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Note: This page contains sample records for the topic "lignite coke coke" from the National Library of EnergyBeta (NLEBeta).
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We encourage you to perform a real-time search of NLEBeta
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1

Investigation of bonding mechanism of coking on semi-coke from lignite with pitch and tar  

SciTech Connect (OSTI)

In coking, the bonding ability of inert macerals by reactive macerals is dependent on various parameters and also is related to the wettability of the inert macerals. In this study, the effect of carbonization temperature on the wettability of semi-cokes produced at various temperatures has been investigated. Soma and Yatagan semicokes represent inert macerals, and pitch was used as a reactive structure in the experiments. The briquetted pitch blocks were located on the semi-cokes and heated from the softening temperature of pitch (60{sup o}C) to 140{sup o}C to observe the wettability. In addition, liquid tar was also used to determine the wettability of semi-cokes. From the standpoint of wettability, the temperature of 900{sup o}C was determined to be the critical point for coke produced from sub-bituminous coals. 15 refs., 6 figs., 2 tabs.

Vedat Arslan [Dokuz Eylul University, Izmir (Turkey). Engineering Faculty

2006-10-15T23:59:59.000Z

2

Blast furnace coke quality in relation to petroleum coke addition  

SciTech Connect (OSTI)

The incorporation of petroleum coke as an additive in industrial coking coal blends is a practice often used by steel companies. A suitable blast furnace coke produced by replacing part of the coking coal blend with a suitable petroleum coke (addition of 5 to 15%), was made by Great Lakes Carbon Corporation and successfully tested at several blast furnaces. This coke had lower reactivity, less ash and slightly higher sulfur content than coke made without the addition of petroleum coke. In contrast with these results, it has been reported in a BCRA study that additions of petroleum coke to a strong coking coal, above 5 wt%, increased coke reactivity. These differences may be explained on the basis of the coal or blend characteristics to which petroleum coke is added. Petroleum coke addition seems to give better results if the coal/blend has high fluidity. The present situation in Spain is favorable for the use of petroleum coke. So, a study of laboratory and semi-industrial scale was made to assess the possibility of using petroleum coke as an additive to the typical industrial coal blend coked by the Spanish Steel Company, ENSIDESA. The influence of the petroleum coke particle size was also studied to semi-industrial scale.

Alvarez, R.; Diez, M.A.; Menendez, J.A.; Barriocanal, C.; Pis, J.J. [CSIC, Oviedo (Spain). Inst. Nacional del Carbon; Sirgado, M. [ENSIDESA, Aviles (Spain)

1995-12-01T23:59:59.000Z

3

Western Canadian coking coals -- Thermal rheology and coking quality  

SciTech Connect (OSTI)

Methods of predicting coke strength developed from the thermal rheological properties of Carboniferous coals frequently indicate that Cretaceous coals would not make high quality coke -- yet both types of coals produce coke suitable for the iron blast furnace. This paper will discuss the reasons why Western Canadian coals exhibit lower rheological values and how to predict the strength of coke produced from them.

Leeder, W.R. [Teck Corp. (Canada); Price, J.T.; Gransden, J.F. [CANMET Energy Technology Centre, Ottawa, Ontario (Canada)

1997-12-31T23:59:59.000Z

4

Met coke world summit 2005  

SciTech Connect (OSTI)

Papers are presented under the following session headings: industry overview and market outlook; coke in the Americas; the global coke industry; and new developments. All the papers (except one) only consist of a copy of the overheads/viewgraphs.

NONE

2005-07-01T23:59:59.000Z

5

Coking and gasification process  

DOE Patents [OSTI]

An improved coking process for normally solid carbonaceous materials wherein the yield of liquid product from the coker is increased by adding ammonia or an ammonia precursor to the coker. The invention is particularly useful in a process wherein coal liquefaction bottoms are coked to produce both a liquid and a gaseous product. Broadly, ammonia or an ammonia precursor is added to the coker ranging from about 1 to about 60 weight percent based on normally solid carbonaceous material and is preferably added in an amount from about 2 to about 15 weight percent.

Billimoria, Rustom M. (Houston, TX); Tao, Frank F. (Baytown, TX)

1986-01-01T23:59:59.000Z

6

High coking value pitch  

SciTech Connect (OSTI)

A high coking value pitch prepared from coal tar distillate and has a low softening point and a high carbon value while containing substantially no quinoline insolubles is disclosed. The pitch can be used as an impregnant or binder for producing carbon and graphite articles.

Miller, Douglas J.; Chang, Ching-Feng; Lewis, Irwin C.; Lewis, Richard T.

2014-06-10T23:59:59.000Z

7

Design and construction of coke battery 1A at Radlin coke plant, Poland  

SciTech Connect (OSTI)

In the design and construction of coke battery 1A at Radlin coke plant (Poland), coking of rammed coke with a stationary system was employed for the first time. The coke batteries are grouped in blocks. Safety railings are provided on the coke and machine sides of the maintenance areas.

A.M. Kravchenko; D.P. Yarmoshik; V.B. Kamenyuka; G.E. Kos'kova; N.I. Shkol'naya; V.V. Derevich; A.S. Grankin [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

8

COKEMASTER: Coke plant management system  

SciTech Connect (OSTI)

To keep coke utilization in ironmaking as competitive as possible, the potential to improve the economics of coke production has to be utilized. As one measure to meet this need of its customers, Krupp Koppers has expanded its existing ECOTROL computer system for battery heating control to a comprehensive Coke Plant Management System. Increased capacity utilization, lower energy consumption, stabilization of plant operation and ease of operation are the main targets.

Johanning, J.; Reinke, M. [Krupp Koppers GmbH, Essen (Germany)

1996-12-31T23:59:59.000Z

9

Coke from coal and petroleum  

DOE Patents [OSTI]

A carbonaceous coke is manufactured by the delayed coking of a slurry mixture of from about 10 to about 30 weight percent of caking or non-caking coal and the remainder a petroleum resid blended at below 50.degree. C.

Wynne, Jr., Francis E. (Allison Park, PA); Lopez, Jaime (Pittsburgh, PA); Zaborowsky, Edward J. (Harwick, PA)

1981-01-01T23:59:59.000Z

10

Converting Petroleum Coke to Electricity  

E-Print Network [OSTI]

contributes 80% of this total. As crude oil coke is a cement kiln, where the alkaline quality deteriorates, and the market for residual components in cement will absorb the sulfur oil. becomes less profitable due to increasingly released by the coke during.... The higher value has been amply demonstrated by the Combustion Power Units, and by commercial gasification systems producing syngas for chemicals We do not anticipate a major system availability debit for adding an industrial-scale, base loaded...

Pavone, A.

11

New coke-sorting system at OAO Koks  

SciTech Connect (OSTI)

A new coke-sorting system has been introduced at OAO Koks. It differs from the existing system in that it has no bunkers for all-purpose coke but only bunkers for commercial coke. In using this system with coke from battery 4, the crushing of the coke on conveyer belts, at roller screens, and in the commercial-coke bunkers is studied. After installing braking elements in the coke path, their effectiveness in reducing coke disintegration and improving coke screening is investigated. The granulometric composition and strength of the commercial coke from coke battery 3, with the new coke-sorting system, is evaluated.

B.Kh. Bulaevskii; V.S. Shved; Yu.V. Kalimin; S.D. Filippov [OAO Koks, Kemerovo (Russian Federation)

2009-05-15T23:59:59.000Z

12

Trends in the automation of coke production  

SciTech Connect (OSTI)

Up-to-date mathematical methods, such as correlation analysis and expert systems, are employed in creating a model of the coking process. Automatic coking-control systems developed by Giprokoks rule out human error. At an existing coke battery, after introducing automatic control, the heating-gas consumption is reduced by {>=}5%.

R.I. Rudyka; Y.E. Zingerman; K.G. Lavrov [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

13

Clean Production of Coke from Carbonaceous Fines  

SciTech Connect (OSTI)

In order to produce steel (a necessary commodity in developed nations) using conventional technologies, you must have metallurgical coke. Current coke-making technology pyrolyzes high-quality coking coals in a slot oven, but prime coking coals are becoming more expensive and slot ovens are being shut-down because of age and environmental problems. The United States typically imports about 4 million tons of coke per year, but because of a world-wide coke scarcity, metallurgical coke costs have risen from about $77 per tonne to more than $225. This coke shortage is a long-term challenge driving up the price of steel and is forcing steel makers to search for alternatives. Combustion Resources (CR) has developed a technology to produce metallurgical coke from alternative feedstocks in an environmentally clean manner. The purpose of the current project was to refine material and process requirements in order to achieve improved economic benefits and to expand upon prior work on the proposed technology through successful prototype testing of coke products. The ultimate objective of this project is commercialization of the proposed technology. During this project period, CR developed coke from over thirty different formulations that meet the strength and reactivity requirements for use as metallurgical coke. The technology has been termed CR Clean Coke because it utilizes waste materials as feedstocks and is produced in a continuous process where pollutant emissions can be significantly reduced compared to current practice. The proposed feed material and operating costs for a CR Clean Coke plant are significantly less than conventional coke plants. Even the capital costs for the proposed coke plant are about half that of current plants. The remaining barrier for CR Clean Coke to overcome prior to commercialization is full-scale testing in a blast furnace. These tests will require a significant quantity of product (tens of thousands of tons) necessitating the construction of a demonstration facility. Talks are currently underway with potential partners and investors to build a demonstration facility that will generate enough coke for meaningful blast furnace evaluation tests. If the testing is successful, CR Clean Coke could potentially eliminate the need for the United States to import any coke, effectively decreasing US Steel industry dependence on foreign nations and reducing the price of domestic steel.

Craig N. Eatough

2004-11-16T23:59:59.000Z

14

Mathematical modeling of clearance between wall of coke oven and coke cake  

SciTech Connect (OSTI)

A mathematical model was developed for estimating the clearance between the wall of the coke oven and the coke cake. The prediction model is based on the balance between the contractile force and the coking pressure. A clearance forms when the contractile force exceeds the coking pressure in this model. The contractile force is calculated in consideration of the visco-elastic behavior of the thermal shrinkage of the coke. The coking pressure is calculated considering the generation and dispersion of gas in the melting layer. The relaxation time off coke used in this model was obtained with a dilatometer under the load application. The clearance was measured by the laser sensor, and the internal gas pressure was measured in a test oven. The clearance calculated during the coking process were in good agreement with the experimental results, which supported the validity of the mathematical model.

Nushiro, K.; Matsui, T.; Hanaoka, K.; Igawa, K.; Sorimachi, K.

1995-12-01T23:59:59.000Z

15

Coke cake behavior under compressive forces  

SciTech Connect (OSTI)

The deformation of the coke cake and load on the side wall during pushing were studied using an electric furnace equipped with a movable wall. Coke cake was found to deform in three stages under compressive forces. The coke cake was shortened in the pushing direction in the cake deformation stage, and load was generated on the side walls in the high wall load stage. Secondary cracks in the coke cake were found to prevent load transmission on the wall. The maximum load transmission rate was controlled by adjusting the maximum fluidity and mean reflectance of the blended coal.

Watakabe, S.; Takeda, T.; Itaya, H.; Suginobe, H.

1997-12-31T23:59:59.000Z

16

Collector main replacement at Indianapolis Coke  

SciTech Connect (OSTI)

Indianapolis Coke is a merchant coke producer, supplying both foundry and blast furnace coke to the industry. The facility has three coke batteries: two 3 meter batteries, one Wilputte four divided and one Koppers Becker. Both batteries are underjet batteries and are producing 100% foundry coke at a net coking time of 30.6 hours. This paper deals with the No. 1 coke battery, which is a 72 oven, gun fired, 5 meter Still battery. No. 1 battery produces both foundry and blast furnace coke at a net coking rate of 25.4 hours. No. 1 battery was commissioned in 1979. The battery is equipped with a double collector main. Although many renovations have been completed to the battery, oven machinery and heating system, to date no major construction projects have taken place. Deterioration of the collector main was caused in part from elevated levels of chlorides in the flushing liquor, and temperature fluctuations within the collector main. The repair procedures are discussed.

Sickle, R.R. Van

1997-12-31T23:59:59.000Z

17

Factors affecting coking pressures in tall coke ovens  

SciTech Connect (OSTI)

The detrimental effects of excessive coking pressures, resulting in the permanent deformation of coke oven walls, have been recognized for many years. Considerable research has been undertaken worldwide in attempts to define the limits within which a plant may safely operate and to quantify the factors which influence these pressures. Few full scale techniques are available for assessing the potential of a coal blend for causing wall damage. Inference of dangerous swelling pressures may be made however by the measurement of the peak gas pressure which is generated as the plastic layers meet and coalesce at the center of the oven. This pressure is referred to in this report as the carbonizing pressure. At the Dawes Lane cokemaking plant of British Steel`s Scunthorpe Works, a large database has been compiled over several years from the regulator measurement of this pressure. This data has been statistically analyzed to provide a mathematical model for predicting the carbonizing pressure from the properties of the component coals, the results of this analysis are presented in this report.

Grimley, J.J.; Radley, C.E. [British Steel plc, Scunthorpe (United Kingdom). Scunthorpe Works

1995-12-01T23:59:59.000Z

18

New designs in the reconstruction of coke-sorting systems  

SciTech Connect (OSTI)

In recent Giprokoks designs for the reconstruction of coke-sorting systems, high-productivity vibrational-inertial screens have been employed. This permits single-stage screening and reduction in capital and especially operating expenditures, without loss of coke quality. In two-stage screening, >80 mm coke (for foundry needs) is additionally separated, with significant improvement in quality of the metallurgical coke (25-80 mm). New designs for the reconstruction of coke-sorting systems employ mechanical treatment of the coke outside the furnace, which offers new scope for stabilization of coke quality and permits considerable improvement in mechanical strength and granulometric composition of the coke by mechanical crushing.

A.S. Larin; V.V. Demenko; V.L. Voitanik [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

19

Simulation of industrial coking -- Phase 1  

SciTech Connect (OSTI)

Two statistically designed experimental programs using an Appalachian and a Western Canadian coal blend were run in CANMET`s 460mm (18 inch) movable wall oven. Factors included coal grind, moisture, oil addition, carbonization rate and final coke temperature. Coke quality parameters including CSR, coal charge characteristics and pressure generation were analyzed.

Todoschuk, T.W.; Price, J.T.; Gransden, J.F.

1997-12-31T23:59:59.000Z

20

Coke oven gas injection to blast furnaces  

SciTech Connect (OSTI)

U.S. Steel has three major facilities remaining in Pennsylvania`s Mon Valley near Pittsburgh. The Clairton Coke Works operates 12 batteries which produce 4.7 million tons of coke annually. The Edgar Thomson Works in Braddock is a 2.7 million ton per year steel plant. Irvin Works in Dravosburg has a hot strip mill and a range of finishing facilities. The coke works produces 120 mmscfd of coke oven gas in excess of the battery heating requirements. This surplus gas is used primarily in steel re-heating furnaces and for boiler fuel to produce steam for plant use. In conjunction with blast furnace gas, it is also used for power generation of up to 90 MW. However, matching the consumption with the production of gas has proved to be difficult. Consequently, surplus gas has been flared at rates of up to 50 mmscfd, totaling 400 mmscf in several months. By 1993, several changes in key conditions provided the impetus to install equipment to inject coke oven gas into the blast furnaces. This paper describes the planning and implementation of a project to replace natural gas in the furnaces with coke oven gas. It involved replacement of 7 miles of pipeline between the coking plants and the blast furnaces, equipment capable of compressing coke oven gas from 10 to 50 psig, and installation of electrical and control systems to deliver gas as demanded.

Maddalena, F.L.; Terza, R.R.; Sobek, T.F.; Myklebust, K.L. [U.S. Steel, Clairton, PA (United States)

1995-12-01T23:59:59.000Z

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


21

Heat treatment of exchangers to remove coke  

SciTech Connect (OSTI)

This patent describes a process for preparing furfural coke for removal from metallic surfaces. It comprises: heating the furfural coke without causing an evolution of heat capable of undesirably altering metallurgical properties of the surfaces in the presence of a gas containing molecular oxygen at a sufficient temperature below 800{degrees}F (427{degrees}C) for a sufficient time to change the crush strength of the coke so as to permit removal with a water jet at a pressure of five thousand pounds per square inch.

Turner, J.D.

1990-02-20T23:59:59.000Z

22

Delayed coking of decant oil and coal in a laboratory-scale coking unit  

SciTech Connect (OSTI)

In this paper, we describe the development of a laboratory-scale delayed coker and present results of an investigation on the recovered liquid from the coking of decant oil and decant oil/coal mixtures. Using quantitative gas chromatography/mass spectroscopy (GC/MS) and {sup 1}H and {sup 13}C NMR, a study was made of the chemical composition of the distillate liquids isolated from the overheads collected during the coking and co-coking process. {sup 1}H and {sup 13}C NMR analyses of combined liquids from coking and co-coking did not show any substantial differences. These NMR results of coking and co-coking liquids agree with those of GC/MS. In these studies, it was observed that co-coking with coal resulted in a decrease in the paraffins contents of the liquid. The percentage of cycloparaffins, indenes, naphthalenes, and tetralins did not change significantly. In contrast, alkyl benzenes and polycyclic aromatic hydrocarbons in the distillate were higher in the co-coking experiments which may have resulted from the distillation of thermally cracked coal macromolecules and the contribution of these molecules to the overall liquid composition. 40 refs., 3 figs., 13 tabs.

Oemer Guel; Leslie R. Rudnick; Harold H. Schobert [Pennsylvania State University Park, PA (United States). Energy Institute, C205 Coal Utilization Laboratory

2006-08-15T23:59:59.000Z

23

New and revised standards for coke production  

SciTech Connect (OSTI)

The need for new and revised standards for coke production in Ukraine and Russia is outlined. Such standards should address improvements in plant operation, working conditions, environmental protection, energy conservation, fire and explosion safety, and economic indices.

G.A. Kotsyuba; M.I. Alpatov; Y.G. Shapoval [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

24

Mozambique becomes a major coking coal exporter?  

SciTech Connect (OSTI)

In addition to its potential role as a major international supplier of coking coal, Mozambique will also become a major source of power generation for southern Africa. 3 figs.

Ruffini, A.

2008-06-15T23:59:59.000Z

25

The waste water free coke plant  

SciTech Connect (OSTI)

Apart from coke which is the actual valuable material a coke oven plant also produces a substantial volume of waste water. These effluent water streams are burdened with organic components (e.g. phenols) and inorganic salts (e.g. NH{sub 4}Cl); due to the concentration of the constituents contained therein these effluent waters must be subjected to a specific treatment before they can be introduced into public waters. For some years a lot of separation tasks have been solved successfully by applying the membrane technology. It was especially the growing number of membrane facilities for cleaning of landfill leakage water whose composition can in fact be compared with that of coking plant waste waters (organic constituents, high salt fright, ammonium compounds) which gave Thyssen Still Otto Anlagentechnik the idea for developing a process for coke plant effluent treatment which contains the membrane technology as an essential component.

Schuepphaus, K.; Brink, N. [Thyssen Still Otto Anlagentechnik GmbH, Bochum (Germany)

1995-12-01T23:59:59.000Z

26

Possibilities of coke manufacture in nonpollutant conditions  

SciTech Connect (OSTI)

The paper presents some possibilities to obtain coke briquettes from anthracite, using as binders petroleum pitch, wheat flour, cement, plaster, ashes from power-plants dried from the electrofilters. Specific thermal post-treatment were proposed for each case, such as: oxidation or heating at low temperatures (under 300 C). As a result the authors obtained coke briquettes to be used in small equipment, with no pollutant pyrogenetic treatment.

Barca, F.; Panaitescu, C.; Vidrighin, C.; Peleanu, I. [Politehnica Univ. Bucharest (Romania); Albastroiu, P. [S.C. ICEM S.A., Bucharest (Romania)

1994-12-31T23:59:59.000Z

27

Physical, chemical and thermal changes of coals and coal maceral concentrates during coke formation.  

E-Print Network [OSTI]

??Research Doctorate - Doctor of Philosophy (PhD) The measured coke reactivity index (CRI) and coke strength after reaction (CSR) determined in experiments based on coke… (more)

Xie, Wei

2013-01-01T23:59:59.000Z

28

Giprokoks proposals for improvement in air quality at coke battery 1A of Radlin coke plant  

SciTech Connect (OSTI)

Coke battery 1A, which uses rammed batch, has gone into production at Radlin coke plant (Poland), on the basis of Giprokoks designs. Up-to-date dust-trapping methods are used for the first time within the aspiration systems in the coal-preparation shop and in improving dust collection within the production buildings.

T.F. Trembach; A.G. Klimenko [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

29

Unmanned operation of the coke guides at Hoogovens IJmuiden Coke Plant 1  

SciTech Connect (OSTI)

Due to the bad condition of batteries and many ovens under repair, Hoogovens was forced to partially repair and rebuild the Coke plant No. 1. The production of coke at Coke plant No. 1 is realized in 3 production blocks subdivided in 6 batteries. Besides a renovated installation, all coke oven machines were renewed. A total of five identical machine sets are available. Each consists of a pusher machine, larry car, coke guide and quench car with diesel locomotive. A complete automated control system was implemented. The main objectives were a highly regular coking and pushing process, automated traveling and positioning and a centrally coordinated interlocking of machine functions. On each operational machine however an operator performed the supervisory control of the automated machine functions. After years of good experience with the automated system, economical reasons urged further personnel reduction from 1994 on. Totally 375 people were involved, including the maintenance department. To reduce the occupation at coke plant No. 1, the coke guide was the first machine to be fully automated because of the isolated and uncomfortable working place.

Vos, D.; Mannes, N.; Poppema, B. [Hoogovens IJmuiden B.V. (Netherlands)

1995-12-01T23:59:59.000Z

30

Fundamentals of Delayed Coking Joint Industry Project  

SciTech Connect (OSTI)

The coking test facilities include three reactors (or cokers) and ten utilities. Experiments were conducted using the micro-coker, pilot-coker, and stirred-batch coker. Gas products were analyzed using an on-line gas chromatograph. Liquid properties were analyzed in-house using simulated distillation (HP 5880a), high temperature gas chromatography (6890a), detailed hydrocarbon analysis, and ASTM fractionation. Coke analyses as well as feedstock analyses and some additional liquid analyses (including elemental analyses) were done off-site.

Volk Jr., Michael; Wisecarver, Keith D.; Sheppard, Charles M.

2003-02-07T23:59:59.000Z

31

Water protection in coke-plant design  

SciTech Connect (OSTI)

Wastewater generation, water consumption, and water management at coke plants are considered. Measures to create runoff-free water-supply and sewer systems are discussed. Filters for water purification, corrosion inhibitors, and biocides are described. An integrated single-phase technology for the removal of phenols, thiocyanides, and ammoniacal nitrogen is outlined.

G.I. Alekseev [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

32

Fundamentals of Delayed Coking Joint Industry Project  

SciTech Connect (OSTI)

Delayed coking evolved steadily over the early to mid 1900s to enable refiners to convert high boiling, residual petroleum fractions to light products such as gasoline. Pound for pound, coking is the most energy intensive of any operation in a modern refinery. Large amounts of energy are required to heat the thick, poor-quality petroleum residuum to the 900 to 950 degrees F required to crack the heavy hydrocarbon molecules into lighter, more valuable products. One common misconception of delayed coking is that the product coke is a disadvantage. Although coke is a low valued (near zero economic value) byproduct, compared to transportation fuels, there is a significant worldwide trade and demand for coke as it is an economical fuel. Coke production has increased steadily over the last ten years, with further increases forecast for the foreseeable future. Current domestic production is near 111,000 tons per day. A major driving force behind this increase is the steady decline in crude quality available to refiners. Crude slates are expected to grow heavier with higher sulfur contents while environmental restrictions are expected to significantly reduce the demand for high-sulfur residual fuel oil. Light sweet crudes will continue to be available and in even greater demand than they are today. Refiners will be faced with the choice of purchasing light sweet crudes at a premium price, or adding bottom of the barrel upgrading capability, through additional new investments, to reduce the production of high-sulfur residual fuel oil and increase the production of low-sulfur distillate fuels. A second disadvantage is that liquid products from cokers frequently are unstable, i.e., they rapidly form gum and sediments. Because of intermediate investment and operating costs, delayed coking has increased in popularity among refiners worldwide. Based on the 2000 Worldwide Refining Survey published in the Oil and Gas, the delayed coking capacity for 101 refineries around the world is 2,937,439 barrels/calendar day. These cokers produce 154,607 tons of coke per day and delayed coking accounts for 88% of the world capacity. The delayed coking charge capacity in the United States is 1,787,860 b/cd. Despite its wide commercial use, only relatively few contractors and refiners are truly knowledgeable in delayed-coking design, so that this process carries with it a ''black art'' connotation. Until recently, the expected yield from cokers was determined by a simple laboratory test on the feedstock. As a result of Tulsa University's prior related research, a process model was developed that with additional work could be used to optimize existing delayed cokers over a wide range of potential feedstocks and operating conditions. The objectives of this research program are to: utilize the current micro, batch and pilot unit facilities at The University of Tulsa to enhance the understanding of the coking process; conduct additional micro and pilot unit tests with new and in-house resids and recycles to make current optimization models more robust; conduct focused kinetic experiments to enhance the furnace tube model and to enhance liquid production while minimizing sulfur in the products; conduct detailed foaming studies to optimize the process and minimize process upsets; quantify the parameters that affect coke morphology; and to utilize the knowledge gained from the experimental and modeling studies to enhance the computer programs developed in the previous JIP for optimization of the coking process. These refined computer models will then be tested against refinery data provided by the member companies. Novel concepts will also be explored for hydrogen sulfide removal of furnace gases as well as gas injection studies to reduce over-cracking. The following deliverables are scheduled from the two projects of the three-year JIP: (1) A novel method for enhancing liquid yields from delayed cokers and data that provide insight as to the optimum temperature to remove hydrogen sulfide from furnace gases. (2) An understanding of what causes foaming in c

Michael Volk Jr; Keith Wisecarver

2005-10-01T23:59:59.000Z

33

Reducing dust emissions at OAO Alchevskkoks coke battery 10A  

SciTech Connect (OSTI)

Coke battery 10A with rammed batch is under construction at OAO Alchevskkoks. The design documentation developed by Giprokoks includes measures for reducing dust emissions to the atmosphere. Aspiration systems with dry dust trapping are employed in the new components of coke battery 10A and in the existing coke-sorting equipment. Two-stage purification of dusty air in cyclones and bag filters is employed for the coke-sorting equipment. This system considerably reduces coke-dust emissions to the atmosphere.

T.F. Trembach; E.N. Lanina [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

34

RESIDUA UPGRADING EFFICIENCY IMPROVEMENT MODELS: COKE FORMATION PREDICTABILITY MAPS  

SciTech Connect (OSTI)

The dispersed particle solution model of petroleum residua structure was used to develop predictors for pyrolytic coke formation. Coking Indexes were developed in prior years that measure how near a pyrolysis system is to coke formation during the coke formation induction period. These have been demonstrated to be universally applicable for residua regardless of the source of the material. Coking onset is coincidental with the destruction of the ordered structure and the formation of a multiphase system. The amount of coke initially formed appears to be a function of the free solvent volume of the original residua. In the current work, three-dimensional coke make predictability maps were developed at 400 C, 450 C, and 500 C (752 F, 842 F, and 932 F). These relate residence time and free solvent volume to the amount of coke formed at a particular pyrolysis temperature. Activation energies for two apparent types of zero-order coke formation reactions were estimated. The results provide a new tool for ranking residua, gauging proximity to coke formation, and predicting initial coke make tendencies.

John F. Schabron; A. Troy Pauli; Joseph F. Rovani Jr.

2002-05-01T23:59:59.000Z

35

REDUCING POWER PRODUCTION COSTS BY UTILIZING PETROLEUM COKE  

SciTech Connect (OSTI)

A Powder River Basin subbituminous coal from the North Antelope mine and a petroleum shot coke were received from Northern States Power Company (NSP) for testing the effects of parent fuel properties on coal-coke blend grindability and evaluating the utility of petroleum coke blending as a strategy for improving electrostatic precipitator (ESP) particulate collection efficiency. Petroleum cokes are generally harder than coals, as indicated by Hardgrove grindability tests. Therefore, the weaker coal component may concentrate in the finer size fractions during the pulverizing of coal-coke blends. The possibility of a coal-coke size fractionation effect is being investigated because it may adversely affect combustion performance. Although the blending of petroleum coke with coal may adversely affect combustion performance, it may enhance ESP particulate collection efficiency. Petroleum cokes contain much higher concentrations of V relative to coals. Consequently, coke blending can significantly increase the V content of fly ash resulting from coal-coke combustion. Pentavalent vanadium oxide (V{sub 2}O{sub 5}) is a known catalyst for transforming gaseous sulfur dioxide (SO{sub 2}[g]) to gaseous sulfur trioxide (SO{sub 3}[g]). The presence of SO{sub 3}(g) strongly affects fly ash resistivity and, thus, ESP performance.

NONE

1998-09-01T23:59:59.000Z

36

Model based control of a coke battery  

SciTech Connect (OSTI)

This paper describes a model-based strategy for coke battery control at BHP Steel`s operations in Pt Kembla, Australia. The strategy uses several models describing the battery thermal and coking behavior. A prototype controller has been installed on the Pt Kembla No. 6 Battery (PK6CO). In trials, the new controller has been well accepted by operators and has resulted in a clear improvement in battery thermal stability, with a halving of the standard deviation of average battery temperature. Along with other improvements to that battery`s operations, this implementation has contributed to a 10% decrease in specific battery energy consumption. A number of enhancements to the low level control systems on that battery are currently being undertaken in order to realize further benefits.

Stone, P.M.; Srour, J.M.; Zulli, P. [BHP Research, Mulgrave (Australia). Melbourne Labs.; Cunningham, R.; Hockings, K. [BHP Steel, Pt Kembla, New South Wales (Australia). Coal and Coke Technical Development Group

1997-12-31T23:59:59.000Z

37

Cyanide treatment options in coke plants  

SciTech Connect (OSTI)

The paper discusses the formation of cyanides in coke oven gas and describes and compares waste processing options. These include desulfurization by aqueous ammonia solution, desulfurization using potash solution, desulfurization in oxide boxes, decomposition of NH{sub 3} and HCN for gas scrubbing. Waste water treatment methods include chemical oxidation, precipitation, ion exchange, reverse osmosis, and biological treatment. It is concluded that biological treatment is the most economical process, safe in operation and requires a minimum of manpower.

Minak, H.P.; Lepke, P. [Krupp Uhde GmbH, Dortmund (Germany)

1997-12-31T23:59:59.000Z

38

Coking properties of perhydrous low-rank vitrains. Influence of pyrolysis conditions  

E-Print Network [OSTI]

generally lead to increased coking potential of coals characterised in the resulting cokes by large sizes equivalent to natural coking coals, since the cokes from these residues are always made of smaller MOD than those obtained for coking coals. For comparison, a similar characterisation, carried out

Paris-Sud XI, Université de

39

Table 23. Coal Receipts at Coke Plants by Census Division  

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

Division (thousand short tons) U.S. Energy Information Administration | Quarterly Coal Report, April - June 2014 Table 23. Coal Receipts at Coke Plants by Census Division...

40

Reducing power production costs by utilizing petroleum coke. Annual report  

SciTech Connect (OSTI)

A Powder River Basin subbituminous coal from the North Antelope mine and a petroleum shot coke were received from Northern States Power Company (NSP) for testing the effects of parent fuel properties on coal-coke blend grindability and evaluating the utility of petroleum coke blending as a strategy for improving electrostatic precipitator (ESP) particulate collection efficiency. Petroleum cokes are generally harder than coals, as indicated by Hardgrove grindability tests. Therefore, the weaker coal component may concentrate in the finer size fractions during the pulverizing of coal-coke blends. The possibility of a coal-coke size fractionation effect is being investigated because it may adversely affect combustion performance, it may enhance ESP particulate collection efficiency. Petroleum cokes contain much higher concentrations of V relative to coals. Consequently, coke blending can significantly increase the V content of fly ash resulting from coal-coke combustion. Pentavalent vanadium oxide (V{sub 2}O{sub 5}) is a known catalyst for transforming gaseous sulfur dioxide (SO{sub 2}[g]) to gaseous sulfur trioxide (SO{sub 3}[g]). The presence of SO{sub 3}(g) strongly affects fly ash resistivity and, thus, ESP performance.

Galbreath, K.C.

1998-07-01T23:59:59.000Z

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


41

The methods of steam coals usage for coke production  

SciTech Connect (OSTI)

Nowadays, high volatile bituminous coals are broadly used for metallurgical coke production in Russia. The share of such coals in the coking blend is variable from 20 to 40% by weight. There are some large coal deposits in Kuznetskii basin which have coals with low caking tendency. The low caking properties of such coals limit of its application in the coking process. At the same time the usage of low caking coals for coke production would allow flexibility of the feedstock for coke production. Preliminary tests, carried out in COAL-C's lab has shown some differences in coal properties with dependence on the size distribution. That is why the separation of the well-caking fraction from petrographically heterogeneous coals and its further usage in coking process may be promising. Another way for low caking coals application in the coke industry is briquettes production from such coals. This method has been known for a very long time. It may be divided into two possible directions. First is a direct coking of briquettes from the low caking coals. Another way is by adding briquettes to coal blends in defined proportion and combined coking. The possibility of application of coal beneficiation methods mentioned above was investigated in present work.

Korobetskii, I.A.; Ismagilov, M.S.; Nazimov, S.A.; Sladkova, I.L.; Shudrikov, E.S.

1998-07-01T23:59:59.000Z

42

DELAYED COKING OF SOLVENT EXTRACTED COAL FOR PRODUCTION OF ANODE GRADE COKE: CHARACTERIZATION OF SOLID AND LIQUID PRODUCTS.  

E-Print Network [OSTI]

??This study investigates the feasibility of using high temperature solvent extraction of coal to produce feedstock for the production of anode grade coke through delayed… (more)

Karri, Vamsi

2011-01-01T23:59:59.000Z

43

Development of an Advanced Combined Heat and Power (CHP) System Utilizing Off-Gas from Coke Calcination  

Broader source: Energy.gov [DOE]

Coke calcination is a process that involves the heating of green petroleum coke in order to remove volatile material and purify the coke for further processing. Calcined coke is vital to the...

44

Dry purification of aspirational air in coke-sorting systems with wet slaking of coke  

SciTech Connect (OSTI)

Coke transportation after wet slaking is accompanied by the release of dust in the production building and in the surrounding atmosphere. Wet methods are traditionally used to purify very humid air. Giprokoks has developed designs for highly efficient dry dust-removal methods in such conditions.

T.F. Trembach; A.G. Klimenko [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

45

Coke Gasification - A Solution to Excess Coke Capacity and High Energy Costs  

E-Print Network [OSTI]

effectively to produce medium-Btu (300 Btu/scf) gas which, in turn, can fuel the refinery furnaces to replace natural gas. Coke gasification should prove economical with natural gas price decontrol and the average price projected to rise to over $14.0 per...

1982-01-01T23:59:59.000Z

46

VACASULF operation at Citizens Gas and Coke Utility  

SciTech Connect (OSTI)

Citizens Gas and Coke Utility is a Public Charitable Trust which operates as the Department of Utilities of the City of Indianapolis, Indiana. Indianapolis Coke, the trade name for the Manufacturing Division of the Utility, operates a by-products coke plant in Indianapolis, Indiana. The facility produces both foundry and blast furnace coke. Surplus Coke Oven gas, generated by the process, is mixed with Natural Gas for sale to industrial and residential customers. In anticipation of regulatory developments, beginning in 1990, Indianapolis Coke undertook the task to develop an alternate Coke Oven Gas desulfurization technology for its facility. The new system was intended to perform primary desulfurization of the gas, dramatically extending the oxide bed life, thus reducing disposal liabilities. Citizens Gas chose the VACASULF technology for its primary desulfurization system. VACASULF requires a single purchased material, Potassium Hydroxide (KOH). The KOH reacts with Carbon Dioxide in the coke Oven Gas to form Potassium Carbonate (potash) which in turn absorbs the Hydrogen Sulfide. The rich solution releases the absorbed sulfide under strong vacuum in the desorber column. Operating costs are reduced through utilization of an inherent heat source which is transferred indirectly via attendant reboilers. The Hydrogen Sulfide is transported by the vacuum pumps to the Claus Kiln and Reactor for combustion, reaction, and elemental Sulfur recovery. Regenerated potash solution is returned to the Scrubber.

Currey, J.H. [Citizens Gas and Coke Utility, Indianapolis, IN (United States)

1995-12-01T23:59:59.000Z

47

Coke formation during pyrolysis of 1,2-dichloroethane  

SciTech Connect (OSTI)

Most processes involving hydrocarbons or carbon oxides at high temperatures suffer from the disadvantage of coke formation. The formation of coke deposits during pyrolysis of hydrocarbons or chlorinated hydrocarbons is of significant practical importance. Examples of such processes are the steam cracking of alkanes to produce olefins and the thermal decomposition of 1,2-dichloroethane (EDC) for the production of vinyl chloride monomer (VCM). Even id the rate of coke production is low, the cumulative nature of the solid product will result in reactor fouling. The present work deals with the thermal decomposition of EDC. Coke formation has been studied on metal surfaces in a quartz tubular reactor. The rate of coke deposition was measures on metal foils hanging from one arm of a microbalance. A complete analysis of the product gas was accomplished using on-line gas chromatography. The results show that coke deposition during thermal decomposition of EDC depends on the composition of the feed as well as on the nature of the surface of the metal foil. Small amounts of other components (contamination with other chlorinated hydrocarbons as an example) may have a large influence on the rate of coke formation. The results are discussed in terms of surface composition/morphology of the metal foil and the free radical mechanism for thermal decomposition of FDC.

Holmen, A. [Norwegian Institute of Technology, Trondheim (Norway); Lindvag, O.A. [SINTEF Applied Chemistry, Trondheim (Norway)

1995-12-31T23:59:59.000Z

48

Method for removal of furfural coke from metal surfaces  

SciTech Connect (OSTI)

This patent describes a process for preparing furfural coke for removal from metallic surfaces. It comprises: heating ship furfural coke without causing an evolution of heat capable of undesirably altering metallurgical properties of the surfaces in the presence of a gas with a total pressure of less than 100 psig containing molecular oxygen. The gas being at a sufficient temperature below 800{degrees}F. (427{degrees}C.) for a sufficient time to change the crush strength of the coke so as to permit removal with a water jet at a pressure of about 5000 psi.

Turner, J.D.

1990-02-27T23:59:59.000Z

49

RESIDUA UPGRADING EFFICIENCY IMPROVEMENT MODELS: WRI COKING INDEXES  

SciTech Connect (OSTI)

Pyrolysis experiments were conducted with three residua at 400 C (752 F) at various residence times. The wt % coke and gaseous products were measured for the product oils. The Western Research Institute (WRI) Coking Indexes were determined for the product oils. Measurements were made using techniques that might correlate with the Coking Indexes. These included spin-echo proton nuclear magnetic resonance spectroscopy, heat capacity measurements at 280 C (536 F), and ultrasonic attenuation. The two immiscible liquid phases that form once coke formation begins were isolated and characterized for a Boscan residuum pyrolyzed at 400 C (752 F) for 55 minutes. These materials were analyzed for elemental composition (CHNS), porphyrins, and metals (Ni,V) content.

John F. Schabron; Joseph F. Rovani, Jr.; Francis P. Miknis; Thomas F. Turner

2003-06-01T23:59:59.000Z

50

New process to avoid emissions: Constant pressure in coke ovens  

SciTech Connect (OSTI)

A chamber pressure regulation (PROven), especially effective in regard to emission control problems of coke ovens is introduced for the first time. Because of the partial vacuum in the collecting main system, it is possible to keep the oven`s raw gas pressure constant on a low level over the full coking time. The individual pressure control for each chamber is assured directly as a function of the oven pressure by an immersion system controlling the flow resistance of the collecting main valve. The latter is a fixed-position design (system name ``FixCup``). By doing away with the interdependence of collecting main pressure and chamber pressure, a parameter seen as a coking constant could not be made variable. This opens a new way to reduce coke oven emissions and simultaneously to prevent the ovens from damage caused by air ingress into the oven.

Giertz, J.; Huhn, F. [DMT-Gesellschaft fuer Forschung und Pruefung mbH, Essen (Germany). Inst. for Cokemaking and Fuel Technology; Hofherr, K. [Thyssen Stahl AG, Duisburg (Germany)

1995-12-01T23:59:59.000Z

51

Priorities in the design of chemical shops at coke plants  

SciTech Connect (OSTI)

Recent trends in the design of chemical equipment at coke plants are described, through the lens of experience at Giprokoks. The main priorities were to improve the removal of impurities from coke oven gas; to improve equipment design on the basis of new materials; to reduce reagent consumption; to reduce the materials and energy consumed in the construction of new equipment; and to minimize impacts on the environment and worker health. Some technological equipment is briefly characterized.

V.I. Rudyka; Y.E. Zingerman; V.V. Grabko; L.A. Kazak [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

52

Prediction of metallurgical coke strength from the petrographic composition of coal blends  

SciTech Connect (OSTI)

Turkey, especially Zonguldak on the West Coast of Black Sea region, has large reserves of bituminous coal that can be used either directly or in blends with other coals for metallurgical coke production. It is possible to predict the coking properties of these coals by petrographic analysis. In this study, semi- and non-coking coals were blended with coking bituminous coals in varying proportions and an estimation was made as to their stability factors through petrographic techniques. It was established that semi- and non-coking bituminous coals could be used in the production of metallurgical coke.

Sutcu, H.; Toroglu, I.; Piskin, S. [Zonguldak Karaelmas University, Zonguldak (Turkey)

2009-07-01T23:59:59.000Z

53

A coke oven model including thermal decomposition kinetics of tar  

SciTech Connect (OSTI)

A new one-dimensional coke oven model has been developed for simulating the amount and the characteristics of by-products such as tar and gas as well as coke. This model consists of both heat transfer and chemical kinetics including thermal decomposition of coal and tar. The chemical kinetics constants are obtained by estimation based on the results of experiments conducted to investigate the thermal decomposition of both coal and tar. The calculation results using the new model are in good agreement with experimental ones.

Munekane, Fuminori; Yamaguchi, Yukio [Mitsubishi Chemical Corp., Yokohama (Japan); Tanioka, Seiichi [Mitsubishi Chemical Corp., Sakaide (Japan)

1997-12-31T23:59:59.000Z

54

New packing in absorption systems for trapping benzene from coke-oven gas  

SciTech Connect (OSTI)

The efficiency of benzene removal from coke-oven gas in absorption units OAO Alchevskkoks with new packing is assessed.

V.V. Grabko; V.M. Li; T.A. Shevchenko; M.A. Solov'ev [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

55

Process for converting coal into liquid fuel and metallurgical coke  

DOE Patents [OSTI]

A method of recovering coal liquids and producing metallurgical coke utilizes low ash, low sulfur coal as a parent for a coal char formed by pyrolysis with a volatile content of less than 8%. The char is briquetted and heated in an inert gas over a prescribed heat history to yield a high strength briquette with less than 2% volatile content.

Wolfe, Richard A. (Abingdon, VA); Im, Chang J. (Abingdon, VA); Wright, Robert E. (Bristol, TN)

1994-01-01T23:59:59.000Z

56

Coke profile and effect on methane/ethylene conversion process  

E-Print Network [OSTI]

The objective of this study was to investigate the coke profile with respect to time on stream and the change of product distribution due to catalyst deactivation. A fixed bed reactor was used to conduct this investigation. A series of runs were...

Al-Solami, Bandar

2002-01-01T23:59:59.000Z

57

Coke battery with 51-m{sup 3} furnace chambers and lateral supply of mixed gas  

SciTech Connect (OSTI)

The basic approaches employed in the construction of coke battery 11A at OAO Magnitogorskii Metallurgicheskii Kombinat are outlined. This battery includes 51.0-m{sup 3} furnaces and a dust-free coke-supply system designed by Giprokoks with lateral gas supply; it is heated exclusively by low-calorific mixed gas consisting of blast-furnace gas with added coke-oven gas. The 82 furnaces in the coke battery are divided into two blocks of 41. The gross coke output of the battery (6% moisture content) is 1140000 t/yr.

V.I. Rudyka; N.Y. Chebotarev; O.N. Surenskii; V.V. Derevich [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

58

An overview of crisis management in the coke industry  

SciTech Connect (OSTI)

Members of the American Coke and Coal Chemicals Institute (ACCCI), as responsible corporate citizens, have embraced the concepts of crisis management and progress down the various paths of planning and preparation, monitoring, media communications, community outreach, emergency response, and recovery. Many of the concepts outlined here reflect elements of crisis management guidelines developed by the Chemical Manufacturers Association (CMA). At a coke plant, crises can take the form of fires, chemical releases, labor strikes, feedstock supply disruptions, and excessive snowfall, just to name a few. The CMA defines a crisis as: ``an unplanned event that has the potential to significantly impact a company`s operability or credibility, or to pose a significant environment, economic or legal liability``; and crisis management as: ``those activities undertaken to anticipate or prevent, prepare for, respond to and recover from any incident that has the potential to greatly affect the way a company conducts its business.

Saunders, D.A.

1995-12-01T23:59:59.000Z

59

Integrated coke, asphalt and jet fuel production process and apparatus  

DOE Patents [OSTI]

A process and apparatus for the production of coke, asphalt and jet fuel m a feed of fossil fuels containing volatile carbon compounds therein is disclosed. The process includes the steps of pyrolyzing the feed in an entrained bed pyrolyzing means, separating the volatile pyrolysis products from the solid pyrolysis products removing at least one coke from the solid pyrolysis products, fractionating the volatile pyrolysis products to produce an overhead stream and a bottom stream which is useful as asphalt for road pavement, condensing the overhead stream to produce a condensed liquid fraction and a noncondensable, gaseous fraction, and removing water from the condensed liquid fraction to produce a jet fuel-containing product. The disclosed apparatus is useful for practicing the foregoing process. the process provides a useful method of mass producing and jet fuels from materials such as coal, oil shale and tar sands.

Shang, Jer Y. (McLean, VA)

1991-01-01T23:59:59.000Z

60

New environmental concepts in the chemical and coke industries  

SciTech Connect (OSTI)

We know that environmentally pure technologies do not exist. Coke production is no exception to the rule. The article considers the logic of environmental decision making. Attention focuses on a new bank of ecologically appropriate materials whose release to the biosphere must be considered solely in quantititative terms. Qualitativily all these materials are familiar; they are assimilated by populations of microorganisms and tar thus compatible with the biosphere.

A.Yu. Naletov; V.A. Naletov [Mendeleev Russian Chemical-Engineering University (Russian Federation)

2007-05-15T23:59:59.000Z

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


61

Development of advanced technology of coke oven gas drainage treatment  

SciTech Connect (OSTI)

In April 1994, commercial-scale application of ozone oxidation to ammonia liquor (which is primarily the water condensing from coke oven gas) to reduce its chemical oxygen demand (COD) was started at the Nagoya Works of Nippon Steel Corporation. This paper deals with the results of technical studies on the optimization of process operating conditions and the enlargement of equipment size and the operating purification system.

Higashi, Tadayuki; Yamaguchi, Akikazu; Ikai, Kyozou; Kamiyama, Hisarou; Muto, Hiroshi

1996-12-31T23:59:59.000Z

62

How to implement a quality program in a coking plant. The AHMSA experience  

SciTech Connect (OSTI)

AHMSA (Altos Hornos de Mexico) is the largest integrated Steel Plant in Mexico, with its 3.1 MMMT of Liquid Steel production program for 1995. AHMSA operates two coke plants which began operations in 1955 and 1976. Total coke monthly production capacity amounts to as much as 106,000 Metric Tons (MT). The coke plants working philosophy was discussed and established in 1986 as part of the Quality Improvement Program, where its ultimate goal is to give the best possible coke quality to its main client--the blast furnaces. With this goal in mind, a planned joint effort with their own coal mines was initiated. This paper deals with the implementation process of the Quality Program, and the results of this commitment at the coal mines, coke plants and blast furnaces. The coke quality improvement is shown since 1985 to 1994, as well as the impact on the blast furnace operation.

Reyes M, M.A.; Perez, J.L.; Garza, C. de la; Morales, M.

1995-12-01T23:59:59.000Z

63

Low-coke rate operation under high PCI at Kobe No. 3 BF  

SciTech Connect (OSTI)

Kobe No. 3 blast furnace (BF) suffered tremendous damage when the Great Hanshin-Awaji Earthquake rocked the area on January 17, 1995. However, working as quickly as possible to dig out of the burden and rehabilitate various facilities, the company managed to restart the No. 3 BF on April 2. After the restart, which went smoothly, production was shifted into the low coke rate operation which was being promoted before the disaster. In October, 1995, only seven months after the restart, the nation record of 296 kg/t low coke rate could be achieved. Subsequently, in January, 1996, coke rate reached 290 kg/t and the low coke rate operation was renewed. Since that time the same level of coke rate has been maintained. The paper discusses how low coke rate operation was achieved.

Matsuo, Tadasu; Kanazuka, Yasuo; Hoshino, Koichi; Yoshida, Yasuo; Kitayama, Syuji; Ishiwaki, Shiro [Kobe Steel Ltd. (Japan). Kobe Works

1997-12-31T23:59:59.000Z

64

The new Kaiserstuhl coking plant: The heating system -- Design, construction and initial operating experience  

SciTech Connect (OSTI)

At the end of 1992 the new coke plant Kaiserstuhl in Dortmund/Germany with presently the largest coke ovens world-wide started its production operation in close linkage to the Krupp-Hoesch Metallurgical Works after about 35 months construction time. This plant incorporating comprehensive equipment geared to improve environmental protection is also considered as the most modern coke plant of the world. The heating-system and first results of operation will be presented.

Strunk, J.

1996-12-31T23:59:59.000Z

65

Heating control methodology in coke oven battery at Rourkela Steel Plant  

SciTech Connect (OSTI)

A methodology of heating control was evolved incorporating temperature data generated through infra-red sensor at quenching station and thermocouples specially installed in the gooseneck of coke oven battery No. 3 of RSP. Average temperature of the red-hot coke as pushed helps in diagnosis of the abnormal ovens and in setting the targeted battery temperature. A concept of coke readiness factor (Q) was introduced which on optimization resulted in lowering the specific heat consumption by 30 KCal/Kg.

Bandyopadhyay, S.S.; Parthasarathy, L.; Gupta, A.; Bose, P.R.; Mishra, U.

1996-12-31T23:59:59.000Z

66

Operational improvements at Jewell Coal and Coke Company`s non-recovery ovens  

SciTech Connect (OSTI)

Operational improvements at Jewell Coal and Coke Company over the past five years includes safety and environmental concerns, product quality, equipment availability, manpower utilization, and productivity. These improvements with Jewell`s unique process has allowed Jewell Coal and Coke Company to be a consistent, high quality coke producer. The paper briefly explains Jewell`s unique ovens, their operating mode, improved process control, their maintenance management program, and their increase in productivity.

Ellis, C.E.; Pruitt, C.W.

1995-12-01T23:59:59.000Z

67

The effects of ash and maceral composition of Azdavay and Kurucasile (Turkey) coals on coking properties  

SciTech Connect (OSTI)

In this study, investigations were made as to the effect of the maceral compositions and mineral matter content of Azdavay and Kurucasile coals on the coking property. Chemical and maceral analyses and coking properties were determined for the products of the float-sink procedure. The coking properties were established on the basis of free swelling index and Ruhr dilatometer tests. Maceral analyses showed that as the ash content of a coal containing both high and medium volatile matter increases, its effective maceral proportion decreases, and the coking property is affected in an unfavorable way.

Toroglu, I. [Zonguldak Karaelmas University, Zonguldak (Turkey). Faculty of Engineering

2006-07-01T23:59:59.000Z

68

Integration of stripping of fines slurry in a coking and gasification process  

DOE Patents [OSTI]

In an integrated fluid coking and gasification process wherein a stream of fluidized solids is passed from a fluidized bed coking zone to a second fluidized bed and wherein entrained solid fines are recovered by a wet scrubbing process and wherein the resulting solids-liquid slurry is stripped to remove acidic gases, the stripped vapors of the stripping zone are sent to the gas cleanup stage of the gasification product gas. The improved stripping integration is particularly useful in the combination coal liquefaction process, fluid coking of bottoms of the coal liquefaction zone and gasification of the product coke.

DeGeorge, Charles W. (Chester, NJ)

1980-01-01T23:59:59.000Z

69

The effect of diabietic acid on the coking of oxidised solvent-extracted coal.  

E-Print Network [OSTI]

??Refcoal is a refined carbon source obtained by extraction of coal with dimethylformamide (DMF). During the coking process, Refcoal goes through a mesophase (fluid) stage… (more)

Ludere, Margaret Tshimangadzo

2008-01-01T23:59:59.000Z

70

Lignin as Both Fuel and Fusing Binder in Briquetted Anthracite Fines for Foundry Coke Substitute.  

E-Print Network [OSTI]

??Lignin that had been extracted from Kraft black liquor was investigated as a fusing binder in briquetted anthracite fines for a foundry coke substitute. Cupola… (more)

Lumadue, Matthew

2012-01-01T23:59:59.000Z

71

CHARACTERIZATION OF COAL- AND PETROLEUM-DERIVED BINDER PITCHES AND THE INTERACTION OF PITCH/COKE MIXTURES IN PRE-BAKED CARBON ANODES.  

E-Print Network [OSTI]

??Carbon anodes are manufactured from calcined petroleum coke (i.e. sponge coke) and recycled anode butts as fillers, and coal tar pitch (SCTP) as the binder.… (more)

Suriyapraphadilok, Uthaiporn

2008-01-01T23:59:59.000Z

72

Teamwork in planning and carrying out the first inspection of the coke dry quenching (CDQ) plant of the Kaiserstuhl Coking Facility  

SciTech Connect (OSTI)

The coke plant Kaiserstuhl operates a coke dry quenching (CDQ) plant with a downstream installed waste heat boiler to satisfy statutory pollution control rules and requirements. This CDQ which went on stream in March 1993 cools the whole coke production output from the Kaiserstuhl coke plant in counterflow to an inert cooling gas. This brief overview on the whole CDQ plant should elucidate the complex of problems posed when trying to make an exact plant revision plan. After all it was impossible to evaluate or to assess all the interior process technology relevant components during the planning stage as the plant was in operation. The revision data for the first interior check was determined and fixed by the statutory rule for steam boilers and pressure vessels. The relevant terms for this check are mandatorily prescribed. In liaison with the testing agency (RW TUEV) the date for the first revision was fixed for April 1995, that means two years after the first commissioning.

Burchardt, G.

1996-12-31T23:59:59.000Z

73

Influence of coal on coke properties and blast-furnace operation  

SciTech Connect (OSTI)

With unstable coal supplies and properties and a fluctuating content of coking coal in the batch at OAO Zapadno-Sibirskii Metallurgicheskii Kombinat (ZSMK) and of bituminous coal at Kuznetskaya enrichment facility, it is important to optimize the rank composition of the batch for coke production.

G.R. Gainieva; L.D. Nikitin [OAO Zapadno-Sibirskii Metallurgicheskii Kombinat (Russian Federation)

2007-07-01T23:59:59.000Z

74

Analytical input-output and supply chain study of China's coke and steel sectors  

E-Print Network [OSTI]

I design an input-output model to investigate the energy supply chain of coal-coke-steel in China. To study the demand, supply, and energy-intensity issues for coal and coke from a macroeconomic perspective, I apply the ...

Li, Yu, 1976-

2004-01-01T23:59:59.000Z

75

Ammonia removal process upgrade to the Acme Steel Coke Plant  

SciTech Connect (OSTI)

The need to upgrade the ammonia removal process at the Acme Steel Coke Plant developed with the installation of the benzene NESHAP (National Emission Standard for Hazardous Air Pollutants) equipment, specifically the replacement of the final cooler. At Acme Steel it was decided to replace the existing open cooling tower type final cooler with a closed loop direct spray tar/water final cooler. This new cooler has greatly reduced the emissions of benzene, ammonia, hydrogen sulfide and hydrogen cyanide to the atmosphere, bringing them into environmental compliance. At the time of its installation it was not fully recognized as to the effect this would have on the coke oven gas composition. In the late seventies the decision had been made at Acme Steel to stop the production of ammonia sulfate salt crystals. The direction chosen was to make a liquid ammonia sulfate solution. This product was used as a pickle liquor at first and then as a liquid fertilizer as more markets were developed. In the fall of 1986 the ammonia still was brought on line. The vapors generated from the operation of the stripping still are directed to the inlet of the ammonia absorber. At that point in time it was decided that an improvement to the cyclical ammonia removal process was needed. The improvements made were minimal yet allowed the circulation of solution through the ammonia absorber on a continuous basis. The paper describes the original batch process and the modifications made which allowed continuous removal.

Harris, J.L. [Acme Steel Co., Chicago, IL (United States). Chicago Coke Plant

1995-12-01T23:59:59.000Z

76

Modelling of a coke oven heating wall M. Landreau, D. Isler, Centre de Pyrolyse de Marienau (CPM)  

E-Print Network [OSTI]

- 1 - Modelling of a coke oven heating wall M. Landreau, D. Isler, Centre de Pyrolyse de Marienau with thermomechanical modelling of a coke oven heating wall. The objective is to define the safe limits of coke oven of walls, roof and larry car, pre-stresses (anchoring system), lateral pressure due to coal pushing A 3D

Boyer, Edmond

77

Hydrogen production from steam reforming of coke oven gas and its utility for indirect reduction of iron oxides in blast  

E-Print Network [OSTI]

of coal and coke are consumed for heating and reducing iron oxides [2,3]. As a result, BFs have becomeHydrogen production from steam reforming of coke oven gas and its utility for indirect reduction 2012 Available online 18 June 2012 Keywords: Steam reforming Hydrogen and syngas production Coke oven

Leu, Tzong-Shyng "Jeremy"

78

Characterization of liquids derived from laboratory coking of decant oil and co-coking of Pittsburgh seam bituminous coal with decant oil  

SciTech Connect (OSTI)

In this study, decant oil and a blend of Pittsburgh seam bituminous coal with decant oil were subjected to coking and co-coking in a laboratory-scale delayed coker. Higher yields of coke and gas were obtained from co-coking than from coking. Coal addition into the feedstock resulted in lighter overhead liquid. GC/MS analyses of gasoline, jet fuel, and diesel show that co-coking of coal/decant oil gave higher quantity aromatic components than that of coking of decant oil alone. Simulated distillation gas chromatography analyses of overhead liquids and GC/MS analyses of vacuum fractions show that when coal was reacted with a decant oil, the coal constituents contributed to the distillable liquids. To address the reproducibility of the liquid products, overhead liquid samples collected at the first, third, and fifth hours of experiments of 6 h duration were evaluated using simulated distillation gas chromatography and {sup 1}H and {sup 13}C NMR. NMR analyses of the liquid products showed that, even though there were slight changes in the {sup 1}H and {sup 13}C spectra, the standard deviation was low for the time-dependent samples. Simulated distillation gas chromatography showed that the yields of refinery boiling range materials (i.e., gasoline, jet fuel, diesel, and fuel oil cuts) were reproducible between runs. Fractionation of the overhead liquids into refinery boiling range materials (gasoline, jet fuel, diesel, fuel oil fractions) showed that the boiling range materials and chemical compositions of fractions were found to be reproducible. 54 refs., 17 tabs.

Omer Gul; Caroline Clifford; Leslie R. Rudnick; Harold H. Schobert [Pennsylvania State University, University Park, PA (United States)

2009-05-15T23:59:59.000Z

79

Development of automatic operation system for coke oven machines at Yawata Works of Nippon Steel Corporation  

SciTech Connect (OSTI)

The coke plant is a working environment involving heavy dust emissions, high heat and demanding physical labor. The labor-saving operation of the coke plant is an essential issue from the standpoints of not only improvement in working environment, but also reduction in fixed cost by enhancement of labor productivity. Under these circumstances, Nippon Steel has implemented the automation of coke oven machines. The first automatic operation system for coke oven machinery entered service at Oita Works in 1992, followed by the second system at the No. 5 coke oven battery of the coke plant at Yawata Works. The Yawata automatic operation system is characterized by the installation of coke oven machinery to push as many as 140 ovens per day within a short cycle time, such as a preliminary ascension pipe cap opening car and cycle time simulator by the manned operation of the pusher, which is advantageous from the standpoint of investment efficiency, and by the monitoring of other oven machines by the pusher. These measures helped to reduce the manpower requirement to 2 persons per shift from 4 persons per shift. The system entered commercial operation in March, 1994 and has been smoothly working with an average total automatic rate of 97%. Results from the startup to recent operation of the system are reported below.

Matsunaga, Masao; Uematsu, Hiroshi; Nakagawa, Yoji; Ishiharaguchi, Yuji

1995-12-01T23:59:59.000Z

80

Gas treatment and by-products recovery of Thailand`s first coke plant  

SciTech Connect (OSTI)

Coke is needed in the blast furnace as the main fuel and chemical reactant and the main product of a coke plant. The second main product of the coke plant is coke oven gas. During treatment of the coke oven gas some coal chemicals like tar, ammonia, sulphur and benzole can be recovered as by-products. Since the market prices for these by-products are rather low and often erratic it does not in most cases justify the investment to recover these products. This is the reason why modern gas treatment plants only remove those impurities from the crude gas which must be removed for technical and environmental reasons. The cleaned gas, however, is a very valuable product as it replaces natural gas in steel work furnaces and can be used by other consumers. The surplus can be combusted in the boiler of a power plant. A good example for an optimal plant layout is the new coke oven facility of Thai Special Steel Industry (TSSI) in Rayong. The paper describes the TSSI`s coke oven gas treatment plant.

Diemer, P.E.; Seyfferth, W. [Krupp Uhde GmbH, Dortmund (Germany)

1997-12-31T23:59:59.000Z

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


81

Investigation of the effects of heating rate on coking of shale during retorting  

SciTech Connect (OSTI)

The retorting of oil shale distributes organic carbon among three possible products: the liquid product, the noncondensible product, and the residual carbon (coke). The production of coke is detrimental because of the economic effects caused by the loss of organic carbon to this relatively intractable carbon form. Two reference oil shales, a Mahogany zone, Parachute Creek Member, Green River Formation oil shale from Colorado and a Clegg Creek Member, New Albany oil shale from Kentucky, were studied to evaluate the conditions that affect coke production during retorting. The variable that was studied in these experiments was the heating rate during retorting because heating rate has been indicated to have a direct effect on coke production (Burnham and Clarkson 1980). The six heating rates investigated covered the range from 1 to 650/degree/C/h (1.8 to 1169/degree/F/h). The data collected during these experiments were evaluated statistically in order to identify trends. The data for the eastern reference oil shale indicated a decrease in coke formation with increases in the heating rate. The liquid and noncondensible product yields both increased with increasing heating rate. The distribution of products in relation to retort heating rate follows the model suggested by Burnham and Clarkson (1980). Coke production during the retorting of western reference oil shale was found to be constant in relation to heating rate. The liquid product yield increased with increasing heating rate but the trend could not be verified at the 95% confidence level. The coke production observed in these experiments does not follow the prediction of the model. This may indicate that coke formation occurs early in the retorting process and may be limited by the availability of organic materials that form coke. 6 refs., 10 tabs.

Guffey, F.D.; Hunter, D.E.

1988-02-01T23:59:59.000Z

82

Demineralization of petroleum cokes and fly ash samples obtained from the upgrading of Athabasca oil sands bitumen  

SciTech Connect (OSTI)

Ash reduction of the cokes and fly ash samples derived from the Athabasca oil sands bitumen was attempted by dissolving the mineral matter in acids. The samples used for this investigation included Syncrude fluid coking coke, Suncor delayed coking coke and the two fly ash samples obtained from the combustion of these cokes. All samples were analyzed for C,H,N,O, and S before and after acid demineralization and the analyses results compared. Further, the ash from the samples before and after acid demineralization was analyzed for silica, alumina, iron titanium, nickel and vanadium to assess the acid leaching of these elements. CP/MAS, /sup 13/C NMR spectroscopic study of the demineralized coke and fly ash samples was also attempted.

Majid, A.; Ratcliffe, C.I.; Ripmeester, J.A. (National Research Council of Canada, Ottawa, ON (Canada). Div. of Chemistry)

1989-01-01T23:59:59.000Z

83

Glass-coating and cleaning system to prevent carbon deposition on coke oven walls  

SciTech Connect (OSTI)

The new technology for protecting the coking chamber bricks from damage by hard-pushing is described. The technology consists of the glass coating on the wall bricks and a wall cleaner to blow deposited carbon. For the glass coating, a specially developed glaze is sprayed onto the wall bricks by a spraying device developed to completely spray one coking chamber in a few minutes. The wall cleaner is installed on a pusher ram in the facility to automatically blow air at a sonic speed during coke pushing. The life of the glazed layer is estimated to be over two years.

Takahira, Takuya; Ando, Takeshi; Kasaoka, Shizuki; Yamauchi, Yutaka [Kawasaki Steel Corp., Mizushima, Kurashiki (Japan). Mizushima Works

1997-12-31T23:59:59.000Z

84

Producing and controlling of the pollutant in the coal`s coking process  

SciTech Connect (OSTI)

In the process of heating and coke shaping, different pollutants and polluting factors will be produced and lost to the environment due to the different coking methods. The paper analyzes the production mechanism, type, emission, average quantity, and damage to the environment of the major pollutants and polluting factors produced in several kinds of coking processes in China at the present. Then, the paper concludes that an assessment for any coking method should include a comprehensive beneficial assessment of economical benefit, environmental benefit and social benefit. The items in the evaluation should consist of infrastructure investment, which includes production equipment and pollution control equipment, production cost, benefit and profit produced by one ton coal, whether the pollution complies with the environmental requirement, extent of the damage, influence to the social development, and etc.

Li, S. [Shanxi Environmental Protection Bureau (China); Fan, Z. [Shanxi Central Environmental Monitoring Station (China)

1997-12-31T23:59:59.000Z

85

Current developments at Giprokoks for coke-battery construction and reconstruction  

SciTech Connect (OSTI)

Approaches developed at Giprokoks for coke-battery construction and reconstruction are considered. Recommendations regarding furnace construction and reconstruction are made on the basis of Ukrainian and world experience.

V.I. Rudyka; Y.E. Zingerman; V.B. Kamenyuka; O.N. Surenskii; G.E. Kos'kova; V.V. Derevich; V.A. Gushchin [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

86

The Videofil probe, a novel instrument to extend the coke oven service life  

SciTech Connect (OSTI)

To prolong the service life of coke oven batteries, the Centre de Pyrolyse de Marienau developed the Videofil probe, a novel instrument to conduct diagnoses and to help repair operations of coke ovens. The Videofil probe is a flexible non-water-cooled endoscope which is used to locate flue wall damage and estimate its importance, to define the oven zones to repair and guide the repair work and to control the quality of the repair work and its durability.

Gaillet, J.P.; Isler, D. [Centre de Pyrolyse de Marienau, Forbach (France)

1997-12-31T23:59:59.000Z

87

Cryogenic fractionator gas as stripping gas of fines slurry in a coking and gasification process  

DOE Patents [OSTI]

In an integrated coking and gasification process wherein a stream of fluidized solids is passed from a fluidized bed coking zone to a second fluidized bed and wherein entrained solid fines are recovered by a scrubbing process and wherein the resulting solids-liquid slurry is stripped with a stripping gas to remove acidic gases, at least a portion of the stripping gas comprises a gas comprising hydrogen, nitrogen and methane separated from the coker products.

DeGeorge, Charles W. (Chester, NJ)

1981-01-01T23:59:59.000Z

88

Effect of thermal treatment on coke reactivity and catalytic iron mineralogy  

SciTech Connect (OSTI)

Iron minerals in coke can catalyze its gasification and may affect coke behavior in the blast furnace. The catalytic behavior of iron depends largely upon the nature of the iron-bearing minerals. To determine the mineralogical changes that iron could undergo in the blast furnace, cokes made from three coals containing iron present in different mineral forms (clays, carbonates, and pyrite) were examined. All coke samples were heat-treated in a horizontal furnace at 1373, 1573, and 1773 K and then gasified with CO{sub 2} at 1173 K in a fixed bed reactor (FBR). Coke mineralogy was characterized using quantitative X-ray diffraction (XRD) analysis of coke mineral matter prepared by low-temperature ashing (LTA) and field emission scanning electron microscopy combined with energy dispersive X-ray analysis (FESEM/EDS). The mineralogy of the three cokes was most notably distinguished by differing proportions of iron-bearing phases. During heat treatment and subsequent gasification, iron-containing minerals transformed to a range of minerals but predominantly iron-silicides and iron oxides, the relative amounts of which varied with heat treatment temperature and gasification conditions. The relationship between initial apparent reaction rate and the amount of catalytic iron minerals - pyrrhotite, metallic iron, and iron oxides - was linear and independent of heat treatment temperature at total catalyst levels below 1 wt %. The study showed that the coke reactivity decreased with increasing temperature of heat treatment due to decreased levels of catalytic iron minerals (largely due to formation of iron silicides) as well as increased ordering of the carbon structure. The study also showed that the importance of catalytic mineral matter in determining reactivity declines as gasification proceeds. 37 refs., 13 figs., 7 tabs.

Byong-chul Kim; Sushil Gupta; David French; Richard Sakurovs; Veena Sahajwalla [University of New South Wales, Sydney, NSW (Australia). Centre for Sustainable Materials Research and Technology

2009-07-15T23:59:59.000Z

89

Coke gasification: the influence and behavior of inherent catalytic mineral matter  

SciTech Connect (OSTI)

Gasification of coke contributes to its degradation in the blast furnace. In this study, the effect of gasification on the inherent catalytic minerals in cokes and their reciprocal influence on gasification are investigated. The catalytic mineral phases identified in the cokes used in this study were metallic iron, iron sulfides, and iron oxides. Metallic iron and pyrrhotite were rapidly oxidized during gasification to iron oxide. The catalysts had a strong influence on the apparent rates at the initial stages of reaction. As gasification proceeds, their effect on the reaction rate diminishes as a result of reducing the surface contact between catalyst and carbon matrix because of carbon consumption around the catalyst particles; with extended burnout the reactivity of the coke becomes increasingly dependent on surface area. The reaction rate in the initial stages was also influenced by the particle size of the catalytic minerals; for a given catalytic iron level, the cokes whose catalytic minerals were more finely dispersed had a higher apparent reaction rate than cokes containing larger catalytic particles. Iron, sodium, and potassium in the amorphous phase did not appear to affect the reaction rate. 40 refs., 16 figs., 6 tabs.

Mihaela Grigore; Richard Sakurovs; David French; Veena Sahajwalla [Commonwealth Scientific and Industrial Research Organisation (CSIRO), Bangor, NSW (Australia)

2009-04-15T23:59:59.000Z

90

Effect of coal and coke qualities on blast furnace injection and productivity at Taranto  

SciTech Connect (OSTI)

Injection rates at Taranto blast furnaces Nos. 2 and 4, for more than 16 months, was maintained above 175 kg/thm. Monthly average injection rate for two months stabilized above 190 kg/thm. This performance was possible due to the very high combined availabilities of Taranto blast furnaces and the KST injection system. Based upon this experience the quantitative relationships between coke/coal and blast furnace operational parameters were studied and are shown graphically. During this period due to coke quality changes, injection rate had to be reduced. The effect of using coke breeze in coke/ferrous charge as well as coal blend was also evaluated. Permeability of the furnace was found to be directly affected by O{sub 2} enrichment level, while at a high PCI rate no correlation between actual change in coke quality and permeability could be established. The future of PCI technology lies in better understanding of relationships between material specifications and blast furnace parameters of which permeability is of prime importance.

Salvatore, E.; Calcagni, M. [ILVA, Taranto (Italy); Eichinger, F.; Rafi, M.

1995-12-01T23:59:59.000Z

91

Automatic coke oven heating control system at Burns Harbor for normal and repair operation  

SciTech Connect (OSTI)

An automatic heating control system for coke oven batteries was developed in 1985 for the Burns Harbor No. 1 battery and reported in the 1989 Ironmaking Conference Proceedings. The original system was designed to maintain a target coke temperature at a given production level under normal operating conditions. Since 1989, enhancements have been made to this control system so that it can also control the battery heating when the battery is under repair. The new control system has improved heating control capability because it adjusts the heat input to the battery in response to anticipated changes in the production schedule. During a recent repair of this 82 oven battery, the pushing schedule changed from 102 ovens/day to 88 ovens/day, then back to 102 ovens/day, then to 107 ovens/day. During this repair, the control system was able to maintain the coke temperature average standard deviation at 44 F, with a maximum 75 F.

Battle, E.T.; Chen, K.L. [Bethlehem Steel Corp., Burns Harbor, IN (United States); [Bethlehem Steel Corp., PA (United States)

1997-12-31T23:59:59.000Z

92

Coking phenomena in the pyrolysis of ethylene dichloride into vinyl chloride  

SciTech Connect (OSTI)

Pyrolysis of ethylene dichloride (EDC) into vinyl chloride (VCM) which is the monomer for polyvinyl chloride, one of the most popular polymers, has been established commercially for quite a time. The process around 500{degrees}C has been proved to give VCM of high purity at very high selectivity about 99% and a reasonable conversion about 50%. However, the coking is a major problem in the long run, requiring decoking treatment every two months. The present paper describes features of carbons produced in the pyrolysis process. Coke of respective features was found in the reactor, the transfer line, the heat exchanger and the rapid quencher. Typical pyrolytic carbon, anisotropic coke produced in the liquid phase, isotropic carbon was produced on the reactor wall as low as 500{degrees}C. The mechanisms for their formation are discussed.

Sotowa, Chiaki; Korai, Yozo; Mochida, Isao [Kyushu Univ., Kasuga, Fukuoka (Japan)] [and others

1995-12-31T23:59:59.000Z

93

Light oil yield improvement project at Granite City Division Coke/By-Product Plant  

SciTech Connect (OSTI)

Light oil removal from coke oven gas is a process that has long been proven and utilized throughout many North American Coke/By-Products Plants. The procedures, processes, and equipment requirements to maximize light oil recovery at the Granite City By-Products Plant will be discussed. The Light Oil Yield Improvement Project initially began in July, 1993 and was well into the final phase by February, 1994. Problem solving techniques, along with utilizing proven theoretical recovery standards were applied in this project. Process equipment improvements and implementation of Operator/Maintenance Standard Practices resulted in an average yield increase of 0.4 Gals./NTDC by the end of 1993.

Holloran, R.A. [National Steel Corp., Granite City, IL (United States). Granite City Div.

1995-12-01T23:59:59.000Z

94

Coal flow aids reduce coke plant operating costs and improve production rates  

SciTech Connect (OSTI)

Chemical coal flow aids can provide many benefits to coke plants, including improved production rates, reduced maintenance and lower cleaning costs. This article discusses the mechanisms by which coal flow aids function and analyzes several successful case histories. 2 refs., 10 figs., 1 tab.

Bedard, R.A.; Bradacs, D.J.; Kluck, R.W.; Roe, D.C.; Ventresca, B.P.

2005-06-01T23:59:59.000Z

95

Simulation of diffusion and trapping in digitized heterogeneous media David A. Coke@ and Salvatore Torquatob)  

E-Print Network [OSTI]

Simulation of diffusion and trapping in digitized heterogeneous media David A. Coke@ and Salvatore of a Brownian particle diffusing among a, digitized lattice-based domain of traps. Following the first, the inverse of the trapping rate, is obtained for a variety of configurations involving digitized spheres

Torquato, Salvatore

96

Coke oven doors: Historical methods of emission control and evaluation of current designs  

SciTech Connect (OSTI)

The containment of oven door leakage has presented challenges to coke producers for many years as the requirements of environmental regulatory agencies have become increasingly stringent. A description and evaluation of past door modifications, leakage control methodologies and luting practices on Armco Steel Company, L.P.'s Ashland No. 4 Battery is detailed to provide a background for recent work, and to expand the industry's technology base. The strict door leakage standards of the 1990 amendments to the USA Clean Air Act has prompted additional technical studies. Both a joint Armco committee's evaluation of successful systems world wide and test door installations at Ashland were incorporated to determine compliance strategy. The eventual installation of Ikio Model II coke oven doors, along with modifications to ancillary equipment, has resulted in door leakage rates approaching zero. Associated methods, problems, results and evaluations are discussed.

Pettrey, J.O.; Greene, D.E. (Armco Steel Co., Middletown, OH (United States))

1993-01-01T23:59:59.000Z

97

A mathematical model for the estimation of flue temperature in a coke oven  

SciTech Connect (OSTI)

The coke plants at the Kwangyang works has adopted an Automatic Battery Control (ABC) system which consists of four main parts, battery heating control, underfiring heat and waste gas oxygen control, pushing and charging schedule and Autotherm-S that measures heating wall temperature during pushing. The measured heating wall temperature is used for calculating Mean Battery Temperature (MBT) which is average temperature of flues for a battery, but the Autotherm-S system can not provide the flue temperatures of an oven. This work attempted to develop mathematical models for the estimation of the flue temperature using the measured heating wall temperature and to examine fitness of the mathematical model for the coke plant operation by analysis of raw gas temperature at the stand pipe. Through this work it is possible to reflect heating wall temperature in calculating MBT for battery heating control without the interruption caused by a maintenance break.

Choi, K.I.; Kim, S.Y.; Suo, J.S.; Hur, N.S.; Kang, I.S.; Lee, W.J.

1997-12-31T23:59:59.000Z

98

Linings with optimum heat-emission surfaces for cars receiving and transporting incandescent coke  

SciTech Connect (OSTI)

The least reliable components of the cars which receive and transport incandescent coke are the lining plates. This applies to both the quenching cars used for wet quenching and the hot-coke cars used in the dry cooling process. Technical advances have been described whereby the life of car linings is prolonged by increasing heat emission from the lining plate surfaces. As the heat emission level is enhanced the mean plate temperature is lowered and the lining life thereby prolonged; moreover, the between-servicings period is prolonged. This involves providing fins on the non-working (outer) plate surfaces. The problem of optimizing the size and shape of the fins with reference to heat emission remains unsolved: the requirement is maximum heat emission from plates of a given weight, or conversely minimum plate weight for a given heat emission level. 6 refs., 3 figs.

Kotlyar, B.D.; Pleshkov, P.I.; Gadyatskii, V.G. [and others

1992-12-31T23:59:59.000Z

99

Operating temperature effects on nozzle coking in a cottonseed oil fueled diesel engine  

E-Print Network [OSTI]

OPERATING TEMPERATURE EFFECTS ON NOZZLE COKING IN A COTTONSEED OIL FUELED DIESEL ENGINE A Thesis CHARLES MICHAEL YARBROUGH Submitted to the Graduate College of Texas ASM University in partial fulfillment of the requirements for the degree cf... MASTER OF SCIENCE December 1984 Major Subject: Agricultural Engineering OPERATING TEMPERATURE EFFECTS ON NOZZLE CORING IN A COTTONSEED OIL FUELED DIESEL ENGINE A Thesis by CHARLES MICHAEL YARBROUGH Approved as to style and content by: ayne A. Le...

Yarbrough, Charles Michael

1984-01-01T23:59:59.000Z

100

Health-hazard evaluation report No. HETA-88-377-2120, Armco Coke Oven, Ashland Kentucky  

SciTech Connect (OSTI)

In response to a request from the Oil, Chemical and Atomic Workers International Union, a study was made of possible hazardous working conditions at ARMCO Coke Oven (SIC-3312), Ashland, Kentucky. The facility produces about 1,000,000 tons of coke annually. Of the approximately 400 total employees at the coke oven site, 55 work in the by products area. Air quality sampling results indicated overexposure to both benzene (71432) and coal tar pitch volatiles (CTPVs). Airborne levels of benzene ranged as high as 117 parts per million (ppm) with three of 17 samples being above the OSHA limit of 1ppm. Airborne concentrations of CTPVs ranged as high as 0.38mg/cu m with two of six readings being above OSHA limit of 0.2mg/cu m. Several polynuclear aromatic hydrocarbons were also detected. The authors conclude that by products area workers are potentially overexposed to carcinogens, including benzene, CTPVs, and polynuclear aromatic hydrocarbons. An epidemiologic study is considered unlikely to yield meaningful information at this time, due to the small number of workers and the short follow up period. The authors recommend specific measures for reducing potential employee exposures, including an environmental sampling program, a preventive maintenance program, improved housekeeping procedures, and reducing exposure in operators' booths.

Kinnes, G.M.; Fleeger, A.K.; Baron, S.L.

1991-06-01T23:59:59.000Z

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


101

An example of alkalization of SiO{sub 2} in a blast furnace coke  

SciTech Connect (OSTI)

Scanning electron microscopy and an electron-microprobe analysis of a sample of blast furnace (BF) coke have revealed alkalization (5.64 wt % Na{sub 2}O + K{sub 2}O) and Al saturation (17.28 wt % Al{sub 2}O{sub 3}) of SiO{sub 2} by BF gases. The K/Na{sub at} value of 1.15 in the new phase (alteration zone) reflects close atomic proportions of the elements and suggests that the abilities to incorporate K and Na during the process are almost equal. This Al saturation and alkalization of SiO{sub 2} indicates an active role for Al along with alkali metals in BF gases. The average width of the altered area in the SiO{sub 2} grain is about 10 m, which suggests that SiO{sub 2} particles of that size can be transformed fully to the new phase, provided that at least one of their faces is open to an external pore (surface of the coke) or internal pore with circulating BF gases. The grains that exceed 10 {mu}m can only be partly altered, which means that smaller SiO{sub 2} grains can incorporate more alkali metals and Al (during their transformation to the Al and alkali-bearing phase) than a similar volume of SiO{sub 2} concentrated in larger grains. Thermodynamic calculations for 100 g{sub solid}/100 g{sub gas} and temperatures 800-1800{sup o}C have shown that the BF gases have very little or no effect on the alkalization of SiO{sub 2}. If the alteration process described in this paper proves to be a generalized phenomenon in blast furnace cokes, then the addition of fine-grained quartz to the surface of the coke before charging a BF can be useful for removing of some of the Al and alkali from the BF gases and reduce coke degradation by alkalis, or at least improve its properties until the temperature reaches approximately 2000{sup o}C. 22 refs., 5 figs., 1 tab.

S.S. Gornostayev; P.A. Tanskanen; E.-P. Heikkinen; O. Kerkkonen; J.J. Haerkki [University of Oulu, Oulu (Finland). Laboratory of Process Metallurgy

2007-09-15T23:59:59.000Z

102

Initial coke deposition on a NiMo/{gamma}-Al{sub 2}O{sub 3} bitumen hydroprocessing catalyst  

SciTech Connect (OSTI)

Athabasca bitumen was hydrocracked over a commercial NiMo/{gamma}-Al{sub 2}O{sub 3} catalyst in two reactors, a microbatch reactor and a 1-L continuous stirred tank reactor (CSTR). Coke deposition on catalyst was measured as a function of hydrogen pressure, time on stream, and liquid composition by measuring the carbon content of the cleaned spent catalyst. The carbon content ranged from 11.3% to 17.6% over the pressure range 6.9--15.2 MPa in CSTR experiments. Batch and CSTR experiments showed a rapid approach to a constant coke content with increasing oil/catalyst ratio. Coke deposition was independent of product composition for residue concentrations ranging from 8% to 32% by weight. Removal of the coke by tetralin at reaction conditions suggested reversible adsorption of residue components on the catalyst surface. A physical model based on clearance of coke by hydrogen in the vicinity of metal crystallites is presented for the coke deposition behavior during the first several hours of hydrocracking use. This model gives good agreement with experimental data, including the effect of reaction time, the ratio of total feed weight to catalyst weight, hydrogen pressure, and feed composition, and it agrees with general observations from industrial usage. The model implies that except at the highest coke levels, the active surfaces of the metal crystallites remain exposed. Severe mass-transfer limitations are caused by the overall narrowing of the pore structure, which in {gamma}-Al{sub 2}O{sub 3} would give very low effective diffusivity for residuum molecules in micropores.

Richardson, S.M.; Nagaishi, Hiroshi; Gray, M.R. [Univ. of Alberta, Edmonton (Canada). Dept. of Chemical Engineering] [Univ. of Alberta, Edmonton (Canada). Dept. of Chemical Engineering

1996-11-01T23:59:59.000Z

103

Usiing NovoCOS cleaning equipment in repairing the furnace-chamber lining in coke batteries 4 & 5 at OAO Koks  

SciTech Connect (OSTI)

Experience with a new surface-preparation technology for the ceramic resurfacing of the refractory furnace-chamber lining in coke batteries is described.

S.G. Protasov; R. Linden; A. Gross [OAO Koks, Kemerovo (Russian Federation)

2009-05-15T23:59:59.000Z

104

Experience and results of new heating control system of coke oven batteries at Rautaruukki Oy Raahe Steel  

SciTech Connect (OSTI)

The latest development and results of the heating control system at Raahe Steel are presented in this paper. From the beginning of coke production in Rautaruukki Oy Raahe Steel (October 1987) the heating control systems have been developed. During the first stage of development work at the coking plant (from year 1987 to 1992), when only the first coke oven battery consisting of 35 ovens was in production, the main progress was in the field of process monitoring. After commissioning of the second stage of the coking plant (November 1992), the development of the new heating control model was started. Target of the project was to develop a dynamic control system which guides the heating of batteries through the various process conditions. Development work took three years and the heating control system was commissioned in the year 1995. Principle of the second generation system is an energy balance calculation, coke end temperature determination and dynamic oven scheduling system. The control is based on simultaneous feedforward and feedback control. The fuzzy logic components were added after about one year experience.

Swanljung, J.; Palmu, P. [Rautaruukki Oy Raahe Steel (Finland)

1997-12-31T23:59:59.000Z

105

Demineralization of petroleum cokes and fly ash samples obtained from the upgrading of Athabasca oil sands bitumen  

SciTech Connect (OSTI)

Today's commercially proved technology to recover oil from the Athabasca oil sands, as practiced by Suncor and Syncrude, involves two major operations, namely: separation of the bitumen from the sand and upgrading of the bitumen to refinery oil. Significant amounts of petroleum coke are produced during the bitumen upgrading process. Suncor burns the bulk of its petroleum coke in boilers to fulfill the energy requirements of the entire operation, still meeting government regulations restricting the amount of sulfur dioxide that can be released to the environment. In contrast, Syncrude is able to burn only 20% of its coke production because of high sulphur dioxide emissions from elsewhere in its operations. The boiler ash (Fly ash) which contains appreciable amounts of metals, such as vanadium, nickel, titianium, iron, aluminum and other elements, is collected in the boiler hoppers and cyclones of the petroleum coke fired steam generation plants. There has been relatively little effort made towards the understanding of the chemical or physical nature of these materials. Knowledge of the physico-chemical properties of these materials will be helpful in assessing their beneficiation and potential use as fuel or metallurigcal coke and the feasibility of extracting some metals, especially Ni and V. In this communication the authors report studies of acid demineralization as a means of reducing ash content of these materials for /sup 13/C NMR spectroscopic investigations.

Majid, A.; Ratcliffe, C.I.; Ripmeester, J.A.

1988-06-01T23:59:59.000Z

106

Proposal of a novel multifunctional energy system for cogeneration of coke, hydrogen, and power - article no. 052001  

SciTech Connect (OSTI)

This paper proposes a novel multifunctional energy system (MES), which cogenerates coke, hydrogen, and power, through the use of coal and coke oven gas (COG). In this system, a new type of coke oven, firing coal instead of COG as heating resource for coking, is adopted. The COG rich in H{sub 2} is sent to a pressure swing adsorption (PSA) unit to separate about 80% of hydrogen first, and then the PSA purge gas is fed to a combined cycle as fuel. The new system combines the chemical processes and power generation system, along with the integration of chemical conversion and thermal energy utilization. In this manner, both the chemical energy of fuel and thermal energy can be used more effectively. With the same inputs of fuel and the same output of coking heat, the new system can produce about 65% more hydrogen than that of individual systems. As a result, the thermal efficiency of the new system is about 70%, and the exergy efficiency is about 66%. Compared with individual systems, the primary energy saving ratio can reach as high as 12.5%. Based on the graphical exergy analyses, we disclose that the integration of synthetic utilization of COG and coal plays a significant role in decreasing the exergy destruction of the MES system. The promising results obtained may lead to a clean coal technology that will utilize COG and coal more efficiently and economically.

Jin, H.G.; Sun, S.; Han, W.; Gao, L. [Chinese Academy of Sciences, Beijing (China)

2009-09-15T23:59:59.000Z

107

Coke oven gas treatment and by-product plant of Magnitogorsk Integrated Iron and Steel Works  

SciTech Connect (OSTI)

Magnitogorsk Integrated Iron and Steel Works, Russia, decided to erect a new coke oven gas treatment and by-product plant to replace the existing obsolete units and to improve the environmental conditions of the area. The paper deals with the technological concept and the design requirements. Commissioning is scheduled at the beginning of 1996. The paper describes H{sub 2}S and NH{sub 3} removal, sulfur recovery and ammonia destruction, primary gas cooling and electrostatic tar precipitation, and the distributed control system that will be installed.

Egorov, V.N.; Anikin, G.J. [Magnitogorsk Integrated Iron and Steel Works, (Russian Federation); Gross, M. [Krupp Koppers GmbH, Essen (Germany)

1995-12-01T23:59:59.000Z

108

Improved wastewater treatment at Wheeling-Pittsburgh Steel Corporations`s Steubenville East Coke Plant  

SciTech Connect (OSTI)

Wheeling-Pittsburgh Steel Corporation recently improved its wastewater treatment at it`s by-products coke plant. This has led to greatly improved effluent quality. Excess ammonia liquor, along with wastewater from the light oil recovery plant, desulfurization facility, and coal pile runoff, must be treated prior to being discharged into the Ohio River. This is accomplished using a biological wastewater treatment plant to remove 99.99% of the organic contaminants and ammonia. Biologically treated, clarified wastewater is now polished in the newly constructed tertiary treatment plant.

Goshe, A.J.; Nodianos, M.J. [Wheeling-Pittsburgh Steel Corp., Follansbee, WV (United States)

1995-12-01T23:59:59.000Z

109

Use of resin-bearing wastes from coke and coal chemicals production at the Novokuznetsk Metallurgical Combine  

SciTech Connect (OSTI)

The coke and coal chemicals plant at the Novokuznetsk Metallurgical Combine is making trial use of a technology that recycles waste products in 'tar ponds.' Specialists from the Ekomash company have installed a recycling unit in one area of the plant's dump, the unit including an inclined conveyor with a steam heater and a receiving hopper The coal preparation shop receives the wastes in a heated bin, where a screw mixes the wastes with pail of the charge for the coking ovens. The mixture subsequently travels along a moving conveyor belt together with the rest of the charge materials. The addition of up to 2% resin-bearing waste materials to the coal charge has not had any significant effect on the strength properties of the coke.

Kul'kova, T.N.; Yablochkin, N.V.; Gal'chenko, A.I.; Karyakina, E.A.; Litvinova, V.A.; Gorbach, D.A.

2007-03-15T23:59:59.000Z

110

Theoretical and experimental investigations into the particular features of the process of converting coal gas hydrocarbons on incandescent coke  

SciTech Connect (OSTI)

The prospects of the use of reducing gases in ferrous metallurgy and the possibilities for using them as a basis for coke production have been presented by the authors of the present article in the past. In the present report, the authors present certain results of theoretical and experimental investigations into the process of converting coal gas hydrocarbons on incandescent coke. The modification of the present-day method of thermodynamically calculating stable compositions of coking products, which was developed by the authors, has made it possible to apply it to specific chemical systems and process conditions not met with before, such as the conversion of hydrocarbons in mixtures of actual industrial gases (coal gas and blast furnace gas) in the presence of carbon and considerable amounts of hydrogen.

Zubilin, I.G.; Umanskii, V.E.

1984-01-01T23:59:59.000Z

111

Cracking of simulated oil refinery off-gas over a coal char, petroleum coke, and quartz  

SciTech Connect (OSTI)

The cracking of oil refinery off-gas, simulated with a gas mixture containing methane (51%), ethylene (21.4%), ethane (21.1%), and propane (6.5%), over a coal char, petroleum coke, and quartz, respectively, has been studied in a fixed bed reactor. The experiments were performed at temperatures between 850 and 1000{sup o}C and at atmospheric pressure. The results show that the conversions of all species considered increased with increasing temperature. Ethane and propane completely decomposed over all three bed materials in the temperature range investigated. However, the higher initial conversion rates of methane and ethylene cracking at all temperatures were observed only over the coal char and not on the petroleum coke and quartz, indicating a significant catalytic effect of the coal char on methane and ethylene cracking. Methane and ethylene conversions decreased with reaction time due to deactivation of the coal char by carbon deposition on the char surface and, in the later stage of a cracking experiment, became negative, suggesting that methane and ethylene had been formed during the cracking of ethane and propane. 16 refs., 13 figs., 2 tabs.

Yuan Zhang; Jin-hu Wu; Dong-ke Zhang [Chinese Academy of Sciences, Taiyuan (China). Institute of Coal Chemistry

2008-03-15T23:59:59.000Z

112

Petroleum Coke  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in Nonproducing ReservoirsYear-MonthCoalbedPricethe PricetheCity Gate Price81,811

113

Petroleum Coke  

Gasoline and Diesel Fuel Update (EIA)

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE:1 First Use of Energy for All Purposes (Fuel and Nonfuel),Feet) Year Jan Feb Mar Apr May Jun Jul(Summary) " ,"ClickPipelines About U.S.30 2013 Macroeconomicper8,170 8,310 8,304PricePriceby81,811 82,516 82,971

114

Urinary 1-hydroxypyrene concentrations in Chinese coke oven workers relative to job category, respirator usage, and cigarette smoking  

SciTech Connect (OSTI)

1-Hydroxypyrene (1-OHP) is a biomarker of recent exposure to polycyclic aromatic hydrocarbons (PAHs). We investigated whether urinary 1-OHP concentrations in Chinese coke oven workers (COWs) are modulated by job category, respirator usage, and cigarette smoking. The present cross-sectional study measured urinary 1-OHP concentrations in 197 COWs from Coking plant I and 250 COWs from Coking plant II, as well as 220 unexposed referents from Control plant I and 56 referents from Control plant II. Urinary 1-OHP concentrations (geometric mean, {mu}mol/mol creatinine) were 5.18 and 4.21 in workers from Coking plants I and II, respectively. The highest 1-OHP levels in urine were found among topside workers including lidmen, tar chasers, and whistlers. Benchmen had higher 1-OHP levels than other workers at the sideoven. Above 75% of the COWs exceeded the recommended occupational exposure limit of 2.3 {mu}mol/mol creatinine. Respirator usage and increased body mass index (BMI) slightly reduced 1-OHP levels in COWs. Cigarette smoking significantly increased urinary 1-OHP levels in unexposed referents but had no effect in COWs. Chinese COWs, especially topside workers and benchmen, are exposed to high levels of PAHs. Urinary 1-OHP concentrations appear to be modulated by respirator usage and BMI in COWs, as well as by smoking in unexposed referents.

Bo Chen; Yunping Hu; Lixing Zheng; Qiangyi Wang; Yuanfen Zhou; Taiyi Jin [Fudan University, Shanghai (China). School of Public Health

2007-09-15T23:59:59.000Z

115

Evaluation of pitches and cokes from solvent-extracted coal materials  

SciTech Connect (OSTI)

Three initial coal-extracted (C-E) samples were received from the West Virginia University (WVU) Chemical Engineering Department. Two samples had been hydrogenated to obtain pitches that satisfy Theological requirements. One of the hydrogenated (HC-E) samples had been extracted by toluene to remove ash and higher molecular weight aromatic compounds. We were unable to measure the softening point and viscosity of the non-hydro treated solid extract sample, Positive characteristics in the HC-E materials were softening points of 113-119{degrees}C, low sulfur and ash. The oxygen and nitrogen content of the HC-E samples may limit future usage in premium carbon and graphite products. Coking values were similar to petroleum pitches. Laboratory anode testing indicates that in combination with standard coal-tar pitch, the HC-E material can be used as a binder pitch.

McHenry, E.R.

1996-12-01T23:59:59.000Z

116

Cyanide leaching from soil developed from coking plant purifier waste as influenced by citrate  

SciTech Connect (OSTI)

Soils in the vicinity of manufactured gas plants and coal coking plants are often highly contaminated with cyanides in the form of the compound Prussian blue. The objective of this study was to investigate the influence of citrate on the leaching of iron-cyanide complexes from an extremely acidic soil (pH 2.3) developed from gas purifier waste near a former coking plant. The soil contained 63 g kg{sup -1} CN, 148 g kg{sup -1} Fe, 123 g kg{sup -1} S, and 222 g kg{sup -1} total C. Analysis of the soil by X-ray diffraction (XRD) and Fourier transform infrared (FT-IR) spectroscopy revealed the presence of Prussian blue, gypsum, elemental sulfur, jarosite, and hematite. For column leaching experiments, air-dried soil was mixed with purified cristabolite sand at a ratio of 1:3 and packed into chromatography columns. The soil was leached with dilute (0.1 or 1 mM) CaCl{sub 2} solutions and the effluent was collected and analyzed for total and dissolved CN, Ca, Fe, SO{sub 4}, pH, and pe. In the absence of citrate, the total dissolved CN concentration in the effluent was always below current drinking water limits (< 1.92 {mu}M), indicating low leaching potential. Adding citrate at a concentration of 1 mM had little effect on the CN concentrations in the column effluent. Addition of 10 or 100 mM citrate to the influent solution resulted in strong increases in dissolved and colloidal CN concentrations in the effluent.

Tim Mansfeldt; Heike Leyer; Kurt Barmettler; Ruben Kretzschmar [Ruhr-University Bochum, Bochum (Germany). Soil Science and Soil Ecology Group, Faculty of Geosciences

2004-07-01T23:59:59.000Z

117

Development and Testing of the Advanced CHP System Utilizing the Off-Gas from the Innovative Green Coke Calcining Process in Fluidized Bed  

SciTech Connect (OSTI)

Green petroleum coke (GPC) is an oil refining byproduct that can be used directly as a solid fuel or as a feedstock for the production of calcined petroleum coke. GPC contains a high amount of volatiles and sulfur. During the calcination process, the GPC is heated to remove the volatiles and sulfur to produce purified calcined coke, which is used in the production of graphite, electrodes, metal carburizers, and other carbon products. Currently, more than 80% of calcined coke is produced in rotary kilns or rotary hearth furnaces. These technologies provide partial heat utilization of the calcined coke to increase efficiency of the calcination process, but they also share some operating disadvantages. However, coke calcination in an electrothermal fluidized bed (EFB) opens up a number of potential benefits for the production enhancement, while reducing the capital and operating costs. The increased usage of heavy crude oil in recent years has resulted in higher sulfur content in green coke produced by oil refinery process, which requires a significant increase in the calcinations temperature and in residence time. The calorific value of the process off-gas is quite substantial and can be effectively utilized as an “opportunity fuel” for combined heat and power (CHP) production to complement the energy demand. Heat recovered from the product cooling can also contribute to the overall economics of the calcination process. Preliminary estimates indicated the decrease in energy consumption by 35-50% as well as a proportional decrease in greenhouse gas emissions. As such, the efficiency improvement of the coke calcinations systems is attracting close attention of the researchers and engineers throughout the world. The developed technology is intended to accomplish the following objectives: - Reduce the energy and carbon intensity of the calcined coke production process. - Increase utilization of opportunity fuels such as industrial waste off-gas from the novel petroleum coke calcination process. - Increase the opportunity of heat (chemical and physical) utilization from process off-gases and solid product. - Develop a design of advanced CHP system utilizing off-gases as an “opportunity fuel” for petroleum coke calcinations and sensible heat of calcined coke. A successful accomplishment of the aforementioned objectives will contribute toward the following U.S. DOE programmatic goals: - Drive a 25% reduction in U. S. industrial energy intensity by 2017 in support of EPAct 2005; - Contribute to an 18% reduction in U.S. carbon intensity by 2012 as established by the Administration’s “National Goal to Reduce Emissions Intensity.” 8

Chudnovsky, Yaroslav; Kozlov, Aleksandr

2013-08-15T23:59:59.000Z

118

Innovative coke oven gas cleaning system for retrofit applications. Environmental Monitoring program. Volume 1 - sampling progrom report. Baseline Sampling Program report  

SciTech Connect (OSTI)

Bethlehem Steel Corporation (BSC), in conjunction with the Department of Energy (DOE) is conducting a Clean Coal Technology (CCT) project at its Sparrows Point, Maryland Coke Oven Plant. This innovative coke oven gas cleaning system combines several existing technologies into an integrated system for removing impurities from Coke Oven Gas (COG) to make it an acceptable fuel. DOE provided cost-sharing under a Cooperative Agreement with BSC. This Cooperative Agreement requires BSC to develop and conduct and Environmental Monitoring Plan for the Clean Coal Technology project and to report the status of the EMP on a quarterly basis. It also requires the preparation of a final report on the results of the Baseline Compliance and Supplemental Sampling Programs that are part of the EMP and which were conducted prior to the startup of the innovative coke oven gas cleaning system. This report is the Baseline Sampling Program report.

Stuart, L.M.

1994-05-27T23:59:59.000Z

119

Effects of HyperCoal addition on coke strength and thermoplasticity of coal blends  

SciTech Connect (OSTI)

Ashless coal, also known as HyperCoal (HPC), was produced by thermal extraction of three coals of different ranks (Gregory caking coal, Warkworth steam coal, and Pasir subbituminous coal) with 1-methylnaphthalene (1-MN) at 360, 380, and 400{sup o}C. The effects of blending these HPCs into standard coal blends were investigated. Blending HPCs as 5-10% of a standard blend (Kouryusho:Goonyella:K9) enhanced the thermoplasticity over a wide temperature range. For blends made with the Pasir-HPC, produced from a noncaking coal, increasing the extraction temperature from 360 to 400{sup o}C increased the thermoplasticity significantly. Blends containing Warkworth-HPC, produced from a slightly caking coal, had a higher tensile strength than the standard blend in semicoke strength tests. The addition of 10% Pasir-HPC, extracted at 400{sup o}C, increased the tensile strength of the semicokes to the same degree as those made with Gregory-HPC. Furthermore, all HPC blends had a higher tensile strength and smaller weight loss during carbonization. These results suggest that the HPC became integrated into the coke matrix, interacting strongly with the other raw coals. 14 refs., 11 figs., 1 tab.

Toshimasa Takanohashi; Takahiro Shishido; Ikuo Saito [National Institute of Advanced Industrial Science and Technology (AIST), Tsukuba (Japan). Energy Technology Research Institute

2008-05-15T23:59:59.000Z

120

Role of hydrogen in blast furnaces to improve productivity and decrease coke consumption  

SciTech Connect (OSTI)

The hydrogen contained in blast furnace gases exerts a variety of physical, thermochemical, and kinetic effects as the gases pass through the various zones. The hydrogen is derived from two sources: (1) the dissociation of moisture in the blast air (ambient and injected with hot blast), and (2) the release from partial combustion of supplemental fuels (including moisture in atomizing water, steam, or transport air, if any). With each atom of oxygen (or carbon), the molar amounts of hydrogen released are more than six times higher for natural gas than for coal, and two times higher for natural gas than for oil. Injection of natural gas in a blast furnace is not a new process. Small amounts of natural gas--about 50--80 lb or 1,100--1,700 SCF/ton of hot metal--have been injected in many of the North American blast furnaces since the early 1960s, with excellent operating results. What is new, however, is a batter understanding of how natural gas reacts in the blast furnace and how natural gas and appropriate quantities of oxygen can be used to increase the driving rate or combustion rate of carbon (coke) in the blast furnace without causing hanging furnace and operating problems. The paper discusses the factors limiting blast furnace productivity and how H{sub 2} and O{sub 2} can increase productivity.

Agarwal, J.C.; Brown, F.C.; Chin, D.L.; Stevens, G.; Clark, R.; Smith, D.

1995-12-01T23:59:59.000Z

Note: This page contains sample records for the topic "lignite coke coke" from the National Library of EnergyBeta (NLEBeta).
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to obtain the most current and comprehensive results.


121

Dispersion modeling of polycyclic aromatic hydrocarbons from combustion of biomass and fossil fuels and production of coke in Tianjin, China  

SciTech Connect (OSTI)

A USEPA procedure, ISCLT3 (Industrial Source Complex Long-Term), was applied to model the spatial distribution of polycyclic aromatic hydrocarbons (PAHs) emitted from various sources including coal, petroleum, natural gas, and biomass into the atmosphere of Tianjin, China. Benzo(a)pyrene equivalent concentrations (BaPeq) were calculated for risk assessment. Model results were provisionally validated for concentrations and profiles based on the observed data at two monitoring stations. The dominant emission sources in the area were domestic coal combustion, coke production, and biomass burning. Mainly because of the difference in the emission heights, the contributions of various sources to the average concentrations at receptors differ from proportions emitted. The shares of domestic coal increased from {approximately} 43% at the sources to 56% at the receptors, while the contributions of coking industry decreased from {approximately} 23% at the sources to 7% at the receptors. The spatial distributions of gaseous and particulate PAHs were similar, with higher concentrations occurring within urban districts because of domestic coal combustion. With relatively smaller contributions, the other minor sources had limited influences on the overall spatial distribution. The calculated average BaPeq value in air was 2.54 {+-} 2.87 ng/m{sup 3} on an annual basis. Although only 2.3% of the area in Tianjin exceeded the national standard of 10 ng/m{sup 3}, 41% of the entire population lives within this area. 37 refs., 9 figs.

Shu Tao; Xinrong Li; Yu Yang; Raymond M. Coveney, Jr.; Xiaoxia Lu; Haitao Chen; Weiran Shen [Peking University, Beijing (China). Laboratory for Earth Surface Processes, College of Environmental Sciences

2006-08-01T23:59:59.000Z

122

Study on the effect of heat treatment and gasification on the carbon structure of coal chars and metallurgical cokes using fourier transform Raman spectroscopy  

SciTech Connect (OSTI)

Differences in the development of carbon structures between coal chars and metallurgical cokes during high-temperature reactions have been investigated using Raman spectroscopy. These are important to differentiate between different types of carbons in dust recovered from the top gas of the blast furnace. Coal chars have been prepared from a typical injectant coal under different heat-treatment conditions. These chars reflected the effect of peak temperature, residence time at peak temperature, heating rate and pressure on the evolution of their carbon structures. The independent effect of gasification on the development of the carbon structure of a representative coal char has also been studied. A similar investigation has also been carried out to study the effect of heat-treatment temperature (from 1300 to 2000{sup o}C) and gasification on the carbon structure of a typical metallurgical coke. Two Raman spectral parameters, the intensity ratio of the D band to the G band (I{sub D}/I{sub G}) and the intensity ratio of the valley between D and G bands to the G band (I{sub V}/I{sub G}), have been found useful in assessing changes in carbon structure. An increase in I{sub D}/I{sub G} indicates the growth of basic graphene structural units across the temperature range studied. A decrease in I{sub V}/I{sub G} appears to suggest the elimination of amorphous carbonaceous materials and ordering of the overall carbon structure. The Raman spectral differences observed between coal chars and metallurgical cokes are considered to result from the difference in the time-temperature history between the raw injectant coal and the metallurgical coke and may lay the basis for differentiation between metallurgical coke fines and coal char residues present in the dust carried over the top of the blast furnace. 41 refs., 17 figs., 3 tabs.

S. Dong; P. Alvarez; N. Paterson; D.R. Dugwell; R. Kandiyoti [Imperial College London, London (United Kingdom). Department of Chemical Engineering

2009-03-15T23:59:59.000Z

123

Further investigation of the impact of the co-combustion of tire-derived fuel and petroleum coke on the petrology and chemistry of coal combustion products  

SciTech Connect (OSTI)

A Kentucky cyclone-fired unit burns coal and tire-derived fuel, sometimes in combination with petroleum coke. A parallel pulverized combustion (pc) unit at the same plant burns the same coal, without the added fuels. The petrology, chemistry, and sulfur isotope distribution in the fuel and resulting combustion products was investigated for several configurations of the fuel blend. Zinc and Cd in the combustion products are primarily contributed from the tire-derived fuel, the V and Ni are primarily from the petroleum coke, and the As and Hg are probably largely from the coal. The sulfur isotope distribution in the cyclone unit is complicated due to the varying fuel sources. The electrostatic precipitator (ESP) array in the pc unit shows a subtle trend towards heavier S isotopic ratios in the cooler end of the ESP.

Hower, J.C.; Robertson, J.D.; Elswick, E.R.; Roberts, J.M.; Brandsteder, K.; Trimble, A.S.; Mardon, S.M. [University of Kentucky, Lexington, KY (United States). Center for Applied Energy Research

2007-07-01T23:59:59.000Z

124

Determination of the effect of different additives in coking blends using a combination of in situ high-temperature {sup 1}H NMR and rheometry  

SciTech Connect (OSTI)

High-temperature {sup 1}H NMR and rheometry measurements were carried out on 4:1 wt/wt blends of a medium volatile bituminous coal with two anthracites, two petroleum cokes, charcoal, wood, a low-temperature coke breeze, tyre crumb, and active carbon to determine the effects on fluidity development to identify the parameters responsible for these effects during pyrolysis and to study possible relationships among the parameters derived from these techniques. Positive, negative, and neutral effects were identified on the concentration of fluid material. Small positive effects (ca. 5-6%) were caused by blending the coal with petroleum cokes. Charcoal, wood, and active carbon all exerted negative effects on concentration (18-27% reduction) and mobility (12-25% reduction in T2) of the fluid phase, which have been associated with the inert character and high surface areas of these additives that adsorb the fluid phase of the coal. One of the anthracites and the low-temperature coke breeze caused deleterious effects to a lesser extent on the concentration (7-12%) and mobility (13-17%) of the fluid material, possibly due to the high concentration of metals in these additives (ca. 11% ash). Despite the high fluid character of tyre crumb at the temperature of maximum fluidity of the coal (73%), the mobility of the fluid phase of the blend was lower than expected. The comparison of {sup 1}H NMR and rheometry results indicated that to account for the variations in minimum complex viscosity for all the blends, both the maximum concentration of fluid phase and the maximum mobility of the fluid material had to be considered. For individual blends, two exponential relationships have been found between the complex viscosity and the concentration of solid phase in both the softening and resolidification stages but the parameters are different for each blend. 30 refs., 8 figs., 5 tabs.

Miguel C. Diaz; Karen M. Steel; Trevor C. Drage; John W. Patrick; Colin E. Snape [Nottingham University, Nottingham (United Kingdom). Nottingham Fuel and Energy Centre, School of Chemical, Environmental and Mining Engineering

2005-12-01T23:59:59.000Z

125

Effects of polymerization and briquetting parameters on the tensile strength of briquettes formed from coal coke and aniline-formaldehyde resin  

SciTech Connect (OSTI)

In this work, the utilization of aniline (C{sub 6}H{sub 7}N) formaldehyde (HCHO) resins as a binding agent of coke briquetting was investigated. Aniline (AN) formaldehyde (F) resins are a family of thermoplastics synthesized by condensing AN and F in an acid solution exhibiting high dielectric strength. The tensile strength sharply increases as the ratio of F to AN from 0.5 to 1.6, and it reaches the highest values between 1.6 and 2.2 F/AN ratio; it then slightly decreases. The highest tensile strength of F-AN resin-coke briquette (23.66 MN/m{sup 2}) was obtained from the run with 1.5 of F/AN ratio by using (NH4){sub 2}S{sub 2}O{sub 8} catalyst at 310 K briquetting temperature. The tensile strength of F-AN resin-coke briquette slightly decreased with increasing the catalyst percent to 0.10%, and then it sharply decreased to zero with increasing the catalyst percent to 0.2%. The effect of pH on the tensile strength is irregular. As the pH of the mixture increases from 9.0 to 9.2, the tensile strength shows a sharp increase, and the curve reaches a plateau value between pH 9.3 and 9.9; then the tensile strength shows a slight increase after pH = 9.9.

Demirbas, A.; Simsek, T. [Selcuk University, Konya (Turkey)

2006-10-15T23:59:59.000Z

126

Reduction of COD in leachate from a hazardous waste landfill adjacent to a coke-making facility  

SciTech Connect (OSTI)

A hazardous waste landfill adjacent to a coke manufacturing facility was in operation between July 1990 and December 1991. A system was constructed to collect and treat the leachate from the landfill prior to discharge to the river. Occasionally, the discharge from the treatment facility exceeded the permit limitations for Chemical Oxygen Demand (COD), Biochemical Oxygen Demand (BOD), and Total Organic Carbon (TOC). The objectives of this study were to determine treatment methods which would enable compliance with the applicable discharge limits; to establish the desired operating conditions of the process; and to investigate the effect of various parameters such as pH, catalyst dosage, and reaction time on the COD destruction efficiency. The characteristics of the landfill leachate in question were significantly variable in terms of chemical composition. A review of the influent quality data suggests that the COD concentration ranges between 80 and 390 mg/l. The oxidation processes using Fenton`s reagent or a combination of UV/hydrogen peroxide/catalyst are capable of reducing the COD concentration of the leachate below the discharge limitation of 35 mg/l. The estimated capital cost associated with the Fenton`s reagent process is approximately $525,000, and the annual operating and maintenance cost is $560,000. The estimated capital cost for the UV/hydrogen peroxide/catalyst treatment system is $565,000. The annual operating and maintenance cost of this process would be approximately $430,000.

Banerjee, K.; O`Toole, T.J. [Chester Environmental, Moon Township, PA (United States)

1995-12-01T23:59:59.000Z

127

Laser ultrasonic furnace tube coke monitor. Quarterly technical progress report. Report No. 5 for reporting period May 1, 1999 through August 1, 1999  

SciTech Connect (OSTI)

The overall aim of the project is to demonstrate the performance and practical use of a probe for measuring the thickness of coke deposits located within the high-temperature tubes of a thermal cracking furnace. The objective of work during this period was to enhance the sensitivity and signal-to-noise ratio of the probe measurement. Testing identified that the primary source of signal noise was traced to imperfections in the sacrificial stand-off, which was formed using a casting procedure. Laminations, voids, and impurities contained in the casting result in attenuation and dispersion of the ultrasonic signal. This report describes the work performed to optimize the signal conductance of the sacrificial stand-off.

NONE

1999-08-15T23:59:59.000Z

128

Coking Coal Import Costs - EIA  

Gasoline and Diesel Fuel Update (EIA)

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129

JV Task 90 - Activated Carbon Production from North Dakota Lignite  

SciTech Connect (OSTI)

The Energy & Environmental Research Center (EERC) has pursued a research program for producing activated carbon from North Dakota lignite that can be competitive with commercial-grade activated carbon. As part of this effort, small-scale production of activated carbon was produced from Fort Union lignite. A conceptual design of a commercial activated carbon production plant was drawn, and a market assessment was performed to determine likely revenue streams for the produced carbon. Activated carbon was produced from lignite coal in both laboratory-scale fixed-bed reactors and in a small pilot-scale rotary kiln. The EERC was successfully able to upgrade the laboratory-scale activated carbon production system to a pilot-scale rotary kiln system. The activated carbon produced from North Dakota lignite was superior to commercial grade DARCO{reg_sign} FGD and Rheinbraun's HOK activated coke product with respect to iodine number. The iodine number of North Dakota lignite-derived activated carbon was between 600 and 800 mg I{sub 2}/g, whereas the iodine number of DARCO FGD was between 500 and 600 mg I{sub 2}/g, and the iodine number of Rheinbraun's HOK activated coke product was around 275 mg I{sub 2}/g. The EERC performed both bench-scale and pilot-scale mercury capture tests using the activated carbon made under various optimization process conditions. For comparison, the mercury capture capability of commercial DARCO FGD was also tested. The lab-scale apparatus is a thin fixed-bed mercury-screening system, which has been used by the EERC for many mercury capture screen tests. The pilot-scale systems included two combustion units, both equipped with an electrostatic precipitator (ESP). Activated carbons were also tested in a slipstream baghouse at a Texas power plant. The results indicated that the activated carbon produced from North Dakota lignite coal is capable of removing mercury from flue gas. The tests showed that activated carbon with the greatest iodine number was superior to commercial DARCO FGD for mercury capture. The results of the activated carbon market assessment indicate an existing market for water treatment and an emerging application for mercury control. That market will involve both existing and new coal-fired plants. It is expected that 20% of the existing coal-fired plants will implement activated carbon injection by 2015, representing about 200,000 tons of annual demand. The potential annual demand by new plants is even greater. In the mercury control market, two characteristics are going to dominate the customer's buying habit-performance and price. As continued demonstration testing of activated carbon injection at the various coal-fired power plants progresses, the importance of fuel type and plant configuration on the type of activated carbon best suited is being identified.

Steven Benson; Charlene Crocker; Rokan Zaman; Mark Musich; Edwin Olson

2008-03-31T23:59:59.000Z

130

Pelletizing lignite  

DOE Patents [OSTI]

Lignite is formed into high strength pellets having a calorific value of at least 9,500 Btu/lb by blending a sufficient amount of an aqueous base bituminous emulsion with finely-divided raw lignite containing its inherent moisture to form a moistened green mixture containing at least 3 weight % of the bituminous material, based on the total dry weight of the solids, pelletizing the green mixture into discrete green pellets of a predetermined average diameter and drying the green pellets to a predetermined moisture content, preferrably no less than about 5 weight %. Lignite char and mixture of raw lignite and lignite char can be formed into high strength pellets in the same general manner.

Goksel, Mehmet A. (Houghton, MI)

1983-11-01T23:59:59.000Z

131

Petroleum Coke: A Viable Fuel for Cogeneration  

E-Print Network [OSTI]

; buy sulfur dioxide credits on the open market; install FGD; or switch to clean coal technology such as circulating fluidized bed combustion and gasification. Current trends in utility modernization are to utilize new clean coal technologies...

Dymond, R. E.

132

Coking Coal Prices for Industry - EIA  

Gasoline and Diesel Fuel Update (EIA)

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133

Table 16. U.S. Coke Exports  

Gasoline and Diesel Fuel Update (EIA)

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134

Table 21. U.S. Coke Imports  

Gasoline and Diesel Fuel Update (EIA)

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135

China's Industrial Carbon Dioxide Emissions in Manufacturing Subsectors and in Selected Provinces  

E-Print Network [OSTI]

Coal Washed Coal Coke Coke Oven Gas Other Gas Other CokingTJ) Coal Coke Coke Oven Gas Other Gas Other Coking Products

Lu, Hongyou

2013-01-01T23:59:59.000Z

136

Lignite Fuel Enhancement  

SciTech Connect (OSTI)

This 6th quarterly Technical Progress Report for the Lignite Fuel Enhancement Project summarizes activities from October 1st through December 31st of 2005. It also summarizes the subsequent purchasing activity and dryer/process construction. Hypothesis remains the same. We will be able to dry lignite an increment to benefit the performance of and reduce emissions from a coal burning electric power generating station.

Charles Bullinger

2006-02-03T23:59:59.000Z

137

E-Print Network 3.0 - activated carbon-based adsorbents Sample...  

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

two primary elements, the filter media (activated carbon or lignite coke) to adsorb pollutants... in that Marker's past experience has been that Hg capture with carbon or carbon...

138

Assessment of Energy Efficiency Improvement and CO2 Emission Reduction Potentials in the Iron and Steel Industry in China  

E-Print Network [OSTI]

factor of bituminous coal, coking coal, and coke consumed inprice of Bituminous coal, coking coal, and coke consumed in

Hasanbeigi, Ali

2013-01-01T23:59:59.000Z

139

Characterisation of coking activity during supercritical hydrocarbon Nicolas Gascoina*  

E-Print Network [OSTI]

(SCRamjet) beyond [3] [4], because of its high specific impulse and its capability to be reusable [5] [6-France company and its partners with calculations [8] and material tests [9]-[11]. The principle of SCRAMJET

Paris-Sud XI, Université de

140

Hydroprocessing Bio-oil and Products Separation for Coke Production  

SciTech Connect (OSTI)

Fast pyrolysis of biomass can be used to produce a raw bio-oil product, which can be upgraded by catalytic hydroprocessing to hydrocarbon liquid products. In this study the upgraded products were distilled to recover light naphtha and oils and to produce a distillation resid with useful properties for coker processing and production of renewable, low-sulfur electrode carbon. For this hydroprocessing work, phase separation of the bio-oil was applied as a preparatory step to concentrate the heavier, more phenolic components thus generating a more amenable feedstock for resid production. Low residual oxygen content products were produced by continuous-flow, catalytic hydroprocessing of the phase separated bio-oil.

Elliott, Douglas C.; Neuenschwander, Gary G.; Hart, Todd R.

2013-04-01T23:59:59.000Z

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


141

Table 33. Coal Carbonized at Coke Plants by Census Division  

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

2014 Year to Date Census Division April - June 2014 January - March 2014 April - June 2013 2014 2013 Percent Change Middle Atlantic 1,599 1,503 1,622 3,102 3,178 -2.4 East North...

142

Cogeneration Waste Heat Recovery at a Coke Calcining Facility  

E-Print Network [OSTI]

hard surface overlays on their impellers and scrolls to prevent erosion. The use of linings was selected after a comprehensive study was performed investi gating the expected wear on unlined equipment, additional cost of linings, frequency of main... is provided fr the pump discharge head r for of the bypass steam e tering carbon steel steam sal s line line of the refine is feet long. The st am is metered by a primary venturi flow nozzle, essure transmitters, and temperature elements ne r...

Coles, R. L.

143

Table 38. Coal Stocks at Coke Plants by Census Division  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE:1 First Use of Energy for All Purposes (Fuel and Nonfuel),Feet) Year Jan Feb Mar Apr MayAtmosphericNuclear Security AdministrationcontrollerNanocrystallineForeign ObjectOUR Table 1. Summary: ReportedEnergyChanges

144

Coke County, Texas: Energy Resources | Open Energy Information  

Open Energy Info (EERE)

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data Center Home5b9fcbce19 NoPublic Utilities Address: 160Benin:EnergyWisconsin: Energy, -105.3774934°Coda BatteryCohoe, Alaska:

145

Nippon Coke and Engineering Sumitomo Corp JV | Open Energy Information  

Open Energy Info (EERE)

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data Center Home5b9fcbce19 No revision hasInformation Earth's HeatMexico: EnergyMithunCenterInformationNexxus(CTI PFAN)Corp JV Jump to:

146

Table 17. Average Price of U.S. Coke Exports  

Gasoline and Diesel Fuel Update (EIA)

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE:1 First Use of Energy for All Purposes (Fuel and Nonfuel),Feet) Year Jan Feb Mar Apr May Jun Jul(Summary) " ,"Click worksheet9,1,50022,3,,,,6,1,,781 2,328AdministrationReleaseMetallurgical Coal Exports byAverage

147

Table 22. Average Price of U.S. Coke Imports  

Gasoline and Diesel Fuel Update (EIA)

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE:1 First Use of Energy for All Purposes (Fuel and Nonfuel),Feet) Year Jan Feb Mar Apr May Jun Jul(Summary) " ,"Click worksheet9,1,50022,3,,,,6,1,,781 2,328AdministrationReleaseMetallurgical Coal ExportsPriceAverage

148

A study of pyrolysis of Texas lignites  

E-Print Network [OSTI]

better correlation for Dulong's formula. Yegua and Dakota lignites are readily obtainable and would provide a good check on the results derived from the Calvert Bluff lignites. The present equ1pment would also be used to study gasification of lignite...A STUDY OF PYROLYSIS OF TEXAS LIGNITES A Thesis by Robert A. Clark, Jr. Submitted to the Graduate College of Texas AAN University in partial fulfillment of the requirement for the degree of MASTER OF SCIENCE Nay 1979 Major Subject...

Clark, Robert A

1979-01-01T23:59:59.000Z

149

Trace element partitioning in Texas lignite  

E-Print Network [OSTI]

lignites and largest individual deposits in Texas occur in the Wilcox group north of the Colorado River; the lowest quality lignite occurs in the Jackson group (2). A comparison between the elemental composition of lignite from the wilcox formation..., Rb, Sc, Th, U, V, Y, Yb, Zn and Zr are positively correlated and B decreases 10 in concentration with increasing levels of ash (15) Combustion. Texas can supply a large portion of its energy needs with its near surface lignite sources (21...

Acevedo, Lillian Esther

1989-01-01T23:59:59.000Z

150

Trace element analysis of Texas lignite  

E-Print Network [OSTI]

or in the planning stages, Near surface lignite re- sources are estimated to be 21 billion metric tons in Texas, while deep basin reserves are estimated at 31 billion metric tons. Near (3] surface reserves alone could fulfill Texas' electrical needs for 100 years... for environmental and health concerns trace element characterization of lignites is important. A needed avenue of research is charact- erization of trace element pathways in lignite fired power plants. :hat is to say what percentage of a certain element...

Mahar, Sean

1982-01-01T23:59:59.000Z

151

Energy Efficiency Improvement and Cost Saving Opportunities for the U.S. Iron and Steel Industry An ENERGY STAR(R) Guide for Energy and Plant Managers  

E-Print Network [OSTI]

In addition, the coking coal market began to deteriorateits permeability. Bituminous, or coking coal, is blended andmerchant coke plants, coking coal is heated in a low-oxygen,

Worrell, Ernst

2011-01-01T23:59:59.000Z

152

Lignite pellets and methods of agglomerating or pelletizing  

DOE Patents [OSTI]

The specification discloses lignite pellets which are relatively hard, dust resistant, of generally uniform size and free from spontaneous ignition and general degradation. Also disclosed are methods for making such pellets which involve crushing as mined lignite, mixing said lignite with a binder such as asphalt, forming the lignite binder mixture into pellets, and drying the pellets.

Baker, Albert F. (Pittsburgh, PA); Blaustein, Eric W. (Pittsburgh, PA); Deurbrouck, Albert W. (Pittsburgh, PA); Garvin, John P. (Pittsburgh, PA); McKeever, Robert E. (Pittsburgh, PA)

1981-01-01T23:59:59.000Z

153

Lignite-based nitrogenous fertilizers  

SciTech Connect (OSTI)

A sample of lignite from Elbistan was oxidized by nitric acid in two stages, using relatively dilute acid in the first stage and concentrated acid in the second stage, and then the oxidized product was ammoniated so that a coal-based fertilizer could be produced. The experiments of all the stages were designed by a 1/2 X full factorial design. It was observed that base exchange capacity and nitrogen content of coal-based fertilizers produced in this work were as good as or better than those obtained by other investigators.

Baris, H.; Dincer, S.

1983-01-01T23:59:59.000Z

154

COFIRING BIOMASS WITH LIGNITE COAL  

SciTech Connect (OSTI)

The University of North Dakota Energy & Environmental Research Center, in support of the U.S. Department of Energy's (DOE) biomass cofiring program, completed a Phase 1 feasibility study investigating aspects of cofiring lignite coal with biomass relative to utility-scale systems, specifically focusing on a small stoker system located at the North Dakota State Penitentiary (NDSP) in Bismarck, North Dakota. A complete biomass resource assessment was completed, the stoker was redesigned to accept biomass, fuel characterization and fireside modeling tests were performed, and an engineering economic analysis was completed. In general, municipal wood residue was found to be the most viable fuel choice, and the modeling showed that fireside problems would be minimal. Experimental ash deposits from firing 50% biomass were found to be weaker and more friable compared to baseline lignite coal. Experimental sulfur and NO{sub x} emissions were reduced by up to 46%. The direct costs savings to NDSP, from cogeneration and fuel saving, results in a 15- to 20-year payback on a $1,680,000 investment, while the total benefits to the greater community would include reduced landfill burden, alleviation of fees for disposal by local businesses, and additional jobs created both for the stoker system as well as from the savings spread throughout the community.

Darren D. Schmidt

2002-01-01T23:59:59.000Z

155

Mitsubishi FGD plants for lignite fired boilers  

SciTech Connect (OSTI)

In order to respond to the increasing electric energy demand for sustaining economic growth, construction of coal-fired thermal power plants worldwide is indispensable. As a countermeasure for environmental pollution which otherwise may reach a serious proportion from the operation of these plants, construction of flue gas desulfurization (FGD) plants is being promoted. Among these power stations where lignite fuel is burnt, the FGD plants concerned have to be designed to cope with high gas volume and SO{sub x} concentration as well as violent fluctuations in their values caused by such features of lignite as high sulfur content, low calorific volume, and unstable properties. Mitsubishi Heavy Industries (MHI) has received construction awards for a total of seven (7) FGD plants for lignite-fired boilers in succession starting from that for CEZ as, Czech Republic followed by those for EGAT, Thailand in 1993. All these plants are presently operating satisfactorily since successful completion of their performance tests in 1996. Further, a construction award of three (3) more FGD plants for lignite-fired boilers was received from ENDESA (Spain) in 1995 which are now being outfitted and scheduled to start commercial operation in 1998. In this paper, the authors discuss the outline design of FGD plants for lignite-fired boilers based on experience of FGD plants constructed since 1970 for heavy oil--as well as black coal-fired boilers, together with items confirmed from the operation and design guideline hereafter.

Kotake, Shinichiro; Okazoe, Kiyoshi; Iwashita, Koichiro; Yajima, Satoru

1998-07-01T23:59:59.000Z

156

Combustion characteristics of 24 lignite samples  

SciTech Connect (OSTI)

In this study, the combustion characteristics such as thermogravimetric analysis (TGA) and differential thermogravimetric analysis (DTGA), burning profile, ignition temperature, and peak temperature were analyzed for 24 lignite samples from different areas of Turkey. The samples were heated up to 900{sup o}C at a constant rate of 10{sup o} C/min in a 5 mL/min flow of dry air. The burning profiles of the samples studied, combined with proximate, sulfur analysis and calorimetry results, contribute to a clearer identification of lignite samples' structure and a better understanding of the coalification process. The lignite samples have been tested with particle size of 0-0.05 mm. Ignition temperatures of the samples have been determined from their burning profiles.

Sensogut, C.; Ozsen, H.; Demirbas, A. [Selcuk University, Konya (Turkey)

2008-07-01T23:59:59.000Z

157

Desulfurization of lignite using steam and air  

E-Print Network [OSTI]

with nitrogen to remove oxygen and then the drums were sealed until needed for a run. This procedure was used to prevent weathering and loss of moisture from the coal. Prior to charging, t' he lignite was sized to minus 18 mesh. The larg- er particles...DESULFURIZATION OF LIGNITE USING STEAM AND AIR A Thesis by GLENN ALLEN CARTER, JR. Submitted to the Graduate College of Texas A&M University in partial fulfillment of the degree of MASTER OF SCIENCE August 1982 Major Subject: Chemical...

Carter, Glenn Allen

1982-01-01T23:59:59.000Z

158

A Comparison of Iron and Steel Production Energy Use and Energy Intensity in China and the U.S.  

E-Print Network [OSTI]

other bituminous coal and coking coal. Small differences incoal (used as fuel) Coking coal Coke oven coke Natural gasrange for typical NCVs of coking coal of 26.6 to 29.8Mj/kg.

Hasanbeigi, Ali

2012-01-01T23:59:59.000Z

159

China Energy Primer  

E-Print Network [OSTI]

35 Table 2-17 Coking Coal Used in Coke Production (1980-Figure 2-5, Figure 2-6). Coking coal accounts for about 45%although less than 40% of coking coal is used for coking (

Ni, Chun Chun

2010-01-01T23:59:59.000Z

160

Technology for processing ammonium rhodanide of coking plants into high-purity ammonium thiocyanate and thiourea  

SciTech Connect (OSTI)

The regularities of the reversible reaction of isomerization of ammonium thiocyanate (NH{sub 4}NCS) into thiourea (NH{sub 2}){sub 2}CS, and the reverse reaction, were analyzed. An ecologically clean and highly efficient method for the extraction, purification, separation, and production of isomers from the coal byproduct ammonium thiocyanate was developed based on the measured volatilities of NH{sub 4}NCS and (NH{sub 2}){sub 2}CS.

Urakaev, F.K. [Institute of Geology & Mineral SB RAS, Novosibirsk (Russian Federation)

2009-04-15T23:59:59.000Z

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


161

Sawdust Pyrolysis and Petroleum Coke CO2 Gasification at High Heating Rates.  

E-Print Network [OSTI]

??Clean and efficient electricity can be generated using an Integrated Gasification Combined Cycle (IGCC). Although IGCC is typically used with coal, it can also be… (more)

Lewis, Aaron D.

2011-01-01T23:59:59.000Z

162

Thermal and hydraulic effects of coke deposit in hydrocarbon pyrolysis process.  

E-Print Network [OSTI]

are of interest, notably in case of regenerative methods to be applied on the SCRamjet engine [1],[2]. Some

Paris-Sud XI, Université de

163

Reconstruction of the paleoenvironments of Jameson (Strawn) Reef field, Coke County, Texas  

E-Print Network [OSTI]

strata filled depressions on the deeply eroded Ellenburger pro- viding a flat surface on which the Strawn could be deposited. Cheney and Goss (1952) classified Bendian rocks as normal marine blanket deposits. They are mainly shale and argillaceous... phreatic from the marine phreatic and is marked by brackish waters. The marine phreatic environment is characterized by rocks that have all pore space filled with normal marine water. As burial of the sediments continues, other forms of diagenesis occur...

Hopkins, Kenneth Warren

1983-01-01T23:59:59.000Z

164

Process safety management (OSHA) and process risk management (CAA) application. Application to a coke plant  

SciTech Connect (OSTI)

Risk Management Programs for Chemical Accidental Release Prevention is the name of the proposed rule for the RMP Risk Management Program. The RMP was written in response to several catastrophic releases of hazardous substances. The rule is applicable to facilities that store, process or use greater than threshold quantities of 62 listed flammable chemicals and another 100 listed toxic substances. Additionally, a Risk Management Plan is registered with the EPA, Chemical Safety and Hazardous Investigation Board, state governments and the local emergency planning commission. The Clean Air Act Amendments of 1990 (specifically Section 112r) required the EPA to develop a three phase Risk Management Plan for industry: prevention program; hazard assessment; and emergency response program. The Prevention Program closely follows the OSHA`s Process Safety Management Standard. The Hazard Assessment section requires facilities to develop plans for a worst case scenario. The Emergency Response section defines the steps the facility and each employee will take if a release occurs. This section also needs to be coordinated with the Local Emergency Planning Commission. These regulations are described using Clairton Works as an example of compliance.

Graeser, W.C.; Mentzer, W.P.

1995-12-01T23:59:59.000Z

165

The nature and formation of coke in the reaction of methanol to hydrocarbons over chabazite  

E-Print Network [OSTI]

). Reactant: methanol t-butanol 1-heotanol Reaction conditions Temp. (K) LHSV (hr ) 644 1. 0 644 1. 0 644 0. 7 Conversion (g) 1 00 100 99. 9 Hydrocarbon distribution (wt g) methane ethane ethylene propane propylene i-butane n-butane bu...

McLaughlin, Kenneth Woot

1983-01-01T23:59:59.000Z

166

Solidification/stabilization of toxic metal wastes using coke and coal combustion by-products  

SciTech Connect (OSTI)

A study has been conducted to evaluate the potential of a special rubber waste, NISCO Cyclone Ash (NCA), which contains substantial calcium oxide and calcium sulfites/sulfates for solidification/stabilization (S/S) of toxic metal wastes. The mineralogical compositions of the NCA and a class ``C`` fly ash have been characterized by X-ray diffraction (XRD). Hydrated mixtures of these wastes have been examined by XRD and found to form ettringite. Low concentrations of As (15 {micro}g ml{sup {minus}1}), Ba (500 {micro}g ml{sup {minus}1}), Pb (15 {micro}g ml{sup {minus}1}), and Zn (1,000 {micro}g ml{sup {minus}1}) were added to these hydrated mixtures and found to be successfully immobilized and solidified, as determined by the Toxicity Characteristic Leaching Procedure (TCLP). In addition, the mineralogy, chemistry and leaching characteristics of these combined waste products and their interactions with toxic metals are discussed.

Vempati, R.K.; Mollah, M.Y.A.; Chinthala, A.K.; Cocke, D.L. [Lamar Univ., Beaumont, TX (United States)] [Lamar Univ., Beaumont, TX (United States); Beeghly, J.H. [Dravo Lime, Pittsburgh, PA (United States)] [Dravo Lime, Pittsburgh, PA (United States)

1995-12-31T23:59:59.000Z

167

High temperature properties and reactivity of coal and coke for ironmaking.  

E-Print Network [OSTI]

??Rapid growth of the steel industry in coming years will be strongly dependent upon coal. Understanding of coal behavior in current or emerging ironmaking processes… (more)

Kim, Byong-Chul

2012-01-01T23:59:59.000Z

168

High ash non-coking coal preparation by tribo-electrostatic dry process.  

E-Print Network [OSTI]

??Coal is the single largest fossil fuel used world-wide and accounts for more than 60% of the total commercial energy consumed. Between 60 to 80%… (more)

Ranjan Dwari

2008-01-01T23:59:59.000Z

169

Effects of hydrogen donor additives on the coking properties of high-temperature coal extracts.  

E-Print Network [OSTI]

?? Refcoal is a carbon precursor obtained by alkali-mediated extraction of coal with aprotic solvents such as DMF. Refcoal can be converted into a graphitic… (more)

Makgato, Matlou Hector

2009-01-01T23:59:59.000Z

170

Improving the technology of creating water-coal fuel from lignites  

SciTech Connect (OSTI)

This paper describes the preparation of coal-water fuel slurries from lignite. The heat of combustion as related to the preparation of the lignite was investigated. The hydrobarothermal processing of suspensions of lignites was studied in autoclaves.

Gorlov, E.G.; Golovin, G.S.; Zotova, O.V. [Rossiiskaya Akadeiya, Nauk (Russian Federation)

1994-12-31T23:59:59.000Z

171

Preserved lignin structures in Miocene-aged lignite lithotypes, Bulgaria  

E-Print Network [OSTI]

Preserved lignin structures in Miocene-aged lignite lithotypes, Bulgaria M. Stefanova, O. Maman, B, Orleans Cedex 2, France Abstract Contents of preserved lignin structures in Miocene-aged lignite lithotypes were determined. Phenol aldehydes, ketones and acids released from lignin by CuO oxidative

Paris-Sud XI, Université de

172

Inventory of China's Energy-Related CO2 Emissions in 2008  

E-Print Network [OSTI]

from Agriculture Energy Consumption Coal Coke and Otherfrom Industry Energy Consumption Coal Coke and Otherfrom Construction Energy Consumption Coal Coke and Other

Fridley, David

2011-01-01T23:59:59.000Z

173

China Energy and Emissions Paths to 2030  

E-Print Network [OSTI]

refining, oil extraction, coking, coal mining, natural gasthe use of expensive heavy coking coal and increase theof inexpensive semi-coking coal. The ability to substitute

Fridley, David

2012-01-01T23:59:59.000Z

174

China's Coal: Demand, Constraints, and Externalities  

E-Print Network [OSTI]

19 3.4. Coking coal for iron & steels FOB export value for coking coal was relatively stables FOB export value for coking coal significantly increased

Aden, Nathaniel

2010-01-01T23:59:59.000Z

175

China Energy Databook - Rev. 4  

E-Print Network [OSTI]

generation, heating, coking and coal gas production, andgeneration, heating, coking and coal gas production, andgeneration, heating, coking and coal gas production, and

Sinton Editor, J.E.

2010-01-01T23:59:59.000Z

176

Inventory of China's Energy-Related CO2 Emissions in 2008  

E-Print Network [OSTI]

gas petroleum waxes coking coal t C/TJ other bituminous coalprocesses of coal washing, coking, petroleum refineries, gaslosses include coal washing, coking, petroleum refining, gas

Fridley, David

2011-01-01T23:59:59.000Z

177

Key China Energy Statistics 2011  

E-Print Network [OSTI]

Heating Supply Coal Washing Coking Petroleum Refineries GasPower Heating Supply Coal Washing Coking Total ConsumptionHeating Supply Coal Washing Coking Petroleum Refineries Gas

Levine, Mark

2013-01-01T23:59:59.000Z

178

Key China Energy Statistics 2012  

E-Print Network [OSTI]

Heating Supply Coal Washing Coking Petroleum Refineries GasHeating Supply Coal Washing Coking Petroleum Refineries GasRefueling in China Coal Washing Coking Petroleum Refineries

Levine, Mark

2013-01-01T23:59:59.000Z

179

China Energy Databook -- User Guide and Documentation, Version 7.0  

E-Print Network [OSTI]

years report coking and oil refining investment in a singleyears report coking and oil refining investment in a singleyears report coking and oil refining investment in a single

Fridley, Ed., David

2008-01-01T23:59:59.000Z

180

Emissions estimation for lignite-fired power plants in Turkey  

SciTech Connect (OSTI)

The major gaseous emissions (e.g. sulfur dioxide, nitrogen oxides, carbon dioxide, and carbon monoxide), some various organic emissions (e.g. benzene, toluene and xylenes) and some trace metals (e.g. arsenic, cobalt, chromium, manganese and nickel) generated from lignite-fired power plants in Turkey are estimated. The estimations are made separately for each one of the thirteen plants that produced electricity in 2007, because the lignite-fired thermal plants in Turkey are installed near the regions where the lignite is mined, and characteristics and composition of lignite used in each power plant are quite different from a region to another. Emission factors methodology is used for the estimations. The emission factors obtained from well-known literature are then modified depending on local moisture content of lignite. Emission rates and specific emissions (per MWh) of the pollutants from the plants without electrostatic precipitators and flue-gas desulfurization systems are found to be higher than emissions from the plants having electrostatic precipitators and flue -gas desulfurization systems. Finally a projection for the future emissions due to lignite-based power plants is given. Predicted demand for the increasing generation capacity based on the lignite-fired thermal power plant, from 2008 to 2017 is around 30%. 39 refs., 13 figs., 10 tabs.

Nurten Vardar; Zehra Yumurtaci [Yildiz Technical University Mechanical Engineering Faculty, Istanbul (Turkey)

2010-01-15T23:59:59.000Z

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


181

Some effects of pressure and temperature on combustion of lignite  

E-Print Network [OSTI]

SOME EFFECTS OF PRESSURE AND TEMPERATURE ON COMBUSTION OF LIGNITE A Thesis by MAX MARABLE Submitted to the Graduate College of Texas A&M University in partial fulfillment of the requirement for the degree of MASTER OF SCIENCE August 1975... Major Subject: Petroleum Engineering SOME EFFECTS OF PRESSURE AND TEMPERATURE ON COMBUSTION OF LIGNITE A Thesis by MAX MARABLE Approved as to style an ontent by: / Chairm of Committee Member Member August 1975 ABSTRACT Some Effects...

Marable, Max

1975-01-01T23:59:59.000Z

182

Desulfurization of Texas lignite using steam and air  

E-Print Network [OSTI]

OESULFURIZATION OF TEXAS LIGNITE USI, IG STEA 1 ANO AIR A Thesis by ROSERT REGINALD STONE Submitted to the Graduate College of Texas AIIN University in partial fulfillment of the requirement for the degree of , 'RASTER OF SCIENCE August 1981... Major Subject: Chemical Engineering DESULFURIZATION OF TEXAS LIGNITE USING STEAM AND AIR A Thesis by ROBERT REGINALD STONE Approved as to style and content by: Dr. . A . Bulli n ( Chai rman of Committee) R. G. Anthony (Member) J. W. J ni ngs ( ber...

Stone, Robert Reginald

1981-01-01T23:59:59.000Z

183

Hydrogeology of a reclaimed Central Texas lignite mine  

E-Print Network [OSTI]

Major Subject: Geology HYDROGEOLOGY Ol A RECLAIMED CENTRAL TEXAS LIGNITE MINE A Thesis by GAIL LOUISE PEPPER Approved as to style and content by: (Chairman of Committee) (Member) (Member) ad of partment) December 1980 ABSTRACT Hydrogeology... of a Reclaimed Central Texas Lignite bovine (December, 1980) Gail Louise Pepper, B. S. , i&onmouth College, Illinois Chairman of Advisory Committee: Dr. C. C. Nathewson The r coverv of the groundwater system and the factors affecting recharge have...

Pepper, Gail Louise

1980-01-01T23:59:59.000Z

184

China Energy Databook -- User Guide and Documentation, Version 7.0  

E-Print Network [OSTI]

2] In 1996, 1997, 1998, coking and coal numbers are combined2] In 1996, 1997, 1998, coking and coal numbers are combined1949-2006 Table 2B.7. Coking Coal Used in Coke Production,

Fridley, Ed., David

2008-01-01T23:59:59.000Z

185

PITTSBURGH REGIONAL ENVIRONMENTAL THREATS ANALYSIS  

E-Print Network [OSTI]

.. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19 Coke Oven Emissions.. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 19 Carbon Tetrachloride.. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 20 Acetaldehyde

Jiang, Huiqiang

186

E-Print Network 3.0 - australian lignite samples Sample Search...  

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

.The peat layers that formed during this period are today mined as lignite in large open-pits. During... -pit lignite mines (Lehner & Pilaar,1997) and a trenched outcrop over...

187

A Long, Contingent Path to Comparative Advantage: Industrial Policy and the Japanese Iron and Steel Industry, 1900-1973  

E-Print Network [OSTI]

Overseas Procurement of Coking Coal By the Japanese Steelendowed as Japan in coking coal and iron ore (Yonekura,

ELBAUM, BERNARD

2006-01-01T23:59:59.000Z

188

Japan's Long-term Energy Demand and Supply Scenario to 2050 - Estimation for the Potential of Massive CO2 Mitigation  

E-Print Network [OSTI]

Consumption of coking coal mainly for steelmaking will dropelectricity and town gas. Coking coal consumption mainly for

Komiyama, Ryoichi

2010-01-01T23:59:59.000Z

189

The Cylinder: Kinematics of the Nineteenth Century  

E-Print Network [OSTI]

distillation. The coking of coal as well as the productionin coal mines, in steel and paper mills, in coking plants,

Müller-Sievers, Helmut

2012-01-01T23:59:59.000Z

190

Adding coal dust to coal batch  

SciTech Connect (OSTI)

The granulometric composition of coke dust from the dry-slaking machine is determined. The influence of additions of 3-7% coke dust on the quality of industrial coking batch and the coke obtained by box coking is estimated. Adding 1% coke dust to coking batch does not markedly change the coke quality. Industrial equipment for the supply of dry-slaking dust to the batch is described.

V.S. Shved; A.V.Berezin [OAO Koks, Kemerovo (Russian Federation)

2009-05-15T23:59:59.000Z

191

Assessment of China's Energy-Saving and Emission-Reduction Accomplishments and Opportunities During the 11th Five Year Plan  

E-Print Network [OSTI]

calcium carbide, coking, cement, coal, plate glass, pulp andcarbide 2 Mt Coking 80 Mt Cement 250 Mt Coal mining (

Levine, Mark D.

2010-01-01T23:59:59.000Z

192

Vol. 60364 P. L. WALKER,JR.,AND EMILERAATS whether the swelling is of the predicted order of  

E-Print Network [OSTI]

ofpetro- leum coke bound together by a thin shell of coal tar pitch coke, which essentially consists

193

The washability of lignites for clay removal  

SciTech Connect (OSTI)

In the washability research of the Seyitomer Lignites (Kutahya-Turkey), with lower calorific value (1,863 kcal/kg) and high ash content (51.91%), by heavy medium separation, it was found out that middling clay in the coal had an effect to change the medium density. To prevent this problem, a trommel sieve with 18 and 5 mm aperture diameter was designed, and the clay in the coal was tried to be removed using it before the coal was released to heavy medium. Following that, the obtained coal in -100 + 18 mm and -18 + 5 mm fractions was subjected to sink and float test having 1.4 gcm{sup -3} and 1.7 gcm{sup -3} medium densities (-5 mm fraction will be evaluated in a separate work). Depending on the raw coal, with the floating of -100 + 18 mm and -18 + 5 mm size fraction in 1.4 gcm{sup -3} medium density, clean coal with 60.10% combustible matter recovery, 19.12% ash, and 3,150 kcal/kg was obtained. Also floating of the samples sinking in 1.4 gcm{sup -3} in the medium density (1.7 gcm{sup -3}), middling with 18.70% combustible matter recovery, 41.93% ash, 2,150 kcal/kg, and tailing having 78.31% ash were obtained.

Oteyaka, B.; Yamik, A.; Ucar, A.; Sahbaz, O.; Demir, U. [Dumlupinar University, Kutahya (Turkey). Dept. of Mining Engineering

2008-07-01T23:59:59.000Z

194

Potential Impact of the Development of Lignite Reserves on Water Resources of East Texas  

E-Print Network [OSTI]

adverse effects of lignite strip mining and lignite utilization on the hydrology and water quality of the area. Both field and desk studies were conducted to evaluate the potential impact of lignite development on water resources of the area. Field studies...

James, W. P.; Slowey, J. F.; Garret, R. L.; Ortiz, C.; Bright, J.; King, T.

195

A kinetic model for the liquefaction of Texas lignite  

E-Print Network [OSTI]

shortages in the United States has led to investigations in alternative energy sources. Of particular interest is the lignite resource in Texas which is mainly situated in the east and central regions north of the Colorado River. There is an estimated...A KINETIC MODEL FOR THE LIQUEFACTION OF TEXAS LIGNITE 4 Thesis by SANDRA KAY BALKY Submitted to the Graduate College of Texas A&M University in partial fulfillment of the requirement for the degree of MASTER OF SCIENCE y 1980 Major Subject...

Haley, Sandra Kay

1980-01-01T23:59:59.000Z

196

A novel technique for on-line coke gasification during propane steam reforming using forced CO2 cycling.  

E-Print Network [OSTI]

??Steam reforming is an important source of synthesis gas production that is used by major petrochemical processes such as ammonia, methanol and the Fisher-Tropsch process.… (more)

Alenazey, Feraih Sheradh

2011-01-01T23:59:59.000Z

197

Enhancing P-xylene selectivity during m-xylene transformation using mildly pre-coked ZSM-5 catalyst  

E-Print Network [OSTI]

catalyst S. Al-Khattaf* Department of Chemical Engineering, King Fahd University of Petroleum & Minerals for various processes, like the production of synthetic fibres and plasticizers, efforts are continually been been investigated in detail by several workers [1-12]. Modifications of ZSM-5 by various compounds have

Al-Khattaf, Sulaiman

198

Minimizing the formation of coke and methane on Co nanoparticles in steam reforming of biomass-derived oxygenates  

SciTech Connect (OSTI)

Fundamental understanding and control of chemical transformations are essential to the development of technically feasible and economically viable catalytic processes for efficient conversion of biomass to fuels and chemicals. Using an integrated experimental and theoretical approach, we report high hydrogen selectivity and catalyst durability of acetone steam reforming (ASR) on inert carbon supported Co nanoparticles. The observed catalytic performance is further elucidated on the basis of comprehensive first-principles calculations. Instead of being considered as an undesired intermediate prone for catalyst deactivation during bioethanol steam reforming (ESR), acetone is suggested as a key and desired intermediate in proposed two-stage ESR process that leads to high hydrogen selectivity and low methane formation on Co-based catalysts. The significance of the present work also sheds a light on controlling the chemical transformations of key intermediates in biomass conversion such as ketones. We gratefully acknowledge the financial support from U. S. Department of Energy (DOE), Office of Basic Energy Sciences, Division of Chemical Sciences, Geosciences, and Biosciences, and the Laboratory directed research and development (LDRD) project of Pacific Northwest National Laboratory (PNNL). Computing time was granted by the William R. Wiley Environmental Molecular Sciences Laboratory (EMSL). The EMSL is a U.S. DOE national scientific user facility located at PNNL, and sponsored by the U.S. DOE’s Office of Biological and Environmental Research.

Sun, Junming; Mei, Donghai; Karim, Ayman M.; Datye, Abhaya K.; Wang, Yong

2013-06-01T23:59:59.000Z

199

Lignites and Low Rank Coals Conference: Proceedings 2001  

SciTech Connect (OSTI)

EPRI and the Technische Vereinigung des Grosskraftswerkbetreiber (Technical Association of Large Power Plant Operators) (VGB) jointly held a Conference on Lignites and Low Rank Coals in Wiesbaden, Germany, May 16-18, 2001. These Proceedings include the plenary papers, technical session papers, and rapporteurs' summaries from the conference.

None

2002-02-01T23:59:59.000Z

200

Hydroliquefaction of Big Brown lignite in supercritical fluids  

E-Print Network [OSTI]

Big Brown lignite was liquefied in a fixed bed tube reactor. Three solvents were used in the liquefaction studies, toluene, cyclohexane and methanol. Two co-solvents, tetralin and water were used with toluene. The effects of the solvents and co...

Chen, Hui

1996-01-01T23:59:59.000Z

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


201

European Customs & Trade Welcome to the twenty-first  

E-Print Network [OSTI]

duties system. The Coal Tax will be levied on coal, cokes and lignite. It is envisaged that the duty rate on Coal in the Netherlands · East African Community (EAC) Partner States Sign Interim Framework Agreement on Coal in the Netherlands From January 1, 2008, the present Dutch Fuel Tax on coal will no longer apply

202

Characterization of Texas lignite and numerical modeling of its in-situ gasification  

E-Print Network [OSTI]

proximate analysis variable and eventually a systematic method of varying these parameters needs to be investigated before a parameter study of the influence of lignite composit1on on gas quality can be done (Russell and Wang, 1983). A characterization... compensate for part of the energy needed to vaporize the moisture in lignite, the sum of these two forms of energy accounts for only about a half of the total energy required for vaporization by a simple calculation using typical Texas lignite...

Wang, Yih-Jy

1983-01-01T23:59:59.000Z

203

An engineering geologic impact analysis of hydraulic dredging for lignite in Texas alluvial valleys  

E-Print Network [OSTI]

, and is the same site used by Cason ( 1982). These two studies exhibit that dredge mining of lignite at the Grimes County site is feasible economically and environmentally. A pilot dredge program is now needed to determine if the studies represent reality... lignite in alluvial valleys is feasible Table 1. Stratigraphic occurrence of Texas lignites (IUodified fram Cason, 1982) . North of the Colorado River OLIGOCENE CATAMOULA FORMATION South of the Colorado River Whitsett Formation Manning Formations...

Nolan, Erich Donald Luis

1985-01-01T23:59:59.000Z

204

A kinetic model for the liquefaction of lignite in a continuous stirred tank reactor  

E-Print Network [OSTI]

can be transported by pipelines or other means at greatly reduced cost. Lignite liquefaction appears especially attractive in North Dakota, where combustion of vast deposits of lignite has made the state a net exporter of electricity. This has..., and equimolar CO/H2. The lignite for this work was mined from the Beulah mine in Mercer County, North Dakota (Beulah 3). The sample was selected for its unusually high ash content, which was INPUT ALTERNATE PREHEATERS ALTERNATE REACTORS GAS ? LIOUIO...

Culpon, Douglas Holmes

1982-01-01T23:59:59.000Z

205

An investigation of changes in groundwater quality caused by in-situ gasification of East Texas lignite  

E-Print Network [OSTI]

to lignite gasification at the Hoe Creek site were determined not to be a serious groundwater quality problem, similar work needs to be done at the Rockdale site due to varying geological controls. LIGNITE Lignite is a low grade coal intermediate between...AN INVESTIGATION OF CHANGES IN GROUNDWATER QUALITY CAUSED BY IN-SITU GASIFICATION OF EAST TEXAS LIGNITE A Thesis by KIMBERLY SUE LEACH Submitted to the Graduate College of Texas AGM University in Partial fulfillment of the requirements...

Leach, Kimberly Sue

1988-01-01T23:59:59.000Z

206

The fractionation and characterization of two North American lignites  

E-Print Network [OSTI]

Assignments for the TMSI Reaction Page TI Product of the Gascoyne Bitumen LIST OF FIGURES FIGURE I, Extraction and Fractionation Scheme for the Page Gascoyne Lignite 24 2. X-Ray Diffractogram of the Low-Temperature Ash of the Demineralized Wilcox... the required data by inductively coupled argon plasma-atomic emissions spectrometry, which was essential in the completion of the thesis. Many thanks goes out to Ahmad Moini for performing the X-ray diffraction on the samples submitted. Finally, I wish...

Garcia Juan Manuel

1985-01-01T23:59:59.000Z

207

Structure parameter correlations on alkali-alcohol treated lignite  

SciTech Connect (OSTI)

The solubility of the Tuncbilek Lignite is increased up to 100%, on daf. basis, after KOH-Benz-hydrol treatment. Meanwhile its oxygen, sulphur and ash contents are decreased considerably. It has been shown that the solubility, H/C and S/C ratios, as well as the sulphur content of the coal are well correlated with the hydrogen transferred from benzhydrol, whereas the oxygen contact does not. The oxygen content correlate with the ash content. A reductive elimination mechanism is suggested for the removal of the heteroatoms, which also cause the degradation and the increase of the solubility of the coal.

Balcioglu, N.; Yilmaz, M.

1989-01-01T23:59:59.000Z

208

Investigation of the combustion characteristics of Zonguldak bituminous coal using DTA and DTG  

SciTech Connect (OSTI)

Combustion characteristics of coking, semicoking, and noncoking Turkish bituminous coal samples from Zonguldak basin were investigated applying differential thermal analysis (DTA) and differential thermogravimetry (DTG) techniques. Results were compared with that of the coke from Zonguldak bituminous coal, a Turkish lignite sample from Soma, and a Siberian bituminous coal sample. The thermal data from both techniques showed some differences depending on the proximate analyses of the samples. Noncombustible components of the volatile matter led to important changes in thermal behavior. The data front both methods were, evaluated jointly, and some thermal properties were interpreted considering these methods in a complementary combination.

Haykiri-Acma, H.; Yaman, S.; Kucukbayrak, S.; Okutan, H. [Istanbul Technical University, Istanbul (Turkey). Dept. of Chemical Engineering

2006-06-21T23:59:59.000Z

209

Microgravity exploration for a sediment-filled channel intersecting a near-surface lignite seam  

E-Print Network [OSTI]

lignite seam. A 1900 foot line running north and south was located such that 1) the south end was at the location of a core which found 8 feet of lignite at a depth of 60 feet and 2) the north end was at the location of a core which found no nea... of anomalies to the full extent possible with the meter. Selection of the Station Locations A 1900 foot line running north and south was located such that 1) the south end was at the location of a core which found 8 feet of lignite at a depth of 60 feet. 2...

May, Clifford John

1984-01-01T23:59:59.000Z

210

Evaluation of the Impact of Texas Lignite Development on Texas Water Resources  

E-Print Network [OSTI]

Fuel shortages and resultant rising fuel costs as well as federal policies prompting energy independence have served to encourage power companies to exploit available lignite deposits of the western states as a viable fuel source. Large reserves...

Mathewson, C. C.; Cason, C. L.

211

DOE-Sponsored Field Test Finds Potential for Permanent Storage of CO2 in Lignite Seams  

Broader source: Energy.gov [DOE]

A field test sponsored by the U.S. Department of Energy has demonstrated that opportunities to permanently store carbon in unmineable seams of lignite may be more widespread than previously documented.

212

Production of Medium BTU Gas by In Situ Gasification of Texas Lignite  

E-Print Network [OSTI]

The necessity of providing clean, combustible fuels for use in Gulf Coast industries is well established; one possible source of such a fuel is to perform in situ gasification of Texas lignite which lies below stripping depths. If oxygen (rather...

Edgar, T. F.

1979-01-01T23:59:59.000Z

213

Water table recovery in a reclaimed surface lignite mine, Grimes County, Texas  

E-Print Network [OSTI]

Water table recovery in four reclaimed mine blocks containing replaced overburden has been monitored at Gibbons Creek Lignite Mine in Grimes County, Texas since 1986. Recovery analysis was conducted based on data recorded at 27 wells installed...

Peace, Kelley H.

1995-01-01T23:59:59.000Z

214

Reclamation planning and operation at the Mae Moh Lignite Mine, Thailand  

SciTech Connect (OSTI)

The Mae Moh Mine is a large open cut lignite mine situated in Northern Thailand. The mine produces lignite for coal fired power stations located adjacent to the mine. Current mine production is approximately 9 Mtpa providing lignite to eight power stations with a total output of 1,125 MW. The power development plan for Mae Moh provides for 19 power stations by the year 1999 which will require lignite production to be increased to 30.5 Mtpa and overburden will be mined at a rate approaching 300 Mtpa. Environmental management and reclamation planning at Mae Moh are major issues due to water quality impact and land use conflicts. This paper presents the key elements of the reclamation master plan and works strategy for progressive reclamation and water pollution control.

Miller, S.D. [Stuart D. Miller & Associates, Balmain (Australia); Teparat, C. [Electricity Generating Authority of Thailand, Mae Moh (Thailand)

1990-12-31T23:59:59.000Z

215

Molten alkali-alcohol and molten alkali treatment of lignite; A comparative study  

SciTech Connect (OSTI)

The solubility of the Tun cedilla c bilek lignite is increased up to 100% on daf basis, after molten alkali-benzhydrol treatment. Meanwhile its oxygen, sulphur and ash-content are decreased considerably. Similar results are also obtained by simple molten alkali treatment of lignite, although the oxygen content was increased in the product. A reductive cleavage mechanism for the former but an oxydative cleavage mechanism for the latter process are suggested.

Balcioglu, N. (Dept. of Chemistry, Hacettepe Univ., Ankara (TR)); Yilmaz, M. (Dept. of Chemistry, Selcuk Univ., Konya (TR))

1990-01-01T23:59:59.000Z

216

Ground-water hydrogeology and geochemistry of a reclaimed lignite surface mine  

E-Print Network [OSTI]

GROUND-WATER HYDROGEOLOGY AND GEOCHEMISTRY OF A RECLAIMED LIGNITE SURFACE MINE A Thesis by CLIFFORD RALPH POLLOCK Submitted to the Graduate College of Texas A&M University in partial fulfillment of the requirement for the degree of MASTER... OF SCIENCE August 1982 Major Subject: Geology GROUND-WATER HYDROGEOLOGY AND GEOCHEMISTRY OF A RECLAIMED LIGNITE SURFACE MINE A Thesis by CLIFFORD RALPH POLLOCK Approved as to sty1e and content by: (Chairman of Committee) ember) (Member (Member) F...

Pollock, Clifford Ralph

1982-01-01T23:59:59.000Z

217

Development and evaluation of two reactor designs for desulfurization of Texas lignites  

E-Print Network [OSTI]

exhibited can be given at this time, but this behavior may be indicative of transformations of inorganic matter, changes in the forms of sulfur present in the lignite, and the overall composition. The results of this test series show a need for further...DEVELOPMENT AND EVALUATION OF TWO REACTOR DESIGNS FOR DESULFURIZATION OF TEXAS LIGNITES A Thesis by STANLEY DUANE MERRITT Submitted to the Office of Graduate Studies of Texas A&M University in partial fulfillment of the requirements...

Merritt, Stanley Duane

1991-01-01T23:59:59.000Z

218

Development of a thermobalance and analysis of lignites by thermogravimetric and statistical methods  

E-Print Network [OSTI]

coal or lignite is its calorific values, Q, the heat it produces when combusted. A simple, inexpensive, and rapid method for accurately predicting Q is needed because the pres- ently available methods are complicated, expensive, and take a great...DEVELOPMENT OF A THERMOBALANCE AND ANALYSIS OF LIGNITES BY THERMOGRAVIMETRIC AND STATISTICAL METHODS A Thesis by JAMES ALLEN PERGUSON Submitted to the Graduate College of Texas ASM University in partial fulfillment of the requirements...

Ferguson, James Allen

1984-01-01T23:59:59.000Z

219

Geology and engineering geology of a Wilcox lignite deposit in northeastern Rusk County, Texas  

E-Print Network [OSTI]

GEOLOGY AND ENGINEERING GEOLOGY OF A WILCOX LIGNITE DEPOSIT IN NORTHEASTERN RUSK COUNTY, TEXAS A Thesis by William F. Cole Submitted to the Graduate College of Texas A&M University in partial fulfillment of the requirement for the degree...) (Member) (Member) (Member) (Member) ad of Department) August 1980 ABSTRACT Geology and Engineering Geology of a Wilcox Lignite Deposit in Northeastern Rusk County, Texas (August, 1980) William 7. Cole, B. S. , Texas ASM University Chairman...

Cole, William F.

1980-01-01T23:59:59.000Z

220

Correlation of stratigraphy with revegetation conditions at the Gibbons Creek Lignite Mine, Grimes County, Texas  

E-Print Network [OSTI]

CORRELATION OF STRATIGRAPHY WITH REVEGETATION CONDITIONS AT THE GIBBONS CREEK LIGNITE MINE, GRIMES COUNTY, TEXAS A Thesis by LAURENCE D. PARISOT Submitted to the Office of Graduate Studies of Texas ARM University in partial fulfillment... of the requirements for the degree of MASTER OF SCIENCE December 1991 Major Subject: Geology CORRELATION OF STRATIGRAPHY WITH REVEGETATION CONDITIONS AT THE GIBBONS CREEK LIGNITE MINE, GRIMES COUNTY, TEXAS A Thesis by LAURENCE D. PARISOT ; Approved...

Parisot, Laurence D.

1991-01-01T23:59:59.000Z

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


221

Hydrogeology of a proposed surface lignite mine, southwestern Harrison County, Texas  

E-Print Network [OSTI]

HYDROGEOLOGY OF A PROPOSED SURFACE LIGNITE MINE, SOUTHWESTERN HARRISON COUNTY, TEXAS A Thesis by ROBERT JOHN CHARLES Submitted to the Graduate College of Texas A&M University in partial fulfillment of the requirement for the degree of MASTER... OF SCIENCE May l979 Major Subject: Geology HYDROGEOLOGY OF A PROPOSED SURFACE LIGNITE N1NE, SOUTHNESTERN HARRISON COUNTY, TEXAS A Thesis by ROBERT JOHN CHARLES Approved as to style and content by: (Chairman of Cossdttee) (H d of Department) (Nesber...

Charles, Robert John

1979-01-01T23:59:59.000Z

222

Engineering geologic feasibility of lignite mining in alluvial valleys by hydraulic dredging methods  

E-Print Network [OSTI]

. . . . . . . . . . . . . . . . . . . . . . . . . . 135 64 Lignite volume calculation blocks, test mine site, Grimes County, Texas 166 INTRODUCTION Federal policies emphasizing the need for energy independence in conjunction with continuously escalating costs in all phases of U. S. oil and gas... lignites. North of the Colorado South of the Colorado River River OLIGOCENE CATAHQULA FORMATION Whitsett Formation EQCENE JACXSQN GROUp Manning Formation* Wellborn Formation lower Jackson* Caddell Formation EOCENE CLAIBORNE GROUP Yegua Formation...

Cason, Cynthia Lynn

1982-01-01T23:59:59.000Z

223

Characterizing a lignite formation before and after an underground coal gasification experiment  

E-Print Network [OSTI]

water. To answer questions relating to the amount of lignite gasified, subsidence, ground water pollution problems and to obtain a better understanding of the process itself, work is needed to define the size, shape and orientation of the cavity...CHARACTERIZING A LIGNITE FORMATION BEFORE AND AFTER AN UNDERGROUND COAL GASIFICATION EXPERIMENT A Thesis by USMAN AHMED Submitted to the Graduate College of Texas A&M University in partial fulfillment of the requirement for the degree...

Ahmed, Usman

1981-01-01T23:59:59.000Z

224

JV Task - 129 Advanced Conversion Test - Bulgarian Lignite  

SciTech Connect (OSTI)

The objectives of this Energy & Environmental Research Center (EERC) project were to evaluate Bulgarian lignite performance under both fluid-bed combustion and gasification conditions and provide a recommendation as to which technology would be the most technically feasible for the particular feedstock and also identify any potential operating issues (such as bed agglomeration, etc.) that may limit the applicability of a potential coal conversion technology. Gasification tests were run at the EERC in the 100-400-kg/hr transport reactor development unit (TRDU) on a 50-tonne sample of lignite supplied by the Bulgarian Lignite Power Project. The quality of the test sample was inferior to any coal previously tested in this unit, containing 50% ash at 26.7% moisture and having a higher heating value of 5043 kJ/kg after partial drying in preparation for testing. The tentative conclusion reached on the basis of tests in the TRDU is that oxygen-blown gasification of this high-ash Bulgarian lignite sample using the Kellogg, Brown, and Root (KBR) transport gasifier technology would not provide a syngas suitable for directly firing a gas turbine. After correcting for test conditions specific to the pilot-scale TRDU, including an unavoidably high heat loss and nitrogen dilution by transport air, the best-case heating value for oxygen-blown operation was estimated to be 3316 kJ/m{sup 3} for a commercial KRB transport gasifier. This heating value is about 80% of the minimum required for firing a gas turbine. Removing 50% of the carbon dioxide from the syngas would increase the heating value to 4583 kJ/m{sup 3}, i.e., to about 110% of the minimum requirement, and 95% removal would provide a heating value of 7080 kJ/m{sup 3}. Supplemental firing of natural gas would also allow the integrated gasification combined cycle (IGCC) technology to be utilized without having to remove CO{sub 2}. If removal of all nitrogen from the input gas streams such as the coal transport air were achieved, a heating value very close to that needed to fire a gas turbine would be achieved; however, some operational issues associated with utilizing recycled syngas or carbon dioxide as the transport gas would also have to be resolved. Use of a coal with a quality similar to the core samples provided earlier in the test program would also improve the gasifier performance. Low cold-gas efficiencies on the order of 20% calculated for oxygen-blown tests resulted in part from specific difficulties experienced in trying to operate the pilot-scale TRDU on this very high-ash lignite. These low levels of efficiency are not believed to be representative of what could be achieved in a commercial KRB transport gasifier. Combustion tests were also performed in the EERC's circulating fluidized-bed combustor (CFBC) to evaluate this alternative technology for use of this fuel. It was demonstrated that this fuel does have sufficient heating value to sustain combustion, even without coal drying; however, it will be challenging to economically extract sufficient energy for the generation of steam for electrical generation. The boiler efficiency for the dried coal was 73.5% at 85% sulfur capture (21.4% moisture) compared to 55.3% at 85% sulfur capture (40% moisture). Improved boiler efficiencies for this coal will be possible operating a system more specifically designed to maximize heat extraction from the ash streams for this high-ash fuel. Drying of the coal to approximately 25% moisture probably would be recommended for either power system. Fuel moisture also has a large impact on fuel feedability. Pressurized gasifiers generally like drier fuels than systems operating at ambient pressures. The commercially recommended feedstock moisture for a pressurized transport reactor gasifier is 25% moisture. Maximum moisture content for a CFB system could be approximately 40% moisture as has been demonstrated on the Alstom CFB operating on Mississippi lignite. A preliminary economic evaluation for CO{sub 2} was performed on the alternatives of (1) precombustion separation of CO{sub 2} in

Michael Swanson; Everett Sondreal; Daniel Laudal; Douglas Hajicek; Ann Henderson; Brandon Pavlish

2009-03-27T23:59:59.000Z

225

Strategies for Low Carbon Growth In India: Industry and Non Residential Sectors  

E-Print Network [OSTI]

of medium / poor coking coals (i.e. Partial Briquetting andNevertheless, the Indian non-coking coals, suitable for SSI,blast furnaces require coking coal that is mostly imported.

Sathaye, Jayant

2011-01-01T23:59:59.000Z

226

REGULATION AND SYSTEM INTERDEPENDENCE: EFFECTS ON THE SITING OF CALIFORNIA ELECTRICAL ENERGY FACILITIES  

E-Print Network [OSTI]

p. 297. Allan Rodgers, "Coking Coal Supply: Its Role in theChanges in the Supply of Coking Coal in Belgium since 1945,"Changes in the Supply of Coking Coal in Belgiumsince 1945,"

Kooser, J.C.

2013-01-01T23:59:59.000Z

227

Energy and Greenhouse Gas Emissions in China: Growth, Transition, and Institutional Change  

E-Print Network [OSTI]

coal mining, petroleum extraction and refining, coking, andCoal Mining and Dressing Petroleum and Natural Gas Extraction Petroleum Processing, Coking andCoal Mining and Dressing Petroleum and Natural Gas Extraction Petroleum Processing, Coking and

Kahrl, Fredrich James

2011-01-01T23:59:59.000Z

228

China's Energy and Carbon Emissions Outlook to 2050  

E-Print Network [OSTI]

power generation and coal input to coking is not included inTransformation Coking Generation CIS Total Coal Demand (Coking Generation AIS Figure 44 CIS and AIS Coal Demand by

Zhou, Nan

2011-01-01T23:59:59.000Z

229

ME 4171 --HOMEWORK: LIFE-CYCLE DESIGN WHEEL SYNOPSIS OF ASSIGNMENT  

E-Print Network [OSTI]

are Cokes in 12-pack cans or in 6-pack plastic bottles. Each have multiple materials (the Coke, the container, the cap on the plastic bottles, the package to hold the Cokes) and most of us are familiar

230

E-Print Network 3.0 - air blast circuit Sample Search Results  

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

the conversion of an important share of the coal to coke. The demands... consists of coking gas and coal tar. Coke is essential in the blast furnace. Some ... Source:...

231

GEORGEBUSHDR. NRD(FM2154)  

E-Print Network [OSTI]

Green COKE GEORGEBUSHDR. BIZZELL OLDMAINDR. W LAMAR JOEROUTT HOUSTON NRD(FM2154) LEWIS LUBBOCK E LAMAR MOSHER CENTRAL LAMAR NAGLE COKE THROCKMORTON COKE THROCKMORTON STON SPENCE WELLBORNRD(FM GEORGE BUSH DR. R U SSEL

Behmer, Spencer T.

232

Development and evaluation of a lignite-stillage carrier system for application and study of biological control agents  

E-Print Network [OSTI]

broth (38, 47, 60). New carrier component combina- tions need to be devised to provide an effective, low cost method of applying biocontro 1 agents to the soil. The purpose of this resear ch includes: ). ) determining the potential of lignite for use... means for reducing the carrier volumes needed by concentrating the nutrient substrate onto granules. Sporu 1ation was significantly greater on doubly amended lignite compared to singly amended lignite. Determinants of a successful two com onent...

Jones, Richard Worth

1983-01-01T23:59:59.000Z

233

How Godzilla Ate Pittsburgh: The Long Rise of the Japanese Iron and Steel Industry, 1900–1973  

E-Print Network [OSTI]

poorly endowed as Japan in coking coal and iron ore (WarrenYawata of iron ore for coking coal and the progressive in-

Bernard Elbaum

2007-01-01T23:59:59.000Z

234

Development of Bottom-up Representation of Industrial Energy Efficiency Technologies in Integrated Assessment Models for the Iron and Steel Sector  

E-Print Network [OSTI]

around 8-9% for good coking coal (IISI, 1982). Dryingof steam coal and coking coal to be $15/t (IEA, 1995). This

Xu, T.T.

2011-01-01T23:59:59.000Z

235

India Energy Outlook: End Use Demand in India to 2020  

E-Print Network [OSTI]

5% of its reserve is coking coal used by the steel industry.imports around 70% of coking coal annually. More recently,

de la Rue du Can, Stephane

2009-01-01T23:59:59.000Z

236

DISTRIBUTED ENERGY SYSTEMS IN CALIFORNIA'S FUTURE: A PRELIMINARY REPORT, VOLUME I  

E-Print Network [OSTI]

d The predominant use is coking coal for steel production.a,metallurgical grade coal for coking use in steel making (

Authors, Various

2010-01-01T23:59:59.000Z

237

National Level Co-Control Study of the Targets for Energy Intensity and Sulfur Dioxide in China  

E-Print Network [OSTI]

coal Gas coal Fat coal Coking coal Lean coal Meagre coalCoal used for coking Natural Gas Coal used as fuel Source:

Zhou, Nan

2013-01-01T23:59:59.000Z

238

To place your meal order please dial MEAL (ext. 6325)  

E-Print Network [OSTI]

, Lactaid, Soymilk : Coke, Diet Coke, Sprite, Diet Sprite, Gingerale, Juice Apple, Cranberry, Orange Sour Cream Parmesan Cheese Cranberry Sauce The goal of our Food and Nutrition staff

Oliver, Douglas L.

239

Industrial Sector Energy Conservation Programs in the People's Republic of China during the Seventh Five-Year Plan (1986-1990)  

E-Print Network [OSTI]

in coking, sterling, ironmaking, and open hearth processes,injections for coke in ironmaking is a common practiceinjection methods i n ironmaking. Data from the Anshan Iron

Zhiping, L.

2010-01-01T23:59:59.000Z

240

Desulfurization of organic sulfur from lignite by an electron transfer process  

SciTech Connect (OSTI)

This study is an attempt to desulfurize organic sulfur from lignite samples with ferrocyanide ion as the electron transferring agent. Effect of temperature, particle size and concentration of ferrocyanide ion on desulfurization from the lignite samples has been investigated. The desulfurization process has been found to be continuous and gradually increases with increase of temperature from 298 to 368 K. The particle size has no significant impact on sulfur removal from the lignite samples. Particle size has no profound impact on the amount of sulfur removal. The desulfurization reaction has been found to be dependent on the concentration of potassium ferrocyanide. Gradual increase in the concentration of potassium ferrocyanide raised the magnitude of desulfurization, but at a higher concentration, the variation is not significant.

Demirbas, A. [Selcuk University, Konya (Turkey). Dept. for Chemical Engineering

2006-10-15T23:59:59.000Z

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


241

Innovative coke oven gas cleaning system for retrofit applications: Environmental Monitoring Program. Baseline sampling program report: Volume 2, Appendix sections 1--7  

SciTech Connect (OSTI)

This report contains no text. It consist entirely of results monitoring stack opacity, benzene surveys, chemical effluent in wastewater, etc.

Stuart, L.M.

1994-05-27T23:59:59.000Z

242

Evaluation of co-cokes from bituminous coal with vacuum resid or decant oil, and evaluation of anthracites, as precursors to graphite.  

E-Print Network [OSTI]

??Graphite is utilized as a neutron moderator and structural component in some nuclear reactor designs. During the reactor operaction the structure of graphite is damaged… (more)

Nyathi, Mhlwazi

2011-01-01T23:59:59.000Z

243

,,,,,,"Coal Components",,,"Coke",,,"Electricity Components",,,,,,,,,,,,,,"Natural Gas Components",,,"Steam Components"  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia, Virginia:FAQProved Reserves, Reserves Changes, and Production" ,"Click worksheet nameNumber of Relative Standard

244

,,,,,,"Coal Components",,,"Coke",,,"Electricity Components",,,,,,,,,,,,,,"Natural Gas Components",,,"Steam Components"  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia, Virginia:FAQProved Reserves, Reserves Changes, and Production" ,"Click worksheet nameNumber of Relative

245

Comparative radiocarbon dating of lignite, pottery, and charcoal samples from Babeldaob Island, Republic of Palau  

SciTech Connect (OSTI)

It is difficult to construct archaeological chronologies for Babeldaob, the main island of Palau (western Micronesia), because the saprolitic clays of the dominant terraced-hill sites and associated ceramic sherds often contain old carbon that originated in lignites. This has implications, as well, for chronologies of sedimentary sequences. Comparative analysis of the dating problem using lignite, pottery, and charcoal samples indicates that, in fact, there are both old and young sources of potential contamination. It is concluded that radiocarbon samples from Babeldaob need to be tested for appropriate carbon content rather than relying solely upon material identification.

Anderson, A.; Chappell, J.; Clark, G.; Phear, S. [Australian National University, Canberra, ACT (Australia)

2005-07-01T23:59:59.000Z

246

Effects of hydrogeology on lignite recovery in the Manning Formation, Grimes County, Texas  

E-Print Network [OSTI]

EFFECTS OF HyDROGEOLOGY ON LIGNITE RECOVER IN THE IVJBiING FOiVcATION, GR MES COU!!a I, TEXAS A Thesis IZSIIE NARX LEUITAN Su'omitteu to ' he Graduate ColleSe of Texas A@I1 University in parti ! t'ulfill!n nt cf the requiremert for the degree... of !IASTER OF SCIENCE Decesher 1976 Najor Suhject: Geolody EFFECTS OF HYDROGEOLOGY ON LIGNITE RECOVERY IN THE MAIDNING FORMATION, GRIMES COUNTY, TEXAS A Thesis LESLIE MARK IZVITAN Approved as to style and content by: (Ctwirman of Committee Head...

Levitan, Leslie Mark

1976-01-01T23:59:59.000Z

247

Variation in physical rock properties determined from sonic logs at a South Texas lignite mine  

E-Print Network [OSTI]

or underburden units which were identified as potential problem units. S1gn1ficance of Study In the planning and design of a Gulf Coast lignite mi ne, a need exists to deter nine the variability of phys1cal rock properties within strati graphic units...VARIATION IN PHVSICAL ROCK PROPERTIES DETERMINED FROM SONIC LOGS AT A SOUTH TEXAS LIGNITE MINE A Thesis by KERRV OON CATO Submitted to the Graduate College of Texas A&M University in Partial fulfillment of the requirements for the degree...

Cato, Kerry Don

1985-01-01T23:59:59.000Z

248

A solvent study of the direct liquefaction of Big Brown lignite  

E-Print Network [OSTI]

of an experiment. A commercially obtained anthracene oil spiked with tetralin was used in conjunction with a lignite obtained from a mine located near Beulah, North Dakota. Knudson found that the primary role of the gas phase in low-rank coal liquefaction appears... by the University of North Dakota Energy Research Center (UNDERC) and were stored in polyethylene bags inside 5 gallon containers. The particle size distribution of the lignite was such that all of it was below 246 microns and 90% was below 74 microns. Proximate...

Helton, Terry Eugene

1986-01-01T23:59:59.000Z

249

Cofiring lignite with hazelnut shell and cotton residue in a pilot-scale fluidized bed combustor  

SciTech Connect (OSTI)

In this study, cofiring of high ash and sulfur content lignite with hazelnut shell and cotton residue was investigated in 0.3 MWt METU Atmospheric Bubbling Fluidized Bed Combustion (ABFBC) Test Rig in terms of combustion and emission performance of different fuel blends. The results reveal that cofiring of hazelnut shell and cotton residue with lignite increases the combustion efficiency and freeboard temperatures compared to those of lignite firing with limestone addition only. CO{sub 2} emission is not found sensitive to increase in hazelnut shell and cotton residue share in fuel blend. Cofiring lowers SO{sub 2} emissions considerably. Cofiring of hazelnut shell reduces NO and N{sub 2}O emissions; on the contrary, cofiring cotton residue results in higher NO and N{sub 2}O emissions. Higher share of biomass in the fuel blend results in coarser cyclone ash particles. Hazelnut shell and cotton residue can be cofired with high ash and sulfur-containing lignite without operational problems. 32 refs., 12 figs., 11 tabs.

Zuhal Gogebakan; Nevin Selcuk [Middle East Technical University, Ankara (Turkey). Department of Chemical Engineering

2008-05-15T23:59:59.000Z

250

Soil microbial biomass: an estimator of soil development in reclaimed lignite mine soil  

E-Print Network [OSTI]

A two-year study was conducted at the Big Brown lignite mine in Fairfield, Texas, to determine the rate and extent of recovery of the soil microbial biomass (SMB) in mixed overburden. The relationships between SMB carbon (SMBC), basal respiration...

Swanson, Eric Scott

1996-01-01T23:59:59.000Z

251

Prediction of postmine ground-water quality at a Texas surface lignite mine  

E-Print Network [OSTI]

. The predominant factors which affect spoil water quality have not been completely identified to date. Therefore, the Gibbons Creek Lignite Mine in Grimes County, Texas was chosen as a test site to evaluate the potential factors that can affect the geochemical...

Wise, Clifton Farrell

1995-01-01T23:59:59.000Z

252

Stratigraphy and environment of deposition of the San Miguel lignite deposit northern McMullen and southeastern Atascosa counties, Texas  

E-Print Network [OSTI]

deposits. Coastal swamp deposits occur within the lignite interval, a zone of lignite and clay of 3. 7 m (12 ft) ave age thickness. The 1'g. . ite interval has an overall strike-trend with local dip-trending segments. The lignite represents accumulation...). . . . . . . . . ~ ~ ~ 26 12 ~2 f ' ' 2~2'6' 2 ~l f* MK-26, 14. 2 m (46. 75 ft) . 26 13 Regional stratigraphic correlation of the upper and middle Eocene of the Gulf Coast. 28 Electric log correlations in Atascosa and Live Oak counties of Texas. 29 15 Interpretation...

Snedden, John William

1979-01-01T23:59:59.000Z

253

Department of Ecosystem Science & SOIL RESEARCH CLUSTER LABORATORY  

E-Print Network [OSTI]

, Organometallics, Gasoline and fuels, Coal and coke, Graphite and carbides, Metals and alloys · Operator: Julie

Boyer, Elizabeth W.

254

A Online appendix to accompany "A Spatial Approach to Energy Economics"  

E-Print Network [OSTI]

of the Standard International Trade Classification, Rev. 4 as: coal, coke and briquettes; petroleum, petroleum

Calgary, University of

255

Description: Start | Grid View | Browse by Day OR Group/Topical | Author Index | Keyword Index | Personal Scheduler  

E-Print Network [OSTI]

Knowlton (172b) COAL Direct Chemical Looping Process: Metallurigical Coke and PRB COAL Conversions L. - S

Gilchrist, James F.

256

Production of a nitrogeneous humic fertilizer by the oxidation-ammoniation of lignite  

SciTech Connect (OSTI)

Two lignite samples were oxidised with HNO/sub 3/ (20% wt) at 75 C and treated afterwards with NH/sub 3/ in a fluidised-bed reactor in a temperature range 100-375 C. The effects of temperature, NH/sub 3/ flow rate, and reaction time on the total N/sub 2/ content of the product are reported. The product contained 7-13% wt of total N/sub 2/ which increased as the ammoniation temperature increased. Soil nitrification measurements of the N/sub 2/-enriched lignites showed that the maximum conversion to nitrates and rate of nitrification are exhibited by the product obtained at the lowest ammoniation temperature, i.e. 100 C. Maximum conversion to nitrates at that temperature was 45%, which compares well with similar products such as ammoniated peat (35%) and ammonium nitrohumates (45%).

Coca, J.

1984-12-01T23:59:59.000Z

257

Detailed mining study executive summary: Saba Yoi lignite deposit. Export trade information  

SciTech Connect (OSTI)

The study, conducted by John T. Boyd Company, was funded by the U.S. Trade and Development Agency on behalf of the Electricity Generating Authority of Thailand. The report shows the results of a feasibility study conducted for the development of the Saba Yoi Coal Mine. The study gives an economic assessment of the project, as well as capital costs for mining and materials. This volume contains the Executive Summary and is divided into the following sections: (1) Project Setting; (2) Land Issues; (3) Geological Setting; (4) Lignite Resource Estimate; (5) Mine Design Parameters; (6) Lignite Reserve Estimate; (7) Annual Mine Output; (8) Phase 2: Conceptual Mining Systems Comparison; (9) Phase 3: Mining Plan Economic Assessment; (10) Recommendations; (11) Conclusion.

NONE

1994-07-01T23:59:59.000Z

258

Potential for selenium migration at a lignite power plant solid waste disposal facility  

E-Print Network [OSTI]

. All groundwater that recharges on the disposal site is slightly saline and flows east, probably discharging into the Gibbons Creek Reservoir. Selenium, arsenic, boron, iron, manganese, and sulfate in the lignite waste effluent exceed either EPA... ( 1975) drinking water standards or EPA (1973) recommended livestock water standards. Since the natural groundwater contains higher concentrations of selenium, iron, manganese, and sulfate than the waste effluent, only arsenic and boron should...

Hall, Steven Douglas

1986-01-01T23:59:59.000Z

259

Advanced power assessment for Czech lignite. Task 3.6, Volume 1  

SciTech Connect (OSTI)

The US has invested heavily in research, development, and demonstration of efficient and environmentally acceptable technologies for the use of coal. The US has the opportunity to use its leadership position to market a range of advanced coal-based technologies internationally. For example, coal mining output in the Czech Republic has been decreasing. This decrease in demand can be attributed mainly to the changing structure of the Czech economy and to environmental constraints. The continued production of energy from indigenous brown coals is a major concern for the Czech Republic. The strong desire to continue to use this resource is a challenge. The Energy and Environmental Research Center undertook two major efforts recently. One effort involved an assessment of opportunities for commercialization of US coal technologies in the Czech Republic. This report is the result of that effort. The technology assessment focused on the utilization of Czech brown coals. These coals are high in ash and sulfur, and the information presented in this report focuses on the utilization of these brown coals in an economically and environmentally friendly manner. Sections 3--5 present options for utilizing the as-mined coal, while Sections 6 and 7 present options for upgrading and generating alternative uses for the lignite. Contents include Czech Republic national energy perspectives; powering; emissions control; advanced power generation systems; assessment of lignite-upgrading technologies; and alternative markets for lignite.

Sondreal, E.A.; Mann, M.D.; Weber, G.W.; Young, B.C.

1995-12-01T23:59:59.000Z

260

Investigation of lignite and firewood co-combustion in a furnace for tobacco curing application  

SciTech Connect (OSTI)

Co-combustion of lignite and firewood was investigated for an application in tobacco curing industry in Northern Thailand. Extensive experiments have been carried out in a newly developed furnace suitable for small curing unit, in place of locally made furnace. The aim of this investigation is to evaluate the performance of the combustion chamber in the required thermal output range for tobacco curing and to examine the influence of fuel feed rate, fuel mixture ratio and air staging on the combustion and emission characteristics of the furnace during steady state operation. Their effects are characterized in terms of the observed variations of temperature distributions, emissions of CO, SO{sub 2}, CO{sub 2}, O{sub 2} and combustion efficiency. Co-firing of firewood and lignite has been found to exhibit acceptable temperature distribution, high combustion efficiency and low emissions over a wide thermal output span. Stable operation at low (50 kW) and high (150 kW) thermal output was achieved with average CO and SO{sub 2} content in flue gas typically below 1400 and 100 ppm, respectively. Under the conditions considered, it was showed that the fuel feed rate had greater influence on combustion and emissions than firewood and lignite mixture ratio and air staging.

Nakorn Tippayawong; Chutchawan Tantakitti; Satis Thavornun

2006-07-01T23:59:59.000Z

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


261

Enhancing Carbon Reactivity in Mercury Control in Lignite-Fired Systems  

SciTech Connect (OSTI)

This project was awarded through the U.S. Department of Energy (DOE) National Energy Technology Laboratory Program Solicitation DE-PS26-03NT41718-01. The Energy & Environmental Research Center (EERC) led a consortium-based effort to resolve mercury (Hg) control issues facing the lignite industry. The EERC team-the Electric Power Research Institute (EPRI); the URS Corporation; the Babcock & Wilcox Company; ADA-ES; Apogee; Basin Electric Power Cooperative; Otter Tail Power Company; Great River Energy; Texas Utilities; Montana-Dakota Utilities Co.; Minnkota Power Cooperative, Inc.; BNI Coal Ltd.; Dakota Westmoreland Corporation; the North American Coal Corporation; SaskPower; and the North Dakota Industrial Commission-demonstrated technologies that substantially enhanced the effectiveness of carbon sorbents to remove Hg from western fuel combustion gases and achieve a high level ({ge} 55% Hg removal) of cost-effective control. The results of this effort are applicable to virtually all utilities burning lignite and subbituminous coals in the United States and Canada. The enhancement processes were previously proven in pilot-scale and limited full-scale tests. Additional optimization testing continues on these enhancements. These four units included three lignite-fired units: Leland Olds Station Unit 1 (LOS1) and Stanton Station Unit 10 (SS10) near Stanton and Antelope Valley Station Unit 1 (AVS1) near Beulah and a subbituminous Powder River Basin (PRB)-fired unit: Stanton Station Unit 1 (SS1). This project was one of three conducted by the consortium under the DOE mercury program to systematically test Hg control technologies available for utilities burning lignite. The overall objective of the three projects was to field-test and verify options that may be applied cost-effectively by the lignite industry to reduce Hg emissions. The EERC, URS, and other team members tested sorbent injection technologies for plants equipped with electrostatic precipitators (ESPs) and spray dryer absorbers combined with fabric filters (SDAs-FFs). The work focused on technology commercialization by involving industry and emphasizing the communication of results to vendors and utilities throughout the project.

Chad Wocken; Michael Holmes; John Pavlish; Jeffrey Thompson; Katie Brandt; Brandon Pavlish; Dennis Laudal; Kevin Galbreath; Michelle Olderbak

2008-06-30T23:59:59.000Z

262

Plant mixtures and monocultures on topsoiled and nontopsoiled lignite spoil in the Post Oak Savannah of Texas  

E-Print Network [OSTI]

PLANT MIXTURES AND MONOCULTURES ON TOPSOILED AND NONTOPSOILED LIGNITE SPOIL IN THE POST OAK SAVANNAH OF TEXAS A Thesis KEVIN VAN HOOK Submitted to the Graduate College of Texas ASM University in partial fulfillment of the requirements... for the degree of MASTER OF SCIENCE August 1984 Major Subject: Range Science PLANT MIXTURES AND MONOCULTURES OiN TOPSOILED AND NONTOPSOILED LIGNITE SPOIL IiN THE POST OAK SAVANNAH OF TEXAS A Thesis by KEVIN VAN HOOK Approved as to style and content by...

Van Hook, Kevin

1984-01-01T23:59:59.000Z

263

Development and chemical quality of a ground-water system in cast overburden as the Gibbons Creek Lignite Mine  

E-Print Network [OSTI]

-water conditions which develop in response to surface mining. TMPA has supported research at the Gibbons Creek Lignite Mine in order to meet the needs of mine develop- ment and permitting, Most of the data on ground-water conditions 1n reclaimed spoil has been... on the west by the Navasota River, on the south by Gibbons Creek, and on the north by State Highway 30 (Figure 1). This area includes the Gibbons Creek Steam Electric Station. Lignite is extracted from two pits within the permit boundary, termed the A...

Borbely, Evelyn Susanna

1988-01-01T23:59:59.000Z

264

Reaction rate kinetics for the non-catalytic hydrogenation of Texas lignite with tetralin and hydrogen gas  

E-Print Network [OSTI]

to 717 K, a time range of 3, 2 to 270 minutes, and a sol- vent-lignite ratio (weight basis) range of 0. 32/1 to 3. 68/1 were studied. The experimental results showed that Texas lignite on an as-received basis has the potential of being a very good... Observations, Definitions, and Discussion 32 39 41 45 V. KINETIC MODELLING VI. CONCLUSIONS AND RECOMMENDATIONS 47 79 LITERATURE CITED APPENDIX A APPENDIX B APPENDIX C APPENDIX D 82 84 87 104 113 VITA 123 viii LIST OF TABLES TABLE PAGE 1...

Shumbera, David Allen

1980-01-01T23:59:59.000Z

265

Effect of potassium permanganate as an oxidizing agent in the production of lignite-based fertilizers  

SciTech Connect (OSTI)

The purpose of this work was to observe the effect of potassium permanganate oxidation of lignites from Elbistan for end use as fertilizers, after being ammoniated. The experiments at each stage were designed by a 1/2 x full factorial design. The oxidation was carried out by three different methods. In the first two methods potassium permanganate in neutral or basic medium was used. In the other method two stages of oxidation were used: nitric acid followed by potassium permanganate in acidic medium. The latter proved to be more successful.

Baris, S.; Dincer, S.

1986-01-01T23:59:59.000Z

266

Impacts of stripmining lignite on net returns for agricultural enterprises in East Texas  

E-Print Network [OSTI]

. Southern Methodist University Chairman of Advisory Committee: Dr, Lonnie L. Jones The study aims to determine whether or not returns to typical pare-time and full-time farms in Preestone County change after lignite mining. Net returns used are to land... pieces of mined and unmined land. The general opinion of experts is that forage yields on reclaimed land are not less than before mining. Although the carrying capacity for unmined and reclaimed pasture is the same in the study, the mined farm cases...

Morris, Christina

1984-01-01T23:59:59.000Z

267

A study of uranium distribution in an upper Jackson lignite-sandstone ore body, South Texas  

E-Print Network [OSTI]

-central Wyoming (Denson, 1959). Since then similar discoveries have been made in North and South Dakota, Montana, Idaho, New Mexico, and most recently, in Texas. Porous, organic-r1ch sediments have repeatedly been proven to be favorable sites for uranium...A STUDY OF URANIUM DISTRIBUTION IN AN UPPER JACKSON LIGNITE-SANDSTONE ORE BODY, SOUTH TEXAS A Thesis James Randall Chatham Subnitted to the Graduate College of Texas A8M University in Partial fulfillment of the requirement for the degree...

Chatham, James Randall

1979-01-01T23:59:59.000Z

268

A study of the volatile matter of coal as a function of the heating rate  

SciTech Connect (OSTI)

A study of the volatile matter yields as a function of the heating rate was conducted. A suite of 21 coal and coke samples varying in rank from anthracitic to lignitic and heating rates from 10{degrees}C/min to about 450{degrees}C/min were used in the study. Heating rates up to 60{degrees}C per minute, which are typically used in ASTM Test Method 5142 (instrumental Proximate Analysis), were achieved in a macro thermogravimetric analysis (TGA) system. Heating rates of 50-200{degrees}C/min were obtained in a micro TGA system. All measurements were made in a nitrogen atmosphere. The results of the study illustrate the dependence of the volatile matter yield on the heating rate. For most coals and cokes the optimum heating rate for determining volatile matter values that agree with those obtained by ASTM Method D 3175 appears to be in the 100-150{degrees}C range.

Yanes, E.; Wilhite, D.; Riley, J.M. Jr. [Western Kentucky Univ., Bowling Green, KY (United States)] [and others

1996-12-31T23:59:59.000Z

269

JV Task 117 - Impact of Lignite Properties on Powerspan's NOx Oxidation System  

SciTech Connect (OSTI)

Powerspan's multipollutant control process called electrocatalytic oxidation (ECO) technology is designed to simultaneously remove SO{sub 2}, NO{sub x}, PM{sub 2.5}, acid gases (such as hydrogen fluoride [HF], hydrochloric acid [HCl], and sulfur trioxide [SO{sub 3}]), Hg, and other metals from the flue gas of coal-fired power plants. The core of this technology is a dielectric barrier discharge reactor composed of cylindrical quartz electrodes residing in metal tubes. Electrical discharge through the flue gas, passing between the electrode and the tube, produces reactive O and OH radicals. The O and OH radicals react with flue gas components to oxidize NO to NO{sub 2} and HNO{sub 3} and a small portion of the SO{sub 2} to SO{sub 3} and H{sub 2}SO{sub 4}. The oxidized compounds are subsequently removed in a downstream scrubber and wet electrostatic precipitator. A challenging characteristic of selected North Dakota lignites is their high sodium content. During high-sodium lignite combustion and gas cooling, the sodium vaporizes and condenses to produce sodium- and sulfur-rich aerosols. Based on past work, it was hypothesized that the sodium aerosols would deposit on and react with the silica electrodes and react with the silica electrodes, resulting in the formation of sodium silicate. The deposit and reacted surface layer would then electrically alter the electrode, thus impacting its dielectric properties and NO{sub x} conversion capability. The purpose of this project was to determine the impact of lignite-derived flue gas containing sodium aerosols on Powerspan's dielectric barrier discharge (DBD) reactor with specific focus on the interaction with the quartz electrodes. Partners in the project were Minnkota Power Cooperative; Basin Electric Power Cooperative; Montana Dakota Utilities Co.; Minnesota Power; the North Dakota Industrial Commission, the Lignite Energy Council, and the Lignite Research Council; the Energy & Environmental Research Center (EERC); and the U.S. Department of Energy. An electrocatalytic oxidation (ECO) reactor slipstream system was designed by Powerspan and the EERC. The slipstream system was installed by the EERC at Minnkota Power Cooperative's Milton R. Young Station Unit 1 downstream of the electrostatic precipitator where the flue gas temperature ranged from 300 to 350 F. The system was commissioned on July 3, 2007, operated for 107 days, and then winterized upon completion of the testing campaign. Operational performance of the system was monitored, and data were archived for postprocessing. A pair of electrodes were extracted and replaced on a biweekly basis. Each pair of electrodes was shipped to Powerspan to determine NO conversion efficiency in Powerspan's laboratory reactor. Tested electrodes were then shipped to the EERC for scanning electron microscopy (SEM) and x-ray microanalysis. Measurement of NO{sub x} conversion online in operating the slipstream system was not possible because the nitric and sulfuric acid production by the DBD reactor results in conditioning corrosion challenges in the sample extraction system and NO measurement technologies. The operational observations, performance results, and lab testing showed that the system was adversely affected by accumulation of the aerosol materials on the electrode. NO{sub x} conversion by ash-covered electrodes was significantly reduced; however, with electrodes that were rinsed with water, the NOx conversion efficiency recovered to nearly that of a new electrode. In addition, the visual appearance of the electrode after washing did not show evidence of a cloudy reacted surface but appeared similar to an unexposed electrode. Examination of the electrodes using SEM x-ray microanalysis showed significant elemental sodium, sulfur, calcium, potassium, and silica in the ash coating the electrodes. There was no evidence of the reaction of the sodium with the silica electrodes to produce sodium silicate layers. All SEM images showed a clearly marked boundary between the ash and the silica. Sodium and sulfur are the main culprits in the

Scott Tolbert; Steven Benson

2008-02-29T23:59:59.000Z

270

LARGE-SCALE MECURY CONTROL TECHNOLOGY TESTING FOR LIGNITE-FIRED UTILITIES-OXIDATION SYSTEMS FOR WET FGD  

SciTech Connect (OSTI)

The Energy & Environmental Research Center (EERC) is conducting a consortium-based effort directed toward resolving the mercury (Hg) control issues facing the lignite industry. Specifically, the EERC team--the EERC, EPRI, URS, ADA-ES, Babcock & Wilcox, the North Dakota Industrial Commission, SaskPower, and the Mercury Task Force, which includes Basin Electric Power Cooperative, Otter Tail Power Company, Great River Energy, Texas Utilities (TXU), Montana-Dakota Utilities Co., Minnkota Power Cooperative, BNI Coal Ltd., Dakota Westmoreland Corporation, and the North American Coal Company--has undertaken a project to significantly and cost-effectively oxidize elemental mercury in lignite combustion gases, followed by capture in a wet scrubber. This approach will be applicable to virtually every lignite utility in the United States and Canada and potentially impact subbituminous utilities. The oxidation process is proven at the pilot-scale and in short-term full-scale tests. Additional optimization is continuing on oxidation technologies, and this project focuses on longer-term full-scale testing. The lignite industry has been proactive in advancing the understanding of and identifying control options for Hg in lignite combustion flue gases. Approximately 1 year ago, the EERC and EPRI began a series of Hg-related discussions with the Mercury Task Force as well as utilities firing Texas and Saskatchewan lignites. This project is one of three being undertaken by the consortium to perform large-scale Hg control technology testing to address the specific needs and challenges to be met in controlling Hg from lignite-fired power plants. This project involves Hg oxidation upstream of a system equipped with an electrostatic precipitator (ESP) followed by wet flue gas desulfurization (FGD). The team involved in conducting the technical aspects of the project includes the EERC, Babcock & Wilcox, URS, and ADA-ES. The host sites include Minnkota Power Cooperative Milton R. Young Unit 2 and TXU Monticello Unit 3. The work involves establishing Hg oxidation levels upstream of air pollution control devices (APCDs) and removal rates across existing ESP and FGD units, determining costs associated with those removal rates, investigating the possibility of the APCD acting as a multipollutant control device, quantifying the balance of plant impacts of the control technologies, and facilitating technology commercialization.

Michael J. Holmes; Steven A. Benson; Jeffrey S. Thompson

2004-03-01T23:59:59.000Z

271

Thirteenth biennial lignite symposium: technology and utilization of low-rank coals proceedings. Volume 2  

SciTech Connect (OSTI)

These proceedings are the collected manuscripts from the 1985 Lignite Symposium held at Bismarck, North Dakota on May 21-23, 1985. Sponsorship of the thirteenth biennial meeting was by the United States Department of Energy, the University of North Dakota Energy Research Center, and the Texas University Coal Research Consortium. Seven technical sessions plus two luncheons and a banquet were held during the two and a half day meeting. The final half day included tours of the Great Plains Gasification Plant; Basin Electric's Antelope Valley Power Station; and the Freedom Mine. Sessions covered diverse topics related to the technology and use of low-rank coals including coal development and public policy, combustion, gasification, environmental systems for low-rank coal utilization, liquefaction, beneficiation and coal mining and coal inorganics. All the papers have been entered individually into EDB and ERA.

Jones, M.L. (ed.)

1986-02-01T23:59:59.000Z

272

Thirteenth biennial lignite symposium: technology and utilization of low-rank coals proceedings. Volume 1  

SciTech Connect (OSTI)

These proceedings are the collected manuscripts from the 1985 Lignite Symposium held at Bismarck, North Dakota on May 21-23. Sponsorship of the thirteenth biennial meeting was by the United States Department of Energy, the University of North Dakota Energy Research Center, and the Texas University Coal Research Consortium. Seven technical sessions were held during the two and a half day meeting. The final half day included tours of the Great Plains Gasification Plant; Basin Electric's Antelope Valley Power Station; and the Freedom Mine. Sessions covered diverse topics related to the technology and use of low-rank coals including coal development and public policy, combustion, gasification, environmental systems for low-rank coal utilization, liquefaction, beneficiation and coal mining and coal inorganics. Twenty-four papers have been entered individually into EDB and ERA.

Jones, M.L. (ed.)

1986-02-01T23:59:59.000Z

273

Advanced power assessment for Czech lignite task 3.6. Topical report  

SciTech Connect (OSTI)

Major reforms in the Czech energy sector have been initiated to reverse 40 years of central planning, subsidized energy pricing, unchecked pollution from coal-fired plants, concerns over nuclear safety and fuel cycle management, and dependence on the former U.S.S.R. for oil, gas, and nuclear fuel processing. Prices for electricity, heat, and natural gas paid by industry are close to western levels, but subsidized prices for households are as much as 40% lower and below economic cost. State control of major energy enterprises is being reduced by moving toward government-regulated, investor-owned companies to raise needed capital, but with a strategic stake retained by the state. Foreign firms will participate in privatization, but they are not expected to acquire a controlling interest in Czech energy companies. Economic conditions in the Czech Republic are now improving after the disruptions caused by restructuring since 1989 and separation of the former Czech and Slovak Federal Republics in January 1993. The downturn in the economy after 1989 was concentrated in energy-intensive heavy industry, and recovery is paced by consumer trade, services, light industry and construction. Energy use in relation to gross domestic product (GDP) has declined, but it is still significantly higher than in OECD (Organization for Economic Cooperation and Development) countries. The GDP increased by 2% in 1994 after dropping 22% between 1989 and 1993. A positive balance of payments has been achieved, with foreign investment offsetting a small trade deficit. The government`s external debt is only 4% of GDP. This report studies the application of lignite resources within the newly formulated energy policies of the republic, in light of a move toward privatization and stronger air pollution regulations. Lignite has represented the major energy source for the country.

Sondreal, E.A.; Mann, M.D.; Weber, G.W.; Young, B.C.

1995-12-01T23:59:59.000Z

274

The distribution of ten trace elements and minerals in three lignite seams from the Mae Moh Mine, Thailand  

SciTech Connect (OSTI)

Understanding the association of major, minor and trace elements in lignites and their accompanying strata is important from a number of perspectives which include: potential health problems from environmental pollutants, rehabilitation after mining, combustion for power etc. The material which follows represents some preliminary observations on the mineralogy and distribution of 10 trace elements in lignites and accompanying sediments from the Mae Moh mine, Thailand. Samples collected from freshly exposed mine faces were air dried and analyzed for moisture and ash. Trace element concentrations were determined on {open_quotes}whole{close_quotes} coals and sediments by NAA and XRF. All chemical analyses are expressed as a fraction of the total dry sediment. Mineralogy of both LTA and sediments was determined by XRD. The chemistry and morphology of individual particles were examined by the Electron microprobe. The analyses are used to make some conclusions about the spatial occurrence of these elements within the seam and their partitioning between organic and inorganic phases.

Hart, B.; Powell, M.P.; Fyfe, W.S. [Univ. of Ontario (Canada)

1994-12-31T23:59:59.000Z

275

Large-Scale Mercury Control Technology Testing for Lignite-Fired Utilities - Oxidation Systems for Wet FGD  

SciTech Connect (OSTI)

Mercury (Hg) control technologies were evaluated at Minnkota Power Cooperative's Milton R. Young (MRY) Station Unit 2, a 450-MW lignite-fired cyclone unit near Center, North Dakota, and TXU Energy's Monticello Steam Electric Station (MoSES) Unit 3, a 793-MW lignite--Powder River Basin (PRB) subbituminous coal-fired unit near Mt. Pleasant, Texas. A cold-side electrostatic precipitator (ESP) and wet flue gas desulfurization (FGD) scrubber are used at MRY and MoSES for controlling particulate and sulfur dioxide (SO{sub 2}) emissions, respectively. Several approaches for significantly and cost-effectively oxidizing elemental mercury (Hg{sup 0}) in lignite combustion flue gases, followed by capture in an ESP and/or FGD scrubber were evaluated. The project team involved in performing the technical aspects of the project included Babcock & Wilcox, the Energy & Environmental Research Center (EERC), the Electric Power Research Institute, and URS Corporation. Calcium bromide (CaBr{sub 2}), calcium chloride (CaCl{sub 2}), magnesium chloride (MgCl{sub 2}), and a proprietary sorbent enhancement additive (SEA), hereafter referred to as SEA2, were added to the lignite feeds to enhance Hg capture in the ESP and/or wet FGD. In addition, powdered activated carbon (PAC) was injected upstream of the ESP at MRY Unit 2. The work involved establishing Hg concentrations and removal rates across existing ESP and FGD units, determining costs associated with a given Hg removal efficiency, quantifying the balance-of-plant impacts of the control technologies, and facilitating technology commercialization. The primary project goal was to achieve ESP-FGD Hg removal efficiencies of {ge}55% at MRY and MoSES for about a month.

Steven A. Benson; Michael J. Holmes; Donald P. McCollor; Jill M. Mackenzie; Charlene R. Crocker; Lingbu Kong; Kevin C. Galbreath

2007-03-31T23:59:59.000Z

276

Petrographic characteristics of Romanian lignite and solid by-products resulting from circulating fluidized bed combustion -- CFBC  

SciTech Connect (OSTI)

The low rank coals -- lignites -- are the main source, in Romania for power and thermal energy generation. The Circulating Fluidized Bed Combustion -- CFBC -- was chosen to be used for its particular features with very low emission levels. Carbopetrographic research, using optical microscopy, was carried out on the raw coals and, especially, on the carbonaceous products in different thermal stages and the residues. The existence of successive and simultaneous phases of degasing, pyrolysis and burning of organic and mineral material was revealed. The study gave the possibility of improving the process-governing parameters, in order to raise the combustion efficiency on once-through combustors. The main solid fuel fired in power plants is the lignite obtained from surface exploitation. Experience of its use in high load power systems has shown that it can be fired only by adding liquid fuel. Moreover, it is rather difficult to prepare it to exact size requested. The only technology conveniently applied for this fuel was the fluidized bed combustion (FBC), which uses a 0--7 mm-sized lignite. On the basis of this original concept technology, steam and hot water load generators were built in Romania, that is 2 t/h, 8 bar, 170 C, and 10 t/h, 16 bar, 350 C steam generators and 5 Gcal/h, and 10 Gcal/h hot water boilers. For loads over 100 Gcal/h, 100 t/h, circulating fluidized bed combustion boilers were conceived.

Panaitescu, C. [Politehnica Univ. Bucharest (Romania); Dragos, L.; Fluieraru, C.; Nistor, I. [Thermal Power Engineering Inst., Bucharest (Romania)

1994-12-31T23:59:59.000Z

277

Environmental assessment of remedial action at the inactive uraniferous lignite ashing sites at Belfield and Bowman, North Dakota  

SciTech Connect (OSTI)

The Uranium Mill Tailings Radiation Control Act (UMTRCA) of 1978 authorized the US Department of Energy (DOE) to perform remedial actions at Belfield and Bowman inactive lignite ashing sites in southwestern North Dakota to reduce the potential public health impacts from the residual radioactivity remaining at the sites. The US Environmental Protection Agency (EPA) promulgated standards (40 CFR 192) that contain measures to control the residual radioactive materials and other contaminated materials, and proposed standards to protect the groundwater from further degradation. Remedial action at the Belfield and Bowman sites must be performed in accordance with these standards and with the concurrence of the US Nuclear Regulatory Commission (NRC) and the state of North Dakota. The Belfield and Bowman designated sites were used by Union Carbide and Kerr-McGee, respectively, to process uraniferous lignite in the 1960s. Uranium-rich ash from rotary kiln processing of the lignite was loaded into rail cars and transported to uranium mills in Rifle, Colorado, and Ambrosia Lake, New Mexico, respectively. As a result of the ashing process, there is a total of 158,400 cubic yards (yd{sup 3}) [121,100 cubic meters (m{sup 3})] of radioactive ash-contaminated soils at the two sites. Windblown ash-contaminated soil covers an additional 21 acres (8.5 ha) around the site, which includes grazing land, wetlands, and a wooded habitat.

Not Available

1993-09-01T23:59:59.000Z

278

Mercury Control for Plants Firing Texas Lignite and Equipped with ESP-wet FGD  

SciTech Connect (OSTI)

This report presents the results of a multi-year test program conducted as part of Cooperative Agreement DE-FC26-06NT42779, 'Mercury Control for Plants Firing Texas Lignite and Equipped with ESP-wet FGD.' The objective of this program was to determine the level of mercury removal achievable using sorbent injection for a plant firing Texas lignite fuel and equipped with an ESP and wet FGD. The project was primarily funded by the U.S. DOE National Energy Technology Laboratory. EPRI, NRG Texas, Luminant (formerly TXU), and AEP were project co-funders. URS Group was the prime contractor, and Apogee Scientific and ADA-ES were subcontractors. The host site for this program was NRG Texas Limestone Electric Generating Station (LMS) Units 1 and 2, located in Jewett, Texas. The plant fires a blend of Texas lignite and Powder River Basin (PRB) coal. Full-scale tests were conducted to evaluate the mercury removal performance of powdered sorbents injected into the flue gas upstream of the ESP (traditional configuration), upstream of the air preheater, and/or between electric fields within the ESP (Toxecon{trademark} II configuration). Phases I through III of the test program, conducted on Unit 1 in 2006-2007, consisted of three short-term parametric test phases followed by a 60-day continuous operation test. Selected mercury sorbents were injected to treat one quarter of the flue gas (e.g., approximately 225 MW equivalence) produced by Limestone Unit 1. Six sorbents and three injection configurations were evaluated and results were used to select the best combination of sorbent (Norit Americas DARCO Hg-LH at 2 lb/Macf) and injection location (upstream of the ESP) for a two-month performance evaluation. A mercury removal rate of 50-70% was targeted for the long-term test. During this continuous-injection test, mercury removal performance and variability were evaluated as the plant operated under normal conditions. Additional evaluations were made to determine any balance-of-plant impacts of the mercury control process, including those associated with ESP performance and fly ash reuse properties. Upon analysis of the project results, the project team identified several areas of interest for further study. Follow-on testing was conducted on Unit 2 in 2009 with the entire unit treated with injected sorbent so that mercury removal across the FGD could be measured and so that other low-ash impact technologies could be evaluated. Three approaches to minimizing ash impacts were tested: (1) injection of 'low ash impact' sorbents, (2) alterations to the injection configuration, and (3) injection of calcium bromide in conjunction with sorbent. These conditions were tested with the goal of identifying the conditions that result in the highest mercury removal while maintaining the sorbent injection at a rate that preserves the beneficial use of ash.

Katherine Dombrowski

2009-12-31T23:59:59.000Z

279

Key China Energy Statistics 2011  

E-Print Network [OSTI]

AAGR Total Primary Energy (Mtce) Coal Production (1985-2009)Physical Unit to Coal Equivalent For this energy form 1Total Primary Energy Supply Coke Coal Gas not Coke Other

Levine, Mark

2013-01-01T23:59:59.000Z

280

INTERACTION OF ORGANIC SOLVENTS WITH A SUBBITUMINOUS COAL BELOW PYROLYSIS TEMPERATURE  

E-Print Network [OSTI]

this substance could be added to a poor coking coal in ordersubstance from the coal called the "coking principle." Itcoking properties. These attempts failed, but they provided the starting point for further investigation of coal

Dorighi, G.P.

2010-01-01T23:59:59.000Z

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


281

7, 14791506, 2007 apportionment of the  

E-Print Network [OSTI]

, coal residential, coke oven, coal power plant, biomass burning, natural gas (NG) combustion. The major showed distinct seasonal variations. High contributions of biomass burning and coal (residential and coke is the world's largest coal consumption region (IEA, 2006). Thu

Paris-Sud XI, Université de

282

Valorization of Automotive Shredder Residues in metallurgical furnaces Project REFORBA  

E-Print Network [OSTI]

) and the electric arc furnace (EAF) routes, P1 could be used as substitute for coal or coke, and P2 could replace with raw materials cheaper than coke. As additional potential benefits the amount of CO2 generated

Paris-Sud XI, Université de

283

Energy intensity in China's iron and steel sector  

E-Print Network [OSTI]

In this study, I examine the spatial and economic factors that influence energy intensity in China's iron and steel sector, namely industrial value added, renovation investment, coke consumption, and local coke supply. ...

Xu, Jingsi, M.C.P. Massachusetts Institute of Technology

2011-01-01T23:59:59.000Z

284

Ethylbenzene dehydrogenation into styrene: kinetic modeling and reactor simulation  

E-Print Network [OSTI]

detailed kinetic model for coke formation and gasification, which was coupled to the kinetic model for the main reactions. The calculation of the dynamic equilibrium coke content provided a crucial guideline for the selection of the steam to ethylbenzene...

Lee, Won Jae

2007-04-25T23:59:59.000Z

285

To link to this article : DOI:10.1016/j.fuel.2011.11.066 URL : http://www.sciencedirect.com/science/article/pii/S0016236111007800#  

E-Print Network [OSTI]

, alexandre and Debenest, Gérald Modelling of non-consolidated oil shale semi- coke forward combustion : 10.1016/j.fuel.2011.11.066 #12;Modelling of non-consolidated oil shale semi-coke forward combustion

Paris-Sud XI, Université de

286

Atmos. Chem. Phys., 11, 931954, 2011 www.atmos-chem-phys.net/11/931/2011/  

E-Print Network [OSTI]

for the brick and coke industries, as well as for coal- burning stoves and biofuel usage in the residential

Meskhidze, Nicholas

287

Graphite fountain: Modeling of growth on transition metals under a thermal Jongpil Ye and Rodney S. Ruoff  

E-Print Network [OSTI]

petroleum cokes and coal tar pitch at high temperatures around 3000 K to 3300 K.3 Uniaxial stress is also

288

Sohn International Symposium, 27-31 Aug. 06, San Diego. Proceedings edited by F. Kongoli and R.G. Reddy, TMS, vol. 1, pp. 141-153.  

E-Print Network [OSTI]

and reduction, the oxidation of metals, the pyrolysis of coal, the oxidation of coke. In most cases the kinetic

Paris-Sud XI, Université de

289

Trends in the Carbonyl Core (C 1S, O 1S) f *C)O Transition in the Near-Edge X-ray Absorption Fine Structure Spectra of Organic Molecules  

E-Print Network [OSTI]

,2 meteorites3 and interplanetary dust particles,4 eocene and recent wood,5,6 coal, coke, and other organic

290

SOLVENT EXTRACTION OF PHENOLS FROM WATER  

E-Print Network [OSTI]

coking (Wurm, 1968) • Phenols are also the principal organic constituents in con- densate waters formed during coal

Greminger, Douglas C.

2012-01-01T23:59:59.000Z

291

Nordic Energy Basics Tiina Koljonen, Esa Pursiheimo  

E-Print Network [OSTI]

% - 4 17 49 10 Nuclear fuel % - 18 - - 33 Coal and coke % 21 12 - 157) 4 Geothermal % - - 55 - - Other1

292

Constraining uncertainties about the sources and magnitude of ambient air exposures to polycyclic aromatic hydrocarbons (PAHs): The state of Minnesota as a case study  

E-Print Network [OSTI]

wood, wood waste, and ‘black liquor’ are reported by thee other= wood waste, black liquor, used oil, petroleum coke,

Lobscheid, Agnes B.; McKone, Thomas E.

2004-01-01T23:59:59.000Z

293

Determination of foraminiferal criteria for environmental interpretation using Upper Cretaceous sandstones, Brazos, Frio, Walker, and Zavala counties, Texas  

E-Print Network [OSTI]

of the Amalga- mated Bonanza Smith 2 and a basinal depositional en- vironment for the shale of the Morgan Central Coal and Coke, G-4 Wildcat 7) Few tests were recovered from the sediments of the Amalgamated Bonanza Smith 2 and the Norgan Central Coal... Johnson 3-Sand Niguel Sandstone Amalgamated Bonanza Smith 2-Woodbine Sand- stone ~ ~ ~ ~ Morgan Central Coal & Coke, G-4 Wildcat- Woodbine Shale Norgan Central Coal & Coke, G-4 wildcat- Georgetown Limestone Morgan Central Coal & Coke, G-4 Wildcat...

Nufer, Janet Ann

2012-06-07T23:59:59.000Z

294

Assessment of China's Energy-Saving and Emission-Reduction Accomplishments and Opportunities During the 11th Five Year Plan  

E-Print Network [OSTI]

clean coal, petroleum coke and natural gas, accelerate transmission of electricity from the western to the eastern region of China

Levine, Mark D.

2010-01-01T23:59:59.000Z

295

Vegetation trends in reclaimed areas at Gibbons Creek Lignite Mine, Grimes County, Texas  

SciTech Connect (OSTI)

Vegetation productivity and cover studies have been conducted annually at the Gibbons Creek Lignite Mine since 1989, and multiple annual clippings have been collected since 1991. The primary purpose of these studies was to examine revegetation success, in terms of herbaceous productivity, for various post-mine soil types. However, the studies also contain detailed information on species composition. For the years in which multiple annual clippings have been collected (1991 through 1996), total vegetation cover increased, with the mean proportion of bare ground dropping from 12% in 1991 to 1% in 1996. Relative proportions of most introduced and native grasses were virtually static from 1991 through 1994; in 1995, however, herbicide applications to reduce clover cover resulted in a dramatic increase in total grass cover, especially in bahiagrass (Paspalum notatum) and Indiangrass (Sorgastrum nutans). In contrast to the trends of other introduced and native grasses, bahiagrass increased in cover throughout the study period, increasing from 7% in 1991 to 21 % in 1996. Annual and weedy grass species decreased in cover throughout the study period, falling from 12% cover in 1991 to 2% in 1996. This trend of displacement of annuals by perennials is typically observed during ecological succession in natural vegetation communities, and appears to have been accelerated by the herbicide application.

Westerman, C.A. [Morrison Knudsen Corp., San Antonio, TX (United States)

1997-12-31T23:59:59.000Z

296

Fe(II) adsorption onto natural polymers derived from low-grade lignites  

SciTech Connect (OSTI)

In comparison with conventional chemical treatment methods for Fe(II) ions, adsorption and ion exchange are considered more easily applicable and economical, depending on the material used. Polymeric rnaterials are the examples used in these commonly applied removal processes. In this study, the adsorption of Fe(II) ions from aqueous solutions onto two different natural polymers, insoluble humic acids (IHAs) extracted from low-grade lignites from Beysehir and Ermenek (in the central Anatolia region, Konya, Turkey), was investigated. The IHAs were synthesized through a series of acid-base reactions, and the obtained precipitates were chemically stable and had about 40% humic matter together with functional carboxyl and hydroxyl groups. The effects of the time and initial metal concentration on the effectiveness of the IHAs for Fe(II) adsorption were determined through batch experiments; the adsorption isotherms and capacities were calculated. The IHAs were effective, with capacities of 59 mg/g for the Beysehir IHA and 57 mg/g for the Ermenek IHA, for Fe removal under neutral pH conditions. The adsorption followed mainly a Freundlich isotherm for both IHAs, and the calculated adsorption rates were 0.86 for the Beysehir IHA and 0.81 for the Ermenek IHA. This indicated that the effectiveness of the Beysehir IHA was slightly higher than that of the Ermenek IHA. The results confirmed the real possibility of the practical application of IHAs for the separation of Fe(II) in aqueous systems.

Tarlan, E.; Ahmetli, G. [Selcuk University, Konya (Turkey)

2007-09-15T23:59:59.000Z

297

Industrial properties of lignitic and lignocellulosic fly ashes from Turkish sources  

SciTech Connect (OSTI)

Fly ash is an inorganic matter from combustion of the carbonaceous solid fuels. More than half the electricity in Turkey is produced from lignite-fired power plants. This energy production has resulted in the formation of more than 13 million tons of fly ash waste annually. The presence of carbon in fly ash inducing common faults include adding unwanted black color and adsorbing process or product materials such as water and chemicals. One of the reasons for not using fly ash directly is its carbon content. For some uses carbon must be lower than 3%. Fly ash has been used for partial replacement of cement, aggregate, or both for nearly 70 years, and it is still used on a very limited scale in Turkey. The heavy metal content of industrial wastewaters is an important source of environmental pollution. Each of the three major oxides (SiO{sub 2} + Al{sub 2}O{sub 3} + Fe{sub 2}O{sub 3}) in fly ash can be ideal as a metal adsorbent.

Demirbas, A.; Cetin, S. [Selcuk University, Konya (Turkey)

2006-01-21T23:59:59.000Z

298

Effect of environment atmosphere on the sintering of Thai lignite fly ashes  

SciTech Connect (OSTI)

Sintering of ash particles, related to deposit formation in a pulverized coal-fired boiler, was investigated for two lignite fly ashes obtained from Mae Moh and Bangpudum coal seams. The tests involved measuring the compressive strength of cold sintered pellets at varying sintering temperature, both under oxidizing (air) and non-oxidizing atmospheres (CO{sub 2}). Under ambient air condition, Mae Moh fly ash which contained higher amount of glassy phase gave significantly higher sinter strength than Bangpudum fly ash. The role of glassy phase was confirmed by the lowering of sinter strength when HF-extracted fly ash was tested. Sintering under CO{sub 2} environment resulted in larger strength development than sintering in air. Under this non-oxidizing condition, the pellet color turned black, indicating that most of the iron was in the reduced state and could form additional low melting-point glassy phase, hence facilitated sintering rate. In addition, blending of the two ashes yielded intermediate maximum strength, under both air and CO{sub 2} environments. This observation substantiates the important role of glassy phase in the sintering process and indicates the possibility of lowering deposit strength by judicious mixing of different raw coal feeds.

Tangsathitkulchai, C.; Tangsathitkulchai, M. [Suranaree Univ. of Technology, Nakhon Ratchasima (Thailand)

1996-12-31T23:59:59.000Z

299

Tracking Progress Last updated 6/2/2014 Current and Expected Energy From Coal for California 1  

E-Print Network [OSTI]

2007 to 2012, energy from in-state coal and petroleum (pet) coke plants declined by 62 percent. These trends are shown in Figure 1. Eight in-state coal and pet coke plants retired or stopped operating in 2011 and 2012. Of the 16 in-state coal and pet coke plants that once operated in California, only two

300

ENERGY UTILIZATION AND ENVIRONMENTAL CONTROL TECHNOLOGIES IN THE COAL-ELECTRIC CYCLE  

E-Print Network [OSTI]

Plant - without coking (lb/hr) Feed Coal* Hydrogen YieldsCoking Summary Cost Estimates for Solvent Refining of Five U.S. CoalsCoal Handling and Preparation Preheaters and Dissolvers Mineral Separation (Filters) Solvent Recovery Gas Recovery Mineral Residue Processing and Storage Coking

Ferrell, G.C.

2010-01-01T23:59:59.000Z

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


301

UV Resonance Raman Detection of Artificial Sweetener in Soda Pop-  

E-Print Network [OSTI]

in complicated fuel, coal liquid, and petroleum mixtures? An increase of up to six orders of magnitude. In this correspondance, the UVRR spectra of two soft drinks, Diet Coke and New Coke, are reported. UV ex- citation enhances phenylalanine ring modes in the ar- tifical sweetener Nutrasweet in Diet Coke. This artifical

Asher, Sanford A.

302

Novel Regenerated Solvent Extraction Processes for the Recovery of Carboxylic Acids or Ammonia from Aqueous Solutions Part II. Recovery of Ammonia from Sour Waters  

E-Print Network [OSTI]

19,20). In the coking step, coal is heated III the absencethe "coking" process in In the second step the which coal isCoal Liquefaction Wastewaters Sour Waters from Oil Shale Retorting Sour Waters from Petroleum Refining Sour Waters from Coking

Poole, L.J.

2008-01-01T23:59:59.000Z

303

PAH Sorption Mechanism and Partitioning Behavior in  

E-Print Network [OSTI]

. Introduction Prior to the widespread distribution of natural gas, manu- factured gas from coke, coal, and oil. In the eastern United States, where coal was plentiful, gas was derived from coal or coke. Along the West Coast, because of the availability of oil and the expense in transporting coal or coke to this region, gas

Zare, Richard N.

304

This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research  

E-Print Network [OSTI]

-scale reactor for producing hot metal where coke and coal are consumed as reducing agent and fuel, respectively]. In addition to coke, coal has also been extensively consumed in BFs for supplying heat through pulverized coal. At the same time, the consumptions of coal and coke will liberate a large amount of greenhouse gases

Leu, Tzong-Shyng "Jeremy"

305

ANT Automation, LLC is an American company dedicated to provide high quality Automation Ser-  

E-Print Network [OSTI]

to be accepted before releasing it to production. COBOP: Coal Blend Optimization for Coke Plants. Predict the coke quality. Help to the process Engineer in decision making for the coal's purchasing. Minimize coal / Carbon, Scrap Consumption, Coke, Additives & Refractories among others. Minimizes overall cost in seconds

Maguitman, Ana Gabriela

306

Near Surface 2011 17th European Meeting of Environmental and Engineering Geophysics  

E-Print Network [OSTI]

campaigns performed around a housing estate located downstream to an old coke tar site in France. This coke than water, such as chlorinated solvents, wood preservative wastes, coal tar wastes, and pesticides electrical resistivity campaigns performed around a housing estate located downstream an old coke tar site

Boyer, Edmond

307

RAIRO Operations Research Will be set by the publisher  

E-Print Network [OSTI]

of the model is to prescribe optimal mixes of coal used to produce coke. The problem is formulated as a mixed In this paper, we consider a real life problem: a coal blending problem for coke production. The model includes, the coke delivered to the customers can be obtained using different mixes of coals. However, the total

Boyer, Edmond

308

Mezza Plate $6.00 Hummus, Mediterranean Eggplant Pure, Dolmades, Cucumbers, Olives and Artichokes served with Pita  

E-Print Network [OSTI]

.00 Traditional or Strawberry Soft Drinks $3.00 Coke, Diet Coke, Sprite or Coke Zero Tazo Iced Tea $4.00 Zen Green Tea $4.00 Zen Green or Peach Black Izze Sparkling Juices $4.00 Clementine, Blackberry, Pink Grapefruit and Noodles Marinated in Sesame Dressing, Mixed Greens, Crisp Cut Veggies and a light ginger rice vinegar

Hampton, Randy

309

Combination process for upgrading reduced crude  

SciTech Connect (OSTI)

A reduced crude conversion process is described for heavy oil feeds having Conradson carbon numbers above two, which process comprises contacting a heavy oil feed with a catalyst to form products comprising lower molecular weight hydrocarbons and coke-on-catalyst, the coke containing minor amounts of hydrogen, and thereafter regenerating the catalyst by removing at least a portion of the coke.

Hettinger, W.P. Jr.

1986-07-15T23:59:59.000Z

310

"Code(a)","End Use","Electricity(b)","Fuel Oil","Diesel Fuel(c)"," Gas(d)","NGL(e)","Coke and Breeze)"  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia, Virginia:FAQ <Information Administration (EIA) 10 MECSPropaneResidential"Total" "(Data051.3

311

"End Use","for Electricity(a)","Fuel Oil","Diesel Fuel(b)","Natural Gas(c)","NGL(d)","Coke and Breeze)"  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia, Virginia:FAQ <Information Administration (EIA) 10 MECSPropaneResidential"Total"2.4 Relative4 Relative2268

312

Correlation of Paleocene Harmon and Hansen lignite beds, Adams, Billings, Bowman, Golden Valley, Hettinger, and Slope Counties, Williston Basin, North Dakota  

SciTech Connect (OSTI)

In southwestern North Dakota, minable lignite beds in the Paleocene Fort Union Formation include the Harmon and Hansen beds in the Bowman-Gascoyne area. Data from more than 700 drill holes penetrating these beds was used to construct stratigraphic cross sections. The Harmon and Hansen beds are the thickest and most laterally persistent lignites found under < 150 ft of overburden. The Harmon coal bed is as much as 34 ft thick, and is often split by claystone interbeds of variable thickness. The Hansen coal bed typically occurs 10--100 ft below the Harmon coal bed; it rarely attains a thickness of 15 ft, and averages 4 ft in thickness.

Keighin, C.W.; Flores, R.M.; Ochs, A. [Geological Survey, Denver, CO (United States)

1998-12-31T23:59:59.000Z

313

Establishment, growth and water use of Quercus virginiana (Mill.) on lignite surface-mined soils in response to irrigation  

E-Print Network [OSTI]

1 percent slope and an aspect of 95'. The plot location is at latitude 30'35'N and longitude 96 06'W at an elevation of 85 meters. The study site is in the Post Oak Savannah region of Texas which is characterized by gently rolling to hilly... applied to 12 live oak seedlings on reclaimed lignite surface-mined soils in central Texas as a means to study the physiology and growth of seedlings during establishment. The study period was 4 July 1990 through 30 September 1990. Transpiration...

Duncan, Jacalyn E.

1991-01-01T23:59:59.000Z

314

STUDIES OF THE SPONTANEOUS COMBUSTION OF LOW RANK COALS AND LIGNITES  

SciTech Connect (OSTI)

Spontaneous combustion has always been a problem in coal utilization especially in the storage and transportation of coal. In the United States, approximately 11% of underground coal mine fires are attributed to spontaneous coal combustion. The incidence of such fires is expected to increase with increased consumption of lower rank coals. The cause is usually suspected to be the reabsorption of moisture and oxidation. To understand the mechanisms of spontaneous combustion this study was conducted to (1) define the initial and final products during the low temperature (10 to 60 C) oxidation of coal at different partial pressures of O{sub 2}, (2) determine the rate of oxidation, and (3) measure the reaction enthalpy. The reaction rate (R) and propensity towards spontaneous combustion were evaluated in terms of the initial rate method for the mass gained due to adsorbed O{sub 2}. Equipment that was used consisted of a FT-IR (Fourier Transform-Infrared Spectrometer, Perkin Elmer), an accelerated surface area porosimeter (ASAP, Micromeritics model 2010), thermogravimetric analyzer (TGA, Cahn Microbalance TG 121) and a differential scanning calorimeter (DSC, Q1000, thermal analysis instruments). Their combination yielded data that established a relation between adsorption of oxygen and reaction enthalpy. The head space/ gas chromatograph/ mass spectrometer system (HS/GC/MS) was used to identify volatiles evolved during oxidation. The coal samples used were Beulah lignite and Wyodak (sub-bituminous). Oxygen (O{sub 2}) absorption rates ranged from 0.202 mg O{sub 2}/mg coal hr for coal sample No.20 (Beulah pyrolyzed at 300 C) to 6.05 mg O{sub 2}/mg coal hr for coal sample No.8 (wyodak aged and pyrolyzed at 300 C). Aging of coal followed by pyrolysis was observed to contribute to higher reaction rates. Reaction enthalpies ranged from 0.42 to 1580 kcal/gm/mol O{sub 2}.

Joseph M. Okoh; Joseph N.D. Dodoo

2005-07-26T23:59:59.000Z

315

Baseline risk assessment of ground water contamination at the inactive uraniferous lignite ashing site near Bowman, North Dakota  

SciTech Connect (OSTI)

This baseline risk assessment of ground water contamination at the inactive uraniferous lignite ashing site near Bowman, North Dakota, evaluates the potential impacts to public health or the environment from contaminated ground water at this site. This contamination is a result of the uraniferous lignite ashing process, when coal containing uranium was burned to produce uranium. Potential risk is quantified only for constituents introduced by the processing activities and not for the constituents naturally occurring in background ground water in the site vicinity. Background ground water, separate from any site-related contamination, imposes a percentage of the overall risk from ground water ingestion in the Bowman site vicinity. The US Department of Energy (DOE) Uranium Mill Tailings Remedial Action (UMTRA) Project is developing plans to address soil and ground water contamination at the site. The UMTRA Surface Project involves the determination of the extent of soil contamination and design of an engineered disposal cell for long-term storage of contaminated materials. The UMTRA Ground Water Project evaluates ground water contamination. Based on results from future site monitoring activities as defined in the site observational work plan and results from this risk assessment, the DOE will propose an approach for managing contaminated ground water at the Bowman site.

Not Available

1994-11-01T23:59:59.000Z

316

Raceway behaviors in blast furnace with pulverized coal injection  

SciTech Connect (OSTI)

The blast furnace raceway shows different characteristics with PCR (pulverized coal injection rate). It was found in this study that with the increase of PCR the raceway depth decreases, and the size of birds nest and sometimes with liquid holdup, increases. Oxygen enrichment with co-axial lances was known to be very effective on the extension of raceway depth and size reduction of birds nest. It was also found that there are various factors which affect the coke properties at tuyere level of the blast furnace. Coke traveling time was calculated to be extended with PCR and it had a close relationship with the coke size in bosh. Coke mean size decreased with the increase of coke traveling time, that is, with the increase of PCR. Both DI (the strength of coke in cold) and CSR (the strength of coke after reaction) were also decreased with PCR. RAFT (Raceway Adiabatic Flame Temperature) had a tendency to be decreased with the increase of PCR, which is obtained by the estimation of coke temperature via XRD analysis. From the analysis of alkali contents in coke sampled along the radius of the blast furnace, it was understood that no difference in alkali contents between fine and lump coke represents that coke fines generated from upper burden might appear at tuyere level.

Chung, J.K.; Han, J.W.; Cho, B.R. [POSCO, Cheollanamdo (Korea, Republic of)

1995-12-01T23:59:59.000Z

317

CALDERON COKEMAKING PROCESS/DEMONSTRATION PROJECT  

SciTech Connect (OSTI)

This project deals with the demonstration of a coking process using proprietary technology of Calderon, with the following objectives geared to facilitate commercialization: (1) making coke of such quality as to be suitable for use in hard-driving, large blast furnaces; (2) providing proof that such process is continuous and environmentally closed to prevent emissions; (3) demonstrating that high-coking-pressure (non-traditional) coal blends which cannot be safely charged into conventional by-product coke ovens can be used in the Calderon process; (4) conducting a blast furnace test to demonstrate the compatibility of the coke produced; and (5) demonstrating that coke can be produced economically, at a level competitive with coke imports. The activities of the past quarter were focused on the following: Detailed workings of the team; Proposal to FETC for Phase II; Permitting and Environmental Work; and Engineering Progress.

Albert Calderon

1999-09-22T23:59:59.000Z

318

Market Assessment and Demonstration of Lignite FBC Ash Flowable Fill Applications  

SciTech Connect (OSTI)

Montana-Dakota Utilities (MDU) and Western Research Institute (WRI) have been developing flowable fill materials formulated using ash from the Montana-Dakota Utilities R. M. Heskett Station in Mandan, North Dakota. MDU and WRI have partnered with the U.S. Department of Energy (DOE) and the North Dakota Industrial Commission (NDIC) to further the development of these materials for lignite-fired fluidized-bed combustion (FBC) facilities. The MDU controlled density fill (CDF) appears to be a viable engineering material and environmentally safe. WRI is pursuing the commercialization of the technology under the trademark Ready-Fill{trademark}. The project objectives were to: (1) assess the market in the Bismarck-Mandan area; (2) evaluate the geotechnical properties and environmental compatibility; and (3) construct and monitor demonstrations of the various grades of flowable fill products in full-scale demonstrations. The scope of initial phase of work entailed the following: Task I--Assess Market for MDU Flowable Fill Products; Task II--Assess Geotechnical and Environmental Properties of MDU Flowable Fill Products; and Task III--Demonstrate and Monitor MDU Flowable Fill Products in Field-Scale Demonstrations. The results of these testing and demonstration activities proved the following: (1) The market assessment indicated that a market exists in the Bismarck-Mandan area for structural construction applications, such as sub-bases for residential and commercial businesses, and excavatable fill applications, such as gas line and utility trench filling. (2) The cost of the MDU flowable fill product must be lower than the current $35-$45/cubic yard price if it is to become a common construction material. Formulations using MDU ash and lower-cost sand alternatives offer that opportunity. An estimated market of 10,000 cubic yards of MDU flowable fill products could be realized if prices could be made competitive. (3) The geotechnical properties of the MDU ash-based flowable fill can be modified to meet the needs of a range of applications from structural fill applications to excavatable applications, such as utility trench fill. (4) Environmental assessments using standard testing indicate that the environmental properties of the fill materials are compatible with numerous construction applications and do not pose a threat to either adjacent groundwater or soils. (5) WRI developed an Environmental Field Simulator (EFS) method for assessing the impact of flowable fill materials on adjacent soils and found that the zone of impact is less than a couple of inches, thereby posing no threat to adjacent soils. (6) Field-scale demonstrations of the MDU flowable fill were constructed and were successful for structural, as well as excavatable applications. Monitoring has demonstrated the geotechnical performance, environmental performance, and compatibility with common embed materials with the MDU flowable fill products. Technical and economic issues were identified that may hinder the commercial acceptance of MDU flowable fill materials, including: (1) the ability to produce a consistent product; (2) the ability to provide a product year round (cold weather retards strength development); and (3) the ability to evaluate and produce commercial quantities of MDU flowable fill using inexpensive materials.

Alan E. Bland

2003-09-30T23:59:59.000Z

319

Task 50 - deposition of lignites in the Fort Union Group and related strata of the northern Great Plains  

SciTech Connect (OSTI)

Late Cretaceous, Paleocene, and early Eocene geologic and paleontologic studies were undertaken in western North Dakota, eastern and south-central Montana, and northwestern and northeastern Wyoming. These study areas comprise the Williston, Bighorn, and Powder River Basins, all of which contain significant lignite resources. Research was undertaken in these basins because they have the best geologic sections and fossil record for the development of a chronostratigraphic (time-rock) framework for the correlation of lignite beds and other economic resources. A thorough understanding of the precise geologic age of the deposition of sediments permits a powerful means of interpreting the record of geologic events across the northern Great Plains. Such an understanding allows for rigorous interpretation of paleoenviromnents and estimates of resource potential and quality in this area of economically significant deposits. This work is part of ongoing research to document change in the composition of molluscan fossil faunas to provide a paleoenvironmentally sensitive independent means of interpreting time intervals of brief duration during the Late Cretaceous, Paleocene, and Eocene. This study focuses on the record of mollusks and, to a lesser extent, mammals in the (1) Hell Creek-Tullock Formations, which include the Cretaceous-Paleocene boundary, in the western portion of the Williston Basin, Montana; (2) uppermost Cretaceous, Paleocene, and lowermost Eocene strata in western North Dakota, which -includes the last interior seaway in North Dakota; (3) upper Paleocene and lowermost Eocene of the northern portion of the Bighorn Basin of south-central Montana and northwestern Wyoming; and (4) Powder River Basin of northeastern Wyoming and southeastern Montana. The geologic record provides different physical and paleontological information to aid in interpreting the geologic record through the study interval.

Hartman, J.H.; Roth, B.; Kihm, A.J.

1997-08-11T23:59:59.000Z

320

Aspects of coal pyrogenation with high heating rates  

SciTech Connect (OSTI)

The present paper describes the conversion of different rank coals into coke of required quality, influenced by heating rate variation. The study has been made for romanian coals and the imported coals too. Theoretical aspects of the coking process kinetics with special practical applications are shown. In Romania, classical coke making technology involves some theoretical and practical problems because of the local coal supply, weak in coking coals. Petrographical methods, as a complementary source of information for coking mechanisms understanding were used, for blends with high content of weakly coking coals. The results reveal the importance of rank and petrographical composition determinations for complex blends making. The paper continues previous studies of coke making kinetics, influenced by heating rate variation. On the basis of the relationship between coal charge composition and coke structure, including its use in the blast furnace, the influence of an increase in heating rate on the structure of the coke produced from different rank and petrographical composition coals, was studied. The heating rates ranged between 3 and 40 C/min. The structural changes produced during pyrogenation were more evident for the heating rates: 3, 6, 10 and 40 C/min. Table 2 reveals the optical aspects of coke matrix and inertinitic inclusions evolution, that is, the differences in structure arrangement by changing the plastic phase characteristics due to the increase in the heating rate.

Panaitescu, C.; Barca, F. [Politehnica Univ., Bucharest (Romania); Predeanu, G.; Albastroiu, P. [Metallurgical Research Inst., Bucharest (Romania)

1994-12-31T23:59:59.000Z

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


321

Removal of Cu(II) and Ni(II) from aqueous solution by lignite-based humic acids  

SciTech Connect (OSTI)

The removal of Cu(II) and Ni(II) metal ions from an aqueous solution were investigated by using humic acids (HAs) in a batch arrangement. HAs were prepared by using alkaline extraction, following sedimentation and acidic precipitation from three Turkish lignites: Ilgin, Beysehir, and Ermenek. The interactions of Cu(II) and Ni(II) with solid HAs and influence of three parameters (initial metal concentration, solution pH and temperature) on the removal of metals were studied. Adsorption equilibrium was achieved in about 120 min for Cu(II) and Ni(II) ions. The sorption of Cu(II) and Ni(II) on the surface of HAs depended strongly on the pH, and increased with increasing pH and the initial concentration of metal. The sorption of Cu(II) was higher than that of Ni(II) for HAs. The equilibrium relationship between adsorbent and adsorbate is described by adsorption isotherms at a fixed temperature 35 {sup o}C, at pH about 4.0. The Langmuir adsorption isotherm was used to describe observed sorption phenomena. Adsorption isotherms and kinetics data of Cu(II) and Ni(II) ions removed by HAs are presented and discussed.

Arslan, G.; Cetin, S.; Pehlivan, E. [Selcuk University, Konya (Turkey). Dept. of Chemistry

2007-07-01T23:59:59.000Z

322

Environmental assessment of no remedial action at the inactive uraniferous lignite ashing sites at Belfield and Bowman, North Dakota  

SciTech Connect (OSTI)

The Belfield and Bowman sites were not included on the original congressional list of processing sites to be designated by the Secretary of Energy. Instead, the sites were nominated for designation by the Dakota Resource Council in a letter to the DOE (September 7, 1979). In a letter to the DOE (September 12, 1979), the state of North Dakota said that it did not believe the sites would qualify as processing sites under the Uranium Mill Tailings Radiation Control Act (UMTRCA) because the activities at the sites involved only the ashing of uraniferous lignite coal and the ash was shipped out of state for actual processing. Nevertheless, on October 11, 1979, the state of North Dakota agreed to the designation of the sites because they met the spirit of the law (reduce public exposure to radiation resulting from past uranium operations). Therefore, these sites were designated by the Secretary of Energy for remedial action. Because of the relatively low health impacts determined for these sites, they were ranked as low priority and scheduled to be included in the final group of sites to be remediated.

NONE

1997-06-01T23:59:59.000Z

323

Baseline risk assessment of ground water contamination at the inactive uriniferous lignite ashing site near Belfield, North Dakota  

SciTech Connect (OSTI)

This Baseline Risk Assessment of Ground Water Contamination at the Inactive Uraniferous Lignite Ashing Site Near Belfield, North Dakota, evaluates potential impacts to public health or the environment resulting from ground water contamination at the site where coal containing uranium was burned to produce uranium. The US Department of Energy`s Uranium Mill Tailings Remedial Action (UMTRA) Project is evaluating plans to remedy soil and ground water contamination at the site. Phase I of the UMTRA Project consists of determining the extent of soil contamination. Phase II of the UMTRA Project consists of evaluating ground water contamination. Under Phase II, results of this risk assessment will help determine what remedial actions may be necessary for contaminated ground water at the site. This risk assessment evaluates the potential risks to human health and the environment resulting from exposure to contaminated ground water as it relates to historic processing activities at the site. Potential risk is quantified for constituents introduced from the processing activities, and not for those constituents naturally occurring in water quality in the site vicinity. Background ground water quality has the potential to cause adverse health effects from exposure through drinking. Any risks associated with contaminants attributable to site activities are incremental to these risks from background ground water quality. This incremental risk from site-related contaminants is quantified in this risk assessment. The baseline risk from background water quality is incorporated only into the assessment of potential chemical interactions and the definition of the overall site condition.

NONE

1994-08-01T23:59:59.000Z

324

A study on the flow of molten iron in the hearth of blast furnace  

SciTech Connect (OSTI)

The flow of molten iron in the hearth of blast furnace was investigated by using a water model test and a numerical simulation. The water model apparatus was set up in order to evaluate the effects of coke size, coke bed structure, drain rate, and coke free space on the fluidity of molten iron through measurement of residence time and visualization of flow pattern. In addition, the flow was calculated by solving momentum equation in porous media using finite element method. The residence time increased with the coke size decrease, but decreased with the drain rate increase. If small coke was placed in the center of deadman, peripheral flow was enhanced. The flow path was changed due to the coke free space.

Suh, Y.K.; Lee, Y.J.; Baik, C.Y. [Pohang Iron and Steel Co., Ltd. (Korea, Republic of). Technical Research Labs.

1996-12-31T23:59:59.000Z

325

Characterization of the mineralogy of the oxidized portion of the overburden and relation of pre-mine mineralogy to success of post-mine reclamation at a lignite mine near Jewett, Texas  

E-Print Network [OSTI]

in general and in certain lignite mines in specific. However, the field of study is not closed and the body of knowledge continues to increase. The study of the mineralogy at the Jewett lignite mine and its relation to reclamation processes was part of a.... (Diogenes could have saved himself and his lamp a lot of havel if they had started in College Station. ) Hail to the field Chiefs: Dr. "dirt" Kenny White and "Dr. Mud" David White. I can truly say that Dave gave me direction ? the direction North...

Oliver, Julie

1993-01-01T23:59:59.000Z

326

Supplement of Atmos. Chem. Phys., 14, 65716603, 2014 http://www.atmos-chem-phys.net/14/6571/2014/  

E-Print Network [OSTI]

for coal-charging process 0 0 0 0 10 10 0 FGD for coke oven gas 0 0 0 0 10 10 0 Combination[1] BAU[2]/PC[2] 2005 2010 2020 2030 2020 2030 2030 Sintering FGD 0 10 20 40 95 100 100 Coke oven FGD 100 Hot rolling ESP 0 0 0 0 70 95 100 Cold rolling HED 0 0 0 0 70 95 100 Coke oven WET 100 100 100 100

Pierce, Jeffrey

327

Prolongation technologies for campaign life of tall oven  

SciTech Connect (OSTI)

In Kashima Steel Works, 25-year-old 7-meter-high coke ovens have damage on their walls. However, by using new methods of internal in-situ investigation, ceramic welding for the extended central and upper portions of coke ovens has prolonged the campaign life for over 40 years without large-scale hot repair. In this paper, introduction of these new methods, its application in Kashima and the policy of repairing the tall coke oven are reported.

Doko, Yoshiji; Saji, Takafumi; Kitayama, Yoshiteru; Yoshida, Shuhei [Sumitomo Metal Industries, Ltd., Kashima, Ibaraki (Japan). Kashima Steel Works

1997-12-31T23:59:59.000Z

328

Estimating Total Energy Consumption and Emissions of China's Commercial and Office Buildings  

E-Print Network [OSTI]

Primary Electricity Coal Final energy use in buildings is9 million tonnes of coal equivalent energy could be saved byproportion of energy consumed from coal, coke, liquid fuels,

Fridley, David G.

2008-01-01T23:59:59.000Z

329

CALDERON COKEMAKING PROCESS/DEMONSTRATION PROJECT  

SciTech Connect (OSTI)

This project deals with the demonstration of a coking process using proprietary technology of Calderon, with the following objectives geared to facilitate commercialization: (i) making coke of such quality as to be suitable for use in hard-driving, large blast furnaces; (ii) providing proof that such process is continuous and environmentally closed to prevent emissions; (iii) demonstrating that high-coking-pressure (non-traditional) coal blends which cannot be safely charged into conventional by-product coke ovens can be used in the Calderon process; and (iv) demonstrating that coke can be produced economically, at a level competitive with coke imports. The activities of the past quarter were focused on the following: ? Consolidation of the project team-players; ? Recruiting Koppers Industries as an additional stakeholder; ? Developing a closed system for the production of binder pitch from tar in the Calderon coking process as the incentive for Koppers to join the team; ? Gathering appropriate equipment for conducting a set of experiments at bench scale to simulate tar quality produced from the Calderon coking process for the production of binder pitch; and ? Further progress made in the design of the commercial coking reactor.

ALBERT CALDERON

1998-09-22T23:59:59.000Z

330

SILICON--1997 68.1 By Thomas S. Jones  

E-Print Network [OSTI]

or quartzite) and costs of energy, reductant coke or low ash coal, iron in the form of steel scrap (if required

331

A Guidebook for Low-Carbon Development at the Local Level  

E-Print Network [OSTI]

Coal mining (production) Cement Iron-making Steel-making Electricity Pulp & paper Alcohol Monosodium glutamate Electrolytic aluminum Citric acid Coking

Zhou, Nan

2012-01-01T23:59:59.000Z

332

Refines Efficiency Improvement  

SciTech Connect (OSTI)

Refinery processes that convert heavy oils to lighter distillate fuels require heating for distillation, hydrogen addition or carbon rejection (coking). Efficiency is limited by the formation of insoluble carbon-rich coke deposits. Heat exchangers and other refinery units must be shut down for mechanical coke removal, resulting in a significant loss of output and revenue. When a residuum is heated above the temperature at which pyrolysis occurs (340 C, 650 F), there is typically an induction period before coke formation begins (Magaril and Aksenova 1968, Wiehe 1993). To avoid fouling, refiners often stop heating a residuum before coke formation begins, using arbitrary criteria. In many cases, this heating is stopped sooner than need be, resulting in less than maximum product yield. Western Research Institute (WRI) has developed innovative Coking Index concepts (patent pending) which can be used for process control by refiners to heat residua to the threshold, but not beyond the point at which coke formation begins when petroleum residua materials are heated at pyrolysis temperatures (Schabron et al. 2001). The development of this universal predictor solves a long standing problem in petroleum refining. These Coking Indexes have great potential value in improving the efficiency of distillation processes. The Coking Indexes were found to apply to residua in a universal manner, and the theoretical basis for the indexes has been established (Schabron et al. 2001a, 2001b, 2001c). For the first time, a few simple measurements indicates how close undesired coke formation is on the coke formation induction time line. The Coking Indexes can lead to new process controls that can improve refinery distillation efficiency by several percentage points. Petroleum residua consist of an ordered continuum of solvated polar materials usually referred to as asphaltenes dispersed in a lower polarity solvent phase held together by intermediate polarity materials usually referred to as resins. The Coking Indexes focus on the amount of these intermediate polarity species since coke formation begins when these are depleted. Currently the Coking Indexes are determined by either titration or solubility measurements which must be performed in a laboratory. In the current work, various spectral, microscopic, and thermal techniques possibly leading to on-line analysis were explored for measuring the Coking Indexes.

WRI

2002-05-15T23:59:59.000Z

333

EA-0404: Finding of No Significant Impact  

Broader source: Energy.gov [DOE]

Innovative Clean Coal Technology Program - Coke Oven Gas Cleaning Demonstration Project at the Bethlehem Steel Corp. Sparrows Point Plant, Baltimore County, Maryland

334

A Spectrum Of Potentially Diamondiferous Lamproites And Minettes...  

Open Energy Info (EERE)

fluids derived from the magmas themselves, from carbonatite-like fluids, and perhaps from coking of the invaded coal seams. Minor crystal fractionation within sills as little as...

335

Inventory of China's Energy-Related CO2 Emissions in 2008  

E-Print Network [OSTI]

Diesel Oil Fuel Oil LPG Refinery Gas Other PetroleumPipelines. All still gas/refinery gas in China is reportedlubricants petroleum coke refinery feedstock still gas/

Fridley, David

2011-01-01T23:59:59.000Z

336

Key China Energy Statistics 2011  

E-Print Network [OSTI]

Washing Coking Petroleum Refineries Gas Works Gas Works -Gas Petroleum Other Products Refinery Production by ProductGas Petroleum Other Products Refinery Gas Consumption Total

Levine, Mark

2013-01-01T23:59:59.000Z

337

Characterization of carbon dissolution from the new Auscarb clean carbon for ironmaking  

SciTech Connect (OSTI)

In the foundry industry, the recarburizing materials used can range from high purity graphite to chars. The dissolution performance of recarburizing materials is critical to the industry, as it has a direct bearing on productivity. In this study, the dissolution performance of a variety of clean Auscarb carbon materials has been determined to assess their suitability as recarburizing material. The carbon sources investigated were graphite (synthetic), coke A (2.5 and 18 hr), coke B (2.5, 3 and 18 hr) and coke C (2.5 hr). In addition, the effect of melt sulfur content and coke supplier (ACIRL or CSIRO laboratories) on dissolution performance was examined. Dissolution performance was characterized on the basis of the measured rate constant. The experimental investigation conducted in this study has established the trend in performance of the carbons. The results show that, for a fixed melt sulfur content of 0.2%, synthetic graphite was the best, although the dissolution performance of coke B approaches half that of synthetic graphite. The performance of cokes A and C fall slightly behind that of coke B. The cokes supplied from different sources were found to have similar dissolution performance only on extended coking times. Decreased melt sulfur content was found to increase the dissolution rate, and it was found that the extent of improvement was influenced by the nature of the carbonaceous material.

Sahajwalla, V.; Farrell, K.; Gao, K. [Univ. of New South Wales, Sydney, New South Wales (Australia); Waugh, B. [CSIRO, North Ryde, New South Wales (Australia). Div. of Coal and Energy Technology; Roberts, C. [Australian Coal Industry Research Labs. Ltd., North Ryde, New South Wales (Australia); Langley, J.M. [White Mining Ltd., North Sydney, New South Wales (Australia)

1995-12-01T23:59:59.000Z

338

Development of an Energy Conservation Voluntary Agreement, Pilot Project in the Steel Sector in Shandong Province. Project Report to the State Economic and Trade Commission, People's Republic of China  

E-Print Network [OSTI]

sintering, pelleting), ironmaking, steelmaking (basic oxygenfor steelmaking covers ironmaking (including coking andEE_..) The six spreadsheets (ironmaking, BOF, EAF, Casting,

Price, Lynn; Yun, Jiang; Worrell, Ernst; Wenwei, Du; Sinton, Jonathan E.

2003-01-01T23:59:59.000Z

339

Battery operation experience at SSAB, Luleaa six years after rehabilitation  

SciTech Connect (OSTI)

SSAB operates a coke oven plant in Luleaa, Sweden, consisting of one 7 m battery. Pushing the first coke in 1975, the battery encountered over the years more and more difficulties in keeping coking time and operation level at the design rate. In order to improve the coke supply a major repair of the battery was made. In 1989 the battery was fully rehabilitated by Krupp Koppers. The experience made during the years before and during repair contributed to a new policy for the operation of the plant. The policy has led to considerable improvements. It is clear that it is possible to successfully operate a rehabilitated battery.

Petrini, H.; Sundgren, M. [SSAB Tunnplaat, Luleaa (Sweden); Meyer, G. [Krupp Koppers GmbH, Essen (Germany)

1995-12-01T23:59:59.000Z

340

Development of an Advanced Combined Heat and Power (CHP) System...  

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

an Advanced Combined Heat and Power (CHP) System Utilizing Off-Gas from Coke Calcination - Fact Sheet, 2011 Development of an Advanced Combined Heat and Power (CHP) System...

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


341

January 2013 Most Viewed Documents for Environmental Sciences...  

Office of Scientific and Technical Information (OSTI)

Karlsruhe GmbH, Institut fuer Neutronenphysik und Reaktortechnik, Karlsruhe (Germany) Microbial rehabilitation of soils in the vicinity of former coking plants;...

342

RE-WEAVING A DECOLONIZED SOUTH IN CONTEMPORARY CHEROKEE WOMEN'S POETRY.  

E-Print Network [OSTI]

??Appalachian Cherokee women writers Marilou Awiakta, Allison Adelle Hedge Coke, and MariJo Moore have recently created poems reminiscent of an important Cherokee female tradition: basketweaving.… (more)

Cornell, Caleigh Breanne

2014-01-01T23:59:59.000Z

343

Improving the Carbon Dioxide Emission Estimates from the Combustion of Fossil Fuels in California  

E-Print Network [OSTI]

product consumption Nat Gas NGL Additives Crude Tot Pet.Pet Coke Lubricants Asphalt Waxes Special Naphtha Petrochem feedstocks Other Petro Prods Coal Net reconciliation error Total Consumption

de la Rue du Can, Stephane

2010-01-01T23:59:59.000Z

344

Rice Hull Silica, A Silicon Carbide Precursor For Collagen, Lignin And Silicon Metal Powder Bindered Anthracite Briquettes.  

E-Print Network [OSTI]

??Foundry coke is currently the primary energy source of U.S. iron foundries employing cupolas to produce iron. The availability, cost and environmental impact of this… (more)

Jiles, Allura

2013-01-01T23:59:59.000Z

345

A Review of Hazardous Chemical Species Associated with CO2 Capture from Coal-Fired Power Plants and Their Potential Fate in CO2 Geologic Storage  

E-Print Network [OSTI]

from combustion and gasification of coal – an equilibriumHolysh, M. 2005. Coke Gasification: Advanced technology forfrom a Coal-Fired Gasification Plant. Final Report, December

Apps, J.A.

2006-01-01T23:59:59.000Z

346

E-Print Network 3.0 - australian bituminous coal Sample Search...  

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

extractable material from perhydrous vitrinites Summary: an important role in their coking ability 19. The development of a mobile phase during the bituminous coal... to...

347

E-Print Network 3.0 - abandoned coal mines Sample Search Results  

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

78 Economic Impact of Standard Reference Materials Summary: . Although many mines, coking plants, coal preparation plants, utilities, and refineries have their own... -4 2.2...

348

E-Print Network 3.0 - anthracite Sample Search Results  

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

Source: Fusiongnition Research Experiment (FIRE) Collection: Plasma Physics and Fusion 75 Coking properties of perhydrous low-rank vitrains. Influence of pyrolysis conditions...

349

E-Print Network 3.0 - aromatic aliphatic copolyester Sample Search...  

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

changes... . An investigation of the aromatic and aliphatic structural changes in the coking coals during carbonisation using... of heat treated coal in relation to the...

350

E-Print Network 3.0 - australian bread wheat Sample Search Results  

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

Salad, Pimento Cheese, Ham & Turkey Served on White and Wheat Bread Pickle Potato Chips Cookie Coke Source: Consortium for Fossil Fuel Science, C1 Chemistry Program...

351

China Energy Databook - Rev. 4  

E-Print Network [OSTI]

1992: Power Generation Coal Consumption Allocated to End-Use1992: Power Generation Coal Consumption Allocated to End-Useused in electricity generation, coking, coal gas production,

Sinton Editor, J.E.

2010-01-01T23:59:59.000Z

352

Automação no controle do tempo de coqueificação em baterias de coque-siderurgia.  

E-Print Network [OSTI]

??This work presents the architecture of hardware, software and the results of implantation of a steel industrial automation environment, specifically in the group of Coke… (more)

Nilson Magalhães Bueno

2012-01-01T23:59:59.000Z

353

Sedimentology, Stratigraphy and Petrography of the Permian-Triassic Coal-bearing New Lenton Deposit, Bowen Basin, Australia .  

E-Print Network [OSTI]

??The Bowen Basin is one of the most intensely explored sedimentary basins in Australia and hosts one of the world’s largest coking coal deposits. This… (more)

Coffin, Lindsay M.

2013-01-01T23:59:59.000Z

354

Pitch Production Using Solvent Extraction of Coal: Suitability as Carbon Anode Precursor.  

E-Print Network [OSTI]

??Albertan coal has been used to produce extracts as precursor for production of anode coke. Coal extractability was studied using digestion with Tetralin in a… (more)

Mohammad Ali Pour, Mehdi

2009-01-01T23:59:59.000Z

355

brwtp-icoke | netl.doe.gov  

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

(Dec 1989) Comprehensive Report to Congress Comprehensive Report to Congress on the Clean Coal Technology Program: Innovative Coke Oven Gas Cleaning System for Retrofit...

356

Fact #863 March 9, 2015 Crude Oil Accounts for the Majority of...  

Energy Savers [EERE]

natural gas (12%). The remaining sources of primary energy imports: coal, coal coke, biofuels, and electricity only made up about 2% of all imports. Primary energy exports are...

357

The Role of the Flexicoking Process in Heavy Oil Processing  

E-Print Network [OSTI]

is transferred by crr FLUID COKING process, which in turn built on the culating coke from the exothermic reaction t~king fluid solids experience accumulated in cat crack- i place in the gasifier to the endothermic reaftion ing since the second world war... liquid volume basis. Virtually all of the energy input to the process comes from the exothermic reaction taking place in the gasification of the coke. Thus, oxidation of coke supplies the energy for con version to 1ight products, and no premium fuel...

Taylor, R. I.

1980-01-01T23:59:59.000Z

358

PETROLEUM AND PETROLEUM/COAL BLENDS AS FEEDSTOCKS IN LABORATORY-SCALE AND PILOT-SCALE COKERS TO OBTAIN CARBONS OF POTENTIALLY HIGH VALUE.  

E-Print Network [OSTI]

??The main goal of this research is to understand how the chemical composition of the feedstock and reactor design affects the quality of the coke… (more)

Escallon, Maria

2008-01-01T23:59:59.000Z

359

The recovery of purified coal from solution.  

E-Print Network [OSTI]

??A new process is being developed to produce graphite from prime coking coal. Coal is dissolved in dimethylformamide (DMF), on addition of sodium hydroxide. The… (more)

Botha, Mary Alliles

2008-01-01T23:59:59.000Z

360

E-Print Network 3.0 - acute ammonia challenge Sample Search Results  

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

Asia (coastal China, Korea and Japan) and Western Europe - experienced most acutely... Germany and the UK were also the world's leading producers of ammonia recovered from coke...

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


361

By-Products Utilization  

E-Print Network [OSTI]

wood with supplementary fuels such as coal, oil, natural gas, and coke by pulp and paper mills and wood, knots, chips, etc. with other supplementary fuels such as coal, oil, natural gas, and coke to generateCenter for By-Products Utilization DEVELOPMENT OF CLSM USING COAL ASH AND WOOD ASH, A SOURCE OF NEW

Wisconsin-Milwaukee, University of

362

Carbon Vol. 28, Nos. 213. pp. 261-279, 1990 Printed in Great Britain.  

E-Print Network [OSTI]

: carbon formation from catalyzed CO decomposition over iron and from liquid phase coking of hydrocarbons. preparation of carbons via catalytic cracking of CO and coking processes, 2. carbon active sites of concern. In par- ticular. we envisioned gasifying plentiful anthracite coal, with its attendant mineral matter

363

Neutrons for Catalysis: A Workshop on Neutron Scattering Techniques for Studies in Catalysis  

E-Print Network [OSTI]

-EM Fischer Tropsch Catalysis on Fe- or Co-catalysts, ,,CTL" Coal to Liquids ­ ,a rough (?) analogy #12;Peter Albers, AQ-EM Carbonaceous Deposits on Catalysts #12;Peter Albers, AQ-EM IINS on Coked Catalysts from Industrial Plants High-temperature and low-temperature cokes deposited on catalysts during

Pennycook, Steve

364

PressurePressure Indiana Coal Characteristics  

E-Print Network [OSTI]

TimeTime PressurePressure · Indiana Coal Characteristics · Indiana Coals for Coke · Coal Indiana Total Consumption Electricity 59,664 Coke 4,716 Industrial 3,493 Major Coal- red power plantsTransportation in Indiana · Coal Slurry Ponds Evaluation · Site Selection for Coal Gasification · Coal-To-Liquids Study, CTL

Fernández-Juricic, Esteban

365

Briefing Note 2010 22 19 November 2010  

E-Print Network [OSTI]

for cement production in 2008 came from coal and petroleum coke.iii Given the percentage of GHGs produced of alternative fuels involves replacing conventional fuels (mainly coal and petroleum coke), with alternative in efficiencies because of high-energy prices and low coal availability. A major limitation of increased thermal

Pedersen, Tom

366

JOURNALDE PHYSIQUE IV ColloqueC7, supplkmentau Journal de Physique 111, Volume3,novembre 1993  

E-Print Network [OSTI]

to that of a mixture of light benzene and bitumious coal tar if the pyrolysis gas is used as fluidizing gas. The other in the gas conditioning. Furthermore, the pollutants are concentrated in a coke-like residue surrounding them in melting vessels, blast furnaces, autoclaves, tube reactors, rotary kilns, coking chambers and fluidized

Paris-Sud XI, Université de

367

Project Sponsors: California Energy Commission  

E-Print Network [OSTI]

Generation: H2 from Natural Gas (SMR) H2 from Petroleum Coke H2 from Coal with Carbon Capture H2 from from Natural Gas (SMR) H2 from Petroleum Coke H2 from Coal with Carbon Capture H2 from Renewable

Mease, Kenneth D.

368

Energy conservation and efficiency in Giprokoks designs at Ukrainian ferrous-metallurgical enterprises  

SciTech Connect (OSTI)

Energy conditions at Ukrainian ferrous-metallurgical enterprises are analyzed. Measures to boost energy conservation and energy efficiency are proposed: specifically, the introduction of systems for dry slaking of coke; and steam-gas turbines that employ coke-oven gas or a mixture of gases produced at metallurgical enterprises. Such turbines may be built from Ukrainian components.

M.I. Fal'kov [Giprokoks, the State Institute for the Design of Coke-Industry Enterprises, Kharkov (Ukraine)

2009-07-15T23:59:59.000Z

369

F90 Journal of The Electrochemical Society, 160 (2) F90-F93 (2013) 0013-4651/2013/160(2)/F90/4/$28.00 The Electrochemical Society  

E-Print Network [OSTI]

materials, Ni-cermets, are susceptible to coking in many coal- and bio-derived syngas compositions,2, and coking behavior in surrogate coal gas fuel compositions have been reported.21 In order to understand. Solid oxide fuel cells (SOFCs) are well suited to replace coal com- bustion technologies because higher

Poeppelmeier, Kenneth R.

370

www.eprg.group.cam.ac.uk EPRGWORKINGPAPERNON-TECHNICALSUMMARY  

E-Print Network [OSTI]

, most cement kilns today use coal and petroleum coke as primary fuels, whereas aluminum smelters-energy purposes, such as coking coal, petrochemical feedstocks, or lubricants, have few available substitutes are based on electrochemical operational processes. Therefore, observable substitution of coal

de Gispert, Adrià

371

In: . Proceedings of the 91st Annual Meeting (held June 14-18 in San Diego, CA), Air and Waste Management Association, Pittsburgh, Pennsylvania, June 1998 (CD-ROM). 1998 H.C. Frey  

E-Print Network [OSTI]

natural gas, petroleum residuals, petroleum coke, refinery wastes, and coal as inputs. In recent years 27695-7908 ABSTRACT Gasification systems, such as coal-based integrated gasification combined cycle there is currently a lack of high-value markets for low-value liquid residues and coke.(2) Integrated Gasification

Frey, H. Christopher

372

Invariant solutions of two models of evolution of turbulent bursts  

E-Print Network [OSTI]

) represents a version arising in the so-called coal-coke problem. In the latter model, let us present a short of heat Q. Let T #3; #21; 0 be the critical ignition temperature of the coal-coke transformation. Assuming]. Consider the heat wave propagation in a plane thin coal layer in R 2 generated by the initial amount

Bath, University of

373

Atmos. Chem. Phys., 7, 35873596, 2007 www.atmos-chem-phys.net/7/3587/2007/  

E-Print Network [OSTI]

on the emis- sion data in Seoul and Northeast Asia: Gasoline and diesel vehicles, residential coal use, coke daily and seasonal variations. High contributions of biomass burning and coal (residential and coke oven ovens, coal power plants, biomass burning, and natural gas (NG) combustion. The ma- jor sources

Meskhidze, Nicholas

374

By-Products Utilization  

E-Print Network [OSTI]

in a combination with a number of fuels including coal, petroleum coke, natural gas, etc. In the mid 1990s, the unit was firing a combination of coal and petroleum coke to generate energy. It has been established;1 PROJECT 1 - COAL COMBUSTION BY-PRODUCTS: CHARACTERIZATION AND USE OPTIONS Introduction An AFBC system

Wisconsin-Milwaukee, University of

375

Presented by Lemonade $3.00  

E-Print Network [OSTI]

or Coke Zero Tazo Iced Tea $4.00 Zen Green or Peach Black Izze Sparkling Juices $4.00 Clementine, Sprite or Coke Zero Tazo Iced Tea $4.00 Zen Green or Peach Black Izze Sparkling Juices $4.00 Clementine.00 Noodles Marinated in Sesame Dressing, Mixed Greens, Crisp Cut Veggies and a light ginger rice vinegar

Hampton, Randy

376

To place your meal order please dial MEAL (ext. 6325) Room Service is available from 6:30am6:30pm  

E-Print Network [OSTI]

White Rice Rice Pilaf Green Beans Butternut Squash Carrots Broccoli California/Decaf Coffee Tea/Decaf Tea/Herbal Tea Hot Cocoa/SugarFree Hot Cocoa Iced Tea Ice Water Milk: Skim, 2%,Whole, Chocolate, Lactaid, Soymilk : Coke, Diet Coke, Sprite

Oliver, Douglas L.

377

Toplaceyourmealorder,pleasedial MEAL(ext.6325)  

E-Print Network [OSTI]

/Gravy SouthwestVegetarianChili Pasta:RotiniorWholeWheatPennewith Marinara Meatballs FromtheGrill: GrilledSalad PeanutButter&Jelly BreadsWhite,Wheat,Rye,KaiserRoll Extras:Coke/DietCoke,Sprite/DietSprite,Gingerale/Diet Gingerale BREAKFASTITEMS: LowCholesterolEggSubstitute TurkeySausage FrenchToast Pancakes CreamofWheat

Oliver, Douglas L.

378

TRP0033 - PCI Coal Combustion Behavior and Residual Coal Char Carryover in the Blast Furnace of 3 American Steel Companies during Pulverized Coal Injection (PCI) at High Rates  

SciTech Connect (OSTI)

Combustion behavior of pulverized coals (PC), gasification and thermal annealing of cokes were investigated under controlled environments. Physical and chemical properties of PCI, coke and carbon residues of blast furnace dust/sludge samples were characterized. The strong influence of carbon structure and minerals on PCI reactivity was demonstrated. A technique to characterize char carryover in off gas emissions was established.

Veena Sahajwalla; Sushil Gupta

2005-04-15T23:59:59.000Z

379

Calderon cokemaking process/demonstration project  

SciTech Connect (OSTI)

The Clean Air Act Amendments of 1990 set new emission standards for hazardous air pollutants from coke ovens. Congress, recognizing that the coke industry faces technological and financial difficulties in meeting these new, stringent emission standards, required the U.S. Environmental Protection Agency and DOE to conduct a joint six-year research and development program to assist the industry in developing and commercializing new technologies and work practices that would significantly reduce hazardous coke oven emissions. DOE`s purpose for sponsoring the proposed demonstration project is to provide the coke industry with a new option for the economical production of high quality coke that significantly reduces the quantity of pollutants entering the environment.

NONE

1995-10-01T23:59:59.000Z

380

"Code(a)","End Use","Total","Electricity(b)","Fuel Oil","Diesel Fuel(c)","Natural Gas(d)","NGL(e)","Coke and Breeze)","Other(f)"  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia, Virginia:FAQ <Information Administration (EIA) 10 MECSPropaneResidential"Total" "(Data051.32

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


381

"Code(a)","End Use","for Electricity(b)","Fuel Oil","Diesel Fuel(c)","Natural Gas(d)","NGL(e)","Coke and Breeze)"  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia, Virginia:FAQ <Information Administration (EIA) 10 MECSPropaneResidential"Total" "(Data051.324

382

"End Use","Total","Electricity(a)","Fuel Oil","Diesel Fuel(b)","Natural Gas(c)","NGL(d)","Coke and Breeze)","Other(e)"  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia, Virginia:FAQ <Information Administration (EIA) 10 MECSPropaneResidential"Total"2.4 Relative4 Relative226

383

Development of an advanced continuous mild gasification process for the production of co-products. Final report, September 1987--September 1996  

SciTech Connect (OSTI)

Char, the major co-product of mild coal gasification, represents about 70 percent of the total product yield. The only viable use for the char is in the production of formed coke. Early work to develop formed coke used char from a pilot plant sized mild gasification unit (MGU), which was based on commercial units of the COALITE plant in England. Formed coke was made at a bench-scale production level using MGU chars from different coals. An evolutionary formed coke development process over a two-year period resulted in formed coke production at bench-scale levels that met metallurgical industries` specifications. In an ASTM D5341 reactivity test by a certified lab, the coke tested CRI 30.4 and CSR 67.0 which is excellent. The standard is CRI < 32 and CSR > 55. In 1991, a continuous 1000 pounds per hour coal feed mild coal gasification pilot plant (CMGU) was completed. The gasification unit is a heated unique screw conveyor designed to continuously process plastic coal, vent volatiles generated by pyrolysis of coal, and convert the plastic coal to free flowing char. The screw reactor auxiliary components are basic solids materials handling equipment. The screw reactor will convert coal to char and volatile co-products at a rate greater than 1000 pounds per hour of coal feed. Formed coke from CMGU char is comparable to that from the MGU char. In pilot-plant test runs, up to 20 tons of foundry coke were produced. Three formed coke tests at commercial foundries were successful. In all of the cupola tests, the iron temperature and composition data indicated that the formed coke performed satisfactorily. No negative change in the way the cupola performed was noticed. The last 20-ton test was 100 percent CTC/DOE coke. With conventional coke in this cupola charging rates were 10 charges per hour. The formed coke charges were 11 to 12 charges per hour. This equates to a higher melt rate. A 10 percent increase in cupola production would be a major advantage. 13 figs., 13 tabs.

NONE

1996-12-31T23:59:59.000Z

384

Measurement of gas species, temperatures, coal burnout, and wall heat fluxes in a 200 MWe lignite-fired boiler with different overfire air damper openings  

SciTech Connect (OSTI)

Measurements were performed on a 200 MWe, wall-fired, lignite utility boiler. For different overfire air (OFA) damper openings, the gas temperature, gas species concentration, coal burnout, release rates of components (C, H, and N), furnace temperature, and heat flux and boiler efficiency were measured. Cold air experiments for a single burner were conducted in the laboratory. The double-swirl flow pulverized-coal burner has two ring recirculation zones starting in the secondary air region in the burner. As the secondary air flow increases, the axial velocity of air flow increases, the maxima of radial velocity, tangential velocity and turbulence intensity all increase, and the swirl intensity of air flow and the size of recirculation zones increase slightly. In the central region of the burner, as the OFA damper opening widens, the gas temperature and CO concentration increase, while the O{sub 2} concentration, NOx concentration, coal burnout, and release rates of components (C, H, and N) decrease, and coal particles ignite earlier. In the secondary air region of the burner, the O{sub 2} concentration, NOx concentration, coal burnout, and release rates of components (C, H, and N) decrease, and the gas temperature and CO concentration vary slightly. In the sidewall region, the gas temperature, O{sub 2} concentration, and NOx concentration decrease, while the CO concentration increases and the gas temperature varies slightly. The furnace temperature and heat flux in the main burning region decrease appreciably, but increase slightly in the burnout region. The NOx emission decreases from 1203.6 mg/m{sup 3} (6% O{sub 2}) for a damper opening of 0% to 511.7 mg/m{sup 3} (6% O{sub 2}) for a damper opening of 80% and the boiler efficiency decreases from 92.59 to 91.9%. 15 refs., 17 figs., 3 tabs.

Jianping Jing; Zhengqi Li; Guangkui Liu; Zhichao Chen; Chunlong Liu [Harbin Institute of Technology, Harbin (China). School of Energy Science and Engineering

2009-07-15T23:59:59.000Z

385

Pulverized coal injection (PCI) at Inland`s No. 7 blast furnace  

SciTech Connect (OSTI)

Fuel injection at the tuyeres has always been part of normal operating practice on this blast furnace. It has been used as much because of the beneficial effects on furnace operation as for the replacement of some of the coke that would otherwise be consumed. Fuel oil was used at first, but since the early 1980s it was more economical to inject natural gas. Studies in 1990 indicated that natural gas could be increased to 75 kg/tHM on No. 7 Furnace, and this would result in a coke rate of approximately 360 kg/tHM. It was apparent that coal injection offered significantly more opportunity for coke savings. Coke rate could be lowered to 300 kg/tHM with coal injected at 175 kg/tHM. Some combustion limitations were expected at that level. A coke rate of 270 kg/tHM with coal at 200 kg/tHM may be possible once these limitations are overcome. Furnace permeability was expected to limit the ability to reduce coke rate any further. In addition, the relative cost of coal would be significantly lower than the cost of coke it replaced. This lead to the decision late in 1991 to install pulverized coal injection (PCI) equipment for all of Inland`s blast furnaces. This paper will deal with PCI experience at No. 7 Blast Furnace.

Carter, W.L.; Greenawald, P.B.; Ranade, M.G.; Ricketts, J.A.; Zuke, D.A. [Inland Steel Co., East Chicago, IN (United States)

1995-12-01T23:59:59.000Z

386

CALDERON COKEMAKING PROCESS/DEMONSTRATION PROJECT  

SciTech Connect (OSTI)

This project deals with the demonstration of a coking process using proprietary technology of Calderon, with the following objectives geared to facilitating commercialization: (1) making coke of such quality as to be suitable for use in hard-driving, large blast furnaces; (2) providing proof that such process is continuous and environmentally closed to prevent emissions; (3) demonstrating that high-coking-pressure (non-traditional) coal blends which cannot be safely charged into conventional by-product coke ovens can be used in the Calderon process; and (4) demonstrating that coke can be produced economically, at a level competitive with coke imports. The activities of the past quarter were focused on three main activities: Continuation of design of the coking reactor; Raising funds from the private sector; and Detailed analysis of the tests conducted in Alliance, Ohio. The design of the reactor work centered on the provision for the capability to inspect and maintain the internals of the reactor. The activities relating to raising funds from the steel industry have been fruitful. Bethlehem Steel has agreed to contribute funds. The collected data from the tests at Alliance were analyzed and a detailed report was completed and presented to the International Iron & Steel Institute by invitation.

ALBERT CALDERON

1998-06-22T23:59:59.000Z

387

CALDERON COKEMAKING PROCESS/DEMONSTRATION PROJECT  

SciTech Connect (OSTI)

This project deals with the demonstration of a coking process using proprietary technology of Calderon, with the following objectives geared to facilitate commercialization: (i) making coke of such quality as to be suitable for use in hard-driving, large blast furnaces; (ii) providing proof that such process is continuous and environmentally closed to prevent emissions; (iii) demonstrating that high-coking-pressure (non-traditional) coal blends which cannot be safely charged into conventional by-product coke ovens can be used in the Calderon process; (iv) conducting a blast furnace test to demonstrate the compatibility of the coke produced; and (v) demonstrating that coke can be produced economically, at a level competitive with coke imports. The activities of the past quarter continued to be focused on the following: Concluding the Negotiation and completing Contracts among Stakeholders of the Team; Revision of Final Report for Phase I; Engineering Design Progress; Selection of Systems Associates, Inc. for design of Control System; Conclusion of Secrecy Agreement with Carborundum (St. Gobain); and Permitting Work and Revisions.

Albert Calderon

2000-03-22T23:59:59.000Z

388

Calderon cokemaking process/demonstration project  

SciTech Connect (OSTI)

This project deals with the demonstration of a coking process using proprietary technology of Calderon, with the following objectives geared to facilitate commercialization: (1) making coke of such quality as to be suitable for use in hard-driving, large blast furnaces; (2) providing proof that such a process is continuous and environmentally closed to prevent emissions; (3) demonstrating that high-coking-pressure (non-traditional) coal blends which cannot be safely charged into conventional by-product coke ovens can be used in the Calderon process; (4) conducting a blast furnace test to demonstrate the compatibility of the coke produced; and (5) demonstrating that coke can be produced economically, at a level competitive with coke imports. The activities of the past quarter continued to be focused on the following: Drafting of Contracts among the Stakeholders of the Team, Completion and Delivery of Proposal for Phase 2 Permitting and Environmental Work Engineering Progress Preparation of Final Report for Phase 1 DCAA Audit Funding for Phase 2.

Albert Calderon

1999-12-21T23:59:59.000Z

389

CALDERON COKEMAKING PROCESS/DEMONSTRATION PROJECT  

SciTech Connect (OSTI)

This project deals with the demonstration of a coking process using proprietary technology of Calderon, with the following objectives geared to facilitate commercialization: (i) making coke of such quality as to be suitable for use in hard-driving, large blast furnaces; (ii) providing proof that such process is continuous and environmentally closed to prevent emissions; (iii) demonstrating that high-coking-pressure (non-traditional) coal blends which cannot be safely charged into conventional by-product coke ovens can be used in the Calderon process; (iv) conducting a blast furnace test to demonstrate the compatibility of the coke produced; and (v) demonstrating that coke can be produced economically, at a level competitive with coke imports. The activities of the past quarter continued to be focused on the following: Concluding the Negotiation and completing Contracts among Stakeholders of the Team; Revision of Final Report for Phase I; Engineering Design Progress; Selection of Systems Associates, Inc. for design of Control System; Conclusion of Secrecy Agreement with Carborundum (St. Gobain); and Permitting Work and Revisions.

Albert Calderon

2000-06-21T23:59:59.000Z

390

Geologic and climatic controls on the formation of the Permian coal measures in the Sohagpur coal field, Madhya Pradesh, India  

SciTech Connect (OSTI)

The U.S. Geological Survey (USGS) and the Geological Survey of India (GSI) are concluding a cooperative study of the coking coal deposits in the Sohagpur coal field in central India. Because of the importance of coal in India's economy, the Coal Wing of the Geological Survey of India has studied the area intensely since the early 1980's. This report summarizes the overall stratigraphic, tectonic, and sedimentologic framework of the Sohagpur coal field area, and the interpretations of the geologic and climatic environments required for the accumulation of the thick Gondwana coal deposits, both coking and non-coking.

Milici, R.C.; Warwick, P.D.; Mukhopadhyah, A.; Adhikari, S.; Roy, S.P.; Bhattacharyya, S.

1999-07-01T23:59:59.000Z

391

StephenLeharne Thechemistryofocid  

E-Print Network [OSTI]

combuslionof 1o$rlInelsj Both coaL lnd oil combustion sill enir !ar!ing qurntniesof sulphurdioxidcand nnrogen Such proce$esinclude the relninC oI pefoleun.thesmchlngol metaloresand coking.lndeeda cof

Short, Daniel

392

Surface Science 123 ( 1982) 413-426 North-Holland Publishing Company  

E-Print Network [OSTI]

for the efficient utilization of our national energy resources through, for example, coal gasification the support's acidity or to catalyze coke removal via hydrogen or steam reactions [20]. At atmospheric

Goodman, Wayne

393

Synthetic Biology and reshaping plant form Jim Haseloff  

E-Print Network [OSTI]

Industrial Revolution: based on innovations in coal, iron, steam and mechanical engineering #12; Steam power machines.This enabled rapid development of e cient semi-automated factories Iron founding - Coke replaced

Rosso, Lula

394

DOI: 10.1002/cssc.201100798 Design of a Highly Nanodispersed PdMgO/SiO2  

E-Print Network [OSTI]

and coal combustion, which emits sub- stantial amounts of CO2--the most critical greenhouse gas.[3] Several by carbonaceous deposition on the active site, coking, and ag- glomeration of metal catalysts have been critical

Henkelman, Graeme

395

Journal of Colloid and Interface Science 267 (2003) 178193 www.elsevier.com/locate/jcis  

E-Print Network [OSTI]

[15]. Coke generation and asphaltene adsorption within catalytic cracking beds can reduce the effective cata- lyst surface area as well as the efficiency of coal hydropy- * Corresponding author. E

Kilpatrick, Peter K.

396

Overview of the Electrical Energy Segment of the Energy Information Administration/ Manufacturing Consumption Report  

E-Print Network [OSTI]

, liquefied petroleum gas, coke and breeze, coal, and electricity, only the electricity segment is overviewed. Along with pure electrical energy consumption information, newly available data covers methods that manufacturers used to purchase and modify...

Lockhead, S.

397

Peer Reviewed Archival Publications  

E-Print Network [OSTI]

-176. Bayraktar* , O. and E.L. Kugler. 2002. Characterization of coke on equilibrium fluid-catalytic- cracking. Characteristics and carbonization behaviors of coal extracts. Fuel Processing Technology 79: 207-215. Stiller, A

Mohaghegh, Shahab

398

Coal keeps the home fires burning, at a price  

SciTech Connect (OSTI)

The wild ride of 2007 thermal and coking coal and freight prices does not show any signs of abating as 2008 nears, leaving consumers coping with historic high costs, except in the US. 3 figs.

O'Connell, J.

2007-11-15T23:59:59.000Z

399

EIA - Annual Energy Outlook 2013 Early Release  

Gasoline and Diesel Fuel Update (EIA)

for by production from lower-cost mines in the West and higher price projections for coking coal. Electricity Following the recent rapid decline of natural gas prices, real...

400

Solid Oxide Fuel Cell Development at Topsoe Fuel Cell A/S and Ris National Laboratory  

E-Print Network [OSTI]

catalyst. The range of fuels has further been extended to include ethanol and coal syn-gas by development of a new coke resistant catalyst suitable for future SOFC technology. CELL DEVELOPMENT AND PRODUCTION

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


401

Electrodes for energy applications Development of improved high-performance electrodes is critically important to the efficiency  

E-Print Network [OSTI]

, longer and safer operation. Further developments of coking- and contaminant- tolerant anodes for solid of a wide variety of fuels, including hydrogen, hydrocarbon fuels, coal gas, and bio-derived fuels

Li, Mo

402

LITERATURE REPORT part of the MSc project  

E-Print Network [OSTI]

and the impact when improvements can be made. Typically, steel is made by melting iron ore with cokes, resulting on the whole process of steel making, starting from the resources iron ore and coal. The prediction of the nal

Vuik, Kees

403

Calderon Cokemaking Process/Demonstration Project  

SciTech Connect (OSTI)

This project deals with the demonstration of a coking process using proprietary technology of Calderon with the following objectives in order to enable its commercialization: (i) making coke of such quality as to be suitable for use in high driving (highly productive) blast furnaces; (ii) providing proof that such process is continuous and environmentally closed to prevent emissions; and (iii) demonstrating that high-coking-pressure (non-traditional) coal blends which cannot be safely charged into conventional by-product coke ovens can be used in the Calderon process. The activities of the past quarter were entirely focused on operating the Calderon Process Development Unit (PDU-I) in Alliance, Ohio conducting a series of tests under steady state using coal from Bethlehem Steel and U.S. Steel in order to demonstrate the above. The objectives mentioned above were successfully demonstrated.

None

1998-04-08T23:59:59.000Z

404

Pyrolysis in Porous Media:1 Part 1. Numerical model and parametric study.2  

E-Print Network [OSTI]

due to the formation of light species and heavy ones (up to solid coke particles). The1 presence by the formation of3 permeable char [10,11]. The coal pyrolysi

Boyer, Edmond

405

Adsorption of Hydrogen Sulfide onto Activated Carbon Fibers: Effect of  

E-Print Network [OSTI]

. These processes include natural gas processing, petroleum refining, petrochemical plants, Kraft mills, coke ovens, and coal gasifiers. H2S concentrations in these processes vary from 0 to 60 vol % (6). The Claus process

Borguet, Eric

406

Toward new solid and liquid phase systems for the containment, transport and delivery of  

E-Print Network [OSTI]

Storage Tube Trailer Liquid H2 Truck H2 Pipeline Multi-vehicle filling stations Feedstock: N. gas, Coal, Biomass Pet. Coke, Resids. Future: Carbon sequestration Storage: Underground well? Output: Depends

407

Rencontres Gosynthtiques -9-11 avril 2013, Dijon BASSIN HOUILLER LORRAIN : RHABILITATION DU TRIANGLE DE  

E-Print Network [OSTI]

: R�HABILITATION DU TRIANGLE DE MARIENAU, DES TRAVAUX � LA SURVEILLANCE LORRAIN COAL BASIN: TRIANGLE DE MARIENAU of France and Germany. At this place, the Houillères du Bassin de Lorraine coking plant process waters were

Paris-Sud XI, Université de

408

Separation of Fischer-Tropsch Wax from Catalyst Using Near-Critical Fluid Extraction: Analysis of Process  

E-Print Network [OSTI]

", can be produced from materials such as coal, natural gas, waste biomass, and petroleum coke. A great of coal and natural gas exist in many geographical regions that lack sufficient petroleum. Therefore

Kilpatrick, Peter K.

409

BEFORE THE ENERGY RESOURCES CONSERVATION AND DEVELOPMENT COMMISSION OF THE STATE OF CALIFORNIA  

E-Print Network [OSTI]

Combined-Cycle (IGCC) polygeneration technology. It would gasify a 75 percent coal and 25 percent petroleum coke (petcoke) fuel blend to produce synthesis gas (syngas). Syngas produced via gasification would

410

JOURNAL DE PHYSIQUEIV ColloqueC7, supplkmentau Journal de Physique111, Volume 3,novembre 1993  

E-Print Network [OSTI]

, the manufacturing of flat coated products involve many operations starting from the ore and coal: pyrometallurgy in coking and sinter plants, elaboration of liquid metal in blast-furnace and converter, solidification

Paris-Sud XI, Université de

411

e l e m e n t a l a n a l y s i s Carbon, Hydrogen, Nitrogen, Sulfur and Oxygen analyzers  

E-Print Network [OSTI]

Scientific FLASH 2000 Series Organic Elemental Analyzers Organic Chemistry & Pharmaceuticals Petrochemistry · Catalysts · Textiles · Pesticides · Detergents · Fluorine-compounds Organic/Inorganic Chemistry · Cokes · Crude oils · Gasoline/Diesel · Alternative fuels · Petroleum derivates · Lubricants · Oil

Wells, Mathew G. - Department of Physical and Environmental Sciences, University of Toronto

412

HOW TO LIVE (almost) FOREVER Justyna Derkach, UG Lab/Research  

E-Print Network [OSTI]

before you work with these. acrylonitrile arsenic asbestos benzene coke oven emissions ethylene from ABB Scientific Stores or Justyna ­ JHE-A106) #12;NASTIES (designated substances) More paperwork

Thompson, Michael

413

EA-1091: Calderon Cokemaking Process/Demonstration Project, Alliance, Ohio  

Broader source: Energy.gov [DOE]

This EA evaluates the environmental impacts of a proposal to evaluate a new design that allows coke production to occur in a completely closed system at the Calderon Energy Company, thus...

414

1 novembre 8, 2011 Title: The Employment Potential of Site Remediation Policies: a Micro-  

E-Print Network [OSTI]

, the first gathering gasworks and coke ovens and the other dealing with petrol filling stations. As regards are only beginning to design a policy. It is very likely that this will become a major policy issue

Paris-Sud XI, Université de

415

A Comparison of Iron and Steel Production Energy Use and Energy Intensity in China and the U.S.  

E-Print Network [OSTI]

energy use for the pellet production is fuel, so this valueof energy used for the production of pellets, the followingthe energy use for the production of pellet, lime, coke, and

Hasanbeigi, Ali

2012-01-01T23:59:59.000Z

416

Computer simulation of GTL and various problems in thermodynamics  

E-Print Network [OSTI]

simulation results show that methane conversion increases with higher reaction temperature and longer residence times. Hydrogen can both inhibit methane decomposition and reduce coke formation. The rich components in the natural gas are found to decompose...

Wang, Xiaonian

2005-08-29T23:59:59.000Z

417

An Explanation for the Lack of a Dilute Freshwater Lens in Unconfined Tropical Coastal Aquifers: Yucatan Example  

E-Print Network [OSTI]

by the Bay of Campeche, on the north by the Gulf of Mexico and on the east by the Caribbean Sea of Geological Societies Transactions, v. 56, p. 785-792. 785 #12;Stoessell and Coke Figure 1. Yucatan Peninsula

Stoessell, Ronald K.

418

Water Challenges for Geologic Carbon Capture and Sequestration  

E-Print Network [OSTI]

pet-coke or biomass) is ?rst gasi?ed, creating syngas. Usingshift reac- tion, the syngas can be chemically shifted; theto further cool the syngas before entering the Selexol

Newmark, Robin L.; Friedmann, Samuel J.; Carroll, Susan A.

2010-01-01T23:59:59.000Z

419

Method for making spherical binderless pellets  

DOE Patents [OSTI]

A method for making spherical binderless pellets using a rotating drum mixer whereby at least a portion of the particles comprising the pellets is comprised of coking coal particles.

Grubbs, Donald K. (Rector, PA); Kochanowski, Andrew T. (Spring Church, PA)

1983-01-01T23:59:59.000Z

420

Renewable Hydrogen: Technology Review and Policy Recommendations for State-Level Sustainable Energy Futures  

E-Print Network [OSTI]

and pipeline delivery. Clean Energy Group Other Renewable HydrogenHydrogen Cost Estimates (continued) Production Method Petroleum Coke Gasification kg/day $5.35/kg ($37.68/GJ) Central production Pipeline

Lipman, Timothy; Edwards, Jennifer Lynn; Brooks, Cameron

2006-01-01T23:59:59.000Z

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


421

STATE OF CALIFORNIA NATURAL RESOURCES AGENCY EDMUND G. BROWN JR., Governor CALIFORNIA ENERGY COMMISSION  

E-Print Network [OSTI]

,000 $750,000 86.7% Awardee 10 Kenworth Truck Company Deployment of a Next Generation Alternative Fuel Power-Cola Enterprises n Series Hydraulic-Hybrid Drivetrain Impleme Beverage Delivery Trucks ntation in Coke $750

422

Micromorphology and Stable Isotope Geochemistry of Historical Pedogenic Siderite Formed in PAH-Contaminated Alluvial Clay Soils, Tennessee, USA  

E-Print Network [OSTI]

Alluvial clay soil samples from six boreholes advanced to depths of 400–450 cm (top of limestone bedrock) from the Chattanooga Coke Plant (CCP) site were examined micromorphologically and geochemically in order to determine if pedogenic siderite (Fe...

Driese, S.G.; Ludvigson, Greg A.; Roberts, Jennifer A.; Fowle, David A.; Gonzalez, Luis A.; Smith, Jon Jay; Vulava, V.M.; McKay, L.D.

2010-11-01T23:59:59.000Z

423

EAST CAROLINA UNIVERSITY HAZARDOUS CHEMICAL USE GRANT REVIEW FORM ECU policy requires that all grant proposals involving the use of hazardous chemicals be reviewed by an institutional review committee or  

E-Print Network [OSTI]

-benezene 4-Aminodiphenyl Asbestos Coal tar pitch volatiles Methyl chloromethyl ether Formaldehyde Vinyl chloride Coke oven emissions 1,2-dibromo-3-chloropropane Lead Cadmium Benzene Cotton dust Chromium VI

424

SAS Output  

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

,,,,"Year to Date" "Commodity","April - June","January - March","April - June",2014,2013,"Percent" ,2014,2014,2013,,,"Change" "Coke" " Sales",1969,1865,1969,3834,3905,-1.8 "...

425

Inventory of China's Energy-Related CO2 Emissions in 2008  

E-Print Network [OSTI]

from Other (Public Sector) Energy Consumption Coal Coke andother(public) sector’s share of final energy consumption ofother(public) sector’s share of final energy consumption of

Fridley, David

2011-01-01T23:59:59.000Z

426

Work supported by the Department of Energy, UCLA and UCOP. LAPTAG, Encouraging High School students to Consider Physics Related  

E-Print Network [OSTI]

://coke.physics.ucla.edu/laptag and web service is provided to schools without servers or Internet access. LAPTAG encourages communication experiment in which ten schools received seismometers. LAPTAG provided a Web based astronomy class in which

California at Los Angles, University of

427

Analysis of Energy Savings by Painting a Rotary Kiln Surface  

E-Print Network [OSTI]

Rotary Kilns has been widely used for processing minerals, producing cement, calcining petroleum cokes, or drying biomass and wastes. Most of rotary kilns consume energy intensively. Therefore it is desired to assess the thermal losses from the kiln...

Li, X.; Wang, T.; Tonti, R. T.; Edwards, L.

2007-01-01T23:59:59.000Z

428

Identifying Opportunities for Industrial Energy Conservation  

E-Print Network [OSTI]

. Cement Making 5. Vacuum Distillation 4. Cooking 6. Hydrocracking 5. Glass Melting 7. Hydrogen Production 6. Copper Smelting 8. Hydrorefining/Hydrotreating 7. Miscellaneous 9. Visbreaking 10. Petroleum Coking 11. Desulfurization C. Iron and Steel I...

Hoffman, A. R.

1981-01-01T23:59:59.000Z

429

Concentration of carbon types from fly ash by density gradient centrifugation  

SciTech Connect (OSTI)

Although the increasing amount of unburned carbon in fly ash is known to preclude the use of ash in the cement industry, very little is known about the characteristics of the unburned carbon. Three types of carbon particles have been identified microscopically: inertinite, isotropic coke and anisotropic coke. This manuscript describes a method to isolate these three types of carbon. A preliminary enrichment, followed by density gradient centrifugation (DGC) with a high-density polytungstate media (2.85 g/cm{sup 3} max), resulted in an enrichment of inertinites from a starting concentration of 3.8% to 61%, isotropic coke from 13.4% to 65%, and anisotropic coke from 19.2% to 74%. Large scale runs (LS) have been conducted to accumulate sufficient sample for subsequent analyses. The recovery weights and petrography composition of the PS and LS fractions are very similar.

Maroto-Valer, M.M.; Taulbee, D.N.; Hower, J.C. [Univ. of Kentucky, Lexington, KY (United States). Center for Applied Energy Research

1998-12-31T23:59:59.000Z

430

Refinery Energy Profiling Procedure  

E-Print Network [OSTI]

Coolers Steam System Petroleum Coke Electrical System '" Cf) .Po Feed Streams Radiation and Convection Exothermic Reaction Products and Wastes Endothermic Reactions Oil Charge Losa 2 Oil and Gas Losses Subtotal Imbalance TOTAL TOTAL 560...

Maier, R. W.

1981-01-01T23:59:59.000Z

431

Quarterly coal report, April 1996--June 1996  

SciTech Connect (OSTI)

This report provides information about U.S. coal production, distribution; exports, imports, prices, consumption, and stocks. Data on coke production is also provided. This report presents data for April 1996 thru June 1996.

NONE

1996-11-01T23:59:59.000Z

432

Inventory of China's Energy-Related CO2 Emissions in 2008  

E-Print Network [OSTI]

of unadjusted energy-related CO2 emissions is attributed toEMISSIONS- T C EMISSIONS -T CO2 TOTAL Energy EmissionsEMISSIONS- T C EMISSIONS -T CO2 Coal Coke and Other

Fridley, David

2011-01-01T23:59:59.000Z

433

Estimation of Collection Efficiency Change of Moving Granular Bed Filter by Dust Load  

SciTech Connect (OSTI)

Final goal of this study is to theoretically describe effects of influencing factors on the performance of the coke bed filter as a material classifier and to predict its optimal operating condition. In this paper, the author focuses on the basic investigation on collection mechanism of a fixed coke bed filter on the basis of the depth filtration theory, in which an influence of dust load on the dust collection efficiency.

Furuuchi, M.; Hata, M.; Kanaoka, C.; Kawaminami, Y.

2002-09-18T23:59:59.000Z

434

Supplementary Information for Refined Estimate of China's CO2 Emissions in  

E-Print Network [OSTI]

.95-0.98); Weibull Other washed coal 0.96 (0.92-1); Triangular Briquettes 0.90 (0.89-0.98); Weibull IPCC( 2006); Coke coal 0.93 (0.89-0.98); Gamma IPCC( 2006); Cai et al. (2009); Zhao et al (2012) Cleaned coal 0.96 (0 0.93 (0.89-1); Triangular Coke Oven Gas 0.99 (0.98-1); Triangular Other Gas 0.99 (0

Meskhidze, Nicholas

435

Innovative Self- Generating Projects  

E-Print Network [OSTI]

Steam Driven Cooling Water Pump Blast Furnace Coke Plant Flares Boilers Steam Header Electric Cooling Water Pump (Back-up) Process Steam (Main Plant) Coal Hot Mill Reheat Furnace COG Bunker Oil ESL-IE-13-05-06 Proceedings... Driven Cooling Pump (New Back-up) Blast Furnace Coke Plant Flares Boilers Parastic Loads Natural Gas Turbine Steam Header Electric Cooling Water Pump (with Power Meter) Net ElectricityG Process Steam (Main Plant) Coal Hot Mill Reheat...

Kelly, L.

2013-01-01T23:59:59.000Z

436

Supplement of Atmos. Chem. Phys., 14, 56175638, 2014 http://www.atmos-chem-phys.net/acp-14-5617-2014/  

E-Print Network [OSTI]

.2 Industry Combustion Coal/Boiler, Kilns Liu et al. (2008), 1185 1185 1701.2 Coke Oven Blast Furnace Gas in the original INTEX-B NMVOC Emissions /Gg Power Coal 1178 1178 1130.7 Biofuel Tsai et al. (2003), Liu et al, 4421, 5561 (Andreae and Merlet, 2001) Tsai et al.(2003) 16.8 Industry Non-combustion Coke 11, 217 11

Meskhidze, Nicholas

437

Cokemaking from coals of Kuzbas and Donbas  

SciTech Connect (OSTI)

The paper discusses features of Donetsk and Kuznetsk coals, the export capability of Ukraine coking industry, the selection of coal blends involving coals from different basins, and practical recommendations and techno-economic considerations. It is concluded that by raising the share of low-sulfur Kuznetsk coal in the blend to 50%, coke produced will meet all the requirements of European and American consumers.

Umansky, R.Z. [Resourcecomplect, Donetsk (Ukraine); Kovalev, E.T.; Drozdnik, I.D. [UKHIN, Kharkov (Ukraine)

1997-12-31T23:59:59.000Z

438

Pushing schedule derivation method  

SciTech Connect (OSTI)

The development of a Pushing Schedule Derivation Method has allowed the company to sustain the maximum production rate at CSH`s Coke Oven Battery, in spite of having single set oven machinery with a high failure index as well as a heat top tendency. The stated method provides for scheduled downtime of up to two hours for machinery maintenance purposes, periods of empty ovens for decarbonization and production loss recovery capability, while observing lower limits and uniformity of coking time.

Henriquez, B. [Compania Siderurgica Huachipato S.A., Talcahuano (Chile)

1996-12-31T23:59:59.000Z

439

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. Biogenic

440

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.

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


441

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6.

442

Modification of environmental control of cokemaking plant  

SciTech Connect (OSTI)

Recently, global environmental protection has been a great concern in the world. In the United States of America, the Clean Air Act (CAA) has been revised to control emissions strictly. Especially in the field of cokemaking, the restriction of fume emission from a coke oven is so severe that old coke ovens will stop operation with the application of CAA. In Japan, it is expected that more severe protection measures are going to be requested for keeping environmental quality. In this situation, it is indispensable to strengthen environmental protection measures for cokemaking plants to continue coke production in the 21st century. In Chiba Works, Kawasaki Steep Corp., the Ironmaking Department has been struggling for the improvement of environmental measures for. These activities for coke ovens are described in this report. The paper describes fume emission control from the coke oven door and dust emission control measures, including the dust monitoring system, prevention of secondary dust scattering from coke ovens, replacement of dedusters, and fume and dust control of stack emission.

Katoh, H.; Yasuno, M.; Gotch, T.; Yoshida, F.

1993-01-01T23:59:59.000Z

443

Pellet property requirements for future blast-furnace operations and other new ironmaking processes  

SciTech Connect (OSTI)

The requirements for the physical, chemical and metallurgical properties of pellets have continued to become more stringent as blast-furnace productivity and coke rate have been rapidly improved during the last decade. In addition, the age and deterioration of the North American coke batteries, the lack of capital to sufficiently rebuild them, and the threat of increasingly more stringent environmental controls for the coke batteries has forced North American ironmakers to begin implementing pulverized coal injection to minimize the coke requirements for the blast furnace and to seriously investigate developing other ironmaking processes that use coal instead of coke. Therefore, the next major step in North American ironmaking has included injecting pulverized coal (PC) at 200 kilograms per ton of hot metal (kg/ton) [400 pounds per net ton of hot metal (lb/NTHM)] or greater which will result in the coke rate decreasing to less than 300 kg/ton (600 lb/NTHM) or less. As a result, the pellets will spend more time in the furnace and will be required to support more total weight. Pellets can also be a major iron unit source for other cokeless ironmaking processes such as the COREX process or the AISI direct ironmaking process. This paper will explore the pellet property requirements for future blast-furnace operations and cokeless ironmaking processes.

Agrawal, A.K.; Oshnock, T.W. [U.S. Steel, Monroeville, PA (United States)

1995-12-01T23:59:59.000Z

444

Graphite having improved thermal stress resistance and method of preparation  

DOE Patents [OSTI]

An improved method for fabricating a graphite article comprises the steps of impregnating a coke article by first heating the coke article in contact with a thermoplastic pitch at a temperature within the range of 250.degree.-300.degree. C. at a pressure within the range of 200-2000 psig for at least 4-10 hours and then heating said article at a temperature within the range of 450.degree.-485.degree. C. at a pressure of 200-2000 psig for about 16-24 hours to provide an impregnated article; heating the impregnated article for sufficient time to carbonize the impregnant to provide a second coke article, and graphitizing the second coke article. A graphite having improved thermal stress resistance results when the coke to be impregnated contains 1-3 wt.% sulfur and no added puffing inhibitors. An additional improvement in thermal stress resistance is achieved when the second coke article is heated above about 1400.degree. C. at a rate of at least 10.degree. C./minute to a temperature above the puffing temperature.

Kennedy, Charles R. (Oak Ridge, TN)

1980-01-01T23:59:59.000Z

445

Geochemistry of coal from Cretaceous Corwin and Chandler formations, National Petroleum Reserve in Alaska (NPRA)  

SciTech Connect (OSTI)

Ninety coal samples from these formations within NPRA were collected and analyzed in order to evaluate coal quality and elemental distribution. Their apparent rank ranges from lignite A in the northern part of NPRA to high-volatile AS bituminous coal in the southern part. Mean vitrinite reflectance values range from 0.65 to 0.74%. Some Corwin Formation coal samples west of NPRA have coking potential with free-swelling indexes between 3.0 and 5.0. Compared to other western United States Cretaceous coal, NPRA coal is significantly lower in ash, volatile matter, O, Si, Al, Ca, Fe, Ti, Cu, F, Li, Mn, Mo, Pb, Sb, Se, Th, and Zn. Statistical comparisons of element concentrations indicate that the mean content of Si, Al, K, Li, Sc, Y, and Yb increases as the mean ash content increases (correlation coefficient at least 0.7). Sulfur values are extremely low (0.1%), and elements that normally show positive correlation with sulfur, such as Fe, As, Cd, Co, Cu, Mo, Pb, and Zn, are also low. Therefore, coal from NPRA can be characterized by low ash and sulfur contents and low contents of elements of environmental concern, such as As, Be, Hg, Mo, Sb, and Se. The elements found to have positive correlations with ash content are probably present as aluminosilicate or stable oxide minerals. Variations in element content and quality of NPRA coal were probably influenced by the geochemical conditions that existed in the Corwin and Umiat delta systems.

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

1985-04-01T23:59:59.000Z

446

PULSE COMBUSTOR DESIGN QUALIFICATION TEST AND CLEAN COAL FEEDSTOCK TEST - VOLUME I AND VOLUME II  

SciTech Connect (OSTI)

For this Cooperative Agreement, the pulse heater module is the technology envelope for an indirectly heated steam reformer. The field of use of the steam reformer pursuant to this Cooperative Agreement with DOE is for the processing of sub-bituminous coals and lignite. The main focus is the mild gasification of such coals for the generation of both fuel gas and char--for the steel industry is the main focus. An alternate market application for the substitution of metallurgical coke is also presented. This project was devoted to qualification of a 253-tube pulse heater module. This module was designed, fabricated, installed, instrumented and tested in a fluidized bed test facility. Several test campaigns were conducted. This larger heater is a 3.5 times scale-up of the previous pulse heaters that had 72 tubes each. The smaller heater has been part of previous pilot field testing of the steam reformer at New Bern, North Carolina. The project also included collection and reduction of mild gasification process data from operation of the process development unit (PDU). The operation of the PDU was aimed at conditions required to produce char (and gas) for the Northshore Steel Operations. Northshore Steel supplied the coal for the process unit tests.

Unknown

2002-02-08T23:59:59.000Z

447

A review of the global emissions, transport and effects of heavy metals in the environment  

SciTech Connect (OSTI)

The purpose of this report is to describe the current state of knowledge regarding the sources and quantities of heavy metal emissions, their transport and fate, their potential health and environmental effects, and strategies to control them. The approach is to review the literature on this topic and to consult with experts in the field. Ongoing research activities and research needs are discussed. Estimates of global anthropogenic and natural emissions indicate that anthropogenic emissions are responsible for most of the heavy metals released into the atmosphere and that industrial activities have had a significant impact on the global cycling of trace metals. The largest anthropogenic sources of trace metals are coal combustion and the nonferrous metal industry. Atmospheric deposition is an important pathway by which trace metals enter the environment. Atmospheric deposition varies according to the solubility of the element and the length of time it resides in the atmosphere. Evidence suggests that deposition is influenced by other chemicals in the atmosphere, such as ozone and sulfur dioxide. Trace metals also enter the environment through leaching. Existing emissions-control technologies such as electrostatic precipitators, baghouses, and scrubbers are designed to remove other particulates from the flue gas of coal-fired power plants and are only partially effective at removing heavy metals. Emerging technologies such as flue gas desulfurization, lignite coke, and fluidized bed combustion could further reduce emissions. 108 refs.

Friedman, J.R.; Ashton, W.B.; Rapoport, R.D.

1993-06-01T23:59:59.000Z

448

Development of an advanced, continuous mild gasification process for the production of co-products. Quarterly report, April--June 1995  

SciTech Connect (OSTI)

The objective of this research and development effort was to develop an advanced, continuous ``mild gasification`` process. The relative quantities and properties of the products are appropriate for making the concept economically and environmentally viable. In ``mild gasification,`` coal is converted under relatively mild conditions of temperature and pressure in the absence of air into products which include a high heating value gas, high aromatic condensibles, char and coke all with physical and chemical properties suitable for the anticipated end uses. Two tons of CTC/DOE continuous coke of 6 in. {times} 5 in. {times} 4 in. size was produced in the Pilot Demonstration Unit. This coke was tested under actual foundry conditions in a 96 in. diameter commercial cupola. The test was run on the first shift on April 19, 1995. The coke sample was used as a direct replacement for 25 percent of the coke charge. A total of 51 scrap iron charges were run with the CTC/DOE continuous coke. Results of the test were excellent. The two main indicators improved., Tap temperature increased from an average of 2846{degrees}F to 2890{degrees}F. Carbon pickup improved from 3.49 percent C to 3.59 percent C when the CTC coke, hit the bed. These results are very meaningful because they cannot be measured in the lab. ChemChar Research, Inc. in Columbia, Missouri, is evaluating CTC chars as potential agents for removing pollutants from gas streams. Composite CTC char treated with the ChemChar activation process resulted in promising results. A 11.8 percent toluene adsorption and 13.4 percent monochlorobenzene adsorption were achieved with CTC char after activation.

NONE

1995-08-01T23:59:59.000Z

449

Method for producing low and medium BTU gas from coal  

SciTech Connect (OSTI)

A process for producing low and medium BTU gas from carbonizable material is described which comprises: partly devolatizing the material and forming hot incandescent coke therefrom by passing a bed of the same part way through a hot furnace chamber on a first horizontally moving grate while supplying a sub-stoichiometric quantity of air to the same and driving the reactions: C + O/sub 2/ = CO/sub 2/; 2C + O/sub 2/ = 2CO discharging the hot incandescent coke from the end of the first grate run onto a second horizontally moving grate run below the first grate run in the same furnace chamber so as to form a bed thereon, the bed formed on the second grate run being considerably thicker than the bed formed on the first grate run, passing the hot incandescent coke bed on the second grate run further through the furnace chamber in a substantially horizontal direction while feeding air and stream thereto so as to fully burn the coke and in ratio of steam to air driving the following reactions: 2C + O/sub 2/ = 2CO; C + H/sub 2/O = H/sub 2/ + CO; C + 2H/sub 2/O = 2H/sub 2/ + CO/sub 2/; CO + H/sub 2/O = H/sub 2/ + CO/sub 2/ taking off the ash residue of the burned coke and taking off the gaseous products of the reactions.

Mansfield, V.; Francoeur, C.M.

1988-06-07T23:59:59.000Z

450

ccpi-lignite | netl.doe.gov  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE:1 First Use of Energy for All Purposes (Fuel and Nonfuel),Feet) Year Jan Feb Mar Apr MayAtmosphericNuclear SecurityTensile Strain Switched5 Industrial Carbon Capture and Storage Clean CoalCoal-Biomass Feed3GilbertonWestern31

451

Market integration in the international coal industry: A cointegration approach  

SciTech Connect (OSTI)

The purpose of this paper is to test the hypothesis of the existence of a single economic market for the international coal industry, separated for coking and steam coal, and to investigate market integration over time. This has been conducted by applying cointegration and error-correction models on quarterly price series data in Europe and Japan over the time period 1980-2000. Both the coking and the steam coal markets show evidence of global market integration, as demonstrated by the stable long-run cointegrating relationship between the respective price series in different world regions. This supports the hypothesis of a globally integrated market. However, when analyzing market integration over time it is not possible to confirm cointegration in the 1990s for steam coal. Thus, compared to the coking coal market, the steam coal market looks somewhat less global in scope.

Warell, L. [University of Lulea, Lulea (Sweden). Dept. of Business Administration & Social Science

2006-07-01T23:59:59.000Z

452

Gary No. 13 blast furnace achieves 400 lbs/THM coal injection in 9 months  

SciTech Connect (OSTI)

Number 13 Blast Furnace at Gary began injecting Pulverized Coal in March 1993. The injection level was increased over the next nine months until a level off 409 lbs/THM was achieved for the month of December 1993. Several major areas were critical in achieving this high level of Pulverized coal injection (PCI) including furnace conditions, lance position, tuyere blockage, operating philosophy, and outages. The paper discusses the modifications made to achieve this level of injection. This injection level decreased charged dry coke rate from 750 lbs/THM to about 625 lbs/THM, while eliminating 150 lbs/THM of oil and 20 lbs/THM of natural gas. Assuming a 1.3 replacement ratio for an oil/natural gas mixture, overall coke replacement for the coal is about 0.87 lbs coke/lbs coal. Gary Works anticipates levels of 500 lbs/THM are conceivable.

Sherman, G.J.; Schuett, K.J.; White, D.G.; O`Donnell, E.M. [U.S. Steel Group, Gary, IN (United States)

1995-12-01T23:59:59.000Z

453

Control of cooling losses at high pulverized coal injection rates  

SciTech Connect (OSTI)

One of the problems which is encountered by many blast furnace operators is the appropriate control of the cooling losses of the blast furnace. This problem has been aggravated by the introduction of pulverized coal injection. Even with equal burden and coke composition, both Sidmar furnaces behave differently with respect to the cooling losses. This phenomenon is possibly attributable to the different profile and cooling circuitry of the furnaces. Among other parameters the angles of bosh and stack may favor the formation of scabs or not. Some operators experience a decrease of their cooling losses, other operators have problems to limit their cooling losses to an acceptable level. As a result, different operating practices exist with respect to the burden distribution. The increase of the ore to coke ratio with pulverized coal injection suggests that the coke and sinter quality has to be monitored very carefully in order to avoid permeability problems.

Bonte, L.; Nieuwerburgh, H. Van [Sidmar N.V., Gent (Belgium)

1996-12-31T23:59:59.000Z

454

Ironmaking conference proceedings. Volume 54  

SciTech Connect (OSTI)

The technical presentations at this conference displayed a renewed sense of viability of the coke and ironmaking community. In addition, many of the papers show that the environmental aspects of ironmaking are being integrated into day-to-day operations rather than being thought of as separate responsibilities. This volume contains 68 papers divided into the following sections: Blast furnace injection; Blast furnace fundamental studies; Blast furnace general; Blast furnace repairs/rebuilds/modernization; Process control techniques for blast furnaces; Cokemaking general; Cokemaking environmental; Coke--by-products--plant operations; Coal and coke research; Battery operations; Pelletizing; Direct reduction and smelting; and Sintering. Most of the papers have been processed separately for inclusion on the data base.

NONE

1995-12-01T23:59:59.000Z

455

Fluid catalytic cracking of heavy petroleum fractions  

SciTech Connect (OSTI)

A process is claimed for fluid catalytic cracking of residuum and other heavy oils comprising of gas oil, petroleum residue, reduced and whole crudes and shale oil to produce gasoline and other liquid products which are separated in various streams in a fractionator and associated vapor recovery equipment. The heat from combustion of coke on the coked catalyst is removed by reacting sulfur-containing coke deposits with steam and oxygen in a separate stripper-gasifier to produce a low btu gas stream comprising of sulfur compounds, methane, carbon monoxide, hydrogen, and carbon dioxide at a temperature of from about 1100/sup 0/F. To about 2200/sup 0/F. The partially regenerated catalyst then undergoes complete carbon removal in a regeneration vessel. The regenerated catalyst is recycled for re-use in the cracking of heavy petroleum fractions. The liquid products are gasoline, distillates, heavy fuel oil, and light hydrocarbons.

McHenry, K.W.

1981-06-30T23:59:59.000Z

456

The relationship between the thermoplastic behavior of blends and their component coals  

SciTech Connect (OSTI)

The thermoplastic behaviors of a number of coking coal blends were measured using proton magnetic resonance thermal analysis (PMRTA) to determine to what extent they were affected by interactions between the component coals. Most blends showed evidence that at temperatures near their temperatures of maximum fluidity the extent to which they fused was different to that expected if the coals did not interact. Only blends of coking coals of different rank fused to a greater extent than expected in the absence of interactions. Semi-anthracite, low rank coals and charcoal reduced the extent of fusion of coking coals to values below those expected if they were acting as inert diluents. These interactions are interpreted as being mediated by transfer of volatile material between the coals on heating.

Sakurovs, R.

1999-07-01T23:59:59.000Z

457

Synthesis and Understanding of Novel Catalysts  

SciTech Connect (OSTI)

The research took advantage of our capabilities to perform in-situ and operando Raman spectroscopy on complex systems along with our developing expertise in the synthesis of uniform, supported metal oxide materials to investigate relationships between the catalytically active oxide composition, atomic structure, and support and the corresponding chemical and catalytic properties. The project was organized into two efforts: 1) Synthesis of novel catalyst materials by atomic layer deposition (ALD). 2) Spectroscopic and chemical investigations of coke formation and catalyst deactivation. ALD synthesis was combined with conventional physical characterization, Raman spectroscopy, and probe molecule chemisorption to study the effect of supported metal oxide composition and atomic structure on acid-base and catalytic properties. Operando Raman spectroscopy studies of olefin polymerization leading to coke formation and catalyst deactivation clarified the mechanism of coke formation by acid catalysts.

Stair, Peter C. [Northwestern University] [Northwestern University

2013-07-09T23:59:59.000Z

458

ATMOSPHERIC AEROSOL SOURCE-RECEPTOR RELATIONSHIPS: THE ROLE OF COAL-FIRED POWER PLANTS  

SciTech Connect (OSTI)

This report describes the technical progress made on the Pittsburgh Air Quality Study (PAQS) during the period of March 2003 through August 2003. Significant progress was made this project period on the source characterization, source apportionment, and deterministic modeling activities. Major accomplishments included: Development of an emission profile for an integrated coke production facility and simulations using PMCAMx for a two week period during July 2001. The emissions from the coke facility are dominated by carbonaceous compounds. Forty seven percent of the organic carbon mass was identified on a compound level basis. Polycyclic aromatic hydrocarbons were the dominant organic compound class in the coke emissions. Initial comparisons with the data collected in Pittsburgh suggest good agreement between the model predictions and observations. Single particle composition data appear useful for identifying primary sources. An example of this unique approach is illustrated using the Fe and Ce particle class with appear associated with steel production.

Allen L. Robinson; Spyros N. Pandis; Cliff I. Davidson

2003-11-01T23:59:59.000Z

459

Mercury capture by distinct fly ash carbon forms  

SciTech Connect (OSTI)

Carbon was separated from the fly ash from a Kentucky power plant using density gradient centrifugation. Using a lithium heterolpolytungstate high-density media, relative concentrations of inertinite (up to 85% vol.), isotropic carbon (up to 79% vol.), and anisotropic carbon (up to 76% vol.) were isolated from the original fly ash. Mercury concentration was lowest in the parent fly ash (which contains non-carbon components); followed by inertinite, isotropic coke, mixed isotropic-anisotropic coke fraction, and, with the highest concentration, the anisotropic coke concentrate. The latter order corresponds to the increase in BET surface area of the fly ash carbons. Previous studies have demonstrated the capture of mercury by fly ash carbon. This study confirms prior work demonstrating the varying role of carbon types in the capture, implying that variability in the carbon content influences the amount of mercury retained on the fly ash.

Hower, J.C.; Maroto-Valer, M.M.; Taulbee, D.N.; Sakulpitakphon, T.

1999-07-01T23:59:59.000Z

460

Petrography and chemistry of high-carbon fly ash from the Shawnee Power Station, Kentucky  

SciTech Connect (OSTI)

The Shawnee power station in western Kentucky consists of ten 150-MW units, eight of which burn low-sulfur (< 1 wt %) eastern Kentucky and central West Virginia coal. The other units burn medium- and high-sulfur (> 1 wt %) coal in an atmospheric fluidized-bed combustion unit and in a research unit. The eight low-sulfur coal units were sampled in a 1992 survey of Kentucky utilities. Little between-unit variation is seen in the ash-basis major oxide and minor element chemistry. The carbon content of the fly ashes varies from 5 to 25 wt %. Similarly, the isotropic and anisotropic coke in the fly ash varies from 6% to 42% (volume basis). Much of the anisotropic coke is a thin-walled macroporous variety, but there is a portion that is a thick-walled variety similar to a petroleum coke.

Hower, J.C.; Thomas, G.A.; Robertson, J.D.; Wong, A.S. [Univ. of Kentucky, Lexington, KY (United States); Clifford, D.S.; Eady, J.D. [Tennessee Valley Authority, Chattanooga, TN (United States)

1996-01-01T23:59:59.000Z

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


461

Petrography and chemistry of fly ash from the Shawnee Power Station, Kentucky  

SciTech Connect (OSTI)

The Shawnee Power Station in western Kentucky consists of ten 150 MW units, eight of which burn low-sulfur eastern Kentucky and central West Virginia coal. The other units bum medium and high-sulfur coal in an AFBC unit and in a research unit. The eight low-sulfur coal units were sampled in a 1992 survey of Kentucky utilities. Little between-unit variation is seen in the ash-basis major oxide and minor element chemistry. The carbon content of the fly ashes varies from 5 to 25%. Similarly, the isotropic and anisotropic coke in the fly ash varies from 6 to 42% (volume basis). Much of the anisotropic coke is a thin-walled macroporous variety but there is a portion which is a thick-walled variety similar to a petroleum coke.

Hower, J.C.; Thomas, G.A.; Wild, G.D. [Univ. of Kentucky, Lexington, KY (United States). Center for Applied Energy Research; Clifford, D.S.; Eady, J.D. [Tennessee Valley Authority, Chattanooga, TN (United States)

1994-12-31T23:59:59.000Z

462

Novel Pt/Mg(In)(Al)O catalysts for ethane and propane dehydrogenation  

SciTech Connect (OSTI)

Catalysts for the dehydrogenation of light alkanes were prepared by dispersing Pt on the surface of a calcined hydrotalcite-like support containing indium, Mg(In)(Al)O. Upon reduction in H{sub 2} at temperatures above 673 K, bimetallic particles of PtIn are observed by TEM, which have an average diameter of 1 nm. Analysis of Pt LIII-edge extended X-ray absorption fine structure (EXAFS) data shows that the In content of the bimetallic particles increases with increasing bulk In/Pt ratio and reduction temperature. Pt LIII-edge X-ray absorption near edge structure (XANES) indicates that an increasing donation of electronic charge from In to Pt occurs with increasing In content in the PtIn particles. The activity and selectivity of the Pt/Mg(In)(Al)O catalysts for ethane and propane dehydrogenation reactions are strongly dependent on the bulk In/Pt ratio. For both reactants, maximum activity was achieved for a bulk In/Pt ratio of 0.48, and at this In/Pt ratio, the selectivity to alkene was nearly 100%. Coke deposition was observed after catalyst use for either ethane or propane dehydrogenation, and it was observed that the alloying of Pt with In greatly reduced the amount of coke deposited. Characterization of the deposit by Raman spectroscopy indicates that the coke is present as highly disordered graphite particles <30 nm in diameter. While the amount of coke deposited during ethane and propane dehydrogenation are comparable, the effects on activity are dependent on reactant composition. Coke deposition had no effect on ethane dehydrogenation activity, but caused a loss in propane dehydrogenation activity. This difference is attributed to the greater ease with which coke produced on the surface of PtIn nanoparticles migrates to the support during ethane dehydrogenation versus propane dehydrogenation.

Sun, Pingping; Siddiqi, Georges; Vining, William C.; Chi, Miaofang; Bell, Alexis T. (UCB); (ORNL)

2011-10-28T23:59:59.000Z

463

INDUST: An Industrial Data Base  

E-Print Network [OSTI]

.5% of the natural gas consump tion, 98.1% of the fuel oil consumption, 99.2% of the coal/coke consumption, and 99.7% of a class of fuels called "other" fuels. Within these 13 indus try groups, INDUST addresses a wide variety of energy-intense industries... the manufac turing sector, Table 1 shows the latest EIA pro visional estimate of energy consumption (in trillion Btu) for 1985. The EIA reports fuel consumption according to five categories: electricity, fuel oil, natural gas, coal and coke, and other...

Wilfert, G. L.; Moore, N. L.

464

Fuel Switching Strategies for the 1990s  

E-Print Network [OSTI]

, petroleum coke, waste hydrocarbons (such as recovered from lubricants), biomass, and in the near future, methanol and other oxygenates or alcohols. Coal may also conceivably be a long-term sWitching candidate when utilized in a number of advanced open... under mos t conditions, in a manner that generates less NO x than heavier fuels such as coal, coke, and residual oil. Achieving NO x reductions with the latter is often a matter of capital investments and operating costs in either combustion...

Cascone, R.

465

Life Cycle Inventory of CO2 in a EOR System Supporting Information  

E-Print Network [OSTI]

/MJ) Combustion (g CO2e/MJ) Coal [1] 4.99 88 LPG-NGL [2, 3] 17.5 58.4 Pet-Coke [2, 3] 17.5 95.9 Other Pet Natural Gas (m3/bbl) 7.08 Coal (metric ton/bbl) 6.3-06 Electricity (kWh/bbl) 7.6 LPG (bbl/bbl) 4.8E-04-04 Petroleum Coke (bbl/bbl) 1.6E-02 Results Figure S1 shows the sources of these emissions

Jaramillo, Paulina

466

Interfuel Substitution and Energy Use in the UK Manufacturing Sector  

E-Print Network [OSTI]

of the following reasons. First, studies based on the aggregate data fail to account for large di¤erences in technological requirements for fuel types used in speci?c industries. For ex- ample, most cement kilns today use coal and petroleum coke as primary fuels... in the manufacturing processes. Waverman (1992) pointed out that fuels used by industrial sectors for non-energy purposes, such as coking coal, petrochemical feedstocks, or lubricants, have few available substitutes, and should therefore be excluded from the data...

Steinbuks, Jevgenijs

467

Rank enhancement of Permian Barakar and Raniganj coal measures in the western part of the Sohagpur coalfield, Madhya Pradesh, India  

SciTech Connect (OSTI)

The Geological Survey of India (GSI) and the U.S. Geological Survey (USGS) are engaged in a study of the coking coal deposits in the Sohagpur coalfield, near Shahdol, Madhya Pradesh. The major occurrences of coking coal in the Sohagpur coalfield are on the northern, down-thrown side of the regional Bamhani-Chilpa fault, where depths to the coking coal range generally from 100 to 500 m. These coal deposits are within the Permian Barakar Formation, which comprises the lower coal measures of the Gondwana Supergroup. Equivalent coal beds on the south side of the fault are generally non-coking, and are currently being mined in open-cast and underground mines, for use as fuel for electric power generation. In this paper, new data are presented which expands on data and ideas originally presented in Mukhopadyay and others. The purpose of this paper is to integrate thermal signatures (vitrinite reflectance and volatile matter) of the principal coal beds of the Sohagpur coalfield with stratigraphic and structural data. In order to characterize the coking coal deposits, the authors have collected more than 100 coal samples from both the Barakar and Raniganj Formations for analyses. The occurrence of coking coal in the Sohagpur coalfield is related primarily to the thermal alteration of the coal beds in the different geologic settings within the coalfield. In addition, differences in the maceral content of the various coal beds and in the chemical and physical composition within each bed depending upon location, play an important role in determining the existence of coking properties for a particular coal deposit. Potential heat sources for thermal alteration include the abundant dolerite intrusives in the region, and greater depth of burial of the coking coal beds on the down-thrown side of the Bamhani-Chilpa fault. Offset along the Bamhani-Chilpa system has been suggested to greater than 400 m. Hot water, similar to that found in other Permian coalfields in India, may have been the agent that metamorphosed the coal in some places but not in others.

Warwick, P.D.; Milici, R.C.; Mukhopadyay, A.; Adhikari, S.

1999-07-01T23:59:59.000Z

468

Effectiveness of environmental policies at OAO Koks  

SciTech Connect (OSTI)

OAO Koks has introduced a comprehensive program for more stable plant operation and reduced environmental impact in the period 2004 2010. Methods of group relining of the coking-furnace chambers and hot repair of coke furnaces with complete relining of the heating walls have been adopted. Water-protection measures include the construction of an additional water-circulation cycle for the chemical shops, completion of the first stage of wastewater treatment, and reconstruction of the biochemical processing system for phenolic and oily water. A mobile environmental station has been acquired for air-quality monitoring.

B.D. Zubitskii; S.N. D'yakov; V.Ya. Krasnukhin; S.V. Kozyreva [Kuznetsk Basin State Technical University, Kemerovo (Russian Federation)

2009-05-15T23:59:59.000Z

469

Guidelines to Defra's GHG conversion factors for company reporting Annexes updated June 2007  

E-Print Network [OSTI]

.498 Coking Coal tonnes x 2810 x 2810 kWh x 0.349 x 0.332 Aviation Spirit tonnes x 3128 x 3128 kWh x 0.250 x 0.281 x 0.267 Burning Oil1 tonnes x 3150 x 3150 kWh x 0.258 x 0.245 litres x 2.518 x 2.518 Coal 2 tonnes xWh x 0.249 x 0.237 Lubricants tonnes x 3171 x 3171 kWh x 0.263 x 0.250 Petroleum Coke tonnes x 3410 x

470

Guidelines for Company Reporting on Greenhouse Gas Emissions Annexes updated July 2005  

E-Print Network [OSTI]

0.32 LPG kWh x 0.214 therms x 6.27 litres x 1.49 Coking Coal tonnes x 2736 kWh x 0.331 Aviation.63 Petrol tonnes x 3135 kWh x 0.24 litres x 2.30 Fuel Oil tonnes x 3223 kWh x 0.27 Coal2 tonnes x 2548 kWh xWh x 0.25 Petroleum Coke tonnes x 3410 kWh x 0.34 Refinery Miscellaneous kWh x 0.24 therms x 7

471

Continuous measurement of blast furnace burden profile at SSAB Tunnplat AB  

SciTech Connect (OSTI)

A unique profile meter system is installed on Blast Furnace No. 2 in SSAB - Swedish Steel AB, Lulea, Sweden. This system measures the charge material burden profile across the furnace top diameter before and after each charge. The system generates real-time data, which is graphically presented by the system on a monitor and includes burden descent speed, layer thickness of the coke and ore (corrected for descent), ore to coke ratio, and burden skewing. The system is described along with operational results.

Virtala, J.; Edberg, N.; Hallin, M. (SSAB Tunnplat AB, Lulea (Sweden). Ironmaking Division)

1993-01-01T23:59:59.000Z

472

An investigation of three problems concerning the analysis of airborne asphalt fumes  

E-Print Network [OSTI]

and well documented carcinogens; however, the BaP content of asphalt fumes is only about 0. 03 percent of the BaP content of coal fed coke oven emissions. 4 This strongly illustrates the need to avoid confusion between asphalts and tars or pitches from... in the composition of asphalt and tar or pitch . The principal significant difference lies in the fact that there are much smaller amounts of PNA's in asphalt fumes than are found in tar or pitch fumes. Coke ovens and coal gasification plants also produce a fume...

Laird, Larry Teal

1981-01-01T23:59:59.000Z

473

Federal/Industry Development of Energy-Conserving Technologies for the Chemical and Petroleum Refining Industries  

E-Print Network [OSTI]

. Alternatives to aqueous waste incineration. 8. Coal-fired process furnaces. Our conclusions to-date in one of these tech nology areas -- integration of a coal/coke gasifier into a h~pothetical petroleum refinery -- are as follows: 1. Hedium...-btu gasification of coal or petroleum coke in a petroleum refinery can reduce imports to the refinery of scarce natural gas and can provide additional energy supplies through sale of high-btu refinery fuel gas. The potential gain in national energy supplies...

Alston, T. G.; Humphrey, J. L.

1981-01-01T23:59:59.000Z

474

Originally Released: July 2009  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in Nonproducing ReservoirsYear-Month WeekReservesYearYearAugust 2009 Coke and Coke

475

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. Biogenic Municipal

476

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. Biogenic MunicipalF.

477

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. Biogenic MunicipalF.D.

478

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF. Other Waste

479

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF. Other

480

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF. Other0.

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


481

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF. Other0.1.

482

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF. Other0.1.2.

483

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.

484

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.4.

485

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.4.1. Stocks

486

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.4.1. Stocks2

487

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.4.1.

488

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.4.1.4.

489

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.4.1.4..

490

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.4.1.4..3.

491

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E. BiogenicF.4.1.4..3.4.

492

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts, Average

493

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts, Average7

494

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts, Average78.

495

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts,

496

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts,0.

497

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts,0.1.

498

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts,0.1.2.

499

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts,0.1.2.3.

500

SAS Output  

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

AFDC Printable Version Share this resource Send a link to EERE: Alternative Fuels Data Center Home Page to someone by E-mail Share EERE: Alternative Fuels Data Center Home Page on Facebook Tweet about EERE: Alternative Fuels Data Center Home Page on Twitter Bookmark EERE: Alternative Fuels Data Center Home Page on Google Bookmark EERE: Alternative Fuels Data CenterFranconia,(Million Barrels) Crude Oil Reserves in NonproducingAdditions to Capacity onF. Petroleum Coke:E.6. Receipts,0.1.2.3.4.