1 0 0 w 6.f 5 1 0 1- 8 9 1 k- b 1/ 02 Upgrading Coal Liquids 1 0. 1 oi: d 1 | 8 9 1 0, 2 e n u J e: at D n o ati c bli u P In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. 1 0 0 w 6.f 5 1 0 1- 8 9 1 k- b 1/ 2 0 1 0. 1 oi: d 1 | 8 9 1 0, 2 e n u J e: at D n o ati c bli u P In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. Upgrading Coal Liquids Richard F. Sullivan, EDITOR Chevron Research Company Based on a symposium jointly sponsored by the 1 0 0 w 6.f Division of Fuel Chemistry 5 1 0 1- and the Division of 8 9 1 k- b 1/ Petroleum Chemistry at the 2 0 1 0. oi: 1 179th Meeting of the d 1 | 8 American Chemical Society, 9 1 0, 2 ne Houston, Texas, u J e: Dat March 24-25, 1980. n o ati c bli u P ACS SYMPOSIUM SERIES 156 AMERICAN CHEMICAL SOCIETY WASHINGTON, D. C. 1981 In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. 1 0 0 w 6.f 5 1 Library of Congress CIP Data 0 1- Upgrading coal liquids. 8 19 (ACS symposium series; 156) bk- Includes bibliographies and index. 1/ 2 1. Coal liquefaction—Congresses. 0 0.1 I. Sullivan, Richard F., 1929- II. American 1 Chemical Society, Division of Fuel Chemistry. III. oi: American Chemical Society. Division of Petroleum 1 | d Chemistry. IV. Series. 8 TP352.U63 662'.6622 81-1277 9 1 ISBN 0-8412-0629-5 AACR2 0, ACSMC8 156 1-277 1981 2 e n u J e: at D n Copyright © 1981 o cati American Chemical Society bli u All Rights Reserved. The appearance of the code at the bottom of the first page of each P article in this volume indicates the copyright owner's consent that reprographic copies of the article may be made for personal or internal use or for the personal or internal use of specific clients. 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The citation of trade names and/or names of manufacturers in this publication is not to be construed as an endorsement or as approval by ACS of the commercial products or services referenced herein; nor should the mere reference herein to any drawing, specification, chemical process, or other data be regarded as a license or as a conveyance of any right or permission, to the holder, reader, or any other person or corporation, to manufacture, repro duce, use, or sell any patented invention or copyrighted work that may in any way be related thereto. PRINTED IN THE UNITED STATES OF AMERICA In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. ACS Symposium Series M. Joan Comstock, Series Editor 1 0 0 w 6.f 5 1 0 1- 8 Advisory Board 9 1 k- b 1/ David L. Allara James P. Lodge 2 0 1 0. 1 Kenneth B. Bischoff Marvin Margoshes oi: d 1 | Donald D. Dollberg Leon Petrakis 8 9 1 0, Robert E. Feeney Theodore Provder 2 e n u e: J Jack Halpern F. Sherwood Rowland at D n Brian M. Harney Dennis Schuetzle o ati c bli W. Jeffrey Howe Davis L. Temple, Jr. u P James D. Idol, Jr. Gunter Zweig In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. FOREWORD The ACS SYMPOSIUM SERIES was founded in 1974 to provide a medium for publishing symposia quickly in book form. The 1 0 format of the Series parallels that of the continuing ADVANCES 0 w 6.f IN CHEMISTRY SERIES except that in order to save time the 15 papers are not typeset but are reproduced as they are sub 0 1- mitted by the authors in camera-ready form. Papers are re 8 9 1 viewed under the supervision of the Editors with the assistance k- b of the Series Advisory Board and are selected to maintain the 1/ 02 integrity of the symposia; however, verbatim reproductions of 1 0. previously published papers are not accepted. Both reviews 1 oi: and reports of research are acceptable since symposia may d 1 | embrace both types of presentation. 8 9 1 0, 2 e n u J e: at D n o ati c bli u P In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. PREFACE O ur current dependence on petroleum is a natural result of economic forces: petroleum products until recently were much cheaper than liquid hydrocarbons derived from other sources such as coal, oil shale, 01 and tar sands. We have also developed over the years transportation and 0 pr domestic uses for liquid fuels that could be produced from petroleum at 6. 15 a relatively low cost. As the supply of petroleum becomes shorter, the 0 1- alternative of synthetic fuels, derived from hydrocarbon resources other 8 9 1 than petroleum, becomes more attractive, provided that they can be up k- b graded to suit our needs. If synthetic fuels could not be refined to suit 1/ 02 our existing uses, we would be forced at an extraordinarily high expense 1 0. to reinvent, redesign, and replace much of our end use equipment. There 1 oi: fore, both production and upgrading of synfuels are critical to the goal of d 1 | developing alternative energy resources. 8 9 1 Although coal can be used directly in many stationary power plants 0, 2 equipped with appropriate environmental safeguards, it must be converted e un to a liquid before it can serve as a substitute for present-day transportation J e: fuels or home heating oils. Liquids have been obtained from coal for at D many years. However, as a direct result of recent energy shortages, a n atio major effort is now being made to develop new and improved coal lique blic faction technologies. u P Typically, liquids derived from coal are lower in hydrogen content and contain more impurities than do petroleum products. These impuri ties consist of atoms other than hydrogen and carbon, that is, nitrogen, sulfur, oxygen, and inorganic materials. Upgrading of coal liquids to make specification fuels typically involves both hydrogen addition and removal of impurities. This book presents results of studies representative of the type of work in progress today on the upgrading of coal liquids. Information is presented on composition of coal liquids, the chemistry of upgrading, a variety of processing routes, catalyst evaluations, biological tests, and cost studies. Most of the chapters in this book were originally presented at the 179th National Meeting of the American Chemical Society in March ix In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. of 1980; many of them have been revised and updated. It is our hope that this book will serve as a convenient reference for those currently involved in related research areas and will serve as a building block for future work. RICHARD F. SULLIVAN Chevron Research Company Richmond, California November 7, 1980 1 0 0 pr 6. 5 1 0 1- 8 9 1 k- b 1/ 2 0 1 0. 1 oi: d 1 | 8 9 1 0, 2 e n u J e: at D n o ati c bli u P x In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. 1 The Composition of Liquids From Coals of Different Rank G. P. STURM, JR., J. E. DOOLEY, J. S. THOMSON, P. W. WOODWARD, and J. W. VOGH U.S. Department of Energy, Bartlesville Energy Technology Center, Bartlesville, OK 74003 1 0 0 Among the many reports in the literature on coal liquefaction, h 6.c several indicate a relationship between the rank of the coal and 15 the complexity of the hydrocarbon groups in the coal and in its 0 1- liquefaction products. This subject was reviewed in some detail 8 9 in previous reports (l.,2_) and will only be summarized and updated 1 k- here. b 1/ 2 10 Background 0. 1 oi: Early German work indicated that the lower-rank brown coals d 1 | (lignite) are more reactive, require less hydrogen pressure, and 98 produce smaller polynuclear hydrocarbon units (3) than bituminous 1 0, coals. Also, the asphaltene content of the coal liquids decreases e 2 with the coal rank to a minimum for sub-bituminous coals. Early n u work by the U.S. Bureau of Mines produced similar results (. J e: Low-rank coals were found to be so reactive that, at a reaction Dat temperature of 430° C, high hydrogen pressure was required to pre on vent repolymerization of reactive fragments to coke. More recent ati studies have shown that the product from the liquefaction of a c bli Utah sub-bituminous coal with hydrogen donor solvent (5) contains u P less benzene insoluble material than that from Pittsburgh bitumin ous coal. Although the literature suggests that the complexity of hydro carbon groups in coal and coal liquefaction products can differ substantially with the rank of the coal, specific data are limited and sometimes appear to be contradictory. A recent report on the comparison of solvent-refined lignite and solvent-refined sub- bituminous and bituminous coals (6) indicates hardly any difference among the products in terms of gross combustion analysis; acid and basic titres; molecular weight; and nuclear-magnetic resonance, ultraviolet, and electron-spin-resonance spectra. Only the nitro gen content of the coal was reflected in the solvent-refined pro ducts. However, in another recent study of a lignite, a bitumin ous coal, and an anthracite coal, analysis of the organic compounds trapped in the coals and contained in the products of selective This chapter not subject to U.S. copyright. Published 1981 American Chemical Society In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981. 2 UPGRADING COAL LIQUIDS oxidation indicated an increased condensation of aromatic rings with increasing rank (_7) . Analysis was performed by gas chrom atography/ time-of-flight mass spectrometry and high-resolution mass spectrometry. Furthermore, an extensive, detailed study revealed compositional differences in the pyridine extracts of three coals of different rank and also in their liquefaction products produced by the Synthoil process (8). For example, larger quantities of saturates and higher percentages of lower ring-number saturate compound types were observed in the two higher rank coal extracts. However, the ring distributions of the aromatic fractions from the coal extracts indicated slightly higher average ring numbers for the higher rank coals. Similar results were obtained in a study characterizing liquid products obtained from six coals of different rank by treatment of 1 the coals with NaOH-alcohol for 1 hour at 300° to 350° C (9). 0 0 Characterization by elemental analysis, molecular-weight determin h 6.c ation, and proton NMR indicated that the younger (lower-rank) coals 5 1 gave simpler products with primarily two-ring, tetralin-type nuclei 0 1- and more abundant ether linkages than the higher-rank bituminous 8 19 coals which yielded products with five to six rings, about two of k- which were naphthenic. Similarly, in Japanese studies of pyridine b 1/ extracts of coals of different rank (10), analysis by proton NMR 2 0 1 indicated more condensed aromatic rings with less substitution and 0. 1 shorter aliphatic chains in the higher-rank-coal extracts. Ex oi: tracts from bituminous coals contained an average of four or five d 1 | aromatic rings with side chains averaging three or four carbons in 98 length, whereas a lignite extract had an average of one or two 1 0, aromatic rings with seven- or eight-carbon, aliphatic side chains. 2 e Finally, a study using carbon-13 NMR to characterize a hard-coal-tar n u pitch and a brown-coal-tar pitch indicated a predominance of fused- J e: aromatic-ring systems with small amounts of methyl and hydroaro- at D matic methylene groups for the hard-coal-tar pitch (11). The on results for the brown-coal-tar pitch indicated primarily long, ati straight-chain aliphatics estimated at 25 to 40 carbon atoms in c bli length. u P The coal liquids characterized at the Bartlesville Energy Technology Center previous to this study have come from different projects in which the primary objective was the development of a specific process. This precluded a systematic study of the re lationship of coal rank to coal liquid composition, which is the objective of this study. Eight coal liquids prepared from six coals (1,2) of widely differing rank were characterized by procedures previously de veloped for petroleum (12^,13,14) and by ASTM methods. The liquids were prepared and upgraded by hydrogenation in a batch autoclave under conditions intended to minimize cracking of the hydrocarbons (especially those of cyclic and aromatic structure) and yet pro duce most of the liquid hydrocarbons potentially obtainable from a given coal. The extent of the hydrogenation/hydrogenolysis (henceforth referred to as hydrogenation) of the raw coal liquids In Upgrading Coal Liquids; Sullivan, R.; ACS Symposium Series; American Chemical Society: Washington, DC, 1981.
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