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OIL SHALE<br />

TABLE 1<br />

ECONOMICS OF A 10,000 BBL/DAY PLANT<br />

Description<br />

Capital cost @ 15% IRR -<br />

725 Million<br />

Unocal's projected operating costs (full<br />

production excluding hydrotreating)<br />

Hydrotreat/refine 50% into transpor<br />

tation fuel (cost $10/Bbl)<br />

Convert 40% to SOMAT (seasonal<br />

- average cost $5/Bbl)<br />

Convert 10% to specialty chemicals<br />

(cost $25/BpI)<br />

Subtotal -<br />

Capital & Operating Costs<br />

Off-site electricity sales @ $0.03/kWh<br />

SOMAT asphalt additive @ $100/Bbl<br />

Specialty chemicals @ $100/Bbl<br />

Required transportation fuel price<br />

for 15% rate of return<br />

Transportation fuel wholesale price<br />

in 1993<br />

Chemical Society meeting<br />

Washington, D.C. last August.<br />

held in<br />

Fluidized bed pyrolysis of oil shale in a non-<br />

hydrogen atmosphere has been shown to sig<br />

nificantly increase oil yield in laboratory-scale<br />

reactors compared to the Fischer Assay. The<br />

enhancement in oil yield by this relatively simple<br />

and efficient thermal technique has led to the<br />

2-10<br />

Cost&<br />

Revenue<br />

$37<br />

$23<br />

$5<br />

$2<br />

$3<br />

$70<br />

($5)<br />

($40)<br />

($10)<br />

$30<br />

$31<br />

development of several oil shale retorting<br />

processes based on fluidized bed and related<br />

technologies over the past 15 years. Since 1986,<br />

the CAER has been developing one such<br />

process, KENTORT II, which is mainly tailored for<br />

the Devonian oil shales that occur in the Eastern<br />

U.S. The process contains three main fluidized<br />

bed zones to pyrolyze, gasify, and combust the<br />

oil shale. A fourth fluidized bed zone serves to<br />

THE SYNTHETIC FUELS REPORT, JANUARY 1995

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