Liquefaction co-processing of coal shale oil at - Argonne National ...
Liquefaction co-processing of coal shale oil at - Argonne National ...
Liquefaction co-processing of coal shale oil at - Argonne National ...
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Compar<strong>at</strong>ive E<strong>co</strong>nomics <strong>of</strong> Two-Stage <strong>Liquefaction</strong> Processes<br />
David Gray, Glen Tomllnson, Abdel El Sawy and Abu Talib<br />
The MITRE Corpor<strong>at</strong>ion. 1820 Dolley Madison Blvd. Mclean, Va. 22102<br />
Background<br />
It has been re<strong>co</strong>gnized in research and development carried out<br />
by Lummus-Crest (1). th<strong>at</strong> two stage liquefaction provides an<br />
<strong>at</strong>tractive route to <strong>co</strong>al liquefaction by optimizing the discrete<br />
stages in <strong>co</strong>nversion <strong>of</strong> solid <strong>co</strong>al to distill<strong>at</strong>e. While<br />
improvements in process efficiency, product yield and quality have<br />
been demonstr<strong>at</strong>ed, the current limited kowledge <strong>of</strong> <strong>co</strong>al structure<br />
and liquefaction chemistry still necessit<strong>at</strong>es empirical testing <strong>of</strong><br />
process altern<strong>at</strong>ives.<br />
A number <strong>of</strong> promising process altern<strong>at</strong>ives have been developed<br />
and are under current investig<strong>at</strong>ion <strong>at</strong> a bench or process<br />
development unit (PDU) scale by a number <strong>of</strong> <strong>co</strong>ntractors under DOE<br />
sponsorship. The <strong>co</strong>ntractors include Lummus-Crest, Southern<br />
Services (Wilsonville) (2), Hydrocarbon Research Inc., (3) and Amo<strong>co</strong><br />
(4). The process vari<strong>at</strong>ions under current investig<strong>at</strong>ion are as<br />
follows:<br />
0<br />
Production <strong>of</strong> a major part <strong>of</strong> the distill<strong>at</strong>e product in<br />
Stage 1 versus Stage 2.<br />
C<strong>at</strong>alytic first and se<strong>co</strong>nd stage versus thermal first<br />
stage and c<strong>at</strong>alytic se<strong>co</strong>nd stage.<br />
Critical Solvent Deashing versus Anti-Solvent Deashing.<br />
Direct <strong>co</strong>upling <strong>of</strong> Stages 1 and 2 without intermedi<strong>at</strong>e<br />
deashing.<br />
DOE requested th<strong>at</strong> MITRE undertake a <strong>co</strong>mprehensive technical<br />
and e<strong>co</strong>nomic analysis <strong>of</strong> all the two-stage <strong>co</strong>al liquefaction<br />
<strong>co</strong>nfigur<strong>at</strong>ions currently under development in order to quantify the<br />
improvements made in the production <strong>of</strong> high quality distill<strong>at</strong>es from<br />
<strong>co</strong>al. Table 1 lists the processes th<strong>at</strong> were analyzed in this task.<br />
The methodology used to perform this analysis was as follows:<br />
0<br />
0<br />
0<br />
0<br />
Review te<strong>at</strong> d<strong>at</strong>a. Select most represent<strong>at</strong>ive run for each<br />
process using both Illinois #6 and Wyoming <strong>co</strong>als.<br />
Scale test d<strong>at</strong>a to develop m<strong>at</strong>erial balances for<br />
<strong>co</strong>nceptual <strong>co</strong>mmercial plants <strong>processing</strong> 30,000 tons per<br />
day <strong>of</strong> moisture free <strong>co</strong>al to the liquefaction units.<br />
Identify unit oper<strong>at</strong>ions for <strong>co</strong>mmercial plants.<br />
Compute <strong>co</strong>al and energy requirements for plant balance.<br />
Estim<strong>at</strong>e capital and oper<strong>at</strong>ing <strong>co</strong>sts for <strong>co</strong>mmerciai plants.<br />
300<br />
i