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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The vari<strong>at</strong>ion in hydrotre<strong>at</strong>ing <strong>co</strong>sts reflects vari<strong>at</strong>ion in both<br />
the quality <strong>of</strong> the raw product and the quantity <strong>of</strong> the C4-850°F<br />
fraction. Hydrotre<strong>at</strong>ing <strong>co</strong>sts <strong>of</strong> EDS are lower than the other<br />
systems, because <strong>of</strong> the rel<strong>at</strong>ively low yield and high API quality <strong>of</strong><br />
the raw EDS product. The total annual revenue requirements vary<br />
from a low <strong>of</strong> 89.7 percent <strong>of</strong> base for EDS, to a high <strong>of</strong> 107.5<br />
percent <strong>of</strong> base for CTSL.<br />
The equivalent barrels <strong>of</strong> yield show a much wider vari<strong>at</strong>ion<br />
than the annual revenue requirements. EDS yield is lowest <strong>at</strong> 84.6<br />
percent <strong>of</strong> base, while CTSL is highest <strong>at</strong> 115.7 percent.<br />
The lower portion <strong>of</strong> Figure 1 <strong>co</strong>mpares the required selling<br />
price <strong>of</strong> hydrotre<strong>at</strong>ed products from the <strong>co</strong>nceptual plants. The<br />
prices vary from 105.9 percent <strong>of</strong> base for EDS to a low <strong>of</strong> 92.9<br />
percent <strong>of</strong> base for CTSL, a spread <strong>of</strong> 13 percent. The most advanced<br />
systems, e.g., modified Lummus, Wilsonville RITSL, and CTSL, <strong>of</strong>fer<br />
the lowest product prices. All these systems c<strong>at</strong>alytically tre<strong>at</strong> an<br />
ash-<strong>co</strong>ntaining extract. It is doubtful th<strong>at</strong> the one-percent<br />
difference between CTSL and RITSL is significant. However, the<br />
slight superiority <strong>of</strong> these systems rel<strong>at</strong>ive to the modified Lummus<br />
is believed to be significant and is traceable to the higher<br />
rejection <strong>of</strong> soluble m<strong>at</strong>erial which is inherent in the deashing<br />
system employed <strong>at</strong> Lummus. Lummus has suggested th<strong>at</strong> the additional<br />
liquids in the deashed overflow <strong>co</strong>uld be re<strong>co</strong>vered by <strong>co</strong>king.<br />
Figure 2 shows e<strong>co</strong>nomic <strong>co</strong>mparisons for plants oper<strong>at</strong>ed with<br />
Wyoming <strong>co</strong>al. Capital re<strong>co</strong>very <strong>co</strong>st vari<strong>at</strong>ions between the plants<br />
are very similar to those observed in the Illinois No. 6 plants.<br />
The total revenue requirements vary from 93.8 to 100 percent <strong>of</strong> base<br />
for the two-stage plants, but are much lower <strong>at</strong> 89 and 83.3 percent<br />
<strong>of</strong> base for the single-stage H-Coal and EDS plants, respectively.<br />
Plant yields show a much gre<strong>at</strong>er vari<strong>at</strong>ion than was observed in<br />
the plants <strong>processing</strong> Illinois No. 6 <strong>co</strong>al. Yields vary from a low<br />
<strong>of</strong> 91.6 percent <strong>of</strong> base for EDS to a high <strong>of</strong> 141.5 percent <strong>of</strong> base<br />
for CTSL.<br />
The required selling prices also show a wide vari<strong>at</strong>ion. The<br />
Lummus ITSL shows the highest selling price <strong>at</strong> 100 percent <strong>of</strong> base,<br />
while CTSL <strong>of</strong>fers the lowest price <strong>at</strong> 68.9 percent <strong>of</strong> base. The<br />
single-stage H-Coal and Wilsonville DITSL processes <strong>of</strong>fer similar<br />
prices <strong>of</strong> 80.3 and 80.7 percent <strong>of</strong> base, respectively.<br />
The results with both Illinois No. 6 and Wyoming <strong>co</strong>als indic<strong>at</strong>e<br />
th<strong>at</strong> the additional <strong>co</strong>st and <strong>co</strong>mplexity <strong>of</strong> two-stage <strong>processing</strong> is<br />
justified by the increases in yield and product quality which can be<br />
obtained.<br />
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