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Title: Solvent tailoring in coal liquefaction. Quarterly report, July-September 1983

Abstract

A series of twenty-three aromatic compounds were ranked for their donor solvent efficacy for the dissolution of Western Kentucky No. 9/14 coal. The transfer of hydrogen from the solvent to the coal fragments, as measured by coal conversion, was examined at three levels of available hydrogen. The hydrogen donors are ranked according to their ability to convert coal to THF solubles. Aromatic analogs of the donors showed little ability to convert coal to THF solubles. Factors which influence hydrogen donation include the presence of heteroatoms or substituents both internal and external to the aromatic or hydroaromatic rings, the degree of hydrogenation, the aromaticity or nonaromaticity of the hydroaromatics, and the presence of five-membered rings. A relationship between heats of formation and hydrogen donor ability is shown for hydroaromatics within two ring or three ring homologous series. A model hydrogen acceptor, benzophenone, is also used to rank donors. No correlation exists in the ranking of hydrogen donors by the model acceptor used in this work and in other experimental studies and that obtained by conversion of Western Kentucky coal at typical liquefaction conditions. 24 references.

Authors:
; ; ;
Publication Date:
Research Org.:
Auburn Univ., AL (USA). Coal Conversion Lab.
OSTI Identifier:
7090349
Report Number(s):
DOE/PC/30209-T9
ON: DE84014514
DOE Contract Number:
FG22-80PC30209
Resource Type:
Technical Report
Country of Publication:
United States
Language:
English
Subject:
01 COAL, LIGNITE, AND PEAT; COAL LIQUEFACTION; ORGANIC SOLVENTS; CHEMICAL REACTIONS; COMPARATIVE EVALUATIONS; BENZOPHENONE; COAL; DISSOLUTION; EXPERIMENTAL DATA; HYDROGEN TRANSFER; STRUCTURAL MODELS; CARBONACEOUS MATERIALS; DATA; ENERGY SOURCES; FOSSIL FUELS; FUELS; INFORMATION; KETONES; LIQUEFACTION; MATERIALS; NUMERICAL DATA; ORGANIC COMPOUNDS; SOLVENTS; THERMOCHEMICAL PROCESSES; 010405* - Coal, Lignite, & Peat- Hydrogenation & Liquefaction

Citation Formats

Tarrer, A.R., Curtis, C.W., Guin, J.A., and Williams, D.C.. Solvent tailoring in coal liquefaction. Quarterly report, July-September 1983. United States: N. p., 1983. Web. doi:10.2172/7090349.
Tarrer, A.R., Curtis, C.W., Guin, J.A., & Williams, D.C.. Solvent tailoring in coal liquefaction. Quarterly report, July-September 1983. United States. doi:10.2172/7090349.
Tarrer, A.R., Curtis, C.W., Guin, J.A., and Williams, D.C.. Sat . "Solvent tailoring in coal liquefaction. Quarterly report, July-September 1983". United States. doi:10.2172/7090349. https://www.osti.gov/servlets/purl/7090349.
@article{osti_7090349,
title = {Solvent tailoring in coal liquefaction. Quarterly report, July-September 1983},
author = {Tarrer, A.R. and Curtis, C.W. and Guin, J.A. and Williams, D.C.},
abstractNote = {A series of twenty-three aromatic compounds were ranked for their donor solvent efficacy for the dissolution of Western Kentucky No. 9/14 coal. The transfer of hydrogen from the solvent to the coal fragments, as measured by coal conversion, was examined at three levels of available hydrogen. The hydrogen donors are ranked according to their ability to convert coal to THF solubles. Aromatic analogs of the donors showed little ability to convert coal to THF solubles. Factors which influence hydrogen donation include the presence of heteroatoms or substituents both internal and external to the aromatic or hydroaromatic rings, the degree of hydrogenation, the aromaticity or nonaromaticity of the hydroaromatics, and the presence of five-membered rings. A relationship between heats of formation and hydrogen donor ability is shown for hydroaromatics within two ring or three ring homologous series. A model hydrogen acceptor, benzophenone, is also used to rank donors. No correlation exists in the ranking of hydrogen donors by the model acceptor used in this work and in other experimental studies and that obtained by conversion of Western Kentucky coal at typical liquefaction conditions. 24 references.},
doi = {10.2172/7090349},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Sat Jan 01 00:00:00 EST 1983},
month = {Sat Jan 01 00:00:00 EST 1983}
}

Technical Report:

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  • Although the numerous functions of the solvent during liquefaction are not completely understood, the provision for and the maintenance of an effective process solvent is necessary for effective coal liquefaction. In this project, the function of the process solvent regarding vapor-liquid equilibrium, hydrogen donation, and catalyst activity has been explored. An in-depth literature study has been completed to examine in detail the salient factors affecting coal solvation and solvent quality. Work is continuing with selected model hydroaromatic compounds to determine if the chemical nature of the model hydroaromatic influences the product distribution obtained from coal during liquefaction as well asmore » affecting the amount of conversion. The study has focused on two compounds: tetralin and tetrahydroquinoline. The product distribution which is being used to evaluate the liquefaction products is based upon extraction of the products into different solvents. The products are divided into oil, pentane soluble material; asphaltenes, pentane insoluble, benzene soluble material; preasphaltenes, benzene insoluble, methylene chloride/methanol soluble material; and insoluble organic matter, methylene chloride/methanol insoluble material. The effectiveness of the hydrogen donor solvent will be measured by the amount of higher quality material, oil and asphaltenes, obtained from coal as well as by the amount of coal converted. In addition, the change in the solvent composition is also being measured by gas chromatography. A method using size exclusion chromatography to monitor the effects of process parameters and the effect of solvent composition on products obtained from coal liquefaction reactions is being developed. 62 references, 10 figures, 8 tables.« less
  • The contribution of transferable hydrogen in coal-derived solvents to coal conversion was investigated in a two-step process. Initially, the amount of transferable hydrogen in the coal-derived solvents was analyzed by spectroscopic methods and by catalytic dehydrogenation. The spectroscopic methods included carbon magnetic resonance, proton magnetic resonance as well as a combination of these two methods. Three of the methods gave nearly equivalent quantities for the amount of transferable hydrogen present in the complex coal liquids. Coal conversion determined in each of the coal-derived solvents was correlated to the amount of transferable hydrogen present. The contribution of transferable hydrogen is amore » significant factor in coal dissolution and the presence of saturates and hexane insolubles compounds in these solvents may have a detrimental effect on coal dissolution. 20 references, 9 figures, 2 tables.« less
  • A simple kinetic model, including a first-order catalyst deactivation rate, was applied to the upgrading of coal-derived feedstocks prepared from two solvent-refined coal fractions. A catalyst deactivation mechanism was proposed which involves the adsorption and surface reaction of coke precursors on active catalytic sites. The effect of feedstock composition, temperature, and pressure on kinetic parameters and, in particular, the catalyst deactivation rate, was determined. 21 references, 6 figures, 7 tables.
  • Work this quarter focused on staged liquefaction. The effect of residence time on conversion in single pass experiments was found to be quite different for the subbituminous Belle Ayr Mine and bituminous Illinois No. 6 coals studied. With bituminous coal, conversion to soluble material is quite high and the limit of conversion is approached in only a few minutes. With a subbituminous coal, however, conversion is much lower and the limit of conversion is approached much more slowly. Short contact time (SCT) dissolution of Belle Ayr coal was studied as a possible first stage in a two-stage process. Conversion, hydrocarbonmore » gas yield and hydrogen consumption were increased as residence time or temperature were increased. Conversion was also significantly increased by partial slurry recycle. Pyrite was found to be the most effective slurry catalyst for increasing conversion, followed by ammonium molybdate emulsion and finally nickel-molybdenum on alumina. Illinois No. 6 coal was liquefied in two stages. Conditions in the first stage dissolution were varied to determine the effect on upgradability in the second stage. An SCT (6 minute) coal dissolution stage is preferred over one at 30 minutes because hydrocarbon gas yield was much lower while overall oil yields for the combined dissolution and upgrading stages were nearly the same. Use of a NiMo/Al/sub 2/O/sub 3/ catalyst in a trickle-bed second stage resulted in a higher oil yield and lower product heteroatom content than use of the same catalyst in the slurry phase. The total oil yield was lower with a pyrite slurry catalyst than with a NiMo/Al/sub 2/O/sub 3/ slurry catalyst. With Belle Ayr coal and added pyrite, there was no change in total oil yield, conversion or product quality brought about by adding an 8-minute first stage at 450/sup 0/C (842/sup 0/F) to a 2-hour second stage operated at 420/sup 0/C (788/sup 0/F). 39 figures, 12 tables.« less
  • The scope of the program consists of the following tasks: (1) Task 1A, survey of current practices for centrifugal and reciprocating coal slurry pump seals; (2) Task 1B, preliminary evaluation of three alternative centrifugal and reciprocating fluid seal concepts; (3) Task 2, detail evaluation of the best two centrifugal and reciprocating fluid seal concepts; (4) Task 3A, design and fabrication of the selected centrifugal and reciprocating fluid seal concept. Design and fabrication of the centrifugal and reciprocating seal testers; (5) Task 3B, laboratory seal testing of the centrifugal and reciprocating fluid seals; (6) Task 4, field testing of the centrifugalmore » and reciprocating fluid seals. Tasks 1 and 2 have been completed. The technical results were reported in the interim technical reports. Task 3A is in process. Design of the selected fluid seal concepts and the design requirements to modify field type pumps for the seal testers was completed during the previous period. 12 figs., 9 tabs.« less