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Liquefaction co-processing of coal shale oil at - Argonne National ...

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CHEMICAL AND TOXICOLOGIC CHARACTERIZATION OF CO-PROCESSlh% AND<br />

TWO-STAGE DIRECT COAL LIQUEFAcIlON MATERIALS<br />

Cherylyn W. Wright, Dorothy L. Stewart, D. Dennis Mahlum,<br />

Edward K. Chess, and Bary W. Wilson<br />

Pacific Northwest Labor<strong>at</strong>ory<br />

P. 0. Box 999<br />

Richland, WA 99352<br />

Research and development <strong>of</strong> advanced <strong>co</strong>al liquefaction technology is being supported by the U.S.<br />

Department <strong>of</strong> Energy (DOE) as a means <strong>of</strong> utilizing domestic supplies <strong>of</strong> <strong>co</strong>al to produce petroleum-<br />

substitute fuels. As a <strong>co</strong>mponent <strong>of</strong> this effort, the U.S. DOE has supported the chemical analyses v d<br />

toxi<strong>co</strong>logical evalu<strong>at</strong>ions <strong>of</strong> <strong>co</strong>al <strong>co</strong>nversion products and internal process m<strong>at</strong>erials to assess the potenhal<br />

health effects and industrial hygiene <strong>co</strong>ncerns associ<strong>at</strong>ed with <strong>co</strong>al liquefaction technology.<br />

Recent advances in <strong>co</strong>al liquefaction have included two-stage direct <strong>co</strong>al liquefaction processes and<br />

petroleum residkoa1 <strong>co</strong>-<strong>processing</strong> technology. Two-stage <strong>co</strong>al liquefaction processes are generally<br />

<strong>co</strong>mprised <strong>of</strong> a first-stage thermal or liquefaction reactor followed by a se<strong>co</strong>nd-stage hydrogen<strong>at</strong>ion step.<br />

Petroleum resids and <strong>co</strong>al are simultaneously <strong>co</strong>nverted to liquefaction products in <strong>co</strong>-<strong>processing</strong><br />

technology. The purpose <strong>of</strong> this paper is to report the preliminary results <strong>of</strong> the chemical analysis and<br />

toxi<strong>co</strong>logical testing <strong>of</strong> a <strong>co</strong>al liquefaction <strong>co</strong>-<strong>processing</strong> sample set, and to <strong>co</strong>mpare. these results to those<br />

obtained from two-stage <strong>co</strong>al liquefaction m<strong>at</strong>erials.<br />

SAMPLES<br />

Samples for <strong>co</strong>mpar<strong>at</strong>ive chemical analysis and toxi<strong>co</strong>logical evalu<strong>at</strong>ion were provided from the<br />

proprietary UOP, Inc. <strong>co</strong>-<strong>processing</strong> technology (Des Plaines, Illinois) and the integr<strong>at</strong>ed, non-integr<strong>at</strong>ed,<br />

re<strong>co</strong>nfigured integr<strong>at</strong>ed, and close-<strong>co</strong>upled re<strong>co</strong>nfigured integr<strong>at</strong>ed two-stage <strong>co</strong>al liquefaction processes<br />

(ITSL, NTSL, RITSL, and CCRITSL respectively) from the Wilsonville Advanced Coal <strong>Liquefaction</strong><br />

Research and Development Facility (Wilsonville, Alabama) oper<strong>at</strong>ed by C<strong>at</strong>alytic, Inc. A summary is<br />

<strong>co</strong>ntained in Table 1 <strong>of</strong> the <strong>co</strong>-<strong>processing</strong> samples received from UOP, Inc. and the two-stage <strong>co</strong>al<br />

liquefaction m<strong>at</strong>erials analyzed for <strong>co</strong>mpar<strong>at</strong>ive purposes. Since the samples provided were from pilot<br />

plant or bench-scale advanced <strong>co</strong>al liquefaction origins, they may not necessarily be represent<strong>at</strong>ive <strong>of</strong><br />

m<strong>at</strong>erials produced on a <strong>co</strong>mmercial basis.<br />

A description <strong>of</strong> the proprietary UOP, Inc. c<strong>at</strong>alyzed, slurry, single-stage <strong>co</strong>al liquefaction <strong>co</strong>-<br />

<strong>processing</strong> technology has been given by G<strong>at</strong>sis, et al. (1). ITSL and NTSL processes have been<br />

described by L<strong>at</strong>er (2). For a brief overview <strong>of</strong> the RlTSL and CCRlTSL, see Gough et a1 . (3).<br />

EXPERIMENTAL<br />

Samples were chemically characterized by chemical class fraction<strong>at</strong>ion, gas chrom<strong>at</strong>ography, gas<br />

chrom<strong>at</strong>ography-mass spectrometry, and low-voltage probe-inlet mass spectrometry. Toxi<strong>co</strong>logical<br />

activity was measured using the standard histidine reversion microbial mutagenicity test and an<br />

initi<strong>at</strong>iodpromotion assay for mouse skin tumorigenesis. A brief description <strong>of</strong> these methods follow.<br />

. .<br />

-Class F~aXxmtm<br />

Samples were fraction<strong>at</strong>ed ac<strong>co</strong>rding to the method described by L<strong>at</strong>er er a1 . (4) and L<strong>at</strong>er and Lee (5)<br />

by sequential elution <strong>of</strong> standardized alumina (1.5% w<strong>at</strong>er, L<strong>at</strong>er er al., 6) with 20 ml hexane, 50 ml<br />

233

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