59:59.000Z

178

Sulfur isotopes in coal constrain the evolution of the Phanerozoic sulfur cycle  

Science Journals Connector (OSTI)

...obviously influence the average isotope values. For the other data, samples...pp 87105 . 19 Price FT Casagrande DJ ( 1991 ) Sulfur...coals. Geology of Fossil Fuels, Proc 30th Int Geol Congress...Jersey Pinelands and its effect on stream water chemistry...223 248 . 29 Price FT Shieh YN ( 1979 ) Fractionation...

Donald E. Canfield

2013-01-01T23:59:59.000Z

179

Advanced Byproduct Recovery: Direct Catalytic Reduction of Sulfur Dioxide to Elemental Sulfur.  

SciTech Connect (OSTI)

More than 170 wet scrubber systems applied, to 72,000 MW of U.S., coal-fired, utility boilers are in operation or under construction. In these systems, the sulfur dioxide removed from the boiler flue gas is permanently bound to a sorbent material, such as lime or limestone. The sulfated sorbent must be disposed of as a waste product or, in some cases, sold as a byproduct (e.g. gypsum). Due to the abundance and low cost of naturally occurring gypsum, and the costs associated with producing an industrial quality product, less than 7% of these scrubbers are configured to produce usable gypsum (and only 1% of all units actually sell the byproduct). The disposal of solid waste from each of these scrubbers requires a landfill area of approximately 200 to 400 acres. In the U.S., a total of 19 million tons of disposable FGD byproduct are produced, transported and disposed of in landfills annually. The use of regenerable sorbent technologies has the potential to reduce or eliminate solid waste production, transportation and disposal. In a regenerable sorbent system, the sulfur dioxide in the boiler flue gas is removed by the sorbent in an adsorber. The S0{sub 2}s subsequently released, in higher concentration, in a regenerator. All regenerable systems produce an off-gas stream from the regenerator that must be processed further in order to obtain a salable byproduct, such as elemental sulfur, sulfuric acid or liquid S0{sub 2}.

NONE

1997-06-01T23:59:59.000Z

180

SYNTHESIS OF SULFUR-BASED WATER TREATMENT AGENT FROM SULFUR DIOXIDE WASTE STREAMS  

SciTech Connect (OSTI)

We propose a process that uses sulfur dioxide from coal combustion as a raw material to synthesize polymeric ferric sulfate (PFS), a water treatment agent. The process uses sodium chlorate as an oxidant and ferrous sulfate as an absorbent. The major chemical mechanisms in this reaction system include oxidation, hydrolysis, and polymerization. Oxidation determines sulfur conversion efficiency while hydrolysis and polymerization control the quality of product. Many factors, including SO{sub 2} inlet concentration, flow rate of simulated flue gas, reaction temperature, addition rate of oxidant and stirring rate, may affect the efficiencies of SO{sub 2} removal. Currently, the effects of SO{sub 2} inlet concentration, the flow rate of simulated flue gas and addition rate of flue gas on removal efficiencies of SO{sub 2}, are being investigated. Experiments shown in this report have demonstrated that the conversion efficiencies of sulfur dioxide with ferrous sulfate as an absorbent are in the range of 60-80% under the adopted process conditions. However, the conversion efficiency of sulfur dioxide may be improved by optimizing reaction conditions to be investigated. Partial quality indices of the synthesized products, including Fe{sup 2+} concentration and total iron concentration, have been evaluated.

Robert C. Brown; Maohong Fan

2001-12-01T23:59:59.000Z

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


181

Lithiumsulfur batteries: Influence of C-rate, amount of electrolyte and sulfur loading on cycle performance  

Science Journals Connector (OSTI)

Abstract In the past four years major improvement of the lithium sulfur battery technology has been reported. Novel carbon cathode materials offer high sulfur loading, sulfur utilization and cycle stability. An often neglected aspect is that sulfur loading and amount of electrolyte strongly impact the performance. In this paper, we demonstrate how the amount of electrolyte, sulfur loading, lithium excess and cycling rate influences the cycle stability and sulfur utilization. We chose vertically aligned carbon nanotubes (VA-CNT) as model system with a constant areal loading of carbon. For a high reproducibility, decreased weight of current collector and good mechanical adhesion of the VA-CNTs we present a layer transfer technique that enables a light-weight sulfur cathode. The sulfur loading of the cathode was adjusted from 20 to 80wt.-%. Keeping the total amount of electrolyte constant and varying the C-rate, we are able to demonstrate that the capacity degradation is reduced for high rates, high amount of electrolyte and low sulfur loading. In addition idle periods in the cycling regiment and lower rates result in an increased degradation. We attribute this to the redox-reaction between reactive lithium and polysulfides that correlates with the cycling time, rather than cycle number.

Jan Brckner; Sren Thieme; Hannah Tamara Grossmann; Susanne Drfler; Holger Althues; Stefan Kaskel

2014-01-01T23:59:59.000Z

182

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ngm_epg0_fgc_sky_mmcfa.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/ngm_epg0_fgc_sky_mmcfa.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:59:11 AM" "Back to Contents","Data 1: Kentucky Natural Gas Gross Withdrawals from Coalbed Wells (MMcf) " "Sourcekey","NGM_EPG0_FGC_SKY_MMCF" "Date","Kentucky Natural Gas Gross Withdrawals from Coalbed Wells (MMcf) "

183

The corrosion behavior of molybdenum and Hastelloy B in sulfur and sodium polysulfides at 623 K  

SciTech Connect (OSTI)

An experimental study was completed to determine the corrosion behavior of molybdenum and Hastelloy B, a nickel-based alloy with high molybdenum content, in sulfur and sodium polysulfides (Na/sub 2/S/sub 3/,Na/sub 2/S/sub 4/, Na/sub 2/S/sub 5/) at 623 K. In sulfur, molybdenum corrodes very slowly, with a parabolic rate constant of 3.6 x 10/sup -9/ cm s/sup -1/2/. Hastelloy B shows no measurable corrosion after 100h of exposure to sulfur. The corrosion reaction of molybdenum in Na/sub 2/S/sub 3/ is characterized by the formation of a protective film that effectively eliminates further corrosion after the first 100h of exposure. Hastelloy B, however, corrodes rapidly in Na/sub 2/S/sub 3/, with corrosion rates approaching those of pure nickel under the same conditions. After the first 4h of exposure, the kinetics for the corrosion of Hastelloy B in Na/sub 2/S/sub 3/ follows a linear rate law. The scale morphology has multiple spalled layers of NiS/sub 2/, with some crystallites of NiS/sub 2/ appearing on the leading face of the scale and between the individual scale layers. This spalling causes smaller coupons of the Hastelloy B to corrode faster than larger coupons.

Brown, A.P.

1987-08-01T23:59:59.000Z

184

Distribution of hazardous air pollutant trace elements, total sulfur, and ash in coals from five Tertiary basins in the Rocky Mountain Region  

SciTech Connect (OSTI)

Arithmetic mean values of the contents of hazardous air pollutant (HAP) trace elements named in the 1990 Clean Air Act Amendments (antimony, arsenic, beryllium, cadmium, chromium, cobalt, lead, manganese, mercury, nickel, selenium, and uranium), ash, and total sulfur were statistically compared on a whole-coal basis for Paleocene coals from five Tertiary basins in the Rocky Mountain Region. The study of proximate and elemental analyses indicate a relationship between trace element contents and paleogeography.

Ellis, M.S.; Stricker, G.D.; Flores, R.M. [Geological Survey, Denver, CO (United States)

1994-12-31T23:59:59.000Z

185

Integrated boiler, superheater, and decomposer for sulfuric acid decomposition  

DOE Patents [OSTI]

A method and apparatus, constructed of ceramics and other corrosion resistant materials, for decomposing sulfuric acid into sulfur dioxide, oxygen and water using an integrated boiler, superheater, and decomposer unit comprising a bayonet-type, dual-tube, counter-flow heat exchanger with a catalytic insert and a central baffle to increase recuperation efficiency.

Moore, Robert (Edgewood, NM); Pickard, Paul S. (Albuquerque, NM); Parma, Jr., Edward J. (Albuquerque, NM); Vernon, Milton E. (Albuquerque, NM); Gelbard, Fred (Albuquerque, NM); Lenard, Roger X. (Edgewood, NM)

2010-01-12T23:59:59.000Z

186

HEALTH AND CLIMATE POLICY IMPACTS ON SULFUR EMISSION CONTROL  

E-Print Network [OSTI]

the climate and health effects of sulfate aerosol into an integrated-assessment model of fossil fuel emission warming and health simultaneously will support more stringent fossil fuel and sulfur controls control. Our simulations show that a policy that adjusts fossil fuel and sulfur emissions to address both

Russell, Lynn

187

Analysis of organic sulfur and nitrogen in coal via tandem degradation methods. Final technical report, 1 September 1991--31 October 1992  

SciTech Connect (OSTI)

With the recent increase in concern for environmental issues and the implication of sulfur and nitrogen in coal combustion preducts as prime causes of acid rain, it has become clear that there is an urgent need for alternative methods for determining the nature of organic sulfur and nitrogen compounds in coal. The principal impediment to the molecular characterization of organic sulfur and nitrogen forms in coal is the polymeric nature of coal`s molecular structure, rendering coal insoluble and impossible to analyze by the necessary gas chromatographic (GC) methods. In our research, we apply mild chemical degradation techniques in order to render coal soluble in common organic solvents and thus amenable to standard GC characterization. The study also seeks to apply the degradative techniques to coal asphaltenes, since they are believed to be polymeric structures similar to the whole coal, but smaller and more readily analyzed. Of the degradation techniques used to date, oxidation by sodium dichromate provides the best chemical structure information. A variety of major sulfur compounds were detected in the dichromate oxidation products of demineralized IBC101 coal, including thiazoles (compounds which contains both sulfur and nitrogen) and a series of isomers of C{sub 2}-, C{sub 3}- and C{sub 4}-alkylthiophene derivatives. Precise agreement between GC-MS and sulfur-selective GC-FPD data was obtained for these compounds, which probably originated as short alkyl chains on exterior portions of the original peat macromolecular structure that were sulfurized shortly after burial by H{sub 2}S. The results were further confirmed by the analysis of a non-Illinois Basin coal with nearly twice the organic sulfur content of IBC101.

Kruge, M.A.; Palmer, S.R. [Southern Illinois Univ., Carbondale, IL (United States)

1992-12-31T23:59:59.000Z

188

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010pa2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010pa2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:52 PM" "Back to Contents","Data 1: Pennsylvania Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010PA2" "Date","Pennsylvania Natural Gas Residential Consumption (MMcf)" 24653,279817 25019,285978 25384,295027 25749,297022 26114,304327

189

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Bcf)" Bcf)" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Dry Natural Gas Production (Bcf)",1,"Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9070us1m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9070us1m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:33:14 PM" "Back to Contents","Data 1: U.S. Dry Natural Gas Production (Bcf)"

190

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","na1504_nus_4m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/na1504_nus_4m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:46:14 PM" "Back to Contents","Data 1: U.S. Natural Gas % of Total Residential - Sales (%)" "Sourcekey","NA1504_NUS_4" "Date","U.S. Natural Gas % of Total Residential - Sales (%)" 37271,98.3 37302,98.5 37330,98.4 37361,98.1

191

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n5050us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n5050us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:29:09 PM" "Back to Contents","Data 1: U.S. Total Natural Gas Injections into Underground Storage (MMcf)" "Sourcekey","N5050US2" "Date","U.S. Total Natural Gas Injections into Underground Storage (MMcf)" 26679 26710 26738 26769 26799

192

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010hi2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010hi2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:19 PM" "Back to Contents","Data 1: Hawaii Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010HI2" "Date","Hawaii Natural Gas Residential Consumption (MMcf)" 29402,1416 29767,1289 30132,1197 30497,1121 30863,1048 31228,625 31593,579 31958,591

193

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010tx2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010tx2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:59 PM" "Back to Contents","Data 1: Texas Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010TX2" "Date","Texas Natural Gas Residential Consumption (MMcf)" 24653,201407 25019,211763 25384,220728 25749,232189 26114,237387 26480,240662

194

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040nd2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040nd2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:40 AM" "Back to Contents","Data 1: North Dakota Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040ND2" "Date","North Dakota Natural Gas Vented and Flared (MMcf)" 35079,232 35110,193 35139,232 35170,176 35200,230 35231,258 35261,269

195

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010de3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010de3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:15 PM" "Back to Contents","Data 1: Delaware Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010DE3" "Date","Delaware Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

196

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020fl2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020fl2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:29 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Florida (MMcf)" "Sourcekey","N3020FL2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Florida (MMcf)"

197

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020ct2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020ct2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:23 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Connecticut (MMcf)" "Sourcekey","N3020CT2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Connecticut (MMcf)"

198

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020az2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020az2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:17 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Arizona (MMcf)" "Sourcekey","N3020AZ2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Arizona (MMcf)"

199

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020ca2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020ca2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:19 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in California (MMcf)" "Sourcekey","N3020CA2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in California (MMcf)"

200

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020dc2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020dc2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:24 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in the District of Columbia (MMcf)" "Sourcekey","N3020DC2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in the District of Columbia (MMcf)"

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


201

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020co2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020co2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:21 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Colorado (MMcf)" "Sourcekey","N3020CO2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Colorado (MMcf)"

202

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010md2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010md2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:30 PM" "Back to Contents","Data 1: Maryland Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010MD2" "Date","Maryland Natural Gas Residential Consumption (MMcf)" 24653,77130 25019,79015 25384,84406 25749,86811 26114,87617 26480,89042

203

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U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040or2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040or2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:43 AM" "Back to Contents","Data 1: Oregon Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040OR2" "Date","Oregon Natural Gas Vented and Flared (MMcf)" 35079 35110 35139 35170 35200 35231 35261 35292 35323 35353 35384 35414 35445,0

204

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010wv3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010wv3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:07 PM" "Back to Contents","Data 1: West Virginia Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010WV3" "Date","West Virginia Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

205

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010la2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010la2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:28 PM" "Back to Contents","Data 1: Louisiana Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010LA2" "Date","Louisiana Natural Gas Residential Consumption (MMcf)" 24653,74386 25019,77762 25384,82965 25749,86148 26114,79893 26480,82847

206

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010al3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010al3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:07 PM" "Back to Contents","Data 1: Alabama Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010AL3" "Date","Alabama Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

207

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010nm3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010nm3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:45 PM" "Back to Contents","Data 1: New Mexico Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010NM3" "Date","New Mexico Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

208

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010id2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010id2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:22 PM" "Back to Contents","Data 1: Idaho Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010ID2" "Date","Idaho Natural Gas Residential Consumption (MMcf)" 24653,6179 25019,6545 25384,6980 25749,7711 26114,8455 26480,10887 26845,9947 27210,9652

209

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010wa2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010wa2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:05 PM" "Back to Contents","Data 1: Washington Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010WA2" "Date","Washington Natural Gas Residential Consumption (MMcf)" 24653,23160 25019,26342 25384,30479 25749,31929 26114,33934 26480,38631

210

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ok2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ok2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:42 AM" "Back to Contents","Data 1: Oklahoma Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040OK2" "Date","Oklahoma Natural Gas Vented and Flared (MMcf)" 35079 35110 35139 35170 35200 35231 35261 35292 35323 35353 35384 35414 35445,0

211

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9132us3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9132us3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 2:23:27 PM" "Back to Contents","Data 1: Price of U.S. Natural Gas Pipeline Exports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9132US3" "Date","Price of U.S. Natural Gas Pipeline Exports (Dollars per Thousand Cubic Feet)" 35445,4.08

212

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040nm2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040nm2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:40 AM" "Back to Contents","Data 1: New Mexico Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040NM2" "Date","New Mexico Natural Gas Vented and Flared (MMcf)" 24653,5992 25019,5987 25384,4058 25749,2909 26114,2823 26480,5696 26845,3791 27210,1227

213

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040sd2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040sd2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:43 AM" "Back to Contents","Data 1: South Dakota Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040SD2" "Date","South Dakota Natural Gas Vented and Flared (MMcf)" 24653,0 25019,0 25384,0 25749,0 26114,0 26480,0 26845,0 27210,0 27575,4 27941,5

214

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040co2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040co2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:33 AM" "Back to Contents","Data 1: Colorado Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040CO2" "Date","Colorado Natural Gas Vented and Flared (MMcf)" 24653,2656 25019,1514 25384,1326 25749,7126 26114,2843 26480,4758 26845,3008 27210,2957

215

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3035us4a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3035us4a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:25:09 PM" "Back to Contents","Data 1: Percent of Industrial Natural Gas Deliveries in U.S. Total Represented by the Price (%)" "Sourcekey","N3035US4" "Date","Percent of Industrial Natural Gas Deliveries in U.S. Total Represented by the Price (%)"

216

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U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ny2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ny2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:41 AM" "Back to Contents","Data 1: New York Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040NY2" "Date","New York Natural Gas Vented and Flared (MMcf)" 33253,0 33284,0 33312,1 33343,0 33373,0 33404,0 33434,0 33465,0 33496,0

217

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ma2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ma2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:29 PM" "Back to Contents","Data 1: Massachusetts Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010MA2" "Date","Massachusetts Natural Gas Residential Consumption (MMcf)" 24653,73471 25019,74919 25384,78451 25749,82646 26114,83434 26480,86171

218

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U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040mt2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040mt2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:39 AM" "Back to Contents","Data 1: Montana Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040MT2" "Date","Montana Natural Gas Vented and Flared (MMcf)" 35079,32 35110,38 35139,34 35170,40 35200,43 35231,27 35261,63 35292,59 35323,60

219

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040us2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040us2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:45 AM" "Back to Contents","Data 1: U.S. Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040US2" "Date","U.S. Natural Gas Vented and Flared (MMcf)" 13331,392528 13696,526159 14061,649106 14426,677311 14792,655967 15157,630212 15522,626782 15887,684115

220

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040mi2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040mi2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:38 AM" "Back to Contents","Data 1: Michigan Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040MI2" "Date","Michigan Natural Gas Vented and Flared (MMcf)" 35079,277 35110,277 35139,277 35170,277 35200,277 35231,277 35261,277

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


221

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1997" Annual",2012,"6/30/1997" ,"Data 2","Futures Prices",4,"Annual",2012,"6/30/1993" ,"Release Date:","12/18/2013" ,"Next Release Date:","12/27/2013" ,"Excel File Name:","ng_pri_fut_s1_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_pri_fut_s1_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/18/2013 12:22:13 PM" "Back to Contents","Data 1: Spot Price" "Sourcekey","RNGWHHD","NGM_EPG0_PLC_NUS_DMMBTU" "Date","Henry Hub Natural Gas Spot Price (Dollars per Million Btu)","U.S. Natural Gas Liquid Composite Price (Dollars per Million Btu)"

222

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9012us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9012us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:55:55 AM" "Back to Contents","Data 1: U.S. Natural Gas Gross Withdrawals from Oil Wells (MMcf)" "Sourcekey","N9012US2" "Date","U.S. Natural Gas Gross Withdrawals from Oil Wells (MMcf)" 33253,475614 33526,500196 33984,513068 34015,462218

223

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ne2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ne2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:40 AM" "Back to Contents","Data 1: Nebraska Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040NE2" "Date","Nebraska Natural Gas Vented and Flared (MMcf)" 33253,0 33284,0 33312,0 33343,0 33373,0 33404,0 33434,0 33465,0 33496,0

224

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040pa2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040pa2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:43 AM" "Back to Contents","Data 1: Pennsylvania Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040PA2" "Date","Pennsylvania Natural Gas Vented and Flared (MMcf)" 33253,0 33284,0 33312,0 33343,0 33373,0 33404,0 33434,0 33465,0

225

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9050us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9050us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:57:04 AM" "Back to Contents","Data 1: U.S. Natural Gas Marketed Production (MMcf)" "Sourcekey","N9050US2" "Date","U.S. Natural Gas Marketed Production (MMcf)" 26679,1948000 26710,1962000 26738,1907000 26769,1814000 26799,1898000 26830,1839000

226

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

mbbl_a.xls" mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_crd_crpdn_adc_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/27/2013 9:07:23 AM" "Back to Contents","Data 1: Crude Oil Production" "Sourcekey","MCRFPUS1","MCRFPP11","MCRFPFL1","MCRFPNY1","MCRFPPA1","MCRFPVA1","MCRFPWV1","MCRFPP21","MCRFPIL1","MCRFPIN1","MCRFPKS1","MCRFPKY1","MCRFP_SMI_1","MCRFPMO1","MCRFPNE1","MCRFPND1","MCRFPOH1","MCRFPOK1","MCRFPSD1","MCRFPTN1","MCRFPP31","MCRFPAL1","MCRFPAR1","MCRFPLA1","MCRFPMS1","MCRFPNM1","MCRFPTX1","MCRFP3FM1","MCRFPP41","MCRFPCO1","MCRFPMT1","MCRFPUT1","MCRFPWY1","MCRFPP51","MCRFPAK1","MCRFPAKS1","MANFPAK1","MCRFPAZ1","MCRFPCA1","MCRFPNV1","MCRFP5F1"

227

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020al2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020al2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:11 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Alabama (MMcf)" "Sourcekey","N3020AL2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Alabama (MMcf)"

228

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9100us3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9100us3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 3:53:51 PM" "Back to Contents","Data 1: Price of U.S. Natural Gas Imports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9100US3" "Date","Price of U.S. Natural Gas Imports (Dollars per Thousand Cubic Feet)" 31228,3.21 31593,2.43 31958,1.95 32324,1.84

229

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/18/2013" ,"Next Release Date:","12/27/2013" ,"Excel File Name:","rngc1a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/rngc1a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/18/2013 12:22:41 PM" "Back to Contents","Data 1: Natural Gas Futures Contract 1 (Dollars per Million Btu)" "Sourcekey","RNGC1" "Date","Natural Gas Futures Contract 1 (Dollars per Million Btu)" 34515,1.934 34880,1.692 35246,2.502 35611,2.475 35976,2.156 36341,2.319

230

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9130us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9130us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 2:23:23 PM" "Back to Contents","Data 1: U.S. Natural Gas Exports (MMcf)" "Sourcekey","N9130US2" "Date","U.S. Natural Gas Exports (MMcf)" 26679,5808 26710,6079 26738,4021 26769,8017 26799,8741 26830,4131 26860,5744 26891,8726 26922,6403 26952,5473

231

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ks3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ks3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:26 PM" "Back to Contents","Data 1: Kansas Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010KS3" "Date","Kansas Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

232

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ca2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ca2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:33 AM" "Back to Contents","Data 1: California Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040CA2" "Date","California Natural Gas Vented and Flared (MMcf)" 35079,97 35110,103 35139,109 35170,107 35200,107 35231,104 35261,108

233

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 3:54:17 PM" "Back to Contents","Data 1: U.S. Liquefied Natural Gas Imports (MMcf)" "Sourcekey","N9103US2" "Date","U.S. Liquefied Natural Gas Imports (MMcf)" 35445,9977 35476,7667 35504,2530 35535,2557 35565,5007 35596,5059 35626,5026 35657,7535

234

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040mt2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040mt2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:39 AM" "Back to Contents","Data 1: Montana Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040MT2" "Date","Montana Natural Gas Vented and Flared (MMcf)" 24653,5022 25019,12551 25384,26458 25749,5203 26114,4917 26480,4222 26845,3691 27210,3901

235

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040tx2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040tx2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:44 AM" "Back to Contents","Data 1: Texas Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040TX2" "Date","Texas Natural Gas Vented and Flared (MMcf)" 33253,2478 33284,2147 33312,2113 33343,2353 33373,3203 33404,2833 33434,3175

236

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9130us3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9130us3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 2:23:24 PM" "Back to Contents","Data 1: Price of U.S. Natural Gas Exports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9130US3" "Date","Price of U.S. Natural Gas Exports (Dollars per Thousand Cubic Feet)" 31228,4.77 31593,2.81 31958,3.07 32324,2.74

237

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ny2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ny2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:41 AM" "Back to Contents","Data 1: New York Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040NY2" "Date","New York Natural Gas Vented and Flared (MMcf)" 24653,0 25019,0 25384,0 25749,0 26114,0 26480,0 26845,0 27210,0 27575,0 27941,0 28306,0 28671,0

238

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ks2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ks2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:35 AM" "Back to Contents","Data 1: Kansas Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040KS2" "Date","Kansas Natural Gas Vented and Flared (MMcf)" 24653,2630 25019,2529 25384,2666 25749,2713 26114,2669 26480,2681 26845,2377 27210,889 27575,846

239

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ar2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ar2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:32 AM" "Back to Contents","Data 1: Arkansas Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040AR2" "Date","Arkansas Natural Gas Vented and Flared (MMcf)" 33253,23 33284,13 33312,12 33343,7 33373,13 33404,28 33434,28 33465,30

240

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010de2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010de2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:15 PM" "Back to Contents","Data 1: Delaware Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010DE2" "Date","Delaware Natural Gas Residential Consumption (MMcf)" 24653,6844 25019,7068 25384,7475 25749,7843 26114,8172 26480,8358 26845,7514

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


241

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

mbblpd_a.xls" mbblpd_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_crd_crpdn_adc_mbblpd_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/27/2013 9:07:25 AM" "Back to Contents","Data 1: Crude Oil Production" "Sourcekey","MCRFPUS2","MCRFPP12","MCRFPFL2","MCRFPNY2","MCRFPPA2","MCRFPVA2","MCRFPWV2","MCRFPP22","MCRFPIL2","MCRFPIN2","MCRFPKS2","MCRFPKY2","MCRFP_SMI_2","MCRFPMO2","MCRFPNE2","MCRFPND2","MCRFPOH2","MCRFPOK2","MCRFPSD2","MCRFPTN2","MCRFPP32","MCRFPAL2","MCRFPAR2","MCRFPLA2","MCRFPMS2","MCRFPNM2","MCRFPTX2","MCRFP3FM2","MCRFPP42","MCRFPCO2","MCRFPMT2","MCRFPUT2","MCRFPWY2","MCRFPP52","MCRFPAK2","MCRFPAKS2","MANFPAK2","MCRFPAZ2","MCRFPCA2","MCRFPNV2","MCRFP5F2"

242

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ngm_epg0_fgc_sky_mmcfm.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/ngm_epg0_fgc_sky_mmcfm.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:59:11 AM" "Back to Contents","Data 1: Kentucky Natural Gas Gross Withdrawals from Coalbed Wells (MMcf) " "Sourcekey","NGM_EPG0_FGC_SKY_MMCF" "Date","Kentucky Natural Gas Gross Withdrawals from Coalbed Wells (MMcf) "

243

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020hi3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020hi3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:34 PM" "Back to Contents","Data 1: Hawaii Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3020HI3" "Date","Hawaii Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)"

244

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

poe2_dcu_nus-z00_a.xls" poe2_dcu_nus-z00_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe2_dcu_nus-z00_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:58:44 PM" "Back to Contents","Data 1: U.S. Total Exports " "Sourcekey","N9132US2","N9132US3","N9133US2","N9133US3" "Date","U.S. Natural Gas Pipeline Exports (MMcf)","Price of U.S. Natural Gas Pipeline Exports (Dollars per Thousand Cubic Feet)","Liquefied U.S. Natural Gas Exports (MMcf)","Price of Liquefied U.S. Natural Gas Exports (Dollars per Thousand Cubic Feet)"

245

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ms2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ms2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:38 AM" "Back to Contents","Data 1: Mississippi Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040MS2" "Date","Mississippi Natural Gas Vented and Flared (MMcf)" 24653,7098 25019,5910 25384,8097 25749,7233 26114,5090 26480,3672 26845,10767 27210,10787

246

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ok3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ok3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:50 PM" "Back to Contents","Data 1: Oklahoma Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010OK3" "Date","Oklahoma Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

247

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010nd3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010nd3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:40 PM" "Back to Contents","Data 1: North Dakota Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010ND3" "Date","North Dakota Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

248

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040or2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040or2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:42 AM" "Back to Contents","Data 1: Oregon Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040OR2" "Date","Oregon Natural Gas Vented and Flared (MMcf)" 35246 35611,0 35976,0 36341,0 36707,0 37072,0 37437,0 37802,0 38168,0 38533,0 38898,0 39263,0

249

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ky2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ky2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:27 PM" "Back to Contents","Data 1: Kentucky Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010KY2" "Date","Kentucky Natural Gas Residential Consumption (MMcf)" 24653,69542 25019,75824 25384,83815 25749,86473 26114,84197 26480,85881

250

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9160us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9160us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:33:48 PM" "Back to Contents","Data 1: U.S. Natural Gas Lease and Plant Fuel Consumption (MMcf)" "Sourcekey","N9160US2" "Date","U.S. Natural Gas Lease and Plant Fuel Consumption (MMcf)" 29235,93000 29266,87000 29295,93000 29326,85000

251

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9030us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9030us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:28 AM" "Back to Contents","Data 1: U.S. Nonhydrocarbon Gases Removed from Natural Gas (MMcf)" "Sourcekey","N9030US2" "Date","U.S. Nonhydrocarbon Gases Removed from Natural Gas (MMcf)" 26679 26710 26738 26769 26799 26830 26860 26891

252

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010mi3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010mi3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:33 PM" "Back to Contents","Data 1: Michigan Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010MI3" "Date","Michigan Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

253

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9070us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9070us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:57:08 AM" "Back to Contents","Data 1: U.S. Dry Natural Gas Production (MMcf)" "Sourcekey","N9070US2" "Date","U.S. Dry Natural Gas Production (MMcf)" 35445,1617923 35476,1465907 35504,1627602 35535,1551268 35565,1610527 35596,1525325

254

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9102us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9102us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 3:53:55 PM" "Back to Contents","Data 1: U.S. Natural Gas Pipeline Imports (MMcf)" "Sourcekey","N9102US2" "Date","U.S. Natural Gas Pipeline Imports (MMcf)" 35445,268310 35476,232878 35504,254455 35535,235621 35565,236725 35596,227059 35626,230567

255

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010wy2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010wy2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:08 PM" "Back to Contents","Data 1: Wyoming Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010WY2" "Date","Wyoming Natural Gas Residential Consumption (MMcf)" 24653,11939 25019,12592 25384,16592 25749,17984 26114,19463 26480,22242 26845,13868

256

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020ak2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020ak2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:09 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Alaska (MMcf)" "Sourcekey","N3020AK2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Alaska (MMcf)"

257

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:00 PM" "Back to Contents","Data 1: U.S. Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010US2" "Date","U.S. Natural Gas Residential Consumption (MMcf)" 26679,843900 26710,747331 26738,648504 26769,465867 26799,326313

258

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010mt2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010mt2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:38 PM" "Back to Contents","Data 1: Montana Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010MT2" "Date","Montana Natural Gas Residential Consumption (MMcf)" 24653,19756 25019,19711 25384,21463 25749,24794 26114,25379 26480,23787 26845,24923

259

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103us3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103us3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 3:54:18 PM" "Back to Contents","Data 1: Price of U.S. Natural Gas LNG Imports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9103US3" "Date","Price of U.S. Natural Gas LNG Imports (Dollars per Thousand Cubic Feet)" 35445,3 35476,3

260

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9132us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9132us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 2:23:27 PM" "Back to Contents","Data 1: U.S. Natural Gas Pipeline Exports (MMcf)" "Sourcekey","N9132US2" "Date","U.S. Natural Gas Pipeline Exports (MMcf)" 35445,6424 35476,6846 35504,10601 35535,8211 35565,6284 35596,5741 35626,6380 35657,10101

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


261

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3035us4m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3035us4m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:25:10 PM" "Back to Contents","Data 1: Percent of Industrial Natural Gas Deliveries in U.S. Total Represented by the Price (%)" "Sourcekey","N3035US4" "Date","Percent of Industrial Natural Gas Deliveries in U.S. Total Represented by the Price (%)"

262

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010wi3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010wi3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:06 PM" "Back to Contents","Data 1: Wisconsin Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010WI3" "Date","Wisconsin Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

263

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040al2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040al2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:31 AM" "Back to Contents","Data 1: Alabama Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040AL2" "Date","Alabama Natural Gas Vented and Flared (MMcf)" 35079,194 35110,200 35139,140 35170,132 35200,106 35231,82 35261,205 35292,152

264

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040wv2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040wv2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:46 AM" "Back to Contents","Data 1: West Virginia Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040WV2" "Date","West Virginia Natural Gas Vented and Flared (MMcf)" 33253,0 33284,0 33312,0 33343,0 33373,0 33404,0 33434,0 33465,0

265

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/1993" Monthly","9/2013","1/15/1993" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_pnp_pct_dc_nus_pct_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_pct_dc_nus_pct_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:23:48 AM" "Back to Contents","Data 1: U.S. Refinery Yield" "Sourcekey","MLRRYUS3","MGFRYUS3","MGARYUS3","MKJRYUS3","MKERYUS3","MDIRYUS3","MRERYUS3","MNFRYUS3","MOTRYUS3","MNSRYUS3","MLURYUS3","MWXRYUS3","MCKRYUS3","MAPRYUS3","MSGRYUS3","MMSRYUS3","MPGRYUS3"

266

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:23:36 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in the U.S. (MMcf)" "Sourcekey","N3020US2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in the U.S. (MMcf)"

267

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U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:45 AM" "Back to Contents","Data 1: U.S. Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040US2" "Date","U.S. Natural Gas Vented and Flared (MMcf)" 26679 26710 26738 26769 26799 26830 26860 26891 26922 26952 26983 27013 27044 27075 27103

268

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","11/2013","1/15/1997" Monthly","11/2013","1/15/1997" ,"Data 2","Futures Prices",4,"Monthly","11/2013","12/15/1993" ,"Release Date:","12/18/2013" ,"Next Release Date:","12/27/2013" ,"Excel File Name:","ng_pri_fut_s1_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_pri_fut_s1_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/18/2013 12:22:17 PM" "Back to Contents","Data 1: Spot Price" "Sourcekey","RNGWHHD","NGM_EPG0_PLC_NUS_DMMBTU"

269

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010pa3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010pa3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:52 PM" "Back to Contents","Data 1: Pennsylvania Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010PA3" "Date","Pennsylvania Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

270

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ut3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ut3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:02 PM" "Back to Contents","Data 1: Utah Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010UT3" "Date","Utah Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

271

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010dc2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010dc2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:13 PM" "Back to Contents","Data 1: District of Columbia Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010DC2" "Date","District of Columbia Natural Gas Residential Consumption (MMcf)" 29402,13730 29767,13686 30132,13041 30497,13007

272

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010tx3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010tx3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:00 PM" "Back to Contents","Data 1: Texas Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010TX3" "Date","Texas Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

273

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1993" Annual",2012,"6/30/1993" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_stoc_typ_d_nus_skn_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_stoc_typ_d_nus_skn_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:41:29 AM" "Back to Contents","Data 1: U.S. Natural Gas Processing Plant " "Sourcekey","MAOSNUS1","MPPSNUS1","MLPSNUS1","METSNUS1","MPRSNUS1","MBNSNUS1","MBISNUS1"

274

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040az2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040az2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:32 AM" "Back to Contents","Data 1: Arizona Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040AZ2" "Date","Arizona Natural Gas Vented and Flared (MMcf)" 26114,347 26480,367 26845,277 27210,26 27575,47 27941,32 29036,101 29402,143 29767,106 30132,162

275

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020ca3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020ca3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:20 PM" "Back to Contents","Data 1: California Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3020CA3" "Date","California Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)"

276

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010oh3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010oh3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:49 PM" "Back to Contents","Data 1: Ohio Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010OH3" "Date","Ohio Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

277

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020fl3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020fl3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:30 PM" "Back to Contents","Data 1: Florida Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3020FL3" "Date","Florida Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)"

278

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ks2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ks2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:36 AM" "Back to Contents","Data 1: Kansas Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040KS2" "Date","Kansas Natural Gas Vented and Flared (MMcf)" 35079,63 35110,63 35139,63 35170,61 35200,62 35231,57 35261,57 35292,55 35323,56

279

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040nv2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040nv2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:41 AM" "Back to Contents","Data 1: Nevada Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040NV2" "Date","Nevada Natural Gas Vented and Flared (MMcf)" 33253,0 33284,0 33312,0 33343,0 33373,0 33404,0 33434,0 33465,0 33496,0 33526,0

280

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ms2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ms2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:38 AM" "Back to Contents","Data 1: Mississippi Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040MS2" "Date","Mississippi Natural Gas Vented and Flared (MMcf)" 35079,217 35110,199 35139,223 35170,219 35200,237 35231,234 35261,239

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


281

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9103us3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9103us3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 3:54:18 PM" "Back to Contents","Data 1: Price of U.S. Natural Gas LNG Imports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9103US3" "Date","Price of U.S. Natural Gas LNG Imports (Dollars per Thousand Cubic Feet)" 31228,4.6 31593,4.62 32324,2.71

282

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9130us3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9130us3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 2:23:24 PM" "Back to Contents","Data 1: Price of U.S. Natural Gas Exports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9130US3" "Date","Price of U.S. Natural Gas Exports (Dollars per Thousand Cubic Feet)" 32523,2.69 32554,2.4

283

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040tx2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040tx2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:44 AM" "Back to Contents","Data 1: Texas Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040TX2" "Date","Texas Natural Gas Vented and Flared (MMcf)" 24653,129403 25019,124584 25384,111499 25749,100305 26114,70222 26480,59821 26845,36133 27210,34431

284

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010al2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010al2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:07 PM" "Back to Contents","Data 1: Alabama Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010AL2" "Date","Alabama Natural Gas Residential Consumption (MMcf)" 24653,45543 25019,51708 25384,54804 25749,55779 26114,54867 26480,53397 26845,55685

285

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010mi2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010mi2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:33 PM" "Back to Contents","Data 1: Michigan Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010MI2" "Date","Michigan Natural Gas Residential Consumption (MMcf)" 24653,302472 25019,315694 25384,333264 25749,340033 26114,343773 26480,355266

286

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010co3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010co3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:12 PM" "Back to Contents","Data 1: Colorado Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010CO3" "Date","Colorado Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

287

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010wa3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010wa3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:05 PM" "Back to Contents","Data 1: Washington Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010WA3" "Date","Washington Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

288

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ak2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ak2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:05 PM" "Back to Contents","Data 1: Alaska Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010AK2" "Date","Alaska Natural Gas Residential Consumption (MMcf)" 24653,1958 25019,2293 25384,4573 25749,6211 26114,6893 26480,8394 26845,5024

289

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ar2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ar2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:08 PM" "Back to Contents","Data 1: Arkansas Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010AR2" "Date","Arkansas Natural Gas Residential Consumption (MMcf)" 24653,52777 25019,56346 25384,58322 25749,59792 26114,48737 26480,47387

290

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2010 Annual",2010 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ok2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ok2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:42 AM" "Back to Contents","Data 1: Oklahoma Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040OK2" "Date","Oklahoma Natural Gas Vented and Flared (MMcf)" 24653,126629 25019,129408 25384,130766 25749,129629 26114,39799 26480,38797 26845,36411

291

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020us4m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020us4m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:23:38 PM" "Back to Contents","Data 1: Percent of Commercial Natural Gas Deliveries in U.S. Total Represented by the Price (%)" "Sourcekey","N3020US4" "Date","Percent of Commercial Natural Gas Deliveries in U.S. Total Represented by the Price (%)"

292

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ak3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ak3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:06 PM" "Back to Contents","Data 1: Alaska Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010AK3" "Date","Alaska Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

293

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ca3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ca3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:11 PM" "Back to Contents","Data 1: California Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010CA3" "Date","California Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

294

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040la2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040la2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:37 AM" "Back to Contents","Data 1: Louisiana Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040LA2" "Date","Louisiana Natural Gas Vented and Flared (MMcf)" 33253,1788 33284,1684 33312,1571 33343,1593 33373,1807 33404,1690 33434,2042

295

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040tn2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040tn2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:44 AM" "Back to Contents","Data 1: Tennessee Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040TN2" "Date","Tennessee Natural Gas Vented and Flared (MMcf)" 33253,0 33284,0 33312,0 33343,0 33373,0 33404,0 33434,0 33465,0 33496,0

296

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010wi2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010wi2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:06 PM" "Back to Contents","Data 1: Wisconsin Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010WI2" "Date","Wisconsin Natural Gas Residential Consumption (MMcf)" 24653,90994 25019,93425 25384,101124 25749,105208 26114,109758 26480,104648

297

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020us4a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020us4a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:23:38 PM" "Back to Contents","Data 1: Percent of Commercial Natural Gas Deliveries in U.S. Total Represented by the Price (%)" "Sourcekey","N3020US4" "Date","Percent of Commercial Natural Gas Deliveries in U.S. Total Represented by the Price (%)"

298

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010nh3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010nh3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:43 PM" "Back to Contents","Data 1: New Hampshire Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010NH3" "Date","New Hampshire Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

299

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010in2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010in2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:24 PM" "Back to Contents","Data 1: Indiana Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010IN2" "Date","Indiana Natural Gas Residential Consumption (MMcf)" 24653,139519 25019,145955 25384,156699 25749,158699 26114,162747 26480,169267

300

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020ct3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020ct3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:23 PM" "Back to Contents","Data 1: Connecticut Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3020CT3" "Date","Connecticut Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)"

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


301

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010mo3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010mo3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:36 PM" "Back to Contents","Data 1: Missouri Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010MO3" "Date","Missouri Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

302

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040la2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040la2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:36 AM" "Back to Contents","Data 1: Louisiana Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040LA2" "Date","Louisiana Natural Gas Vented and Flared (MMcf)" 24653,161849 25019,166439 25384,158852 25749,154089 26114,103564 26480,63667 26845,102091

303

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ut2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ut2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:46 AM" "Back to Contents","Data 1: Utah Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040UT2" "Date","Utah Natural Gas Vented and Flared (MMcf)" 34592,646 34834,696 34865,4590 34895,4767 34926,4382 34957,4389 34987,4603 35018,4932

304

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010az2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010az2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:09 PM" "Back to Contents","Data 1: Arizona Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010AZ2" "Date","Arizona Natural Gas Residential Consumption (MMcf)" 24653,25376 25019,26681 25384,28426 25749,29679 26114,32619 26480,34259 26845,36280

305

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ak3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ak3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:06 PM" "Back to Contents","Data 1: Alaska Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010AK3" "Date","Alaska Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

306

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9132us3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9132us3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 2:23:27 PM" "Back to Contents","Data 1: Price of U.S. Natural Gas Pipeline Exports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9132US3" "Date","Price of U.S. Natural Gas Pipeline Exports (Dollars per Thousand Cubic Feet)" 31228,3.92 31593,2.35

307

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010id3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010id3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:23 PM" "Back to Contents","Data 1: Idaho Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010ID3" "Date","Idaho Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

308

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010me2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010me2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:32 PM" "Back to Contents","Data 1: Maine Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010ME2" "Date","Maine Natural Gas Residential Consumption (MMcf)" 24653,3967 25019,3571 25384,4910 25749,5247 26114,5591 26480,6036 26845,6027 27210,6174

309

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ne3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ne3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:42 PM" "Back to Contents","Data 1: Nebraska Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010NE3" "Date","Nebraska Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

310

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040wy2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040wy2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:47 AM" "Back to Contents","Data 1: Wyoming Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040WY2" "Date","Wyoming Natural Gas Vented and Flared (MMcf)" 24653,1498 25019,13038 25384,17632 25749,18419 26114,3860 26480,8376 26845,6618 27210,6102

311

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010mn3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010mn3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:34 PM" "Back to Contents","Data 1: Minnesota Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010MN3" "Date","Minnesota Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

312

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ca2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ca2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:10 PM" "Back to Contents","Data 1: California Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010CA2" "Date","California Natural Gas Residential Consumption (MMcf)" 24653,522122 25019,517636 25384,562127 25749,552544 26114,630998 26480,637289

313

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040sd2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040sd2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:43 AM" "Back to Contents","Data 1: South Dakota Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040SD2" "Date","South Dakota Natural Gas Vented and Flared (MMcf)" 33253,384 33284,350 33312,382 33343,380 33373,382 33404,376 33434,405

314

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040nm2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040nm2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:41 AM" "Back to Contents","Data 1: New Mexico Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040NM2" "Date","New Mexico Natural Gas Vented and Flared (MMcf)" 35079,236 35110,220 35139,240 35170,230 35200,241 35231,229 35261,217

315

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010co2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010co2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:11 PM" "Back to Contents","Data 1: Colorado Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010CO2" "Date","Colorado Natural Gas Residential Consumption (MMcf)" 24653,75351 25019,78371 25384,81068 25749,82595 26114,84864 26480,89187

316

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Daily","12/17/2013" Daily","12/17/2013" ,"Release Date:","12/18/2013" ,"Next Release Date:","12/27/2013" ,"Excel File Name:","rngc2d.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/rngc2d.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/18/2013 12:22:40 PM" "Back to Contents","Data 1: Natural Gas Futures Contract 2 (Dollars per Million Btu)" "Sourcekey","RNGC2" "Date","Natural Gas Futures Contract 2 (Dollars per Million Btu)" 34346,2.13 34347,2.072 34348,2.139 34351,2.196 34352,2.131

317

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ar3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ar3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:08 PM" "Back to Contents","Data 1: Arkansas Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010AR3" "Date","Arkansas Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

318

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040mo2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040mo2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:38 AM" "Back to Contents","Data 1: Missouri Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040MO2" "Date","Missouri Natural Gas Vented and Flared (MMcf)" 33253,0 33284,0 33312,0 33343,0 33373,0 33404,0 33434,0 33465,0 33496,0

319

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Daily","12/17/2013" Daily","12/17/2013" ,"Release Date:","12/18/2013" ,"Next Release Date:","12/27/2013" ,"Excel File Name:","rngc4d.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/rngc4d.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/18/2013 12:22:29 PM" "Back to Contents","Data 1: Natural Gas Futures Contract 4 (Dollars per Million Btu)" "Sourcekey","RNGC4" "Date","Natural Gas Futures Contract 4 (Dollars per Million Btu)" 34323,1.894 34324,1.83 34325,1.859 34326,1.895 34330,1.965

320

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9010us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9010us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:55:17 AM" "Back to Contents","Data 1: U.S. Natural Gas Gross Withdrawals (MMcf)" "Sourcekey","N9010US2" "Date","U.S. Natural Gas Gross Withdrawals (MMcf)" 26679 26710 26738 26769 26799 26830 26860 26891 26922 26952 26983 27013 27044 27075 27103

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


321

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ut2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ut2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:45 AM" "Back to Contents","Data 1: Utah Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040UT2" "Date","Utah Natural Gas Vented and Flared (MMcf)" 24653,3000 25019,2906 25384,2802 25749,2852 26114,2926 26480,5506 26845,7664 27210,5259 27575,1806

322

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ak2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ak2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:06 PM" "Back to Contents","Data 1: Alaska Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010AK2" "Date","Alaska Natural Gas Residential Consumption (MMcf)" 32523,1793 32554,2148 32582,1566 32613,1223 32643,858 32674,638

323

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040nd2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040nd2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:39 AM" "Back to Contents","Data 1: North Dakota Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040ND2" "Date","North Dakota Natural Gas Vented and Flared (MMcf)" 24653,25795 25019,22050 25384,22955 25749,19862 26114,2686 26480,20786 26845,22533

324

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010al3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010al3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:07 PM" "Back to Contents","Data 1: Alabama Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010AL3" "Date","Alabama Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

325

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ar3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ar3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:09 PM" "Back to Contents","Data 1: Arkansas Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010AR3" "Date","Arkansas Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

326

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010va2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010va2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:02 PM" "Back to Contents","Data 1: Virginia Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010VA2" "Date","Virginia Natural Gas Residential Consumption (MMcf)" 24653,41495 25019,43582 25384,46663 25749,49554 26114,49488 26480,55427

327

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040co2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040co2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:33 AM" "Back to Contents","Data 1: Colorado Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040CO2" "Date","Colorado Natural Gas Vented and Flared (MMcf)" 35079,112 35110,77 35139,78 35170,91 35200,100 35231,89 35261,100 35292,106

328

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ga2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ga2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:17 PM" "Back to Contents","Data 1: Georgia Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010GA2" "Date","Georgia Natural Gas Residential Consumption (MMcf)" 24653,80322 25019,84072 25384,87878 25749,87359 26114,88319 26480,85256 26845,86191

329

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020hi2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020hi2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:33 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Hawaii (MMcf)" "Sourcekey","N3020HI2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Hawaii (MMcf)"

330

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020ga2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020ga2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:31 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Georgia (MMcf)" "Sourcekey","N3020GA2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Georgia (MMcf)"

331

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020ar2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020ar2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:14 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Arkansas (MMcf)" "Sourcekey","N3020AR2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Arkansas (MMcf)"

332

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ct2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ct2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:12 PM" "Back to Contents","Data 1: Connecticut Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010CT2" "Date","Connecticut Natural Gas Residential Consumption (MMcf)" 24653,26177 25019,26437 25384,29048 25749,31187 26114,31878 26480,32879

333

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010dc3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010dc3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:14 PM" "Back to Contents","Data 1: District of Columbia Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010DC3" "Date","District of Columbia Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

334

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ri3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ri3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:54 PM" "Back to Contents","Data 1: Rhode Island Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010RI3" "Date","Rhode Island Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

335

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010sd3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010sd3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:56 PM" "Back to Contents","Data 1: South Dakota Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010SD3" "Date","South Dakota Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

336

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020de2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020de2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:26 PM" "Back to Contents","Data 1: Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Delaware (MMcf)" "Sourcekey","N3020DE2" "Date","Natural Gas Deliveries to Commercial Consumers (Including Vehicle Fuel through 1996) in Delaware (MMcf)"

337

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010tn3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010tn3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:58 PM" "Back to Contents","Data 1: Tennessee Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010TN3" "Date","Tennessee Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

338

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ny3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ny3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:48 PM" "Back to Contents","Data 1: New York Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010NY3" "Date","New York Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

339

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010or2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010or2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:51 PM" "Back to Contents","Data 1: Oregon Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010OR2" "Date","Oregon Natural Gas Residential Consumption (MMcf)" 24653,13427 25019,15126 25384,20507 25749,19742 26114,21217 26480,23331 26845,22271

340

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9140us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9140us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:33:47 PM" "Back to Contents","Data 1: U.S. Natural Gas Total Consumption (MMcf)" "Sourcekey","N9140US2" "Date","U.S. Natural Gas Total Consumption (MMcf)" 36906,2676998 36937,2309464 36965,2246633 36996,1807170 37026,1522382 37057,1444378

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


341

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Daily","12/17/2013" Daily","12/17/2013" ,"Release Date:","12/18/2013" ,"Next Release Date:","12/27/2013" ,"Excel File Name:","rngc1d.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/rngc1d.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/18/2013 12:22:45 PM" "Back to Contents","Data 1: Natural Gas Futures Contract 1 (Dollars per Million Btu)" "Sourcekey","RNGC1" "Date","Natural Gas Futures Contract 1 (Dollars per Million Btu)" 34347,2.194 34348,2.268 34351,2.36 34352,2.318 34353,2.252

342

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010fl3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010fl3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:16 PM" "Back to Contents","Data 1: Florida Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010FL3" "Date","Florida Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

343

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3035us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3035us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:25:08 PM" "Back to Contents","Data 1: U.S. Natural Gas Industrial Consumption (MMcf)" "Sourcekey","N3035US2" "Date","U.S. Natural Gas Industrial Consumption (MMcf)" 36906,686540 36937,640026 36965,664918 36996,622054 37026,576532 37057,536820

344

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040fl2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040fl2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:34 AM" "Back to Contents","Data 1: Florida Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040FL2" "Date","Florida Natural Gas Vented and Flared (MMcf)" 26114,355 26480,284 27941,837 28306,607 29402,677 29767,428 30132,435 30497,198 30863,34

345

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ok2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ok2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:50 PM" "Back to Contents","Data 1: Oklahoma Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010OK2" "Date","Oklahoma Natural Gas Residential Consumption (MMcf)" 24653,67395 25019,74782 25384,75310 25749,77460 26114,75238 26480,77608

346

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ar2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ar2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:31 AM" "Back to Contents","Data 1: Arkansas Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040AR2" "Date","Arkansas Natural Gas Vented and Flared (MMcf)" 24653,997 25019,895 25384,1326 25749,226 26114,1734 26480,2649 26845,1947 27210,1716 27575,1318

347

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010me3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010me3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:32 PM" "Back to Contents","Data 1: Maine Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010ME3" "Date","Maine Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

348

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3060us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3060us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:27:25 PM" "Back to Contents","Data 1: Natural Gas Delivered to Consumers in the U.S. (MMcf)" "Sourcekey","N3060US2" "Date","Natural Gas Delivered to Consumers in the U.S. (MMcf)" 36906,2505011 36937,2156873 36965,2086568 36996,1663832

349

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010us2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010us2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:00 PM" "Back to Contents","Data 1: U.S. Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010US2" "Date","U.S. Natural Gas Residential Consumption (MMcf)" 11139,295700 11504,294406 11870,298520 12235,283197 12600,288236 12965,313498 13331,343346

350

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010in3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010in3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:25 PM" "Back to Contents","Data 1: Indiana Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010IN3" "Date","Indiana Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

351

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9011us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9011us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:55:36 AM" "Back to Contents","Data 1: U.S. Natural Gas Gross Withdrawals from Gas Wells (MMcf)" "Sourcekey","N9011US2" "Date","U.S. Natural Gas Gross Withdrawals from Gas Wells (MMcf)" 33253,1482053 33526,1363737 33984,1452098 34015,1305490

352

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020us3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020us3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:23:37 PM" "Back to Contents","Data 1: U.S. Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3020US3" "Date","U.S. Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)"

353

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010nv3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010nv3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:46 PM" "Back to Contents","Data 1: Nevada Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010NV3" "Date","Nevada Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

354

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9133us3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9133us3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 2:23:31 PM" "Back to Contents","Data 1: Price of Liquefied U.S. Natural Gas Exports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9133US3" "Date","Price of Liquefied U.S. Natural Gas Exports (Dollars per Thousand Cubic Feet)"

355

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010sc3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010sc3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:55 PM" "Back to Contents","Data 1: South Carolina Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010SC3" "Date","South Carolina Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

356

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010vt2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010vt2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:03 PM" "Back to Contents","Data 1: Vermont Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010VT2" "Date","Vermont Natural Gas Residential Consumption (MMcf)" 29402,1301 29767,1290 30132,1278 30497,1252 30863,1352 31228,1456 31593,1595

357

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Weekly","12/13/2013","1/10/1997" Weekly","12/13/2013","1/10/1997" ,"Data 2","Futures Prices",4,"Weekly","12/13/2013","12/24/1993" ,"Release Date:","12/18/2013" ,"Next Release Date:","12/27/2013" ,"Excel File Name:","ng_pri_fut_s1_w.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_pri_fut_s1_w.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/18/2013 12:22:18 PM" "Back to Contents","Data 1: Spot Price" "Sourcekey","RNGWHHD" "Date","Weekly Henry Hub Natural Gas Spot Price (Dollars per Million Btu)"

358

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040in2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040in2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:35 AM" "Back to Contents","Data 1: Indiana Natural Gas Vented and Flared (Million Cubic Feet)" "Sourcekey","N9040IN2" "Date","Indiana Natural Gas Vented and Flared (Million Cubic Feet)" 33253,0 33284,0 33312,0 33343,0 33373,0

359

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3020ga3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3020ga3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:32 PM" "Back to Contents","Data 1: Georgia Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3020GA3" "Date","Georgia Price of Natural Gas Sold to Commercial Consumers (Dollars per Thousand Cubic Feet)"

360

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010hi3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010hi3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:20 PM" "Back to Contents","Data 1: Hawaii Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010HI3" "Date","Hawaii Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


361

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ks2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ks2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:26 PM" "Back to Contents","Data 1: Kansas Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010KS2" "Date","Kansas Natural Gas Residential Consumption (MMcf)" 24653,84912 25019,89372 25384,94320 25749,97317 26114,98644 26480,100720 26845,96468

362

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9100us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9100us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 3:53:50 PM" "Back to Contents","Data 1: U.S. Natural Gas Imports (MMcf)" "Sourcekey","N9100US2" "Date","U.S. Natural Gas Imports (MMcf)" 26679,92694 26710,83870 26738,91581 26769,88407 26799,85844 26830,79121 26860,79428 26891,84400 26922,81157

363

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ga3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ga3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:18 PM" "Back to Contents","Data 1: Georgia Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010GA3" "Date","Georgia Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

364

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9133us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9133us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 2:23:31 PM" "Back to Contents","Data 1: Liquefied U.S. Natural Gas Exports (MMcf)" "Sourcekey","N9133US2" "Date","Liquefied U.S. Natural Gas Exports (MMcf)" 35445,5604 35476,5596 35504,5675 35535,5660 35565,3812 35596,3786 35626,3756 35657,7532

365

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9170us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9170us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:33:48 PM" "Back to Contents","Data 1: U.S. Natural Gas Pipeline & Distribution Use (MMcf)" "Sourcekey","N9170US2" "Date","U.S. Natural Gas Pipeline & Distribution Use (MMcf)" 36906,76386 36937,65770 36965,63626 36996,50736

366

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","na1504_nus_4a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/na1504_nus_4a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:46:13 PM" "Back to Contents","Data 1: U.S. Natural Gas % of Total Residential - Sales (%)" "Sourcekey","NA1504_NUS_4" "Date","U.S. Natural Gas % of Total Residential - Sales (%)" 32689,99.9 33054,99.2 33419,99.2 33785,99.1 34150,99.1 34515,99.1

367

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ct3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ct3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:13 PM" "Back to Contents","Data 1: Connecticut Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010CT3" "Date","Connecticut Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

368

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010us3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010us3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:01 PM" "Back to Contents","Data 1: U.S. Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010US3" "Date","U.S. Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

369

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040fl2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040fl2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:34 AM" "Back to Contents","Data 1: Florida Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040FL2" "Date","Florida Natural Gas Vented and Flared (MMcf)" 35079 35110 35139 35170 35200 35231 35261 35292 35323 35353 35384 35414 35445,0

370

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040mi2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040mi2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:37 AM" "Back to Contents","Data 1: Michigan Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040MI2" "Date","Michigan Natural Gas Vented and Flared (MMcf)" 24653,1861 25019,1120 25384,808 25749,809 26480,1032 26845,1117 27210,1268 27575,1612

371

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010ar2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010ar2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:08 PM" "Back to Contents","Data 1: Arkansas Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010AR2" "Date","Arkansas Natural Gas Residential Consumption (MMcf)" 32523,6774 32554,7118 32582,6736 32613,3835 32643,1927 32674,1402

372

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010la3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010la3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:29 PM" "Back to Contents","Data 1: Louisiana Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010LA3" "Date","Louisiana Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

373

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9100us3m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9100us3m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/13/2013 3:53:51 PM" "Back to Contents","Data 1: Price of U.S. Natural Gas Imports (Dollars per Thousand Cubic Feet)" "Sourcekey","N9100US3" "Date","Price of U.S. Natural Gas Imports (Dollars per Thousand Cubic Feet)" 32523,1.72 32554,1.88

374

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ne2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ne2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:40 AM" "Back to Contents","Data 1: Nebraska Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040NE2" "Date","Nebraska Natural Gas Vented and Flared (MMcf)" 24653,0 25019,0 25384,0 25749,0 26114,1558 26480,1263 26845,834 27210,2137 27575,1398 27941,797

375

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9020us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9020us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:13 AM" "Back to Contents","Data 1: U.S. Natural Gas Repressuring (MMcf)" "Sourcekey","N9020US2" "Date","U.S. Natural Gas Repressuring (MMcf)" 26679 26710 26738 26769 26799 26830 26860 26891 26922 26952 26983 27013 27044 27075 27103 27134 27164

376

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2010 Annual",2010 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040pa2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040pa2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:43 AM" "Back to Contents","Data 1: Pennsylvania Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040PA2" "Date","Pennsylvania Natural Gas Vented and Flared (MMcf)" 24653,0 25019,0 25384,0 25749,0 26114,0 26480,0 26845,0 27210,98 27575,96 27941,99

377

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010oh2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010oh2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:48 PM" "Back to Contents","Data 1: Ohio Natural Gas Residential Consumption (MMcf)" "Sourcekey","N3010OH2" "Date","Ohio Natural Gas Residential Consumption (MMcf)" 24653,442360 25019,444964 25384,456414 25749,459972 26114,460820 26480,478331 26845,439212

378

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n9040ca2a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n9040ca2a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/19/2013 6:56:32 AM" "Back to Contents","Data 1: California Natural Gas Vented and Flared (MMcf)" "Sourcekey","N9040CA2" "Date","California Natural Gas Vented and Flared (MMcf)" 24653,3565 25019,2780 25384,3074 25749,2499 26114,575 26845,1999 27210,1560 27575,1537

379

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010us3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010us3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:22:01 PM" "Back to Contents","Data 1: U.S. Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010US3" "Date","U.S. Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

380

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","11/2013" Monthly","11/2013" ,"Release Date:","12/18/2013" ,"Next Release Date:","12/27/2013" ,"Excel File Name:","rngc1m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/rngc1m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/18/2013 12:22:41 PM" "Back to Contents","Data 1: Natural Gas Futures Contract 1 (Dollars per Million Btu)" "Sourcekey","RNGC1" "Date","Natural Gas Futures Contract 1 (Dollars per Million Btu)" 34349,2.347 34380,2.355 34408,2.109 34439,2.111 34469,1.941

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


381

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012 Annual",2012 ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3010az3a.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3010az3a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:21:09 PM" "Back to Contents","Data 1: Arizona Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)" "Sourcekey","N3010AZ3" "Date","Arizona Price of Natural Gas Delivered to Residential Consumers (Dollars per Thousand Cubic Feet)"

382

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013" Monthly","9/2013" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","n3045us2m.xls" ,"Available from Web Page:","http://tonto.eia.gov/dnav/ng/hist/n3045us2m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.doe.gov" ,,"(202) 586-8800",,,"12/12/2013 5:26:13 PM" "Back to Contents","Data 1: U.S. Natural Gas Deliveries to Electric Power Consumers (MMcf)" "Sourcekey","N3045US2" "Date","U.S. Natural Gas Deliveries to Electric Power Consumers (MMcf)" 36906,340292 36937,312843 36965,362843

383

Metal-sulfur type cell having improved positive electrode  

DOE Patents [OSTI]

An novel metal-sulfur type cell operable at a temperature of 200.degree. C. or less with an energy density of 150 Whrs/Kg or better is disclosed characterized by an organo-sulfur cathode formed from an organic-sulfur compound having the general formula, in its charged state, of (R(S).sub.y).sub.n wherein y=1 to 6; n=2 to 20; and R is one or more different aliphatic or aromatic organic moieties having 1 to 20 carbon atoms, which may include one or more oxygen, sulfur, or nitrogen heteroatoms when R comprisises one of more aromatic rings, or one or more oxygen, sulfur, nitrogen, or fluorine atoms associtated with the chain when R comprises an aliphatic chain, wherein the aliphatic group may be linear or branched, saturated or unsaturated, and wherein either the aliphatic chain or the aromatic ring may have substituted groups thereon.

Dejonghe, Lutgard C. (Berkeley, CA); Visco, Steven J. (Berkeley, CA); Mailhe, Catherine C. (Berkeley, CA); Armand, Michel B. (St. Martin D'Uriage, FR)

1989-01-01T23:59:59.000Z

384

Carbon/Sulfur Nanocomposites and Additives for High-Energy Lithium...  

Broader source: Energy.gov (indexed) [DOE]

May 2011 CarbonSulfur Nanocomposites and Additives for High-Energy Lithium Sulfur Batteries "This presentation does not contain any proprietary, confidential, or otherwise...

385

E-Print Network 3.0 - amoco sulfur recovery process Sample Search...  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

and Medicine 80 Sulfur and oxygen isotope composition of the atmosphere in Saxony (Germany) Tichomirowa et al. Summary: ? a) Mixing processes 12;Sulfur and oxygen isotope...

386

TABLE OF CONTENTS TABLE OF CONTENTS ...........................................................................................................................................II  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

i i ii TABLE OF CONTENTS TABLE OF CONTENTS ...........................................................................................................................................II EXECUTIVE SUMMARY ........................................................................................................................................... 3 INTRODUCTION......................................................................................................................................................... 4 COMPLIANCE SUMMARY ....................................................................................................................................... 6 COMPREHENSIVE ENVIRONMENTAL RESPONSE, COMPENSATION, AND LIABILITY ACT (CERCLA) .................... 6

387

Effect of fuel gas composition in chemical-looping combustion with Ni-based oxygen carriers. 1. Fate of sulfur  

SciTech Connect (OSTI)

Chemical-looping combustion (CLC) has been suggested among the best alternatives to reduce the economic cost of CO{sub 2} capture using fuel gas because CO{sub 2} is inherently separated in the process. For gaseous fuels, natural gas, refinery gas, or syngas from coal gasification can be used. These fuels may contain different amounts of sulfur compounds, such as H{sub 2}S and COS. An experimental investigation of the fate of sulfur during CH{sub 4} combustion in a 500 W{sub th} CLC prototype using a Ni-based oxygen carrier has been carried out. The effect on the oxygen carrier behavior and combustion efficiency of several operating conditions such as temperature and H{sub 2}S concentration has been analyzed. Nickel sulfide, Ni3S{sub 2}, was formed at all operating conditions in the fuel reactor, which produced an oxygen carrier deactivation and lower combustion efficiencies. However, the oxygen carrier recovered their initial reactivity after certain time without sulfur addition. The sulfides were transported to the air reactor where SO{sub 2} was produced as final gas product. Agglomeration problems derived from the sulfides formation were never detected during continuous operation. Considering both operational and environmental aspects, fuels with sulfur contents below 100 vppm H{sub 2}S seem to be adequate to be used in an industrial CLC plant.

Garcia-Labiano, F.; de Diego, L.F.; Gayan, P.; Adanez, J.; Abad, A.; Dueso, C. [CSIC, Zaragoza (Spain)

2009-03-15T23:59:59.000Z

388

High pressure sulfuric acid decomposition experiments for the sulfur-iodine thermochemical cycle.  

SciTech Connect (OSTI)

A series of three pressurized sulfuric acid decomposition tests were performed to (1) obtain data on the fraction of sulfuric acid catalytically converted to sulfur dioxide, oxygen, and water as a function of temperature and pressure, (2) demonstrate real-time measurements of acid conversion for use as process control, (3) obtain multiple measurements of conversion as a function of temperature within a single experiment, and (4) assess rapid quenching to minimize corrosion of metallic components by undecomposed acid. All four of these objectives were successfully accomplished. This report documents the completion of the NHI milestone on high pressure H{sub 2}SO{sub 4} decomposition tests for the Sulfur-Iodine (SI) thermochemical cycle project. All heated sections of the apparatus, (i.e. the boiler, decomposer, and condenser) were fabricated from Hastelloy C276. A ceramic acid injection tube and a ceramic-sheathed thermocouple were used to minimize corrosion of hot liquid acid on the boiler surfaces. Negligible fracturing of the platinum on zirconia catalyst was observed in the high temperature decomposer. Temperature measurements at the exit of the decomposer and at the entry of the condenser indicated that the hot acid vapors were rapidly quenched from about 400 C to less than 20 C within a 14 cm length of the flow path. Real-time gas flow rate measurements of the decomposition products provided a direct measurement of acid conversion. Pressure in the apparatus was preset by a pressure-relief valve that worked well at controlling the system pressure. However, these valves sometimes underwent abrupt transitions that resulted in rapidly varying gas flow rates with concomitant variations in the acid conversion fraction.

Velasquez, Carlos E; Reay, Andrew R.; Andazola, James C.; Naranjo, Gerald E.; Gelbard, Fred

2005-09-01T23:59:59.000Z

389

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/1997" Monthly","9/2013","1/15/1997" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_sum_lsum_a_epg0_fpd_mmcf_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_sum_lsum_a_epg0_fpd_mmcf_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/19/2013 6:41:46 AM" "Back to Contents","Data 1: Natural Gas Dry Production (Annual Supply & Disposition) " "Sourcekey","N9070US2","NA1160_R3FM_2","NA1160_SAL_2","NA1160_SAK_2","NA1160_SAZ_2","NA1160_SAR_2","NA1160_SCA_2","NA1160_SCO_2","NA1160_SFL_2","NA1160_SIL_2","NA1160_SIN_2","NA1160_SKS_2","NA1160_SKY_2","NA1160_SLA_2","NA1160_SMD_2","NA1160_SMI_2","NA1160_SMS_2","NA1160_SMO_2","NA1160_SMT_2","NA1160_SNE_2","NA1160_SNV_2","NA1160_SNM_2","NA1160_SNY_2","NA1160_SND_2","NA1160_SOH_2","NA1160_SOK_2","NA1160_SOR_2","NA1160_SPA_2","NA1160_SSD_2","NA1160_STN_2","NA1160_STX_2","NA1160_SUT_2","NA1160_SVA_2","NA1160_SWV_2","NA1160_SWY_2"

390

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1930" Annual",2012,"6/30/1930" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_sum_snd_a_epg0_fpd_mmcf_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_sum_snd_a_epg0_fpd_mmcf_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 7:08:03 PM" "Back to Contents","Data 1: Natural Gas Dry Production (Annual Supply & Disposition) " "Sourcekey","N9070US2","NA1160_SAL_2","NA1160_SAK_2","NA1160_SAZ_2","NA1160_SAR_2","NA1160_SCA_2","NA1160_SCO_2","NA1160_SFL_2","NA1160_R3FM_2","NA1160_SIL_2","NA1160_SIN_2","NA1160_SKS_2","NA1160_SKY_2","NA1160_SLA_2","NA1160_SMD_2","NA1160_SMI_2","NA1160_SMS_2","NA1160_SMO_2","NA1160_SMT_2","NA1160_SNE_2","NA1160_SNV_2","NA1160_SNM_2","NA1160_SNY_2","NA1160_SND_2","NA1160_SOH_2","NA1160_SOK_2","NA1160_SOR_2","NA1160_SPA_2","NA1160_SSD_2","NA1160_STN_2","NA1160_STX_2","NA1160_SUT_2","NA1160_SVA_2","NA1160_SWV_2","NA1160_SWY_2"

391

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

mbblpd_m.xls" mbblpd_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_exp_dc_nus-z00_mbblpd_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 7:27:48 AM" "Back to Contents","Data 1: U.S. Exports of Crude Oil and Petroleum Products" "Sourcekey","MTTEXUS2","MCREXUS2","MNGEXUS2","MPPEXUS2","MLPEXUS2","METEXUS2","MPREXUS2","MBNEXUS2","MBIEXUS2","MOLEXUS2","MOHEXUS2","M_EPOOXXFE_EEX_NUS-Z00_MBBLD","MMTEX_NUS-Z00_2","MOOEX_NUS-Z00_2","M_EPOOR_EEX_NUS-Z00_MBBLD","M_EPOOXE_EEX_NUS-Z00_MBBLD","M_EPOORDB_EEX_NUS-Z00_MBBLD","MBCEXUS2","MO1EX_NUS-Z00_2","MO5EX_NUS-Z00_2","MBAEXUS2","MTPEXUS2","MGFEXUS2","MGREXUS2","MG4EX_NUS-Z00_2","MGAEXUS2","MKJEXUS2","MKEEXUS2","MDIEXUS2","M_EPDXL0_EEX_NUS-Z00_MBBLD","MD1EX_NUS-Z00_2","MDGEXUS2","MREEXUS2","MNFEXUS2","MOTEXUS2","MNSEXUS2","MLUEXUS2","MWXEXUS2","MCKEXUS2","MAPEXUS2","MMSEXUS2"

392

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

mbbl_m.xls" mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_cons_psup_dc_nus_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 7:26:09 AM" "Back to Contents","Data 1: U.S. Product Supplied for Crude Oil and Petroleum Products" "Sourcekey","MTTUPUS1","MCRUPUS1","MNGUPUS1","MPPUPUS1","MLPUPUS1","METUPUS1","MPRUPUS1","MBNUPUS1","MBIUPUS1","MOLUPUS1","MOHUPUS1","MUOUPUS1","MBCUPUS1","MO1UP_NUS_1","MO5UP_NUS_1","MBAUPUS1","MTPUPUS1","MGFUPUS1","MGRUPUS1","MG4UP_NUS_1","MGAUPUS1","MKJUPUS1","MKEUPUS1","MDIUPUS1","MD0UP_NUS_1","MD1UP_NUS_1","MDGUPUS1","MREUPUS1","MPCUP_NUS_1","MNFUPUS1","MOTUPUS1","MNSUPUS1","MLUUPUS1","MWXUPUS1","MCKUPUS1","MCMUP_NUS_1","MCOUP_NUS_1","MAPUPUS1","MSGUPUS1","MMSUPUS1"

393

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/1985" Monthly","9/2013","1/15/1985" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_pnp_unc_dcu_nus_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_unc_dcu_nus_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:30:03 AM" "Back to Contents","Data 1: U.S. Refinery Utilization and Capacity" "Sourcekey","MGIRIUS2","MOCLEUS2","MOCGGUS2","MOCIDUS2","MOPUEUS2" "Date","U.S. Gross Inputs to Refineries (Thousand Barrels Per Day)","U. S. Operable Crude Oil Distillation Capacity (Thousand Barrels per Calendar Day)","U. S. Operating Crude Oil Distillation Capacity (Thousand Barrels per Day)","U. S. Idle Crude Oil Distillation Capacity (Thousand Barrels per Day)","U.S. Percent Utilization of Refinery Operable Capacity"

394

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

capwork_a_(na)_8sw0_mbbl_a.xls" capwork_a_(na)_8sw0_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_capwork_a_(na)_8sw0_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"6/20/2013 4:20:16 PM" "Back to Contents","Data 1: Total " "Sourcekey","8_NA_8SW0_NUS_MBBL","8_NA_8SW0_R10_MBBL","8_NA_8SW0_R20_MBBL","8_NA_8SW0_R30_MBBL","8_NA_8SW0_R40_MBBL","8_NA_8SW0_R50_MBBL" "Date","U.S. Refinery Working Storage Capacity as of January 1 (Thousand Barrels)","East Coast (PADD 1) Refinery Working Storage Capacity as of January 1 (Thousand Barrels)","Midwest (PADD 2) Refinery Working Storage Capacity as of January 1 (Thousand Barrels)","Gulf Coast (PADD 3) Refinery Working Storage Capacity as of January 1 (Thousand Barrels)","Rocky Mountain (PADD 4) Refinery Working Storage Capacity as of January 1 (Thousand Barrels)","West Coast (PADD 5) Refinery Working Storage Capacity as of January 1 (Thousand Barrels)"

395

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

mbblpd_m.xls" mbblpd_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_cons_psup_dc_nus_mbblpd_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 7:26:11 AM" "Back to Contents","Data 1: U.S. Product Supplied for Crude Oil and Petroleum Products" "Sourcekey","MTTUPUS2","MCRUPUS2","MNGUPUS2","MPPUPUS2","MLPUPUS2","METUPUS2","MPRUPUS2","MBNUPUS2","MBIUPUS2","MOLUPUS2","MOHUPUS2","MUOUPUS2","MBCUPUS2","MO1UP_NUS_2","MO5UP_NUS_2","MBAUPUS2","MTPUPUS2","MGFUPUS2","MGRUPUS2","MG4UP_NUS_2","MGAUPUS2","MKJUPUS2","MKEUPUS2","MDIUPUS2","MD0UP_NUS_2","MD1UP_NUS_2","MDGUPUS2","MREUPUS2","MPCUP_NUS_2","MNFUPUS2","MOTUPUS2","MNSUPUS2","MLUUPUS2","MWXUPUS2","MCKUPUS2","MCMUP_NUS_2","MCOUP_NUS_2","MAPUPUS2","MSGUPUS2","MMSUPUS2"

396

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

capshell_a_(na)_8ss0_mbbl_a.xls" capshell_a_(na)_8ss0_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_capshell_a_(na)_8ss0_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"6/20/2013 4:17:24 PM" "Back to Contents","Data 1: Total " "Sourcekey","8_NA_8SS0_NUS_MBBL","8_NA_8SS0_R10_MBBL","8_NA_8SS0_R20_MBBL","8_NA_8SS0_R30_MBBL","8_NA_8SS0_R40_MBBL","8_NA_8SS0_R50_MBBL" "Date","U.S. Refinery Shell Storage Capacity as of January 1 (Thousand Barrels)","East Coast (PADD 1) Refinery Shell Storage Capacity as of January 1 (Thousand Barrels)","Midwest (PADD 2) Refinery Shell Storage Capacity as of January 1 (Thousand Barrels)","Gulf Coast (PADD 3) Refinery Shell Storage Capacity as of January 1 (Thousand Barrels)","Rocky Mountain (PADD 4) Refinery Shell Storage Capacity as of January 1 (Thousand Barrels)","West Coast (PADD 5) Refinery Shell Storage Capacity as of January 1 (Thousand Barrels)"

397

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1936" Annual",2012,"6/30/1936" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_pnp_refp_dc_nus_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_refp_dc_nus_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:25:40 AM" "Back to Contents","Data 1: U.S. Refinery and Blender Net Production" "Sourcekey","MTTRPUS1","MLPRPUS1","METRPUS1","MENRPUS1","MEYRPUS1","MPRRPUS1","MPARP_NUS_1","MPLRPUS1","MBNRPUS1","MBURPUS1","MBYRPUS1","MBIRPUS1","MIIRPUS1","MIYRPUS1","MGFRPUS1","MGRRPUS1","MG1RP_NUS_1","M_EPM0RO_YPR_NUS_MBBL","MG4RP_NUS_1","MG5RP_NUS_1","M_EPM0CAL55_YPR_NUS_MBBL","M_EPM0CAG55_YPR_NUS_MBBL","MG6RP_NUS_1","MGARPUS1","MKJRPUS1","MKERPUS1","MDIRPUS1","MD0RP_NUS_1","MD1RP_NUS_1","MDGRPUS1","MRERPUS1","MRLRPUS1","MRMRPUS1","MRGRPUS1","MPCRPUS1","MNFRPUS1","MOTRPUS1","MNSRPUS1","MLURPUS1","MWXRPUS1","MCKRPUS1","MCMRPUS1","MCORPUS1","MAPRPUS1","MSGRPUS1","MMSRPUS1","MPGRPUS1"

398

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1981" Annual",2012,"6/30/1981" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_pnp_inpt_dc_nus_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_inpt_dc_nus_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:19:29 AM" "Back to Contents","Data 1: U.S. Refinery & Blender Net Input" "Sourcekey","MTTRIUS1","MCRRIUS1","MNGRIUS1","MPPRIUS1","MLPRIUS1","METRIUS1","MBNRIUS1","MBIRIUS1","MOLRIUS1","MOHRIUS1","M_EPOOOH_YIR_NUS_MBBL","M_EPOOXXFE_YIR_NUS_MBBL","MMTRIUS1","MOORIUS1","M_EPOOR_YIR_NUS_MBBL","MFERIUS1","M_EPOORD_YIR_NUS_MBBL","M_EPOORO_YIR_NUS_MBBL","M_EPOOOXH_YIR_NUS_MBBL","MUORIUS1","MNLRI_NUS_1","MKORI_NUS_1","MH1RI_NUS_1","MRURI_NUS_1","MBCRIUS1","MO1RI_NUS_1","M_EPOBGRR_YIR_NUS_MBBL","MO3RI_NUS_1","MO4RI_NUS_1","MO2RI_NUS_1","MO5RI_NUS_1","MO6RI_NUS_1","MO7RI_NUS_1","MO9RI_NUS_1","MBARIUS1"

399

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/1936" Monthly","9/2013","1/15/1936" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_pnp_refp_dc_nus_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_pnp_refp_dc_nus_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:25:41 AM" "Back to Contents","Data 1: U.S. Refinery and Blender Net Production" "Sourcekey","MTTRPUS1","MLPRPUS1","METRPUS1","MENRPUS1","MEYRPUS1","MPRRPUS1","MPARP_NUS_1","MPLRPUS1","MBNRPUS1","MBURPUS1","MBYRPUS1","MBIRPUS1","MIIRPUS1","MIYRPUS1","MGFRPUS1","MGRRPUS1","MG1RP_NUS_1","M_EPM0RO_YPR_NUS_MBBL","MG4RP_NUS_1","MG5RP_NUS_1","M_EPM0CAL55_YPR_NUS_MBBL","M_EPM0CAG55_YPR_NUS_MBBL","MG6RP_NUS_1","MGARPUS1","MKJRPUS1","MKERPUS1","MDIRPUS1","MD0RP_NUS_1","MD1RP_NUS_1","MDGRPUS1","MRERPUS1","MRLRPUS1","MRMRPUS1","MRGRPUS1","MPCRPUS1","MNFRPUS1","MOTRPUS1","MNSRPUS1","MLURPUS1","MWXRPUS1","MCKRPUS1","MCMRPUS1","MCORPUS1","MAPRPUS1","MSGRPUS1","MMSRPUS1","MPGRPUS1"

400

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

mbbl_m.xls" mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_exp_dc_nus-z00_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 7:27:47 AM" "Back to Contents","Data 1: U.S. Exports of Crude Oil and Petroleum Products" "Sourcekey","MTTEXUS1","MCREXUS1","MNGEXUS1","MPPEXUS1","MLPEXUS1","METEXUS1","MPREXUS1","MBNEXUS1","MBIEXUS1","MOLEXUS1","MOHEXUS1","M_EPOOXXFE_EEX_NUS-Z00_MBBL","MMTEX_NUS-Z00_1","MOOEX_NUS-Z00_1","M_EPOOR_EEX_NUS-Z00_MBBL","M_EPOOXE_EEX_NUS-Z00_MBBL","M_EPOORDB_EEX_NUS-Z00_MBBL","MBCEXUS1","MO1EX_NUS-Z00_1","MO5EX_NUS-Z00_1","MBAEXUS1","MTPEXUS1","MGFEXUS1","MGREXUS1","MG4EX_NUS-Z00_1","MGAEXUS1","MKJEXUS1","MKEEXUS1","MDIEXUS1","M_EPDXL0_EEX_NUS-Z00_MBBL","MD1EX_NUS-Z00_1","MDGEXUS1","MREEXUS1","MNFEXUS1","MOTEXUS1","MNSEXUS1","MLUEXUS1","MWXEXUS1","MCKEXUS1","MAPEXUS1","MMSEXUS1"

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


401

Performance and cost models for the direct sulfur recovery process. Task 1 Topical report, Volume 3  

SciTech Connect (OSTI)

The purpose of this project is to develop performance and cost models of the Direct Sulfur Recovery Process (DSRP). The DSRP is an emerging technology for sulfur recovery from advanced power generation technologies such as Integrated Gasification Combined Cycle (IGCC) systems. In IGCC systems, sulfur present in the coal is captured by gas cleanup technologies to avoid creating emissions of sulfur dioxide to the atmosphere. The sulfur that is separated from the coal gas stream must be collected. Leading options for dealing with the sulfur include byproduct recovery as either sulfur or sulfuric acid. Sulfur is a preferred byproduct, because it is easier to handle and therefore does not depend as strongly upon the location of potential customers as is the case for sulfuric acid. This report describes the need for new sulfur recovery technologies.

Frey, H.C. [North Carolina State Univ., Raleigh, NC (United States); Williams, R.B. [Carneigie Mellon Univ., Pittsburgh, PA (United States)

1995-09-01T23:59:59.000Z

402

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Natural Gas Marketed Production ",35,"Monthly","9/2013","1/15/1973" Natural Gas Marketed Production ",35,"Monthly","9/2013","1/15/1973" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_prod_whv_a_epg0_vgm_mmcf_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_prod_whv_a_epg0_vgm_mmcf_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/19/2013 6:54:27 AM" "Back to Contents","Data 1: Natural Gas Marketed Production " "Sourcekey","N9050US2","N9050FX2","N9050AL2","N9050AK2","N9050AZ2","N9050AR2","N9050CA2","N9050CO2","N9050FL2","N9050IL2","N9050IN2","N9050KS2","N9050KY2","N9050LA2","N9050MD2","N9050MI2","N9050MS2","N9050MO2","N9050MT2","N9050NE2","N9050NV2","N9050NM2","N9050NY2","N9050ND2","N9050OH2","N9050OK2","N9050OR2","N9050PA2","N9050SD2","N9050TN2","N9050TX2","N9050UT2","N9050VA2","N9050WV2","N9050WY2"

403

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1870" Annual",2012,"6/30/1870" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_exp_dc_nus-z00_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_exp_dc_nus-z00_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 7:27:46 AM" "Back to Contents","Data 1: U.S. Exports of Crude Oil and Petroleum Products" "Sourcekey","MTTEXUS1","MCREXUS1","MNGEXUS1","MPPEXUS1","MLPEXUS1","METEXUS1","MPREXUS1","MBNEXUS1","MBIEXUS1","MOLEXUS1","MOHEXUS1","M_EPOOXXFE_EEX_NUS-Z00_MBBL","MMTEX_NUS-Z00_1","MOOEX_NUS-Z00_1","M_EPOOR_EEX_NUS-Z00_MBBL","M_EPOOXE_EEX_NUS-Z00_MBBL","M_EPOORDB_EEX_NUS-Z00_MBBL","MBCEXUS1","MO1EX_NUS-Z00_1","MO5EX_NUS-Z00_1","MBAEXUS1","MTPEXUS1","MGFEXUS1","MGREXUS1","MG4EX_NUS-Z00_1","MGAEXUS1","MKJEXUS1","MKEEXUS1","MDIEXUS1","M_EPDXL0_EEX_NUS-Z00_MBBL","MD1EX_NUS-Z00_1","MDGEXUS1","MREEXUS1","MNFEXUS1","MOTEXUS1","MNSEXUS1","MLUEXUS1","MWXEXUS1","MCKEXUS1","MAPEXUS1","MMSEXUS1"

404

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/2002" Monthly","9/2013","1/15/2002" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_pri_sum_a_epg0_vrx_pct_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_pri_sum_a_epg0_vrx_pct_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 7:00:27 PM" "Back to Contents","Data 1: Percentage of Total Natural Gas Residential Deliveries included in Prices " "Sourcekey","NA1504_NUS_4","NA1504_SAL_4","NA1504_SAK_4","NA1504_SAZ_4","NA1504_SAR_4","NA1504_SCA_4","NA1504_SCO_4","NA1504_SCT_4","NA1504_SDE_4","NA1504_SDC_4","NA1504_SFL_4","NA1504_SGA_4","NA1504_SHI_4","NA1504_SID_4","NA1504_SIL_4","NA1504_SIN_4","NA1504_SIA_4","NA1504_SKS_4","NA1504_SKY_4","NA1504_SLA_4","NA1504_SME_4","NA1504_SMD_4","NA1504_SMA_4","NA1504_SMI_4","NA1504_SMN_4","NA1504_SMS_4","NA1504_SMO_4","NA1504_SMT_4","NA1504_SNE_4","NA1504_SNV_4","NA1504_SNH_4","NA1504_SNJ_4","NA1504_SNM_4","NA1504_SNY_4","NA1504_SNC_4","NA1504_SND_4","NA1504_SOH_4","NA1504_SOK_4","NA1504_SOR_4","NA1504_SPA_4","NA1504_SRI_4","NA1504_SSC_4","NA1504_SSD_4","NA1504_STN_4","NA1504_STX_4","NA1504_SUT_4","NA1504_SVT_4","NA1504_SVA_4","NA1504_SWA_4","NA1504_SWV_4","NA1504_SWI_4","NA1504_SWY_4"

405

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

60,"Monthly","9/2013","1/15/1981" 60,"Monthly","9/2013","1/15/1981" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_stoc_typ_d_nus_skr_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_stoc_typ_d_nus_skr_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:41:32 AM" "Back to Contents","Data 1: U.S. Refinery " "Sourcekey","MTTRSUS1","MCRRSUS1","MPERSUS1","MPPRSUS1","MLPRSUS1","METRSUS1","MPRRSUS1","MBNRSUS1","MBIRSUS1","M_EPOOOXH_SKR_NUS_MBBL","M_EPOOXXFE_SKR_NUS_MBBL","MMTRSUS1","MOORSUS1","M_EPOOR_SKR_NUS_MBBL","MFERSUS1","M_EPOORD_SKR_NUS_MBBL","M_EPOORO_SKR_NUS_MBBL","MUORSUS1","MNLRSUS1","MKORSUS1","MH1RSUS1","MRURSUS1","MBCRSUS1","MO1RS_NUS_1","M_EPOBGRR_SKR_NUS_MBBL","MO3RS_NUS_1","MO4RS_NUS_1","MO5RS_NUS_1","MO6RS_NUS_1","MO7RS_NUS_1","MO9RS_NUS_1","MBARSUS1","MGFRSUS1","MGRRSUS1","MG1RS_NUS_1","M_EPM0RO_SKR_NUS_MBBL","MG4RS_NUS_1","MG5RS_NUS_1","M_EPM0CAL55_SKR_NUS_MBBL","MG6RS_NUS_1","MGARSUS1","MKJRSUS1","MKERSUS1","MDIRSUS1","MD0RS_NUS_1","MD1RS_NUS_1","MDGRSUS1","MRERSUS1","MRLRSUS1","MRMRSUS1","MRGRSUS1","MPCRS_NUS_1","MNFRSUS1","MOTRSUS1","MNSRSUS1","MLURSUS1","MWXRSUS1","MCKRSUS1","MAPRSUS1","MMSRSUS1"

406

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

56,"Annual",2012,"6/30/1981" 56,"Annual",2012,"6/30/1981" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_stoc_typ_d_nus_skr_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_stoc_typ_d_nus_skr_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:41:31 AM" "Back to Contents","Data 1: U.S. Refinery " "Sourcekey","MTTRSUS1","MCRRSUS1","MPERSUS1","MPPRSUS1","MLPRSUS1","METRSUS1","MPRRSUS1","MBNRSUS1","MBIRSUS1","M_EPOOOXH_SKR_NUS_MBBL","M_EPOOXXFE_SKR_NUS_MBBL","MMTRSUS1","MOORSUS1","M_EPOOR_SKR_NUS_MBBL","MFERSUS1","M_EPOORD_SKR_NUS_MBBL","MUORSUS1","MNLRSUS1","MKORSUS1","MH1RSUS1","MRURSUS1","MBCRSUS1","MO1RS_NUS_1","M_EPOBGRR_SKR_NUS_MBBL","MO3RS_NUS_1","MO5RS_NUS_1","MO6RS_NUS_1","MO9RS_NUS_1","MBARSUS1","MGFRSUS1","MGRRSUS1","MG1RS_NUS_1","MG4RS_NUS_1","MG5RS_NUS_1","M_EPM0CAL55_SKR_NUS_MBBL","MG6RS_NUS_1","MGARSUS1","MKJRSUS1","MKERSUS1","MDIRSUS1","MD0RS_NUS_1","MD1RS_NUS_1","MDGRSUS1","MRERSUS1","MRLRSUS1","MRMRSUS1","MRGRSUS1","MPCRS_NUS_1","MNFRSUS1","MOTRSUS1","MNSRSUS1","MLURSUS1","MWXRSUS1","MCKRSUS1","MAPRSUS1","MMSRSUS1"

407

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

2,"Monthly","9/2013","1/15/1973" 2,"Monthly","9/2013","1/15/1973" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_move_poe2_a_epg0_enp_mmcf_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe2_a_epg0_enp_mmcf_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:58:29 PM" "Back to Contents","Data 1: U.S. Natural Gas Pipeline Exports by Point of Exit " "Sourcekey","N9132US2","N9132CN2","NA1287_YEPRT-NCA_2","NGA_EPG0_ENP_YCAL-NCA_MMCF","NA1287_YDTW-NCA_2","NA1287_YMARY-NCA_2","NA1287_YSSM-NCA_2","NA1287_YCHRE-NCA_2","NA1287_YNOYS-NCA_2","NA1287_YBAB-NCA_2","NA1287_YHVR-NCA_2","NGA_EPG0_ENP_YPITT-NCA_MMCF","NGM_EPG0_ENP_YGRIS-NCA_MMCF","NGM_EPG0_ENP_YMSS-NCA_MMCF","NA1287_YUSNI-NCA_2","NGM_EPG0_ENP_YWADD-NCA_MMCF","NA1287_YSUMS-NCA_2","N9132MX2","NA1287_YDUG-NMX_2","NA_EPG0_ENP_YNOGS-NMX_MMCF","NA1287_YCAX-NMX_2","NA1287_YOESA-NMX_2","NA1287_YALA-NMX_2","NA1287_YCLI-NMX_2","NA_EPG0_ENP_YDRT-NMX_MMCF","NA1287_YEGP-NMX_2","NA1287_YELP-NMX_2","NA1287_YHDGO-NMX_2","NA1287_YMFE-NMX_2","NA1287_YPENI-NMX_2","NA1287_Y44RB-NMX_2","NA1287_Y44RM-NMX_2"

408

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

65,"Monthly","9/2013","1/15/1956" 65,"Monthly","9/2013","1/15/1956" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_sum_snd_a_ep00_mbbl_m_cur.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_sum_snd_a_ep00_mbbl_m_cur.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/27/2013 6:57:53 AM" "Back to Contents","Data 1: Total Crude Oil and Petroleum Products Supply and Disposition" "Sourcekey","MTTFPUS1","M_EP00_YNP_NUS_MBBL","MTTRPUS1","MTTIMUS1","MTTUA_NUS_1","MTTSCUS1","MTTRIUS1","MTTEXUS1","MTTUPUS1","MTTSTUS1","MTTFPP11","M_EP00_YNP_R10_MBBL","MTTRPP11","MTTIMP11","MTTNRP11","MTTUA_R10_1","MTTSCP11","MTTRIP11","MTTEXP11","MTTUPP11","MTTSTP11","MTTFPP21","M_EP00_YNP_R20_MBBL","MTTRPP21","MTTIMP21","MTTNRP21","MTTUA_R20_1","MTTSCP21","MTTRIP21","MTTEXP21","MTTUPP21","MTTSTP21","MTTFPP31","M_EP00_YNP_R30_MBBL","MTTRPP31","MTTIMP31","MTTNRP31","MTTUA_R30_1","MTTSCP31","MTTRIP31","MTTEXP31","MTTUPP31","MTTSTP31","MTTFPP41","M_EP00_YNP_R40_MBBL","MTTRPP41","MTTIMP41","MTTNRP41","MTTUA_R40_1","MTTSCP41","MTTRIP41","MTTEXP41","MTTUPP41","MTTSTP41","MTTFPP51","M_EP00_YNP_R50_MBBL","MTTRPP51","MTTIMP51","MTTNRP51","MTTUA_R50_1","MTTSCP51","MTTRIP51","MTTEXP51","MTTUPP51","MTTSTP51"

409

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

59,"Monthly","9/2013","1/15/1963" 59,"Monthly","9/2013","1/15/1963" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_sum_snd_a_ep00_mbblpd_m_cur.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_sum_snd_a_ep00_mbblpd_m_cur.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/27/2013 6:57:55 AM" "Back to Contents","Data 1: Total Crude Oil and Petroleum Products Supply and Disposition" "Sourcekey","MTTFPUS2","M_EP00_YNP_NUS_MBBLD","MTTRPUS2","MTTIMUS2","MTTUA_NUS_2","MTTSCUS2","MTTRIUS2","MTTEXUS2","MTTUPUS2","MTTFPP12","M_EP00_YNP_R10_MBBLD","MTTRPP12","MTTIMP12","MTTNRP12","MTTUA_R10_2","MTTSCP12","MTTRIP12","MTTEXP12","MTTUPP12","MTTFPP22","M_EP00_YNP_R20_MBBLD","MTTRPP22","MTTIMP22","MTTNRP22","MTTUA_R20_2","MTTSCP22","MTTRIP22","MTTEXP22","MTTUPP22","MTTFPP32","M_EP00_YNP_R30_MBBLD","MTTRPP32","MTTIMP32","MTTNRP32","MTTUA_R30_2","MTTSCP32","MTTRIP32","MTTEXP32","MTTUPP32","MTTFPP42","M_EP00_YNP_R40_MBBLD","MTTRPP42","MTTIMP42","MTTNRP42","MTTUA_R40_2","MTTSCP42","MTTRIP42","MTTEXP42","MTTUPP42","MTTFPP52","M_EP00_YNP_R50_MBBLD","MTTRPP52","MTTIMP52","MTTNRP52","MTTUA_R50_2","MTTSCP52","MTTRIP52","MTTEXP52","MTTUPP52"

410

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

2,"Monthly","9/2013","1/15/1989" 2,"Monthly","9/2013","1/15/1989" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_move_poe2_a_epg0_pnp_dpmcf_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe2_a_epg0_pnp_dpmcf_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:58:32 PM" "Back to Contents","Data 1: U.S. Price of Natural Gas Pipeline Exports by Point of Exit " "Sourcekey","N9132US3","N9132CN3","NA1287_YEPRT-NCA_3","NGA_EPG0_PNP_YCAL-NCA_DMCF","NA1287_YDTW-NCA_3","NA1287_YMARY-NCA_3","NA1287_YSSM-NCA_3","NA1287_YCHRE-NCA_3","NA1287_YNOYS-NCA_3","NA1287_YBAB-NCA_3","NA1287_YHVR-NCA_3","NGA_EPG0_PNP_YPITT-NCA_DMCF","NGM_EPG0_PNP_YGRIS-NCA_DMCF","NGM_EPG0_PNP_YMSS-NCA_DMCF","NA1287_YUSNI-NCA_3","NGM_EPG0_PNP_YWADD-NCA_DMCF","NA1287_YSUMS-NCA_3","N9132MX3","NA1287_YDUG-NMX_3","NA_EPG0_PNP_YNOGS-NMX_DMCF","NA1287_YCAX-NMX_3","NA1287_YOESA-NMX_3","NA1287_YALA-NMX_3","NA1287_YCLI-NMX_3","NA_EPG0_PNP_YDRT-NMX_DMCF","NA1287_YEGP-NMX_3","NA1287_YELP-NMX_3","NA1287_YHDGO-NMX_3","NA1287_YMFE-NMX_3","NA1287_YPENI-NMX_3","NA1287_Y44RB-NMX_3","NA1287_Y44RM-NMX_3"

411

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1989" Annual",2012,"6/30/1989" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_pri_sum_a_epg0_vrx_pct_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_pri_sum_a_epg0_vrx_pct_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 7:00:26 PM" "Back to Contents","Data 1: Percentage of Total Natural Gas Residential Deliveries included in Prices " "Sourcekey","NA1504_NUS_4","NA1504_SAL_4","NA1504_SAK_4","NA1504_SAZ_4","NA1504_SAR_4","NA1504_SCA_4","NA1504_SCO_4","NA1504_SCT_4","NA1504_SDE_4","NA1504_SDC_4","NA1504_SFL_4","NA1504_SGA_4","NA1504_SHI_4","NA1504_SID_4","NA1504_SIL_4","NA1504_SIN_4","NA1504_SIA_4","NA1504_SKS_4","NA1504_SKY_4","NA1504_SLA_4","NA1504_SME_4","NA1504_SMD_4","NA1504_SMA_4","NA1504_SMI_4","NA1504_SMN_4","NA1504_SMS_4","NA1504_SMO_4","NA1504_SMT_4","NA1504_SNE_4","NA1504_SNV_4","NA1504_SNH_4","NA1504_SNJ_4","NA1504_SNM_4","NA1504_SNY_4","NA1504_SNC_4","NA1504_SND_4","NA1504_SOH_4","NA1504_SOK_4","NA1504_SOR_4","NA1504_SPA_4","NA1504_SRI_4","NA1504_SSC_4","NA1504_SSD_4","NA1504_STN_4","NA1504_STX_4","NA1504_SUT_4","NA1504_SVT_4","NA1504_SVA_4","NA1504_SWA_4","NA1504_SWV_4","NA1504_SWI_4","NA1504_SWY_4"

412

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1981" Annual",2012,"6/30/1981" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_pipe_dc_r20-r10_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_pipe_dc_r20-r10_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:11:26 AM" "Back to Contents","Data 1: From PADD 1 to PADD 2 Movements by Pipeline" "Sourcekey","MTTMPP2P11","MCRMPP2P11","MPEMPP2P11","MPPMP_R20-R10_1","MLPMPP2P11","MBCMPP2P11","MO5MP_R20-R10_1","MO6MP_R20-R10_1","MO7MP_R20-R10_1","MO9MP_R20-R10_1","M_EPOOR_LMV_R20-R10_MBBL","M_EPOORD_LMV_R20-R10_MBBL","MGFMPP2P11","MGRMPP2P11","MG4MP_R20-R10_1","MG6MP_R20-R10_1","MKJMPP2P11","MKEMPP2P11","MDIMPP2P11","MD0MP_R20-R10_1","MD1MP_R20-R10_1","MDGMPP2P11"

413

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1913" Annual",2012,"6/30/1913" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_stoc_typ_d_nus_sae_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_stoc_typ_d_nus_sae_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:41:10 AM" "Back to Contents","Data 1: U.S. Total Stocks " "Sourcekey","MTTSTUS1","MCRSTUS1","MAOSTUS1","MPPSTUS1","MLPSTUS1","METSTUS1","MPRSTUS1","MBNSTUS1","MBISTUS1","M_EPOOOXH_SAE_NUS_MBBL","M_EPOOXXFE_SAE_NUS_MBBL","MMTSTUS1","MOOSTUS1","M_EPOOR_SAE_NUS_MBBL","MFESTUS1","M_EPOORD_SAE_NUS_MBBL","M_EPOORO_SAE_NUS_MBBL","MUOSTUS1","MNLST_NUS_1","MKOST_NUS_1","MH1ST_NUS_1","MRUST_NUS_1","MBCSTUS1","MO1ST_NUS_1","M_EPOBGRR_SAE_NUS_MBBL","MO3ST_NUS_1","MO4ST_NUS_1","MO2ST_NUS_1","MO5ST_NUS_1","MO6ST_NUS_1","MO7ST_NUS_1","MO9ST_NUS_1","MBASTUS1","MGFSTUS1","MGRSTUS1","MG1ST_NUS_1","M_EPM0RO_SAE_NUS_MBBL","MG4ST_NUS_1","MG5ST_NUS_1","M_EPM0CAL55_SAE_NUS_MBBL","MG6ST_NUS_1","MGASTUS1","MKJSTUS1","MKESTUS1","MDISTUS1","MD0ST_NUS_1","MD1ST_NUS_1","MDGSTUS1","MRESTUS1","MRLSTUS1","MRMSTUS1","MRGSTUS1","MPCST_NUS_1","MNFSTUS1","MOTSTUS1","MNSSTUS1","MLUSTUS1","MWXSTUS1","MCKSTUS1","MAPSTUS1","MMSSTUS1"

414

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/1986" Monthly","9/2013","1/15/1986" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_move_pipe_dc_r20-r10_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_pipe_dc_r20-r10_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:11:27 AM" "Back to Contents","Data 1: From PADD 1 to PADD 2 Movements by Pipeline" "Sourcekey","MTTMPP2P11","MCRMPP2P11","MPEMPP2P11","MPPMP_R20-R10_1","MLPMPP2P11","MBCMPP2P11","MO5MP_R20-R10_1","MO6MP_R20-R10_1","MO7MP_R20-R10_1","MO9MP_R20-R10_1","M_EPOOR_LMV_R20-R10_MBBL","M_EPOORD_LMV_R20-R10_MBBL","MGFMPP2P11","MGRMPP2P11","MG4MP_R20-R10_1","MG6MP_R20-R10_1","MKJMPP2P11","MKEMPP2P11","MDIMPP2P11","MD0MP_R20-R10_1","MD1MP_R20-R10_1","MDGMPP2P11"

415

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

53,"Annual",2012,"6/30/1949" 53,"Annual",2012,"6/30/1949" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_cons_sum_a_epg0_vc0_mmcf_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_cons_sum_a_epg0_vc0_mmcf_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:50:03 PM" "Back to Contents","Data 1: Natural Gas Consumption " "Sourcekey","N9140US2","NA1490_SAL_2","NA1490_SAK_2","NA1490_SAZ_2","NA1490_SAR_2","NA1490_SCA_2","NA1490_SCO_2","NA1490_SCT_2","NA1490_SDE_2","NA1490_SDC_2","NA1490_SFL_2","NA1490_SGA_2","NA1490_R3FM_2","NA1490_SHI_2","NA1490_SID_2","NA1490_SIL_2","NA1490_SIN_2","NA1490_SIA_2","NA1490_SKS_2","NA1490_SKY_2","NA1490_SLA_2","NA1490_SME_2","NA1490_SMD_2","NA1490_SMA_2","NA1490_SMI_2","NA1490_SMN_2","NA1490_SMS_2","NA1490_SMO_2","NA1490_SMT_2","NA1490_SNE_2","NA1490_SNV_2","NA1490_SNH_2","NA1490_SNJ_2","NA1490_SNM_2","NA1490_SNY_2","NA1490_SNC_2","NA1490_SND_2","NA1490_SOH_2","NA1490_SOK_2","NA1490_SOR_2","NA1490_SPA_2","NA1490_SRI_2","NA1490_SSC_2","NA1490_SSD_2","NA1490_STN_2","NA1490_STX_2","NA1490_SUT_2","NA1490_SVT_2","NA1490_SVA_2","NA1490_SWA_2","NA1490_SWV_2","NA1490_SWI_2","NA1490_SWY_2"

416

Terpolymerization of ethylene, sulfur dioxide and carbon monoxide  

DOE Patents [OSTI]

This invention relates to a high molecular weight terpolymer of ethylene, sulfur dioxide and carbon monoxide stable to 280.degree. C. and containing as little as 36 mol % ethylene and about 41-51 mol % sulfur dioxide; and to the method of producing said terpolymer by irradiation of a liquid and gaseous mixture of ethylene, sulfur dioxide and carbon monoxide by means of Co-60 gamma rays or an electron beam, at a temperature of about 10.degree.-50.degree. C., and at a pressure of about 140 to 680 atmospheres, to initiate polymerization.

Johnson, Richard (Shirley, NY); Steinberg, Meyer (Huntington Station, NY)

1981-01-01T23:59:59.000Z

417

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

6,"Annual",2012,"6/30/1985" 6,"Annual",2012,"6/30/1985" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_move_poe2_a_epg0_pnp_dpmcf_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe2_a_epg0_pnp_dpmcf_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:58:31 PM" "Back to Contents","Data 1: U.S. Price of Natural Gas Pipeline Exports by Point of Exit " "Sourcekey","N9132US3","N9132CN3","NA1287_YEPRT-NCA_3","NGA_EPG0_PNP_YCAL-NCA_DMCF","NA1287_YDTW-NCA_3","NA1287_YMARY-NCA_3","NA1287_YSSM-NCA_3","NA1287_YCHRE-NCA_3","NA1287_YNOYS-NCA_3","NA1287_YWARR-NCA_3","NA1287_YBAB-NCA_3","NA1287_YHVR-NCA_3","NA1287_YPMOR-NCA_3","NA1287_YSHER-NCA_3","NGA_EPG0_PNP_YPITT-NCA_DMCF","NGM_EPG0_PNP_YGRIS-NCA_DMCF","NGM_EPG0_PNP_YMSS-NCA_DMCF","NA1287_YUSNI-NCA_3","NGM_EPG0_PNP_YWADD-NCA_DMCF","NA1287_YSUMS-NCA_3","N9132MX3","NA1287_YDUG-NMX_3","NA_EPG0_PNP_YNOGS-NMX_DMCF","NA1287_YCAX-NMX_3","NA1287_YOESA-NMX_3","NA1287_YOTAY-NMX_3","NA1287_YALA-NMX_3","NA1287_YCLI-NMX_3","NA_EPG0_PNP_YDRT-NMX_DMCF","NA1287_YEGP-NMX_3","NA1287_YELP-NMX_3","NA1287_YHDGO-NMX_3","NA1287_YMFE-NMX_3","NA1287_YPENI-NMX_3","NA1287_Y44RB-NMX_3","NA1287_Y44RM-NMX_3"

418

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

32,"Monthly","9/2013","1/15/1992" 32,"Monthly","9/2013","1/15/1992" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_move_poe2_a_epg0_png_dpmcf_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe2_a_epg0_png_dpmcf_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:58:30 PM" "Back to Contents","Data 1: U.S. Price of Liquefied Natural Gas Exports by Point of Exit " "Sourcekey","N9133US3","NGM_EPG0_PNG_NUS-NBR_DMCF","NGM_EPG0_PNG_YFPT-NBR_DMCF","NGA_EPG0_PNG_YSPL-NBR_DMCF","NGM_EPG0_PNG_NUS-NCA_DMCF","NGM_EPG0_PNG_YSWGR-NCA_DMCF","NGM_EPG0_PNG_NUS-NCI_DMCF","NGM_EPG0_PNG_YSPL-NCI_DMCF","NGM_EPG0_PNG_NUS-NCH_DMCF","NGM_EPG0_PNG_YENA-NCH_DMCF","NGM_EPG0_PNG_YSPL-NCH_DMCF","NGM_EPG0_PNG_NUS-NIN_DMCF","NGA_EPG0_PNG_YFPT-NIN_DMCF","NGM_EPG0_PNG_YSPL-NIN_DMCF","N9133JA3","NGM_EPG0_PNG_YCAM-NJA_DMCF","NA1288_YENA-NJA_3","NGA_EPG0_PNG_YSPL-NJA_DMCF","N9133MX3","NA1288_YNOGS-NMX_3","NA1288_YOTAY-NMX_3","NGM_EPG0_PNG_NUS-NPO_DMCF","NGA_EPG0_PNG_YSPL-NPO_DMCF","N9133RU3","NGM_EPG0_PNG_NUS-NKS_DMCF","NGA_EPG0_PNG_YFPT-NKS_DMCF","NGA_EPG0_PNG_YSPL-NKS_DMCF","NGM_EPG0_PNG_NUS-NSP_DMCF","NGM_EPG0_PNG_YCAM-NSP_DMCF","NGA_EPG0_PNG_YSPL-NSP_DMCF","NGM_EPG0_PNG_NUS-NUK_DMCF","NGA_EPG0_PNG_YSPL-NUK_DMCF"

419

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/1981" Monthly","9/2013","1/15/1981" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_move_netr_d_r10-z0p_vnr_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_netr_d_r10-z0p_vnr_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:09:56 AM" "Back to Contents","Data 1: East Coast (PADD 1) Net Receipts of Crude Oil and Petroleum Products by Pipeline, Tanker, and Barge" "Sourcekey","MTTNRP11","MCRNRP11","MPEMNP11","MPPNRP11","MLPNRP11","METNRP11","MPRNRP11","MBNNRP11","MBINRP11","MUONRP11","MBCNRP11","MO1NR_R10-Z0P_1","M_EPOBGRR_VNR_R10-Z0P_MBBL","MO3NR_R10-Z0P_1","MO4NR_R10-Z0P_1","MO2NR_R10-Z0P_1","MO5NR_R10-Z0P_1","MO6NR_R10-Z0P_1","MO7NR_R10-Z0P_1","MO9NR_R10-Z0P_1","M_EPOOR_VNR_R10-Z0P_MBBL","M_EPOOXE_VNR_R10-Z0P_MBBL","M_EPOORD_VNR_R10-Z0P_MBBL","M_EPOORO_VNR_R10-Z0P_MBBL","MGFNRP11","MGRNRP11","MG1NR_R10-Z0P_1","M_EPM0RO_VNR_R10-Z0P_MBBL","MG4NR_R10-Z0P_1","MG5NR_R10-Z0P_1","M_EPM0CAL55_VNR_R10-Z0P_MBBL","MG6NR_R10-Z0P_1","MGANRP11","MKJNRP11","MKENRP11","MDINRP11","MD0NR_R10-Z0P_1","MD1NR_R10-Z0P_1","MDGNRP11","MRENRP11","MPFNRP11","MPNNR_R10-Z0P_1","MPONR_R10-Z0P_1","MNSNRP11","MLUNRP11","MWXNRP11","MAPNRP11","MMSNRP11"

420

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

36,"Annual",2012,"6/30/1985" 36,"Annual",2012,"6/30/1985" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_move_poe1_a_epg0_prp_dpmcf_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe1_a_epg0_prp_dpmcf_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:57:08 PM" "Back to Contents","Data 1: U.S. Price of Natural Gas Pipeline Imports by Point of Entry " "Sourcekey","N9102US3","N9102CN3","NA1277_YEPRT-NCA_3","NA1277_YCAL-NCA_3","NA1277_YDTW-NCA_3","NA1277_YMARY-NCA_3","NA1277_YCHRE-NCA_3","NA1277_YINL-NCA_3","NA1277_YNOYS-NCA_3","NA1277_YWARR-NCA_3","NA1277_YBAB-NCA_3","NA1277_YHVR-NCA_3","NA1277_YPDEB-NCA_3","NA1277_YPMOR-NCA_3","NA1277_YSWGR-NCA_3","NA1277_YWHIH-NCA_3","NA1277_YPORT-NCA_3","NA1277_YSHER-NCA_3","NA1277_YPITT-NCA_3","NA1277_YCHAP-NCA_3","NA1277_YGRIS-NCA_3","NA1277_YMSS-NCA_3","NA1277_YUSNI-NCA_3","NA1277_YWADD-NCA_3","NA1277_YSUMS-NCA_3","NA1277_YHGSP-NCA_3","NA1277_YNTRY-NCA_3","N9102MX3","NGA_EPG0_PRP_YOESA-NMX_DMCF","NGM_EPG0_PRP_YOTAY-NMX_DMCF","NA1277_YALA-NMX_3","NA1277_YELP-NMX_3","NGA_EPG0_PRP_YGRT-NMX_DMCF","NA1277_YHDGO-NMX_3","NA1277_YMFE-NMX_3","NA1277_YPENI-NMX_3"

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


421

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

43,"Monthly","9/2013","1/15/1989" 43,"Monthly","9/2013","1/15/1989" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_move_poe1_a_epg0_pml_dpmcf_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe1_a_epg0_pml_dpmcf_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:57:08 PM" "Back to Contents","Data 1: U.S. Price of Liquefied Natural Gas Imports by Point of Entry " "Sourcekey","N9103US3","NGM_EPG0_NUS-NCA_PML_DMCF","NGM_EPG0_PML_YHGSP-NCA_DMCF","N9103AG3","N9103AU3","N9103BX3","N9103EG3","NGM_EPG0_PML_YCAM-NEG_DMCF","NA_EPG0_PML_YELBA-NEG_DPMCF","NGA_EPG0_PML_YFPT-NEG_DMCF","NGM_EPG0_PML_YGLN-NEG_DMCF","NGM_EPG0_NUS-NEK_PML_DMCF","N9103ID3","N9103MY3","N9103NG3","NA_EPG0_PML_YCPT-NNI_3","NGM_EPG0_NUS-NNO_PML_DMCF","NGA_EPG0_PML_YCPT-NNO_DMCF","NGM_EPG0_PML_YFPT-NNO_DMCF","NGA_EPG0_PML_YSPL-NNO_DMCF","N9103MU3","NGM_EPG0_NUS-NPE_PML_DMCF","NGM_EPG0_PML_YCAM-NPE_DMCF","NGA_EPG0_PML_YFPT-NPE_DMCF","N9103QR3","NGM_EPG0_PML_YELBA-NQA_DMCF","NGA_EPG0_PML_YGPT-NQA_DMCF","NGA_EPG0_PML_YSPL-NQA_DMCF","N9103TD3","NGA_EPG0_PML_YCAM-NTD_DMCF","NA1278_YCPT-NTD_3","NA1278_YELBA-NTD_3","NA1278_YEVTT-NTD_3","NGA_EPG0_PML_YFPT-NTD_DMCF","NGM_EPG0_PML_YGLN-NTD_DMCF","NA1278_YLCH-NTD_3","NGA_EPG0_PML_YSPL-NTD_DMCF","N9103UA3","NGM_EPG0_PML_NUS-NYE_DMCF","NGA_EPG0_PML_YEVTT-NYE_DMCF","NGM_EPG0_PML_YFPT-NYE_DMCF","NGA_EPG0_PML_YSPL-NYE_DMCF","N9103983"

422

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1981" Annual",2012,"6/30/1981" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_netr_d_r10-z0p_vnr_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_netr_d_r10-z0p_vnr_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 11:09:55 AM" "Back to Contents","Data 1: East Coast (PADD 1) Net Receipts of Crude Oil and Petroleum Products by Pipeline, Tanker, and Barge" "Sourcekey","MTTNRP11","MCRNRP11","MPEMNP11","MPPNRP11","MLPNRP11","METNRP11","MPRNRP11","MBNNRP11","MBINRP11","MUONRP11","MBCNRP11","MO1NR_R10-Z0P_1","M_EPOBGRR_VNR_R10-Z0P_MBBL","MO3NR_R10-Z0P_1","MO4NR_R10-Z0P_1","MO2NR_R10-Z0P_1","MO5NR_R10-Z0P_1","MO6NR_R10-Z0P_1","MO7NR_R10-Z0P_1","MO9NR_R10-Z0P_1","M_EPOOR_VNR_R10-Z0P_MBBL","M_EPOOXE_VNR_R10-Z0P_MBBL","M_EPOORD_VNR_R10-Z0P_MBBL","M_EPOORO_VNR_R10-Z0P_MBBL","MGFNRP11","MGRNRP11","MG1NR_R10-Z0P_1","M_EPM0RO_VNR_R10-Z0P_MBBL","MG4NR_R10-Z0P_1","MG5NR_R10-Z0P_1","M_EPM0CAL55_VNR_R10-Z0P_MBBL","MG6NR_R10-Z0P_1","MGANRP11","MKJNRP11","MKENRP11","MDINRP11","MD0NR_R10-Z0P_1","MD1NR_R10-Z0P_1","MDGNRP11","MRENRP11","MPFNRP11","MPNNR_R10-Z0P_1","MPONR_R10-Z0P_1","MNSNRP11","MLUNRP11","MWXNRP11","MAPNRP11","MMSNRP11"

423

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

36,"Annual",2012,"6/30/1973" 36,"Annual",2012,"6/30/1973" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_move_poe1_a_epg0_irp_mmcf_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe1_a_epg0_irp_mmcf_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:56:59 PM" "Back to Contents","Data 1: U.S. Natural Gas Pipeline Imports by Point of Entry " "Sourcekey","N9102US2","N9102CN2","NA1277_YEPRT-NCA_2","NA1277_YCAL-NCA_2","NA1277_YDTW-NCA_2","NA1277_YMARY-NCA_2","NA1277_YCHRE-NCA_2","NA1277_YINL-NCA_2","NA1277_YNOYS-NCA_2","NA1277_YWARR-NCA_2","NA1277_YBAB-NCA_2","NA1277_YHVR-NCA_2","NA1277_YPDEB-NCA_2","NA1277_YPMOR-NCA_2","NA1277_YSWGR-NCA_2","NA1277_YWHIH-NCA_2","NA1277_YPORT-NCA_2","NA1277_YSHER-NCA_2","NA1277_YPITT-NCA_2","NA1277_YCHAP-NCA_2","NA1277_YGRIS-NCA_2","NA1277_YMSS-NCA_2","NA1277_YUSNI-NCA_2","NA1277_YWADD-NCA_2","NA1277_YSUMS-NCA_2","NA1277_YHGSP-NCA_2","NA1277_YNTRY-NCA_2","N9102MX2","NGA_EPG0_IRP_YOESA-NMX_MMCF","NGM_EPG0_IRP_YOTAY-NMX_MMCF","NA1277_YALA-NMX_2","NA1277_YELP-NMX_2","NGA_EPG0_IRP_YGRT-NMX_MMCF","NA1277_YHDGO-NMX_2","NA1277_YMFE-NMX_2","NA1277_YPENI-NMX_2"

424

Reducing the sulfur content of coke by increasing the content of thermally conditioned g coal in the batch  

Science Journals Connector (OSTI)

In periods of economic growth, Ukrainian coke plants face a shortage of Zh and K coal, because of the high demand. In periods of economic stagnation, conversely, there is an excess of Zh coal, on account of the d...

E. I. Malyi

2014-05-01T23:59:59.000Z

425

Low Temperature Sorbents for removal of Sulfur Compounds from fluid feed Streams  

SciTech Connect (OSTI)

A sorbent material is provided comprising a material reactive with sulfur, a binder unreactive with sulfur and an inert material, wherein the sorbent absorbs the sulfur at temperatures between 30 and 200 C. Sulfur absorption capacity as high as 22 weight percent has been observed with these materials.

Siriwardane, Ranjan

1999-09-30T23:59:59.000Z

426

Low Temperature Sorbents for Removal of Sulfur Compounds from Fluid Feed Streams  

DOE Patents [OSTI]

A sorbent material is provided comprising a material reactive with sulfur, a binder unreactive with sulfur and an inert material, wherein the sorbent absorbs the sulfur at temperatures between 30 and 200 C. Sulfur absorption capacity as high as 22 weight percent has been observed with these materials.

Siriwardane, Ranjani

2004-06-01T23:59:59.000Z

427

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1910" Annual",2012,"6/30/1910" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_imp_dc_nus-z00_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_imp_dc_nus-z00_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 8:04:15 AM" "Back to Contents","Data 1: U.S. Imports of Crude Oil and Petroleum Products" "Sourcekey","MTTIMUS1","MCRIMUS1","MNGIMUS1","MPPIMUS1","MLPIMUS1","MENIMUS1","MEYIMUS1","MPAIM_NUS-Z00_1","MPLIMUS1","MBUIM_NUS-Z00_1","MBYIMUS1","MIIIM_NUS-Z00_1","MIYIMUS1","MOLIMUS1","MOHIMUS1","M_EPOOXXFE_IM0_NUS-Z00_MBBL","MMTIMUS1","MOOIMUS1","M_EPOOR_IM0_NUS-Z00_MBBL","MFEIMUS1","M_EPOORDB_IM0_NUS-Z00_MBBL","M_EPOORDO_IM0_NUS-Z00_MBBL","M_EPOORO_IM0_NUS-Z00_MBBL","M_EPOOOXH_IM0_NUS-Z00_MBBL","MUOIMUS1","MNLIMUS1","MKOIMUS1","MHOIMUS1","MRUIMUS1","MBCIMUS1","M_EPOBGRR_IM0_NUS-Z00_MBBL","MO5IM_NUS-Z00_1","MO6IM_NUS-Z00_1","MO7IM_NUS-Z00_1","MO9IM_NUS-Z00_1","MBAIMUS1","MTPIMUS1","MGFIMUS1","MGRIMUS1","MG1IM_NUS-Z00_1","MG4IM_NUS-Z00_1","MG5IM_NUS-Z00_1","M_EPM0CAL55_IM0_NUS-Z00_MBBL","MG6IM_NUS-Z00_1","MGAIMUS1","MKJIMUS1","MKBIMUS1","MK1IMUS1","MKEIMUS1","MDIIMUS1","MD0IM_NUS-Z00_1","MB0IM_NUS-Z00_1","MB5IM_NUS-Z00_1","MD1IM_NUS-Z00_1","MB1IM_NUS-Z00_1","MB6IM_NUS-Z00_1","MDGIMUS1","MD2IM_NUS-Z00_1","MB2IM_NUS-Z00_1","MB7IM_NUS-Z00_1","MD3IM_NUS-Z00_1","MB3IM_NUS-Z00_1","MB8IM_NUS-Z00_1","MREIMUS1","MRXIMUS1","MRYIMUS1","MRZIMUS1","MPFIM_NUS-Z00_1","MNFIMUS1","MOTIMUS1","MNSIMUS1","MLUIMUS1","MWXIMUS1","MCKIMUS1","MAPIMUS1","MMSIMUS1"

428

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

mbbl_m.xls" mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_imp_dc_nus-z00_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 8:04:37 AM" "Back to Contents","Data 1: U.S. Imports of Crude Oil and Petroleum Products" "Sourcekey","MTTIMUS1","MCRIMUS1","MNGIMUS1","MPPIMUS1","MLPIMUS1","MENIMUS1","MEYIMUS1","MPAIM_NUS-Z00_1","MPLIMUS1","MBUIM_NUS-Z00_1","MBYIMUS1","MIIIM_NUS-Z00_1","MIYIMUS1","MOLIMUS1","MOHIMUS1","M_EPOOXXFE_IM0_NUS-Z00_MBBL","MMTIMUS1","MOOIMUS1","M_EPOOR_IM0_NUS-Z00_MBBL","MFEIMUS1","M_EPOORDB_IM0_NUS-Z00_MBBL","M_EPOORDO_IM0_NUS-Z00_MBBL","M_EPOORO_IM0_NUS-Z00_MBBL","M_EPOOOXH_IM0_NUS-Z00_MBBL","MUOIMUS1","MNLIMUS1","MKOIMUS1","MHOIMUS1","MRUIMUS1","MBCIMUS1","M_EPOBGRR_IM0_NUS-Z00_MBBL","MO5IM_NUS-Z00_1","MO6IM_NUS-Z00_1","MO7IM_NUS-Z00_1","MO9IM_NUS-Z00_1","MBAIMUS1","MTPIMUS1","MGFIMUS1","MGRIMUS1","MG1IM_NUS-Z00_1","MG4IM_NUS-Z00_1","MG5IM_NUS-Z00_1","M_EPM0CAL55_IM0_NUS-Z00_MBBL","MG6IM_NUS-Z00_1","MGAIMUS1","MKJIMUS1","MKBIMUS1","MK1IMUS1","MKEIMUS1","MDIIMUS1","MD0IM_NUS-Z00_1","MB0IM_NUS-Z00_1","MB5IM_NUS-Z00_1","MD1IM_NUS-Z00_1","MB1IM_NUS-Z00_1","MB6IM_NUS-Z00_1","MDGIMUS1","MD2IM_NUS-Z00_1","MB2IM_NUS-Z00_1","MB7IM_NUS-Z00_1","MD3IM_NUS-Z00_1","MB3IM_NUS-Z00_1","MB8IM_NUS-Z00_1","MREIMUS1","MRXIMUS1","MRYIMUS1","MRZIMUS1","MPFIM_NUS-Z00_1","MNFIMUS1","MOTIMUS1","MNSIMUS1","MLUIMUS1","MWXIMUS1","MCKIMUS1","MAPIMUS1","MMSIMUS1"

429

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

45,"Annual",2012,"6/30/1985" 45,"Annual",2012,"6/30/1985" ,"Release Date:","12/12/2013" ,"Next Release Date:","1/7/2014" ,"Excel File Name:","ng_move_poe2_a_epg0_png_dpmcf_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/ng/ng_move_poe2_a_epg0_png_dpmcf_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"12/12/2013 6:58:30 PM" "Back to Contents","Data 1: U.S. Price of Liquefied Natural Gas Exports by Point of Exit " "Sourcekey","N9133US3","NGM_EPG0_PNG_NUS-NBR_DMCF","NGM_EPG0_PNG_YFPT-NBR_DMCF","NGA_EPG0_PNG_YSPL-NBR_DMCF","NGM_EPG0_PNG_NUS-NCA_DMCF","NA_EPG0_PNG_YBUF-NCA_DMCF","NGM_EPG0_PNG_YSWGR-NCA_DMCF","NGM_EPG0_PNG_NUS-NCI_DMCF","NGM_EPG0_PNG_YSPL-NCI_DMCF","NGM_EPG0_PNG_NUS-NCH_DMCF","NGM_EPG0_PNG_YENA-NCH_DMCF","NGM_EPG0_PNG_YSPL-NCH_DMCF","NGM_EPG0_PNG_NUS-NIN_DMCF","NGA_EPG0_PNG_YFPT-NIN_DMCF","NGM_EPG0_PNG_YSPL-NIN_DMCF","N9133JA3","NGM_EPG0_PNG_YCAM-NJA_DMCF","NGA_EPG0_PNG_YFPT-NJA_DMCF","NA1288_YENA-NJA_3","NA1288_YPNIK-NJA_3","NGA_EPG0_PNG_YSPL-NJA_DMCF","N9133MX3","NA1288_YNOGS-NMX_3","NA1288_YOTAY-NMX_3","NA1288_YSAN-NMX_3","NGM_EPG0_PNG_NUS-NPO_DMCF","NGA_EPG0_PNG_YSPL-NPO_DMCF","N9133RU3","NA_EPG0_PNG_YENA-NRS_DMCF","NGM_EPG0_PNG_NUS-NKS_DMCF","NGA_EPG0_PNG_YFPT-NKS_DMCF","NGA_EPG0_PNG_YSPL-NKS_DMCF","NGM_EPG0_PNG_NUS-NSP_DMCF","NGM_EPG0_PNG_YCAM-NSP_DMCF","NGA_EPG0_PNG_YSPL-NSP_DMCF","NGM_EPG0_PNG_NUS-NUK_DMCF","NGA_EPG0_PNG_YFPT-NUK_DMCF","NGA_EPG0_PNG_YSPL-NUK_DMCF","NGM_EPG0_PNG_YCAM-Z00_DMCF","NGM_EPG0_PNG_YENA-Z00_DMCF","NGM_EPG0_PNG_YFPT-Z00_DMCF","NGM_EPG0_PNG_YNOGS-Z00_DMCF","NGM_EPG0_PNG_YOTAY-Z00_DMCF","NGM_EPG0_PNG_YSPL-Z00_DMCF","NGM_EPG0_PNG_YSWGR-Z00_DMCF"

430

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

mbblpd_m.xls" mbblpd_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_imp_dc_nus-z00_mbblpd_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 8:05:08 AM" "Back to Contents","Data 1: U.S. Imports of Crude Oil and Petroleum Products" "Sourcekey","MTTIMUS2","MCRIMUS2","MNGIMUS2","MPPIMUS2","MLPIMUS2","MENIMUS2","MEYIMUS2","MPAIM_NUS-Z00_2","MPLIMUS2","MBUIM_NUS-Z00_2","MBYIMUS2","MIIIM_NUS-Z00_2","MIYIMUS2","MOLIMUS2","MOHIMUS2","M_EPOOXXFE_IM0_NUS-Z00_MBBLD","MMTIMUS2","MOOIMUS2","M_EPOOR_IM0_NUS-Z00_MBBLD","MFEIMUS2","M_EPOORDB_IM0_NUS-Z00_MBBLD","M_EPOORDO_IM0_NUS-Z00_MBBLD","M_EPOORO_IM0_NUS-Z00_MBBLD","M_EPOOOXH_IM0_NUS-Z00_MBBLD","MUOIMUS2","MNLIMUS2","MKOIMUS2","MHOIMUS2","MRUIMUS2","MBCIMUS2","M_EPOBGRR_IM0_NUS-Z00_MBBLD","MO5IM_NUS-Z00_2","MO6IM_NUS-Z00_2","MO7IM_NUS-Z00_2","MO9IM_NUS-Z00_2","MBAIMUS2","MTPIMUS2","MGFIMUS2","MGRIMUS2","MG1IM_NUS-Z00_2","MG4IM_NUS-Z00_2","MG5IM_NUS-Z00_2","M_EPM0CAL55_IM0_NUS-Z00_MBBLD","MG6IM_NUS-Z00_2","MGAIMUS2","MKJIMUS2","MKBIMUS2","MK1IMUS2","MKEIMUS2","MDIIMUS2","MD0IM_NUS-Z00_2","MB0IM_NUS-Z00_2","MB5IM_NUS-Z00_2","MD1IM_NUS-Z00_2","MB1IM_NUS-Z00_2","MB6IM_NUS-Z00_2","MDGIMUS2","MD2IM_NUS-Z00_2","MB2IM_NUS-Z00_2","MB7IM_NUS-Z00_2","MD3IM_NUS-Z00_2","MB3IM_NUS-Z00_2","MB8IM_NUS-Z00_2","MREIMUS2","MRXIMUS2","MRYIMUS2","MRZIMUS2","MPFIM_NUS-Z00_2","MNFIMUS2","MOTIMUS2","MNSIMUS2","MLUIMUS2","MWXIMUS2","MCKIMUS2","MAPIMUS2","MMSIMUS2"

431

Cell development obeys maximum Fisher information  

E-Print Network [OSTI]

Eukaryotic cell development has been optimized by natural selection to obey maximal intracellular flux of messenger proteins. This, in turn, implies maximum Fisher information on angular position about a target nuclear pore complex (NPR). The cell is simply modeled as spherical, with cell membrane (CM) diameter 10 micron and concentric nuclear membrane (NM) diameter 6 micron. The NM contains about 3000 nuclear pore complexes (NPCs). Development requires messenger ligands to travel from the CM-NPC-DNA target binding sites. Ligands acquire negative charge by phosphorylation, passing through the cytoplasm over Newtonian trajectories toward positively charged NPCs (utilizing positive nuclear localization sequences). The CM-NPC channel obeys maximized mean protein flux F and Fisher information I at the NPC, with first-order delta I = 0 and approximate 2nd-order delta I = 0 stability to environmental perturbations. Many of its predictions are confirmed, including the dominance of protein pathways of from 1-4 proteins, a 4nm size for the EGFR protein and the approximate flux value F =10^16 proteins/m2-s. After entering the nucleus, each protein ultimately delivers its ligand information to a DNA target site with maximum probability, i.e. maximum Kullback-Liebler entropy HKL. In a smoothness limit HKL approaches IDNA/2, so that the total CM-NPC-DNA channel obeys maximum Fisher I. Thus maximum information approaches non-equilibrium, one condition for life.

B. R. Frieden; R. A. Gatenby

2014-04-29T23:59:59.000Z

432

Behavior of sulfur and chlorine in coal during combustion and boiler corrosion. Final technical report, 1 September, 1992--31 August, 1993  

SciTech Connect (OSTI)

The goals of this project are to investigate the behavior of sulfur and chlorine during pyrolysis and combustion of Illinois coals, the chemistry and mineralogy of boiler deposits, the effects of combustion gases on boiler materials, and remedial measures to reduce the sulfur and chlorine compounds in combustion gases. Replicate determinations of chlorine and sulfur evolution during coal pyrolysis-gas combustion were conducted using a pyrolysis apparatus in conjunction with a quadrupole gas analyzer. HCl is the only gaseous chlorine species measured in combustion gases. Pyrolysis of coal IBC-109 spiked with NaCl solution shows a strong peak of HCl evolution above 700C. The absence of this peak during pyrolysis of Illinois coal indicates that little chlorine in Illinois coal occurs in the NaCl form. Evolution of sulfur during coal pyrolysis was studied; the sulfur evolution profile may be explained by the sulfur forms in coal. To determine the fate of sulfur and chlorine during combustion, a set of six samples of boiler deposits from superheater and reheater tubes of an Illinois power plant was investigated. Scanning electron microscopy shows microscopic calcium sulfate droplets on cenospheres. Superheater deposits are high in mullite, hematite, and cristobalite, whereas a reheater deposit is enriched in anhydrite. The chlorine content is very low, indicating that most of the chlorine in the feed coal is lost as volatile HCl during he combustion process. The profiles of SO{sub 2} released during combustion experiments at 825 C indicate that calcium hydroxide added to the coal has a significant effect on reducing the SO{sub 2} vapors in combustion gases.

Chou, C.L.; Hackley, K.C.; Cao, J.; Moore, D.M.; Xu, J.; Ruch, R.R. [Illinois State Geological Survey, Champaign, IL (United States); Pan, W.P.; Upchurch, M.L.; Cao, H.B. [Western Kentucky Univ., Bowling Green, KY (United States)

1993-12-31T23:59:59.000Z

433

Martinez Sulfuric Acid Regeneration Plt Biomass Facility | Open Energy  

Open Energy Info (EERE)

Martinez Sulfuric Acid Regeneration Plt Biomass Facility Martinez Sulfuric Acid Regeneration Plt Biomass Facility Jump to: navigation, search Name Martinez Sulfuric Acid Regeneration Plt Biomass Facility Facility Martinez Sulfuric Acid Regeneration Plt Sector Biomass Facility Type Non-Fossil Waste Location Contra Costa County, California Coordinates 37.8534093°, -121.9017954° Loading map... {"minzoom":false,"mappingservice":"googlemaps3","type":"ROADMAP","zoom":14,"types":["ROADMAP","SATELLITE","HYBRID","TERRAIN"],"geoservice":"google","maxzoom":false,"width":"600px","height":"350px","centre":false,"title":"","label":"","icon":"","visitedicon":"","lines":[],"polygons":[],"circles":[],"rectangles":[],"copycoords":false,"static":false,"wmsoverlay":"","layers":[],"controls":["pan","zoom","type","scale","streetview"],"zoomstyle":"DEFAULT","typestyle":"DEFAULT","autoinfowindows":false,"kml":[],"gkml":[],"fusiontables":[],"resizable":false,"tilt":0,"kmlrezoom":false,"poi":true,"imageoverlays":[],"markercluster":false,"searchmarkers":"","locations":[{"text":"","title":"","link":null,"lat":37.8534093,"lon":-121.9017954,"alt":0,"address":"","icon":"","group":"","inlineLabel":"","visitedicon":""}]}

434

Diesel Emissions Control-Sulfur Effects (DECSE) Program Status  

SciTech Connect (OSTI)

Determine the impact of fuel sulfur levels on emission control systems that could be implemented to lower emissions of NO{sub x} and PM from on-highway trucks in the 2002-2004 time frame.

None

1999-06-29T23:59:59.000Z

435

Hybrid Microfabricated Device for Field Measurement of Atmospheric Sulfur Dioxide  

Science Journals Connector (OSTI)

It is also now generally agreed that forthcoming major volcanic eruptions will sensitively monitored for increasing sulfur gas emissions as indicated by increasing seismic activity. ... (12)?Fish, B. R.; Durham, J. L. Environ. ...

Shin-Ichi Ohira; Kei Toda; Shin-Ichiro Ikebe; Purnendu K. Dasgupta

2002-10-10T23:59:59.000Z

436

Sulfur meter for blending coal at Plant Monroe: Final report  

SciTech Connect (OSTI)

An on-line sulfur analyzer, installed at the Detroit Edison, Monroe Power station, was placed into service and evaluated for coal blending optimization to minimize the cost of complying with changing stack gas sulfur dioxide regulations. The project involved debugging the system which consisted of an /open quotes/as-fired/close quotes/ sampler and nuclear source sulfur analyzer. The system was initially plagued with mechanical and electronic problems ranging from coal flow pluggages to calibration drifts in the analyzer. Considerable efforts were successfully made to make the system reliable and accurate. On-line testing showed a major improvement in control of sulfur dioxide emission rates and fuel blending optimization equivalent to as much as $6 million in fuel costs at the time of the evaluation. 7 refs., 14 figs., 12 tabs.

Trentacosta, S.D.; Yurko, J.O.

1988-04-01T23:59:59.000Z

437

Novel Sulfur-Tolerant Anodes for Solid Oxide Fuel Cells  

SciTech Connect (OSTI)

One of the unique advantages of SOFCs over other types of fuel cells is the potential for direct utilization of hydrocarbon fuels (it may involve internal reforming). Unfortunately, most hydrocarbon fuels contain sulfur, which would dramatically degrade SOFC performance at parts-per-million (ppm) levels. Low concentration of sulfur (ppm or below) is difficult to remove efficiently and cost-effectively. Therefore, knowing the exact poisoning process for state-of-the-art anode-supported SOFCs with Ni-YSZ cermet anodes, understanding the detailed anode poisoning mechanism, and developing new sulfur-tolerant anodes are essential to the promotion of SOFCs that run on hydrocarbon fuels. The effect of cell operating conditions (including temperature, H{sub 2}S concentration, cell voltage/current density, etc.) on sulfur poisoning and recovery of nickel-based anode in SOFCs was investigated. It was found that sulfur poisoning is more severe at lower temperature, higher H{sub 2}S concentration or lower cell current density (higher cell voltage). In-situ Raman spectroscopy identified the nickel sulfide formation process on the surface of a Ni-YSZ electrode and the corresponding morphology change as the sample was cooled in H{sub 2}S-containing fuel. Quantum chemical calculations predicted a new S-Ni phase diagram with a region of sulfur adsorption on Ni surfaces, corresponding to sulfur poisoning of Ni-YSZ anodes under typical SOFC operating conditions. Further, quantum chemical calculations were used to predict the adsorption energy and bond length for sulfur and hydrogen atoms on various metal surfaces. Surface modification of Ni-YSZ anode by thin Nb{sub 2}O{sub 5} coating was utilized to enhance the sulfur tolerance. A multi-cell testing system was designed and constructed which is capable of simultaneously performing electrochemical tests of 12 button cells in fuels with four different concentrations of H{sub 2}S. Through systematical study of state-of-the-art anode-supported SOFC button cells, it is seen that the long-term sulfur poisoning behavior of those cells indicate that there might be a second-stage slower degradation due to sulfur poisoning, which would last for a thousand hour or even longer. However, when using G-18 sealant from PNNL, the 2nd stage poisoning was effectively prohibited.

Lei Yang; Meilin Liu

2008-12-31T23:59:59.000Z

438

Selective catalytic reduction of sulfur dioxide to elemental sulfur. Final report  

SciTech Connect (OSTI)

This project has investigated new metal oxide catalysts for the single stage selective reduction of SO{sub 2} to elemental sulfur by a reductant, such as CO. Significant progress in catalyst development has been made during the course of the project. We have found that fluorite oxides, CeO{sub 2} and ZrO{sub 2}, and rare earth zirconates such as Gd{sub 2}Zr{sub 2}O{sub 7} are active and stable catalysts for reduction Of SO{sub 2} by CO. More than 95% sulfur yield was achieved at reaction temperatures about 450{degrees}C or higher with the feed gas of stoichiometric composition. Reaction of SO{sub 2} and CO over these catalysts demonstrated a strong correlation of catalytic activity with the catalyst oxygen mobility. Furthermore, the catalytic activity and resistance to H{sub 2}O and CO{sub 2} poisoning of these catalysts were significantly enhanced by adding small amounts of transition metals, such as Co, Ni, Co, etc. The resulting transition metal-fluorite oxide composite catalyst has superior activity and stability, and shows promise in long use for the development of a greatly simplified single-step sulfur recovery process to treat variable and dilute SO{sub 2} concentration gas streams. Among various active composite catalyst systems the Cu-CeO{sub 2} system has been extensively studied. XRD, XPS, and STEM analyses of the used Cu-CeO{sub 2} catalyst found that the fluorite crystal structure of ceria was stable at the present reaction conditions, small amounts of copper was dispersed and stabilized on the ceria matrix, and excess copper oxide particles formed copper sulfide crystals of little contribution to catalytic activity. A working catalyst consisted of partially sulfated cerium oxide surface and partially sulfided copper clusters. The overall reaction kinetics were approximately represented by a first order equation.

Liu, W.; Flytzani-Stephanopoulos, M.; Sarofim, A.F.

1995-06-01T23:59:59.000Z

439

METHOD TO PREVENT SULFUR ACCUMULATION INSIDE MEMBRANE ELECTRODE ASSEMBLY  

SciTech Connect (OSTI)

HyS is conceptually the simplest of the thermochemical cycles and involves only sulfur chemistry. In the HyS Cycle hydrogen gas (H{sub 2}) is produced at the cathode of the electrochemical cell (or electrolyzer). Sulfur dioxide (SO{sub 2}) is oxidized at the anode to form sulfuric acid (H{sub 2}SO{sub 4}) and protons (H{sup +}) as illustrated below. A separate high temperature reaction decomposes the sulfuric acid to water and sulfur dioxide which are recycled to the electrolyzers, and oxygen which is separated out as a secondary product. The electrolyzer includes a membrane that will allow hydrogen ions to pass through but block the flow of hydrogen gas. The membrane is also intended to prevent other chemical species from migrating between electrodes and undergoing undesired reactions that could poison the cathode or reduce overall process efficiency. In conventional water electrolysis, water is oxidized at the anode to produce protons and oxygen. The standard cell potential for conventional water electrolysis is 1.23 volts at 25 C. However, commercial electrolyzers typically require higher voltages ranging from 1.8 V to 2.6 V [Kirk-Othmer, 1991]. The oxidation of sulfur dioxide instead of water in the HyS electrolyzer occurs at a much lower potential. For example, the standard cell potential for sulfur dioxide oxidation at 25 C in 50 wt % sulfuric acid is 0.29 V [Westinghouse, 1980]. Since power consumption by the electrolyzers is equal to voltage times current, and current is proportional to hydrogen production, a large reduction in voltage results in a large reduction in electrical power cost per unit of hydrogen generated.

Steimke, J.; Steeper, T.; Herman, D.; Colon-Mercado, H.; Elvington, M.

2009-06-22T23:59:59.000Z

440

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/1973" Monthly","9/2013","1/15/1973" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_move_neti_a_ep00_imn_mbblpd_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_neti_a_ep00_imn_mbblpd_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 10:47:08 AM" "Back to Contents","Data 1: Net Imports of Total Crude Oil and Products into the U.S. by Country" "Sourcekey","MTTNTUS2","MTTNTUSPG2","MTTNT_NUS-ME0_2","MTTNTUSAG2","MTTNTUSAO2","MTTNTUSEC2","MTTNTUSIR2","MTTNT_NUS-NIZ_2","MTTNTUSKU2","MTTNT_NUS-NLY_2","MTTNTUSNI2","MTTNTUSQA2","MTTNTUSSA2","MTTNTUSTC2","MTTNTUSVE2","MTTNTUSVV2","MTTNT_NUS-NAF_2","MTTNT_NUS-NAL_2","MTTNT_NUS-NAN_2","MTTNT_NUS-NAV_2","MTTNT_NUS-NAC_2","MTTNTUSAR2","MTTNT_NUS-NAE_2","MTTNT_NUS-NAA_2","MTTNTUSAS2","MTTNT_NUS-NAU_2","MTTNT_NUS-NAJ_2","MTTNTUSBF2","MTTNT_NUS-NBA_2","MTTNT_NUS-NBG_2","MTTNT_NUS-NBB_2","MTTNT_NUS-NBO_2","MTTNTUSBE2","MTTNT_NUS-NBH_2","MTTNT_NUS-NBN_2","MTTNT_NUS-NBD_2","MTTNT_NUS-NBL_2","MTTNT_NUS-NBK_2","MTTNTUSBR2","MTTNTUSBX2","MTTNT_NUS-NBU_2","MTTNT_NUS-NBM_2","MTTNT_NUS-NCB_2","MTTNTUSCM2","MTTNTUSCA2","MTTNT_NUS-NCJ_2","MTTNT_NUS-NCD_2","MTTNT_NUS-NCI_2","MTTNTUSCH2","MTTNTUSCO2","MTTNTUSCF2","MTTNTUSCG2","MTTNT_NUS-NCW_2","MTTNT_NUS-NCS_2","MTTNT_NUS-NHR_2","MTTNT_NUS-NCY_2","MTTNT_NUS-NCZ_2","MTTNT_NUS-NDA_2","MTTNT_NUS-NDJ_2","MTTNT_NUS-NDO_2","MTTNT_NUS-NDR_2","MTTNTUSEG2","MTTNT_NUS-NES_2","MTTNT_NUS-NEK_2","MTTNT_NUS-NET_2","MTTNT_NUS-NER_2","MTTNT_NUS-NEN_2","MTTNT_NUS-NFJ_2","MTTNT_NUS-NFI_2","MTTNTUSFR2","MTTNT_NUS-NFP_2","MTTNT_NUS-NFG_2","MTTNTUSGB2","MTTNT_NUS-NGG_2","MTTNTUSBZ2","MTTNT_NUS-NGH_2","MTTNT_NUS-NGI_2","MTTNTUSGR2","MTTNT_NUS-NGL_2","MTTNT_NUS-NGJ_2","M_EP00_IMN_NUS-NGP_2","MTTNTUSGT2","MTTNT_NUS-NGV_2","MTTNT_NUS-NGY_2","MTTNT_NUS-NHA_2","MTTNT_NUS-NHO_2","MTTNT_NUS-NHK_2","MTTNT_NUS-NHU_2","MTTNT_NUS-NIC_2","MTTNTUSIN2","MTTNTUSID2","MTTNT_NUS-NEI_2","MTTNT_NUS-NIS_2","MTTNTUSIT2","MTTNT_NUS-NIV_2","MTTNTUSJM2","MTTNTUSJA2","MTTNT_NUS-NJO_2","MTTNT_NUS-NKZ_2","MTTNT_NUS-NKE_2","MTTNTUSKS2","MTTNT_NUS-NKT_2","MTTNT_NUS-NKG_2","MTTNT_NUS-NLG_2","MTTNT_NUS-NLE_2","MTTNT_NUS-NLI_2","MTTNT_NUS-NLH_2","MTTNT_NUS-NMC_2","MTTNT_NUS-NMK_2","MTTNT_NUS-NMA_2","MTTNTUSMY2","MTTNT_NUS-NMV_2","MTTNT_NUS-NML_2","MTTNT_NUS-NMT_2","MTTNT_NUS-NRM_2","MTTNT_NUS-NMR_2","MTTNT_NUS-NMP_2","MTTNTUSMX2","MTTNT_NUS-NFM_2","MTTNT_NUS-NMQ_2","MTTNT_NUS-NMN_2","MTTNT_NUS-NMD_2","MTTNT_NUS-NMG_2","M_EP00_IMN_NUS-NMJ_2","MTTNT_NUS-NMH_2","MTTNT_NUS-NMO_2","MTTNT_NUS-NMZ_2","MTTNT_NUS-NWA_2","MTTNT_NUS-NNP_2","MTTNTUSNL2","MTTNTUSNA2","MTTNT_NUS-NNC_2","MTTNT_NUS-NNZ_2","MTTNT_NUS-NNU_2","MTTNT_NUS-NNG_2","MTTNT_NUS-NNE_2","MTTNTUSNO2","MTTNTUSMU2","MTTNT_NUS-NPK_2","MTTNTUSPM2","MTTNT_NUS-NPP_2","MTTNT_NUS-NPF_2","MTTNT_NUS-NPA_2","MTTNTUSPE2","MTTNT_NUS-NRP_2","MTTNT_NUS-NPL_2","MTTNT_NUS-NPO_2","MTTNTUSRQ2","MTTNTUSRO2","MTTNT_NUS-NRS_2","MTTNT_NUS-NSC_2","MTTNT_NUS-NST_2","MTTNT_NUS-NSB_2","MTTNT_NUS-NVC_2","MTTNT_NUS-NWS_2","MTTNT_NUS-NSM_2","MTTNT_NUS-NSG_2","MTTNT_NUS-NYI_2","MTTNT_NUS-NSL_2","MTTNT_NUS-NSN_2","MTTNT_NUS-NSK_2","MTTNT_NUS-NSI_2","MTTNT_NUS-NSF_2","MTTNTUSSP2","MTTNT_NUS-NPG_2","MTTNT_NUS-NCE_2","MTTNT_NUS-NNS_2","MTTNT_NUS-NWZ_2","MTTNTUSSW2","MTTNT_NUS-NSZ_2","MTTNTUSSY2","MTTNTUSTW2","MTTNT_NUS-NTZ_2","MTTNTUSTH2","MTTNT_NUS-NTO_2","MTTNT_NUS-NTN_2","MTTNTUSTD2","MTTNT_NUS-NTS_2","MTTNTUSTU2","MTTNT_NUS-NTX_2","MTTNT_NUS-NTK_2","MTTNT_NUS-NUG_2","MTTNT_NUS-NUR_2","MTTNTUSUK2","MTTNT_NUS-NUY_2","MTTNT_NUS-NUZ_2","MTTNT_NUS-NNH_2","MTTNT_NUS-NVM_2","MTTNT_NUS-NVI_2","MTTNTUSVQ2","MTTNTUSYE2","MTTNT_NUS-NYO_2","MTTNTUSWW2"

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


441

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

6,"Monthly","9/2013","1/15/1981" 6,"Monthly","9/2013","1/15/1981" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_move_impcp_a2_r30_ep00_ip0_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_impcp_a2_r30_ep00_ip0_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 9:12:12 AM" "Back to Contents","Data 1: Gulf Coast (PADD 3) Total Crude Oil and Products Imports" "Sourcekey","MTTIPP31","MTTIPP3PG1","MTTIP_R30-ME0_1","MTTIPP3AG1","MTTIPP3AO1","MTTIPP3EC1","MTTIP_R30-NIZ_1","MTTIPP3KU1","MTTIP_R30-NLY_1","MTTIPP3NI1","MTTIP_R30-NQA_1","MTTIPP3SA1","MTTIPP3TC1","MTTIPP3VE1","MTTIPP3VV1","MTTIP_R30-NAL_1","MTTIPP3AR1","MTTIP_R30-NAA_1","MTTIPP3AS1","MTTIP_R30-NAU_1","MTTIP_R30-NAJ_1","MTTIP_R30-NBF_1","MTTIP_R30-NBA_1","MTTIP_R30-NBO_1","MTTIPP3BE1","MTTIP_R30-NBH_1","MTTIP_R30-NBN_1","MTTIP_R30-NBL_1","MTTIP_R30-NBR_1","MTTIP_R30-NBX_1","MTTIP_R30-NBU_1","MTTIP_R30-NBM_1","MTTIP_R30-NCM_1","MTTIPP3CA1","MTTIP_R30-NCD_1","MTTIP_R30-NCI_1","MTTIP_R30-NCH_1","MTTIPP3CO1","MTTIPP3CF1","MTTIPP3CG1","MTTIP_R30-NCW_1","MTTIP_R30-NCS_1","MTTIP_R30-NHR_1","MTTIP_R30-NCY_1","MTTIP_R30-NCZ_1","MTTIP_R30-NDA_1","MTTIPP3EG1","MTTIP_R30-NES_1","MTTIP_R30-NEK_1","MTTIP_R30-NEN_1","MTTIP_R30-NFI_1","MTTIPP3FR1","MTTIPP3GB1","MTTIP_R30-NGG_1","MTTIP_R30-NGM_1","MTTIP_R30-NGH_1","MTTIP_R30-NGR_1","MTTIP_R30-NGT_1","MTTIP_R30-NGV_1","MTTIP_R30-NHU_1","MTTIP_R30-NIN_1","MTTIPP3ID1","MTTIP_R30-NEI_1","MTTIP_R30-NIS_1","MTTIPP3IT1","MTTIP_R30-NIV_1","MTTIP_R30-NJM_1","MTTIP_R30-NJA_1","MTTIP_R30-NKZ_1","MTTIPP3KS1","MTTIP_R30-NKG_1","MTTIP_R30-NLG_1","MTTIP_R30-NLI_1","MTTIP_R30-NLH_1","MTTIP_R30-NMY_1","MTTIP_R30-NMT_1","MTTIP_R30-NMR_1","MTTIPP3MX1","MTTIP_R30-NMQ_1","MTTIP_R30-NMO_1","MTTIP_R30-NNL_1","MTTIPP3NA1","MTTIP_R30-NNZ_1","MTTIPP3NO1","MTTIP_R30-NMU_1","MTTIP_R30-NPK_1","MTTIP_R30-NPM_1","MTTIP_R30-NPP_1","MTTIP_R30-NPE_1","MTTIP_R30-NRP_1","MTTIP_R30-NPL_1","MTTIP_R30-NPO_1","MTTIP_R30-NPZ_1","MTTIP_R30-NRO_1","MTTIP_R30-NRS_1","MTTIP_R30-NSN_1","MTTIP_R30-NSK_1","MTTIP_R30-NSF_1","MTTIPP3SP1","MTTIPP3SW1","MTTIP_R30-NSZ_1","MTTIPP3SY1","MTTIP_R30-NTW_1","MTTIPP3TH1","MTTIP_R30-NTO_1","MTTIPP3TD1","MTTIP_R30-NTS_1","MTTIP_R30-NTU_1","MTTIP_R30-NTX_1","MTTIP_R30-NUR_1","MTTIPP3UK1","MTTIP_R30-NUY_1","MTTIP_R30-NUZ_1","MTTIP_R30-NVM_1","MTTIPP3VQ1","MTTIPP3YE1"

442

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

2,"Monthly","9/2013","1/15/1981" 2,"Monthly","9/2013","1/15/1981" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_move_expc_a_ep00_eex_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_expc_a_ep00_eex_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 7:29:07 AM" "Back to Contents","Data 1: Total Crude Oil and Products Exports by Destination" "Sourcekey","MTTEXUS1","MTTEX_NUS-NAF_1","MTTEX_NUS-NAL_1","MTTEX_NUS-NAG_1","MTTEX_NUS-NAN_1","MTTEX_NUS-NAO_1","MTTEX_NUS-NAV_1","MTTEX_NUS-NAC_1","MTTEXAR1","MTTEX_NUS-NAE_1","MTTEX_NUS-NAA_1","MTTEXAS1","MTTEX_NUS-NAU_1","MTTEX_NUS-NAJ_1","MTTEXBF1","MTTEXBA1","MTTEX_NUS-NBB_1","MTTEX_NUS-NBO_1","MTTEXBE1","MTTEX_NUS-NBH_1","MTTEX_NUS-NBN_1","MTTEX_NUS-NBL_1","MTTEX_NUS-NBK_1","MTTEXBR1","MTTEX_NUS-NBX_1","MTTEX_NUS-NBU_1","MTTEX_NUS-NBM_1","MTTEX_NUS-NBD_1","MTTEX_NUS-NCB_1","MTTEX_NUS-NCM_1","MTTEXCA1","MTTEX_NUS-NCJ_1","MTTEX_NUS-NCD_1","MTTEXCI1","MTTEXCH1","MTTEXCO1","MTTEX_NUS-NCF_1","MTTEX_NUS-NCG_1","MTTEXCS1","MTTEX_NUS-NHR_1","MTTEX_NUS-NCY_1","MTTEX_NUS-NCZ_1","MTTEXDA1","MTTEX_NUS-NDJ_1","MTTEXDO1","M_EP00_EEX_NUS-NDR_1","MTTEXEC1","MTTEXEG1","MTTEXES1","MTTEX_NUS-NEK_1","MTTEX_NUS-NER_1","MTTEX_NUS-NEN_1","MTTEX_NUS-NET_1","MTTEX_NUS-NFJ_1","MTTEXFI1","MTTEXFR1","MTTEX_NUS-NFG_1","MTTEXFP1","MTTEX_NUS-NGB_1","MTTEX_NUS-NGG_1","MTTEXBZ1","MTTEXGH1","MTTEX_NUS-NGI_1","MTTEXGR1","MTTEX_NUS-NGL_1","MTTEX_NUS-NGJ_1","M_EP00_EEX_NUS-NGP_1","MTTEXGT1","MTTEX_NUS-NGV_1","MTTEX_NUS-NGY_1","MTTEX_NUS-NHA_1","MTTEXHO1","MTTEXHK1","MTTEX_NUS-NHU_1","MTTEX_NUS-NIC_1","MTTEXIN1","MTTEXID1","MTTEX_NUS-NIR_1","MTTEX_NUS-NIZ_1","MTTEXEI1","MTTEXIS1","MTTEXIT1","MTTEX_NUS-NIV_1","MTTEXJM1","MTTEXJA1","MTTEX_NUS-NJO_1","MTTEX_NUS-NKZ_1","MTTEX_NUS-NKE_1","MTTEXKS1","MTTEX_NUS-NKN_1","MTTEX_NUS-NKG_1","MTTEX_NUS-NKT_1","MTTEX_NUS-NKU_1","MTTEX_NUS-NLG_1","MTTEX_NUS-NLE_1","MTTEX_NUS-NLI_1","MTTEX_NUS-NLY_1","MTTEX_NUS-NLH_1","MTTEX_NUS-NMC_1","MTTEX_NUS-NMK_1","MTTEX_NUS-NMA_1","MTTEXMY1","MTTEX_NUS-NMV_1","MTTEX_NUS-NML_1","MTTEX_NUS-NMT_1","MTTEX_NUS-NRM_1","MTTEX_NUS-NMR_1","MTTEX_NUS-NMP_1","MTTEXMX1","MTTEX_NUS-NFM_1","MTTEX_NUS-NMQ_1","MTTEX_NUS-NMD_1","MTTEX_NUS-NMN_1","MTTEX_NUS-NMG_1","M_EP00_EEX_NUS-NMJ_1","MTTEX_NUS-NMH_1","MTTEX_NUS-NMO_1","MTTEX_NUS-NMZ_1","MTTEX_NUS-NWA_1","MTTEX_NUS-NNP_1","MTTEXNL1","MTTEXNA1","MTTEX_NUS-NNC_1","MTTEXNZ1","MTTEX_NUS-NNU_1","MTTEX_NUS-NNG_1","MTTEXNI1","MTTEX_NUS-NNE_1","MTTEXNO1","MTTEX_NUS-NMU_1","MTTEX_NUS-NPK_1","MTTEXPM1","MTTEX_NUS-NPP_1","MTTEX_NUS-NPF_1","MTTEX_NUS-NPA_1","MTTEXPE1","MTTEXRP1","MTTEXPL1","MTTEXPO1","MTTEXRQ1","MTTEX_NUS-NQA_1","MTTEX_NUS-NRO_1","MTTEX_NUS-NRS_1","MTTEX_NUS-NSC_1","MTTEX_NUS-NST_1","MTTEX_NUS-NSB_1","MTTEX_NUS-NVC_1","MTTEX_NUS-NWS_1","MTTEX_NUS-NSM_1","MTTEXSA1","MTTEX_NUS-NSG_1","MTTEX_NUS-NYI_1","MTTEX_NUS-NSE_1","MTTEX_NUS-NSL_1","MTTEXSN1","MTTEX_NUS-NSK_1","MTTEX_NUS-NSI_1","MTTEX_NUS-NBP_1","MTTEXSF1","MTTEXSP1","MTTEX_NUS-NPG_1","MTTEX_NUS-NCE_1","MTTEX_NUS-NSU_1","MTTEXNS1","MTTEX_NUS-NWZ_1","MTTEXSW1","MTTEXSZ1","MTTEX_NUS-NSY_1","MTTEXTW1","MTTEX_NUS-NTZ_1","MTTEXTH1","MTTEX_NUS-NTN_1","MTTEX_NUS-NTO_1","MTTEXTD1","MTTEX_NUS-NTS_1","MTTEXTU1","MTTEX_NUS-NTX_1","MTTEX_NUS-NTK_1","MTTEX_NUS-NUG_1","MTTEX_NUS-NUR_1","MTTEXTC1","MTTEXUK1","MTTEXUY1","MTTEX_NUS-NUZ_1","MTTEX_NUS-NNH_1","MTTEXVE1","MTTEX_NUS-NVM_1","MTTEX_NUS-NVI_1","MTTEXVQ1","MTTEX_NUS-NYE_1","MTTEXYO1","MTTEX_NUS-NZA_1"

443

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Monthly","9/2013","1/15/1981" Monthly","9/2013","1/15/1981" ,"Release Date:","11/27/2013" ,"Next Release Date:","Last Week of December 2013" ,"Excel File Name:","pet_move_impcp_a2_r10_ep00_ip0_mbbl_m.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_impcp_a2_r10_ep00_ip0_mbbl_m.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 9:03:09 AM" "Back to Contents","Data 1: East Coast (PADD 1) Total Crude Oil and Products Imports" "Sourcekey","MTTIPP11","MTTIPP1PG1","MTTIP_R10-ME0_1","MTTIPP1AG1","MTTIPP1AO1","MTTIPP1EC1","MTTIP_R10-NIZ_1","MTTIP_R10-NKU_1","MTTIP_R10-NLY_1","MTTIPP1NI1","MTTIP_R10-NQA_1","MTTIPP1SA1","MTTIP_R10-NTC_1","MTTIPP1VE1","MTTIPP1VV1","MTTIP_R10-NAR_1","MTTIP_R10-NAA_1","MTTIP_R10-NAS_1","MTTIP_R10-NAU_1","MTTIP_R10-NAJ_1","MTTIPP1BF1","MTTIP_R10-NBA_1","MTTIP_R10-NBB_1","MTTIP_R10-NBO_1","MTTIP_R10-NBE_1","MTTIPP1BR1","MTTIP_R10-NBX_1","MTTIP_R10-NBU_1","MTTIPP1CM1","MTTIPP1CA1","MTTIP_R10-NCD_1","MTTIP_R10-NCI_1","MTTIP_R10-NCH_1","MTTIPP1CO1","MTTIP_R10-NCF_1","MTTIPP1CG1","MTTIP_R10-NCS_1","MTTIP_R10-NHR_1","MTTIP_R10-NCY_1","MTTIP_R10-NDA_1","MTTIP_R10-NDR_1","MTTIPP1EG1","MTTIP_R10-NES_1","MTTIP_R10-NEK_1","MTTIP_R10-NEN_1","MTTIP_R10-NFI_1","MTTIPP1FR1","MTTIPP1GB1","MTTIP_R10-NGG_1","MTTIPP1BZ1","MTTIP_R10-NGH_1","MTTIP_R10-NGI_1","MTTIP_R10-NGR_1","MTTIP_R10-NGT_1","MTTIP_R10-NGV_1","MTTIP_R10-NHK_1","MTTIP_R10-NHU_1","MTTIP_R10-NIN_1","MTTIP_R10-NID_1","MTTIP_R10-NEI_1","MTTIP_R10-NIS_1","MTTIPP1IT1","MTTIP_R10-NIV_1","MTTIP_R10-NJM_1","MTTIPP1JA1","MTTIP_R10-NKZ_1","MTTIP_R10-NKS_1","MTTIP_R10-NKG_1","MTTIP_R10-NLG_1","MTTIP_R10-NLI_1","MTTIP_R10-NLH_1","MTTIP_R10-NMY_1","MTTIP_R10-NMT_1","MTTIP_R10-NMR_1","MTTIPP1MX1","MTTIP_R10-NMO_1","MTTIP_R10-NWA_1","MTTIPP1NL1","MTTIPP1NA1","MTTIP_R10-NNE_1","MTTIPP1NO1","MTTIP_R10-NMU_1","MTTIP_R10-NPK_1","MTTIP_R10-NPM_1","MTTIP_R10-NPE_1","MTTIP_R10-NRP_1","MTTIP_R10-NPL_1","MTTIP_R10-NPO_1","MTTIPP1RQ1","MTTIP_R10-NRO_1","MTTIP_R10-NRS_1","MTTIP_R10-NSG_1","MTTIP_R10-NSN_1","MTTIP_R10-NSF_1","MTTIPP1SP1","MTTIP_R10-NWZ_1","MTTIP_R10-NSW_1","MTTIP_R10-NSZ_1","MTTIP_R10-NSY_1","MTTIP_R10-NTW_1","MTTIP_R10-NTH_1","MTTIP_R10-NTO_1","MTTIPP1TD1","MTTIP_R10-NTS_1","MTTIP_R10-NTU_1","MTTIP_R10-NTX_1","MTTIP_R10-NUR_1","MTTIPP1UK1","MTTIP_R10-NUY_1","MTTIP_R10-NVM_1","MTTIPP1VQ1","MTTIP_R10-NYE_1"

444

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1981" Annual",2012,"6/30/1981" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_impcp_a2_r10_ep00_ip0_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_impcp_a2_r10_ep00_ip0_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 9:02:39 AM" "Back to Contents","Data 1: East Coast (PADD 1) Total Crude Oil and Products Imports" "Sourcekey","MTTIPP11","MTTIPP1PG1","MTTIP_R10-ME0_1","MTTIPP1AG1","MTTIPP1AO1","MTTIPP1EC1","MTTIP_R10-NIZ_1","MTTIP_R10-NKU_1","MTTIP_R10-NLY_1","MTTIPP1NI1","MTTIP_R10-NQA_1","MTTIPP1SA1","MTTIP_R10-NTC_1","MTTIPP1VE1","MTTIPP1VV1","MTTIP_R10-NAR_1","MTTIP_R10-NAA_1","MTTIP_R10-NAS_1","MTTIP_R10-NAU_1","MTTIP_R10-NAJ_1","MTTIPP1BF1","MTTIP_R10-NBA_1","MTTIP_R10-NBB_1","MTTIP_R10-NBO_1","MTTIP_R10-NBE_1","MTTIPP1BR1","MTTIP_R10-NBX_1","MTTIP_R10-NBU_1","MTTIPP1CM1","MTTIPP1CA1","MTTIP_R10-NCD_1","MTTIP_R10-NCI_1","MTTIP_R10-NCH_1","MTTIPP1CO1","MTTIP_R10-NCF_1","MTTIPP1CG1","MTTIP_R10-NCS_1","MTTIP_R10-NHR_1","MTTIP_R10-NCY_1","MTTIP_R10-NDA_1","MTTIP_R10-NDR_1","MTTIPP1EG1","MTTIP_R10-NES_1","MTTIP_R10-NEK_1","MTTIP_R10-NEN_1","MTTIP_R10-NFI_1","MTTIPP1FR1","MTTIPP1GB1","MTTIP_R10-NGG_1","MTTIPP1BZ1","MTTIP_R10-NGH_1","MTTIP_R10-NGI_1","MTTIP_R10-NGR_1","MTTIP_R10-NGT_1","MTTIP_R10-NGV_1","MTTIP_R10-NHK_1","MTTIP_R10-NHU_1","MTTIP_R10-NIN_1","MTTIP_R10-NID_1","MTTIP_R10-NEI_1","MTTIP_R10-NIS_1","MTTIPP1IT1","MTTIP_R10-NIV_1","MTTIP_R10-NJM_1","MTTIPP1JA1","MTTIP_R10-NKZ_1","MTTIP_R10-NKS_1","MTTIP_R10-NKG_1","MTTIP_R10-NLG_1","MTTIP_R10-NLI_1","MTTIP_R10-NLH_1","MTTIP_R10-NMY_1","MTTIP_R10-NMT_1","MTTIPP1MX1","MTTIP_R10-NMO_1","MTTIP_R10-NWA_1","MTTIPP1NL1","MTTIPP1NA1","MTTIP_R10-NNE_1","MTTIPP1NO1","MTTIP_R10-NMU_1","MTTIP_R10-NPK_1","MTTIP_R10-NPM_1","MTTIP_R10-NPE_1","MTTIP_R10-NRP_1","MTTIP_R10-NPL_1","MTTIP_R10-NPO_1","MTTIPP1RQ1","MTTIP_R10-NRO_1","MTTIP_R10-NRS_1","MTTIP_R10-NSG_1","MTTIP_R10-NSN_1","MTTIP_R10-NSF_1","MTTIPP1SP1","MTTIP_R10-NWZ_1","MTTIP_R10-NSW_1","MTTIP_R10-NSZ_1","MTTIP_R10-NSY_1","MTTIP_R10-NTW_1","MTTIP_R10-NTH_1","MTTIP_R10-NTO_1","MTTIP_R10-NTN_1","MTTIPP1TD1","MTTIP_R10-NTS_1","MTTIP_R10-NTU_1","MTTIP_R10-NTX_1","MTTIP_R10-NUR_1","MTTIPP1UK1","MTTIP_R10-NUY_1","MTTIP_R10-NVM_1","MTTIPP1VQ1","MTTIP_R10-NYE_1"

445

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

98,"Annual",2012,"6/30/1981" 98,"Annual",2012,"6/30/1981" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_impcp_a2_r50_ep00_ip0_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_impcp_a2_r50_ep00_ip0_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 9:20:29 AM" "Back to Contents","Data 1: West Coast (PADD 5) Total Crude Oil and Products Imports" "Sourcekey","MTTIPP51","MTTIPP5PG1","MTTIP_R50-ME0_1","MTTIP_R50-NAG_1","MTTIP_R50-NAO_1","MTTIPP5EC1","MTTIP_R50-NIZ_1","MTTIP_R50-NKU_1","MTTIP_R50-NLY_1","MTTIP_R50-NNI_1","MTTIP_R50-NQA_1","MTTIPP5SA1","MTTIP_R50-NTC_1","MTTIPP5VE1","MTTIPP5VV1","MTTIPP5AR1","MTTIP_R50-NAA_1","MTTIPP5AS1","MTTIP_R50-NAJ_1","MTTIP_R50-NBF_1","MTTIP_R50-NBA_1","MTTIP_R50-NBO_1","MTTIP_R50-NBE_1","MTTIP_R50-NBN_1","MTTIP_R50-NBL_1","MTTIP_R50-NBR_1","MTTIP_R50-NBX_1","MTTIP_R50-NCM_1","MTTIPP5CA1","MTTIP_R50-NCD_1","MTTIP_R50-NCI_1","MTTIPP5CH1","MTTIPP5CO1","MTTIPP5CF1","MTTIP_R50-NCG_1","MTTIP_R50-NCS_1","MTTIP_R50-NHR_1","MTTIP_R50-NDA_1","MTTIP_R50-NDR_1","MTTIP_R50-NEG_1","MTTIP_R50-NES_1","MTTIP_R50-NEK_1","MTTIP_R50-NEN_1","MTTIP_R50-NFI_1","MTTIP_R50-NFR_1","MTTIP_R50-NGB_1","MTTIP_R50-NGM_1","MTTIP_R50-NGR_1","MTTIP_R50-NGT_1","MTTIP_R50-NGV_1","MTTIP_R50-NHK_1","MTTIP_R50-NHU_1","MTTIP_R50-NIN_1","MTTIPP5ID1","MTTIP_R50-NIS_1","MTTIP_R50-NIT_1","MTTIP_R50-NIV_1","MTTIP_R50-NJM_1","MTTIP_R50-NJA_1","MTTIP_R50-NKZ_1","MTTIP_R50-NKS_1","MTTIP_R50-NLH_1","MTTIP_R50-NMY_1","MTTIP_R50-NMT_1","MTTIPP5MX1","MTTIP_R50-NMO_1","MTTIP_R50-NNL_1","MTTIP_R50-NNA_1","MTTIP_R50-NNZ_1","MTTIP_R50-NNU_1","MTTIP_R50-NNO_1","MTTIP_R50-NMU_1","MTTIP_R50-NPM_1","MTTIP_R50-NPP_1","MTTIPP5PE1","MTTIP_R50-NRP_1","MTTIP_R50-NPL_1","MTTIP_R50-NPO_1","MTTIP_R50-NRO_1","MTTIP_R50-NRS_1","MTTIPP5SN1","MTTIP_R50-NSF_1","MTTIP_R50-NSP_1","MTTIP_R50-NPG_1","MTTIP_R50-NSW_1","MTTIP_R50-NSY_1","MTTIP_R50-NTW_1","MTTIP_R50-NTH_1","MTTIP_R50-NTD_1","MTTIP_R50-NTS_1","MTTIP_R50-NTU_1","MTTIP_R50-NTX_1","MTTIP_R50-NUR_1","MTTIPP5UK1","MTTIP_R50-NUY_1","MTTIP_R50-NVM_1","MTTIPP5VQ1","MTTIP_R50-NYE_1"

446

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

1,"Annual",2012,"6/30/1981" 1,"Annual",2012,"6/30/1981" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_expc_a_ep00_eex_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_expc_a_ep00_eex_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 7:28:29 AM" "Back to Contents","Data 1: Total Crude Oil and Products Exports by Destination" "Sourcekey","MTTEXUS1","MTTEX_NUS-NAF_1","MTTEX_NUS-NAL_1","MTTEX_NUS-NAG_1","MTTEX_NUS-NAN_1","MTTEX_NUS-NAO_1","MTTEX_NUS-NAV_1","MTTEX_NUS-NAC_1","MTTEXAR1","MTTEX_NUS-NAE_1","MTTEX_NUS-NAA_1","MTTEXAS1","MTTEX_NUS-NAU_1","MTTEX_NUS-NAJ_1","MTTEXBF1","MTTEXBA1","MTTEX_NUS-NBB_1","MTTEX_NUS-NBO_1","MTTEXBE1","MTTEX_NUS-NBH_1","MTTEX_NUS-NBN_1","MTTEX_NUS-NBL_1","MTTEX_NUS-NBK_1","MTTEXBR1","MTTEX_NUS-NBX_1","MTTEX_NUS-NBU_1","MTTEX_NUS-NBM_1","MTTEX_NUS-NBD_1","MTTEX_NUS-NCB_1","MTTEX_NUS-NCM_1","MTTEXCA1","MTTEX_NUS-NCJ_1","MTTEX_NUS-NCD_1","MTTEXCI1","MTTEXCH1","MTTEXCO1","MTTEX_NUS-NCF_1","MTTEX_NUS-NCG_1","MTTEXCS1","MTTEX_NUS-NHR_1","MTTEX_NUS-NCY_1","MTTEX_NUS-NCZ_1","MTTEXDA1","MTTEX_NUS-NDJ_1","MTTEXDO1","M_EP00_EEX_NUS-NDR_1","MTTEXEC1","MTTEXEG1","MTTEXES1","MTTEX_NUS-NEK_1","MTTEX_NUS-NER_1","MTTEX_NUS-NEN_1","MTTEX_NUS-NET_1","MTTEX_NUS-NFJ_1","MTTEXFI1","MTTEXFR1","MTTEX_NUS-NFG_1","MTTEXFP1","MTTEX_NUS-NGB_1","MTTEX_NUS-NGG_1","MTTEXBZ1","MTTEXGH1","MTTEX_NUS-NGI_1","MTTEXGR1","MTTEX_NUS-NGL_1","MTTEX_NUS-NGJ_1","M_EP00_EEX_NUS-NGP_1","MTTEXGT1","MTTEX_NUS-NGV_1","MTTEX_NUS-NGY_1","MTTEX_NUS-NHA_1","MTTEXHO1","MTTEXHK1","MTTEX_NUS-NHU_1","MTTEX_NUS-NIC_1","MTTEXIN1","MTTEXID1","MTTEX_NUS-NIZ_1","MTTEXEI1","MTTEXIS1","MTTEXIT1","MTTEX_NUS-NIV_1","MTTEXJM1","MTTEXJA1","MTTEX_NUS-NJO_1","MTTEX_NUS-NKZ_1","MTTEX_NUS-NKE_1","MTTEXKS1","MTTEX_NUS-NKN_1","MTTEX_NUS-NKG_1","MTTEX_NUS-NKT_1","MTTEX_NUS-NKU_1","MTTEX_NUS-NLG_1","MTTEX_NUS-NLE_1","MTTEX_NUS-NLI_1","MTTEX_NUS-NLY_1","MTTEX_NUS-NLH_1","MTTEX_NUS-NMC_1","MTTEX_NUS-NMK_1","MTTEX_NUS-NMA_1","MTTEXMY1","MTTEX_NUS-NMV_1","MTTEX_NUS-NML_1","MTTEX_NUS-NMT_1","MTTEX_NUS-NRM_1","MTTEX_NUS-NMR_1","MTTEX_NUS-NMP_1","MTTEXMX1","MTTEX_NUS-NFM_1","MTTEX_NUS-NMQ_1","MTTEX_NUS-NMD_1","MTTEX_NUS-NMN_1","MTTEX_NUS-NMG_1","M_EP00_EEX_NUS-NMJ_1","MTTEX_NUS-NMH_1","MTTEX_NUS-NMO_1","MTTEX_NUS-NMZ_1","MTTEX_NUS-NWA_1","MTTEX_NUS-NNP_1","MTTEXNL1","MTTEXNA1","MTTEX_NUS-NNC_1","MTTEXNZ1","MTTEX_NUS-NNU_1","MTTEX_NUS-NNG_1","MTTEXNI1","MTTEX_NUS-NNE_1","MTTEXNO1","MTTEX_NUS-NMU_1","MTTEX_NUS-NPK_1","MTTEXPM1","MTTEX_NUS-NPP_1","MTTEX_NUS-NPF_1","MTTEX_NUS-NPA_1","MTTEXPE1","MTTEXRP1","MTTEXPL1","MTTEXPO1","MTTEXRQ1","MTTEX_NUS-NQA_1","MTTEX_NUS-NRO_1","MTTEX_NUS-NRS_1","MTTEX_NUS-NSC_1","MTTEX_NUS-NST_1","MTTEX_NUS-NSB_1","MTTEX_NUS-NVC_1","MTTEX_NUS-NWS_1","MTTEX_NUS-NSM_1","MTTEXSA1","MTTEX_NUS-NSG_1","MTTEX_NUS-NYI_1","MTTEX_NUS-NSE_1","MTTEX_NUS-NSL_1","MTTEXSN1","MTTEX_NUS-NSK_1","MTTEX_NUS-NSI_1","MTTEX_NUS-NBP_1","MTTEXSF1","MTTEXSP1","MTTEX_NUS-NPG_1","MTTEX_NUS-NCE_1","MTTEX_NUS-NSU_1","MTTEXNS1","MTTEX_NUS-NWZ_1","MTTEXSW1","MTTEXSZ1","MTTEX_NUS-NSY_1","MTTEXTW1","MTTEX_NUS-NTZ_1","MTTEXTH1","MTTEX_NUS-NTN_1","MTTEX_NUS-NTO_1","MTTEXTD1","MTTEX_NUS-NTS_1","MTTEXTU1","MTTEX_NUS-NTX_1","MTTEX_NUS-NTK_1","MTTEX_NUS-NUG_1","MTTEX_NUS-NUR_1","MTTEXTC1","MTTEXUK1","MTTEXUY1","MTTEX_NUS-NUZ_1","MTTEX_NUS-NNH_1","MTTEXVE1","MTTEX_NUS-NVM_1","MTTEX_NUS-NVI_1","MTTEXVQ1","MTTEX_NUS-NYE_1","MTTEXYO1","MTTEX_NUS-NZA_1"

447

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

7,"Annual",2012,"6/30/1981" 7,"Annual",2012,"6/30/1981" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_impcp_a2_r30_ep00_ip0_mbbl_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_impcp_a2_r30_ep00_ip0_mbbl_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 9:11:43 AM" "Back to Contents","Data 1: Gulf Coast (PADD 3) Total Crude Oil and Products Imports" "Sourcekey","MTTIPP31","MTTIPP3PG1","MTTIP_R30-ME0_1","MTTIPP3AG1","MTTIPP3AO1","MTTIPP3EC1","MTTIP_R30-NIZ_1","MTTIPP3KU1","MTTIP_R30-NLY_1","MTTIPP3NI1","MTTIP_R30-NQA_1","MTTIPP3SA1","MTTIPP3TC1","MTTIPP3VE1","MTTIPP3VV1","MTTIP_R30-NAL_1","MTTIPP3AR1","MTTIP_R30-NAA_1","MTTIPP3AS1","MTTIP_R30-NAU_1","MTTIP_R30-NAJ_1","MTTIP_R30-NBF_1","MTTIP_R30-NBA_1","MTTIP_R30-NBO_1","MTTIPP3BE1","MTTIP_R30-NBH_1","MTTIP_R30-NBN_1","MTTIP_R30-NBL_1","MTTIP_R30-NBR_1","MTTIP_R30-NBX_1","MTTIP_R30-NBU_1","MTTIP_R30-NBM_1","MTTIP_R30-NCM_1","MTTIPP3CA1","MTTIP_R30-NCD_1","MTTIP_R30-NCI_1","MTTIP_R30-NCH_1","MTTIPP3CO1","MTTIPP3CF1","MTTIPP3CG1","MTTIP_R30-NCW_1","MTTIP_R30-NCS_1","MTTIP_R30-NHR_1","MTTIP_R30-NCY_1","MTTIP_R30-NCZ_1","MTTIP_R30-NDA_1","MTTIPP3EG1","MTTIP_R30-NES_1","MTTIP_R30-NEK_1","MTTIP_R30-NEN_1","MTTIP_R30-NFI_1","MTTIPP3FR1","MTTIPP3GB1","MTTIP_R30-NGG_1","MTTIP_R30-NGM_1","MTTIP_R30-NGH_1","MTTIP_R30-NGR_1","MTTIP_R30-NGT_1","MTTIP_R30-NGV_1","MTTIP_R30-NHU_1","MTTIP_R30-NIN_1","MTTIPP3ID1","MTTIP_R30-NEI_1","MTTIP_R30-NIS_1","MTTIPP3IT1","MTTIP_R30-NIV_1","MTTIP_R30-NJM_1","MTTIP_R30-NJA_1","MTTIP_R30-NKZ_1","MTTIPP3KS1","MTTIP_R30-NKG_1","MTTIP_R30-NLG_1","MTTIP_R30-NLI_1","MTTIP_R30-NLH_1","MTTIP_R30-NMY_1","MTTIP_R30-NMT_1","MTTIP_R30-NMR_1","MTTIPP3MX1","MTTIP_R30-NMQ_1","MTTIP_R30-NMO_1","MTTIP_R30-NNL_1","MTTIPP3NA1","MTTIP_R30-NNZ_1","MTTIPP3NO1","MTTIP_R30-NMU_1","MTTIP_R30-NPK_1","MTTIP_R30-NPM_1","MTTIP_R30-NPP_1","MTTIP_R30-NPE_1","MTTIP_R30-NRP_1","MTTIP_R30-NPL_1","MTTIP_R30-NPO_1","MTTIP_R30-NPZ_1","MTTIP_R30-NRO_1","MTTIP_R30-NRS_1","MTTIP_R30-NSN_1","MTTIP_R30-NSK_1","MTTIP_R30-NSF_1","MTTIPP3SP1","MTTIPP3SW1","MTTIP_R30-NSZ_1","MTTIPP3SY1","MTTIP_R30-NTW_1","MTTIPP3TH1","MTTIP_R30-NTO_1","MTTIP_R30-NTN_1","MTTIPP3TD1","MTTIP_R30-NTS_1","MTTIP_R30-NTU_1","MTTIP_R30-NTX_1","MTTIP_R30-NUR_1","MTTIPP3UK1","MTTIP_R30-NUY_1","MTTIP_R30-NUZ_1","MTTIP_R30-NVM_1","MTTIPP3VQ1","MTTIPP3YE1"

448

Workbook Contents  

U.S. Energy Information Administration (EIA) Indexed Site

Annual",2012,"6/30/1973" Annual",2012,"6/30/1973" ,"Release Date:","9/27/2013" ,"Next Release Date:","9/26/2014" ,"Excel File Name:","pet_move_neti_a_ep00_imn_mbblpd_a.xls" ,"Available from Web Page:","http://www.eia.gov/dnav/pet/pet_move_neti_a_ep00_imn_mbblpd_a.htm" ,"Source:","Energy Information Administration" ,"For Help, Contact:","infoctr@eia.gov" ,,"(202) 586-8800",,,"11/25/2013 10:46:04 AM" "Back to Contents","Data 1: Net Imports of Total Crude Oil and Products into the U.S. by Country" "Sourcekey","MTTNTUS2","MTTNTUSPG2","MTTNT_NUS-ME0_2","MTTNTUSAG2","MTTNTUSAO2","MTTNTUSEC2","MTTNTUSIR2","MTTNT_NUS-NIZ_2","MTTNTUSKU2","MTTNT_NUS-NLY_2","MTTNTUSNI2","MTTNTUSQA2","MTTNTUSSA2","MTTNTUSTC2","MTTNTUSVE2","MTTNTUSVV2","MTTNT_NUS-NAF_2","MTTNT_NUS-NAL_2","MTTNT_NUS-NAN_2","MTTNT_NUS-NAV_2","MTTNT_NUS-NAC_2","MTTNTUSAR2","MTTNT_NUS-NAE_2","MTTNT_NUS-NAA_2","MTTNTUSAS2","MTTNT_NUS-NAU_2","MTTNT_NUS-NAJ_2","MTTNTUSBF2","MTTNT_NUS-NBA_2","MTTNT_NUS-NBG_2","MTTNT_NUS-NBB_2","MTTNT_NUS-NBO_2","MTTNTUSBE2","MTTNT_NUS-NBH_2","MTTNT_NUS-NBN_2","MTTNT_NUS-NBD_2","MTTNT_NUS-NBL_2","MTTNT_NUS-NBK_2","MTTNTUSBR2","MTTNTUSBX2","MTTNT_NUS-NBU_2","MTTNT_NUS-NBM_2","MTTNT_NUS-NCB_2","MTTNTUSCM2","MTTNTUSCA2","MTTNT_NUS-NCJ_2","MTTNT_NUS-NCD_2","MTTNT_NUS-NCI_2","MTTNTUSCH2","MTTNTUSCO2","MTTNTUSCF2","MTTNTUSCG2","MTTNT_NUS-NCW_2","MTTNT_NUS-NCS_2","MTTNT_NUS-NHR_2","MTTNT_NUS-NCY_2","MTTNT_NUS-NCZ_2","MTTNT_NUS-NDA_2","MTTNT_NUS-NDJ_2","MTTNT_NUS-NDO_2","MTTNT_NUS-NDR_2","MTTNTUSEG2","MTTNT_NUS-NES_2","MTTNT_NUS-NEK_2","MTTNT_NUS-NET_2","MTTNT_NUS-NER_2","MTTNT_NUS-NEN_2","MTTNT_NUS-NFJ_2","MTTNT_NUS-NFI_2","MTTNTUSFR2","MTTNT_NUS-NFP_2","MTTNT_NUS-NFG_2","MTTNTUSGB2","MTTNT_NUS-NGG_2","MTTNTUSBZ2","MTTNT_NUS-NGH_2","MTTNT_NUS-NGI_2","MTTNTUSGR2","MTTNT_NUS-NGL_2","MTTNT_NUS-NGJ_2","M_EP00_IMN_NUS-NGP_2","MTTNTUSGT2","MTTNT_NUS-NGV_2","MTTNT_NUS-NGY_2","MTTNT_NUS-NHA_2","MTTNT_NUS-NHO_2","MTTNT_NUS-NHK_2","MTTNT_NUS-NHU_2","MTTNT_NUS-NIC_2","MTTNTUSIN2","MTTNTUSID2","MTTNT_NUS-NEI_2","MTTNT_NUS-NIS_2","MTTNTUSIT2","MTTNT_NUS-NIV_2","MTTNTUSJM2","MTTNTUSJA2","MTTNT_NUS-NJO_2","MTTNT_NUS-NKZ_2","MTTNT_NUS-NKE_2","MTTNTUSKS2","MTTNT_NUS-NKT_2","MTTNT_NUS-NKG_2","MTTNT_NUS-NLG_2","MTTNT_NUS-NLE_2","MTTNT_NUS-NLI_2","MTTNT_NUS-NLH_2","MTTNT_NUS-NMC_2","MTTNT_NUS-NMK_2","MTTNT_NUS-NMA_2","MTTNTUSMY2","MTTNT_NUS-NMV_2","MTTNT_NUS-NML_2","MTTNT_NUS-NMT_2","MTTNT_NUS-NRM_2","MTTNT_NUS-NMR_2","MTTNT_NUS-NMP_2","MTTNTUSMX2","MTTNT_NUS-NFM_2","MTTNT_NUS-NMQ_2","MTTNT_NUS-NMN_2","MTTNT_NUS-NMD_2","MTTNT_NUS-NMG_2","M_EP00_IMN_NUS-NMJ_2","MTTNT_NUS-NMH_2","MTTNT_NUS-NMO_2","MTTNT_NUS-NMZ_2","MTTNT_NUS-NWA_2","MTTNT_NUS-NNP_2","MTTNTUSNL2","MTTNTUSNA2","MTTNT_NUS-NNC_2","MTTNT_NUS-NNZ_2","MTTNT_NUS-NNU_2","MTTNT_NUS-NNG_2","MTTNT_NUS-NNE_2","MTTNTUSNO2","MTTNTUSMU2","MTTNT_NUS-NPK_2","MTTNTUSPM2","MTTNT_NUS-NPP_2","MTTNT_NUS-NPF_2","MTTNT_NUS-NPA_2","MTTNTUSPE2","MTTNT_NUS-NRP_2","MTTNT_NUS-NPL_2","MTTNT_NUS-NPO_2","MTTNTUSRQ2","MTTNTUSRO2","MTTNT_NUS-NRS_2","MTTNT_NUS-NSC_2","MTTNT_NUS-NST_2","MTTNT_NUS-NSB_2","MTTNT_NUS-NVC_2","MTTNT_NUS-NWS_2","MTTNT_NUS-NSM_2","MTTNT_NUS-NSG_2","MTTNT_NUS-NYI_2","MTTNT_NUS-NSL_2","MTTNT_NUS-NSN_2","MTTNT_NUS-NSK_2","MTTNT_NUS-NSI_2","MTTNT_NUS-NSF_2","MTTNTUSSP2","MTTNT_NUS-NPG_2","MTTNT_NUS-NCE_2","MTTNT_NUS-NNS_2","MTTNT_NUS-NWZ_2","MTTNTUSSW2","MTTNT_NUS-NSZ_2","MTTNTUSSY2","MTTNTUSTW2","MTTNT_NUS-NTZ_2","MTTNTUSTH2","MTTNT_NUS-NTO_2","MTTNT_NUS-NTN_2","MTTNTUSTD2","MTTNT_NUS-NTS_2","MTTNTUSTU2","MTTNT_NUS-NTX_2","MTTNT_NUS-NTK_2","MTTNT_NUS-NUG_2","MTTNT_NUS-NUR_2","MTTNTUSUK2","MTTNT_NUS-NUY_2","MTTNT_NUS-NUZ_2","MTTNT_NUS-NNH_2","MTTNT_NUS-NVM_2","MTTNT_NUS-NVI_2","MTTNTUSVQ2","MTTNTUSYE2","MTTNT_NUS-NYO_2","MTTNTUSWW2"

449

Recent advances in lithiumsulfur batteries  

Science Journals Connector (OSTI)

Abstract Lithiumsulfur (LiS) batteries have attracted much attention lately because they have very high theoretical specific energy (2500Whkg?1), five times higher than that of the commercial LiCoO2/graphite batteries. As a result, they are strong contenders for next-generation energy storage in the areas of portable electronics, electric vehicles, and storage systems for renewable energy such as wind power and solar energy. However, poor cycling life and low capacity retention are main factors limiting their commercialization. To date, a large number of electrode and electrolyte materials to address these challenges have been investigated. In this review, we present the latest fundamental studies and technological development of various nanostructured cathode materials for LiS batteries, including their preparation approaches, structure, morphology and battery performance. Furthermore, the development of other significant components of LiS batteries including anodes, electrolytes, additives, binders and separators are also highlighted. Not only does the intention of our review article comprise the summary of recent advances in LiS cells, but also we cover some of our proposals for engineering of LiS cell configurations. These systematic discussion and proposed directions can enlighten ideas and offer avenues in the rational design of durable and high performance LiS batteries in the near future.

Lin Chen; Leon L. Shaw

2014-01-01T23:59:59.000Z

450

Heat Transfer Characteristics of Sulfur and Sulfur Diluted with Hydrogen Sulfide Flowing Through Circular Tubes  

E-Print Network [OSTI]

is called the pumping-power advantage factor, and has the value 2. 5 x 10 for sodium. The only metals having a higher value of H are 13 lithium 7 and bismuth. Lithium 7 comprises 92. 5% of natural lithium, but the cost of separating it from lithium 6...-section for thermal neutrons being 0. 130 barns. For comparison, water has an absorption cross-section of 0. 58 barns for thermal neutrons (2) . Sulfur is not activated by exposure to neutron flux in such a way as to produce a radioactive isotope which...

Stone, Porter Walwyn

1960-01-01T23:59:59.000Z

451

Polyaniline-modified cetyltrimethylammonium bromide-graphene oxide-sulfur nanocomposites with enhanced performance for lithium-sulfur batteries  

Science Journals Connector (OSTI)

Conductive polymer coatings can boost the power storage capacity of lithium-sulfur batteries. We report here on the design and ... polyaniline (PANI)-modified cetyltrimethylammonium bromide (CTAB)-graphene oxide ...

Yongcai Qiu; Wanfei Li; Guizhu Li; Yuan Hou; Lisha Zhou; Hongfei Li

2014-09-01T23:59:59.000Z

452

COMPONENT DEVELOPMENT NEEDS FOR THE HYBRID SULFUR ELECTROLYZER  

SciTech Connect (OSTI)

Fiscal year 2008 studies in electrolyzer component development have focused on the characterization of membrane electrode assemblies (MEA) after performance tests in the single cell electrolyzer, evaluation of electrocatalysts and membranes using a small scale electrolyzer and evaluating the contribution of individual cell components to the overall electrochemical performance. Scanning electron microscopic (SEM) studies of samples taken from MEAs testing in the SRNL single cell electrolyzer test station indicates a sulfur-rich layer forms between the cathode catalyst layer and the membrane. Based on a review of operating conditions for each of the MEAs evaluated, we conclude that the formation of the layer results from the reduction of sulfur dioxide as it passes through the MEA and reaches the catalyst layer at the cathode-membrane interface. Formation of the sulfur rich layer results in partial delamination of the cathode catalyst layer leading to diminished performance. Furthermore we believe that operating the electrolyzer at elevated pressure significantly increases the rate of formation due to increased adsorption of hydrogen on the internal catalyst surface. Thus, identification of a membrane that exhibits much lower transport of sulfur dioxide is needed to reduce the quantity of sulfur dioxide that reaches the cathode catalyst and is reduced to produce the sulfur-rich layer. Three candidate membranes are currently being evaluated that have shown promise from preliminary studies, (1) modified Nafion{reg_sign}, (2) polybenzimidazole (PBI), and (3) sulfonated Diels Alder polyphenylene (SDAPP). Testing examined the activity for the sulfur dioxide oxidation of platinum (Pt) and platinum-alloy catalysts in 30 wt% sulfuric acid solution. Linear sweep voltammetry showed an increase in activity when catalysts in which Pt is alloyed with non-noble transition metals such as cobalt and chromium. However when Pt is alloyed with noble metals, such as iridium or ruthenium, the kinetic activity decreases. We recommend further testing to determine if these binary alloys will provide the increased reaction kinetic needed to meet the targets. We also plan to test the performance of these catalyst materials for both proton and sulfur dioxide reduction. The latter may provide another parameter by which we can control the reduction of sulfur dioxide upon transport to the cathode catalyst surface. A small scale electrolyzer (2 cm{sup 2}) has been fabricated and successfully installed as an additional tool to evaluate the effect of different operating conditions on electrolyzer and MEA performance. Currently this electrolyzer is limited to testing at temperatures up to 80 C and at atmospheric pressure. Selected electrochemical performance data from the single cell sulfur dioxide depolarized electrolyzer were analyzed with the aid of an empirical equation which takes into account the overpotential of each of the components. By using the empirical equation, the performance data was broken down into its components and a comparison of the potential losses was made. The results indicated that for the testing conditions of 80 C and 30 wt% sulfuric acid, the major overpotential contribution ({approx}70 % of all losses) arise from the slow reaction rate of oxidation of sulfur dioxide. The results indicate that in order to meet the target of hydrogen production at 0.5 A/cm{sup 2} at 0.6 V and 50 wt% sulfuric acid, identification of a better catalyst for sulfur dioxide oxidation will provide the largest gain in electrolyzer performance.

Hobbs, D; Hector Colon-Mercado, H; Mark Elvington, M

2008-05-30T23:59:59.000Z

453

Particle size distributions from heavy-duty diesel engine operated on low-sulfur marine fuel  

Science Journals Connector (OSTI)

Particulate matter (PM) emission characteristics of a four-stroke diesel engine were investigated while operating on low-sulfur marine gas oil. PM size distributions appeared to be unimodal (accumulation mode) with fairly constant count median diameter (CMD) of 5565nm for all test modes at maximum engine speed. The slightly bigger CMD of around 76nm for unimodal particle size distributions at 1080rpm at medium- and high-load conditions was observed. The bimodal size distribution was registered only at very low load with nuclei CMD being below 15nm, accumulation CMD of around 82nm and percentage of nanoparticles of around 65%. The study of primary dilution air temperature (PDT) effect revealed a significant reduction in total particle number for all operating conditions when PDT was increased from 30C to 400C. This also had an effect on particle CMD values and is believed to be due to evaporation of sulfuric acid with bound water and certain organic fractions that were formed during dilution process (at PDT=30C). At very low load intermediate speed conditions, the heating of dilution air had a very little effect on the nucleation mode, which could suggest that it primarily consists of heavy hydrocarbons associated with lubrication oil.

Sergey Ushakov; Harald Valland; Jrgen B. Nielsen; Erik Hennie

2013-01-01T23:59:59.000Z

454

Table of Contents Chapter and Content Pages  

E-Print Network [OSTI]

#12;Page 2 Table of Contents Chapter and Content Pages 1. Field Trip Itinerary ................................................................................. 7 4. Geologic Framework of the Netherlands Antilles 5. Coral Reefs of the Netherlands Antilles

Fouke, Bruce W.

455

Notes on Frequentist, Maximum Likelihood & Bayesian Statistics  

E-Print Network [OSTI]

, theory, "gut feeling," etc. · Changes the probability distribution #12;Bayesian Statistics · ProbabilityNotes on Frequentist, Maximum Likelihood & Bayesian Statistics #12;Statistical Methods · Probability is a long-term frequency statement about the data ­ if repeated, what proportion of the time would

Ernest, Holly

456

PublicationsmailagreementNo.40014024 maximum depth  

E-Print Network [OSTI]

and a video camera to complete installation of the world's first regional cabled ocean observatory. NEPTUNE- tion systems that--using power and the internet--provide continuous, long-term monitoring of oceanPublicationsmailagreementNo.40014024 THE 2.7km maximum depth beneath the ocean surface of neptune

Pedersen, Tom

457

Coal Cleaning Using Resonance Disintegration for Mercury and Sulfur Reduction Prior to Combustion  

SciTech Connect (OSTI)

Coal-cleaning processes have been utilized to increase the heating value of coal by extracting ash-forming minerals in the coal. These processes involve the crushing or grinding of raw coal followed by physical separation processes, taking advantage of the density difference between carbonaceous particles and mineral particles. In addition to the desired increase in the heating value of coal, a significant reduction of the sulfur content of the coal fed to a combustion unit is effected by the removal of pyrite and other sulfides found in the mineral matter. WRI is assisting PulseWave to develop an alternate, more efficient method of liberating and separating the undesirable mineral matter from the carbonaceous matter in coal. The approach is based on PulseWave's patented resonance disintegration technology that reduces that particle size of materials by application of destructive resonance, shock waves, and vortex generating forces. Illinois No.5 coal, a Wyodak coal, and a Pittsburgh No.8 coal were processed using the resonance disintegration apparatus then subjected to conventional density separations. Initial microscopic results indicate that up to 90% of the pyrite could be liberated from the coal in the machine, but limitations in the density separations reduced overall effectiveness of contaminant removal. Approximately 30-80% of the pyritic sulfur and 30-50% of the mercury was removed from the coal. The three coals (both with and without the pyritic phase separated out) were tested in WRI's 250,000 Btu/hr Combustion Test Facility, designed to replicate a coal-fired utility boiler. The flue gases were characterized for elemental, particle bound, and total mercury in addition to sulfur. The results indicated that pre-combustion cleaning could reduce a large fraction of the mercury emissions.

Andrew Lucero

2005-04-01T23:59:59.000Z

458

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District  

Gasoline and Diesel Fuel Update (EIA)

57.3 57.3 61.4 66.0 65.3 62.6 51.3 56.6 62.7 66.3 60.3 49.1 February ........................... 55.3 59.2 63.2 63.3 60.2 49.6 55.4 61.1 63.7 58.8 47.9 March ................................ 53.0 57.1 61.1 61.7 58.1 47.2 52.8 58.3 61.6 56.2 45.1 April .................................. 54.6 58.4 61.5 63.6 59.1 49.7 54.8 59.7 63.8 58.6 46.8 May ................................... 53.8 57.9 61.7 63.8 59.0 48.8 54.4 58.2 64.1 58.5 45.5 June .................................. 50.7 54.2 59.0 60.3 56.0 45.0 50.9 56.3 60.3 55.1 42.4 July ................................... 49.8 53.8 57.9 57.9 54.9 43.8 50.0 55.5 58.2 53.7 41.6 August .............................. 48.5 53.1 56.2 57.3 53.6 42.4 49.5 53.2 58.3 52.8 40.7 September ........................ 51.6 55.9 58.2 60.1 55.9 46.6 50.8 55.8 60.5 54.8 44.0 October .............................

459

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District  

Gasoline and Diesel Fuel Update (EIA)

62.7 62.7 68.1 69.9 69.7 67.1 57.5 59.9 66.9 68.8 64.1 55.1 February ........................... 64.2 70.1 70.7 71.2 68.3 59.3 61.1 67.8 69.6 65.2 56.9 March ................................ 68.7 74.6 75.1 75.3 72.7 63.6 64.2 71.6 73.6 68.7 59.9 April .................................. 76.7 82.7 82.6 84.5 80.8 71.8 71.4 78.1 80.8 75.9 65.8 May ................................... 74.4 82.6 81.2 83.4 79.1 68.4 70.4 76.6 78.3 74.2 63.2 June .................................. 66.5 75.7 74.5 76.7 72.0 60.4 63.5 70.5 73.3 68.2 57.7 July ................................... 67.0 74.4 73.2 75.8 71.4 61.4 63.4 71.0 73.9 68.2 58.3 August .............................. 71.1 78.0 75.8 79.6 74.8 66.1 67.0 74.3 76.2 71.2 63.1 September ........................ 77.0 84.5 81.7 85.1 80.7 72.5 74.3 80.9 82.7 78.3 70.9 October .............................

460

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District  

Gasoline and Diesel Fuel Update (EIA)

76.6 76.6 82.7 84.1 83.7 81.2 71.0 73.8 80.7 83.7 78.2 69.4 February ........................... 74.9 81.6 81.9 82.5 79.3 68.8 71.5 76.8 81.7 75.4 66.5 March ................................ 69.0 74.8 76.5 76.7 73.7 64.0 67.0 71.7 76.6 70.6 60.9 April .................................. 67.7 74.4 75.5 77.0 72.8 63.2 65.8 71.0 77.4 70.6 60.6 May ................................... 66.4 72.0 74.5 76.3 71.8 61.8 65.1 70.5 76.3 69.9 59.1 June .................................. 62.9 68.7 72.2 73.9 69.1 57.7 62.6 67.6 73.0 66.9 56.1 July ................................... 61.7 67.7 70.5 72.5 67.7 56.9 61.9 66.5 71.4 65.9 55.1 August .............................. 64.4 69.8 71.9 74.2 69.6 59.9 63.9 68.4 72.7 67.5 58.0 September ........................ 63.5 70.3 71.4 74.2 68.9 58.7 63.7 68.1 73.2 67.5 57.9 October .............................

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


461

Table 41. No. 2 Diesel Fuel Prices by Sulfur Content, Sales Type, and PAD District  

Gasoline and Diesel Fuel Update (EIA)

56.9 56.9 63.4 65.6 64.6 62.1 51.4 54.0 60.9 64.4 58.4 49.7 February ........................... 56.9 63.4 65.0 64.4 61.7 51.9 54.2 60.9 63.5 58.6 49.9 March ................................ 57.6 64.4 65.1 66.2 62.4 52.6 53.7 61.4 64.5 58.7 49.4 April .................................. 60.6 67.4 66.8 68.8 64.9 56.0 56.8 63.6 67.4 61.6 52.6 May ................................... 61.5 67.7 68.5 70.4 66.1 56.9 58.6 65.4 68.6 63.3 54.4 June .................................. 59.2 65.3 67.4 68.7 64.4 53.7 56.8 63.7 67.5 61.7 51.6 July ................................... 57.8 63.8 65.9 67.3 63.0 52.7 55.3 62.1 65.5 59.9 50.2 August .............................. 59.7 66.3 66.5 68.3 64.3 55.4 57.2 63.3 65.9 61.3 52.5 September ........................ 61.1 67.3 67.9 70.4 65.8 56.8 57.8 64.5 68.1 62.5 53.8 October .............................

462

Table 17. U.S. No. 2 Diesel Fuel Prices by Sulfur Content and...  

Gasoline and Diesel Fuel Update (EIA)

1996 January ... 62.7 68.1 69.9 69.7 67.1 57.5 59.9 66.9 68.8 64.1 55.1 February ... 64.2 70.1 70.7 71.2 68.3 59.3 61.1 67.8 69.6...

463

Table 17. U.S. No. 2 Diesel Fuel Prices by Sulfur Content and...  

Gasoline and Diesel Fuel Update (EIA)

3 January ... - - - - - - - - - - - February ... - - - - - - - - - - - March ... - - - - - - - - - -...

464

Table 17. U.S. No. 2 Diesel Fuel Prices by Sulfur Content and...  

Annual Energy Outlook 2013 [U.S. Energy Information Administration (EIA)]

1996 ... 72.3 79.1 78.8 80.6 76.7 67.3 68.7 75.9 78.4 73.2 63.9 1997 January ... 76.6 82.7 84.1 83.7 81.2 71.0 73.8...

465

Hybrid Sulfur Thermochemical Process Development Annual Report  

SciTech Connect (OSTI)

The Hybrid Sulfur (HyS) Thermochemical Process is a means of producing hydrogen via water-splitting through a combination of chemical reactions and electrochemistry. Energy is supplied to the system as high temperature heat (approximately 900 C) and electricity. Advanced nuclear reactors (Generation IV) or central solar receivers can be the source of the primary energy. Large-scale hydrogen production based on this process could be a major contributor to meeting the needs of a hydrogen economy. This project's objectives include optimization of the HyS process design, analysis of technical issues and concerns, creation of a development plan, and laboratory-scale proof-of-concept testing. The key component of the HyS Process is the SO2-depolarized electrolyzer (SDE). Studies were performed that showed that an electrolyzer operating in the range of 500-600 mV per cell can lead to an overall HyS cycle efficiency in excess of 50%, which is superior to all other currently proposed thermochemical cycles. Economic analysis indicated hydrogen production costs of approximately $1.60 per kilogram for a mature nuclear hydrogen production plant. However, in order to meet commercialization goals, the electrolyzer should be capable of operating at high current density, have a long operating lifetime , and have an acceptable capital cost. The use of proton-exchange-membrane (PEM) technology, which leverages work for the development of PEM fuel cells, was selected as the most promising route to meeting these goals. The major accomplishments of this project were the design and construction of a suitable electrolyzer test facility and the proof-of-concept testing of a PEM-based SDE.

Summers, William A.; Buckner, Melvin R.

2005-07-21T23:59:59.000Z

466

Site Content and Metadata  

Science Journals Connector (OSTI)

Metadata is data about data, and is essentially the categorization of the content within a content management system. A good example of metadata is in the classification of documents in a Content Man...

Robert Garrett

2011-01-01T23:59:59.000Z

467

Molten iron oxysulfide as a superior sulfur sorbent. Final report, [September 1989--1993  

SciTech Connect (OSTI)

The studies had as original objective the analysis of conditions for using liquid iron oxysulfide as a desulfuring agent during coal gasification. Ancillary was a comparison of iron oxysulfide with lime as sorbents under conditions where lime reacts with S-bearing gases to form Ca sulfate or sulfide. Primary thrust is to determine the thermodynamic requirements for desulfurization by iron additions (e.g., taconite concentrate) during combustion in gasifiers operating at high equivalence ratios. Thermodynamic analysis of lime-oxygen-sulfur system shows why lime is injected into burners under oxidizing conditions; reducing conditions forms CaS, requiring its removal, otherwise oxidation and release of S would occur. Iron as the oxysulfide liquid has a range of stability and can be used as a desulfurizing agent, if the burner/gasifier operates in a sufficiently reducing regime (high equivalence ratio); this operating range is given and is calculable for a coal composition, temperature, stoichiometry. High moisture or hydrogen contents of the coal yield a poorer degree of desulfurization. Kinetic tests on individual iron oxide particles on substrates or Pt cups with a TGA apparatus fail to predict reaction rates within a burner. Preliminary tests on the Dynamic Containment Burner with acetylene give some promise that this system can produce the proper conditions of coal gasification for use of added iron as a sulfur sorbent.

Hepworth, M.T.

1993-03-31T23:59:59.000Z

468

Caloric content of phytoplankton  

Science Journals Connector (OSTI)

Jul 10, 1972 ... from carbon content, enabling much smaller ... surement of the energy efficiency of primary ... caloric content of the tissues of organisms.

1999-12-27T23:59:59.000Z

469

Maximum likelihood estimation of aggregated Markov processes  

Science Journals Connector (OSTI)

...calculated derivatives for the search of the likelihood surface...probabilities for the process to enter the states in class a...summation in the last term takes into account the...maximally efficient in terms of the information content...optimization method for search of the likelihood space...

1997-01-01T23:59:59.000Z

470

Design of maximum density aggregate grading  

Science Journals Connector (OSTI)

An aggregate grading that yields maximum solid density and maximum particle interlock is highly desirable for both bound mixtures, such as asphalt concrete and plain and reinforced concrete, and for unbound mixtures such as those used in base courses. Maximum particle interlock leads to high strength. Whereas minimum voids in a certain material composition is conducive to high strength and low compression. Aggregate grading may be obtained, for instance, from the ASTM, which is based on experience or may be designed according to Lees method. In the present work five different types of aggregates were used, each with a variety of chosen grading. It was found that Lees method produced the lowest porosity of all types of aggregates as well as for the various employed gradings. Lees rational method of aggregate grading, however, is a very lengthy and time-consuming procedure. Therefore, programming of Lees method is an essential step to make such an excellent method available to practicing engineers. A program named ratmix was developed and has incorporated 58 design graphs of the Lees method. ratmix is a comprehensive program for Lees rational method; it conducts interpolation for intermediate points within the design graphs as well as between graphs of different properties.

Yahia A Abdel-Jawad; Waddah Salman Abdullah

2002-01-01T23:59:59.000Z

471

ADDITIVE TESTING FOR IMPROVED SULFUR RETENTION: PRELIMINARY REPORT  

SciTech Connect (OSTI)

The Savannah River National Laboratory is collaborating with Alfred University to evaluate the potential for additives in borosilicate glass to improve sulfur retention. This preliminary report provides further background on the incorporation of sulfur in glass and outlines the experiments that are being performed by the collaborators. A simulated waste glass composition has been selected for the experimental studies. The first phase of experimental work will evaluate the impacts of BaO, PbO, and V{sub 2}O{sub 5} at concentrations of 1.0, 2.0, and 5.0 wt % on sulfate retention in simulated high level waste borosilicate glass. The second phase of experimental work will evaluate the effects of time at the melt temperature on sulfur retention. The resulting samples will be characterized to determine the amount of sulfur remaining as well as to identify the formation of any crystalline phases. The results will be used to guide the future selection of frits and glass forming chemicals in vitrifying Department of Energy wastes containing high sulfur concentrations.

Amoroso, J.; Fox, K.

2011-09-07T23:59:59.000Z

472

MHUG process for production of low sulfur and low aromatic diesel fuel. [Medium-pressure Hydro UpGrading  

SciTech Connect (OSTI)

A new hydro-upgrading process operated under medium pressure has been developed to reduce the sulfur and the aromatics content in light cycle oil (LCO). Two catalysts were used in series in this technology. The commercial RN-1 catalyst, which is known as having high activity in hydrodenitrogenation, desulfurization and aromatic saturation, was chosen as the first catalyst. The second one was a nickel-tungsten zeolite catalyst, named RT-5, which was developed by RIPP specially for hydrogenolysis of naphthenic and aromatic hydrocarbons. The pilot plant tests showed that high quality diesel oil with aromatics content less than 20 v% and sulfur content less than 0.05 wt% could be produced from various LCO/straight-run-gas-oil (SRGO) blended feedstocks under hydrogen partial pressure of 6.4 MPa. The reaction temperature and overall space velocity (S.V.) varied in the range of 350--380 C and 0.6--1.2 h[sup [minus]1], respectively, depending on the properties of the feedstocks to be processed and the upgrading depth required. Several examples presented also illustrated that this technology could be used to prepare catalytic reforming feedstock as well, which is in urgent need in China. A life test operated in relatively high severity for 3,000 hr. indicated that the catalysts possessed excellent stability. A commercial demonstration unit has been running well since the last Oct 1.

Shi, Yu Lin; Shi, Jian Wen; Zhang, Xin Wei; Shi, Ya Hua; Li, Da Dong (SINOPEC, Beijing (China). Research Inst. of Petroleum Processing)

1993-01-01T23:59:59.000Z

473

Full-scale tests of sulfur polymer cement and non-radioactive waste in heated and unheated prototypical containers  

SciTech Connect (OSTI)

Sulfur polymer cement has been demonstrated to be superior to portland cement in the stabilization of numerous troublesome low- level radioactive wastes, notably mixed waste fly ash, which contains heavy metals. EG G Idaho, Inc. conducted full-scale, waste-stabilization tests with a mixture of sulfur polymer cement and nonradioactive incinerator ash poured over simulated steel and ash wastes. The container used to contain the simulated waste for the pour was a thin-walled, rectangular, steel container with no appendages. The variable in the tests was that one container and its contents were at 65{degree}F (18{degree}C) at the beginning of the pour, while the other was preheated to 275{degree}F (135{degree}C) and was insulated before the pour. The primary goal was to determine the procedures and equipment deemed operationally acceptable and capable of providing the best probability of passing the only remaining governmental test for sulfur polymer cement, the Nuclear Regulatory Commission's full-scale test. The secondary goal was to analyze the ability of the molten cement and ash mixture to fill different size pipes and thus eliminate voids in the resultant 24 ft{sup 3} monolith.

Darnell, G.R.; Aldrich, W.C.; Logan, J.A.

1992-02-01T23:59:59.000Z

474

Full-scale tests of sulfur polymer cement and non-radioactive waste in heated and unheated prototypical containers  

SciTech Connect (OSTI)

Sulfur polymer cement has been demonstrated to be superior to portland cement in the stabilization of numerous troublesome low- level radioactive wastes, notably mixed waste fly ash, which contains heavy metals. EG&G Idaho, Inc. conducted full-scale, waste-stabilization tests with a mixture of sulfur polymer cement and nonradioactive incinerator ash poured over simulated steel and ash wastes. The container used to contain the simulated waste for the pour was a thin-walled, rectangular, steel container with no appendages. The variable in the tests was that one container and its contents were at 65{degree}F (18{degree}C) at the beginning of the pour, while the other was preheated to 275{degree}F (135{degree}C) and was insulated before the pour. The primary goal was to determine the procedures and equipment deemed operationally acceptable and capable of providing the best probability of passing the only remaining governmental test for sulfur polymer cement, the Nuclear Regulatory Commission`s full-scale test. The secondary goal was to analyze the ability of the molten cement and ash mixture to fill different size pipes and thus eliminate voids in the resultant 24 ft{sup 3} monolith.

Darnell, G.R.; Aldrich, W.C.; Logan, J.A.

1992-02-01T23:59:59.000Z

475

Removal of organic and inorganic sulfur from Ohio coal by combined physical and chemical process. Final report  

SciTech Connect (OSTI)

This project consisted of three sections. In the first part, the physical cleaning of Ohio coal by selective flocculation of ultrafine slurry was considered. In the second part, the mild oxidation process for removal of pyritic and organic sulfur.was investigated. Finally, in-the third part, the combined effects of these processes were studied. The physical cleaning and desulfurization of Ohio coal was achieved using selective flocculation of ultrafine coal slurry in conjunction with froth flotation as flocs separation method. The finely disseminated pyrite particles in Ohio coals, in particular Pittsburgh No.8 seam, make it necessary to use ultrafine ({minus}500 mesh) grinding to liberate the pyrite particles. Experiments were performed to identify the ``optimum`` operating conditions for selective flocculation process. The results indicated that the use of a totally hydrophobic flocculant (FR-7A) yielded the lowest levels of mineral matters and total sulfur contents. The use of a selective dispersant (PAAX) increased the rejection of pyritic sulfur further. In addition, different methods of floc separation techniques were tested. It was found that froth flotation system was the most efficient method for separation of small coal flocs.

Attia, Y.A.; Zeky, M.El.; Lei, W.W.; Bavarian, F.; Yu, S. [Ohio State Univ., Columbus, OH (United States). Dept. of Materials Science and Engineering

1989-04-28T23:59:59.000Z

476

Why sequence Sulfur cycling in the Frasassi aquifer?  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

sulfur cycling in the Frasassi aquifer? sulfur cycling in the Frasassi aquifer? The terrestrial subsurface remains one of the least explored microbial habitats on earth, and is critical for understanding pollutant migration and attenuation, subsurface processes such as limestone dissolution (affecting porosity), and the search for life elsewhere in the solar system and beyond. The deep and sulfidic Frasassi aquifer (of Ancona, Italy) has emerged as a model system for studying sulfur cycling in the terrestrial subsurface, and this sequencing project has relevance for developing applications for wastewater treatment and capabilities relevant for radionuclide, metal and organic pollutant remediation that can be applied at environments at DOE subsurface sites. Principal Investigators: Jennifer Macalady, Penn State University

477

Sodium/Phosphorus-Sulfur Cells II. Phase Equilibria  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

II. Phase Equilibria II. Phase Equilibria Title Sodium/Phosphorus-Sulfur Cells II. Phase Equilibria Publication Type Journal Article Year of Publication 1996 Authors Ridgway, Paul L., Frank R. McLarnon, and John S. Newman Journal Journal of the Electrochemistry Society Volume 143 Issue 2 Pagination 412-417 Keywords 25 ENERGY STORAGE, 36 MATERIALS SCIENCE, ALUMINIUM OXIDES, equilibrium, performance, PHASE DIAGRAMS, PHOSPHIDES, PHOSPHORUS ADDITIONS, SODIUM COMPOUNDS, SODIUM SULFIDES, SODIUM-SULFUR BATTERIES Abstract Equilibrium open-circuit cell voltage data from a sodium/{beta}{double_prime}-alumina/phosphorus-sulfur cell utilizing P/S ratios of 0, 0.143, and 0.332 and a sodium atom fraction ranging from 0 to 0.4 were interpreted to construct ternary phase diagrams of the Na-P-S ternary system at 350 and 400 C.

478

Historical Sulfur Dioxide Emissions 1850-2000: Methods and Results  

SciTech Connect (OSTI)

A global, self-consistent estimate of sulfur dioxide emissions over the last one and a half century were estimated by using a combination of bottom-up and best available inventory methods including all anthropogenic sources. We find that global sulfur dioxide emissions peaked about 1980 and have generally declined since this time. Emissions were extrapolated to a 1{sup o} x 1{sup o} grid for the time period 1850-2000 at annual resolution with two emission height levels and by season. Emissions are somewhat higher in the recent past in this new work as compared with some comprehensive estimates. This difference is largely due to our use of emissions factors that vary with time to account for sulfur removals from fossil fuels and industrial smelting processes.

Smith, Steven J.; Andres, Robert; Conception , Elvira; Lurz, Joshua

2004-01-25T23:59:59.000Z

479

Indication of Meissner Effect in Sulfur-Substituted Strontium Ruthenates  

E-Print Network [OSTI]

Ceramic samples of Sr2RuO(4-y)Sy (y=0.03-1.2) with intended isovalent substitution of oxygen by sulfur have been synthesized and explored in the temperature range 4-300K. It is found that at a range of optimum sulfur substitution the magnetic response of ceramic samples reveals large diamagnetic signal with amplitudes approaching comparability with that of the YBCO-superconductors. Contrary to a pure ceramic Sr2RuO4, if properly optimized, the resistivity of sulfur-substituted samples has a metallic behavior except at lower temperatures where an upturn occurs. Both synthesis conditions and results of measurements are reported. The Meissner effect may point to high-temperature superconductivity.

Gulian, Armen

2011-01-01T23:59:59.000Z

480

HYBRID SULFUR ELECTROLYZER DEVELOPMENT FY09 SECOND QUARTER REPORT  

SciTech Connect (OSTI)

The primary objective of the DOE-NE Nuclear Hydrogen Initiative (NHI) is to develop the nuclear hydrogen production technologies necessary to produce hydrogen at a cost competitive with other alternative transportation fuels. The focus of the NHI is on thermochemical cycles and high temperature electrolysis that can be powered by heat from high temperature gas reactors. The Savannah River National Laboratory (SRNL) has been tasked with the primary responsibility to perform research and development in order to characterize, evaluate and develop the Hybrid Sulfur (HyS) thermochemical process. This report documents work during the first quarter of Fiscal Year 2009, for the period between January 1, 2009 and March 31, 2009. The HyS Process is a two-step hybrid thermochemical cycle that is part of the 'Sulfur Family' of cycles. As a sulfur cycle, it uses high temperature thermal decomposition of sulfuric acid to produce oxygen and to regenerate the sulfur dioxide reactant. The second step of the process uses a sulfur dioxide depolarized electrolyzer (SDE) to split water and produce hydrogen by electrochemically reacting sulfur dioxide with H{sub 2}O. The SDE produces sulfuric acid, which is then sent to the acid decomposer to complete the cycle. The DOE NHI program is developing the acid decomposer at Sandia National Laboratory for application to both the HyS Process and the Sulfur Iodine Cycle. The SDE is being developed at SRNL. During FY05 and FY06, SRNL designed and conducted proof-of-concept testing for a SDE using a low temperature, PEM fuel cell-type design concept. The advantages of this design concept include high electrochemical efficiency, small footprint and potential for low capital cost, characteristics that are crucial for successful implementation on a commercial scale. During FY07, SRNL extended the range of testing of the SDE to higher temperature and pressure, conducted a 100-hour longevity test with a 60-cm{sup 2} single cell electrolyzer, and designed and built a larger, multi-cell stack electrolyzer. During FY08, SRNL continued SDE development, including development and successful testing of a three-cell electrolyzer stack with a rated capacity of 100 liters per hour. The HyS program for FY09 program will address improving SDE performance by focusing on preventing or minimizing sulfur deposition inside the cell caused by SO{sub 2} crossover, reduction of cell voltage for improved efficiency, an extension of cell operating lifetime. During FY09 a baseline technology development program is being conducted to address each of these issues. Button-cell (2-cm{sup 2}) and single cell (60-cm{sup 2}) SDEs will be fabricated and tested. A pressurized button-cell test facility will be designed and constructed to facilitate addition testing. The single cell test facility will be upgraded for unattended operation, and later for operation at higher temperature and pressure. Work will continue on development of the Gas Diffusion Electrode (GDE), or Gap Cell, as an alternative electrolyzer design approach that is being developed under subcontract with industry partner Giner Electrochemical Systems. If successful, it could provide an alternative means of preventing sulfur crossover through the proton exchange membrane, as well as the possibility for higher current density operation based on more rapid mass transfer in a gas-phase anode. Promising cell components will be assembled into membrane electrode assemblies (MEAs) and tested in the single cell test facility. Upon modification for unattended operation, test will be conducted for 200 hours or more. Both the button-cell and modified single cell facility will be utilized to demonstrate electrolyzer operation without sulfur build-up limitations, which is a Level 1 Milestone.

Herman, D; David Hobbs, D; Hector Colon-Mercado, H; Timothy Steeper, T; John Steimke, J; Mark Elvington, M

2009-04-15T23:59:59.000Z

Note: This page contains sample records for the topic "maximum sulfur content" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


481

Selective catalytic reduction of sulfur dioxide to elemental sulfur. Quarterly technical progress report No. 6, October--December 1993  

SciTech Connect (OSTI)

Elemental sulfur recovery from SO{sub 2}-containing gas stream is highly attractive as it produces a salable product and no waste to dispose of. However, commercially available schemes are complex and involve multi-stage reactors, such as, most notably in the Resox (reduction of SO{sub 2} with coke) and Claus plant (reaction of SO{sub 2} with H{sub 2}S over catalyst). This project will investigate a cerium oxide catalyst for the single stage selective reduction of SO{sub 2} to elemental sulfur by a reductant, such as carbon monoxide. Cerium oxide has been identified in recent work at MIT as a superior catalyst for SO{sub 2} reduction by CO to elemental sulfur because its high activity and high selectivity to sulfur over COS over a wide temperature range (400--650{degree}C). The detailed kinetic and parametric studies of SO{sub 2} reduction planned in this work over various CeO{sub 2} formulations will provide the necessary basis for development of a very simplified process, namely that of a single-stage elemental sulfur recovery scheme from variable concentration gas streams. The potential cost- and energy-efficiency benefits from this approach can not be overstated. A first apparent application is treatment of a regenerator off-gases in power plants using regenerative flue gas desulfurization. Such a simple catalytic converter may offer the long-sought ``Claus-alternative`` for coal-fired power plant applications.

Liu, W.; Flytzani-Stephanopoulos, M.; Sarofim, A.F.

1993-12-31T23:59:59.000Z

482

Selective catalytic reduction of sulfur dioxide to elemental sulfur. Quarterly technical progress report No. 4, April--June 1993  

SciTech Connect (OSTI)

Elemental sulfur recovery from SO{sub 2}-containing gas stream is highly attractive as it produces a salable product and no waste to dispose of. However, commercially available schemes are complex and involve multi-stage reactors, such as, most notably in the Resox (reduction of SO{sub 2} with coke) and Claus plant(reaction of SO{sub 2} with H{sub 2}S over catalyst). This project will investigate a cerium oxide catalyst for the single stage selective reduction of SO{sub 2} to elemental sulfur by a reductant, such as carbon monoxide. Cerium oxide has been identified in recent work at MIT as a superior catalyst for SO{sub 2} reduction by CO to elemental sulfur because its high activity and high selectivity to sulfur over COS over a wide temperature range(400--650{degrees}C). The detailed kinetic and parametric studies of SO{sub 2} reduction planned in this work over various CeO{sub 2}-formulations will provide the necessary basis for development of a very simplified process, namely that of a single-stage elemental sulfur recovery scheme from variable concentration gas streams, The potential cost- and energy-efficiency benefits from this approach can not be overstated. A first apparent application is treatment of a regenerator off-gases in power plants using regenerative flue gas desulfurization. Such a simple catalytic converter may offer the long-sought ``Claus-alternative`` for coal-fired power plant applications.

Liu, Wei; Flytzani-Stephanopoulos, M.; Sarofim, A.F.; Williams, R.S.

1993-12-31T23:59:59.000Z

483

Advanced byproduct recovery: Direct catalytic reduction of sulfur dioxide to elemental sulfur. Fourth quarterly technical progress report  

SciTech Connect (OSTI)

The team of Arthur D. Little, Tufts University and Engelhard Corporation are conducting Phase 1 of a four and a half year, two-phase effort to develop and scale-up an advanced byproduct recovery technology that is a direct, single-stage, catalytic process for converting sulfur dioxide to elemental sulfur. This catalytic process reduces SO{sub 2} over a fluorite-type oxide (such as ceria and zirconia). The catalytic activity can be significantly promoted by active transition metals, such as copper. More than 95% elemental sulfur yield, corresponding to almost complete sulfur dioxide conversion, was obtained over a Cu-Ce-O oxide catalyst as part of an on-going DOE-sponsored, University Coal Research Program. This type of mixed metal oxide catalyst has stable activity, high selectivity for sulfur production, and is resistant to water and carbon dioxide poisoning. Tests with CO and CH{sub 4} reducing gases indicate that the catalyst has the potential for flexibility with regard to the composition of the reducing gas, making it attractive for utility use. The performance of the catalyst is consistently good over a range of SO{sub 2} inlet concentration (0.1 to 10%) indicating its flexibility in treating SO{sub 2} tail gases as well as high concentration streams.

NONE

1997-01-01T23:59:59.000Z

484

Content is not King  

E-Print Network [OSTI]

The Internet is widely regarded as primarily a content delivery system. Yet historically, connectivity

Odlyzko, Andrew

2000-01-01T23:59:59.000Z

485

Direct sulfur recovery during sorbent regeneration. Final report  

SciTech Connect (OSTI)

The objective of this research project was to improve the direct elemental sulfur yields that occur during the regeneration of SO{sub 2}-saturated MgO-vermiculite sorbents (MagSorbents) by examining three approaches or strategies. The three approaches were regeneration-gas recycle, high-pressure regeneration, and catalytic reduction of the SO{sub 2} gas using a new catalyst developed by Research Triangle Institute (RTI). Prior to the project, Sorbent Technologies Corporation (Sorbtech) had developed a sorbent-regeneration process that yielded directly a pure elemental sulfur product. In the process, typically about 25 to 35 percent of the liberated S0{sub 2} was converted directly to elemental sulfur. The goal of this project was to achieve a conversion rate of over 90 percent. Good success was attained in the project. About 90 percent or more conversion was achieved with two of the approaches that were examined, regeneration-gas recycle and use of the RTI catalyst. Of these approaches, regeneration-gas recycle gave the best results (essentially 100 percent conversion in some cases). In the regeneration-gas recycle approach, saturated sorbent is simply heated to about 750{degree}C in a reducing gas (methane) atmosphere. During heating, a gas containing elemental sulfur, water vapor, H{sub 2}S, S0{sub 2}, and C0{sub 2} is evolved. The elemental sulfur and water vapor in the gas stream are condensed and removed, and the remaining gas is recycled back through the sorbent bed. After several recycles, the S0{sub 2} and H{sub 2}S completely disappear from the gas stream, and the stream contains only elemental sulfur, water vapor and C0{sub 2}.

Nelson, S.G.; Little, R.C. [Sorbent Technologies Corp., Twinsburg, OH (United States)

1993-08-01T23:59:59.000Z

486

Accelerated maximum likelihood parameter estimation for stochastic biochemical systems  

E-Print Network [OSTI]

as: Daigle et al. : Accelerated maximum likelihood parame-Gillespie DT: Approximate accelerated stochastic simulationARTICLE Open Access Accelerated maximum likelihood parameter

Daigle, Bernie J; Roh, Min K; Petzold, Linda R; Niemi, Jarad

2012-01-01T23:59:59.000Z

487

The Hybrid Maximum Principle is a consequence of Pontryagin ...  

E-Print Network [OSTI]

We give a simple proof of the Maximum Principle for smooth hybrid control sys- ... result in the study of such problems is Hybrid Maximum Principle proved in [4]...

2006-10-31T23:59:59.000Z

488

Extraction, separation, and analysis of high sulfur coal. Final report  

SciTech Connect (OSTI)

The work described in this report studies the removal of sulfur by oxidative interaction of various cupric salts with coal and also considers the possibility of removing organic sulfur by the selective interaction of supercritical ethanol with the organic coal matrix. Either one of these methods could potentially be used to pretreat coals before burning. The primary purpose of these studies is to ascertain the nature of the chemical reactions occurring, the chemical composition of the resultant products, and information on possible reaction mechanisms. This information should allow prediction of reasonable reaction conditions for the removal of organosulfur compound from coal.

Olesik, S.V.; Pekay, L.A.; Larkins, W. Jr. [comps.

1992-05-31T23:59:59.000Z

489

Extraction, separation, and analysis of high sulfur coal  

SciTech Connect (OSTI)

The work described in this report studies the removal of sulfur by oxidative interaction of various cupric salts with coal and also considers the possibility of removing organic sulfur by the selective interaction of supercritical ethanol with the organic coal matrix. Either one of these methods could potentially be used to pretreat coals before burning. The primary purpose of these studies is to ascertain the nature of the chemical reactions occurring, the chemical composition of the resultant products, and information on possible reaction mechanisms. This information should allow prediction of reasonable reaction conditions for the removal of organosulfur compound from coal.

Olesik, S.V.; Pekay, L.A.; Larkins, W. Jr. (comps.)

1992-05-31T23:59:59.000Z

490

HYBRID SULFUR RECOVERY PROCESS FOR NATURAL GAS UPGRADING  

SciTech Connect (OSTI)

This second quarter report of 2002 describes progress on a project funded by the U.S. Department of Energy (DOE) to test a hybrid sulfur recovery process for natural gas upgrading. The process concept represents a low cost option for direct treatment of natural gas streams to remove H{sub 2}S in quantities equivalent to 0.2-25 metric tons (LT) of sulfur per day. This process is projected to have lower capital and operating costs than the competing technologies, amine/aqueous iron liquid redox and amine/Claus/tail gas treating, and have a smaller plant footprint, making it well suited to both on-shore and offshore applications. CrystaSulf (service mark of CrystaTech, Inc.) is a new nonaqueous sulfur recovery process that removes hydrogen sulfide (H{sub 2}S) from gas streams and converts it into elemental sulfur. CrystaSulf features high sulfur recovery similar to aqueous-iron liquid redox sulfur recovery processes, but differs from the aqueous processes in that CrystaSulf controls the location where elemental sulfur particles are formed. In the hybrid process, approximately 1/3 of the total H{sub 2}S in the natural gas is first oxidized to SO{sub 2} at low temperatures over a heterogeneous catalyst. Low temperature oxidation is done so that the H{sub 2}S can be oxidized in the presence of methane and other hydrocarbons without oxidation of the hydrocarbons. The project involves the development of a catalyst using laboratory/bench-scale catalyst testing, and then demonstration of the catalyst at CrystaTech's pilot plant in west Texas. Previous reports described development of a catalyst with the required selectivity and efficiency for producing sulfur dioxide from H{sub 2}S. In the laboratory, the catalyst was shown to be robust and stable in the presence of several intentionally added contaminants, including condensate from the pilot plant site. This report describes testing using the laboratory apparatus but operated at the pilot plant using the actual pilot plant gas, which contains far more contaminants than can be simulated in the laboratory. The results are very encouraging, with stable and efficient operation being obtained for a prolonged period of time.

Girish Srinivas; Steven C. Gebhard; David W. DeBerry

2002-07-01T23:59:59.000Z

491

Alternative Fuels Data Center: Tier 2 Vehicle and Gasoline Sulfur Program  

Alternative Fuels and Advanced Vehicles Data Center [Office of Energy Efficiency and Renewable Energy (EERE)]

Tier 2 Vehicle and Tier 2 Vehicle and Gasoline Sulfur Program to someone by E-mail Share Alternative Fuels Data Center: Tier 2 Vehicle and Gasoline Sulfur Program on Facebook Tweet about Alternative Fuels Data Center: Tier 2 Vehicle and Gasoline Sulfur Program on Twitter Bookmark Alternative Fuels Data Center: Tier 2 Vehicle and Gasoline Sulfur Program on Google Bookmark Alternative Fuels Data Center: Tier 2 Vehicle and Gasoline Sulfur Program on Delicious Rank Alternative Fuels Data Center: Tier 2 Vehicle and Gasoline Sulfur Program on Digg Find More places to share Alternative Fuels Data Center: Tier 2 Vehicle and Gasoline Sulfur Program on AddThis.com... More in this section... Federal State Advanced Search All Laws & Incentives Sorted by Type Tier 2 Vehicle and Gasoline Sulfur Program

492

Sulfur Effect and Performance Recovery of a DOC + CSF + Cu-Zeolite...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

Sulfur Effect and Performance Recovery of a DOC + CSF + Cu-Zeolite SCR System Sulfur Effect and Performance Recovery of a DOC + CSF + Cu-Zeolite SCR System effect and performance...

493

Revisit Carbon/Sulfur Composite for Li-S Batteries. | EMSL  

Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

Revisit CarbonSulfur Composite for Li-S Batteries. Revisit CarbonSulfur Composite for Li-S Batteries. Abstract: To correlate the carbon properties e.g. surface area and porous...

494

A design strategy applied to sulfur resistant lean NOx̳ automotive catalysts  

E-Print Network [OSTI]

Catalyst poisoning due to sulfur compounds derived from fuel sulfur presents a major challenge, intractable thus far, to development of many advanced technologies for automotive catalysts such as the lean NOx, trap. Under ...

Tang, Hairong

2005-01-01T23:59:59.000Z

495

Ultra-Low Sulfur diesel Update & Future Light Duty Diesel | Department...  

Broader source: Energy.gov (indexed) [DOE]

Ultra-Low Sulfur diesel Update & Future Light Duty Diesel Ultra-Low Sulfur diesel Update & Future Light Duty Diesel Presentation given at DEER 2006, August 20-24, 2006, Detroit,...

496

Sulfur Degassing From Volcanoes: Source Conditions, Surveillance, Plume Chemistry and Earth System Impacts  

E-Print Network [OSTI]

of sulfur in magmas owes much to its multiple valence states (-II, 0, IV, VI), speciation (e.g., S2, H2S, SO on the redox chemistry of sulfur: by reducing sulfur, thiosulfate, sulfite and sulfate to H2S, or oxidizing sulfur and H2S to sulfate (e.g., Takano et al. 1997; Amend and Shock 2001; Shock et al. 2010

Boyer, Edmond

497

Sulfur-deactivated steam reforming of gasified biomass  

SciTech Connect (OSTI)

The effect of hydrogen sulfide on the stream reforming of methane has been studied. Methane is the most difficult component to convert by steam reforming in the mixture of hydrocarbons, which is produced in biomass gasification. Two catalysts were subjected to hydrogen sulfide levels up to 300 ppm so as to study the effect of sulfur on their deactivation. These catalysts were the C11-9-061, from United Catalyst Inc., and the HTSR1, from Haldor Topsoee. The activation energy of the sulfur-deactivated steam-reforming reaction was calculated to be 280 and 260 kJ/mol, for each catalyst, respectively. The high values most probably originate from the fact that the degree of sulfur coverage of the nickel surface is close to 1 for these experiments. Even under these severe conditions, steam reforming of methane is possible without any carbon formation. The HTSR1 catalyst exhibits a very high sulfur-free activity, resulting in a performance in the presence of hydrogen sulfide higher than that for the C11-9-061 catalyst. By using the HTSR1 catalyst, the reactor temperature can be lowered by 60 C in order to reach comparable levels of conversion.

Koningen, J.; Sjoestroem, K. [Kungl Tekniska Hoegskolan, Stockholm (Sweden)] [Kungl Tekniska Hoegskolan, Stockholm (Sweden)

1998-02-01T23:59:59.000Z

498

Effect of sulfur on heavy duty diesel engine lubricants  

SciTech Connect (OSTI)

Diesel engine exhaust legislation has become quite onerous for heavy duty engines. Yet, these high thermal efficiency engines continue to meet lower exhaust particulate and NOx emissions limits, due to new engine designs and the complementary engine oil performance requirements of the API service categories. In addition, the EPA has mandated changes in on-highway diesel fuel to help meet particulate emissions regulations. On October 1, 1993, when the EPA outlawed high sulfur fuels for on-highway use, the development of the API CG-4 engine oil performance specification was already in progress. All the new diesel engine tests in the category were therefore designed to run with low (< 0.05% wt.) sulfur fuel. In some engine tests, this new fuel improved some lubricant performance characteristics and degraded others. An engine oil specification for low sulfur fuel brings new challenges to developing future specifications for diesel engine oils. Both higher and lower lubricant additive treat rate products, high performance single grade oils, and formulations to meet world-wide specifications become viable. This paper discusses the results of a diesel engine oil technology that performs well with the new, low sulfur fuel in both engine tests and in the field.

Hayden, T.E. [Texaco Fuels and Lubricants Research Dept., Beacon, NY (United States)

1996-12-01T23:59:59.000Z

499

Revisit Carbon/Sulfur Composite for Li-S Batteries  

SciTech Connect (OSTI)

To correlate the carbon properties e.g. surface area and porous structure, with the electrochemical behaviors of carbon/sulfur (C/S) composite cathodes for lithium-sulfur (Li-S) batteries, four different carbon frameworks including Ketjen Black (KB, high surface area and porous), Graphene (high surface area and nonporous), Acetylene Black (AB, low surface area and nonporous) and Hollow Carbon Nano Sphere (HCNS, low surface area and porous) are employed to immobilize sulfur (80 wt.%). It has been revealed that high surface area of carbon improves the utilization rate of active sulfur and decreases the real current density during the electrochemical reactions. Accordingly, increased reversible capacities and reduced polarization are observed for high surface area carbon hosts such as KB/S and graphene/S composites. The porous structure of KB or HCNS matrix promotes the long-term cycling stability of C/S composites but only at relatively low rate (0.2 C). Once the current density increases, the pore effect completely disappears and all Li-S batteries show similar trend of capacity degradation regardless of the different carbon hosts used in the cathodes. The reason has been assigned to the formation of reduced amount of irreversible Li2S on the cathode as well as shortened time for polysulfides to transport towards lithium anode at elevated current densities. This work provides valuable information for predictive selection on carbon materials to construct C/S composite for practical applications from the electrochemical point of view.

Zheng, Jianming; Gu, Meng; Wagner, Michael J.; Hays, Kevin; Li, Xiaohong S.; Zuo, Pengjian; Wang, Chong M.; Zhang, Jiguang; Liu, Jun; Xiao, Jie

2013-07-23T23:59:59.000Z

500

Workshop on sulfur chemistry in flue gas desulfurization  

SciTech Connect (OSTI)

The Flue Gas Desulfurization Workshop was held at Morgantown, West Virginia, June 7-8, 1979. The presentations dealt with the chemistry of sulfur and calcium compounds in scrubbers. DOE and EPRI programs in this area are described. Ten papers have been entered individually into EDB and ERA. (LTN)

Wallace, W.E. Jr.

1980-05-01T23:59:59.000Z