Ikelic - Alliance Digital Repository
Ikelic - Alliance Digital Repository
Ikelic - Alliance Digital Repository
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OIL SHALE<br />
TABLE 1<br />
OIL SHALE RF HEATING FORECASTS<br />
(Without Standing Waves and Current Decay)<br />
Time Cum Oil Recovery Cum Water Cum Gas Fluid Cum Elec.<br />
(Years) (kbbis) f%OOIP> (kt?bl?) (Mscf) Temo. rF) (kW-hr)<br />
1 0.15 0.06 12.35 0.17 112 7.20E+06<br />
2 1.40 0.55 24.79 1.68 151 1.44E + 07<br />
3 14.44 5.66 26.01 17.32 204 2.16E + 07<br />
4 45.22 17.72 28.87 54.27 267 2.88E + 07<br />
5 75.92 29.75 31.72 91.11 336 3.60E + 07<br />
6 107.46 42.11 34.66 128.86 409 4.21E + 07<br />
7 131.73 51.62 36.92 158.08 466 4.32E + 07<br />
8 150.31 58.90 38.64 180.38 506 4.32E + 07<br />
9 163.99 64.26 39.92 196.79 533 4.32E + 07<br />
10 171.49 67.20 40.61 205.79 550 4.32E + 07<br />
11 176.57 69.19 41.09 211.89 561 4.32E + 07<br />
12 179.89 70.49 41.39 215.87 568 4.32E + 07<br />
13 181.98 71.31 41.59 218.38 571 4.32E + 07<br />
14 183.90 72.06 41.77 220.68 573 4.32E + 07<br />
15 185.63 72.74 41.93 222.76 575 4.32E + 07<br />
16 187.21 73.36 42.07 224.66 575 4.32E + 07<br />
17 188.64 73.92 42.21 226.37 575 4.32E + 07<br />
18 189.95 74.43 42.33 227.93 575 4.32E + 07<br />
19 191.12 74.89 42.44 229.34 574 4.32E + 07<br />
20 191.12 74.89 42.44 229.34 574 4.32E + 07<br />
is additionally contacted with a strong inorganic<br />
acid, such as hydrochloric acid, in the pretreat<br />
ment.<br />
In the preferred embodiment, the reaction water<br />
and organic acid leachate is reacted with sulfuric<br />
acid and distilled to produce a liquid containing<br />
the corresponding organic acid which may be<br />
recycled to contact fresh oil shale.<br />
Carbon dioxide liberated during the organic acid<br />
pretreatment can be reduced to carbon<br />
monoxide which can be absorbed into a<br />
hydroxide solution and subsequently distilled<br />
2-18<br />
with sulfuric acid to produce formic acid for use<br />
in the pretreatment process.<br />
Oil shale subjected to the pretreatment process<br />
of this invention has reduced mineral carbonates<br />
content, increased porosity and increased sur<br />
face area providing increased permeability and<br />
potential reaction surface area for further reac<br />
tion. The process requires little energy, thermal<br />
or mechanical, and is claimed to be economical<br />
because the principal treating agent, an organic<br />
acid such as formic acid or acetic acid, can be<br />
readily and efficiently<br />
recovered for recycle.<br />
THE SYNTHETIC FUELS REPORT, JANUARY 1995