National Library of Energy BETA

Sample records for distillate pro pane

  1. Multi-pane glass unit having seal with adhesive and hermetic coating layer

    DOE Patents [OSTI]

    Miller, Seth A; Stark, David H; Francis, IV, William H; Puligandla, Viswanadham; Boulos, Edward N; Pernicka, John

    2015-02-10

    A vacuum insulated glass unit (VIGU) comprises a first pane of a transparent material and a second pane of a transparent material. The second pane is spaced apart from the first pane to define a cavity therebetween. At least one of a spacer and an array of stand-off members is disposed between the first and second panes to maintain separation therebetween. A first adhesive layer forms at least a portion of a gas-tight connection between the first pane and the second pane. A highly hermetic coating is disposed over the adhesive layer, where the coating is an inorganic layer.

  2. Filament-strung stand-off elements for maintaining pane separation in vacuum insulating glazing units

    DOE Patents [OSTI]

    Bettger, Kenneth J; Stark, David H

    2013-08-20

    A vacuum insulating glazing unit (VIGU) comprises first and second panes of transparent material, first and second anchors, a plurality of filaments, a plurality of stand-off elements, and seals. The first and second panes of transparent material have edges and inner and outer faces, are disposed with their inner faces substantially opposing one another, and are separated by a gap having a predetermined height. The first and second anchors are disposed at opposite edges of one pane of the VIGU. Each filament is attached at one end to the first anchor and at the other end to the second anchor, and the filaments are collectively disposed between the panes substantially parallel to one another. The stand-off elements are affixed to each filament at predetermined positions along the filament, and have a height substantially equal to the predetermined height of the gap such that the each stand-off element touches the inner surfaces of both panes. The seals are disposed about the edges of the panes, enclosing the stand-off elements within a volume between the panes from which the atmosphere may be evacuated to form a partial vacuum.

  3. Catalytic distillation structure

    DOE Patents [OSTI]

    Smith, Jr., Lawrence A.

    1984-01-01

    Catalytic distillation structure for use in reaction distillation columns, a providing reaction sites and distillation structure and consisting of a catalyst component and a resilient component intimately associated therewith. The resilient component has at least about 70 volume % open space and being present with the catalyst component in an amount such that the catalytic distillation structure consist of at least 10 volume % open space.

  4. Catalytic distillation structure

    DOE Patents [OSTI]

    Smith, L.A. Jr.

    1984-04-17

    Catalytic distillation structure is described for use in reaction distillation columns, and provides reaction sites and distillation structure consisting of a catalyst component and a resilient component intimately associated therewith. The resilient component has at least about 70 volume % open space and is present with the catalyst component in an amount such that the catalytic distillation structure consists of at least 10 volume % open space. 10 figs.

  5. Catalytic distillation process

    DOE Patents [OSTI]

    Smith, Jr., Lawrence A. (Bellaire, TX)

    1982-01-01

    A method for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contacting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C.sub.4 feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.

  6. Catalytic distillation process

    DOE Patents [OSTI]

    Smith, L.A. Jr.

    1982-06-22

    A method is described for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contacting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C[sub 4] feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.

  7. Advanced Distillation Final Report

    SciTech Connect (OSTI)

    Maddalena Fanelli; Ravi Arora; Annalee Tonkovich; Jennifer Marco; Ed Rode

    2010-03-24

    The Advanced Distillation project was concluded on December 31, 2009. This U.S. Department of Energy (DOE) funded project was completed successfully and within budget during a timeline approved by DOE project managers, which included a one year extension to the initial ending date. The subject technology, Microchannel Process Technology (MPT) distillation, was expected to provide both capital and operating cost savings compared to conventional distillation technology. With efforts from Velocys and its project partners, MPT distillation was successfully demonstrated at a laboratory scale and its energy savings potential was calculated. While many objectives established at the beginning of the project were met, the project was only partially successful. At the conclusion, it appears that MPT distillation is not a good fit for the targeted separation of ethane and ethylene in large-scale ethylene production facilities, as greater advantages were seen for smaller scale distillations. Early in the project, work involved flowsheet analyses to discern the economic viability of ethane-ethylene MPT distillation and develop strategies for maximizing its impact on the economics of the process. This study confirmed that through modification to standard operating processes, MPT can enable net energy savings in excess of 20%. This advantage was used by ABB Lumus to determine the potential impact of MPT distillation on the ethane-ethylene market. The study indicated that a substantial market exists if the energy saving could be realized and if installed capital cost of MPT distillation was on par or less than conventional technology. Unfortunately, it was determined that the large number of MPT distillation units needed to perform ethane-ethylene separation for world-scale ethylene facilities, makes the targeted separation a poor fit for the technology in this application at the current state of manufacturing costs. Over the course of the project, distillation experiments were

  8. Distillation Column Flooding Predictor

    SciTech Connect (OSTI)

    2002-02-01

    This factsheet describes a research project whose goal is to develop the flooding predictor, an advanced process control strategy, into a universally useable tool that will maximize the separation yield of a distillation column.

  9. DISTILLATION OF CALCIUM

    DOE Patents [OSTI]

    Barton, J.

    1954-07-27

    This invention relates to an improvement in the process for the purification of caicium or magnesium containing an alkali metal as impurity, which comprises distiiling a batch of the mixture in two stages, the first stage distillation being carried out in the presence of an inert gas at an absolute pressure substantially greater than the vapor pressure of calcium or maguesium at the temperature of distillation, but less than the vaper pressure at that temperature of the alkali metal impurity so that only the alkali metal is vaporized and condensed on a condensing surface. A second stage distilso that substantially only the calcium or magnesium distills under its own vapor pressure only and condenses in solid form on a lower condensing surface.

  10. Genie Pro

    Energy Science and Technology Software Center (OSTI)

    2004-05-15

    Genie Pro is a general purpose, interactive, adaptive tool for automatically labeling regions and finding objects in large amounts of image data. Genie Pro uses supervised learning techniques to search for spatio-spectral algorithms that are best able to match exaple labels provided by a user during a training session. After Genie Pro has discovered a useful algorithm, this algorith can then be applied to other similar types of image data, to label regions and objectsmore » similar to those provided during the training session. Genie Pro was originally developed for analyzing multispectral satellite data, but it works equally well with panchromatic (grayscale) and hyperspectral satellite data, aerial imagery, and various kinds of medical imagery. AS a rough guideline, Genie Pro can work with any imagery where the scene being imaged is all approximately at a constant distance fromt he imaging device, and so the scale of imagery is fixed. Applications for Genie Pro include: Crop and terrain type mapping, Road and river network mapping, Broad area search for vehicles and buildings, and Cancer identification in histological images.« less

  11. Word Pro - S12

    Gasoline and Diesel Fuel Update

    ... fuels. d Distillate fuel oil, excluding biodiesel. e Liquefied petroleum gases. f Finished ... fuels. c Distillate fuel oil, excluding biodiesel. d Liquefied petroleum gases. e ...

  12. Word Pro - A

    Gasoline and Diesel Fuel Update

    ... renewable diesel fuel (including biodiesel) blended into distillate fuel oil. d ... renewable diesel fuel (including biodiesel) blended into distillate fuel oil. g ...

  13. Distillate Fuel Oil Sales for Residential Use

    U.S. Energy Information Administration (EIA) (indexed site)

    End Use/ Product: Residential - Distillate Fuel Oil Residential - No. 1 Residential - No. 2 Residential - Kerosene Commercial - Distillate Fuel Oil Commercial - No. 1 Distillate Commercial - No. 2 Distillate Commercial - No. 2 Fuel Oil Commercial - Ultra Low Sulfur Diesel Commercial - Low Sulfur Diesel Commercial - High Sulfur Diesel Commercial - No. 4 Fuel Oil Commercial - Residual Fuel Oil Commercial - Kerosene Industrial - Distillate Fuel Oil Industrial - No. 1 Distillate Industrial - No. 2

  14. Distributive Distillation Enabled by Microchannel Process Technology...

    Office of Scientific and Technical Information (OSTI)

    distillation for new plants. A design concept for a modular microchannel distillation unit was developed in Task 3. In Task 4, Ultrasonic Additive Machining (UAM) was evaluated...

  15. American Distillation Inc | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Distillation Inc Jump to: navigation, search Name: American Distillation Inc. Place: Leland, North Carolina Zip: 28451 Product: Biodiesel producer in North Carolina. References:...

  16. Distillation process using microchannel technology

    DOE Patents [OSTI]

    Tonkovich, Anna Lee; Simmons, Wayne W.; Silva, Laura J.; Qiu, Dongming; Perry, Steven T.; Yuschak, Thomas; Hickey, Thomas P.; Arora, Ravi; Smith, Amanda; Litt, Robert Dwayne; Neagle, Paul

    2009-11-03

    The disclosed invention relates to a distillation process for separating two or more components having different volatilities from a liquid mixture containing the components. The process employs microchannel technology for effecting the distillation and is particularly suitable for conducting difficult separations, such as the separation of ethane from ethylene, wherein the individual components are characterized by having volatilities that are very close to one another.

  17. Distillation Column Flooding Predictor

    SciTech Connect (OSTI)

    George E. Dzyacky

    2010-11-23

    The Flooding Predictor™ is a patented advanced control technology proven in research at the Separations Research Program, University of Texas at Austin, to increase distillation column throughput by over 6%, while also increasing energy efficiency by 10%. The research was conducted under a U. S. Department of Energy Cooperative Agreement awarded to George Dzyacky of 2ndpoint, LLC. The Flooding Predictor™ works by detecting the incipient flood point and controlling the column closer to its actual hydraulic limit than historical practices have allowed. Further, the technology uses existing column instrumentation, meaning no additional refining infrastructure is required. Refiners often push distillation columns to maximize throughput, improve separation, or simply to achieve day-to-day optimization. Attempting to achieve such operating objectives is a tricky undertaking that can result in flooding. Operators and advanced control strategies alike rely on the conventional use of delta-pressure instrumentation to approximate the column’s approach to flood. But column delta-pressure is more an inference of the column’s approach to flood than it is an actual measurement of it. As a consequence, delta pressure limits are established conservatively in order to operate in a regime where the column is never expected to flood. As a result, there is much “left on the table” when operating in such a regime, i.e. the capacity difference between controlling the column to an upper delta-pressure limit and controlling it to the actual hydraulic limit. The Flooding Predictor™, an innovative pattern recognition technology, controls columns at their actual hydraulic limit, which research shows leads to a throughput increase of over 6%. Controlling closer to the hydraulic limit also permits operation in a sweet spot of increased energy-efficiency. In this region of increased column loading, the Flooding Predictor is able to exploit the benefits of higher liquid

  18. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

    Table A3. Approximate Heat Content of Petroleum Consumption and Fuel Ethanol (Million Btu ... renewable diesel fuel (including biodiesel) blended into distillate fuel oil. d ...

  19. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    ... renewable diesel fuel (including biodiesel) blended into distillate fuel oil. c ... Notes: * Petroleum products supplied is an approximation of petroleum consumption and is ...

  20. Word Pro - S12

    Gasoline and Diesel Fuel Update

    ... fuels. c Distillate fuel oil, excluding biodiesel. d Liquefied petroleum gases. e Finished ... products. g Emissions from energy consumption (for electricity and a small amount of ...

  1. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    ... renewable diesel fuel (including biodiesel) blended into distillate fuel oil. c ... * For total heat content of petroleum consumption by all sectors, see data for heat ...

  2. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    ... renewable diesel fuel (including biodiesel) blended into distillate fuel oil. c ... Notes: * Transportation sector data are estimates. * For total petroleum consumption by ...

  3. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    Crude Oil a Distillate Fuel Oil f Jet Fuel g LPG b Motor Gasoline i Residual Fuel Oil ... finished motor gasoline and motor gasoline blending components; excludes oxygenates. ...

  4. Word Pro - S3

    Gasoline and Diesel Fuel Update

    ... Beginning in 2009, also includes renewable diesel fuel (including biodiesel). g Beginning in 2009, includes renewable diesel fuel (including biodiesel) blended into distillate fuel ...

  5. Word Pro - S12

    U.S. Energy Information Administration (EIA) (indexed site)

    ... Natural gas, excluding supplemental gaseous fuels. c Distillate fuel oil, excluding biodiesel. d Liquefied petroleum gases. e Emissions from energy consumption (for electricity ...

  6. Word Pro - S3

    Annual Energy Outlook

    Includes fuel ethanol blended into motor gasoline. d Includes renewable diesel fuel (including biodiesel) blended into distillate fuel oil. e Includes kerosene-type jet fuel only. ...

  7. Word Pro - S12

    Gasoline and Diesel Fuel Update

    ... 1244. b Natural gas, excluding supplemental gaseous fuels. c Distillate fuel oil, excluding biodiesel. d Municipal solid waste from non-biogenic sources, and tire-derived fuels. ...

  8. Word Pro - Glossary

    Gasoline and Diesel Fuel Update

    ... content of emulsions (exclusive of water), and petroleum distillates blended with ... the temperature of 1 pound of liquid water by 1 degree Fahrenheit at the temperature ...

  9. Adjusted Distillate Fuel Oil Sales for Residential Use

    U.S. Energy Information Administration (EIA) (indexed site)

    End Use Product: Residential - Distillate Fuel Oil Residential - No. 1 Residential - No. 2 Residential - Kerosene Commercial - Distillate Fuel Oil Commercial - No. 1 Distillate ...

  10. Corrosion inhibition for distillation apparatus

    DOE Patents [OSTI]

    Baumert, Kenneth L.; Sagues, Alberto A.; Davis, Burtron H.; Schweighardt, Frank K.

    1985-01-01

    Tower material corrosion in an atmospheric or sub-atmospheric distillation tower in a coal liquefaction process is reduced or eliminated by subjecting chloride-containing tray contents to an appropriate ion-exchange resin to remove chloride from such tray contents materials.

  11. Distributive Distillation Enabled by Microchannel Process Technology

    Office of Scientific and Technical Information (OSTI)

    (Technical Report) | SciTech Connect Distributive Distillation Enabled by Microchannel Process Technology Citation Details In-Document Search Title: Distributive Distillation Enabled by Microchannel Process Technology The application of microchannel technology for distributive distillation was studied to achieve the Grand Challenge goals of 25% energy savings and 10% return on investment. In Task 1, a detailed study was conducted and two distillation systems were identified that would meet

  12. ITP Chemicals: Hybripd Separations/Distillation Technology. Research...

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Hybripd SeparationsDistillation Technology. Research Opportunities for Energy and Emissions Reduction ITP Chemicals: Hybripd SeparationsDistillation Technology. Research ...

  13. ITP Chemicals: Hybrid Separations/Distillation Technology. Research...

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Hybrid SeparationsDistillation Technology. Research Opportunities for Energy and Emissions Reduction ITP Chemicals: Hybrid SeparationsDistillation Technology. Research ...

  14. Word Pro - S12

    U.S. Energy Information Administration (EIA) (indexed site)

    ... fuels. d Distillate fuel oil, excluding biodiesel. e Liquefied petroleum gases. f Finished ... See Table 12.6. i Excludes emissions from biomass energy consumption. See Table 12.7. ...

  15. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    Crude Oil d NGPL e Other Liquids f Total Distillate Fuel Oil g Jet Fuel h LPG c Motor ... Beginning in 1981, also includes aviation and motor gasoline blending components (net). ...

  16. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    Asphalt Aviation Distillate Jet Kerosene Liquefied Lubricants Motor Petroleum Residual Other 0.0 0.6 1.2 1.8 Quadrillion Btu a Includes renewable diesel fuel (including biodiesel) ...

  17. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    Energy Review 2011 Jet Fuel 1 Distillate fuel oil and residual fuel oil. 2 Includes ethanol blended into motor gasoline. Note: U.S. Government's fiscal year was October 1...

  18. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 3.7a Petroleum Consumption: Residential and Commercial Sectors (Thousand Barrels per Day) Residential Sector Commercial Sector a Distillate Fuel Oil Kero- sene Liquefied Petroleum Gases Total Distillate Fuel Oil Kero- sene Liquefied Petroleum Gases Motor Gasoline b Petro- leum Coke Residual Fuel Oil Total 1950 Average .................... 390 168 104 662 123 23 28 52 NA 185 411 1955 Average .................... 562 179 144 885 177 24 38 69 NA 209 519 1960 Average .................... 736

  19. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    0 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 3.8a Heat Content of Petroleum Consumption: Residential and Commercial Sectors (Trillion Btu) Residential Sector Commercial Sector a Distillate Fuel Oil Kerosene Liquefied Petroleum Gases Total Distillate Fuel Oil Kerosene Liquefied Petroleum Gases Motor Gasoline b Petroleum Coke Residual Fuel Oil Total 1950 Total ........................ 829 347 146 1,322 262 47 39 100 NA 424 872 1955 Total

  20. Distributive Distillation Enabled by Microchannel Process Technology

    SciTech Connect (OSTI)

    Arora, Ravi

    2013-01-22

    The application of microchannel technology for distributive distillation was studied to achieve the Grand Challenge goals of 25% energy savings and 10% return on investment. In Task 1, a detailed study was conducted and two distillation systems were identified that would meet the Grand Challenge goals if the microchannel distillation technology was used. Material and heat balance calculations were performed to develop process flow sheet designs for the two distillation systems in Task 2. The process designs were focused on two methods of integrating the microchannel technology 1) Integrating microchannel distillation to an existing conventional column, 2) Microchannel distillation for new plants. A design concept for a modular microchannel distillation unit was developed in Task 3. In Task 4, Ultrasonic Additive Machining (UAM) was evaluated as a manufacturing method for microchannel distillation units. However, it was found that a significant development work would be required to develop process parameters to use UAM for commercial distillation manufacturing. Two alternate manufacturing methods were explored. Both manufacturing approaches were experimentally tested to confirm their validity. The conceptual design of the microchannel distillation unit (Task 3) was combined with the manufacturing methods developed in Task 4 and flowsheet designs in Task 2 to estimate the cost of the microchannel distillation unit and this was compared to a conventional distillation column. The best results were for a methanol-water separation unit for the use in a biodiesel facility. For this application microchannel distillation was found to be more cost effective than conventional system and capable of meeting the DOE Grand Challenge performance requirements.

  1. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    5 Fuel Oil and Kerosene Sales, 1984-2010 Total by Fuel Distillate Fuel Oil by Selected End Use Residual Fuel Oil by Major End Use Kerosene by Major End Use 154 U.S. Energy Information Administration / Annual Energy Review 2011 Source: Table 5.15. On-Highway Diesel Commercial Railroad 1985 1990 1995 2000 2005 2010 0 1 2 3 4 5 Million Barrels per Day Residential Distillate Fuel Oil 1985 1990 1995 2000 2005 2010 0.0 0.5 1.0 1.5 2.0 2.5 3.0 Million Barrels per Day Kerosene Residual Fuel Oil Vessel

  2. Word Pro - Untitled1

    Gasoline and Diesel Fuel Update

    Index 1949100 0.186 0.073 0.043 0.008 Wood Fuel Ethanol Waste Biodiesel 0.00 0.05 0.10 ... fuels. 5 Distillate fuel oil, excluding biodiesel. 6 Liquefied petroleum gases. 7 Finished ...

  3. AL PRO | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    search Name: AL-PRO Place: Grossheide, Lower Saxony, Germany Zip: 26532 Sector: Wind energy Product: AL-PRO is an inndependent expert office for wind forecasts, wind...

  4. HyPRO Model

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    HyPRO Model (Strategic Analysis, Inc.) Objectives Provide a modeling tool to develop an understanding of how the hydrogen production infrastructure might evolve in the United States and determine the factors that will drive infrastructure development. Key Attributes & Strengths HyPRO provides a transparent enumeration of production, delivery and dispensing costs for comparison of different options. It also provides a graphical projection of production, delivery and dispensing infrastructure

  5. ProMat

    Energy Science and Technology Software Center (OSTI)

    2008-06-12

    ProMAT is a software tool for statistically analyzing data from enzyme-linked immunosorbent assay microarray experiments. The software estimates standard curves, sample protein concentrations and their uncertainties for multiple assays. ProMAT generates a set of comprehensive figures for assessing results and diagnosing process quality. The tool is available for Windows or Mac, and is distributed as open-source Java and R code

  6. The Influence of Molecular Structure of Distillate Fuels on HFRR...

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    The Influence of Molecular Structure of Distillate Fuels on HFRR Lubricity The Influence of Molecular Structure of Distillate Fuels on HFRR Lubricity Presentation given at 2007 ...

  7. New Design Methods and Algorithms for Multi-component Distillation...

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Design Methods and Algorithms for Multi-component Distillation Processes New Design Methods and Algorithms for Multi-component Distillation Processes multicomponent.pdf (517.32 KB) ...

  8. Distillation: Still towering over other options

    SciTech Connect (OSTI)

    Kunesh, J.G.; Kister, H.Z.; Lockett, M.J.; Fair, J.R.

    1995-10-01

    Distillation dominates separations in the chemical process industries (CPI), at least for mixtures that normally are processed as liquids. The authors fully expect that distillation will continue to be the method of choice for many separations, and the method against which other options must be compared. So, in this article, they will put into some perspective just why distillation continues to reign as the king of separations, and what steps are being taken to improve its applicability and performance, as well as basic understanding of the technique.

  9. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    6 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 3.7b Petroleum Consumption: Industrial Sector (Thousand Barrels per Day) Industrial Sector a Asphalt and Road Oil Distillate Fuel Oil Kerosene Liquefied Petroleum Gases Lubricants Motor Gasoline b Petroleum Coke Residual Fuel Oil Other c Total 1950 Average .................... 180 328 132 100 43 131 41 617 250 1,822 1955 Average .................... 254 466 116 212 47 173 67 686 366 2,387 1960 Average

  10. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    47 Table 2.2 Manufacturing Energy Consumption for All Purposes, 2006 (Trillion Btu ) NAICS 1 Code Manufacturing Group Coal Coal Coke and Breeze 2 Natural Gas Distillate Fuel Oil LPG 3 and NGL 4 Residual Fuel Oil Net Electricity 5 Other 6 Shipments of Energy Sources 7 Total 8 311 Food ................................................................................. 147 1 638 16 3 26 251 105 (s) 1,186 312 Beverage and Tobacco Products ..................................... 20 0 41 1 1 3 30 11 -0

  11. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    49 Table 2.3 Manufacturing Energy Consumption for Heat, Power, and Electricity Generation by End Use, 2006 End-Use Category Net Electricity 1 Residual Fuel Oil Distillate Fuel Oil LPG 2 and NGL 3 Natural Gas Coal 4 Total 5 Million Kilowatthours Million Barrels Billion Cubic Feet Million Short Tons Indirect End Use (Boiler Fuel) ......................................... 12,109 21 4 2 2,059 25 - - Conventional Boiler Use ............................................. 12,109 11 3 2 1,245 6 - - CHP 6

  12. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    Household Energy Consumption Household Energy Consumpton by Census Region, Selected Years, 1978-2009¹ Household Energy Consumption by Source, 2009 Energy Consumption per Household, Selected Years, 1978-2009¹ Energy Consumption per Household, by Census Region, 2009 50 U.S. Energy Information Administration / Annual Energy Review 2011 1 For years not shown, there are no data available. 2 Liquefied petroleum gases. Notes: * Data include natural gas, electricity, distillate fuel oil, kerosene,

  13. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    0 Commercial Buildings Energy Consumption and Expenditure Indicators, Selected Years, 1979-2003 Buildings by Energy Source Used Consumption Consumption per Square Foot Square Footage per Building by Expenditures Expenditures Per Square Foot Energy Source Used 62 U.S. Energy Information Administration / Annual Energy Review 2011 1 Electricity only; excludes electrical system energy losses. 2 Distillate fuel oil, residual fuel oil, and kerosene. 3 Prices are not adjusted for inflation. See

  14. Minimizing corrosion in coal liquid distillation

    DOE Patents [OSTI]

    Baumert, Kenneth L.; Sagues, Alberto A.; Davis, Burtron H.

    1985-01-01

    In an atmospheric distillation tower of a coal liquefaction process, tower materials corrosion is reduced or eliminated by introduction of boiling point differentiated streams to boiling point differentiated tower regions.

  15. Word Pro - S12

    U.S. Energy Information Administration (EIA) (indexed site)

    4 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 12.5 Carbon Dioxide Emissions From Energy Consumption: Transportation Sector (Million Metric Tons of Carbon Dioxide a ) Coal Natural Gas b Petroleum Retail Elec- tricity f Total g Aviation Gasoline Distillate Fuel Oil c Jet Fuel LPG d Lubri- cants Motor Gasoline e Residual Fuel Oil Total 1973 Total ........................ (s) 39 6 163 152 3 6 886 57 1,273 2 1,315 1975 Total ........................ (s) 32 5 155

  16. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 3.6 Heat Content of Petroleum Products Supplied by Type (Trillion Btu) Asphalt and Road Oil Aviation Gasoline Distillate Fuel Oil b Jet Fuel c Kero- sene LPG a Lubri- cants Motor Gasoline e Petro- leum Coke Residual Fuel Oil Other f Total Propane d Total 1950 Total ...................... 435 199 2,300 c ( ) 668 NA 343 236 5,015 90 3,482 546 13,315 1955 Total ...................... 615 354 3,385 301 662 NA 592 258 6,640 147 3,502 798 17,255 1960 Total ...................... 734 298 3,992

  17. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 3.8b Heat Content of Petroleum Consumption: Industrial Sector (Trillion Btu) Industrial Sector a Asphalt and Road Oil Distillate Fuel Oil Kerosene Liquefied Petroleum Gases Lubricants Motor Gasoline b Petroleum Coke Residual Fuel Oil Other c Total 1950 Total ........................ 435 698 274 156 94 251 90 1,416 546 3,960 1955 Total ........................ 615 991 241 323 103 332 147 1,573 798 5,123 1960 Total ........................ 734 1,016 161 507 107 381 328 1,584 947 5,766 1965

  18. Word Pro - S3

    U.S. Energy Information Administration (EIA) (indexed site)

    U.S. Energy Information Administration / Monthly Energy Review October 2016 55 Table 3.3b Petroleum Trade: Imports and Exports by Type (Thousand Barrels per Day) Imports Exports Crude Oil a Distillate Fuel Oil Jet Fuel d LPG b Motor Gasoline f Residual Fuel Oil Other g Total Crude Oil a Petroleum Products Total SPR c Total Propane e Total 1950 Average ................ - - 487 7 d ( ) - - (s) 329 27 850 95 210 305 1955 Average ................ - - 782 12 d ( ) - - 13 417 24 1,248 32 336 368 1960

  19. Word Pro - S7

    U.S. Energy Information Administration (EIA) (indexed site)

    4 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 7.3b Consumption of Combustible Fuels for Electricity Generation: Electric Power Sector (Subset of Table 7.3a) Coal a Petroleum Natural Gas f Other Gases g Biomass Other j Distillate Fuel Oil b Residual Fuel Oil c Other Liquids d Petroleum Coke e Total e Wood h Waste i Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels Billion Cubic Feet Trillion Btu 1950 Total .................... 91,871

  20. Word Pro - S7

    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 7.4a Consumption of Combustible Fuels for Electricity Generation and Useful Thermal Output: Total (All Sectors) (Sum of Tables 7.4b and 7.4c) Coal a Petroleum Natural Gas f Other Gases g Biomass Other j Distillate Fuel Oil b Residual Fuel Oil c Other Liquids d Petroleum Coke e Total e Wood h Waste i Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels Billion Cubic Feet Trillion Btu 1950 Total .................... 91,871 5,423 69,998 NA NA 75,421 629 NA 5 NA NA 1955

  1. Word Pro - S7

    U.S. Energy Information Administration (EIA) (indexed site)

    8 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 7.4b Consumption of Combustible Fuels for Electricity Generation and Useful Thermal Output: Electric Power Sector (Subset of Table 7.4a) Coal a Petroleum Natural Gas f Other Gases g Biomass Other j Distillate Fuel Oil b Residual Fuel Oil c Other Liquids d Petroleum Coke e Total e Wood h Waste i Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels Billion Cubic Feet Trillion Btu 1950 Total

  2. Word Pro - S7

    U.S. Energy Information Administration (EIA) (indexed site)

    21 Table 7.5 Stocks of Coal and Petroleum: Electric Power Sector Coal a Petroleum Distillate Fuel Oil b Residual Fuel Oil c Other Liquids d Petroleum Coke e Total e,f Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels 1950 Year ............................. 31,842 NA NA NA NA 10,201 1955 Year ............................. 41,391 NA NA NA NA 13,671 1960 Year ............................. 51,735 NA NA NA NA 19,572 1965 Year ............................. 54,525 NA NA NA NA

  3. Word Pro - S7

    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 7.3a Consumption of Combustible Fuels for Electricity Generation: Total (All Sectors) (Sum of Tables 7.3b and 7.3c) Coal a Petroleum Natural Gas f Other Gases g Biomass Other j Distillate Fuel Oil b Residual Fuel Oil c Other Liquids d Petroleum Coke e Total e Wood h Waste i Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels Billion Cubic Feet Trillion Btu 1950 Total .................... 91,871 5,423 69,998 NA NA 75,421 629 NA 5 NA NA 1955 Total ....................

  4. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 11.1 Carbon Dioxide Emissions From Energy Consumption by Source, Selected Years, 1949-2011 (Million Metric Tons of Carbon Dioxide 1 ) Year Coal 3 Natural Gas 4 Petroleum Total 2,9 Biomass 2 Aviation Gasoline Distillate Fuel Oil 5 Jet Fuel Kero- sene LPG 6 Lubri- cants Motor Gasoline 7 Petroleum Coke Residual Fuel Oil Other 8 Total Wood 10 Waste 11 Fuel Ethanol 12 Bio- diesel Total 1949 1,118 270 12 140 NA 42 13 7 329 8 244 25 820 2,207 145 NA NA NA 145 1950 1,152 313 14 168 NA 48 16 9

  5. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 11.2a Carbon Dioxide Emissions From Energy Consumption: Residential Sector, Selected Years, 1949-2011 (Million Metric Tons of Carbon Dioxide 1 ) Year Coal Natural Gas 3 Petroleum Retail Electricity 5 Total 2 Biomass 2 Distillate Fuel Oil 4 Kerosene Liquefied Petroleum Gases Total Wood 6 Total 6 1949 121 55 51 21 7 80 66 321 99 99 1950 120 66 61 25 9 95 69 350 94 94 1955 83 117 87 27 13 127 110 436 73 73 1960 56 170 115 26 19 160 156 542 59 59 1965 34 214 125 24 24 174 223 644 44 44 1970

  6. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    6 U.S. Energy Information Administration / Annual Energy Review 2011 Table 11.2b Carbon Dioxide Emissions From Energy Consumption: Commercial Sector, Selected Years, 1949-2011 (Million Metric Tons of Carbon Dioxide 1 ) Year Coal Natural Gas 3 Petroleum Retail Electricity 7 Total 2 Biomass 2 Distillate Fuel Oil 4 Kerosene LPG 5 Motor Gasoline 6 Petroleum Coke Residual Fuel Oil Total Wood 8 Waste 9 Fuel Ethanol 10 Total 1949 148 19 16 3 2 7 NA 28 55 58 280 2 NA NA 2 1950 147 21 19 3 2 7 NA 33 66

  7. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 11.2c Carbon Dioxide Emissions From Energy Consumption: Industrial Sector, Selected Years, 1949-2011 (Million Metric Tons of Carbon Dioxide 1 ) Year Coal Coal Coke Net Imports Natural Gas 3 Petroleum Retail Elec- tricity 8 Total 2 Biomass 2 Distillate Fuel Oil 4 Kero- sene LPG 5 Lubri- cants Motor Gasoline 6 Petroleum Coke Residual Fuel Oil Other 7 Total Wood 9 Waste 10 Fuel Ethanol 11 Total 1949 500 -1 166 41 18 3 3 16 8 95 25 209 120 995 44 NA NA 44 1950 531 (s) 184 51 20 4 3 18 8 110

  8. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    8 U.S. Energy Information Administration / Annual Energy Review 2011 Table 11.2d Carbon Dioxide Emissions From Energy Consumption: Transportation Sector, Selected Years, 1949-2011 (Million Metric Tons of Carbon Dioxide 1 ) Year Coal Natural Gas 3 Petroleum Retail Elec- tricity 7 Total 2 Biomass 2 Aviation Gasoline Distillate Fuel Oil 4 Jet Fuel LPG 5 Lubricants Motor Gasoline 6 Residual Fuel Oil Total Fuel Ethanol 8 Biodiesel Total 1949 161 NA 12 30 NA (s) 4 306 91 443 6 611 NA NA NA 1950 146 7

  9. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    9 Table 11.2e Carbon Dioxide Emissions From Energy Consumption: Electric Power Sector, Selected Years, 1949-2011 (Million Metric Tons of Carbon Dioxide 1 ) Year Coal Natural Gas 3 Petroleum Geo- thermal Non- Biomass Waste 5 Total 2 Biomass 2 Distillate Fuel Oil 4 Petroleum Coke Residual Fuel Oil Total Wood 6 Waste 7 Total 1949 187 30 2 NA 30 33 NA NA 250 1 NA 1 1950 206 35 2 NA 35 37 NA NA 278 1 NA 1 1955 324 63 2 NA 35 37 NA NA 424 (s) NA (s) 1960 396 95 2 NA 42 43 NA NA 535 (s) NA (s) 1965 546

  10. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    3 U.S. Government Energy Consumption by Agency and Source, Fiscal Years 2003, 2010, and 2011 By Agency By Source 28 U.S. Energy Information Administration / Annual Energy Review 2011 1 Includes small amount of renewable energy; see Table 1.13, footnote 8. 2 Natural gas, plus a small amount of supplemental gaseous fuels. 3 Chilled water, renewable energy, and other fuels reported as used in facilities. 4 Distillate fuel oil and residual fuel oil. 5 Includes ethanol blended into motor gasoline. 6

  11. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    5 Non-Combustion Use of Fossil Fuels Total, 1980-2011 As Share of Total Energy Consumption, 1980-2011 By Fuel, 2011 By Petroleum Product, 2011 32 U.S. Energy Information Administration / Annual Energy Review 2011 1 Liquefied petroleum gases and pentanes plus are aggregated to avoid disclosure of proprie- tary information. 2 Distillate fuel oil, residual fuel oil, waxes, and miscellaneous products. (s)=Less than 0.05 quadrillion Btu. Note: See Note 2, "Non-Combustion Use of Fossil

  12. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    7 Type of Heating in Occupied Housing Units, 1950 and 2009 By Fuel Type By Fuel Type, Share of Total 56 U.S. Energy Information Administration / Annual Energy Review 2011 1 Sum of components do not equal total due to independent rounding. 2 Liquefied petroleum gases. 3 Includes coal coke. 4 Kerosene, solar, and other. (s)=Less than 0.5. Source: Table 2.7. 57 38 8 6 2 (s) 1 11 (s) 9 1 4 14 2 Natural Gas Electricity Distillate Fuel Oil LPG² Wood Coal³ Other and None 0 20 40 60 Million Occupied

  13. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    9 Commercial Buildings Consumption by Energy Source By Survey Year, 1979-2003 By Census Region, 2003 60 U.S. Energy Information Administration / Annual Energy Review 2011 1 Electricity only; excludes electrical system energy losses. 2 Distillate fuel oil, residual fuel oil, and kerosene. (s)=Less than 0.05 quadrillion Btu. Q=Data withheld because either the relative standard error was greater than 50 percent or fewer than 20 buildings were sampled. Note: See Appendix C for map of Census regions.

  14. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    9 Refinery Capacity and Utilization, 1949-2011 Number of Operable Refineries Utilization Capacity 136 U.S. Energy Information Administration / Annual Energy Review 2011 ¹ Operable refineries capacity on January 1. Source: Table 5.9. 1950 1960 1970 1980 1990 2000 2010 0 100 200 300 400 Total Units 1950 1960 1970 1980 1990 2000 2010 0 20 40 60 80 100 Percent 1955 1965 1975 1985 1995 2005 0 5 10 15 20 Million Barrels per Day Capacity¹ Unused Capacity Gross Input to Distillation Units

  15. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    2 Refiner Sales Prices for Selected Petroleum Products, 1995-2011 To Resellers To End Users 168 U.S. Energy Information Administration / Annual Energy Review 2011 1 Prices are not adjusted for inflation. See "Nominal Dollars" in Glossary. Source: Table 5.22. Residual Fuel Oil 1996 1998 2000 2002 2004 2006 2008 2010 0.00 0.50 1.00 1.50 2.00 2.50 3.00 3.50 Dollars¹ per Gallon, Excluding Taxes Motor Gasoline Residual Fuel Oil Motor Gasoline No. 2 Distillate Propane 1996 1998 2000 2002

  16. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    3 All Sellers Sales Prices for Selected Petroleum Products, 2010 Motor Gasoline, Selected Grades Distillate Fuel Oil, Residual Fuel Oil, and Propane 170 U.S. Energy Information Administration / Annual Energy Review 2011 1 Prices are not adjusted for inflation. See "Nominal Dollars" in Glossary. 2 Includes oxygenated motor gasoline. 3 > 15 and <= 500 parts per million. 4 > 500 parts per million. - - = Not applicable. Note: Data are preliminary. Source: Table 5.23. 2.32 2.29

  17. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    0 U.S. Energy Information Administration / Annual Energy Review 2011 Table 8.5c Consumption of Combustible Fuels for Electricity Generation: Electric Power Sector by Plant Type, Selected Years, 1989-2011 (Breakout of Table 8.5b) Year Coal 1 Petroleum Natural Gas 6 Other Gases 7 Biomass Other 10 Distillate Fuel Oil 2 Residual Fuel Oil 3 Other Liquids 4 Petroleum Coke 5 Total 5 Wood 8 Waste 9 Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels Million Cubic Feet Trillion Btu

  18. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 8.6a Estimated Consumption of Combustible Fuels for Useful Thermal Output at Combined-Heat-and-Power Plants: Total (All Sectors), 1989-2011 (Sum of Tables 8.6b and 8.6c) Year Coal 1 Petroleum Natural Gas 6 Other Gases 7 Biomass Other 10 Distillate Fuel Oil 2 Residual Fuel Oil 3 Other Liquids 4 Petroleum Coke 5 Total 5 Wood 8 Waste 9 Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels Million Cubic Feet Trillion Btu Trillion Btu Trillion Btu 1989 16,510 1,410 16,357

  19. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    4 U.S. Energy Information Administration / Annual Energy Review 2011 Table 8.6b Estimated Consumption of Combustible Fuels for Useful Thermal Output at Combined-Heat-and-Power Plants: Electric Power Sector, 1989-2011 (Subset of Table 8.6a) Year Coal 1 Petroleum Natural Gas 6 Other Gases 7 Biomass Other 10 Distillate Fuel Oil 2 Residual Fuel Oil 3 Other Liquids 4 Petroleum Coke 5 Total 5 Wood 8 Waste 9 Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels Million Cubic Feet

  20. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    45 Table 8.6c Estimated Consumption of Combustible Fuels for Useful Thermal Output at Combined-Heat-and-Power Plants: Commercial and Industrial Sectors, Selected Years, 1989-2011 (Subset of Table 8.6a) Year Coal 1 Petroleum Natural Gas 6 Other Gases 7 Biomass Other 10 Distillate Fuel Oil 2 Residual Fuel Oil 3 Other Liquids 4 Petroleum Coke 5 Total 5 Wood 8 Waste 9 Thousand Short Tons Thousand Barrels Thousand Short Tons Thousand Barrels Million Cubic Feet Trillion Btu Trillion Btu Trillion Btu

  1. Energy Pro USA | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Pro USA Jump to: navigation, search Name: Energy Pro USA Place: Chesterfield, Missouri Zip: MO 63017 Product: Energy Pro funds and implements demand side energy savings programs to...

  2. Classic papers in Solar Energy: Solar distillation

    SciTech Connect (OSTI)

    Howe, E.D.

    1990-06-01

    The following Classic Paper was presented by Professor Howe at the first international Conference on Solar Energy at Tucson, Arizona, USA in 1955. That conference was sponsored by the Association of Applied solar Energy (AFASE), the precursor of ISES. Although this paper does not represent the many developments in solar distillation later applied by Professor Howe in the South Pacific, it is a classic paper because it presents Professor Howe's pioneering work in setting up the Seawater Conversion Laboratory in Richmond for the University of California at Berkeley, US. The research of Professor Howe and his colleagues at the Seawater Conversion Laboratory formed the foundation of contemporary solar energy desalination and distillation systems.

  3. Word Pro - S9

    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 9.9 Cost of Fossil-Fuel Receipts at Electric Generating Plants (Dollars a per Million Btu, Including Taxes) Coal Petroleum Natural Gas e All Fossil Fuels f Residual Fuel Oil b Distillate Fuel Oil c Petroleum Coke Total d 1973 Average .................... 0.41 0.79 NA NA 0.80 0.34 0.48 1975 Average .................... .81 2.01 NA NA 2.02 .75 1.04 1980 Average .................... 1.35 4.27 NA NA 4.35 2.20 1.93 1985 Average .................... 1.65 4.24 NA NA 4.32 3.44 2.09 1990 Average

  4. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 2.7 Type of Heating in Occupied Housing Units, Selected Years, 1950-2009 Year Coal 1 Distillate Fuel Oil Kerosene Liquefied Petroleum Gases Natural Gas Electricity Wood Solar Other 2 None 3 Total Million Occupied Housing Units 1950 14.48 9.46 4 ( ) 0.98 11.12 0.28 4.17 NA 0.77 1.57 42.83 1960 6.46 17.16 4 ( ) 2.69 22.85 .93 2.24 NA .22 .48 53.02 1970 1.82 16.47 4 ( ) 3.81 35.01 4.88 .79 NA .27 .40 63.45 1973 .80 17.24 4 ( ) 4.42 38.46 7.21 .60 NA .15 .45 69.34 1975 .57 16.30 4 ( ) 4.15

  5. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 3.5 Consumer Expenditure Estimates for Energy by Source, 1970-2010 (Million Dollars 1 ) Year Primary Energy 2 Electric Power Sector 11,12 Retail Electricity 13 Total Energy 10,14 Coal Coal Coke Net Imports 3 Natural Gas 4 Petroleum Nuclear Fuel Biomass 9 Total 10 Distillate Fuel Oil Jet Fuel 5 LPG 6 Motor Gasoline 7 Residual Fuel Oil Other 8 Total 1970 4,630 -75 10,891 6,253 1,441 2,395 31,596 2,046 4,172 47,904 44 438 63,872 -4,357 23,345 82,860 1971 4,902 -40 12,065 6,890 1,582 2,483

  6. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 3.3 Consumer Price Estimates for Energy by Source, 1970-2010 (Dollars 1 per Million Btu) Year Primary Energy 2 Electric Power Sector 11,12 Retail Electricity 13 Total Energy 9,10,14 Coal Natural Gas 3 Petroleum Nuclear Fuel Biomass 8 Total 9,10 Distillate Fuel Oil Jet Fuel 4 LPG 5 Motor Gasoline 6 Residual Fuel Oil Other 7 Total 1970 0.38 0.59 1.16 0.73 1.43 2.85 0.42 1.38 1.71 0.18 1.29 1.08 0.32 4.98 1.65 1971 .42 .63 1.22 .77 1.46 2.90 .58 1.45 1.78 .18 1.31 1.15 .38 5.30 1.76 1972

  7. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 5.9 Refinery Capacity and Utilization, Selected Years, 1949-2011 Year Operable Refineries 1 Operable Refineries Capacity Gross Input to Distillation Units 3 Utilization 4 On January 1 Annual Average 2 Number Thousand Barrels per Calendar Day Thousand Barrels per Day Percent 1949 336 6,231 NA 5,556 89.2 1950 320 6,223 NA 5,980 92.5 1955 296 8,386 NA 7,820 92.2 1960 309 9,843 NA 8,439 85.1 1965 293 10,420 NA 9,557 91.8 1970 276 12,021 NA 11,517 92.6 1975 279 14,961 NA 12,902 85.5 1976 276

  8. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 5.15 Fuel Oil and Kerosene Sales, Selected Years, 1984-2010 (Thousand Barrels per Day) Year Distillate Fuel Oil Residential Commercial Industrial Oil Company Farm Electric Power 1 Railroad Vessel Bunkering On-Highway Diesel Military Off-Highway Diesel Other Total 1984 534 360 166 55 208 42 192 115 1,093 46 114 46 2,971 1985 504 291 159 45 202 34 182 111 1,127 43 99 11 2,809 1990 475 260 169 49 222 50 203 135 1,393 46 118 (s) 3,120 1991 442 246 151 48 206 39 188 133 1,336 53 107 (s) 2,949

  9. Table 10.24 Reasons that Made Distillate Fuel Oil Unswitchable...

    Annual Energy Outlook

    4 Reasons that Made Distillate Fuel Oil Unswitchable, 2006; Level: National Data; Row: ... Combinations of NAICS Distillate Fuel Oil Unswitchable Distillate Capable of ...

  10. Conceptual design and optimization for JET water detritiation system cryo-distillation facility

    SciTech Connect (OSTI)

    Lefebvre, X.; Hollingsworth, A.; Parracho, A.; Dalgliesh, P.; Butler, B.; Smith, R.

    2015-03-15

    The aim of the Exhaust Detritiation System (EDS) of the JET Active Gas Handling System (AGHS) is to convert all Q-based species (Q{sub 2}, Q-hydrocarbons) into Q{sub 2}O (Q being indifferently H, D or T) which is then trapped on molecular sieve beds (MSB). Regenerating the saturated MSBs leads to the production of tritiated water which is stored in Briggs drums. An alternative disposal solution to offsite shipping, is to process the tritiated water onsite via the implementation of a Water Detritiation System (WDS) based, in part, on the combination of an electrolyser and a cryo-distillation (CD) facility. The CD system will separate a Q{sub 2} mixture into a de-tritiated hydrogen stream for safe release and a tritiated stream for further processing on existing AGHS subsystems. A sensitivity study of the Souers' model using the simulation program ProSimPlus (edited by ProSim S.A.) has then been undertaken in order to perform an optimised dimensioning of the cryo-distillation system in terms of available cooling technologies, cost of investment, cost of operations, process performance and safety. (authors)

  11. Contact structure for use in catalytic distillation

    DOE Patents [OSTI]

    Jones, E.M. Jr.

    1985-08-20

    A method and apparatus are disclosed for conducting catalytic chemical reactions and fractionation of the reaction mixture, comprising and feeding reactants into a distillation column reactor contracting said reactant in a liquid phase with a fixed bed catalyst in the form of a contact catalyst structure, consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column. 7 figs.

  12. Contact structure for use in catalytic distillation

    DOE Patents [OSTI]

    Jones, Jr., Edward M.

    1984-01-01

    A method for conducting catalytic chemical reactions and fractionation of the reaction mixture comprising feeding reactants into a distillation column reactor contracting said reactant in liquid phase with a fixed bed catalyst in the form of a contact catalyst structure consisting of closed porous containers containing the catatlyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column.

  13. Contact structure for use in catalytic distillation

    DOE Patents [OSTI]

    Jones, Jr., Edward M.

    1985-01-01

    A method and apparatus for conducting catalytic chemical reactions and fractionation of the reaction mixture, comprising and feeding reactants into a distillation column reactor contracting said reactant in a liquid phase with a fixed bed catalyst in the form of a contact catalyst structure, consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column.

  14. Contact structure for use in catalytic distillation

    DOE Patents [OSTI]

    Jones, E.M. Jr.

    1984-03-27

    A method is described for conducting catalytic chemical reactions and fractionation of the reaction mixture comprising feeding reactants into a distillation column reactor, contracting said reactant in liquid phase with a fixed bed catalyst in the form of a contact catalyst structure consisting of closed porous containers containing the catalyst for the reaction and a clip means to hold and support said containers, which are disposed above, i.e., on the distillation trays in the tower. The trays have weir means to provide a liquid level on the trays to substantially cover the containers. In other words, the trays function in their ordinary manner with the addition thereto of the catalyst. The reaction mixture is concurrently fractionated in the column. 7 figs.

  15. Catalytic hydroprocessing of petroleum and distillates

    SciTech Connect (OSTI)

    Oballa, M.C.; Shih, S.S.

    1994-12-31

    There is a strong push for the processing of heavy oils, bitumen and/or residue, which carries with it some problems. These are connected with obtaining state-of-the-art technologies at reasonable capital and operating costs to the refiner. Then there are problems associated with choosing the best catalyst--one specially designed to lower considerably the high content of heteroatoms (S, N, O) and metals (V, Ni, Fe). To address the above considerations, engineers and scientists working in the processing of petroleum and distillates from different parts of the world presented papers covering different facets of residue upgrading and distillate hydrotreating. This book is a compilation of most of the papers presented in the five sessions of the symposium. The editors have broadly classified the papers in terms of content into the following four categories: catalyst deactivation; upgrading of heavy oils and residue; hydrotreating of distillates; and general papers. All papers have been processed separately for inclusion on the data base.

  16. Crude oil steam distillation in steam flooding. Final report

    SciTech Connect (OSTI)

    Wu, C.H.; Elder, R.B.

    1980-08-01

    Steam distillation yields of sixteen crude oils from various parts of the United States have been determined at a saturated steam pressure of 200 psig. Study made to investigate the effect of steam pressure (200 to 500 psig) on steam distillation yields indicates that the maximum yields of a crude oil may be obtained at 200 psig. At a steam distillation correlation factor (V/sub w//V/sub oi/) of 15, the determined steam distillation yields range from 12 to 56% of initial oil volume for the sixteen crude oils with gravity ranging from 12 to 40/sup 0/API. Regression analysis of experimental steam distillation yields shows that the boiling temperature (simulated distillation temperature) at 20% simulated distillation yield can predict the steam distillation yields reasonably well: the standard error ranges from 2.8 to 3.5% (in yield) for V/sub w//V/sub oi/ < 5 and from 3.5 to 4.5% for V/sub w//V/sub oi/ > 5. The oil viscosity (cs) at 100/sup 0/F can predict the steam distillation yields with standard error from 3.1 to 4.3%. The API gravity can predict the steam distillation yields with standard error from 4.4 to 5.7%. Characterization factor is an unsatisfactory correlation independent variable for correlation purpose.

  17. Apparatus for distilling shale oil from oil shale

    SciTech Connect (OSTI)

    Shishido, T.; Sato, Y.

    1984-02-14

    An apparatus for distilling shale oil from oil shale comprises: a vertical type distilling furnace which is divided by two vertical partitions each provided with a plurality of vent apertures into an oil shale treating chamber and two gas chambers, said oil shale treating chamber being located between said two gas chambers in said vertical type distilling furnace, said vertical type distilling furnace being further divided by at least one horizontal partition into an oil shale distilling chamber in the lower part thereof and at least one oil shale preheating chamber in the upper part thereof, said oil shale distilling chamber and said oil shale preheating chamber communication with each other through a gap provided at an end of said horizontal partition, an oil shale supplied continuously from an oil shale supply port provided in said oil shale treating chamber at the top thereof into said oil shale treating chamber continuously moving from the oil shale preheating chamber to the oil shale distilling chamber, a high-temperature gas blown into an oil shale distilling chamber passing horizontally through said oil shale in said oil shale treating chamber, thereby said oil shale is preheated in said oil shale preheating chamber, and a gaseous shale oil is distilled from said preheated oil shale in said oil shale distilling chamber; and a separator for separating by liquefaction a gaseous shale oil from a gas containing the gaseous shale oil discharged from the oil shale preheating chamber.

  18. East Coast (PADD 1) Distillate Fuel Oil Imports

    Gasoline and Diesel Fuel Update

    Decade Year-0 Year-1 Year-2 Year-3 Year-4 Year-5 Year-6 Year-7 Year-8 Year-9 1990's 942 1,260 1,471 1,990 2000's 2,114 1,896 1,914 1,969 2,258 2,132 2,118 1,955 1,695 1,237 2010's 1,471 2,114 2,970 2,608 3,801 4,282

    Other Renewable Fuels Distillate Fuel Oil Distillate F.O., 15 ppm and under Distillate F.O., 15 to 500 ppm Distillate F.O., Greater than 500 ppm Distillate F.O., 501 to 2000 ppm Distillate F.O., Greater than 2000 ppm Kerosene Finished Aviation Gasoline Aviation Gasoline Blending

  19. New Design Methods and Algorithms for Multi-component Distillation

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Processes | Department of Energy Design Methods and Algorithms for Multi-component Distillation Processes New Design Methods and Algorithms for Multi-component Distillation Processes multicomponent.pdf (517.32 KB) More Documents & Publications Development of Method and Algorithms To Identify Easily Implementable Energy-Efficient Low-Cost Multicomponent Distillation Column Trains With Large Energy Savings For Wide Number of Separations CX-100137 Categorical Exclusion Determination ITP

  20. DC Pro Software Tool Suite

    SciTech Connect (OSTI)

    2009-04-01

    This fact sheet describes how DOE's Data Center Energy Profiler (DC Pro) Software Tool Suite and other resources can help U.S. companies identify ways to improve the efficiency of their data centers.

  1. Prime Supplier Sales Volumes of Distillate Fuel Oils and Kerosene...

    Gasoline and Diesel Fuel Update

    Marketing Annual 1997 401 Table 50. Prime Supplier Sales Volumes of Distillate Fuel Oils and Kerosene by PAD District and State (Thousand Gallons per Day) - Continued...

  2. Table 50. Prime Supplier Sales Volumes of Distillate Fuel Oils...

    U.S. Energy Information Administration (EIA) (indexed site)

    Marketing Annual 1999 359 Table 50. Prime Supplier Sales Volumes of Distillate Fuel Oils and Kerosene by PAD District and State (Thousand Gallons per Day) - Continued...

  3. Increasing Distillate Production at U.S. Refineries

    Reports and Publications

    2010-01-01

    Paper explores the potential for U.S. refiners to create more distillate and less gasoline without major additional investments beyond those already planned.

  4. Omniphobic Membrane for Robust Membrane Distillation

    SciTech Connect (OSTI)

    Lin, SH; Nejati, S; Boo, C; Hu, YX; Osuji, CO; Ehmelech, M

    2014-11-01

    In this work, we fabricate an omniphobic microporous membrane for membrane distillation (MD) by modifying a hydrophilic glass fiber membrane with silica nanoparticles followed by surface fluorination and polymer coating. The modified glass fiber membrane exhibits an anti-wetting property not only against water but also against low surface tension organic solvents that easily wet a hydrophobic polytetrafluoroethylene (PTFE) membrane that is commonly used in MD applications. By comparing the performance of the PTFE and omniphobic membranes in direct contact MD experiments in the presence of a surfactant (sodium dodecyl sulfate, SDS), we show that SDS wets the hydrophobic PTFE membrane but not the omniphobic membrane. Our results suggest that omniphobic membranes are critical for MD applications with feed waters containing surface active species, such as oil and gas produced water, to prevent membrane pore wetting.

  5. Distillate Fuel Oil Assessment for Winter 1996-1997

    Reports and Publications

    1997-01-01

    This article describes findings of an analysis of the current low level of distillate stocks which are available to help meet the demand for heating fuel this winter, and presents a summary of the Energy Information Administration's distillate fuel oil outlook for the current heating season under two weather scenarios.

  6. Hybrid Pressure Retarded Osmosis-Membrane Distillation System for Power Generation from Low-Grade Heat: Thermodynamic Analysis and Energy Efficiency

    SciTech Connect (OSTI)

    Lin, SH; Yip, NY; Cath, TY; Osuji, CO; Elimelech, M

    2014-05-06

    We present a novel hybrid membrane system that operates as a heat engine capable of utilizing low-grade thermal energy, which is not readily recoverable with existing technologies. The closed-loop system combines membrane distillation (MD), which generates concentrated and pure water streams by thermal separation, and pressure retarded osmosis (PRO), which converts the energy of mixing to electricity by a hydro-turbine. The PRO-MD system was modeled by coupling the mass and energy flows between the thermal separation (MD) and power generation (PRO) stages for heat source temperatures ranging from 40 to 80 degrees C and working concentrations of 1.0, 2.0, and 4.0 mol/kg NaCl. The factors controlling the energy efficiency of the heat engine were evaluated for both limited and unlimited mass and heat transfer kinetics in the thermal separation stage. In both cases, the relative flow rate between the MD permeate (distillate) and feed streams is identified as an important operation parameter. There is an optimal relative flow rate that maximizes the overall energy efficiency of the PRO-MD system for given working temperatures and concentration. In the case of unlimited mass and heat transfer kinetics, the energy efficiency of the system can be analytically determined based on thermodynamics. Our assessment indicates that the hybrid PRO-MD system can theoretically achieve an energy efficiency of 9.8% (81.6% of the Carnot efficiency) with hot and cold working temperatures of 60 and 20 degrees C, respectively, and a working solution of 1.0 M NaCl. When mass and heat transfer kinetics are limited, conditions that more closely represent actual operations, the practical energy efficiency will be lower than the theoretically achievable efficiency. In such practical operations, utilizing a higher working concentration will yield greater energy efficiency. Overall, our study demonstrates the theoretical viability of the PRO-MD system and identifies the key factors for

  7. A Method to Distill Hydrogen Isotopes from Lithium | Princeton...

    U.S. Department of Energy (DOE) all webpages (Extended Search)

    to Distill Hydrogen Isotopes from Lithium This white paper outlines a method for the removal of tritium and deuterium from liquid lithium. The method is based on rapid or flash ...

  8. Membrane augmented distillation to separate solvents from water

    DOE Patents [OSTI]

    Huang, Yu; Baker, Richard W.; Daniels, Rami; Aldajani, Tiem; Ly, Jennifer H.; Alvarez, Franklin R.; Vane, Leland M.

    2012-09-11

    Processes for removing water from organic solvents, such as ethanol. The processes include distillation to form a rectified overhead vapor, compression of the rectified vapor, and treatment of the compressed vapor by two sequential membrane separation steps.

  9. Heat Integrated Distillation through Use of Microchannel Technology

    Energy.gov [DOE]

    This factsheet describes a research project whose goal is to develop a breakthrough distillation process using Microchannel Process Technology to integrate heat transfer and separation into a single unit operation.

  10. AgPro | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Jump to: navigation, search Name: AgPro Place: Massena, New York Product: Operator of biodiesel plant based on soy. References: AgPro1 This article is a stub. You can help OpenEI...

  11. Si Pro AS | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Pro AS Jump to: navigation, search Name: Si Pro AS Place: Glomfjord, Norway Zip: 8161 Product: Silicon recycler with facility in Singapore. Coordinates: 66.807991, 13.97315...

  12. Correlations estimate volume distilled using gravity, boiling point

    SciTech Connect (OSTI)

    Moreno, A.; Consuelo Perez de Alba, M. del; Manriquez, L.; Guardia Mendoz, P. de la

    1995-10-23

    Mathematical nd graphic correlations have been developed for estimating cumulative volume distilled as a function of crude API gravity and true boiling point (TBP). The correlations can be used for crudes with gravities of 21--34{degree} API and boiling points of 150--540 C. In distillation predictions for several mexican and Iraqi crude oils, the correlations have exhibited accuracy comparable to that of laboratory measurements. The paper discusses the need for such a correlation and the testing of the correlation.

  13. Low Temperature Geothermal Resource Assessment for Membrane Distillation

    Office of Scientific and Technical Information (OSTI)

    Desalination in the United States: Preprint (Conference) | SciTech Connect Low Temperature Geothermal Resource Assessment for Membrane Distillation Desalination in the United States: Preprint Citation Details In-Document Search Title: Low Temperature Geothermal Resource Assessment for Membrane Distillation Desalination in the United States: Preprint Substantial drought and declines in potable groundwater in the United States over the last decade has increased the demand for fresh water.

  14. PIA - Savannah River Nuclear Solution SRNS ProRad Environment...

    Office of Environmental Management (EM)

    SRNS ProRad Environment Management PIA - Savannah River Nuclear Solution SRNS ProRad Environment Management PIA - Savannah River Nuclear Solution SRNS ProRad Environment Management ...

  15. Collateral Duties for Program Records Official (PRO) | Department...

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Program Records Official (PRO) Collateral Duties for Program Records Official (PRO) GUIDANCE - Collateral Duties for PRO FINAL 141224.pdf (222.88 KB) More Documents & Publications ...

  16. FRACTIONAL DISTILLATION SEPARATION OF PLUTONIUM VALUES FROM LIGHT ELEMENT VALUES

    DOE Patents [OSTI]

    Cunningham, B.B.

    1957-12-17

    A process is described for removing light element impurities from plutonium. It has been found that plutonium contaminated with impurities may be purified by converting the plutonium to a halide and purifying the halide by a fractional distillation whereby impurities may be distilled from the plutonium halide. A particularly effective method includes the step of forming a lower halide such as the trior tetrahalide and distilling the halide under conditions such that no decomposition of the halide occurs. Molecular distillation methods are particularly suitable for this process. The apparatus may comprise an evaporation plate with means for heating it and a condenser surface with means for cooling it. The condenser surface is placed at a distance from the evaporating surface less than the mean free path of molecular travel of the material being distilled at the pressure and temperature used. The entire evaporating system is evacuated until the pressure is about 10/sup -4/ millimeters of mercury. A high temperuture method is presented for sealing porous materials such as carbon or graphite that may be used as a support or a moderator in a nuclear reactor. The carbon body is subjected to two surface heats simultaneously in an inert atmosphere; the surface to be sealed is heated to 1500 degrees centigrade; and another surface is heated to 300 degrees centigrade, whereupon the carbon vaporizes and flows to the cooler surface where it is deposited to seal that surface. This method may be used to seal a nuclear fuel in the carbon structure.

  17. Pro Corn LLC | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Pro-Corn LLC Place: Preston, Minnesota Zip: 55965 Product: Minnesotan farmer owned bioethanol production company. Coordinates: 47.526531, -121.936019 Show Map Loading map......

  18. Pro Ventum International | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Jump to: navigation, search Name: Pro Ventum International Place: Forchheim, Germany Zip: 79362 Sector: Wind energy Product: German-based developer of wind power...

  19. ProEco Energy | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Place: South Dakota Product: US South Dakota-based company specializing ethanol refinery project development. References: ProEco Energy1 This article is a stub. You can...

  20. Win pro energy group | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    energy group Place: Berlin, Berlin, Germany Zip: 12165 Sector: Renewable Energy, Solar, Wind energy Product: Win:pro offers location search, development, implementation,...

  1. ProForm | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Spreadsheet ComplexityEase of Use: Simple Website: poet.lbl.govProform Cost: Free References: ProForm1 Related Tools General Equilibrium Modeling Package (GEMPACK)...

  2. ProLogis | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Name: ProLogis Place: Aurora, Colorado Zip: 80011 Sector: Services Product: Provider of distribution facilities and services. Coordinates: 39.325162, -79.54975 Show Map...

  3. ,"No. 2 Distillate Sales to End Users Refiner Sales Volumes"

    U.S. Energy Information Administration (EIA) (indexed site)

    ... Refiners (Thousand Gallons per Day)","New Mexico No 2 Distillate Retail Sales by Refiners ...57.7,6018.7,64.6,101.5,691.5,1553.8,1576.9,2030.5,4320.3,1350.4,683.2,792.4,316.4,804.3,37...

  4. Table A3. Refiner/Reseller Prices of Distillate and Residual...

    U.S. Energy Information Administration (EIA) (indexed site)

    A3. RefinerReseller Prices of Distillate and Residual Fuel Oils, by PAD District, 1983-Present (Cents per Gallon Excluding Taxes) Geographic Area Year No. 1 Distillate No. 2...

  5. New Design Methods and Algorithms for Multi-component Distillation Processes

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Methods and Algorithms for Multi-component Distillation Processes Improved Energy Efficiency through the Determination of Optimal Distillation Configuration The ability to apply low-energy distillation confgurations can allow chemical manufacturers to reduce energy consumption of both existing and grassroots plants. However, the determina- tion of an appropriate confguration is limited by an incomplete knowledge of the 'search space' for a proper distillation network. Currently, no systematic

  6. Distillate Fuel Oil Refinery, Bulk Terminal, and Natural Gas Plant Stocks

    Gasoline and Diesel Fuel Update

    Product: Finished Motor Gasoline Reformulated Gasoline Conventional Gasoline Motor Gasoline Blending Comp. (MGBC) MGBC - Reformulated MGBC - Conventional Kerosene Distillate Fuel Oil Distillate F.O., 15 ppm and under Distillate F.O., Greater than 15 to 500 ppm Distillate F.O., Greater 500 ppm Residual Fuel Oil Propane/Propylene Period-Units: Monthly-Thousand Barrels Annual-Thousand Barrels Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources &

  7. BERLinPro Booster Cavity Design, Fabrication and Test Plans ...

    Office of Scientific and Technical Information (OSTI)

    BERLinPro Booster Cavity Design, Fabrication and Test Plans Citation Details In-Document Search Title: BERLinPro Booster Cavity Design, Fabrication and Test Plans The bERLinPro ...

  8. ProLogis France IX EURL | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    ProLogis France IX EURL Jump to: navigation, search Name: ProLogis France IX EURL Place: Aulnay-Sous-Bois Cedex, France Zip: 93614 Product: French subsidiary of ProLogis, a...

  9. EA-155 ProMark | Department of Energy

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    EA-155 ProMark Order authorizing ProMark Energy, Inc to export electric energy to Canada. EA-155 ProMark (46.89 KB) More Documents & Publications EA-196-A Minnesota Power, Sales ...

  10. Integrated process of distillation with side reactors for synthesis of organic acid esters

    DOE Patents [OSTI]

    Panchal, Chandrakant B; Prindle, John C; Kolah, Aspri; Miller, Dennis J; Lira, Carl T

    2015-11-04

    An integrated process and system for synthesis of organic-acid esters is provided. The method of synthesizing combines reaction and distillation where an organic acid and alcohol composition are passed through a distillation chamber having a plurality of zones. Side reactors are used for drawing off portions of the composition and then recycling them to the distillation column for further purification. Water is removed from a pre-reactor prior to insertion into the distillation column. An integrated heat integration system is contained within the distillation column for further purification and optimizing efficiency in the obtaining of the final product.

  11. Enhanced Separation Efficiency in Olefin/Paraffin Distillation

    Energy.gov [DOE]

    This factsheet describes a research project whose main objective is to develop technologies to enhance separation efficiencies by replacing the conventional packing materials with hollow fiber membranes, which have a high specific area and separated channels for both liquid and vapor phases. The use of hollow fibers in distillation columns can help refineries decrease operating costs, reduce greenhouse gas emissions through reduced heating costs, and help expand U.S. refining capacity through improvements to existing sites, without large scale capital investment.

  12. Reactive Distillation for Esterification of Bio-based Organic Acids

    SciTech Connect (OSTI)

    Fields, Nathan; Miller, Dennis J.; Asthana, Navinchandra S.; Kolah, Aspi K.; Vu, Dung; Lira, Carl T.

    2008-09-23

    The following is the final report of the three year research program to convert organic acids to their ethyl esters using reactive distillation. This report details the complete technical activities of research completed at Michigan State University for the period of October 1, 2003 to September 30, 2006, covering both reactive distillation research and development and the underlying thermodynamic and kinetic data required for successful and rigorous design of reactive distillation esterification processes. Specifically, this project has led to the development of economical, technically viable processes for ethyl lactate, triethyl citrate and diethyl succinate production, and on a larger scale has added to the overall body of knowledge on applying fermentation based organic acids as platform chemicals in the emerging biorefinery. Organic acid esters constitute an attractive class of biorenewable chemicals that are made from corn or other renewable biomass carbohydrate feedstocks and replace analogous petroleum-based compounds, thus lessening U.S. dependence on foreign petroleum and enhancing overall biorefinery viability through production of value-added chemicals in parallel with biofuels production. Further, many of these ester products are candidates for fuel (particularly biodiesel) components, and thus will serve dual roles as both industrial chemicals and fuel enhancers in the emerging bioeconomy. The technical report from MSU is organized around the ethyl esters of four important biorenewables-based acids: lactic acid, citric acid, succinic acid, and propionic acid. Literature background on esterification and reactive distillation has been provided in Section One. Work on lactic acid is covered in Sections Two through Five, citric acid esterification in Sections Six and Seven, succinic acid in Section Eight, and propionic acid in Section Nine. Section Ten covers modeling of ester and organic acid vapor pressure properties using the SPEAD (Step Potential

  13. Pro Sol Energia SA | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Sol Energia SA Jump to: navigation, search Name: Pro Sol Energia SA Place: Algarrobo-Costa (Malaga), Spain Zip: E-29750 Sector: Solar Product: Develops and builds solar power...

  14. New Design Methods and Algorithms for Energy Efficient Multicomponent Distillation Column Trains

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Methods and Algorithms for Energy Efficient Multicomponent Distillation Column Trains Enabling optimal configurations for high volume chemical separations Distillation is a ubiquitous method in the chemical and petrochemical industries to separate mixtures into their individual components and accounts for a large percentage of all separations in chemical and petrochemical plants. A large fraction of the separations are mixtures containing four or more components requiring multiple distillation

  15. New Design Methods and Algorithms for Energy Efficient Multicomponent Distillation Column Trains

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Rakesh Agrawal, School of Chemical Engineering, Purdue University U.S. DOE Advanced Manufacturing Office Program Review Meeting Washington, D.C. June 14-15, 2016 This presentation does not contain any proprietary, confidential, or otherwise restricted information. Project Objective Distillation: Essential to Meet Human Needs Courtesy: static.squarespace.com/ Courtesy: ths.talawanda.org Project Objective Distillation: Essential to Meet Human Needs  Multicomponent distillation: ubiquitous in

  16. Table 46. Refiner No. 2 Distillate, Diesel Fuel, and Fuel Oil...

    Annual Energy Outlook

    Petroleum Marketing Annual 1999 295 Table 46. Refiner No. 2 Distillate, Diesel Fuel, and Fuel Oil Volumes by PAD District and State (Thousand Gallons per Day) - Continued...

  17. Fractional distillation of C/sub 2//C/sub 3/ hydrocarbons at optimum pressures

    SciTech Connect (OSTI)

    Tedder, D.W.

    1984-08-07

    A method of recovering by distillation the separate components of a hydrocarbon gas mixture comprising ethylene, ethane, propylene and propane which comprises separating the ethylene and ethane as an overhead from a propylene and propane bottom in a first distillation tower at from about 400 to about 600 psia, separating ethylene and ethane as an ethylene overhead and an ethane bottom in a second distillation tower at from about 600 to about 700 psia, and separating propylene as an overhead from a propane bottom in a third distillation tower at from about 280 to about 300 psia is disclosed.

  18. T-534: Vulnerability in the PDF distiller of the BlackBerry Attachment...

    Energy.gov (indexed) [DOE]

    PROBLEM: Vulnerability in the PDF distiller of the BlackBerry Attachment Service for the BlackBerry Enterprise Server. PLATFORM: * BlackBerry Enterprise Server Express version...

  19. Comparison of advanced distillation control methods. Third annual report

    SciTech Connect (OSTI)

    Riggs, J.B.

    1997-07-01

    Detailed dynamic simulations of three industrial distillation columns (a propylene/propane splitter, a xylene/toluene column, and a depropanizer) have been used to study the issue of configuration selection for diagonal PI dual composition controls, feedforward from a feed composition analyzer, and decouplers. Auto Tune Variation (ATV) identification with on-line detuning for setpoint changes was used for tuning the diagonal proportional integral (PI) composition controls. In addition, robustness tests were conducted by inducting reboiler duty upsets. For single composition control, the (L, V) configuration was found to be best. For dual composition control, the optimum configuration changes from one column to another. Moreover, the use of analysis tools, such as RGA, appears to be of little value in identifying the optimum configuration for dual composition control. Using feedforward from a feed composition analyzer and using decouplers are shown to offer significant advantages for certain specific cases.

  20. Low capital implementation of distributed distillation in ethylene recovery

    DOE Patents [OSTI]

    Reyneke, Rian; Foral, Michael J.; Lee, Guang-Chung

    2006-10-31

    An apparatus for recovering ethylene from a hydrocarbon feed stream, where the apparatus is a single distillation column pressure shell encasing an upper region and a lower region. The upper region houses an ethylene distributor rectifying section and the lower region houses a C2 distributor section and an ethylene distributor stripping section. Vapor passes from the lower region into the upper region, and liquid passes from the upper region to the lower region. The process for recovering the ethylene is also disclosed. The hydrocarbon feed stream is introduced into the C2 distributor section, and after a series of stripping and refluxing steps, distinct hydrocarbon products are recovered from the C2 distributor section, the ethylene distributor stripping section, and the ethylene distributor rectifying section, respectively.

  1. U.S. Distillate Fuel Oil and Kerosene Sales by End Use

    U.S. Department of Energy (DOE) all webpages (Extended Search)

    Distillate Fuel Oil and Kerosene Sales by End Use (Thousand Gallons) Area: U.S. East Coast ... Residential Distillate Fuel Oil 4,103,881 3,930,517 3,625,747 3,473,310 3,536,111 ...

  2. UV resonance Raman characterization of polycyclic aromatic hydrocarbons in coal liquid distillates

    SciTech Connect (OSTI)

    Rumelfanger, R.; Asher, S.A.; Perry, M.B.

    1988-02-01

    Ultraviolet resonance Raman spectroscopy has been used to characterize the polycyclic aromatic hydrocarbon composition of a series of distillates of coal-derived liquids. The UV Raman spectra easily monitor changes in the polycyclic aromatic hydrocarbon composition as a function of distillation temperature. Specific species, such as pyrene, can be determined by judicious choice of excitation wavelength.

  3. Home Performance Contractor Pro Forma | Department of Energy

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Home Performance Contractor Pro Forma, with program HR, assumptions, marketing actuals and costs, and more, as posted on the U.S. Department of Energy's Better Buildings Neighborhood Program website. Home Performance Contractor Pro Forma (1.18 MB

  4. Cryogenic system for BERLinPro

    SciTech Connect (OSTI)

    Anders, W.; Hellwig, A.; Knobloch, J.; Pflückhahn, D.; Rotterdam, S.

    2014-01-29

    In 2010 Helmholtz-Zentrum Berlin (HZB) received funding to design and build the Berlin Energy Recovery Linac Project BERLinPro. The goal of this compact Energy recovery linac (ERL) is to develop the accelerator physics and technology required to generate and accelerate a 100-mA, 1-mm mrad emittance electron beam. The BERLinPro know-how can then be transferred to various ERL-based applications. All accelerating RF cavities including the electron source are based on superconducting technology operated at 1.8 K. A Linde L700 helium liquefier is supplying 4.5 K helium. The subatmospheric pressure of 16 mbar of the helium bath of the cavities will be achieved by pumping with a set of cold compressors and warm vacuum pumps. While the L700 is already in operating, the 1.8 K system and the helium transfer system are in design phase.

  5. HyPro: Modeling the Hydrogen Transition

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    HyPro: Modeling the H 2 Transition Brian James Directed Technologies, Inc. 9 May 2007 This presentation does not contain any proprietary, confidential, or otherwise restricted information Directed Technologies, Inc. 09 May 2007 2 Outline Model Overview Results Summary Cost & Methodology Assumptions Directed Technologies, Inc. 09 May 2007 3 Project Objectives Overall Create a tool robust enough to test the impact of different assumptions on the development of hydrogen infrastructure and

  6. Perl Embedded in PTC's Pro/ENGINEER, Version 1

    Energy Science and Technology Software Center (OSTI)

    2003-12-22

    Pro-PERL (AKA Pro/PERL) is a Perl extension to the PTC Pro/TOOLKIT API to the PTC Pro/ENGINEER CAD application including an embedded interpreter. It can be used to automate and customize Pro/ENGINEER, create Vendor Neutral Archive (VNA) format files and re-create CAD models from the VNA files. This has applications in sanitizing classified CAD models created in a classified environment for transfer to an open environment, creating template models for modification to finished models by non-expertmore » users, and transfer of design intent data to other modeling technologies.« less

  7. Kinetic and reactor models for HDT of middle distillates

    SciTech Connect (OSTI)

    Cotta, R.M.; Filho, R.M.

    1996-12-31

    Hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) of middle distillates over a commercial Ni-Mo/y-Al{sub 2}O{sub 3} has been studied under wide operating conditions just as 340 to 380{degrees}C and 38 to 98 atm. A Power Law model was presented to each one of those reactions. The parameters of kinetic equations were estimated solving the ordinary differential equations by the 4 order Runge-Kutta-Gill algorithm and Marquardt method for searching of set of kinetic parameters (kinetic constants as well as the orders of reactions). An adiabatic diesel hydrotreating trickle-bed reactor packed with the same catalyst was simulated numerically in order to check up the behavior of this specific reaction system. One dimensional pseudo-homogeneous model was used in this work. For each feed, the mass and energy balance equations were integrated along the length of the catalytic bed using the 4th Runge-Kutta-Gill method. The performance of two industrial reactors was checked. 5 refs., 2 tabs.

  8. Simple rules help select best hydrocarbon distillation scheme

    SciTech Connect (OSTI)

    Sanchezllanes, M.T.; Perez, A.L.; Martinez, M.P.; Aguilar-Rodriguez, E.; Rosal, R. del )

    1993-12-06

    Separation economics depend mainly on investment for major equipment and energy consumption. This relationship, together with the fact that, in most cases, many alternative schemes will be proposed, make it essential to find an optimum scheme that minimizes overall costs. Practical solutions are found by applying heuristics -- exploratory problem-solving techniques that eliminate alternatives without applying rigorous mathematical procedures. These techniques have been applied to a case study. In the case study, a hydrocarbon mixture will be transported through a pipeline to a fractionation plant, where it will be separated into commercial products for distribution. The fractionation will consist of a simple train of distillation columns, the sequence of which will be defined by applying heuristic rules and determining the required thermal duties for each column. The facility must separate ethane, propane and mixed butanes, natural gasoline (light straight-run, or LSR, gasoline), and condensate (heavy naphtha). The ethane will be delivered to an ethylene plant as a gaseous stream, the propane and butanes will be stored in cryogenic tanks, and the gasoline and heavy naphtha also will be stored.

  9. Use of extractive distillation to produce concentrated nitric acid

    SciTech Connect (OSTI)

    Campbell, P.C.; Griffin, T.P.; Irwin, C.F.

    1981-04-01

    Concentrated nitric acid (> 95 wt %) is needed for the treatment of off-gases from a fuels-reprocessing plant. The production of concentrated nitric acid by means of extractive distillation in the two-pot apparatus was studied to determine the steady-state behavior of the system. Four parameters, EDP volume (V/sub EDP/) and temperature (T/sub EDP/), acid feed rate, and solvent recycle, were independently varied. The major response factors were percent recovery (CPRR) and product purity (CCP). Stage efficiencies also provided information about the system response. Correlations developed for the response parameters are: CPRR = 0.02(V/sub EDP/ - 800 cc) + 53.5; CCP = -0.87 (T/sub EDP/ - 140/sup 0/C) + 81; eta/sub V,EDP/ = 9.1(F/sub feed/ - 11.5 cc/min) - 0.047(V/sub EDP/ - 800 cc) - 2.8(F/sub Mg(NO/sub 3/)/sub 2// - 50 cc/min) + 390; and eta/sub L,EDP/ = 1.9(T/sub EDP/ - 140/sup 0/C) + 79. A computer simulation of the process capable of predicting steady-state conditions was developed, but it requires further work.

  10. Refiner/marketer targets production of transportation fuels and distillates

    SciTech Connect (OSTI)

    Thompson, J.E.

    1997-01-01

    Citgo Petroleum Corp., the wholly owned subsidiary of Petroleos de Venezuela, S.A. (PDVSA), the Venezuelan national oil company, owns two gasoline producing refineries, a 305,000-b/d system in Lake Charles, La., and a 130,000-b/d facility in Corpus Christi, Texas. Each is considered a deep conversion facility capable of converting heavy, sour crudes into a high percentage of transportation fuels and distillates. Two smaller refineries, one in Paulsboro, N.J., and one in Savannah, GA., have the capacity to process 40,000 b/d and 28,000 b/d of crude, respectively, for asphalt products. In the past two years, Citgo`s light oils refineries operated safely and reliably with a minimum of unscheduled shutdowns. An ongoing emphasis to increase reliability has resulted in extended run lengths at the refineries. Citgo has invested $314 million at its facilities in 1995, much of this toward environmental and regulatory projects, such as the new waste water treatment unit at the Lake Charles refinery. Over the next few years, Citgo expects to complete $1.5 billion in capital spending for major processing units such as a 60,000-b/d FCC feed hydrotreater unit at the Lake Charles refinery and crude expansion at the Corpus Christi refinery. Product exchanges and expanded transport agreements are allowing Citgo to extend its marketing reach.

  11. Comparison of advanced distillation control methods. Second annual report

    SciTech Connect (OSTI)

    1996-11-01

    Detailed dynamic simulations of three industrial distillation columns (a propylene/propane splitter, a xylene/toluene column, and a depropanizer) have been used to study the issue of configuration selection for diagonal PI dual composition controls. ATV identification with on-line detuning was used for tuning the diagonal PI composition controllers. Each configuration was evaluated with respect to steady-state RGA values, sensitivity to feed composition changes, and open loop dynamic performance. Each configuration was tuned using setpoint changes over a wider range of operation for robustness and tested for feed composition upsets. Overall, configuration selection was shown to have a dominant effect upon control performance. Configuration analysis tools (e.g., RGA, condition number, disturbance sensitivity), were found to reject configuration choices that are obviously poor choices, but were unable to critically differentiate between the remaining viable choices. Configuration selection guidelines are given although it is demonstrated that the most reliable configuration selection approach is based upon testing the viable configurations using dynamic column simulators.

  12. Comparison of advanced distillation control methods. Second annual report

    SciTech Connect (OSTI)

    Riggs, J.B.

    1996-11-01

    Detailed dynamic simulations of two industrial distillation columns (a propylene/propane splitter and a xylene/toluene column) have been used to study the issue of configuration selection for diagonal PI dual composition controls. Auto Tune Variation (ATV) identification with on-line detuning was used for tuning the diagonal proportional integral (PI) composition controls. Each configuration was evaluated with respect to steady-state relative gain array (RGA) values, sensitivity to feed composition changes, and open loop dynamic performance. Each configuration was tuned using setpoint changes over a wider range of operation for robustness and tested for feed composition upsets. Overall, configuration selection was shown to have a dominant effect upon control performance. Configuration analysis tools (e.g., RGA, condition number, disturbance sensitivity) were found to reject configuration choices that are obviously poor choices, but were unable to critically differentiate between the remaining viable choices. Configuration selection guidelines are given although it is demonstrated that the most reliable configuration selection approach is based upon testing the viable configurations using dynamic column simulators.

  13. Distillation sequence for the purification and recovery of hydrocarbons

    DOE Patents [OSTI]

    Reyneke, Rian; Foral, Michael; Papadopoulos, Christos G.; Logsdon, Jeffrey S.; Eng, Wayne W. Y.; Lee, Guang-Chung; Sinclair, Ian

    2007-12-25

    This invention is an improved distillation sequence for the separation and purification of ethylene from a cracked gas. A hydrocarbon feed enters a C2 distributor column. The top of the C2 distributor column is thermally coupled to an ethylene distributor column, and the bottoms liquid of a C2 distributor column feeds a deethanizer column. The C2 distributor column utilizes a conventional reboiler. The top of the ethylene distributor is thermally coupled with a demethanizer column, and the bottoms liquid of the ethylene distributor feeds a C2 splitter column. The ethylene distributor column utilizes a conventional reboiler. The deethanizer and C2 splitter columns are also thermally coupled and operated at a substantially lower pressure than the C2 distributor column, the ethylene distributor column, and the demethanizer column. Alternatively, a hydrocarbon feed enters a deethanizer column. The top of the deethanizer is thermally coupled to an ethylene distributor column, and the ethylene distributor column utilizes a conventional reboiler. The top of the ethylene distributor column is thermally coupled with a demethanizer column, and the bottoms liquid of the ethylene distributor column feeds a C2 splitter column. The C2 splitter column operates at a pressure substantially lower than the ethylene distributor column, the demethanizer column, and the deethanizer column.

  14. Fractional distillation as a strategy for reducing the genotoxic potential of SRC-II coal liquids: a status report

    SciTech Connect (OSTI)

    Pelroy, R.A.; Wilson, B.W.

    1981-09-01

    This report presents results of studies on the effects of fractional distillation on the genotoxic potential of Solvent Refined Coal (SRC-II) liquids. SRC-II source materials and distilled liquids were provided by Pittsburg and Midway Coal Mining Co. Fractional distillations were conducted on products from the P-99 process development unit operating under conditions approximating those anticipated at the SRC-II demonstration facility. Distillation cuts were subjected to chemical fractionation, in vitro bioassay and initial chemical analysis. Findings are discussed as they relate to the temperature at which various distillate cuts were produced. This document is the first of two status reports scheduled for 1981 describing these studies.

  15. U.S. Total No. 2 Distillate Prices by Sales Type

    Gasoline and Diesel Fuel Update

    2010 2011 2012 2013 2014 2015 View History No. 2 Distillate Sales to End Users, Average 2.449 - - - - - 1983-2015 Residential 2.798 - - - - - 1978-2015 CommercialInstitutional ...

  16. Table 46. Refiner No. 2 Distillate, Diesel Fuel, and Fuel Oil...

    Annual Energy Outlook

    839.2 135.0 1,251.9 See footnotes at end of table. 46. Refiner No. 2 Distillate, Diesel Fuel, and Fuel Oil Volumes by PAD District and State Energy Information Administration ...

  17. ,"U.S. Distillate Fuel Oil and Kerosene Sales by End Use"

    U.S. Energy Information Administration (EIA) (indexed site)

    Distillate Fuel Oil and Kerosene Sales by End Use" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description"," Of Series","Frequency","Latest Data for"...

  18. New Design Methods and Algorithms for Multi-component Distillation Processes

    SciTech Connect (OSTI)

    2009-02-01

    This factsheet describes a research project whose main goal is to develop methods and software tools for the identification and analysis of optimal multi-component distillation configurations for reduced energy consumption in industrial processes.

  19. A heat & mass integration approach to reduce capital and operating costs of a distillation configuration

    SciTech Connect (OSTI)

    Madenoor Ramapriya, Gautham; Jiang, Zheyu; Tawarmalani, Mohit; Agrawal, Rakesh

    2015-11-11

    We propose a general method to consolidate distillation columns of a distillation configuration using heat and mass integration. The proposed method encompasses all heat and mass integrations known till date, and includes many more. Each heat and mass integration eliminates a distillation column, a condenser, a reboiler and the heat duty associated with a reboiler. Thus, heat and mass integration can potentially offer significant capital and operating cost benefits. In this talk, we will study the various possible heat and mass integrations in detail, and demonstrate their benefits using case studies. This work will lay out a framework to synthesize an entire new class of useful configurations based on heat and mass integration of distillation columns.

  20. Do-it-yourself guideline for constructing a solar alcohol distillation system

    SciTech Connect (OSTI)

    Kennedy, B.W.

    1982-07-27

    The development and testing of a solar powered distillation system are described. The system consists of a parabolic dish collector, a two axis sun tracking stand, sun tracking solar cell system, condenser, fermentation tanks, and continuous distillation still. The assembly instructions for the parabolic dish are included as well as the basic steps to follow in mashing and fermenting of corn meal. 15 figures. (DMC)

  1. Quantum tomographic cryptography with Bell diagonal states: Nonequivalence of classical and quantum distillation protocols

    SciTech Connect (OSTI)

    Kaszlikowski, Dagomir; Lim, J.Y.; Willeboordse, Frederick H.; Oi, D.K.L.; Gopinathan, Ajay; Kwek, L.C.

    2005-01-01

    We present a generalized tomographic quantum key distribution protocol in which the two parties share a Bell diagonal mixed state of two qubits. We show that if an eavesdropper performs a coherent measurement on many quantum ancilla states simultaneously, classical methods of secure key distillation are less effective than quantum entanglement distillation protocols. We also show that certain classes of Bell diagonal states are resistant to any attempt at incoherent eavesdropping.

  2. Comparison of Advanced Distillation Control Methods, Final Technical Report

    SciTech Connect (OSTI)

    Dr. James B. Riggs

    2000-11-30

    Detailed dynamic simulations of three industrial distillation columns (a propylene/propane splitter, a xylene/toluene column, and a depropanizer) have been used to evaluate configuration selections for single-ended and dual-composition control, as well as to compare conventional and advanced control approaches. In addition, a simulator of a main fractionator was used to compare the control performance of conventional and advanced control. For each case considered, the controllers were tuned by using setpoint changes and tested using feed composition upsets. Proportional Integral (PI) control performance was used to evaluate the configuration selection problem. For single ended control, the energy balance configuration was found to yield the best performance. For dual composition control, nine configurations were considered. It was determined that the use of dynamic simulations is required in order to identify the optimum configuration from among the nine possible choices. The optimum configurations were used to evaluate the relative control performance of conventional PI controllers, MPC (Model Predictive Control), PMBC (Process Model-Based Control), and ANN (Artificial Neural Networks) control. It was determined that MPC works best when one product is much more important than the other, while PI was superior when both products were equally important. PMBC and ANN were not found to offer significant advantages over PI and MPC. MPC was found to outperform conventional PI control for the main fractionator. MPC was applied to three industrial columns: one at Phillips Petroleum and two at Union Carbide. In each case, MPC was found to significantly outperform PI controls. The major advantage of the MPC controller is its ability to effectively handle a complex set of constraints and control objectives.

  3. PILOT-SCALE REMOVAL OF FLUORIDE FROM LEGACY PLUTONIUM MATERIALS USING VACUUM SALT DISTILLATION

    SciTech Connect (OSTI)

    Pierce, R. A.; Pak, D. J.

    2012-09-11

    Between September 2009 and January 2011, the Savannah River National Laboratory (SRNL) and HB-Line designed, developed, tested, and successfully deployed a system for the distillation of chloride salts. In 2011, SRNL adapted the technology for the removal of fluoride from fluoride-bearing salts. The method involved an in situ reaction between potassium hydroxide (KOH) and the fluoride salt to yield potassium fluoride (KF) and the corresponding oxide. The KF and excess KOH can be distilled below 1000{deg}C using vacuum salt distillation (VSD). The apparatus for vacuum distillation contains a zone heated by a furnace and a zone actively cooled using either recirculated water or compressed air. During a vacuum distillation operation, a sample boat containing the feed material is placed into the apparatus while it is cool, and the system is sealed. The system is evacuated using a vacuum pump. Once a sufficient vacuum is attaned, heating begins. Volatile salts distill from the heated zone to the cooled zone where they condense, leaving behind the non-volatile material in the feed boat. Studies discussed in this report were performed involving the use of non-radioactive simulants in small-scale and pilot-scale systems as well as radioactive testing of a small-scale system with plutonium-bearing materials. Aspects of interest include removable liner design considerations, boat materials, in-line moisture absorption, and salt deposition.

  4. Pro Solar Solarstrom GmbH | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    GmbH Jump to: navigation, search Name: Pro Solar Solarstrom GmbH Place: Ravensburg, Germany Zip: 88214 Sector: Solar Product: Distributor of PV modules, including Canadian...

  5. Home Performance Contractor Pro Forma | Department of Energy

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Home Performance Contractor Pro Forma, with program HR, assumptions, marketing actuals and costs, and more, as posted on the U.S. Department of Energy's Better Buildings ...

  6. SolarPro Energy International | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Place: Granite Bay, California Zip: 95746 Sector: Solar Product: SolarPro Energy installs solar power systems using PV panels for residential and commercial properties. References:...

  7. A Variational Pro jection Operator for Mapping of Internal Variables...

    Office of Scientific and Technical Information (OSTI)

    Title: A Variational Pro jection Operator for Mapping of Internal Variables. Authors: Mota, Alejandro ; Sun, WaiChing ; Ostien, Jakob ; Foulk, James W., III ; Long, Kevin...

  8. BatPRO: Battery Manufacturing Cost Estimation | Argonne National Laboratory

    U.S. Department of Energy (DOE) all webpages (Extended Search)

    BatPRO: Battery Manufacturing Cost Estimation BatPRO models a stiff prismatic pouch-type cell battery pack with cells linked in series. BatPRO models a stiff prismatic pouch-type cell battery pack with cells linked in series. BatPRO is the user-friendly, Windows-based version of BatPaC, a software modeling tool designed for policymakers and researchers who are interested in estimating the cost of lithium-ion batteries after they have reached a mature state of development and are being

  9. The cough response to ultrasonically nebulized distilled water in heart-lung transplantation patients

    SciTech Connect (OSTI)

    Higenbottam, T.; Jackson, M.; Woolman, P.; Lowry, R.; Wallwork, J.

    1989-07-01

    As a result of clinical heart-lung transplantation, the lungs are denervated below the level of the tracheal anastomosis. It has been questioned whether afferent vagal reinnervation occurs after surgery. Here we report the cough frequency, during inhalation of ultrasonically nebulized distilled water, of 15 heart-lung transplant patients studied 6 wk to 36 months after surgery. They were compared with 15 normal subjects of a similar age and sex. The distribution of the aerosol was studied in five normal subjects using /sup 99m/technetium diethylene triamine pentaacetate (/sup 99m/Tc-DTPA) in saline. In seven patients, the sensitivity of the laryngeal mucosa to instilled distilled water (0.2 ml) was tested at the time of fiberoptic bronchoscopy by recording the cough response. Ten percent of the aerosol was deposited onto the larynx and trachea, 56% on the central airways, and 34% in the periphery of the lung. The cough response to the aerosol was strikingly diminished in the patients compared with normal subjects (p less than 0.001), but all seven patients coughed when distilled water was instilled onto the larynx. As expected, the laryngeal mucosa of heart-lung transplant patients remains sensitive to distilled water. However, the diminished coughing when the distilled water is distributed by aerosol to the central airways supports the view that vagal afferent nerves do not reinnervate the lungs after heart-lung transplantation, up to 36 months after surgery.

  10. Experimental investigation on hydrogen cryogenic distillation equipped with package made by ICIT

    SciTech Connect (OSTI)

    Bornea, A.; Zamfirache, M.; Stefan, L.; Stefanescu, I.; Preda, A.

    2015-03-15

    ICIT (Institute for Cryogenics and Isotopic Technologies) has used its experience in cryogenic water distillation process to propose a similar process for hydrogen distillation that can be used in detritiation technologies. This process relies on the same packages but a stainless filling is tested instead of the phosphorous bronze filling used for water distillation. This paper presents two types of packages developed for hydrogen distillation, both have a stainless filling but it differs in terms of density, exchange surface and specific volume. Performance data have been obtained on laboratory scale. In order to determine the characteristics of the package, the installation was operated in the total reflux mode, for different flow rate for the liquid. There were made several experiments considering different operating conditions. Samples extracted at the top and bottom of cryogenic distillation column allowed mathematical processing to determine the separation performance. The experiments show a better efficiency for the package whose exchange surface was higher and there were no relevant differences between both packages as the operating pressure of the cryogenic column was increasing. For a complete characterization of the packages, future experiments will be considered to determine performance at various velocities in the column and their correlation with the pressure in the column. We plan further experiments to separate tritium from the mixture of isotopes DT, having in view that our goal is to apply this results to a detritiation plant.

  11. ProPortal: A Database for Prochlorococcus

    DOE Data Explorer [Office of Scientific and Technical Information (OSTI)]

    Huang, Katherine [Chisholm lab, MIT

    Prochlorococcus is a marine cyanobacterium that numerically dominates the mid-latitude oceans, and is the smallest known oxygenic phototroph. All isolates described thus far can be assigned to either a tightly clustered high-light (HL) adapted clade, or a more divergent low-light (LL) adapted group. They are closely related to, but distinct from, marine Synechococcus. The genomes of 12 strains have been sequenced and they range in size from 1.6 to 2.6 Mbp. They represent diverse lineages, spanning the rRNA diversity (97 to 99.93% similarity) of cultured representatives of this group. Our analyses of these genomes inform our understanding of how adaptation occurs in the oceans along gradients of light, nutrients, and other environmental factors, providing essential context for interpreting rapidly expanding metagenomic datasets. [Copied from http://proportal.mit.edu/project/prochlorococcus/] ProPortal allows users to browse and search genome date for not only Prochlorococcus, but Cyanophage and Synechococcus. Microarray data, environmental cell concentration data, and metagenome information are also available.

  12. Low-temperature distillation plants: a comparison with seawater reverse osmosis

    SciTech Connect (OSTI)

    Hoffman, D.

    1981-07-01

    Low-temperature distillation plants using large aluminum-alloy heat-transfer surfaces have reduced energy requirements to levels projected today for second-generation seawater reverse-osmosis (SWRO) plants. Less sensitive to feed contamination, and totally free from maintenance associated with a complex and critical feed-pretreatment system and periodic membrane replacements, the low-temperature distillation plants out-perform SWRO plants also by their higher-quality product, 2-10 ppM TDS versus 300 to 1000 ppM TDS. Energy requirements and operating costs for Low Temperature Vapor Compression (LT-VC) and Multi-Effect-Distillation (LT-MED) plants, in dual-purpose and various waste-heat-utilization schemes, are compared with those of SWRO plants. 10 references, 14 figures, 8 tables.

  13. Global optimization of multicomponent distillation configurations: 2. Enumeration based global minimization algorithm

    DOE PAGES-Beta [OSTI]

    Nallasivam, Ulaganathan; Shah, Vishesh H.; Shenvi, Anirudh A.; Huff, Joshua; Tawarmalani, Mohit; Agrawal, Rakesh

    2016-02-10

    We present a general Global Minimization Algorithm (GMA) to identify basic or thermally coupled distillation configurations that require the least vapor duty under minimum reflux conditions for separating any ideal or near-ideal multicomponent mixture into a desired number of product streams. In this algorithm, global optimality is guaranteed by modeling the system using Underwood equations and reformulating the resulting constraints to bilinear inequalities. The speed of convergence to the globally optimal solution is increased by using appropriate feasibility and optimality based variable-range reduction techniques and by developing valid inequalities. As a result, the GMA can be coupled with already developedmore » techniques that enumerate basic and thermally coupled distillation configurations, to provide for the first time, a global optimization based rank-list of distillation configurations.« less

  14. Conversion of lpg hydrocarbons to distillate fuels or lubes using integration of lpg dehydrogenation and mogdl

    SciTech Connect (OSTI)

    Chang, C. D.; Penick, J. E.; Socha, R. F.

    1985-09-17

    Disclosed is a method and apparatus for producing distillate and/or lubes which employ integrating catalytic (or thermal) dehydrogenation of paraffins with MOGDL. The process feeds the product from a low temperature propane and/or butane dehydrogenation zone into a first catalytic reactor zone, which operates at low pressure and contains zeolite oligomerization catalysts, where the low molecular weight olefins are reacted to primarily gasoline range materials. These gasoline range materials can then be pressurized to the pressure required for reacting to distillate in a second catalytic reactor zone operating at high pressure and containing a zeolite oligomerization catalyst. The distillate is subsequently sent to a hydrotreating unit and product separation zone to form lubes and other finished products.

  15. Source book for planning nuclear dual-purpose electric/distillation desalination plants

    SciTech Connect (OSTI)

    Reed, S.A.

    1981-02-01

    A source book on nuclear dual-purpose electric/distillation desalination plants was prepared to assist government and other planners in preparing broad evaluations of proposed applications of dual-purpose plants. The document is divided into five major sections. Section 1 presents general discussions relating to the benefits of dual-purpose plants, and spectrum for water-to-power ratios. Section 2 presents information on commercial nuclear plants manufactured by US manufacturers. Section 3 gives information on distillation desalting processes and equipment. Section 4 presents a discussion on feedwater pretreatment and scale control. Section 5 deals with methods for coupling the distillation and electrical generating plants to operate in the dual mode.

  16. New Design Methods And Algorithms For High Energy-Efficient And Low-cost Distillation Processes

    SciTech Connect (OSTI)

    Agrawal, Rakesh

    2013-11-21

    This project sought and successfully answered two big challenges facing the creation of low-energy, cost-effective, zeotropic multi-component distillation processes: first, identification of an efficient search space that includes all the useful distillation configurations and no undesired configurations; second, development of an algorithm to search the space efficiently and generate an array of low-energy options for industrial multi-component mixtures. Such mixtures are found in large-scale chemical and petroleum plants. Commercialization of our results was addressed by building a user interface allowing practical application of our methods for industrial problems by anyone with basic knowledge of distillation for a given problem. We also provided our algorithm to a major U.S. Chemical Company for use by the practitioners. The successful execution of this program has provided methods and algorithms at the disposal of process engineers to readily generate low-energy solutions for a large class of multicomponent distillation problems in a typical chemical and petrochemical plant. In a petrochemical complex, the distillation trains within crude oil processing, hydrotreating units containing alkylation, isomerization, reformer, LPG (liquefied petroleum gas) and NGL (natural gas liquids) processing units can benefit from our results. Effluents from naphtha crackers and ethane-propane crackers typically contain mixtures of methane, ethylene, ethane, propylene, propane, butane and heavier hydrocarbons. We have shown that our systematic search method with a more complete search space, along with the optimization algorithm, has a potential to yield low-energy distillation configurations for all such applications with energy savings up to 50%.

  17. ,,,,"Reasons that Made Distillate Fuel Oil Unswitchable"

    U.S. Energy Information Administration (EIA) (indexed site)

    4 Relative Standard Errors for Table 10.24;" " Unit: Percents." ,,,,"Reasons that Made Distillate Fuel Oil Unswitchable" " "," ",,,,,,,,,,,,," " ,,"Total Amount of ","Total Amount of","Equipment is Not","Switching","Unavailable ",,"Long-Term","Unavailable",,"Combinations of " "NAICS"," ","Distillate Fuel Oil","Unswitchable

  18. Systems and methods for reactive distillation with recirculation of light components

    DOE Patents [OSTI]

    Stickney, Michael J. (Nassau Bay, TX); Jones, Jr., Edward M. (Friendswood, TX)

    2011-07-26

    Systems and methods for producing gas-to-liquids products using reactive distillation are provided. The method for producing gas-to-liquids products can include reacting a feedstock in a column having a distillation zone and a reaction zone to provide a bottoms stream and an overhead stream. A first portion of the overhead stream can be recycled to the column at the top of the reaction zone and second portion of the overhead stream can be recycled to the column at the bottom of the reaction zone.

  19. Process for converting heavy oil deposited on coal to distillable oil in a low severity process

    DOE Patents [OSTI]

    Ignasiak, Teresa; Strausz, Otto; Ignasiak, Boleslaw; Janiak, Jerzy; Pawlak, Wanda; Szymocha, Kazimierz; Turak, Ali A.

    1994-01-01

    A process for removing oil from coal fines that have been agglomerated or blended with heavy oil comprises the steps of heating the coal fines to temperatures over 350.degree. C. up to 450.degree. C. in an inert atmosphere, such as steam or nitrogen, to convert some of the heavy oil to lighter, and distilling and collecting the lighter oils. The pressure at which the process is carried out can be from atmospheric to 100 atmospheres. A hydrogen donor can be added to the oil prior to deposition on the coal surface to increase the yield of distillable oil.

  20. ,"New Mexico Sales of Distillate Fuel Oil by End Use"

    U.S. Energy Information Administration (EIA) (indexed site)

    Sales of Distillate Fuel Oil by End Use" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","New Mexico Sales of Distillate Fuel Oil by End Use",13,"Annual",2014,"6/30/1984" ,"Release Date:","12/22/2015" ,"Next Release Date:","Last Week of November 2016" ,"Excel

  1. ,"U.S. Adjusted Sales of Distillate Fuel Oil by End Use"

    U.S. Energy Information Administration (EIA) (indexed site)

    Distillate Fuel Oil by End Use" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","U.S. Adjusted Sales of Distillate Fuel Oil by End Use",13,"Annual",2014,"6/30/1984" ,"Release Date:","12/22/2015" ,"Next Release Date:","Last Week of November 2016" ,"Excel File

  2. Pro Isomerization in MLL1 PHD3-Bromo Cassette Connects H3K4me...

    Office of Scientific and Technical Information (OSTI)

    SciTech Connect Search Results Journal Article: Pro ... Citation Details In-Document Search Title: Pro Isomerization ... Here, we report on structure-function studies that elucidate ...

  3. Pro2 Anlagentechnik GmbH | Open Energy Information

    Open Energy Information (Open El) [EERE & EIA]

    Zip: 47877 Product: Pro2 delivers turn-key plants for utilisation of biogas, sewage, natural gas and landfill gas in the range from 100 to 3,600 kWe. Coordinates: 51.26439,...

  4. Home Performance Contractor Pro Forma | Department of Energy

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Excel sheet for program model, expenses, HR, and marketing, as posted on the U.S. Department of Energy's Better Buildings Neighborhood Program website. Home Performance Contractor Pro Forma (1022.61 KB

  5. Effect of Narrow Cut Oil Shale Distillates on HCCI Engine Performance

    SciTech Connect (OSTI)

    Eaton, Scott J; Bunting, Bruce G; Lewis Sr, Samuel Arthur; Fairbridge, Craig

    2009-01-01

    In this investigation, oil shale crude obtained from the Green River Formation in Colorado using Paraho Direct retorting was mildly hydrotreated and distilled to produce 7 narrow boiling point fuels of equal volumes. The resulting derived cetane numbers ranged between 38.3 and 43.9. Fuel chemistry and bulk properties strongly correlated with boiling point.

  6. U.S. Adjusted Distillate Fuel Oil and Kerosene Sales by End Use

    U.S. Energy Information Administration (EIA) (indexed site)

    Show Data By: End Use Product Area 2009 2010 2011 2012 2013 2014 View History Residential Distillate Fuel Oil 4,328,840 3,897,937 3,713,883 3,223,851 3,714,150 4,041,766 1984-2014 ...

  7. Corrosion and protection of mild steel in petroleum distillates electrolyte mixtures

    SciTech Connect (OSTI)

    Groysman, A.; Erdman, N.

    1999-11-01

    The purpose of this study is to examine the influence of water and salts present on the corrosion process in petroleum distillate electrolyte mixtures and evaluation of inorganic inhibitors efficiency for protection of mild steel in these mixtures. Most of the research in this area until now was done with hydrocarbon water mixtures with relatively high concentrations of water (above 5 % volume). This study was conducted using mixtures of light petroleum distillates (naphtha and gasoline) and water with water concentrations in the mixture below 5% volume. The study confirmed the electrochemical origin of the corrosion mechanism and showed that the main cause of the corrosion in the petroleum distillate water mixtures is the presence of water and dissolved oxygen. Critical added water concentrations were evaluated for naphtha-water and gasoline-water mixtures. The most efficient concentrations of inorganic inhibitors were determined and the inhibition mechanism was confirmed. Valuable data regarding different types of corrosion attack (pitting or uniform corrosion) on mild steel in petroleum distillate electrolyte mixtures was acquired during the study.

  8. Hybrid Separations/Distillation Technology. Research Opportunities for Energy and Emissions Reduction

    SciTech Connect (OSTI)

    Eldridge, R. Bruce; Seibert, A. Frank; Robinson, Sharon; Rogers, Jo

    2005-04-01

    This report focuses on improving the existing separations systems for the two largest energy-consuming sectors: the chemicals and petroleum refining industries. It identifies the technical challenges and research needs for improving the efficiency of distillation systems. Areas of growth are also highlighted.

  9. DOE Will Convert Northeast Home Heating Oil Reserve to Ultra Low Sulfur Distillate

    Office of Energy Efficiency and Renewable Energy (EERE)

    The current inventory of the Northeast Home Heating Oil Reserve will be converted to cleaner burning ultra low sulfur distillate to comply with new, more stringent fuel standards by some Northeastern states, the U.S. Department of Energy said today.

  10. Pennsylvania's Comprehensive, Statewide, Pro-Active Industrial Energy

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Efficiency (E2) Program | Department of Energy Pennsylvania's Comprehensive, Statewide, Pro-Active Industrial Energy Efficiency (E2) Program Pennsylvania's Comprehensive, Statewide, Pro-Active Industrial Energy Efficiency (E2) Program Pennsylvania The U.S. Department of Energy's (DOE's) Advanced Manufacturing Office (AMO; formerly the Industrial Technologies Program) has developed multiple resources and a best practices suite of tools to help industrial manufacturers reduce their energy

  11. Conversion of LPG hydrocarbons to distillate fuels or lubes using integration of LPG dehydrogenation and mogdl

    SciTech Connect (OSTI)

    Chang, C.D.; Penick, J.E.; Socha, R.F.

    1987-07-07

    This patent describes an apparatus for producing distillates of lubes from paraffins, which comprise: (a) a dehydrogenation reactor including means for passing a paraffinic feedstock stream into a dehydrogenation zone at conditions of pressure and temperature selected to convert the paraffins to an olefin rich effluent stream comprising at least one of the group consisting of propylene and butylene; (b) a low pressure oligomerization catalytic reactor including means for contacting the olefin rich effluent stream in a low pressure oligomerization catalytic reactor zone with a crystalline zeolite oligomerization catalyst at conditions of pressure and temperature selected to convert olefins to a first reactor effluent stream rich in liquid olefinic gasoline range hydrocarbons; (c) a first means for separating the first reactor effluent stream to form a substantially liquid C/sub 5/+ rich stream and a C/sub 4/- rich stream; (d) means for passing the C/sub 5/+ rich stream to a high pressure oligomerization catalytic reactor zone; (e) a high pressure oligomerization catalytic reactor including means for contacting the substantially liquid C/sub 5/+ rich stream in the high pressure oligomerization catalytic reactor zone with a crystalline zeolite oligomerization catalyst at conditions of temperature and pressure selected to produce a second reactor effluent stream which is rich in distillate; (f) second means for separating the second reactor effluent stream to recover an olefinic gasoline stream and a distillate stream; and (g) a hydrotreating reactor including means for contacting the distillate stream with hydrogen in a hydrotreating unit to produce a hydrotreated distillate stream comprising lube range hydrocarbons.

  12. APPLICATION OF VACUUM SALT DISTILLATION TECHNOLOGY FOR THE REMOVAL OF FLUORIDE

    SciTech Connect (OSTI)

    Pierce, R.; Pak, D.

    2011-08-10

    Vacuum distillation of chloride salts from plutonium oxide (PuO{sub 2}) and simulant PuO{sub 2} has been previously demonstrated at Department of Energy (DOE) sites using kilogram quantities of chloride salt. The apparatus for vacuum distillation contains a zone heated using a furnace and a zone actively cooled using either recirculated water or compressed air. During a vacuum distillation operation, a sample boat containing the feed material is placed into the apparatus while it is cool, and the system is sealed. The system is evacuated using a vacuum pump. Once a sufficient vacuum is attained, heating begins. Volatile salts distill from the heated zone to the cooled zone where they condense, leaving behind the non-volatile materials in the feed boat. The application of vacuum salt distillation (VSD) is of interest to the HB-Line Facility and the MOX Fuel Fabrication Facility (MFFF) at the Savannah River Site (SRS). Both facilities are involved in efforts to disposition excess fissile materials. Many of these materials contain chloride and fluoride salt concentrations which make them unsuitable for dissolution without prior removal of the chloride and fluoride salts. Between September 2009 and January 2011, the Savannah River National Laboratory (SRNL) and HB-Line designed, developed, tested, and successfully deployed a system for the distillation of chloride salts. Subsequent efforts are attempting to adapt the technology for the removal of fluoride. Fluoride salts of interest are less-volatile than the corresponding chloride salts. Consequently, an alternate approach is required for the removal of fluoride without significantly increasing the operating temperature. HB-Line Engineering requested SRNL to evaluate and demonstrate the feasibility of an alternate approach using both non-radioactive simulants and plutonium-bearing materials. Whereas the earlier developments targeted the removal of sodium chloride (NaCl) and potassium chloride (KCl), the current

  13. Fuel-blending stocks from the hydrotreatment of a distillate formed by direct coal liquefaction

    SciTech Connect (OSTI)

    Andile B. Mzinyati

    2007-09-15

    The direct liquefaction of coal in the iron-catalyzed Suplex process was evaluated as a technology complementary to Fischer-Tropsch synthesis. A distinguishing feature of the Suplex process, from other direct liquefaction processes, is the use of a combination of light- and heavy-oil fractions as the slurrying solvent. This results in a product slate with a small residue fraction, a distillate/naphtha mass ratio of 6, and a 65.8 mass % yield of liquid fuel product on a dry, ash-free coal basis. The densities of the resulting naphtha (C{sub 5}-200{sup o}C) and distillate (200-400{sup o}C) fractions from the hydroprocessing of the straight-run Suplex distillate fraction were high (0.86 and 1.04 kg/L, respectively). The aromaticity of the distillate fraction was found to be typical of coal liquefaction liquids, at 60-65%, with a Ramsbottom carbon residue content of 0.38 mass %. Hydrotreatment of the distillate fraction under severe conditions (200{sup o}C, 20.3 MPa, and 0.41 g{sub feed} h{sup -1} g{sub catalyst}{sup -1}) with a NiMo/Al{sub 2}O{sub 3} catalyst gave a product with a phenol content of {lt}1 ppm, a nitrogen content {lt}200 ppm, and a sulfur content {lt}25 ppm. The temperature was found to be the main factor affecting diesel fraction selectivity when operating at conditions of WHSV = 0.41 g{sub feed} h{sup -1} g{sub catalyst}{sup -1} and PH{sub 2} = 20.3 MPa, with excessively high temperatures (T {gt} 420{sup o}C) leading to a decrease in diesel selectivity. The fuels produced by the hydroprocessing of the straight-run Suplex distillate fraction have properties that make them desirable as blending components, with the diesel fraction having a cetane number of 48 and a density of 0.90 kg/L. The gasoline fraction was found to have a research octane number (RON) of 66 and (N + 2A) value of 100, making it ideal as a feedstock for catalytic reforming and further blending with Fischer-Tropsch liquids. 44 refs., 9 figs., 12 tabs.

  14. Future perspectives of using hollow fibers as structured packings in light hydrocarbon distillation

    SciTech Connect (OSTI)

    Yang, Dali; Orler, Bruce; Tornga, Stephanie; Welch, Cindy

    2011-01-26

    Olefin and paraffin are the largest chemical commodities. Furthermore, they are major building blocks for the petrochemical industry. Each year, petroleum refining, consumes 4,500 TBtu/yr in separation energy, making it one of the most energy-intensive industries in the United States). Just considering liquefied petroleum gas (ethane/propane/butane) and olefins (ethylene and propylene) alone, the distillation energy consumption is about 400 TBtu/yr in the US. Since petroleum distillation is a mature technology, incremental improvements in column/tray design will only provide a few percent improvements in the performance. However, each percent saving in net energy use amounts to savings of 10 TBtu/yr and reduces CO{sub 2} emissions by 0.2 MTon/yr. In practice, distillation columns require 100 to 200 trays to achieve the desired separation. The height of a transfer unit (HTU) of conventional packings is typical in the range of 36-60 inch. Since 2006, we had explored using several non-selective membranes as the structured packings to replace the conventional packing materials used in propane and propylene distillation. We obtained the lowest HTU of < 8 inch for the hollow fiber column, which was >5 times shorter than that of the conventional packing materials. In 2008, we also investigated this type of packing materials in iso-/n-butane distillation. Because of a slightly larger relative volatility of iso-/n-butane than that of propane/propylene, a wider and a more stable operational range was obtained for the iso-/n-butane pair. However, all of the experiments were conducted on a small scale with flowrate of < 25 gram/min. Recently, we demonstrated this technology on a larger scale (<250 gram/min). Within the loading range of F-factor < 2.2 Pa{sup 0.5}, a pressure drop on the vapor side is below 50 mbar/m, which suggests that the pressure drop of hollow fibers packings is not an engineering barrier for the applications in distillations. The thermal stability study

  15. GeoPro: Technology to Enable Scientific Modeling

    SciTech Connect (OSTI)

    C. Juan

    2004-02-09

    Development of the ground-water flow model for the Death Valley Regional Groundwater Flow System (DVRFS) required integration of numerous supporting hydrogeologic investigations. The results from recharge, discharge, hydraulic properties, water level, pumping, model boundaries, and geologic studies were integrated to develop the required conceptual and 3-D framework models, and the flow model itself. To support the complex modeling process and the needs of the multidisciplinary DVRFS team, a hardware and software system called GeoPro (Geoscience Knowledge Integration Protocol) was developed. A primary function of GeoPro is to manage the large volume of disparate data compiled for the 100,000-square-kilometer area of southern Nevada and California. The data are primarily from previous investigations and regional flow models developed for the Nevada Test Site and Yucca Mountain projects. GeoPro utilizes relational database technology (Microsoft SQL Server{trademark}) to store and manage these tabular point data, groundwater flow model ASCII data, 3-D hydrogeologic framework data, 2-D and 2.5-D GIS data, and text documents. Data management consists of versioning, tracking, and reporting data changes as multiple users access the centralized database. GeoPro also supports the modeling process by automating the routine data transformations required to integrate project software. This automation is also crucial to streamlining pre- and post-processing of model data during model calibration. Another function of GeoPro is to facilitate the dissemination and use of the model data and results through web-based documents by linking and allowing access to the underlying database and analysis tools. The intent is to convey to end-users the complex flow model product in a manner that is simple, flexible, and relevant to their needs. GeoPro is evolving from a prototype system to a production-level product. Currently the DVRFS pre- and post-processing modeling tools are being re

  16. Conversion of LPG hydrocarbons into distillate fuels using an integral LPG dehydrogenation-MOGD process

    SciTech Connect (OSTI)

    Owen, H.; Zahner, J.C.

    1987-06-23

    This patent describes a process for converting lower paraffinic hydrocarbon feedstock comprising propane and/or butane into heavier hydrocarbons comprising gasoline and distillate, comprising the steps of: feeding the paraffinic feedstock to a dehydrogenation zone under conversion conditions for dehydrogenating at least a portion of the feedstock; recovering a first dehydrogenation gaseous effluent stream comprising propene and/or butene; contacting the first gaseous effluent steam with a liquid lean oil sorbent stream comprising C/sub 5//sup +/ hydrocarbons under sorption conditions to produce a C/sub 3//sup +/ rich liquid absorber stream and a light gas stream; sequentially pressurizing, heating and passing the C/sub 3//sup +/ rich liquid absorber stream to an oligomerization reactor zone at elevated temperature and pressure; contacting the C/sub 3//sup +/ rich stream with oligomerization catalyst in the oligomerization reactor zone for conversion of at least a portion of lower olefins to heavier hydrocarbons under oligomerization reaction conditions to provide a second reactor effluent stream comprising gasoline and distillate boiling range hydrocarbons; flash separating the second reactor effluent stream into a separator vapor stream comprising a major portion of the hydrocarbons which later form the lean oil stream, and a major portion of the C/sub 4//sup -/ hydrocarbons and a separator liquid stream comprising the gasoline and distillate boiling range materials produced in the oligomerization reactor zone; fractionating the separator liquid stream in a first product debutanizer tower into a first debutanizer overhead vapor stream comprising C/sub 4//sup -/ hydrocarbons and a product debutanizer liquid bottoms stream comprising C/sub 5//sup +/ gasoline and distillate boiling range hydrocarbons.

  17. Composition-explicit distillation curves of aviation fuel JP-8 and a coal-based jet fuel

    SciTech Connect (OSTI)

    Beverly L. Smith; Thomas J. Bruno

    2007-09-15

    We have recently introduced several important improvements in the measurement of distillation curves for complex fluids. The modifications to the classical measurement provide for (1) a composition explicit data channel for each distillate fraction (for both qualitative and quantitative analysis); (2) temperature measurements that are true thermodynamic state points; (3) temperature, volume, and pressure measurements of low uncertainty suitable for an equation of state development; (4) consistency with a century of historical data; (5) an assessment of the energy content of each distillate fraction; (6) a trace chemical analysis of each distillate fraction; and (7) a corrosivity assessment of each distillate fraction. The most significant modification is achieved with a new sampling approach that allows precise qualitative as well as quantitative analyses of each fraction, on the fly. We have applied the new method to the measurement of rocket propellant, gasoline, and jet fuels. In this paper, we present the application of the technique to representative batches of the military aviation fuel JP-8, and also to a coal-derived fuel developed as a potential substitute. We present not only the distillation curves but also a chemical characterization of each fraction and discuss the contrasts between the two fluids. 26 refs., 5 figs., 6 tabs.

  18. MEMS Pro Design Kit - Parts A, B, and C

    Energy Science and Technology Software Center (OSTI)

    2006-06-15

    Part A: SUMMiT V design Kit components for use with MEMS Pro from SoftMEMS Part B: SUMMiT V remote DRC and gear generator source code for use with autocad visual basic Part C: SUMMiT V DRC rules source and test cases for Calibre DRC engine

  19. Vacuum Distillation

    U.S. Energy Information Administration (EIA) (indexed site)

    Thermal Cracking: OtherGas Oil Thermal Cracking: Coking (BarrelsCalendar Day) Catalytic Cracking Fresh Feed Catalytic Cracking Fresh Feed (BarrelsCalendar Day) Catalytic ...

  20. Design, start up, and three years operating experience of an ammonia scrubbing, distillation, and destruction plant

    SciTech Connect (OSTI)

    Gambert, G.

    1996-12-31

    When the rebuilt Coke Plant started operations in November of 1992, it featured a completely new closed circuit secondary cooler, ammonia scrubbing, ammonia distillation, and ammonia destruction plants. This is the second plant of this type to be built in North America. To remove the ammonia from the gas, it is scrubbed with three liquids: Approximately 185 gallons/minute of cooled stripped liquor from the ammonia stills; Light oil plant condensate; and Optionally, excess flushing liquor. These scrubbers typically reduce ammonia content in the gas from 270 Grains/100 standard cubic feet to 0.2 Grains/100 standard cubic feet.

  1. ,"U.S. Adjusted Distillate Fuel Oil and Kerosene Sales by End Use"

    U.S. Energy Information Administration (EIA) (indexed site)

    Distillate Fuel Oil and Kerosene Sales by End Use" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Residential",4,"Annual",2014,"6/30/1984" ,"Data 2","Commercial",10,"Annual",2014,"6/30/1984" ,"Data

  2. ,"U.S. Distillate Fuel Oil and Kerosene Sales by End Use"

    U.S. Energy Information Administration (EIA) (indexed site)

    Distillate Fuel Oil and Kerosene Sales by End Use" ,"Click worksheet name or tab at bottom for data" ,"Worksheet Name","Description","# Of Series","Frequency","Latest Data for" ,"Data 1","Residential",4,"Annual",2014,"6/30/1984" ,"Data 2","Commercial",10,"Annual",2014,"6/30/1984" ,"Data

  3. VWA-0015- In the Matter of Am-Pro Protective Services, Inc.

    Office of Energy Efficiency and Renewable Energy (EERE)

    This Initial Agency Decision concerns a whistleblower complaint filed by Barry Stutts, a former security officer for Am-Pro Protective Services, Inc. (Am-Pro). It is undisputed that: Mr. Stutts and...

  4. PIA - Savannah River Nuclear Solution SRNS ProRad Environment Management |

    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Department of Energy SRNS ProRad Environment Management PIA - Savannah River Nuclear Solution SRNS ProRad Environment Management PIA - Savannah River Nuclear Solution SRNS ProRad Environment Management PIA - Savannah River Nuclear Solution SRNS ProRad Environment Management (3.45 MB) More Documents & Publications PIA - Savannah River Nuclear Solutions (SRNS) Human Resource Management System (HRMS) PIA - Savannah River Nuclear Solution (SRNS) Procurement Cycle System (PCS) PIA - Savannah

  5. Synthesis of zeolite from Italian coal fly ash: Differences in crystallization temperature using seawater instead of distilled water

    SciTech Connect (OSTI)

    Belviso, Claudia; Cavalcante, Francesco; Fiore, Saverio

    2010-05-15

    In this study Italian coal fly ash was converted into several types of zeolite in laboratory experiments with temperatures of crystallization ranging from 35 up to 90 deg. C. Distilled and seawater were used during the hydrothermal synthesis process in separate experiments, after a pre-treatment fusion with NaOH. The results indicate that zeolites could be formed from different kind of Italian coal fly ash at low temperature of crystallization using both distilled and seawater. SEM data and the powder patterns of X-ray diffraction analysis show that faujasite, zeolite ZK-5 and sodalite were synthesized when using both distilled and seawater; zeolite A crystallized only using distilled water. In particular the experiments indicate that the synthesis of zeolite X and zeolite ZK-5 takes place at lower temperatures when using seawater (35 and 45 deg. C, respectively). The formation of sodalite is always competitive with zeolite X which shows a metastable behaviour at higher temperatures (70-90 deg. C). The chemical composition of the fly ash source could be responsible of the differences on the starting time of synthesized zeolite with distilled water, in any case our data show that the formation of specific zeolites takes place always at lower temperatures when using seawater.

  6. Advanced Multi-Effect Distillation System for Desalination Using Waste Heat fromGas Brayton Cycles

    SciTech Connect (OSTI)

    Haihua Zhao; Per F. Peterson

    2012-10-01

    Generation IV high temperature reactor systems use closed gas Brayton Cycles to realize high thermal efficiency in the range of 40% to 60%. The waste heat is removed through coolers by water at substantially greater average temperature than in conventional Rankine steam cycles. This paper introduces an innovative Advanced Multi-Effect Distillation (AMED) design that can enable the production of substantial quantities of low-cost desalinated water using waste heat from closed gas Brayton cycles. A reference AMED design configuration, optimization models, and simplified economics analysis are presented. By using an AMED distillation system the waste heat from closed gas Brayton cycles can be fully utilized to desalinate brackish water and seawater without affecting the cycle thermal efficiency. Analysis shows that cogeneration of electricity and desalinated water can increase net revenues for several Brayton cycles while generating large quantities of potable water. The AMED combining with closed gas Brayton cycles could significantly improve the sustainability and economics of Generation IV high temperature reactors.

  7. Integrated hydroprocessing scheme for production of premium quality distillates and lubricants

    SciTech Connect (OSTI)

    Chen, N.Y.; LaPierre, R.B.; Partridge, R.D.; Wong, S.S.

    1989-07-25

    This patent describes a method of upgrading a gas oil hydrocarbon feedstock into a naphtha product and a distillate product having a boiling range above that of the naptha product and below that of the gas oil and also having content of iso-paraffins. The method comprises hydrocracking the gas oil feedstock over a large pore size, aromatic selective hydrocracking catalyst having acidic functionality and hydrogenation-deydrogenation functionality, at a hydrogen pressure up to about 10,000 kPa and at a conversion below 50 percent to 650{sup 0}F.-products, to effects a removal of aromatic components by hydrocracking and to form the naptha product and a product boiling above the naptha product which is enriched in paraffinic components; separating the naptha product from the product enriched in paraffinic components; and hydroprocessing the product enriched in paraffinic components over a hydroprocessing catalyst comprising zeolite beta as an acidic component and a hydrogenation-dehydrogenation component, to produce a distillate boiling range product having an enhanced content of isoparaffinic components.

  8. Rotation Manager Pro Version 1.0b1

    Energy Science and Technology Software Center (OSTI)

    2002-02-01

    The Rotation Manager Pro Package maintains databases of instructions to replicate plate tectonic movements. The instructions are in the standard of tectonic plate rotations, including plate identification and location and angle of the rotation pole. Each database is accompanied by various metadata, including information about each rotation pole and the database itself. The package provides a range of tools to actively manage the database using methods specifically required for rotations: rotation pole addition and subtraction,more » viewing of a rotation chain through the rotation hierarchy, and the rotation of data points.« less

  9. Distillation efficiencies of an industrial-scale i-butane/n-butane fractionator

    SciTech Connect (OSTI)

    Klemola, K.T.; Ilme, J.K.

    1996-12-01

    Rarely published industrial-scale distillation efficiency data are presented. The Murphree tray efficiencies are determined from the i-butane/n-butane fractionator performance data. Point efficiencies, numbers of overall vapor phase transfer units, numbers of vapor and liquid phase transfer units, and liquid phase resistances of mass transfer are backcalculated from the Murphree tray efficiencies. Various efficiency prediction and scale-up methods have been tested against experimental results. A new model for the prediction of the numbers of vapor and liquid phase transfer units has been developed. The model can be applied to hydrocarbon systems at high pressure. The influence of the mass-transfer coefficients, the interfacial area, and the vapor and liquid residence times on mass transfer has been analyzed separately, and as a result the NTU correlations for vapor and liquid phases are obtained. The constants of the model can be obtained by fitting the model to experimental efficiency data from a similar system.

  10. V-210: HP LaserJet Pro Printer Bug Lets Remote Users Access Data

    Energy.gov [DOE]

    A potential security vulnerability has been identified with certain HP LaserJet Pro printers. The vulnerability could be exploited remotely to gain unauthorized access to data.

  11. Clean Cities Guide to Alternative Fuel and Advanced Medium- and...

    Alternative Fuels and Advanced Vehicles Data Center

    ... in the presence of a catalyst to convert smog-forming NOx into nitrogen and water vapor . ... In addition, pro- pane is nontoxic, so it isn't harmful to soil or water when spilled or ...

  12. Thermodynamic assessment of the Pr-O system

    SciTech Connect (OSTI)

    McMurray, Jake W.

    2015-12-24

    We found that the Calphad method was used to perform a thermodynamic assessment of the Pr–O system. Compound energy formalism representations were developed for the fluorite α-PrO 2–x and bixbyite σ-Pr 3 O 5 ± x solid solutions while the two-sublattice liquid model was used to describe the binary melt. The series of phases between Pr 2 O 3 and PrO 2 were taken to be stoichiometric. Moreover, the equilibrium oxygen pressure, phase equilibria, and enthalpy data were used to optimize the adjustable parameters of the models for a self-consistent representation of the thermodynamic behavior of the Pr–O system from 298 K to melting.

  13. Thermodynamic assessment of the Pr-O system

    DOE PAGES-Beta [OSTI]

    McMurray, Jake W.

    2015-12-24

    We found that the Calphad method was used to perform a thermodynamic assessment of the Pr–O system. Compound energy formalism representations were developed for the fluorite α-PrO 2–x and bixbyite σ-Pr 3 O 5 ± x solid solutions while the two-sublattice liquid model was used to describe the binary melt. The series of phases between Pr 2 O 3 and PrO 2 were taken to be stoichiometric. Moreover, the equilibrium oxygen pressure, phase equilibria, and enthalpy data were used to optimize the adjustable parameters of the models for a self-consistent representation of the thermodynamic behavior of the Pr–O system frommore » 298 K to melting.« less

  14. Recovery of Navy distillate fuel from reclaimed product. Volume II. Literature review

    SciTech Connect (OSTI)

    Brinkman, D.W.; Whisman, M.L.

    1984-11-01

    In an effort to assist the Navy to better utilize its waste hydrocarbons, NIPER, with support from the US Department of Energy, is conducting research designed to ultimately develop a practical technique for converting Reclaimed Product (RP) into specification Naval Distillate Fuel (F-76). This first phase of the project was focused on reviewing the literature and available information from equipment manufacturers. The literature survey has been carefully culled for methodology applicable to the conversion of RP into diesel fuel suitable for Navy use. Based upon the results of this study, a second phase has been developed and outlined in which experiments will be performed to determine the most practical recycling technologies. It is realized that the final selection of one particular technology may be site-specific due to vast differences in RP volume and available facilities. A final phase, if funded, would involve full-scale testing of one of the recommended techniques at a refueling depot. The Phase I investigations are published in two volumes. Volume 1, Technical Discussion, includes the narrative and Appendices I and II. Appendix III, a detailed Literature Review, includes both a narrative portion and an annotated bibliography containing about 800 references and abstracts. This appendix, because of its volume, has been published separately as Volume 2.

  15. "Table A2. Total Consumption of LPG, Distillate Fuel Oil, and Residual Fuel"

    U.S. Energy Information Administration (EIA) (indexed site)

    . Total Consumption of LPG, Distillate Fuel Oil, and Residual Fuel" " Oil for Selected Purposes by Census Region, Industry Group, and Selected" " Industries, 1991" " (Estimates in Barrels per Day) " ,,,,," Input for Heat,",,," Primary" " ",," Consumption for All Purposes",,,"Power, and Generation of Electricity",,," Consumption for Nonfuel Purposes ",,,"RSE" "SIC",,"

  16. Catalytic hydroprocessing of SRC-II heavy distillate fractions. 4. Hydrodeoxygenation of phenolic compounds in the acidic fractions

    SciTech Connect (OSTI)

    Li, C.L.

    1985-01-01

    Heavy distillate obtained by hydroliquefaction of Powhatan No.5 coal was separated into 9 fractions by liquid chromatography. The very-weak-acid and weak-acid fractions were used as feeds in hydroprocessing experiments with sulphided Ni-Mo/Al/sub 2/O/sub 3/ catalyst at 350 C and 120 atm. The hydrodeoxygenation of the acidic compounds was shown to be rapid in comparison with other hydroprocessing reactions of coal liquids, including hydrogenation of aromatics, hydrodesulphurisation and hydrodenitrogenation.

  17. Cryogenic distillation: a fuel enrichment system for near-term tokamak-type D-T fusion reactors

    SciTech Connect (OSTI)

    Misra, B.; Davis, J.F.

    1980-02-01

    The successful operation and economic viability of deuterium-tritium- (D-T-) fueled tokamak-type commercial power fusion reactors will depend to a large extent on the development of reliable tritium-containment and fuel-recycle systems. Of the many operating steps in the fuel recycle scheme, separation or enrichment of the isotropic species of hydrogen by cryogenic distillation is one of the most important. A parametric investigation was carried out to study the effects of the various operating conditions and the composition of the spent fuel on the degree of separation. A computer program was developed for the design and analysis of a system of interconnected distillation columns for isotopic separation such that the requirements of near-term D-T-fueled reactors are met. The analytical results show that a distillation cascade consisting of four columns is capable of reprocessing spent fuel varying over a wide range of compositions to yield reinjection-grade fuel with essentially unlimited D/T ratio.

  18. BERLinPro Booster Cavity Design, Fabrication and Test Plans

    SciTech Connect (OSTI)

    Burrill, Andrew; Anders, W; Frahm, A.; Knobloch, Jens; Neumann, Axel; Ciovati, Gianluigi; Kneisel, Peter K.; Turlington, Larry D.

    2014-12-01

    The bERLinPro project, a 100 mA, 50 MeV superconducting RF (SRF) Energy Recovery Linac (ERL) is under construction at Helmholtz-Zentrum Berlin for the purpose of studying the technical challenges and physics of operating a high current, c.w., 1.3 GHz ERL. This machine will utilize three unique SRF cryomodules for the injector, booster and linac module respectively. The booster cryomodule will contain three 2-cell SRF cavities, based on the original design by Cornell University, and will be equipped with twin 115 kW RF power couplers in order to provide the appropriate acceleration to the high current electron beam. This paper will review the status of the fabrication of the 4 booster cavities that have been built for this project by Jefferson Laboratory and look at the challenges presented by the incorporation of fundamental power couplers capable of delivering 115 kW. The test plan for the cavities and couplers will be given along with a brief overview of the cryomodule design.

  19. Evaluation of Exxon donor solvent full-range distillate as a utility boiler fuel. Final report

    SciTech Connect (OSTI)

    Reese, J.; Folsom, B.; Jones, F.

    1984-03-01

    The use of Exxon Donor Solvent (EDS) as a utility boiler fuel was evaluated at Southern California Edison Company's Highgrove Unit 4, a Combustion Engineering 44.5 net Mw wall-fired boiler. The EDS evaluated was a full range solvent oil produced at the Exxon Coal-Liquefaction Pilot Plant in Baytown, Texas. This evaluation involved modifying the boiler equipment and operating procedures for EDS, and then firing 4500 barrels of EDS in the boiler. The resulting boiler performance and emissions with EDS were compared to those with a blended low-sulfur petroleum distillate similar to No. 4 fuel oil and with natural gas. The boiler was operated over a range of load and excess air conditions during the tests. The potential for NO/sub x/ reduction with a burner out of service (BOOS) was also evaluated. Boiler performance, including excess air requirements, maximum load, thermal efficiency and heat rate efficiency was similar to that with oil. The NO/sub x/ emissions with EDS were about 12 percent higher than with oil. NO/sub x/ reduction with BOOS was about 20 percent with both oil and EDS. EDS use did not result in an increase in particulate emissions. Submicron particulate, however, was increased with EDS. Required equipment modifications at Highgrove primarily involved material compatibility with EDS, fuel system capacity, and the burner nozzles. The use of EDS required the implementation of health and safety procedures due to the adverse health effects that could result from prolonged exposure to the fuel. The results of the evaluation demostrated that EDS can be used in a utility boiler designed for oil with only minor modifications.

  20. Update of distillers grains displacement ratios for corn ethanol life-cycle analysis.

    SciTech Connect (OSTI)

    Arora, S.; Wu, M.; Wang, M.; Energy Systems

    2011-02-01

    Production of corn-based ethanol (either by wet milling or by dry milling) yields the following coproducts: distillers grains with solubles (DGS), corn gluten meal (CGM), corn gluten feed (CGF), and corn oil. Of these coproducts, all except corn oil can replace conventional animal feeds, such as corn, soybean meal, and urea. Displacement ratios of corn-ethanol coproducts including DGS, CGM, and CGF were last updated in 1998 at a workshop at Argonne National Laboratory on the basis of input from a group of experts on animal feeds, including Prof. Klopfenstein (University of Nebraska, Lincoln), Prof. Berger (University of Illinois, Urbana-Champaign), Mr. Madson (Rapheal Katzen International Associates, Inc.), and Prof. Trenkle (Iowa State University) (Wang 1999). Table 1 presents current dry milling coproduct displacement ratios being used in the GREET model. The current effort focuses on updating displacement ratios of dry milling corn-ethanol coproducts used in the animal feed industry. Because of the increased availability and use of these coproducts as animal feeds, more information is available on how these coproducts replace conventional animal feeds. To glean this information, it is also important to understand how industry selects feed. Because of the wide variety of available feeds, animal nutritionists use commercial software (such as Brill Formulation{trademark}) for feed formulation. The software recommends feed for the animal on the basis of the nutritional characteristics, availability, and price of various animal feeds, as well as on the nutritional requirements of the animal (Corn Refiners Association 2006). Therefore, feed formulation considers both the economic and the nutritional characteristics of feed products.

  1. Analysis of Oxygenated Compounds in Hydrotreated Biomass Fast Pyrolysis Oil Distillate Fractions

    SciTech Connect (OSTI)

    Christensen, Earl D.; Chupka, Gina; Luecke, Jon; Smurthwaite, Tricia D.; Alleman, Teresa L.; Iisa, Kristiina; Franz, James A.; Elliott, Douglas C.; McCormick, Robert L.

    2011-10-06

    Three hydrotreated bio-oils with different oxygen contents (8.2, 4.9, and 0.4 w/w) were distilled to produce Light, Naphtha, Jet, Diesel, and Gasoil boiling range fractions that were characterized for oxygen containing species by a variety of analytical methods. The bio-oils were originally generated from lignocellulosic biomass in an entrained-flow fast pyrolysis reactor. Analyses included elemental composition, carbon type distribution by {sup 13}C NMR, acid number, GC-MS, volatile organic acids by LC, and carbonyl compounds by DNPH derivatization and LC. Acid number titrations employed an improved titrant-electrode combination with faster response that allowed detection of multiple endpoints in many samples and for acid values attributable to carboxylic acids and to phenols to be distinguished. Results of these analyses showed that the highest oxygen content bio-oil fractions contained oxygen as carboxylic acids, carbonyls, aryl ethers, phenols, and alcohols. Carboxylic acids and carbonyl compounds detected in this sample were concentrated in the Light, Naphtha, and Jet fractions (<260 C boiling point). Carboxylic acid content of all of the high oxygen content fractions was likely too high for these materials to be considered as fuel blendstocks although potential for blending with crude oil or refinery intermediate streams may exist for the Diesel and Gasoil fractions. The 4.9 % oxygen sample contained almost exclusively phenolic compounds found to be present throughout the boiling range of this sample, but imparting measurable acidity primarily in the Light, Naphtha and Jet fractions. Additional study is required to understand what levels of the weakly acidic phenols could be tolerated in a refinery feedstock. The Diesel and Gasoil fractions from this upgraded oil had low acidity but still contained 3 to 4 wt% oxygen present as phenols that could not be specifically identified. These materials appear to have excellent potential as refinery feedstocks and some

  2. DC Pro Software Tool Suite, Data Center Fact Sheet, Industrial Technologies Program

    SciTech Connect (OSTI)

    Not Available

    2009-04-01

    This fact sheet describes how DOE's Data Center Energy Profiler (DC Pro) Software Tool Suite and other resources can help U.S. companies identify ways to improve the efficiency of their data centers.

  3. VWA-0015- Deputy Secretary Decision- In the Matter of Am-Pro Protective Services, Inc.

    Energy.gov [DOE]

    Barry Stutts, Complainant v. Am-Pro Protective Agency, Inc., Respondent, OHA Case No. VWA-0015 DECISION DENYING REVIEW OF INITIAL AGENCY DECISION This is a request for review by Complainant Barry...

  4. ProForce marks 65 years protecting Sandia resources, facilities, people |

    National Nuclear Security Administration (NNSA)

    National Nuclear Security Administration | (NNSA) ProForce marks 65 years protecting Sandia resources, facilities, people Monday, October 26, 2015 - 12:00am NNSA Blog Current and former members of the Lab's Protective Force gathered to reflect on and recognize the contributions ProForce has made to securing Sandia National Laboratory's resources, facilities, and people. Over the past 65 years, the force has changed in size and structure but its mission has remained the same: To ensure the

  5. Waste Heat Recovery and Recycling in Thermal Separation Processes: Distillation, Multi-Effect Evaporation (MEE) and Crystallization Processes

    SciTech Connect (OSTI)

    Emmanuel A. Dada; Chandrakant B. Panchal; Luke K. Achenie; Aaron Reichl; Chris C. Thomas

    2012-12-03

    Evaporation and crystallization are key thermal separation processes for concentrating and purifying inorganic and organic products with energy consumption over 1,000 trillion Btu/yr. This project focused on a challenging task of recovering low-temperature latent heat that can have a paradigm shift in the way thermal process units will be designed and operated to achieve high-energy efficiency and significantly reduce the carbon footprint as well as water footprint. Moreover, this project has evaluated the technical merits of waste-heat powered thermal heat pumps for recovery of latent heat from distillation, multi-effect evaporation (MEE), and crystallization processes and recycling into the process. The Project Team has estimated the potential energy, economics and environmental benefits with the focus on reduction in CO2 emissions that can be realized by 2020, assuming successful development and commercialization of the technology being developed. Specifically, with aggressive industry-wide applications of heat recovery and recycling with absorption heat pumps, energy savings of about 26.7 trillion Btu/yr have been estimated for distillation process. The direct environmental benefits of this project are the reduced emissions of combustible products. The estimated major reduction in environmental pollutants in the distillation processes is in CO2 emission equivalent to 3.5 billion lbs/year. Energy consumption associated with water supply and treatments can vary between 1,900 kWh and 23,700 kWh per million-gallon water depending on sources of natural waters [US DOE, 2006]. Successful implementation of this technology would significantly reduce the demand for cooling-tower waters, and thereby the use and discharge of water treatment chemicals. The Project Team has also identified and characterized working fluid pairs for the moderate-temperature heat pump. For an MEE process, the two promising fluids are LiNO3+KNO3+NANO3 (53:28:19 ) and LiNO3+KNO3+NANO2

  6. Hollow Fibers Structured Packings in Olefin/Paraffin Distillation: Apparatus Scale-Up and Long-Term Stability

    DOE PAGES-Beta [OSTI]

    Yang, Dali; Le, Loan; Martinez, Ronald; Morrison, Malcolm

    2013-06-21

    Following the conceptual demonstration of high separation efficiency and column capacity obtained in olefin/paraffin distillation using hollow fiber structured packings (HFSPs) in a bench scale (J. Membr. Sci.2006, 2007, and 2010), we scaled-up this process with a 10-fold increase in the internal flow rate and a 3-fold increase in the module length. We confirmed that the HFSPs technology gives high separation efficiency and column capacity in iso-/n-butane distillation for 18 months. We systematically investigated the effects of packing density, concentration of light component, reflux ratio, and module age on the separation efficiency and operating stability. The comprehensive characterizations using scanningmore » electron microscopy (SEM), Brunauer–Emmett–Teller (BET), thermogravimetric analysis (TGA), differential scanning calorimetry (DSC), and dynamic mechanical analysis (DMA) were carried out to probe the changes in the morphological, thermal, and mechanical properties of polypropylene (PP) hollow fibers over the aging process. Our results suggest that after a long-term exposure to light hydrocarbon environments at ≤70 °C the morphological and mechanical properties of the PP polymer do not degrade significantly in a propane/propylene and iso-/n-butane environment.« less

  7. Hollow Fibers Structured Packings in Olefin/Paraffin Distillation: Apparatus Scale-Up and Long-Term Stability

    SciTech Connect (OSTI)

    Yang, Dali; Le, Loan; Martinez, Ronald; Morrison, Malcolm

    2013-06-21

    Following the conceptual demonstration of high separation efficiency and column capacity obtained in olefin/paraffin distillation using hollow fiber structured packings (HFSPs) in a bench scale (J. Membr. Sci.2006, 2007, and 2010), we scaled-up this process with a 10-fold increase in the internal flow rate and a 3-fold increase in the module length. We confirmed that the HFSPs technology gives high separation efficiency and column capacity in iso-/n-butane distillation for 18 months. We systematically investigated the effects of packing density, concentration of light component, reflux ratio, and module age on the separation efficiency and operating stability. The comprehensive characterizations using scanning electron microscopy (SEM), Brunauer–Emmett–Teller (BET), thermogravimetric analysis (TGA), differential scanning calorimetry (DSC), and dynamic mechanical analysis (DMA) were carried out to probe the changes in the morphological, thermal, and mechanical properties of polypropylene (PP) hollow fibers over the aging process. Our results suggest that after a long-term exposure to light hydrocarbon environments at ≤70 °C the morphological and mechanical properties of the PP polymer do not degrade significantly in a propane/propylene and iso-/n-butane environment.

  8. Cancer Associated Fibroblasts express pro-inflammatory factors in human breast and ovarian tumors

    SciTech Connect (OSTI)

    Erez, Neta; Glanz, Sarah; Raz, Yael; Avivi, Camilla; Barshack, Iris

    2013-08-02

    Highlights: •CAFs in human breast and ovarian tumors express pro-inflammatory factors. •Expression of pro-inflammatory factors correlates with tumor invasiveness. •Expression of pro-inflammatory factors is associated with NF-κb activation in CAFs. -- Abstract: Inflammation has been established in recent years as a hallmark of cancer. Cancer Associated Fibroblasts (CAFs) support tumorigenesis by stimulating angiogenesis, cancer cell proliferation and invasion. We previously demonstrated that CAFs also mediate tumor-enhancing inflammation in a mouse model of skin carcinoma. Breast and ovarian carcinomas are amongst the leading causes of cancer-related mortality in women and cancer-related inflammation is linked with both these tumor types. However, the role of CAFs in mediating inflammation in these malignancies remains obscure. Here we show that CAFs in human breast and ovarian tumors express high levels of the pro-inflammatory factors IL-6, COX-2 and CXCL1, previously identified to be part of a CAF pro-inflammatory gene signature. Moreover, we show that both pro-inflammatory signaling by CAFs and leukocyte infiltration of tumors are enhanced in invasive ductal carcinoma as compared with ductal carcinoma in situ. The pro-inflammatory genes expressed by CAFs are known NF-κB targets and we show that NF-κB is up-regulated in breast and ovarian CAFs. Our data imply that CAFs mediate tumor-promoting inflammation in human breast and ovarian tumors and thus may be an attractive target for stromal-directed therapeutics.

  9. A characterization and evaluation of coal liquefaction process streams. The kinetics of coal liquefaction distillation resid conversion

    SciTech Connect (OSTI)

    Klein, M.T.; Calkins, W.H.; Huang, H.; Wang, S.; Campbell, D.

    1998-03-01

    Under subcontract from CONSOL Inc., the University of Delaware studied the mechanism and kinetics of coal liquefaction resid conversion. The program at Delaware was conducted between August 15, 1994, and April 30, 1997. It consisted of two primary tasks. The first task was to develop an empirical test to measure the reactivity toward hydrocracking of coal-derived distillation resids. The second task was to formulate a computer model to represent the structure of the resids and a kinetic and mechanistic model of resid reactivity based on the structural representations. An introduction and Summary of the project authored by CONSOL and a report of the program findings authored by the University of Delaware researchers are presented here.

  10. Photo of the Week: The First Energy-Efficient Dual-Paned Windows...

    Energy.gov (indexed) [DOE]

    Sarah Gerrity Sarah Gerrity Former Multimedia Editor, Office of Public Affairs Every week, we'll feature our favorite energy-related photo here on Energy.gov, at Facebook.com...

  11. Genome Sequences of Industrially Relevant Saccharomyces cerevisiae Strain M3707, Isolated from a Sample of Distillers Yeast and Four Haploid Derivatives

    SciTech Connect (OSTI)

    Brown, Steven D.; Klingeman, Dawn M.; Johnson, Courtney M.; Clum, Alicia; Aerts, Andrea; Salamov, Asaf; Sharma, Aditi; Zane, Matthew; Barry, Kerrie; Grigoriev, Igor V.; Davison, Brian H.; Lynd, Lee R.; Gilna, Paul; Hau, Heidi; Hogsett, David A.; Froehlich, Allan C.

    2013-04-19

    Saccharomyces cerevisiae strain M3707 was isolated from a sample of commercial distillers yeast, and its genome sequence together with the genome sequences for the four derived haploid strains M3836, M3837, M3838, and M3839 has been determined. Yeasts have potential for consolidated bioprocessing (CBP) for biofuel production, and access to these genome sequences will facilitate their development.

  12. T-534: Vulnerability in the PDF distiller of the BlackBerry Attachment Service for the BlackBerry Enterprise Server

    Energy.gov [DOE]

    BlackBerry advisory describes a security issue that the BlackBerry Attachment Service component of the BlackBerry Enterprise Server is susceptible to. The issue relates to a known vulnerability in the PDF distiller component of the BlackBerry Attachment Service that affects how the BlackBerry Attachment Service processes PDF files.

  13. Geothermal Energy Market Study on the Atlantic Coastal Plain: Technical Feasibility of use of Eastern Geothermal Energy in Vacuum Distillation of Ethanol Fuel

    SciTech Connect (OSTI)

    1981-04-01

    The DOE is studying availability, economics, and uses of geothermal energy. These studies are being conducted to assure maximum cost-effective use of geothermal resources. The DOE is also aiding development of a viable ethanol fuel industry. One important point of the ethanol program is to encourage use of non-fossil fuels, such as geothermal energy, as process heat to manufacture ethanol. Geothermal waters available in the eastern US tend to be lower in temperature (180 F or less) than those available in the western states (above 250 F). Technically feasible use of eastern geothermal energy for ethanol process heat requires use of technology that lowers ethanol process temperature requirements. Vacuum (subatmospheric) distillation is one such technology. This study, then, addresses technical feasibility of use of geothermal energy to provide process heat to ethanol distillation units operated at vacuum pressures. They conducted this study by performing energy balances on conventional and vacuum ethanol processes of ten million gallons per year size. Energy and temperature requirements for these processes were obtained from the literature or were estimated (for process units or technologies not covered in available literature). Data on available temperature and energy of eastern geothermal resources was obtained from the literature. These data were compared to ethanol process requirements, assuming a 150 F geothermal resource temperature. Conventional ethanol processes require temperatures of 221 F for mash cooking to 240 F for stripping. Fermentation, conducted at 90 F, is exothermic and requires no process heat. All temperature requirements except those for fermentation exceed assumed geothermal temperatures of 150 F. They assumed a 130 millimeter distillation pressure for the vacuum process. It requires temperatures of 221 F for mash cooking and 140 F for distillation. Data indicate lower energy requirements for the vacuum ethanol process (30 million BTUs per

  14. Single-Step Syngas-to-Distillates (S2D) Synthesis via Methanol and Dimethyl Ether Intermediates: Final Report

    SciTech Connect (OSTI)

    Dagle, Robert A.; Lebarbier, Vanessa MC; Lizarazo Adarme, Jair A.; King, David L.; Zhu, Yunhua; Gray, Michel J.; Jones, Susanne B.; Biddy, Mary J.; Hallen, Richard T.; Wang, Yong; White, James F.; Holladay, Johnathan E.; Palo, Daniel R.

    2013-11-26

    The objective of the work was to enhance price-competitive, synthesis gas (syngas)-based production of transportation fuels that are directly compatible with the existing vehicle fleet (i.e., vehicles fueled by gasoline, diesel, jet fuel, etc.). To accomplish this, modifications to the traditional methanol-to-gasoline (MTG) process were investigated. In this study, we investigated direct conversion of syngas to distillates using methanol and dimethyl ether intermediates. For this application, a Pd/ZnO/Al2O3 (PdZnAl) catalyst previously developed for methanol steam reforming was evaluated. The PdZnAl catalyst was shown to be far superior to a conventional copper-based methanol catalyst when operated at relatively high temperatures (i.e., >300°C), which is necessary for MTG-type applications. Catalytic performance was evaluated through parametric studies. Process conditions such as temperature, pressure, gas-hour-space velocity, and syngas feed ratio (i.e., hydrogen:carbon monoxide) were investigated. PdZnAl catalyst formulation also was optimized to maximize conversion and selectivity to methanol and dimethyl ether while suppressing methane formation. Thus, a PdZn/Al2O3 catalyst optimized for methanol and dimethyl ether formation was developed through combined catalytic material and process parameter exploration. However, even after compositional optimization, a significant amount of undesirable carbon dioxide was produced (formed via the water-gas-shift reaction), and some degree of methane formation could not be completely avoided. Pd/ZnO/Al2O3 used in combination with ZSM-5 was investigated for direct syngas-to-distillates conversion. High conversion was achieved as thermodynamic constraints are alleviated when methanol and dimethyl are intermediates for hydrocarbon formation. When methanol and/or dimethyl ether are products formed separately, equilibrium restrictions occur. Thermodynamic relaxation also enables the use of lower operating pressures than what

  15. HyPro: A Financial Tool for Simulating Hydrogen Infrastructure Development, Final Report

    SciTech Connect (OSTI)

    Brian D. James, Peter O. Schmidt, Julie Perez

    2008-12-01

    This report summarizes a multi-year Directed Technologies Inc. (DTI) project to study the build-out of hydrogen production facilities during the transition from gasoline internal combustion engine vehicle to hydrogen fuel cell vehicles. The primary objectives of the project are to develop an enhanced understanding of hydrogen production issues during the transition period (out to 2050) and to develop recommendations for the DOE on areas of further study. These objectives are achieved by conducting economic and scenario analysis to predict how industry would provide the hydrogen production, delivery and dispensing capabilities necessary to satisfy increased hydrogen demand. The primary tool used for the analysis is a custom created MatLab simulation tool entitled HyPro (short for Hydrogen Production). This report describes the calculation methodology used in HyPro, the baseline assumptions, the results of the baseline analysis and several corollary studies. The appendices of this report included a complete listing of model assumptions (capital costs, efficiencies, feedstock prices, delivery distances, etc.) and a step-by-step manual on the specific operation of the HyPro program. This study was made possible with funding from the U.S. Department of Energy (DOE).

  16. Influence of Pro-Qura-generated Plans on Postimplant Dosimetric Quality: A Review of a Multi-Institutional Database

    SciTech Connect (OSTI)

    Allen, Zachariah |||; Merrick, Gregory S. ||| Grimm, Peter; Blasko, John; Sylvester, John; Butler, Wayne; Chaudry, Usman-Ul-Haq; Sitter, Michael |||

    2008-10-01

    The influence of Pro-Qura-generated plans vs. community-generated plans on postprostate brachytherapy dosimetric quality was compared. In the Pro-Qura database, 2933 postplans were evaluated from 57 institutions. A total of 1803 plans were generated by Pro-Qura and 1130 by community institutions. Iodine-125 ({sup 125}I) plans outnumbered Palladium 103 ({sup 103}Pd) plans by a ratio of 3:1. Postimplant dosimetry was performed in a standardized fashion by overlapping the preimplant ultrasound and the postimplant computed tomography (CT). In this analysis, adequacy was defined as a V{sub 100} > 80% and a D{sub 90} of 90% to 140% for both isotopes along with a V{sub 150} < 60% for {sup 125}I and < 75% for {sup 103}Pd. The mean postimplant V{sub 100} and D{sub 90} were 88.6% and 101.6% vs. 89.3% and 102.3% for Pro-Qura and community plans, respectively. When analyzed in terms of the first 8 sequence groups (10 patients/sequence group) for each institution, Pro-Qura planning resulted in less postimplant variability for V{sub 100} (86.2-89.5%) and for D{sub 90} (97.4-103.2%) while community-generated plans had greater V{sub 100} (85.3-91.2%) and D{sub 90} (95.9-105.2%) ranges. In terms of sequence groups, postimplant dosimetry was deemed 'too cool' in 11% to 30% of cases and 'too hot' in 12% to 27%. On average, no clinically significant postimplant dosimetric differences were discerned between Pro-Qura and community-based planning. However, substantially greater variability was identified in the community-based plan cohort. It is possible that the Pro-Qura plan and/or the routine postimplant dosimetric evaluation may have influenced dosimetric outcomes at community-based centers.

  17. Single-Step Syngas-to-Distillates (S2D) Process Based on Biomass-Derived Syngas - A Techno-Economic Analysis

    SciTech Connect (OSTI)

    Zhu, Y.; Jones, S. B.; Biddy, M. J.; Dagle, R. A.; Palo, D. R.

    2012-08-01

    This study compared biomass gasification based syngas-to-distillate (S2D) systems using techno-economic analysis (TEA). Three cases, state of technology (SOT), goal, and conventional, were compared in terms of performance and cost. The SOT case represented the best available experimental results for a process starting with syngas using a single-step dual-catalyst reactor for distillate generation. The conventional case mirrored a conventional two-step S2D process consisting of separate syngas-to-methanol and methanol-to-gasoline (MTG) processes. The goal case assumed the same performance as the conventional, but with a single-step S2D technology. TEA results revealed that the SOT was more expensive than the conventional and goal cases. The SOT case suffers from low one-pass yield and high selectivity to light hydrocarbons, both of which drive up production cost. Sensitivity analysis indicated that light hydrocarbon yield and single pass conversion efficiency were the key factors driving the high cost for the SOT case.

  18. CHARACTERIZATION OF Pro-Beam LOW VOLTAGE ELECTRON BEAM WELDING MACHINE

    SciTech Connect (OSTI)

    Burgardt, Paul; Pierce, Stanley W.

    2015-02-18

    The purpose of this paper is to present and discuss data related to the performance of a newly acquired low voltage electron beam welding machine. The machine was made by Pro-Beam AG &Co. KGaA of Germany. This machine was recently installed at LANL in building SM -39; a companion machine was installed in the production facility. The PB machine is substantially different than the EBW machines typically used at LANL and therefore, it is important to understand its characteristics as well as possible. Our basic purpose in this paper is to present basic machine performance data and to compare those with similar results from the existing EBW machines. It is hoped that this data will provide a historical record of this machine’s characteristics as well as possibly being helpful for transferring welding processes from the old EBW machines to the PB machine or comparable machines that may be purchased in the future.

  19. Towards a 100mA Superconducting RF Photoinjector for BERLinPro

    SciTech Connect (OSTI)

    Neumann, Axel; Anders, W.; Burrill, Andrew; Jankowiak, Andreas; Kamps, T.; Knobloch, Jens; Kugeler, Oliver; Lauinger, P.; Matveenko, A.N.; Schmeisser, M.; Volker, J.; Ciovati, Gianluigi; Kneisel, Peter; Nietubyc, R.; Schubert, S.G.; Smedley, John; Sekutowicz, Jacek; Volkov, V.; Will, I.; Zaplatin, Evgeny

    2013-09-01

    For BERLinPro, a 100 mA CW-driven SRF energy recovery linac demonstrator facility, HZB needs to develop a photo-injector superconducting cavity which delivers a at least 1mm*mr emittance beam at high average current. To address these challenges of producing a high peak brightness beam at high repetition rate, at first HZB tested a fully superconducting injector with a lead cathode*,followed now by the design of a SC cavity allowing operation up to 4 mA using CW-modified TTF-III couplers and inserting a normal conducting high quantum efficiency cathode using the HZDR-style insert scheme. This talk will present the latest results and an overview of the measurements with the lead cathode cavity and will describe the design and optimization process, the first production results of the current design and an outlook to the further development steps towards the full power version.

  20. Processing and Testing of the SRF Photoinjector Cavity for BERLinPro

    SciTech Connect (OSTI)

    Burrill, Andrew; Anders, W.; Frahm, A.; Knobloch, Jens; Neumann, Axel; Ciovati, Gianluigi; Clemens, William; Kneisel, Peter; Turlington, Larry; Zaplatin, Evgeny

    2014-07-01

    The BERLinPro project is a compact, c.w. SRF energy recovery linac (ERL) that is being built to develop the accelerator physics and technology required to operate the next generation of high current ERLs. The machine is designed to produce a 50 MeV 100 mA beam, with better than 1 mm-mrad emittance. The electron source for the ERL will be a SRF photoinjector equipped with a multi-alkali photocathode. In order to produce a SRF photoinjector to operate reliably at this beam current HZB has undertaken a 3 stage photoinjector development program to study the operation of SRF photoinjectors in detail. The 1.4 cell cavity being reported on here is the second stage of this development, and represents the first cavity designed by HZB for use with a high quantum efficiency multi-alkali photocathode. This paper will describe the work done to prepare the cavity for RF testing in the vertical testing dewar at Jefferson Laboratory as well as the results of these RF tests.

  1. Chemistry of hydrotreating heavy crudes: II. Detailed analysis of polar compounds in Wilmington 650-1000 degree F distillate and hydrotreated products

    SciTech Connect (OSTI)

    Sturm, G.P. Jr.; Green, J.B.; Tang, S.Y.; Reynolds, J.W.; Yu, S.K.T. )

    1987-04-01

    Notwithstanding the current oversupply of crude oil, the future importance of heavy crude as a primary energy resource is widely recognized. In addition, with the market for resid declining, refiners are facing an increasing challenge to convert more of the bottom of the barrel to transportation fuels. The problems that have been predicted for refinery products made from heavier feedstocks are now beginning to surface. State-of-the-art upgrading procedures have proven to be inadequate for removal of many of the chemical compound types that cause problems in the processing sequence or adversely affect the quality of the end products. These problems include instability or incompatibility of process streams or products, corrosiveness and catalyst poisoning. Before new approaches can be intelligently developed to remove the problem components, it is necessary to know what compound types are causing the observed problems. This study is focused on determination of polar compounds in the feedstock and products from hydrotreating a distillate of a representative heavy crude, Wilmington. The ultimate objective is to acquire an understanding of the compound types and reaction mechanisms contributing to instability, incompatibility, corrosiveness, catalyst poisoning and other problems exhibited by some crude oil feedstocks, intermediate process streams and final products resulting from the processing of lower quality fossil fuel feedstocks.

  2. Acute Toxicity of Radiochemotherapy in Rectal Cancer Patients: A Risk Particularly for Carriers of the TGFB1 Pro25 variant

    SciTech Connect (OSTI)

    Schirmer, Markus Anton; Mergler, Caroline Patricia Nadine; Rave-Fraenk, Margret; Herrmann, Markus Karl; Hennies, Steffen; Gaedcke, Jochen; Conradi, Lena-Christin; Jo, Peter; Beissbarth, Tim; Hess, Clemens Friedrich; Becker, Heinz; Ghadimi, Michael; Brockmoeller, Juergen; Christiansen, Hans; Wolff, Hendrik Andreas

    2012-05-01

    Purpose: Transforming growth factor-beta1 is related to adverse events in radiochemotherapy. We investigated TGFB1 genetic variability in relation to quality of life-impairing acute organ toxicity (QAOT) of neoadjuvant radiochemotherapy under clinical trial conditions. Methods and Materials: Two independent patient cohorts (n = 88 and n = 75) diagnosed with International Union Against Cancer stage II/III rectal cancer received neoadjuvant radiation doses of 50.4 Gy combined with 5-fluorouracil-based chemotherapy. Toxicity was monitored according to Common Terminology Criteria for Adverse Events. QAOT was defined as a CTCAE grade {>=}2 for at least one case of enteritis, proctitis, cystitis, or dermatitis. Nine germline polymorphisms covering the common genetic diversity in the TGFB1 gene were genotyped. Results: In both cohorts, all patients carrying the TGFB1 Pro25 variant experienced QAOT (positive predictive value of 100%, adjusted p = 0.0006). In a multivariate logistic regression model, gender, age, body mass index, type of chemotherapy, or disease state had no significant impact on QAOT. Conclusion: The TGFB1 Pro25 variant could be a relevant marker for individual treatment stratification and carriers may benefit from adaptive clinical care or specific radiation techniques.

  3. Stocks of Distillate Fuel Oil

    U.S. Energy Information Administration (EIA) (indexed site)

    156,972 155,732 152,378 150,550 148,602 148,912 1982-2016 PADD 1 67,073 66,391 64,764 65,721 64,801 64,939 1990-2016 New England 12,875 12,828 12,753 12,790 13,008 12,791 1990-2016 Central Atlantic 40,330 40,422 39,313 40,033 39,994 39,737 1990-2016 Lower Atlantic 13,868 13,141 12,699 12,898 11,800 12,411 1990-2016 PADD 2 33,149 31,751 32,827 32,393 31,107 30,589 1990-2016 PADD 3 38,605 40,303 38,538 37,081 37,451 38,580 1990-2016 PADD 4 3,830 3,492 3,151 3,304 3,676 3,687 1990-2016 PADD 5

  4. Imports of Distillate Fuel Oil

    Annual Energy Outlook

    175 90 207 126 118 52 1982-2016 East Coast (PADD 1) 173 81 199 120 107 48 2004-2016 Midwest (PADD 2) 2 1 2 3 2 1 2004-2016 Gulf Coast (PADD 3) 0 0 0 0 0 0 2004-2016 Rocky Mountain ...

  5. No. 2 Distillate Prices - Industrial

    Gasoline and Diesel Fuel Update

    09 - - - - - 1983-2015 East Coast (PADD 1) 2.380 - - - - - 1983-2015 New England (PADD 1A) 2.381 - - - - - 1983-2015 Connecticut 2.400 - - - - - 1983-2015 Maine 2.452 - - - - - 1983-2015 Massachusetts NA - - - - - 1983-2015 New Hampshire 2.482 - - - - - 1983-2015 Rhode Island 2.559 - - - - - 1983-2015 Vermont 2.492 - - - - - 1983-2015 Central Atlantic (PADD 1B) 2.380 - - - - - 1983-2015 Delaware 2.344 - - - - - 1983-2015 District of Columbia W - - - - - 1983-2015 Maryland 2.287 - - - - -

  6. No. 2 Distillate Prices - Residential

    Gasoline and Diesel Fuel Update

    798 - - - - - 1978-2015 East Coast (PADD 1) 2.829 - - - - - 1983-2015 New England (PADD 1A) 2.804 - - - - - 1983-2015 Connecticut 2.835 - - - - - 1978-2015 Maine 2.639 - - - - - 1978-2015 Massachusetts 2.850 - - - - - 1978-2015 New Hampshire 2.680 - - - - - 1978-2015 Rhode Island 2.927 - - - - - 1978-2015 Vermont 2.795 - - - - - 1978-2015 Central Atlantic (PADD 1B) 2.878 - - - - - 1983-2015 Delaware 2.951 - - - - - 1978-2015 District of Columbia W - - - - - 1978-2015 Maryland 2.925 - - - - -

  7. No. 2 Distillate Prices - Residential

    U.S. Energy Information Administration (EIA) (indexed site)

    Connecticut - - - - - - 1983-2016 Maine - - - - - - 1983-2016 Massachusetts - - - - - - 1983-2016 New Hampshire - - - - - - 1983-2016 Rhode Island - - - - - - 1983-2016 Vermont - - ...

  8. Evaluation of the effect of organic pro-degradant concentration in polypropylene exposed to the natural ageing

    SciTech Connect (OSTI)

    Montagna, L. S. E-mail: andrecatto@terra.com.br E-mail: mmcforte@hotmail.com Catto, A. L. E-mail: andrecatto@terra.com.br E-mail: mmcforte@hotmail.com Rossini, K. E-mail: andrecatto@terra.com.br E-mail: mmcforte@hotmail.com Forte, M. M. C. E-mail: andrecatto@terra.com.br E-mail: mmcforte@hotmail.com Santana, R. M. C. E-mail: andrecatto@terra.com.br E-mail: mmcforte@hotmail.com

    2014-05-15

    The production and consumption of plastics in the last decade has recorded a remarkable increase in the scientific and industrial interest in environmentally degradable polymer (EDPs). Polymers wastes are deposited improperly, such as dumps, landfills, rivers and seas, causing a serious problem by the accumulation in the environment. The abiotic processes, like the photodegradation, are the most efficient occurring in the open environmental, where the polymers undergo degradation from the action of sunlight that result from direct exposure to solar radiation, however depend of the type of chemical ageing, which is the principal component of climatic ageing. The subject of this work is to study the influence of concentration of organic pro-degradant (1, 2 and 3 % w/w) in the polypropylene (PP) exposed in natural ageing. PP samples with and without the additive were processed in plates square form, obtained by thermal compression molding (TCM) using a press at 200C under 2 tons for 5 min, and then were exposed at natural ageing during 120 days. The presence of organic additive influenced on PP degradability, this fact was assessed by changes in the thermal and morphology properties of the samples after 120 days of natural ageing. Scanning Electronic Microscopy (SEM) results of the morphological surface of the modified PP samples showed greater degradation photochemical oxidative when compared to neat PP, due to increase of rugosity and formation of microvoids. PP samples with different pro-degradant concentration under natural ageing presented a degree of crystallinity, obtained by Differential Scanning Calorimeter (DSC) increases in comparing the neat PP.

  9. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    degree-days are deviations above the mean daily temperature of 65 F. For example, a weather station recording a mean daily temperature of 78 F would report 13 cooling...

  10. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    Energy Consumption and Expenditures Indicators Estimates Energy Consumption, 1949-2011 Energy Expenditures, 1970-2010 Energy Consumption per Real Dollar of Gross Domestic...

  11. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    Monthly Value (Year of Record) 2010- 2011 Heating Season 30-Year Monthly Normal Record Low Monthly Value (Year of Record) 260 (1981) (1985) 1 Based on calculations of data from...

  12. Word Pro - Untitled1

    U.S. Energy Information Administration (EIA) (indexed site)

    High Monthly Value (Year of Record) 2011 Cooling Season 30-Year Monthly Normal Record Low Monthly Value (Year of Record) 83 (1963) 118 (1967) 27 (1976) 268 (1950) 147 (1991) 228...

  13. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

  14. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

    7 a Exact conversion. b Calculated by the U.S. Energy Information Administration. Web Page: http://www.eia.gov/totalenergy/data/monthly/#appendices. Source: U.S. Department of Commerce, National Institute of Standards and Technology, Specifications, Tolerances, and Other Techni- cal Requirements for Weighing and Measuring Devices, NIST Handbook 44, 1994 Edition (Washington, DC, October 1993), pp. B-10, C-17, and C-21. cubic feet (ft 3 ) 128 a = 1 cord (cd) shorts tons 1.25 b = 1 cord (cd) Wood

  15. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

    9 Appendix C Table C1. Population, U.S. Gross Domestic Product, and U.S. Gross Output Population U.S. Gross Domestic Product U.S. Gross Output a United States b World United States as Share of World Billion Nominal Dollars d Billion Chained (2009) Dollars e Implicit Price Deflator c (2009 = 1.00000) Billion Nominal Dollars d Million People Percent 1950 .............. 152.3 2,557.6 6.0 300.2 2,184.0 0.13745 NA 1955 .............. 165.9 2,782.1 6.0 426.2 2,739.0 .15559 NA 1960 .............. 180.7

  16. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

    ec 192 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table A2. Approximate Heat Content of Petroleum Production, Imports, and Exports (Million Btu per Barrel) Production Imports Exports Crude Oil a Petroleum Products Total Crude Oil a Petroleum Products Total Crude Oil a Natural Gas Plant Liquids Motor Gasoline b Total Products Motor Gasoline c Total Products 1950 ...................... 5.800 4.522 5.943 5.253 6.263 6.080 5.800 5.253 5.751 5.766 1955

  17. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

    1 Appendix D Table D1. Estimated Primary Energy Consumption in the United States, Selected Years, 1635-1945 (Quadrillion Btu) Fossil Fuels Renewable Energy Electricity Net Imports b Total Coal Natural Gas Petroleum Total Conventional Hydroelectric Power Biomass Total Wood a 1635 .............. NA - - - - NA - - (s) (s) - - (s) 1645 .............. NA - - - - NA - - 0.001 0.001 - - 0.001 1655 .............. NA - - - - NA - - .002 .002 - - .002 1665 .............. NA - - - - NA - - .005 .005 - -

  18. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

    Note. Geographic Coverage of Statistics for 1635-1945. Table D1 presents estimates of U.S. energy consumption by energy source for a period that begins a century and a half before the original 13 colonies formed a political union and continues through the decades during which the United States was still expanding territorially. The question thus arises, what exactly is meant by "U.S. consumption" of an energy source for those years when the United States did not formally exist or

  19. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

    195 Table A5. Approximate Heat Content of Coal and Coal Coke (Million Btu per Short Ton) Coal Coal Coke Production a Waste Coal Supplied b Consumption Imports Exports Imports and Exports Residential and Commercial Sectors c Industrial Sector Electric Power Sector e,f Total Coke Plants Other d 1950 ........................ 25.090 NA 24.461 26.798 24.820 23.937 24.989 25.020 26.788 24.800 1955 ........................ 25.201 NA 24.373 26.794 24.821 24.056 24.982 25.000 26.907 24.800 1960

  20. Word Pro - A

    U.S. Energy Information Administration (EIA) (indexed site)

    6 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table A6. Approximate Heat Rates for Electricity, and Heat Content of Electricity (Btu per Kilowatthour) Approximate Heat Rates a for Electricity Net Generation Heat Content j of Electricity k Fossil Fuels b Nuclear h Noncombustible Renewable Energy g,i Coal c Petroleum d Natural Gas e Total Fossil Fuels f,g 1950 .............................. NA NA NA 14,030 - - 14,030 3,412 1955 .............................. NA NA

  1. Word Pro - S1

    U.S. Energy Information Administration (EIA) (indexed site)

    Consumption by Sector 1. Energy Overview Figure 1.1 Primary Energy Overview (Quadrillion Btu) Overview, 1949-2015 Overview, Monthly Overview, July 2016 Net Imports, January-July Web Page: http://www.eia.gov/totalenergy/data/monthly/#summary. Source: Table 1.1. 2 U.S. Energy Information Administration / Monthly Energy Review October 2016 6.515 6.443 6.944 2014 2015 2016 0 2 4 6 8 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 20 40 60 80 100 120 Consumption Production

  2. Word Pro - S1

    U.S. Energy Information Administration (EIA) (indexed site)

    Monthly Energy Review October 2016 Table 1.4a Primary Energy Imports by Source (Quadrillion Btu) Imports Coal Coal Coke Natural Gas Petroleum Biofuels c Electricity Total Crude Oil a Petroleum Products b Total 1950 Total ...................... 0.009 0.011 0.000 1.056 0.830 1.886 NA 0.007 1.913 1955 Total ...................... .008 .003 .011 1.691 1.061 2.752 NA .016 2.790 1960 Total ...................... .007 .003 .161 2.196 1.802 3.999 NA .018 4.188 1965 Total ...................... .005 .002

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Merchandise Trade Value (Billion Dollars a ) Imports and Exports, 1974-2015 Imports and Exports, Monthly Trade Balance, 1974-2015 Trade Balance, Monthly a Prices are not adjusted for inflation. S ee "Nominal Dollars" in Glossary. http://www.eia.gov/totalenergy/data/monthly/#summary. Source: Table 1.5. 12 U.S. Energy Information Administration / Monthly Energy Review October 2016 Energy Exports 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 500 1,000 1,500 2,000 2,500 J F MA M J J A S

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    U.S. Energy Information Administration (EIA) (indexed site)

    Table 1.5 Merchandise Trade Value (Million Dollars a ) Petroleum b Energy c Non- Energy Balance Total Merchandise Exports Imports Balance Exports Imports Balance Exports Imports Balance 1974 Total ................ 792 24,668 -23,876 3,444 25,454 -22,010 18,126 99,437 103,321 -3,884 1975 Total ................ 907 25,197 -24,289 4,470 26,476 -22,006 31,557 108,856 99,305 9,551 1980 Total ................ 2,833 78,637 -75,803 7,982 82,924 -74,942 55,246 225,566 245,262 -19,696 1985 Total

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    U.S. Energy Information Administration (EIA) (indexed site)

    7 Primary Energy Consumption and Energy Expenditures Indicators Energy Consumption per Capita, 1949-2015 Primary Energy Consumption per Real Dollar a of Gross Domestic Product, 1949-2015 Energy Expenditures as Share of Gross Domestic Product and Gross Output, b 1987-2013 16 U.S. Energy Information Administration / Monthly Energy Review October 2016 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 100 200 300 400 Million Btu Thousand Btu per Chained (2009) Dollar a 1950

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    U.S. Energy Information Administration (EIA) (indexed site)

    Table 1.7 Primary Energy Consumption, Energy Expenditures, and Carbon Dioxide Emissions Indicators Primary Energy Consumption a Energy Expenditures b Carbon Dioxide Emissions c Consump- tion Consump- tion per Capita Consumption per Real Dollar d of GDP e Expendi- tures Expendi- tures per Capita Expenditures as Share of GDP e Expenditures as Share of Gross Output f Emissions Emissions per Capita Emissions per Real Dollar d of GDP e Quadrillion Btu Million Btu Thousand Btu per Chained (2009)

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    U.S. Energy Information Administration (EIA) (indexed site)

    Monthly Energy Review October 2016 Table 1.9 Heating Degree Days by Census Division New England a Middle Atlantic b East North Central c West North Central d South Atlantic e East South Central f West South Central g Mountain h Pacific i United States 1950 Total .................... 6,794 6,324 7,027 7,455 3,521 3,547 2,277 6,341 3,906 5,367 1955 Total .................... 6,872 6,231 6,486 6,912 3,508 3,513 2,294 6,704 4,320 5,246 1960 Total .................... 6,828 6,391 6,908 7,184 3,780

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    U.S. Energy Information Administration (EIA) (indexed site)

    Table 1.10 Cooling Degree Days by Census Division New England a Middle Atlantic b East North Central c West North Central d South Atlantic e East South Central f West South Central g Mountain h Pacific i United States 1950 Total .................... 295 401 505 647 1,414 1,420 2,282 682 629 871 1955 Total .................... 532 761 922 1,139 1,636 1,674 2,508 780 558 1,144 1960 Total .................... 318 487 626 871 1,583 1,532 2,367 974 796 1,000 1965 Total .................... 310 498

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 1.1 Primary Energy Overview (Quadrillion Btu) Production Trade Stock Change and Other d Consumption Fossil Fuels a Nuclear Electric Power Renew- able Energy b Total Imports Exports Net Imports c Fossil Fuels e Nuclear Electric Power Renew- able Energy b Total f 1950 Total .................... 32.563 0.000 2.978 35.540 1.913 1.465 0.448 -1.372 31.632 0.000 2.978 34.616 1955 Total .................... 37.364 .000 2.784 40.148 2.790 2.286 .504 -.444 37.410 .000 2.784 40.208 1960 Total

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    U.S. Energy Information Administration (EIA) (indexed site)

    2 Primary Energy Production (Quadrillion Btu) By Source, 1949-2015 By Source, Monthly Total, January-July By Source, July 2016 a Natural gas plant liquids. Web Page: http://www.eia.gov/totalenergy/data/monthly/#summary. Source: Table 1.2. 4 U.S. Energy Information Administration / Monthly Energy Review October 2016 2014 2015 2016 Renewable Energy Crude Oil and NGPL a Nuclear Electric Power Coal Natural Gas Crude Oil and NGPL a Renewable Energy Nuclear Electric Power 1950 1955 1960 1965 1970 1975

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    U.S. Energy Information Administration (EIA) (indexed site)

    Table 1.2 Primary Energy Production by Source (Quadrillion Btu) Fossil Fuels Nuclear Electric Power Renewable Energy a Total Coal b Natural Gas (Dry) Crude Oil c NGPL d Total Hydro- electric Power e Geo- thermal Solar Wind Bio- mass Total 1950 Total .................. 14.060 6.233 11.447 0.823 32.563 0.000 1.415 NA NA NA 1.562 2.978 35.540 1955 Total .................. 12.370 9.345 14.410 1.240 37.364 .000 1.360 NA NA NA 1.424 2.784 40.148 1960 Total .................. 10.817 12.656 14.935

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Primary Energy Consumption (Quadrillion Btu) By Source, a 1949-2015 By Source, a Monthly Total, January-July By Source, a July 2016 a Small quantities of net imports of coal coke and electricity are not shown. Web Page: http://www.eia.gov/totalenergy/data/monthly/#summary. Source: Table 1.3. 6 U.S. Energy Information Administration / Monthly Energy Review October 2016 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 15 30 45 Petroleum Natural Gas Coal Nuclear Electric

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    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 1.3 Primary Energy Consumption by Source (Quadrillion Btu) Fossil Fuels Nuclear Electric Power Renewable Energy a Total f Coal Natural Gas b Petro- leum c Total d Hydro- electric Power e Geo- thermal Solar Wind Bio- mass Total 1950 Total .................... 12.347 5.968 13.315 31.632 0.000 1.415 NA NA NA 1.562 2.978 34.616 1955 Total .................... 11.167 8.998 17.255 37.410 .000 1.360 NA NA NA 1.424 2.784 40.208 1960 Total .................... 9.838 12.385 19.919 42.137 .006

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    U.S. Energy Information Administration (EIA) (indexed site)

    a Primary Energy Imports and Exports (Quadrillion Btu) Imports by Source, 1949-2015 Exports by Source, 1949-2015 Imports by Source, Monthly Exports by Major Source, Monthly a Coal, coal coke, biofuels, and electricity. Web Page: http://www.eia.gov/totalenergy/data/monthly/#summary. b Includes coal coke. Sources: Tables 1.4a and 1.4b. 8 U.S. Energy Information Administration / Monthly Energy Review October 2016 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 5 10 15 20 25

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    U.S. Energy Information Administration (EIA) (indexed site)

    b Primary Energy Net Imports (Quadrillion Btu) Total, 1949-2015 By Major Source, 1949-2015 Total, Monthly By Major Source, Monthly U.S. Energy Information Administration / Monthly Energy Review October 2016 9 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 -5 0 5 10 15 20 25 30 35 Natural Gas Crude Oil a Petroleum Products b Coal Crude Oil a 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 -5 0 5 10 15 20 25 0 -5 Petroleum Products b Coal Natural Gas J

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    U.S. Energy Information Administration (EIA) (indexed site)

    . Renewable Energy Figure 10.1 Renewable Energy Consumption (Quadrillion Btu) Major Sources, 1949-2015 By Source, 2015 By Sector, 2015 Compared With Other Resources, 1949-2015 150 U.S. Energy Information Administration / Monthly Energy Review October 2016 Solar a Hydroelectric Power b Wind a Renewable Energy a See Table 10.1 for definition. b Conventional hydroelectric power. Web Page: http://www.eia.gov/totalenergy/data/monthly/#renewable. Sources: Tables 1.3 and 10.1-10.2c. Power fuels a

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    U.S. Energy Information Administration (EIA) (indexed site)

    8 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 10.6 Solar Electricity Net Generation (Million Kilowatthours) Distributed a Solar Generation b Utility-Scale c Solar Generation b Total Residential Sector Commercial Sector Industrial Sector Total Commercial Sector d Industrial Sector e Electric Power Sector f Total 1985 Total ...................... NA NA NA NA NA NA 11 11 11 1990 Total ...................... 10 14 3 27 - - 367 367 394 1995 Total

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Renewable Energy Consumption (Quadrillion Btu) Major Sources, 1949-2015 By Source, 2015 By Sector, 2015 Compared With Other Resources, 1949-2015 150 U.S. Energy Information Administration / Monthly Energy Review October 2016 Solar a Hydroelectric Power b Wind a Renewable Energy a See Table 10.1 for definition. b Conventional hydroelectric power. Web Page: http://www.eia.gov/totalenergy/data/monthly/#renewable. Sources: Tables 1.3 and 10.1-10.2c. Power fuels a Fossil Fuels Biomass a Nuclear

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    U.S. Energy Information Administration (EIA) (indexed site)

    2 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 10.2a Renewable Energy Consumption: Residential and Commercial Sectors (Trillion Btu) Residential Sector Commercial Sector a Geo- thermal b Solar c Biomass Total Hydro- electric Power e Geo- thermal b Solar f Wind g Biomass Total Wood d Wood d Waste h Fuel Ethanol i Total 1950 Total .................... NA NA 1,006 1,006 NA NA NA NA 19 NA NA 19 19 1955 Total .................... NA NA 775 775 NA NA NA NA 15 NA NA

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    U.S. Energy Information Administration (EIA) (indexed site)

    4 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 10.2c Renewable Energy Consumption: Electric Power Sector (Trillion Btu) Hydro- electric Power a Geo- thermal b Solar c Wind d Biomass Total Wood e Waste f Total 1950 Total .................... 1,346 NA NA NA 5 NA 5 1,351 1955 Total .................... 1,322 NA NA NA 3 NA 3 1,325 1960 Total .................... 1,569 (s) NA NA 2 NA 2 1,571 1965 Total .................... 2,026 2 NA NA 3 NA 3 2,031 1970 Total

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    U.S. Energy Information Administration (EIA) (indexed site)

    U.S. Energy Information Administration / Monthly Energy Review October 2016 157 Table 10.5 Solar Energy Consumption (Trillion Btu) Distributed a Solar Energy b Utility-Scale c Solar Energy b Total k Heat f Electricity d Total g Electricity e Residential Sector Commercial Sector Industrial Sector Total Commercial Sector h Industrial Sector i Electric Power Sector j Total 1985 Total ...................... NA NA NA NA NA NA NA NA (s) (s) (s) 1990 Total ...................... 55 (s) (s) (s) (s) 55 -

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    U.S. Energy Information Administration (EIA) (indexed site)

    Energy Note. Renewable Energy Production and Consumption. In Tables 1.1, 1.3, and 10.1, renewable energy consumption consists of: conventional hydroelectricity net generation (converted to Btu by multiplying by the total fossil fuels heat rate factors in Table A6); geothermal electricity net generation (converted to Btu by multiplying by the total fossil fuels heat rate factors in Table A6), and geothermal heat pump and geothermal direct use energy; solar thermal and photovoltaic electricity net

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    U.S. Energy Information Administration (EIA) (indexed site)

    . International Petroleum Figure 11.1a World Crude Oil Production Overview (Million Barrels per Day) World Production, 1973-2015 World Production, Monthly Selected Producers, 1973-2015 Selected Producers, Monthly 168 U.S. Energy Information Administration / Monthly Energy Review October 2016 United States 2014 2015 2016 2014 2015 2016 Non-OPEC J F MA M J J A S O N D J F MA M J J A S O N D J F MA M J J A S O N D 0 20 40 60 80 100 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 30 60 90 Non-OPEC

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    U.S. Energy Information Administration (EIA) (indexed site)

    a World Crude Oil Production Overview (Million Barrels per Day) World Production, 1973-2015 World Production, Monthly Selected Producers, 1973-2015 Selected Producers, Monthly 168 U.S. Energy Information Administration / Monthly Energy Review October 2016 United States 2014 2015 2016 2014 2015 2016 Non-OPEC J F MA M J J A S O N D J F MA M J J A S O N D J F MA M J J A S O N D 0 20 40 60 80 100 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 30 60 90 Non-OPEC World 1975 1980 1985 1990 1995 2000

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    U.S. Energy Information Administration (EIA) (indexed site)

    b World Crude Oil Production by Selected Countries (Million Barrels per Day) U.S. Energy Information Administration / Monthly Energy Review October 2016 169 3.652 3.938 0.482 2.193 1.763 10.254 0.970 8.685 1.320 1.876 0.545 0.845 4.130 4.415 2.570 0.310 1.880 1.537 10.670 2.840 2.220 3.821 4.263 0.524 2.308 1.611 10.213 0.839 9.418 1.370 1.890 0.538 0.772 3.300 4.325 2.550 0.400 2.245 1.537 10.400 2.820 2.500 Canada China Egypt Mexico Norway Russia United Kingdom United States Algeria Angola

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    U.S. Energy Information Administration (EIA) (indexed site)

    70 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 11.1a World Crude Oil Production: Selected OPEC Members (Thousand Barrels per Day) Algeria Angola Ecuador Indo- nesia Iran Iraq Kuwait a Libya Nigeria Qatar Saudi Arabia a United Arab Emirates Vene- zuela Total OPEC b 1973 Average ................ 1,097 162 209 1,339 5,861 2,018 3,020 2,175 2,054 570 7,596 1,533 3,366 R 31,150 1975 Average ................ 983 165 161 1,307 5,350 2,262 2,084 1,480 1,783 438

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 11.1b World Crude Oil Production: Persian Gulf Nations, Non-OPEC, and World (Thousand Barrels per Day) Persian Gulf Nations b Selected Non-OPEC a Producers Total Non- OPEC a World Canada China Egypt Mexico Norway Former U.S.S.R. Russia United Kingdom United States 1973 Average .................... 20,668 1,798 1,090 165 465 32 8,324 NA 2 9,208 R 24,529 55,679 1975 Average .................... 18,934 1,430 1,490 235 705 189 9,523 NA 12 8,375 R 25,509 52,828 1980 Average

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 11.2 Petroleum Consumption in OECD Countries (Thousand Barrels per Day) France Germany a Italy United Kingdom OECD Europe b Canada Japan South Korea United States Other OECD c OECD d World 1973 Average .................... 2,601 3,324 2,068 2,341 15,879 1,729 4,949 281 17,308 1,768 41,913 57,237 1975 Average .................... 2,252 2,957 1,855 1,911 14,314 1,779 4,621 311 16,322 1,885 39,232 56,198 1980 Average .................... 2,256 3,082 1,934 1,725 14,995 1,873 4,960 537 17,056

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 11.3 Petroleum Stocks in OECD Countries (Million Barrels) France Germany a Italy United Kingdom OECD Europe b Canada Japan South Korea United States Other OECD c OECD d 1973 Year ......................... 201 181 152 156 1,070 140 303 NA 1,008 67 2,588 1975 Year ......................... 225 187 143 165 1,154 174 375 NA 1,133 67 2,903 1980 Year ......................... 243 319 170 168 1,464 164 495 NA 1,392 72 3,587 1985 Year ......................... 139 277 156 131 1,154 112 500 13

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    U.S. Energy Information Administration (EIA) (indexed site)

    6 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 12.7 Carbon Dioxide Emissions From Biomass Energy Consumption (Million Metric Tons of Carbon Dioxide a ) By Source By Sector Wood b Biomass Waste c Fuel Ethanol d Bio- diesel Total Resi- dential Com- mercial e Indus- trial f Trans- portation Electric Power g Total 1973 Total ...................... 143 (s) NA NA 143 33 1 109 NA (s) 143 1975 Total ...................... 140 (s) NA NA 141 40 1 100 NA (s) 141 1980

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    U.S. Energy Information Administration (EIA) (indexed site)

    2 Carbon Dioxide Emissions From Energy Consumption by Sector (Million Metric Tons of Carbon Dioxide) Total a by End-Use Sector, b 1973-2015 Residential Sector by Major Source, 1973-2015 Commercial Sector by Major Source, 1973-2015 Industrial Sector by Major Source, 1973-2015 Transportation Sector by Major Source, 1973-2015 Electric Power Sector by Major Source, 1973-2015 180 U.S. Energy Information Administration / Monthly Energy Review October 2016 1975 1980 1985 1990 1995 2000 2005 2010 2015 0

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    U.S. Energy Information Administration (EIA) (indexed site)

    2. Energy Consumption by Sector Figure 2.1 Energy Consumption by Sector (Quadrillion Btu) Total Consumption by End-Use Sector, 1949-2015 Total Consumption by End-Use Sector, Monthly By Sector, July 2016 28 U.S. Energy Information Administration / Monthly Energy Review October 2016 Transportation Residential 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 10 20 30 40 Industrial Transportation Residential Commercial J F M A M J J A S O N D J F M A M J J A S O N D J F M A M

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    U.S. Energy Information Administration (EIA) (indexed site)

    Transportation Sector Energy Consumption (Quadrillion Btu) By Major Source, 1949-2015 By Major Source, Monthly Total, January-July Total, Monthly . 36 U.S. Energy Information Administration / Monthly Energy Review October 2016 2014 2015 2016 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 5 10 15 20 25 30 Petroleum Natural Gas Renewable Energy J F M A M J J A S O N D J F M A M J J A S O N D J F M A M J J A S O N D 0.0 0.5 1.0 1.5 2.0 2.5 3.0 Petroleum Natural Gas

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    U.S. Energy Information Administration (EIA) (indexed site)

    Electric Power Sector Energy Consumption (Quadrillion Btu) By Major Source, 1949-2015 By Major Source, Monthly Total, January-July By Major Source, July 2016 . 38 U.S. Energy Information Administration / Monthly Energy Review October 2016 2014 2015 2016 Nuclear Electric Power Natural Gas Petroleum Renewable Energy Coal Renewable Energy Natural Gas 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 4 8 12 16 20 24 J F M A M J J A S O N D J F M A M J J A S O N D J F M A M J J

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    U.S. Energy Information Administration (EIA) (indexed site)

    9 Table 2.6 Electric Power Sector Energy Consumption (Trillion Btu) Primary Consumption a Fossil Fuels Nuclear Electric Power Renewable Energy b Elec- tricity Net Imports f Total Primary Coal Natural Gas c Petro- leum Total Hydro- electric Power d Geo- thermal Solar e Wind Bio- mass Total 1950 Total ...................... 2,199 651 472 3,322 0 1,346 NA NA NA 5 1,351 6 4,679 1955 Total ...................... 3,458 1,194 471 5,123 0 1,322 NA NA NA 3 1,325 14 6,461 1960 Total ......................

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    U.S. Energy Information Administration (EIA) (indexed site)

    0 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 2.7 U.S. Government Energy Consumption by Agency, Fiscal Years (Trillion Btu) Fiscal Year a Agri- culture Defense Energy GSA b HHS c Interior Justice NASA d Postal Service Trans- portation Veterans Affairs Other e Total 1975 .............. 9.5 1,360.2 50.4 22.3 6.5 9.4 5.9 13.4 30.5 19.3 27.1 10.5 1,565.0 1976 .............. 9.3 1,183.3 50.3 20.6 6.7 9.4 5.7 12.4 30.0 19.5 25.0 11.2 1,383.4 1977 ..............

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 2.8 U.S. Government Energy Consumption by Source, Fiscal Years (Trillion Btu) Fiscal Year a Coal Natural Gas b Petroleum Other Mobility Fuels f Elec- tricity Purchased Steam and Other g Total Aviation Gasoline Fuel Oil c Jet Fuel LPG d Motor Gasoline e Total 1975 .............. 77.9 166.2 22.0 376.0 707.4 5.6 63.2 1,174.2 0.0 141.5 5.1 1,565.0 1976 .............. 71.3 151.8 11.6 329.7 610.0 4.7 60.4 1,016.4 .0 139.3 4.6 1,383.4 1977 .............. 68.4 141.2 8.8 348.5 619.2 4.1 61.4

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    U.S. Energy Information Administration (EIA) (indexed site)

    2.1 Energy Consumption by Sector (Quadrillion Btu) Total Consumption by End-Use Sector, 1949-2015 Total Consumption by End-Use Sector, Monthly By Sector, July 2016 28 U.S. Energy Information Administration / Monthly Energy Review October 2016 Transportation Residential 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 10 20 30 40 Industrial Transportation Residential Commercial J F M A M J J A S O N D J F M A M J J A S O N D J F M A M J J A S O N D 0 1 2 3 4 Industrial

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 2.2 Residential Sector Energy Consumption (Trillion Btu) Primary Consumption a Electricity Retail Sales e Electrical System Energy Losses f Total Fossil Fuels Renewable Energy b Total Primary Coal Natural Gas c Petro- leum Total Geo- thermal Solar d Bio- mass Total 1950 Total .................... 1,261 1,240 1,322 3,824 NA NA 1,006 1,006 4,829 246 913 5,989 1955 Total .................... 867 2,198 1,767 4,833 NA NA 775 775 5,608 438 1,232 7,278 1960 Total .................... 585 3,212

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    U.S. Energy Information Administration (EIA) (indexed site)

    Commercial Sector Energy Consumption (Quadrillion Btu) By Major Source, 1949-2015 By Major Source, Monthly Total, January-July By Major Source, July 2016 32 U.S. Energy Information Administration / Monthly Energy Review October 2016 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 1 2 3 4 5 Electricity a Natural Gas Petroleum Coal Renewable Energy 2014 2015 2016 J F M A M J J A S O N D J F M A M J J A S O N D J F M A M J J A S O N D 0.0 0.2 0.4 0.6 0.8 Natural Gas

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 2.3 Commercial Sector Energy Consumption (Trillion Btu) Primary Consumption a Elec- tricity Retail Sales g Electrical System Energy Losses h Total Fossil Fuels Renewable Energy b Total Primary Coal Natural Gas c Petro- leum d Total Hydro- electric Power e Geo- thermal Solar f Wind Bio- mass Total 1950 Total .................... 1,542 401 872 2,815 NA NA NA NA 19 19 2,834 225 834 3,893 1955 Total .................... 801 651 1,095 2,547 NA NA NA NA 15 15 2,561 350 984 3,895 1960 Total

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    U.S. Energy Information Administration (EIA) (indexed site)

    Industrial Sector Energy Consumption (Quadrillion Btu) By Major Source, 1949-2015 By Major Source, Monthly Total, January-July By Major Source, July 2016 34 U.S. Energy Information Administration / Monthly Energy Review October 2016 Coal 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 3 6 9 12 Natural Gas Petroleum Electricity a Renewable Energy J F M A M J J A S O N D J F M A M J J A S O N D J F M A M J J A S O N D 0.0 0.2 0.4 0.6 0.8 1.0 Natural Gas Petroleum

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 2.4 Industrial Sector Energy Consumption (Trillion Btu) Primary Consumption a Elec- tricity Retail Sales h Electrical System Energy Losses i Total e Fossil Fuels Renewable Energy b Total Primary Coal Natural Gas c Petro- leum d Total e Hydro- electric Power f Geo- thermal Solar g Wind Bio- mass Total 1950 Total .................... 5,781 3,546 3,960 13,288 69 NA NA NA 532 602 13,890 500 1,852 16,241 1955 Total .................... 5,620 4,701 5,123 15,434 38 NA NA NA 631 669 16,103 887

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    U.S. Energy Information Administration (EIA) (indexed site)

    Consumption by Sector Note 1. Electrical System Energy Losses. Electrical system energy losses are calculated as the difference between total primary consumption by the electric power sector (see Table 2.6) and the total energy content of electricity retail sales (see Tables 7.6 and A6). Most of these losses occur at steam- electric power plants (conventional and nuclear) in the conver- sion of heat energy into mechanical energy to turn electric generators. The loss is a thermodynamically

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    U.S. Energy Information Administration (EIA) (indexed site)

    6 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 3.3c Petroleum Trade: Imports From OPEC Countries (Thousand Barrels per Day) Algeria a Angola b Ecuador c Iraq Kuwait d Libya e Nigeria f Saudi Arabia d Vene- zuela Other g Total OPEC 1960 Average ...................... a ( ) b ( ) c ( ) 22 182 e ( ) f ( ) 84 911 34 1,233 1965 Average ...................... a ( ) b ( ) c ( ) 16 74 42 f ( ) 158 994 155 1,439 1970 Average ...................... 8 b ( ) c ( ) - 48

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    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 3.3d Petroleum Trade: Imports From Non-OPEC Countries (Thousand Barrels per Day) Brazil Canada Colombia Mexico Nether- lands Norway Russia a United Kingdom U.S. Virgin Islands Other Total Non-OPEC 1960 Average ...................... 1 120 42 16 NA NA - (s) NA NA 581 1965 Average ...................... - 323 51 48 1 - - (s) - 606 1,029 1970 Average ...................... 2 766 46 42 39 - 3 11 189 1,027 2,126 1975 Average ...................... 5 846 9 71 19 17 14 14 406 1,052 2,454 1980

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    U.S. Energy Information Administration (EIA) (indexed site)

    U.S. Energy Information Administration / Monthly Energy Review October 2016 53 Table 3.3a Petroleum Trade: Overview Imports From Persian Gulf a Imports From OPEC b Imports Exports Net Imports Products Supplied As Share of Products Supplied As Share of Total Imports Imports From Persian Gulf a Imports From OPEC b Imports Net Imports Imports From Persian Gulf a Imports From OPEC b Thousand Barrels per Day Percent 1950 Average .................... NA NA 850 305 545 6,458 NA NA 13.2 8.4 NA NA 1955

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    U.S. Energy Information Administration (EIA) (indexed site)

    Gas Resource Development . 4. Natural Gas Figure 4.1 Natural Gas (Trillion Cubic Feet) Overview, 1949-2015 Consumption by Sector, 1949-2015 Overview, Monthly Consumption by Sector, Monthly Web Page: http://www.eia.gov/totalenergy/data/monthly/#naturalgas. Sources: Tables 4.1 and 4.3. 82 U.S. Energy Information Administration / Monthly Energy Review October 2016 Commercial Electric Power Industrial Industrial Trans- portation Transportation 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 4.1 Natural Gas Overview (Billion Cubic Feet) Gross With- drawals a Marketed Production (Wet) b NGPL Production c Dry Gas Production d Supple- mental Gaseous Fuels e Trade Net Storage With- drawals f Balancing Item g Consump- tion h Imports Exports Net Imports 1950 Total .................... 8,480 i 6,282 260 i 6,022 NA 0 26 -26 -54 -175 5,767 1955 Total .................... 11,720 i 9,405 377 i 9,029 NA 11 31 -20 -68 -247 8,694 1960 Total .................... 15,088 i 12,771 543 i

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    U.S. Energy Information Administration (EIA) (indexed site)

    4 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 4.2 Natural Gas Trade by Country (Billion Cubic Feet) Imports Exports a Algeria b Canada c Egypt b Mexico c Nigeria b Qatar b Trinidad and Tobago b Other b,d Total Canada c Japan b Mexico c Other b,e Total 1950 Total .................... 0 0 0 0 0 0 0 0 0 3 0 23 0 26 1955 Total .................... 0 11 0 (s) 0 0 0 0 11 11 0 20 0 31 1960 Total .................... 0 109 0 47 0 0 0 0 156 6 0 6 0 11 1965 Total

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    6 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 4.4 Natural Gas in Underground Storage (Volumes in Billion Cubic Feet) Natural Gas in Underground Storage, End of Period Change in Working Gas From Same Period Previous Year Storage Activity Base Gas Working Gas Total a Volume Percent Withdrawals Injections Net b,c 1950 Total .................... NA NA NA NA NA 175 230 -54 1955 Total .................... 863 505 1,368 40 8.7 437 505 -68 1960 Total

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    . Crude Oil and Natural Gas Resource Development Figure 5.1 Crude Oil and Natural Gas Resource Development Indicators Rotary Rigs in Operation by Type, 1949-2015 Rotary Rigs in Operation by Type, Monthly Active Well Service Rig Count, Monthly Total Wells Drilled by Type, 1949-2010 . 90 U.S. Energy Information Administration / Monthly Energy Review October 2016 Total 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 1 2 3 4 Thousand Rigs 1950 1955 1960 1965 1970 1975 1980

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    1 Crude Oil and Natural Gas Resource Development Indicators Rotary Rigs in Operation by Type, 1949-2015 Rotary Rigs in Operation by Type, Monthly Active Well Service Rig Count, Monthly Total Wells Drilled by Type, 1949-2010 . 90 U.S. Energy Information Administration / Monthly Energy Review October 2016 Total 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 1 2 3 4 Thousand Rigs 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 0 10 20 30 40 50 Thousand

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    91 Table 5.1 Crude Oil and Natural Gas Drilling Activity Measurements (Number of Rigs) Rotary Rigs in Operation a Active Well Service Rig Count c By Site By Type Total b Onshore Offshore Crude Oil Natural Gas 1950 Average ........................ NA NA NA NA 2,154 NA 1955 Average ........................ NA NA NA NA 2,686 NA 1960 Average ........................ NA NA NA NA 1,748 NA 1965 Average ........................ NA NA NA NA 1,388 NA 1970 Average ........................ NA NA NA NA 1,028

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    . Coal Figure 6.1 Coal (Million Short Tons) Overview, 1949-2015 Consumption by Sector, 1949-2015 Overview, Monthly Electric Power Sector Consumption, Monthly 96 U.S. Energy Information Administration / Monthly Energy Review October 2016 2014 20 15 2016 Electric Power Consumption J F MA M J J A S O N D J F MA M J J A S O N D J F MA M J J A S O N D 0 20 40 60 80 100 Net Exports 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 200 400 600 800 1,000 1,200 a Includes

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    1 Coal (Million Short Tons) Overview, 1949-2015 Consumption by Sector, 1949-2015 Overview, Monthly Electric Power Sector Consumption, Monthly 96 U.S. Energy Information Administration / Monthly Energy Review October 2016 2014 20 15 2016 Electric Power Consumption J F MA M J J A S O N D J F MA M J J A S O N D J F MA M J J A S O N D 0 20 40 60 80 100 Net Exports 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 200 400 600 800 1,000 1,200 a Includes combined-heat-and-power

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    7 Table 6.1 Coal Overview (Thousand Short Tons) Production a Waste Coal Supplied b Trade Stock Change d,e Losses and Unaccounted for e,f Consumption Imports Exports Net Imports c 1950 Total .................... 560,388 NA 365 29,360 -28,995 27,829 9,462 494,102 1955 Total .................... 490,838 NA 337 54,429 -54,092 -3,974 -6,292 447,012 1960 Total .................... 434,329 NA 262 37,981 -37,719 -3,194 1,722 398,081 1965 Total .................... 526,954 NA 184 51,032 -50,848 1,897

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    8 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 6.2 Coal Consumption by Sector (Thousand Short Tons) End-Use Sectors Electric Power Sector e,f Total Resi- dential Commercial Industrial Trans- portation CHP a Other b Total Coke Plants Other Industrial Total CHP c Non-CHP d Total 1950 Total .................... 51,562 g ( ) 63,021 63,021 104,014 h ( ) 120,623 120,623 224,637 63,011 91,871 494,102 1955 Total .................... 35,590 g ( ) 32,852 32,852 107,743

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    9 Table 6.3 Coal Stocks by Sector (Thousand Short Tons) Producers and Distributors End-Use Sectors Electric Power Sector c,d Total Residential a and Commercial Industrial Total Coke Plants Other b Total 1950 Year ..................... NA 2,462 16,809 26,182 42,991 45,453 31,842 77,295 1955 Year ..................... NA 998 13,422 15,880 29,302 30,300 41,391 71,691 1960 Year ..................... NA 666 11,122 11,637 22,759 23,425 51,735 75,160 1965 Year ..................... NA 353 10,640 13,122

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    5 Table 7.3c Consumption of Selected Combustible Fuels for Electricity Generation: Commercial and Industrial Sectors (Subset of Table 7.3a) Commercial Sector a Industrial Sector b Coal c Petroleum d Natural Gas e Biomass Coal c Petroleum d Natural Gas e Other Gases g Biomass Other i Waste f Wood h Waste f Thousand Short Tons Thousand Barrels Billion Cubic Feet Trillion Btu Thousand Short Tons Thousand Barrels Billion Cubic Feet Trillion Btu 1990 Total .................... 417 953 28 15 10,740

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    19 Table 7.4c Consumption of Selected Combustible Fuels for Electricity Generation and Useful Thermal Output: Commercial and Industrial Sectors (Subset of Table 7.4a) Commercial Sector a Industrial Sector b Coal c Petroleum d Natural Gas e Biomass Coal c Petroleum d Natural Gas e Other Gases g Biomass Other i Waste f Wood h Waste f Thousand Short Tons Thousand Barrels Billion Cubic Feet Trillion Btu Thousand Short Tons Thousand Barrels Billion Cubic Feet Trillion Btu 1990 Total

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    23 Table 7.6 Electricity End Use (Million Kilowatthours) Retail Sales a Direct Use f Total End Use g Residential Commercial b Industrial c Transpor- tation d Total Retail Sales e 1950 Total .................... 72,200 E 65,971 146,479 E 6,793 291,443 NA 291,443 1955 Total .................... 128,401 E 102,547 259,974 E 5,826 496,748 NA 496,748 1960 Total .................... 201,463 E 159,144 324,402 E 3,066 688,075 NA 688,075 1965 Total .................... 291,013 E 231,126 428,727 E 2,923

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    7 Table 7.1 Electricity Overview (Billion Kilowatthours) Net Generation a Trade T&D Losses f and Unaccounted for g End Use Electric Power Sector b Com- mercial Sector c Indus- trial Sector d Total Imports e Exports e Net Imports e Retail Sales h Direct Use i Total 1950 Total .................... 329 NA 5 334 2 (s) 2 44 291 NA 291 1955 Total .................... 547 NA 3 550 5 (s) 4 58 497 NA 497 1960 Total .................... 756 NA 4 759 5 1 5 76 688 NA 688 1965 Total ....................

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    9 Table 7.2a Electricity Net Generation: Total (All Sectors) (Sum of Tables 7.2b and 7.2c; Million Kilowatthours) Fossil Fuels Nuclear Electric Power Hydro- electric Pumped Storage e Renewable Energy Total j Coal a Petro- leum b Natural Gas c Other Gases d Conven- tional Hydro- electric Power f Biomass Geo- thermal Solar i Wind Wood g Waste h 1950 Total .............. 154,520 33,734 44,559 NA 0 f ( ) 100,885 390 NA NA NA NA 334,088 1955 Total .............. 301,363 37,138 95,285 NA 0 f ( )

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    3 Consumption of Selected Combustible Fuels for Electricity Generation Coal by Sector, 1989-2015 Petroleum by Sector, 1989-2015 Natural Gas by Sector, 1989-2015 Other Gases b by Sector, 1989-2015 Wood by Sector, 1989-2015 Waste by Sector, 1989-2015 112 U.S. Energy Information Administration / Monthly Energy Review October 2016 Commercial Industrial Electric Power Electric Power Industrial Industrial Total a Total a 1990 1995 2000 2005 2010 2015 0.0 0.3 0.6 0.9 1.2 Billion Short Tons Total a

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    8. Nuclear Energy Figure 8.1 Nuclear Energy Overview Electricity Net Generation, 1957-2015 Nuclear Share of Electricity Net Generation, 1957-2015 Nuclear Electricity Net Generation Capacity Factor, Monthly 128 U.S. Energy Information Administration / Monthly Energy Review October 2016 Web Page: http://www.eia.gov/totalenergy/data/monthly/#nuclear. Sources: Tables 7.2a and 8.1. 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 1 2 3 4 5 Trillion Kilowatthours Nuclear Electric Power

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    Nuclear Energy Overview Electricity Net Generation, 1957-2015 Nuclear Share of Electricity Net Generation, 1957-2015 Nuclear Electricity Net Generation Capacity Factor, Monthly 128 U.S. Energy Information Administration / Monthly Energy Review October 2016 Web Page: http://www.eia.gov/totalenergy/data/monthly/#nuclear. Sources: Tables 7.2a and 8.1. 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 1 2 3 4 5 Trillion Kilowatthours Nuclear Electric Power Total 1960 1965 1970 1975 1980

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    U .S. Energy Information Administration / Monthly Energy Review October 2016 129 Table 8.1 Nuclear Energy Overview Total Operable Units a,b Net Summer Capacity of Operable Units b,c Nuclear Electricity Net Generation Nuclear Share of Electricity Net Generation Capacity Factor d Number Million Kilowatts Million Kilowatthours Percent 1957 Total .......................... 1 0.055 10 (s) NA 1960 Total .......................... 3 .411 518 .1 NA 1965 Total .......................... 13 .793 3,657 .3

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    Nuclear Energy Note 1. Operable Nuclear Reactors. A reactor is generally defined as operable while it possessed a full-power license from the Nuclear Regulatory Commission or its predecessor the Atomic Energy Commission, or equivalent permission to operate, at the end of the year or month shown. The definition is liberal in that it does not exclude units retaining full-power licenses during long, non-routine shutdowns that for a time rendered them unable to generate electricity. Examples are:

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    9. Energy Prices Figure 9.1 Petroleum Prices Crude Oil Prices, 1949-2015 Composite Refiner Acquisition Cost, Monthly Refiner Prices to End Users: Selected Products, July 2016 132 U.S. Energy Information Administration / Monthly Energy Review October 2016 a Prices are not adjusted for inflation. See "Nominal Dollars" in Glossary. Web Page: http://www.eia.gov/totalenergy/data/monthly/#prices. Sources: Tables 9.1, 9.5, and 9.7. 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005

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    Petroleum Prices Crude Oil Prices, 1949-2015 Composite Refiner Acquisition Cost, Monthly Refiner Prices to End Users: Selected Products, July 2016 132 U.S. Energy Information Administration / Monthly Energy Review October 2016 a Prices are not adjusted for inflation. See "Nominal Dollars" in Glossary. Web Page: http://www.eia.gov/totalenergy/data/monthly/#prices. Sources: Tables 9.1, 9.5, and 9.7. 1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 0 20 40 60 80 100

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    3 Table 9.1 Crude Oil Price Summary (Dollars a per Barrel) Domestic First Purchase Price c F.O.B. Cost of Imports d Landed Cost of Imports e Refiner Acquisition Cost b Domestic Imported Composite 1950 Average .................. 2.51 NA NA NA NA NA 1955 Average .................. 2.77 NA NA NA NA NA 1960 Average .................. 2.88 NA NA NA NA NA 1965 Average .................. 2.86 NA NA NA NA NA 1970 Average .................. 3.18 NA NA E 3.46 E 2.96 E 3.40 1975 Average ..................

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    34 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 9.2 F.O.B. Costs of Crude Oil Imports From Selected Countries (Dollars a per Barrel) Selected Countries Persian Gulf Nations b Total OPEC c Total Non-OPEC c Angola Colombia Mexico Nigeria Saudi Arabia United Kingdom Venezuela 1973 Average d ................. W W - 7.81 3.25 - 5.39 3.68 5.43 4.80 1975 Average .................. 10.97 - 11.44 11.82 10.87 - 11.04 10.88 11.34 10.62 1980 Average ..................

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    5 Table 9.3 Landed Costs of Crude Oil Imports From Selected Countries (Dollars a per Barrel) Selected Countries Persian Gulf Nations b Total OPEC c Total Non-OPEC c Angola Canada Colombia Mexico Nigeria Saudi Arabia United Kingdom Venezuela 1973 Average d ............... W 5.33 W - 9.08 5.37 - 5.99 5.91 6.85 5.64 1975 Average ................ 11.81 12.84 - 12.61 12.70 12.50 - 12.36 12.64 12.70 12.70 1980 Average ................ 34.76 30.11 W 31.77 37.15 29.80 35.68 25.92 30.59 33.56 33.99 1985

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    6 U.S. Energy Information Administration / Monthly Energy Review October 2016 Table 9.4 Retail Motor Gasoline and On-Highway Diesel Fuel Prices (Dollars a per Gallon, Including Taxes) Platt's / Bureau of Labor Statistics Data U.S. Energy Information Administration Data Motor Gasoline by Grade Regular Motor Gasoline by Area Type On-Highway Diesel Fuel Leaded Regular Unleaded Regular Unleaded Premium b All Grades c Conventional Gasoline Areas d Reformulated Gasoline Areas e All Areas 1950 Average

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    7 Table 9.5 Refiner Prices of Residual Fuel Oil (Dollars a per Gallon, Excluding Taxes) Residual Fuel Oil Sulfur Content Less Than or Equal to 1% Residual Fuel Oil Sulfur Content Greater Than 1% Average Sales for Resale Sales to End Users Sales for Resale Sales to End Users Sales for Resale Sales to End Users 1978 Average ...................... 0.293 0.314 0.245 0.275 0.263 0.298 1980 Average ...................... .608 .675 .479 .523 .528 .607 1985 Average ...................... .610 .644 .560

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    ... fuel oil, excluding biodiesel. d Liquefied petroleum gases. e Finished motor gasoline, excluding fuel ethanol. f Emissions from energy consumption (for electricity and a ...

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    Consumer Price Index, All Urban Consumers a Motor Gasoline b Residential Heating Oil c Residential Natural Gas b Residential Electricity b Index 1982-1984100 Dollars per Gallon ...

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    2 Average Retail Prices of Electricity (Cents a per Kilowatthour) By Sector, 1960-2015 By ... See "Nominal Price" in Glossary. b Public street and highway lighting, interdepartmental ...

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    Finished Motor Gasoline b Finished Aviation Gasoline Kerosene- Type Jet Fuel Kerosene No. ... See "Nominal Dollars" in Glossary. b See Note 5, "Motor Gasoline Prices," at end of ...

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    a per Gallon, Excluding Taxes) Finished Motor Gasoline b Finished Aviation Gasoline ... See "Nominal Dollars" in Glossary. b See Note 5, "Motor Gasoline Prices," at end of ...

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    Table 1.8 Motor Vehicle Mileage, Fuel Consumption, and Fuel Economy Light-Duty Vehicles, Short Wheelbase a Light-Duty Vehicles, Long Wheelbase b Heavy-Duty Trucks c All Motor ...

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    ... Revenue may not correspond to sales for a particular month because of energy service provider billing and accounting procedures. That lack of correspondence could result in ...

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    the residential, commercial, and industrial sectors and "Primary Energy Total Consumption" are due, in whole or in part, to the incorporation of new distributed solar energy data. ...

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    used to convert nominal dollars to chained (2005) dollars. RRevised. NANot available. Web Pages: * See http:www.eia.govtotalenergydataannualappendices for all data...

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    Table 10.4 Biodiesel and Other Renewable Fuels Overview Biodiesel Other Renew- able Fuels f Feed- stock a Losses and Co- prod- ucts b Production Trade Stocks d Stock Change e ...

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    ... of fuel ethanol and biodiesel. c Wood and wood-derived fuels, biomass waste, and total biomass inputs to the production of fuel ethanol and biodiesel. d Hydroelectric power, ...

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    ... of fuel ethanol and biodiesel. Does not include natural gas, electricity, and other non-biomass energy used in the production of fuel ethanol and biodiesel-these are included in ...

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    Jet Fuel c Residual Fuel Oil a Beginning in 1993, includes fuel ethanol blended into motor gasoline. b Beginning in 2009, includes renewable diesel fuel (including biodiesel) ...

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    ... converted to Btu by multiplying by the biodiesel heat content factor in Table A1; for ... converted to Btu by multiplying by the biodiesel heat content factor in Table A1; for ...

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    ... be 5.359 million Btu per barrel or equal to the thermal conversion factor for Biodiesel. ... Approximate Heat Content of Biofuels Biodiesel. EIA estimated the thermal conversion ...

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    ... converted to Btu by multiplying by the biodiesel 22 U.S. Energy Information ... converted to Btu by multiplying by the biodiesel heat content factor in Table A1; for ...

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    ... Does not include biofuels. d Through 2010, data are for biodiesel only. Beginning in 2011, data are for fuel ethanol (minus denaturant) and biodiesel. RRevised. NANot available. ...

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    5 Table 10.3 Fuel Ethanol Overview Feed- stock a Losses and Co- products b Dena- turant c ... used for fuel ethanol. b Losses and co-products from the production of fuel ethanol. ...

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    7 Table 10.3 Fuel Ethanol Overview, 1981-2011 Year Feed- stock 1 Losses and Co- products 2 ... used for fuel ethanol. 2 Losses and co-products from the production of fuel ethanol. ...

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    Gas Note 1. Natural Gas Production. Final annual data are from the U.S. Energy Information Administration's (EIA) Natural Gas Annual (NGA). Data for the two most recent months ...

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    Fossil Fuels Nuclear Electric Power Hydro- electric Pumped Storage e Renewable Energy ... generation from solar thermal and photovoltaic (PV) energy at utility-scale facilities. ...

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    Coal 1,344 1,241 797 516 27 Coal Natural Nuclear Renewable Petro- 0 500 1,000 1,500 J F MA ... Note: Data are for utility-scale facilities. Web Page: http:www.eia.govtotalenergy...

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    ... Coal 1,344 1,241 797 516 27 Coal Natural Nuclear Renewable Petro- 0 500 1,000 1,500 J F MA ... Note: Data are for utility-scale facilities. Web Page: http:www.eia.govtotalenergy...

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    . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 141 10.4 Biodiesel Overview. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ....

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    Publications 330, 811, and 814. * American National Standards InstituteInstitute of Electrical and Electronic Engineers, ANSIIEEE Std 268-1992, pp. 28 and 29. degrees Celsius ...

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    ... "Annual Report of International Electrical ExportImport Data." 1989: DOE, Fossil Energy, Form FE-781R, "Annual Report of International Electrical ExportImport Data." 1990-2000: ...

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    0 U.S. Energy Information Administration Monthly Energy Review June 2016 Table A4. Approximate Heat Content of Natural Gas (Btu per Cubic Foot) Production Consumption a Imports ...

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    EIA, International Energy Statistics Database, June 2016. All Other Countries and ... EIA, International Energy Statistics Database, June 2016. 172 U.S. Energy Information ...

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    Power Sector. . . . . . . . . . . . . . . . 165 12.7 Carbon Dioxide Emissions From Biomass Energy Consumption . . . . . . . . . . . . . . . . . . . . . . . . . . . 166...

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    in the United States, Selected Years, 1635-1945 (Quadrillion Btu) Year Fossil Fuels Renewable Energy Electricity Net Imports Total Coal Natural Gas Petroleum Total...

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    . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 128 9.10 Cost of Fossil-Fuel Receipts at Electric Generating Plants. . . . . . . . . . . . . . . . . . . . . . . ....

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    . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 127 9.9 Cost of Fossil-Fuel Receipts at Electric Generating Plants. . . . . . . . . . . . . . . . . . . . . . . ....

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    Btu of coal coke net imports. 4 Conventional hydroelectric power, geothermal, solarphotovoltaic, wind, and biomass. 5 Includes industrial combined-heat-and-power (CHP)...

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    Gas 3 Other Gases 4 Total Conventional Hydroelectric Power 6 Biomass Geo- thermal SolarPV 9 Wind Total Wood 7 Waste 8 1949 135.5 28.5 37.0 NA 201.0 0.0 6 ( ) 89.7 0.4 NA NA...

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    1,000 2,000 3,000 4,000 5,000 6,000 Degree-Days 30-Year Normal 1 Excludes Alaska and Hawaii. 2 Based on calculations of data from 1971 through 2000. Note: See Appendix C for map...

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    2005 2010 0 500 1,000 1,500 2,000 Degree-Days 30-Year Normal 1 Excludes Alaska and Hawaii. 2 Based on calculations of data from 1971 through 2000. Note: See Appendix C for map...

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    Manufacturing Energy Consumption for All Purposes, 2006 By Energy Source By North American Industry Classification System (NAICS) Code 6 46 U.S. Energy Information Administration / Annual Energy Review 2011 1 Liquefied petroleum gases. 2 Natural gas liquids. 3 See "Breeze" in Glossary. 4 Includes all other types of energy that respondents indicated were consumed or allocated. 5 Energy sources produced onsite from the use of other energy sources but sold or trans- ferred to another

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    2 Natural Gas Production Gross Withdrawals and Dry Gas Production, 1949-2011 Production Flow, 2011 (Trillion Cubic Feet) Gross Withdrawals by Well Type, 2011 180 U.S. Energy Information Administration / Annual Energy Review 2011 Dry Gas Production 1 Volume reduction resulting from the removal of natural gas plant liquids, which are trans- ferred to petroleum supply. 2 Includes natural gas gross withdrawals from coalbed wells and shale gas wells. Source: Table 6.2. Gross Withdrawals 1950 1960

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    7 Coal Mining Productivity Total, 1949-2011 By Mining Method, 2011 By Location, 2011 By Mining Method, 1 1949-2011 By Region and Mining Method, 2011 210 U.S. Energy Information Administration / Annual Energy Review 2011 Mississippi 1 For 1979 forward, includes all coal; prior to 1979, excludes anthracite. Note: Beginning in 2001, surface mining includes a small amount of refuse recovery. Source: Table 7.7. 2.68 15.98 East of the West of the 0 5 10 15 20 Short Tons per Employee Hour 1950 1960

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    Energy GSA 1 HHS 2 Interior Justice NASA 3 Postal Service Trans- portation Veterans Affairs Other 4 Total 1975 9.5 1,360.2 50.4 22.3 6.5 9.4 5.9 13.4 30.5 19.3 27.1 10.5...

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    2 U.S. Energy Information Administration Annual Energy Review 2011 Table A2. Approximate Heat Content of Petroleum Production, Imports, and Exports, Selected Years, 1949-2011...

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    Transportation Sector Electric Power Sector 2 Total CHP 3 Other 4 Total Coke Plants Other Industrial Total Electricity Only CHP Total CHP 5 Non-CHP 6 Total 1949 52.4 7 ( ) 64.1 ...

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    historical energy statistics. Included are statistics on total energy production, consumption, trade, and energy prices; overviews of petroleum, natural gas, coal, electricity,...

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    retail sales to ultimate customers by electric utilities and, beginning in 1996, other energy service providers. 8 Use of electricity that is 1) self-generated, 2)...

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    3 Table 1.10 Cooling Degree-Days by Census Division, Selected Years, 1949-2011 Year New England Middle Atlantic East North Central West North Central South Atlantic East South...

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    Administration Annual Energy Review 2011 1 General Services Administration. 2 Health and Human Services. 3 National Aeronautics and Space Administration. 4 See Table 1.11...

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    (HFCs), perfluorocarbons (PFCs), and sulfur hexafluoride-that are transparent to solar (short- wave) radiation but opaque to long-wave (infrared) radiation, thus...

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    Census divisions and the national average. * See Appendix C for map of Census divisions. Web Pages: * See http:www.eia.govtotalenergydataannualsummary for all data...

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    U.S. Energy Information Administration (EIA) (indexed site)

    State figures are aggregated into Census divisions and the national average. Web Pages: * See http:www.eia.govtotalenergydataannualsummary for all data...

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    U.S. Department of Energy (DOE) all webpages (Extended Search)

    3 Table 9.2 Nuclear Power Plant Operations, 1957-2011 Year Nuclear Electricity Net Generation Nuclear Share of Total Electricity Net Generation Net Summer Capacity of Operable ...

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    Gasoline and Diesel Fuel Update

    Electric Power Sector f,g Total Resi- dential Com- mercial a Industrial Transportation Lease and Plant Fuel Other Industrial Total Pipelines d and Dis- tribution e Vehicle Fuel ...

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    Gasoline and Diesel Fuel Update

    Residential Commercial c Industrial d Transportation Electric Power e Price h Percentage of Sector i Price h Percentage of Sector i Price h Percentage of Sector i Vehicle Fuel j ...

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    ... Delivered- to-consumers prices for 1987 forward represent natural gas delivered and sold to residential, commercial, indus- trial, vehicle fuel, and electric power consumers. They ...

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    Annual Energy Outlook

    ... monthly and annual data. * See http:www.eia.govpetroleum for related information. ... 1976-Federal Energy Administration (FEA), Form FEA-96, "Monthly Cost Allocation ...

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 a Exact conversion. b Calculated by the U.S. Energy Information Administration. Web Page: For related information, see http:www.eia.govtotalenergydataannualappendices....

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    U.S. Energy Information Administration (EIA) (indexed site)

    Sources: * 1949-1975-Bureau of Mines, Minerals Yearbook, "Coke and Coal Chemicals" chapter. * 1976-1980-U.S. Energy Information Administration (EIA), Energy Data Report, Coke and ...

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    U.S. Energy Information Administration (EIA) (indexed site)

    Total g Coal c Petro- leum d Natural Gas e Other Gases h Hydro- electric Power i Biomass ... and 5,024 million kilowatthours in 2015. h Blast furnace gas, and other manufactured ...

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    Average Productivity 122 U.S. Energy Information Administration Annual Energy Review 2011 1 United States excluding Alaska and Hawaii. Note: Crude oil includes lease condensate. ...

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    U.S. Energy Information Administration (EIA) (indexed site)

    Stock Change j Adjust- ments c,k Petroleum Products Supplied Crude Oil b,c NGPL e Total c Im- ports h Ex- ports Net Imports i 48 States d Alaska Total 1950 Average ...

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    Annual Energy Outlook

    Pentanes Plus 4 Total Ethane 2 Isobutane Normal Butane 3 Propane 2,3 Total 1949 53 8 11 61 ... 2 Reported production of ethane-propane mixtures has been allocated 70 percent ...

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    Gasoline and Diesel Fuel Update

    Carbon Dioxide Emissions From Energy Consumption by Sector, 1949-2011 Residential and Commercial, by Major Source Industrial, by Major Source Transportation, by Major Source ...

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    Gasoline and Diesel Fuel Update

    based on 2013 Petroleum Supply Monthly data) Preliminary Crude Imports by Top 10 Countries of Origin (ranking based on 2013 Petroleum Supply Monthly data) (Thousand Barrels per Day) Period: Weekly 4-Week Average Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Country 10/07/16 10/14/16 10/21/16 10/28/16 11/04/16 11/11/16 View History 1- Canada 3,203 2,945 2,885 3,282 3,206 3,243 2010-2016 2- Saudi Arabia 951 703 983 1,170 1,295

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    Annual Energy Outlook

    3 (Million Barrels per Day) 1 Unfinished oils, hydrogenoxygenatesrenewablesother hydrocarbons, and motor gasoline and aviation gasoline blending components. 2 Renewable fuels...

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    other manufactured and waste gases derived from fossil fuels. 2 Batteries, chemicals, hydrogen, pitch, purchased steam, sulfur, miscellaneous technologies, and non-renewable waste...

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    Flow, 2014 (Trillion Cubic Feet) 1 Natural gas plant liquids production (NGPL), gaseous equivalent. 2 Quantities lost and imbalances in data due to differences among data sources. ...

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    3 (Trillion Cubic Feet) 1 Natural gas plant liquids production (NGPL), gaseous equivalent. 2 Quantities lost and imbalances in data due to differences among data sources. Excludes...

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    Annual Energy Outlook

    3 (Million Short Tons) Notes: * Production categories are estimated; all data are preliminary. * Values are derived from source data prior to rounding for publication. * Totals may...

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    Gasoline and Diesel Fuel Update

    6,487 33,575 26,955 42,270 64,056 51,127 1980-2015 Alabama 968 829 583 759 1,869 1,130 1980-2015 Alaska 0 0 0 0 0 0 1999-2015 Arkansas 40 53 48 40 42 55 1980-2015 California 54 66 36 92 82 51 1980-2015 Colorado 0 0 0 0 0 0 1980-2015 Connecticut 473 526 484 626 1,359 1,810 1980-2015 Delaware 76 96 66 131 128 131 1980-2015 Georgia 2,314 764 719 180 4,046 3,339 1980-2015 Idaho 72 166 73 271 740 117 1981-2015 Illinois 325 530 331 362 503 230 1980-2015 Indiana 1,148 989 977 1,005 1,422 830 1980-2015

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    3 Table 10.2b Renewable Energy Consumption: Industrial and Transportation Sectors, Selected Years, 1949-2011 (Trillion Btu) Year Industrial Sector 1 Transportation Sector Hydro- electric Power 2 Geo- thermal 3 Solar/PV 4 Wind 5 Biomass Total Biomass Wood 6 Waste 7 Fuel Ethanol 8 Losses and Co-products 9 Total Fuel Ethanol 10 Biodiesel Total 1949 76 NA NA NA 468 NA NA NA 468 544 NA NA NA 1950 69 NA NA NA 532 NA NA NA 532 602 NA NA NA 1955 38 NA NA NA 631 NA NA NA 631 669 NA NA NA 1960 39 NA NA NA

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    Gasoline and Diesel Fuel Update

    6 U.S. Energy Information Administration / Annual Energy Review 2011 Table A6. Approximate Heat Rates for Electricity, and Heat Content of Electricity, Selected Years, 1949-2011 (Btu per Kilowatthour) Year Approximate Heat Rates 1 for Electricity Net Generation Heat Content 10 of Electricity 11 Fossil Fuels 2 Nuclear 8 Noncombustible Renewable Energy 7,9 Coal 3 Petroleum 4 Natural Gas 5 Total Fossil Fuels 6,7 1949 NA NA NA 15,033 - - 15,033 3,412 1950 NA NA NA 14,030 - - 14,030 3,412 1955 NA NA

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    Gasoline and Diesel Fuel Update

    Table 1.5 Energy Consumption, Expenditures, and Emissions Indicators Estimates, Selected Years, 1949-2011 Year Energy Consumption Energy Consumption per Capita Energy Expenditures 1 Energy Expenditures 1 per Capita Gross Output 3 Energy Expenditures 1 as Share of Gross Output 3 Gross Domestic Product (GDP) Energy Expenditures 1 as Share of GDP Gross Domestic Product (GDP) Energy Consumption per Real Dollar of GDP Carbon Dioxide Emissions 2 per Real Dollar of GDP Quadrillion Btu Million Btu

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    Gasoline and Diesel Fuel Update

    9 Table 2.8 Motor Vehicle Mileage, Fuel Consumption, and Fuel Economy, Selected Years, 1949-2010 Year Light-Duty Vehicles, Short Wheelbase 1 Light-Duty Vehicles, Long Wheelbase 2 Heavy-Duty Trucks 3 All Motor Vehicles 4 Mileage Fuel Consumption Fuel Economy Mileage Fuel Consumption Fuel Economy Mileage Fuel Consumption Fuel Economy Mileage Fuel Consumption Fuel Economy Miles per Vehicle Gallons per Vehicle Miles per Gallon Miles per Vehicle Gallons per Vehicle Miles per Gallon Miles per vehicle

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    Gasoline and Diesel Fuel Update

    3 Table 2.1d Industrial Sector Energy Consumption Estimates, Selected Years, 1949-2011 (Trillion Btu) Year Primary Consumption 1 Electricity Retail Sales 11 Electrical System Energy Losses 12 Total Fossil Fuels Renewable Energy 2 Total Primary Coal Coal Coke Net Imports Natural Gas 3 Petroleum 4,5 Total Hydroelectric Power 6 Geothermal 7 Solar/PV 8 Wind 9 Biomass 10 Total 1949 5,433 -7 3,188 3,475 12,090 76 NA NA NA 468 544 12,633 418 1,672 14,724 1950 5,781 1 3,546 3,960 13,288 69 NA NA NA 532

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    Gasoline and Diesel Fuel Update

    1 Table 5.1b Petroleum Overview, Selected Years, 1949-2011 (Thousand Barrels per Day) Year Field Production 1 Renewable Fuels and Oxygenates 5 Processing Gain 6 Trade Stock Change 8,10 Adjust- ments 11 Petroleum Products Supplied 8 Crude Oil 2 Natural Gas Plant Liquids 4 Total Imports 7,8 Exports Net Imports 8,9 48 States 3 Alaska Total 1949 5,046 0 5,046 430 5,477 NA -2 645 327 318 -8 -38 5,763 1950 5,407 0 5,407 499 5,906 NA 2 850 305 545 -56 -51 6,458 1955 6,807 0 6,807 771 7,578 NA 34 1,248

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    Gasoline and Diesel Fuel Update

    27 Table 8.2d Electricity Net Generation: Commercial and Industrial Sectors, Selected Years, 1989-2011 (Subset of Table 8.2a; Billion Kilowatthours) Year Fossil Fuels Nuclear Electric Power Hydro- electric Pumped Storage 5 Renewable Energy Other 9 Total Coal 1 Petroleum 2 Natural Gas 3 Other Gases 4 Total Conventional Hydroelectric Power Biomass Geo- themal Solar/PV 8 Wind Total Wood 6 Waste 7 Commercial Sector 10 1989 0.7 0.6 2.2 0.1 3.6 - - 0.1 0.1 0.5 - - - 0.7 - 4.3 1990 .8 .6 3.3 .1 4.8 - -

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    Annual Energy Outlook

    . Energy Consumption by Sector THIS PAGE INTENTIONALLY LEFT BLANK Figure 2.0 Primary Energy Consumption by Source and Sector, 2011 (Quadrillion Btu) U.S. Energy Information ...

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    Gasoline and Diesel Fuel Update

    Note 1. Emissions of Carbon Dioxide and Other Green- house Gases. Greenhouse gases are those gases-such as water vapor, carbon dioxide (CO 2 ), methane, nitrous oxide, ...

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    Office of Energy Efficiency and Renewable Energy (EERE) (indexed site)

    Basic Protective Force Training Program DOE/IG-0641 March 2004 * None of the 10 sites included instruction in rappelling even though it was part of the special response team core curriculum and continued to be offered by the Nonprolif- eration and National Security Institute; * Only one site conducted basic training on use of a shotgun, despite the fact that a num- ber of sites used the weapon for breaching exercises and other purposes; and, * Seven of the sites modified prescribed training

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    ... Census Bureau Annual Survey of Manufactures or Census of Manufactures. For 1978 and 1979, monthly estimates were derived from data reported on Forms EIA-3 and 100 U.S. Energy ...

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    Data presented in the Monthly Energy Review and in other U.S. Energy Information Administration publications are expressed predominately in units that historically have been used in the United States, such as British thermal units, barrels, cubic feet, and short tons. The metric conversion factors presented in Table B1 can be used to calculate the metric-unit equivalents of values expressed in U.S. Customary units. For example, 500 short tons are the equivalent of 453.6 metric tons (500 short

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Estimated Number of Alternative-Fueled Vehicles in Use and Alternative Fuel Consumption Vehicles in Use, 1995-2010 Vehicles in Use by Fuel Type, 2010 Fuel Consumption, 5 1995-2010 Fuel Consumption by Type, 2010 290 U.S. Energy Information Administration / Annual Energy Review 2011 1 Ethanol, 85 percent (E85). Includes only those E85 vehicles believed to be used as alternative-fueled vehicles, primarily fleet-operated vehicles; excludes other vehicles with E85- fueling capability. 2 Liquefied

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 10.5 Estimated Number of Alternative-Fueled Vehicles in Use and Fuel Consumption, 1992-2010 Year Alternative and Replacement Fuels 1 Liquefied Petroleum Gases Compressed Natural Gas Liquefied Natural Gas Methanol, 85 Percent (M85) 3 Methanol, Neat (M100) 4 Ethanol, 85 Percent (E85) 3,5 Ethanol, 95 Percent (E95) 3 Elec- tricity 6 Hydro- gen Other Fuels 7 Subtotal Oxygenates 2 Bio- diesel 10 Total Methyl Tertiary Butyl Ether 8 Ethanol in Gasohol 9 Total Alternative-Fueled Vehicles in Use

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    6 Solar Thermal Collector Shipments by Type, Price, and Trade Total Shipments, 1974-2009 Trade, 1978-2009 Price of Total Shipments, 1986-2009 Number of U.S. Manufacturers by Type of Collector, 1974-2009 Average Annual Shipments per Manufacturer, 1974-2009 292 U.S. Energy Information Administration / Annual Energy Review 2011 1 Prices are not adjusted for inflation. See "Nominal Dollars" in Glossary. 2 Collectors that generally operate in the temperature range of 140 degrees Fahrenheit

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 10.6 Solar Thermal Collector Shipments by Type, Price, and Trade, 1974-2009 (Thousand Square Feet, Except as Noted) Year Low-Temperature Collectors 1 Medium-Temperature Collectors 2 High-Temperature Collectors 3 Total Shipments Trade Number of U.S. Manu- facturers Quantity Shipped Shipments per Manu- facturer Price 4 (dollars 5 per square foot) Number of U.S. Manu- facturers Quantity Shipped Shipments per Manu- facturer Price 4 (dollars 5 per square foot) Quantity Shipped Price 4

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    7 Solar Thermal Collector Domestic Shipments by Market Sector, End-Use, and Type, 2009 End Use Market Sector Type of Collector End Use by Type of Collector 294 U.S. Energy Information Administration / Annual Energy Review 2011 1 Combined space and water heating. 2 Space heating, combined heating, and space cooling. 3 Collectors that generally operate at temperatures below 110 degrees Fahrenheit. 4 Collectors that generally operate in the temperature range of 140 degrees Fahrenheit to 180 degrees

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 10.7 Solar Thermal Collector Shipments by Market Sector, End Use, and Type, 2001-2009 (Thousand Square Feet) Year and Type By Market Sector By End Use Total Residential Commercial 1 Industrial 2 Electric Power 3 Other 4 Pool Heating Water Heating Space Heating Space Cooling Combined Heating 5 Process Heating Electricity Generation Total Shipments 6 2001 Total .... 10,125 1,012 17 1 35 10,797 274 70 0 12 34 2 11,189 Low 7 .......... 9,885 987 12 0 34 10,782 42 61 0 0 34 0 10,919 Medium 8

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    U.S. Energy Information Administration (EIA) (indexed site)

    8 Photovoltaic Cell and Module Shipments, Trade, and Prices Number of U.S. Companies Reporting Shipments, 1982-2010 Total Shipments, 1982-2010 Trade, Modules Only, 1996-2010 Prices, 1989-2010 296 U.S. Energy Information Administration / Annual Energy Review 2011 1 Prices are not adjusted for inflation. See "Nominal Dollars" in Glossary. Note: Shipments are for domestic and export shipments, and may include imports that subsequently were shipped to domestic or foreign customers. Source:

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    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 10.8 Photovoltaic Cell and Module Shipments by Type, Trade, and Prices, 1982-2010 Year U.S. Companies Reporting Shipments Shipments Trade Prices 1 Crystalline Silicon Thin-Film Total 2 Imports Exports Cells Modules Cells and Modules Modules Only Cells and Modules Modules Only Cells and Modules Modules Only Cells and Modules Modules Only Cells and Modules Modules Only Number Peak Kilowatts 3 Dollars 4 per Peak Watt 3 1982 19 NA NA NA NA 6,897 NA NA NA NA NA NA NA 1983 18 NA NA NA NA

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    U.S. Energy Information Administration (EIA) (indexed site)

    9 U.S. Shipments of Photovoltaic Modules Only by Sector and End Use, 2010 By End Use By Sector 298 U.S. Energy Information Administration / Annual Energy Review 2011 1 See "Electric Power Grid" in Glossary. 2 Photovoltaic modules that are connected to the electric power grid, and whose output is fed directly into the grid. 3 Photovoltaic modules that are connected to the electric power grid, and whose output is consumed mainly onsite. 4 Photovoltaic modules that are not connected to

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    U.S. Energy Information Administration (EIA) (indexed site)

    9 Table 10.9 Photovoltaic Cell and Module Shipments by Sector and End Use, 1989-2010 (Peak Kilowatts 1 ) Year By Sector By End Use Total Residential Commercial 3 Industrial 4 Electric Power 5 Other 6 Grid-Connected 2 Off-Grid 2 Centralized 7 Distributed 8 Domestic 9 Non-Domestic 10 Total Shipments of Photovoltaic Cells and Modules 11 1989 1,439 R 6,057 3,993 785 551 12 ( ) 12 1,251 2,620 8,954 12,825 1990 1,701 R 8,062 2,817 826 432 12 ( ) 12 469 3,097 10,271 13,837 1991 3,624 R 5,715 3,947

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    U.S. Energy Information Administration (EIA) (indexed site)

    Methane Emissions Total, 1980-2009 By Source, 2009 Energy Sources by Type 1980-2009 Agricultural Sources by Major Type, 1980-2009 310 U.S. Energy Information Administration / Annual Energy Review 2011 1 Chemical production, and iron and steel production. 2 Natural gas production, processing, and distribution. 3 Petroleum production, refining, and distribution. 4 Consumption of coal, petroleum, natural gas, and wood for heat or electricity. 5 Emissions from passenger cars, trucks, buses,

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 11.3 Methane Emissions, 1980-2009 (Million Metric Tons of Methane) Year Energy Sources Waste Management Agricultural Sources Industrial Processes 9 Total 5 Coal Mining Natural Gas Systems 1 Petroleum Systems 2 Mobile Com- bustion 3 Stationary Com- bustion 4 Total 5 Landfills Waste- water Treatment 6 Total 5 Enteric Fermen- tation 7 Animal Waste 8 Rice Cultivation Crop Residue Burning Total 5 1980 3.06 4.42 NA 0.28 0.45 8.20 10.52 0.52 11.04 5.47 2.87 0.48 0.04 8.86 0.17 28.27 1981 2.81

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    U.S. Energy Information Administration (EIA) (indexed site)

    4 Nitrous Oxide Emissions Total, 1980-2009 By Source, 2009 Energy Sources by Type, 1980-2009 Agricultural Sources by Major Type, 1980-2009 312 U.S. Energy Information Administration / Annual Energy Review 2011 1 Adipic acid production (primarily for the manufacture of nylon fibers and plastics) and nitric acid production (primarily for fertilizers). 2 Emissions from passenger cars and trucks; air, rail, and marine transportation; and farm and construction equipment. 3 Consumption of coal,

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 11.4 Nitrous Oxide Emissions, 1980-2009 (Thousand Metric Tons of Nitrous Oxide) Year Energy Sources Waste Management Agricultural Sources Industrial Processes 3 Total Mobile Combustion 1 Stationary Combustion 2 Total Waste Combustion Human Sewage in Wastewater Total Nitrogen Fertilization of Soils Crop Residue Burning Solid Waste of Domesticated Animals Total 1980 60 44 104 1 10 11 364 1 75 440 88 642 1981 63 44 106 1 10 11 364 2 74 440 84 641 1982 67 42 108 1 10 11 339 2 74 414 80 614

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Emissions From Energy Consumption for Electricity Generation and Useful Thermal Output Emissions by Type of Generating Unit, 2010 Emissions by Sector, 1989-2010 314 U.S. Energy Information Administration / Annual Energy Review 2011 5.0 (s) 0.2 0.2 0 1 2 3 4 5 6 Million Metric Tons of Gas Sulfur Dioxide ¹ For carbon dioxide: municipal solid waste from non-biogenic sources; tire-derived fuel, and geothermal. For sulfur dioxide and nitrogen oxides: blast furnace gas, propane gas, and other

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 11.5a Emissions From Energy Consumption for Electricity Generation and Useful Thermal Output: Total (All Sectors), 1989-2010 (Sum of Tables 11.5b and 11.5c; Thousand Metric Tons of Gas) Year Carbon Dioxide 1 Sulfur Dioxide Nitrogen Oxides Coal 2 Natural Gas 3 Petroleum 4 Geo- thermal 5 Non- Biomass Waste 6 Total Coal 2 Natural Gas 3 Petroleum 4 Other 7 Total Coal 2 Natural Gas 3 Petroleum 4 Other 7 Total 1989 1,573,566 218,384 145,399 363 5,590 1,943,302 14,469 1 984 39 15,493 7,281 495

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    U.S. Energy Information Administration (EIA) (indexed site)

    6 U.S. Energy Information Administration / Annual Energy Review 2011 Table 11.5b Emissions From Energy Consumption for Electricity Generation and Useful Thermal Output: Electric Power Sector, 1989-2010 (Subset of Table 11.5a; Thousand Metric Tons of Gas) Year Carbon Dioxide 1 Sulfur Dioxide Nitrogen Oxides Coal 2 Natural Gas 3 Petroleum 4 Geo- thermal 5 Non- Biomass Waste 6 Total Coal 2 Natural Gas 3 Petroleum 4 Other 7 Total Coal 2 Natural Gas 3 Petroleum 4 Other 7 Total 1989 1,520,230 169,653

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    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 11.5c Emissions From Energy Consumption for Electricity Generation and Useful Thermal Output: Commercial and Industrial Sectors, 1989-2010 (Subset of Table 11.5a; Thousand Metric Tons of Gas) Year Carbon Dioxide 1 Sulfur Dioxide Nitrogen Oxides Coal 2 Natural Gas 3 Petroleum 4 Geo- thermal 5 Non- Biomass Waste 6 Total Coal 2 Natural Gas 3 Petroleum 4 Other 7 Total Coal 2 Natural Gas 3 Petroleum 4 Other 7 Total Commercial Sector 8 1989 2,320 1,542 637 - 804 5,303 37 (s) 5 1 43 9 3 2 3 17

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    U.S. Energy Information Administration (EIA) (indexed site)

    6 Installed Nameplate Capacity of Fossil-Fuel Steam-Electric Generators With Environmental Equipment By Fuel and Equipment Type, 2010 Total Units by Equipment Type, 1985-2010² Coal Units by Equipment Type, Petroleum and Natural Gas Units 1985-2010² by Equipment Type, 1985-2010² 318 U.S. Energy Information Administration / Annual Energy Review 2011 Coal Units Petroleum and Natural Gas Units Particulate Collectors Thousand Megawatts 329 165 185 26 75 1 Particulate Collectors Cooling Towers Flue

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    U.S. Energy Information Administration (EIA) (indexed site)

    9 Table 11.6 Installed Nameplate Capacity of Fossil-Fuel Steam-Electric Generators With Environmental Equipment, 1985-2010 (Megawatts) Year Coal Petroleum and Natural Gas Total 1 Particulate Collectors Cooling Towers Flue Gas Desulfurization (Scrubbers) Total 2 Particulate Collectors Cooling Towers Flue Gas Desulfurization (Scrubbers) Total 2 Particulate Collectors Cooling Towers Flue Gas Desulfurization (Scrubbers) Total 2 1985 302,056 120,591 56,955 304,706 36,054 28,895 65 62,371 338,110

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    U.S. Energy Information Administration (EIA) (indexed site)

    Carbon Dioxide Emissions From Energy Consumption Total¹ 1949-2011 Economic Growth and Carbon Dioxide Emissions, 1949-2011 By Major Source, 1949-2011 By Biomass¹ Source, 2011 302 U.S. Energy Information Administration / Annual Energy Review 2011 ¹ Carbon dioxide emissions from biomass energy consumption are excluded from total emissions. See Note, "Accounting for Carbon Dioxide Emissions From Biomass Energy Combustion," at end of section. 2 Metric tons of carbon dioxide can be

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    U.S. Energy Information Administration (EIA) (indexed site)

    Introduction This year, the U.S. Energy Information Administration (EIA) has examined different ways to represent energy consumption in the Annual Energy Review (AER). This examination centered on two methods for representing related aspects of energy consumption and losses. The first is an alternative method for deriving the energy content of noncombustible renewable resources, which has been implemented in AER 2010 (Table 1.3). The second is a new representation of delivered total energy and

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    U.S. Energy Information Administration (EIA) (indexed site)

    F1. Conversion Efficiencies of Noncombustible Renewable Energy Sources (Percent) 1 Efficiencies may vary significantly for each technology based on site-specific technology and environmental factors. Factors shown represent engineering estimates for typical equipment under specific operational conditions. Sources: Geothermal: Estimated by EIA on the basis of an informal survey of relevant plants. Conventional Hydroelectric: Based on published estimates for the efficiency of large-scale

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    U.S. Energy Information Administration (EIA) (indexed site)

    F1. Primary Energy Consumption and Delivered Total Energy, 2010 (Quadrillion Btu) U.S. Energy Information Administration / Annual Energy Review 2011 347 Primary Energy Consumption by Source 1 Delivered Total Energy by Sector 8 1 Includes electricity net imports, not shown separately. 2 Does not include biofuels that have been blended with petroleum-biofuels are included in "Renewable Energy." 3 Excludes supplemental gaseous fuels. 4 Includes less than 0.1 quadrillion Btu of coal coke

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    U.S. Energy Information Administration (EIA) (indexed site)

    Includes Adjustment for Fossil Fuel Equivalence. See "Primary Energy Consumption" in Glossary. 2 Includes electricity sales to each sector in addition to Primary Energy consumed in the sector. 3 Small amounts of coal consumed for transportation are reported as industrial sector consumption. Includes net imports of s upplemental liquids and coal coke. 4 Calculated as the primary energy consumed by the electric power sector minus the energy content of electricity retail sales. 26,784

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    U.S. Energy Information Administration (EIA) (indexed site)

    chemical compounds composed of carbon, hydrogen, and oxygen. The series of molecules vary in chain length and are composed of a hydrocarbon plus a hydroxyl group: CH 3 -(CH 2 )n-OH (e.g., metha- nol, ethanol, and tertiary butyl alcohol). See Fuel Ethanol. Alternative Fuel: Alternative fuels, for transportation applications, include the following: methanol; denatured ethanol, and other alcohols; fuel mixtures contain- ing 85 percent or more by volume of methanol, denatured ethanol, and other

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    U.S. Energy Information Administration (EIA) (indexed site)

    State-Level Energy Consumption Estimates and Estimated Consumption per Capita, 2010 Consumption Consumption per Capita 14 U.S. Energy Information Administration / Annual Energy Review 2011 TX CA FL LA IL OH PA NY GA IN MI NC VA NJ TN WA KY AL MO MN WI SC OK CO IA MD AZ MA MS KS AR OR NE UT CT WV NM NV AK WY ID ND ME MT SD NH HI DE RI DC VT 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 0 2 4 6 8 10

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    U.S. Energy Information Administration (EIA) (indexed site)

    Table 1.6 State-Level Energy Consumption, Expenditure, and Price Estimates, 2010 Rank Consumption Consumption per Capita Expenditures 1 Expenditures 1 per Capita Prices 1 Trillion Btu Million Btu Million Dollars 2 Dollars 2 Dollars 2 per Million Btu 1 Texas 11,769.9 Wyoming 948.1 Texas 137,532 Alaska 8,807 Hawaii 30.75 2 California 7,825.7 Alaska 898.5 California 117,003 Louisiana 8,661 District of Columbia 26.19 3 Florida 4,381.9 Louisiana 894.4 New York 61,619 Wyoming 7,904 Connecticut 25.63

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    U.S. Energy Information Administration (EIA) (indexed site)

    Table 1.13 U.S. Government Energy Consumption by Agency and Source, Fiscal Years 2003, 2010, and 2011 (Trillion Btu) Resource and Fiscal Years Agriculture Defense Energy GSA 1 HHS 2 Interior Justice NASA 3 Postal Service Trans- portation Veterans Affairs Other 4 Total Coal 2003 ..................................... (s) 15.4 2.0 0.0 (s) (s) 0.0 0.0 0.0 0.0 0.2 0.0 17.7 2010 ..................................... (s) 15.5 4.5 .0 0.0 0.0 .0 .0 (s) .0 .1 .0 20.1 2011 P

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    U.S. Energy Information Administration (EIA) (indexed site)

    4 Sales of Fossil Fuels Produced on Federal and American Indian Lands Total, Fiscal Years¹ 2003-2011 Federal and American Indian Lands Fossil Fuels Sales as Share of Total U.S. Fossil Fuels Production, Fiscal Years¹ 2003-2011 By Source, Fiscal Years¹ 2003-2011 Federal and American Indian Lands Fossil Fuels Sales as Share of Total U.S. Fossil Fuels Production, By Source, Fiscal Year¹ 2011 30 U.S. Energy Information Administration / Annual Energy Review 2011 ¹ The U.S. Government's fiscal

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 1.14 Sales of Fossil Fuels Produced on Federal and American Indian Lands, Fiscal Years 2003-2011 Fiscal Year 7 Crude Oil and Lease Condensate Natural Gas Plant Liquids 1 Natural Gas 2 Coal 3 Total Fossil Fuels 4 Sales 5,6 Sales as Share of Total U.S. Production Sales 5,6 Sales as Share of Total U.S. Production Sales 5,6 Sales as Share of Total U.S. Production Sales 5,6 Sales as Share of Total U.S. Production Sales 5,6 Sales as Share of Total U.S. Production Million Barrels Quadrillion

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    U.S. Energy Information Administration (EIA) (indexed site)

    Table 1.15 Non-Combustion Use of Fossil Fuels, Selected Years, 1980-2011 Year Petroleum Products Natural Gas 4 Coal Total Percent of Total Energy Consumption Asphalt and Road Oil Liquefied Petroleum Gases 1 Lubricants Petro- chemical Feedstocks 2 Petroleum Coke Special Naphthas Other 3 Total Physical Units 5 1980 145 230 58 253 R 14 37 58 R 795 639 2.4 - - - - 1985 156 R 278 53 144 R 16 30 41 R 719 500 1.1 - - - - 1990 176 R 373 60 199 20 20 39 R 887 R 567 .6 - - - - 1991 162 R 426 53 203 17 17

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    U.S. Energy Information Administration (EIA) (indexed site)

    Manufacturing Energy Consumption for All Purposes, 2006 By Energy Source By North American Industry Classification System (NAICS) Code 6 46 U.S. Energy Information Administration / Annual Energy Review 2011 1 Liquefied petroleum gases. 2 Natural gas liquids. 3 See "Breeze" in Glossary. 4 Includes all other types of energy that respondents indicated were consumed or allocated. 5 Energy sources produced onsite from the use of other energy sources but sold or trans- ferred to another

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 2.4 Household 1 Energy Consumption by Census Region, Selected Years, 1978-2009 (Quadrillion Btu, Except as Noted) Census Region 2 1978 1979 1980 1981 1982 1984 1987 1990 1993 1997 2001 2005 2009 United States Total (does not include wood) ...... 10.56 9.74 9.32 9.29 8.58 9.04 9.13 9.22 10.01 10.25 9.86 10.55 10.18 Natural Gas ........................................................ 5.58 5.31 4.97 5.27 4.74 4.98 4.83 4.86 5.27 5.28 4.84 4.79 4.69 Electricity 3

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    U.S. Energy Information Administration (EIA) (indexed site)

    Household Energy Consumption and Expenditures Household Energy Consumption by End Use, Selected Years, Household Energy Expenditures, Selected Years, 1978-2005¹ 1978-2005¹ Household Energy Consumption for Space Heating by Fuel 2005 Appliances, Electronics, and Lighting Expenditures, Selected Years, 1978-2005¹ 52 U.S. Energy Information Administration / Annual Energy Review 2011 1 For years not shown, there are no data available. 2 Prices are not adjusted for inflation. See "Nominal

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 2.5 Household 1 Energy Consumption and Expenditures by End Use, Selected Years, 1978-2005 Year Space Heating Air Conditioning Water Heating Appliances, 2 Electronics, and Lighting Natural Gas Elec- tricity 3 Fuel Oil 4 LPG 5 Total Electricity 3 Natural Gas Elec- tricity 3 Fuel Oil 4 LPG 5 Total Natural Gas Elec- tricity 3 LPG 5 Total Consumption (quadrillion Btu) 1978 4.26 0.40 2.05 0.23 6.94 0.31 1.04 0.29 0.14 0.06 1.53 0.28 1.46 0.03 1.77 1980 3.41 .27 1.30 .23 5.21 .36 1.15 .30 .22

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    U.S. Energy Information Administration (EIA) (indexed site)

    Household End Uses: Fuel Types, Appliances, and Electronics Share of Households With Selected Appliances, 1980 and 2009 Space Heating by Main Fuel, 2009 Share of Households With Selected Electronics, 1997 and 2009 Air-Conditioning Equipment, 1980 and 2009 54 U.S. Energy Information Administration / Annual Energy Review 2011 1 Natural gas and electric. 2 Liquefied petroleum gases. 3 Includes kerosene. 4 Coal, solar, other fuel, or no heating equipment. 5 Video Cassette Recorder. 6 Digital Video

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 2.6 Household End Uses: Fuel Types, Appliances, and Electronics, Selected Years, 1978-2009 Appliance Year Change 1978 1979 1980 1981 1982 1984 1987 1990 1993 1997 2001 2005 2009 1980 to 2009 Total Households (millions) .......... 77 78 82 83 84 86 91 94 97 101 107 111 114 32 Percent of Households Space Heating - Main Fuel 1 Natural Gas .................................... 55 55 55 56 57 55 55 55 53 52 55 52 50 -5 Electricity 2 ...................................... 16 17 18 17 16 17 20

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 2.9 Commercial Buildings Consumption by Energy Source, Selected Years, 1979-2003 (Trillion Btu) Energy Source and Year Square Footage Category Principal Building Activity Census Region 1 All Buildings 1,001 to 10,000 10,001 to 100,000 Over 100,000 Education Food Sales Food Service Health Care Lodging Mercantile and Service Office All Other Northeast Midwest South West Major Sources 2 1979 ................ 1,255 2,202 1,508 511 3 ( ) 336 469 278 894 861 1,616 1,217 1,826 1,395 526 4,965

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 2.10 Commercial Buildings Energy Consumption and Expenditure Indicators, Selected Years, 1979-2003 Energy Source and Year Building Characteristics Energy Consumption Energy Expenditures Number of Buildings Total Square Feet Square Feet per Building Total Per Building Per Square Foot Per Employee Total Per Building Per Square Foot Per Million Btu Thousands Millions Thousands Trillion Btu Million Btu Thousand Btu Million Btu Million Dollars 1 Thousand Dollars 1 Dollars 1 Dollars 1 Major

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Commercial Buildings Electricity Consumption by End Use, 2003 By End Use By Principal Building Activity 64 U.S. Energy Information Administration / Annual Energy Review 2011 1,340 481 436 381 167 156 88 69 24 418 Lighting Cooling Ventilation Refrigeration Space Computers Water Office Cooking Other¹ 0 500 1,000 1,500 Trillion Btu Heating Heating Equipment and Storage Assembly 733 719 371 248 244 235 217 208 167 149 267 Mercantile Office Education Health Care Warehouse Lodging Food Service Food

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 2.11 Commercial Buildings Electricity Consumption by End Use, 2003 (Trillion Btu) End Use Space Heating Cooling Ventilation Water Heating Lighting Cooking Refrigeration Office Equipment Computers Other 1 Total All Buildings .................................... 167 481 436 88 1,340 24 381 69 156 418 3,559 Principal Building Activity Education ...................................... 15 74 83 11 113 2 16 4 32 21 371 Food Sales ................................... 6 12 7 Q 46 2 119 2 2 10 208

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    U.S. Energy Information Administration (EIA) (indexed site)

    Consumer Expenditure Estimates for Energy by Source Total Energy, 1970-2010 By Energy Type, 2010 Expenditures³ by Energy Type, Indexed, 1970-2010 By Petroleum Product, 2010 76 U.S. Energy Information Administration / Annual Energy Review 2011 1 Prices are not adjusted for inflation. See "Nominal Dollars" in Glossary. 2 Wood and wood-derived fuels, and biomass waste; excludes fuel ethanol and biodiesel. 3 Based on nominal dollars. 4 Liquefied petroleum gases. 5 Asphalt and road oil,

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    U.S. Energy Information Administration (EIA) (indexed site)

    Consumer Expenditure Estimates for Energy by End-Use Sector, 2010 By Sector Residential Sector by Major Source² Commercial Sector by Major Source³ Industrial Sector by Major Source 4 78 U.S. Energy Information Administration / Annual Energy Review 2011 561 250 216 178 Transportation Residential Industrial Commercial 0 100 200 300 400 500 600 Billion Dollars¹ 167 54 27 Retail Electricity Natural Gas Petroleum 0 50 100 150 200 Billion Dollars¹ 106 63 37 7 3 Petroleum Retail Electricity

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    U.S. Energy Information Administration (EIA) (indexed site)

    9 Table 3.6 Consumer Expenditure Estimates for Energy by End-Use Sector, 1970-2010 (Million Dollars 1 ) Year Residential Commercial Industrial Transportation Natural Gas 2 Petroleum Retail Electricity 3 Total 4 Natural Gas 2 Petroleum 5 Retail Electricity 3 Total 6,7 Coal Natural Gas 2 Petroleum 5 Biomass 8 Retail Electricity 3 Total 7,9 Petroleum 5 Total 7,10 1970 5,272 4,186 10,352 20,112 1,844 1,440 7,319 10,678 2,082 2,625 6,069 366 5,624 16,691 35,327 35,379 1971 5,702 4,367 11,589 21,934

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    U.S. Energy Information Administration (EIA) (indexed site)

    Value of Fossil Fuel Imports Total, 1949-2011 By Fuel, 1949-2011 By Fuel, 2011 80 U.S. Energy Information Administration / Annual Energy Review 2011 1 In chained (2005) dollars, calculated by using gross domestic product implicit price defla- tors in Table D1. See "Chained Dollars" in Glossary. 2 See "Nominal Dollars" in Glossary. 3 Natural gas, coal, and coal coke. Source: Table 3.7. Crude Oil 1950 1960 1970 1980 1990 2000 2010 0 100 200 300 400 500 Billion Real (2005)

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 3.7 Value of Fossil Fuel Imports, Selected Years, 1949-2011 (Billion Dollars) Year Coal Coal Coke Natural Gas Crude Oil 1 Petroleum Products 2 Total Nominal 3 Real 4 Nominal 3 Real 4 Nominal 3 Real 4 Nominal 3 Real 4 Nominal 3 Real 4 Nominal 3 Real 4 1949 (s) 0.02 (s) 0.03 0.00 0.00 0.30 2.10 0.14 0.95 0.45 3.09 1950 (s) .02 .01 .04 .00 .00 .37 2.52 .21 R 1.46 .59 4.04 1955 (s) .02 (s) .01 (s) .01 .65 R 3.94 .44 2.66 1.10 6.64 1960 (s) .01 (s) .01 .03 .15 .90 4.81 .73 3.93 1.66 R 8.91

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    U.S. Energy Information Administration (EIA) (indexed site)

    Value of Fossil Fuel Exports Total, 1949-2011 By Fuel, 1949-2011 By Fuel, 2011 82 U.S. Energy Information Administration / Annual Energy Review 2011 104 16 7 2 Petroleum Coal Natural Gas Crude Oil 0 20 40 60 80 100 120 Billion Nominal Dollars² 1 In chained (2005) dollars, calculated by using gross domestic product implicit price defla- tors in Table D1. See "Chained Dollars" in Glossary. 2 See "Nominal Dollars" in Glossary. 3 Natural gas, crude oil, and coal coke. Source:

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 3.8 Value of Fossil Fuel Exports, Selected Years, 1949-2011 (Billion Dollars) Year Coal Coal Coke Natural Gas Crude Oil Petroleum Products 1 Total Nominal 2 Real 3 Nominal 2 Real 3 Nominal 2 Real 3 Nominal 2 Real 3 Nominal 2 Real 3 Nominal 2 Real 3 1949 0.30 2.05 0.01 0.06 (s) 0.01 0.10 0.68 0.46 R 3.18 0.87 R 5.98 1950 .27 1.84 .01 .04 (s) .02 .10 .70 .39 2.69 .78 R 5.29 1955 .48 2.92 .01 .05 .01 .04 .04 .23 .60 3.61 1.14 R 6.85 1960 .35 1.90 .01 .04 (s) .02 .01 .04 .47 2.51 .84 4.51

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    U.S. Energy Information Administration (EIA) (indexed site)

    9 Value of Fossil Fuel Net Imports, 1949-2011 Value of Fossil Fuel Net Imports Value of Fossil Fuel Net Imports by Fuel 84 U.S. Energy Information Administration / Annual Energy Review 2011 1 In chained (2005) dollars, calculated by using gross domestic product implicit price deflators in Table D1. See "Chained Dollars" in Glossary. 2 Includes small amounts of coal coke. Note: Negative net imports indicate that the value of exports is greater than the value of imports. Source: Table

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 3.9 Value of Fossil Fuel Net Imports, Selected Years, 1949-2011 (Billion Dollars) Year Coal Coal Coke Natural Gas Crude Oil Petroleum Products 1 Total Nominal 2 Real 3 Nominal 2 Real 3 Nominal 2 Real 3 Nominal 2 Real 3 Nominal 2 Real 3 Nominal 2 Real 3 1949 -0.29 R -2.03 (s) -0.03 (s) -0.01 0.21 1.42 -0.32 -2.24 -0.42 -2.89 1950 -.27 -1.82 (s) -.01 (s) -.02 .27 1.82 -.18 -1.23 -.18 -1.26 1955 -.48 R -2.90 -.01 -.04 -.01 -.03 .62 3.71 -.16 -.95 -.04 -.22 1960 -.35 -1.89 -.01 -.03 .02 .13

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    U.S. Energy Information Administration (EIA) (indexed site)

    Fossil Fuel Production Prices Prices, 1949-2011 Fossil Fuel Composite Price,² Change From Previous Year, 1950-2011 68 U.S. Energy Information Administration / Annual Energy Review 2011 Fossil Fuel Composite Natural Gas Coal 1 In chained (2005) dollars, calculated by using gross domestic product implicit price deflators in Table D1. See "Chained Dollars" in Glossary. 2 Based on real prices in chained (2005) dollars. See "Chained Dollars" in Glossary. Source: Table 3.1. 1950

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    U.S. Energy Information Administration (EIA) (indexed site)

    69 Table 3.1 Fossil Fuel Production Prices, Selected Years, 1949-2011 (Dollars per Million Btu) Year Coal 1 Natural Gas 2 Crude Oil 3 Fossil Fuel Composite 4 Nominal 5 Real 6 Nominal 5 Real 6 Nominal 5 Real 6 Nominal 5 Real 6 Percent Change 7 1949 0.21 1.45 0.05 0.37 0.44 3.02 0.26 1.81 - - 1950 .21 1.41 .06 .43 .43 R 2.95 .26 1.74 -3.6 1955 .19 1.12 .09 .54 .48 2.88 .27 R 1.63 -3.6 1960 .19 1.04 .13 .68 .50 2.67 .28 1.52 -2.3 1965 .18 .92 .15 .73 .49 R 2.47 .28 1.39 -1.5 1970 .27 1.09 .15 .63

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    U.S. Energy Information Administration (EIA) (indexed site)

    Value of Fossil Fuel Production, Imports, and Exports Overview, 1949-2011 Production by Fuel, 1949-2011 Overview, 2011 70 U.S. Energy Information Administration / Annual Energy Review 2011 Production 1 In chained (2005) dollars, calculated by using gross domestic product implicit price defla- tors in Table D1. See "Chained Dollars" in Glossary. 2 See "Nominal Dollars" in Glossary. Sources: Tables 3.2, 3.7, and 3.8. 1950 1960 1970 1980 1990 2000 2010 0 25 50 75 100 125 150 175

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 3.2 Value of Fossil Fuel Production, Selected Years, 1949-2011 (Billion Dollars) Year Coal 1 Natural Gas 2 Crude Oil 3,4 Total Nominal 5 Real 6 Nominal 5 Real 6 Nominal 5 Real 6 Nominal 5 Real 6 1949 2.52 R 17.37 0.33 2.24 4.68 R 32.27 7.52 R 51.88 1950 2.91 R 19.84 .44 3.00 4.95 R 33.80 8.30 R 56.64 1955 2.30 R 13.87 .94 5.67 6.88 R 41.45 10.12 R 60.99 1960 2.10 R 11.27 1.79 9.61 7.42 R 39.84 11.30 R 60.72 1965 2.40 R 12.03 2.57 R 12.87 8.15 R 40.86 13.11 R 65.76 1970 3.88 R 15.96 3.73

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    U.S. Energy Information Administration (EIA) (indexed site)

    Consumer Price Estimates for Energy by Source Total Energy, 1970-2010 By Energy Type, 2010 Prices³ by Energy Type, Indexed, 1970-2010 By Petroleum Product, 2010 72 U.S. Energy Information Administration / Annual Energy Review 2011 Fuel Oil Gasoline 1 Prices are not adjusted for inflation. See "Nominal Dollars" in Glossary. 2 Wood and wood-derived fuels, and biomass waste; excludes fuel ethanol and biodiesel. Prior to 2001, also includes non-biomass waste. 3 Based on nominal dollars.

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    U.S. Energy Information Administration (EIA) (indexed site)

    Consumer Price Estimates for Energy by End-Use Sector, 2010 By Sector Residential Sector by Major Source Commercial Sector by Major Source Industrial Sector by Major Source 74 U.S. Energy Information Administration / Annual Energy Review 2011 22.40 21.00 20.90 12.04 Residential Transportation Commercial Industrial 0 5 10 15 20 25 Dollars¹ per Million Btu 33.81 23.46 11.13 Retail Petroleum Natural 0 10 20 30 40 Dollars¹ per Million Btu Gas Electricity 19.89 17.58 6.25 3.96 2.74 Retail Petroleum

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 3.4 Consumer Price Estimates for Energy by End-Use Sector, 1970-2010 (Dollars 1 per Million Btu) Year Residential Commercial Industrial Transportation Natural Gas 2 Petroleum Retail Electricity 3 Total 4 Natural Gas 2 Petroleum 5 Retail Electricity 3 Total 6,7 Coal Natural Gas 2 Petroleum 5 Biomass 8 Retail Electricity 3 Total 7,9 Petroleum 5 Total 7,10 1970 1.06 1.54 6.51 2.10 0.75 R 0.90 6.09 1.97 0.45 0.38 0.98 1.59 2.99 0.84 2.31 2.31 1971 1.12 1.59 6.80 2.24 .80 1.02 6.44 2.15 .50

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Crude Oil and Natural Gas Exploratory and Development Wells Total Wells Drilled, 1949-2010 Total Wells Drilled by Type, 1949-2010 Successful Wells, 1949-2010 Wells Drilled, 2010 Footage Drilled, 2010 Average Depth, 2010 96 U.S. Energy Information Administration / Annual Energy Review 2011 1 Data are for exploratory and development wells combined. Sources: Tables 4.5-4.7. Total¹ 1950 1960 1970 1980 1990 2000 2010 0 25 50 75 100 Thousand Wells 1950 1960 1970 1980 1990 2000 2010 0 10 20 30 40 50

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    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 4.5 Crude Oil and Natural Gas Exploratory and Development Wells, Selected Years, 1949-2010 Year Wells Drilled Successful Wells Footage Drilled 1 Average Footage Drilled Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Number Percent Thousand Feet Feet per Well 1949 21,352 3,363 12,597 37,312 66.2 79,428 12,437 43,754 135,619 3,720 3,698 3,473 3,635 1950 23,812 3,439 14,799 42,050 64.8 92,695 13,685 50,977

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    U.S. Energy Information Administration (EIA) (indexed site)

    6 Crude Oil and Natural Gas Exploratory Wells, 1949-2010 Exploratory Wells Drilled by Well Type Exploratory Footage Drilled by Well Type Exploratory Wells Average Depth, All Wells Exploratory Wells Average Depth by Well Type 98 U.S. Energy Information Administration / Annual Energy Review 2011 Note: These graphs depict exploratory wells only; see Figure 4.5 for all wells and Figure 4.7 for development wells only. Source: Table 4.6. Dry Holes 1950 1960 1970 1980 1990 2000 2010 0 3 6 9 12 15

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    U.S. Energy Information Administration (EIA) (indexed site)

    9 Table 4.6 Crude Oil and Natural Gas Exploratory Wells, Selected Years, 1949-2010 Year Wells Drilled Successful Wells Footage Drilled 1 Average Footage Drilled Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Number Percent Thousand Feet Feet per Well 1949 1,406 424 7,228 9,058 20.2 5,950 2,409 26,439 34,798 4,232 5,682 3,658 3,842 1950 1,583 431 8,292 10,306 19.5 6,862 2,356 30,957 40,175 4,335 5,466 3,733 3,898

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    U.S. Energy Information Administration (EIA) (indexed site)

    7 Crude Oil and Natural Gas Development Wells, 1949-2010 Development Wells Drilled by Well Type Development Footage Drilled by Well Type Development Wells Average Depth, All Wells Development Wells Average Depth by Well Type 100 U.S. Energy Information Administration / Annual Energy Review 2011 Note: These graphs depict development wells only; see Figure 4.5 for all wells and Figure 4.6 for exploratory wells only. Source: Table 4.7. 1950 1960 1970 1980 1990 2000 2010 0 10 20 30 40 50 Thousand

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 4.7 Crude Oil and Natural Gas Development Wells, Selected Years, 1949-2010 Year Wells Drilled Successful Wells Footage Drilled 1 Average Footage Drilled Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Crude Oil 2 Natural Gas 3 Dry Holes 4 Total Number Percent Thousand Feet Feet per Well 1949 19,946 2,939 5,369 28,254 81.0 73,478 10,028 17,315 100,821 3,684 3,412 3,225 3,568 1950 22,229 3,008 6,507 31,744 79.5 85,833 11,329 20,020 117,183 3,861

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    U.S. Energy Information Administration (EIA) (indexed site)

    8 Coal Demonstrated Reserve Base, January 1, 2011 By Key State By Region West and East of the Mississippi By Mining Method By Rank 102 U.S. Energy Information Administration / Annual Energy Review 2011 Source: Table 4.8. 119 104 61 32 29 27 23 16 12 12 9 Montana Illinois Wyo- West Ken- Penn- Ohio Colo- Texas New Indiana 0 20 40 60 80 100 120 140 Billion Short Tons 230 156 98 Western Interior Appalachian 0 50 100 150 200 250 300 350 Billion Short Tons ming Virginia tucky sylvania rado Mexico 257

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Table 4.8 Coal Demonstrated Reserve Base, January 1, 2011 (Billion Short Tons) Region and State Anthracite Bituminous Coal Subbituminous Coal Lignite Total Underground Surface Underground Surface Underground Surface Surface 1 Underground Surface Total Appalachian .............................................. 4.0 3.3 68.2 21.9 0.0 0.0 1.1 72.1 26.3 98.4 Alabama ................................................... .0 .0 .9 2.1 .0 .0 1.1 .9 3.1 4.0 Kentucky, Eastern

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    U.S. Energy Information Administration (EIA) (indexed site)

    9 Uranium Exploration and Development Drilling Total Holes Drilled, 1958-2011¹ Holes Drilled, Selected Years Total Footage Drilled, 1949-2011¹ Footage Drilled, Selected Years 104 U.S. Energy Information Administration / Annual Energy Review 2011 1 In 2002 and 2003, data are withheld to avoid disclosure. Source: Table 4.9. 19 10 9 2 1 5 8 28 18 2 0 5 1961 1971 1981 1991 2001 2011 0 10 20 30 Thousands Exploration Development 1950 1960 1970 1980 1990 2000 2010 0 20 40 60 80 100 120 Thousands 3 4

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    U.S. Energy Information Administration (EIA) (indexed site)

    5 Table 4.9 Uranium Exploration and Development Drilling, Selected Years, 1949-2011 Year Exploration 1 Development 2 Total Holes Drilled Footage Drilled Holes Drilled Footage Drilled Holes Drilled Footage Drilled Thousands Million Feet Thousands Million Feet Thousands Million Feet 1949 NA 0.36 NA 0.05 NA 0.41 1950 NA .57 NA .21 NA .78 1955 NA 5.27 NA .76 NA 6.03 1960 7.34 1.40 24.40 4.21 31.73 5.61 1965 6.23 1.16 7.33 .95 13.56 2.11 1970 43.98 17.98 14.87 5.55 58.85 23.53 1975 34.29 15.69 21.60

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    U.S. Energy Information Administration (EIA) (indexed site)

    Technically Recoverable Crude Oil and Natural Gas Resource Estimates, 2009 Crude Oil and Lease Condensate, Total Technically Dry Natural Gas, Total Technically Recoverable Resources Recoverable Resources Crude Oil and Lease Condensate by Type Dry Natural Gas by Type 88 U.S. Energy Information Administration / Annual Energy Review 2011 58% 25% 18% 48 States¹ Onshore 48 States¹ Offshore Alaska 20% 13% 13% 54% 48 States¹ Onshore 48 States¹ Offshore Gas Alaska Tight Gas, Shale Gas, and Coalbed

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    U.S. Energy Information Administration (EIA) (indexed site)

    7 Table 4.10 Uranium Reserves, 1 2008 (Million Pounds Uranium Oxide) State Forward-Cost 2 Category (dollars 3 per pound) $50 or Less $100 or Less Total .................................................................................................................................... 539 1,227 Wyoming ......................................................................................................................... 220 446 New Mexico

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Concentrating Solar Resources 108 U.S. Energy Information Administration / Annual Energy Review 2011 Notes: * Annual average direct normal solar resource data are shown. * kWh/m 2 /Day = kilowatthours per square meter per day. Web Page: For related information, see http://www.nrel.gov/gis/maps.html. Sources: This map was created by the National Renewable Energy Laboratory for the Department of Energy (October 20, 2008). The data for Hawaii and the 48 contiguous States are a 10-kilometer (km)

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    U.S. Energy Information Administration (EIA) (indexed site)

    2 Photovoltaic Solar Resources U.S. Energy Information Administration / Annual Energy Review 2011 109 Notes: * Annual average solar resource data are shown for a tilt=latitude collector. * kWh/m 2 /Day = kilowatthours per square meter per day. Web Page: For related information, see http://www.nrel.gov/gis/maps.html. Sources: This map was created by the National Renewable Energy Laboratory for the Depart- ment of Energy (October 20, 2008). The data for Hawaii and the 48 contiguous States are a

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Onshore Wind Resources 110 U.S. Energy Information Administration / Annual Energy Review 2011 Notes: * Data are annual average wind speed at 80 meters. * m/s = meters per second. Web Page: For related information, see http://www.nrel.gov/gis/maps.html. Sources: This map was created by the National Renewable Energy Laboratory for the Department of Energy (April 1, 2011). Wind resource estimates developed by AWS Truepower, LLC for windNavigator®. See http://www.windnavigator.com and

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    U.S. Energy Information Administration (EIA) (indexed site)

    4 Offshore Wind Resources U.S. Energy Information Administration / Annual Energy Review 2011 111 Notes: * Data are annual average wind speed at 90 meters. * m/s = meters per second. * mph = miles per hour. Web Page: For related information, see http://www.nrel.gov/gis/maps.html. Source: This map was created by the National Renewable Energy Laboratory for the Department of Energy (January 10, 2011

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    U.S. Energy Information Administration (EIA) (indexed site)

    89 Table 4.1 Technically Recoverable Crude Oil and Natural Gas Resource Estimates, 2009 Region Proved Reserves 1 Unproved Resources Total Technically Recoverable Resources 2 Crude Oil and Lease Condensate (billion barrels) 48 States 3 Onshore ........................................................................... 14.2 112.6 126.7 48 States 3 Offshore ........................................................................... 4.6 50.3 54.8 Alaska

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    U.S. Energy Information Administration (EIA) (indexed site)

    2 Crude Oil and Natural Gas Cumulative Production and Proved Reserves, 1977-2010 Crude Oil Natural Gas (Dry) Cumulative Production and Proved Reserves, Indexed 90 U.S. Energy Information Administration / Annual Energy Review 2011 Notes: * Data are at end of year. * Crude oil includes lease condensate. Source: Table 4.2. Natural Gas (Dry) Cumulative Production Crude Oil Cumulative Production Natural Gas (Dry) Proved Reserves Crude Oil Proved Reserves 1977 1980 1983 1986 1989 1992 1995 1998 2001

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    U.S. Energy Information Administration (EIA) (indexed site)

    1 Table 4.2 Crude Oil and Natural Gas Cumulative Production and Proved Reserves, 1977-2010 Year Crude Oil and Lease Condensate 1 Natural Gas (Dry) Cumulative Production Proved Reserves 2 Cumulative Production Proved Reserves 3 Billion Barrels Trillion Cubic Feet 1977 118.1 31.8 514.4 207.4 1978 121.3 31.4 533.6 208.0 1979 124.4 31.2 553.2 201.0 1980 127.5 31.3 572.6 199.0 1981 130.7 31.0 591.8 201.7 1982 133.8 29.5 609.6 201.5 1983 137.0 29.3 625.7 200.2 1984 140.2 30.0 643.2 197.5 1985 143.5

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    U.S. Energy Information Administration (EIA) (indexed site)

    3 Crude Oil, Natural Gas, and Natural Gas Liquids Proved Reserves Total, 1949-2010 By Type, 2010 By Type, 1949-2010 92 U.S. Energy Information Administration / Annual Energy Review 2011 1 COE=crude oil equivalent. ² To the extent that lease condensate is measured or estimated it is included in "Natural Gas Liquids"; otherwise, lease condensate is included in "Crude Oil." Notes: * Data are at end of year. * API=American Petroleum Institute. AGA=American Gas Association.