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• <br />rate for the R&D test phase is approximately 23 bbl/day, or about 2,000 bbl over the life <br />of the R&D test nun. <br />The proposed surface facilities will consist of a separation/processing plant to <br />handle the produced liquid and vapor streams generated from the retort. Produced liquids <br />and gasses will be directed to a thermal oxidizer. The production streams may contain up <br />to 15% hydrogen sulfide (H2S) by weight. The H2S control by the oxidizer is designed to <br />be 99.99% efficient (although AMSO's emission calculations in Attachment 4 use 99.9%fl <br />in order to be conservative). Retort products will fiiel the oxidizer and propane will be <br />utilized during periods of startup, shutdown and standby modes. Liquid streams include: <br />1) stripped naphtha, 2) gas oil, 3) slop oil, and 4) sour water. A small fixed roof tank will <br />handle each liquid stream (4 tanks total). Slop oil is a mixture of stripped naphtha and <br />gas oil. This tank provides storage of off-inn-conditions liquid product prior to <br />destruction at the oxidizer. The sour water may contain 1.5% (by wt) hydrogen sulfide <br />(H2S) and 1.8% (by wt) ammonia (NH3) and vapors from the sour water tank will also be <br />directed to the thermal oxidizer. The other tanks will be vented to atmosphere. <br />E <br />• <br />Page 13 of 46