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<br />II. Distillation Process Concerns <br /> <br />We have not yet been provided access to any chemical analysis of the process solution <br />recovered from mining activities. We believe an opportunity to analyze the process solution <br />highly significant for the evaluation of American Soda's plan to meet its duties as an operator <br />with respect to water quality and quantity. We have two related yet independent concerns in <br />this regazd. <br />First, the process and temperature utilized by American Soda is likely to cause an <br />accumulation of oil, or related organics, in the production cavity over time. We understand that <br />American Soda's process may not result in instantaneous distillation of oil shale [Cummins and <br />Robinson, "Thermal Degradation of Green River Kerogen at 150 Degrees Celsius to 350 <br />Degrees Celsius": 1972 USBM, Report of Investigation 7620]. However, instantaneous <br />distillation is not the only issue; distillation is generally temperature and time dependent, and <br />may occur over time at temperatures lower than those required for instantaneous distillation. In <br />the event that this latter type of distillation of oil shale occurs, it will dramatically alter the <br />assessment of aquifer and cavity integrity with respect to water quality, and the way in which <br />the cavern reclamation should be considered. An assessment of this latter type of distillation <br />could conceivably be made requiring American Soda to depressurize its pilot cavity in order to <br />obtain a sample of the liquid surface of the production solution. We distinguish between the <br />liquid surface and the process solution for essentially the same reason as one would look for oil <br />at the top of a vessel containing both oil and water. We have not seen any evidence of such a <br />request, or of any other efforts to fully evaluate the potential for oil shale distillation over time. <br />Our second concern is that there appears to be no attention to the potential for American <br />Soda's process to take dawsonite along with nacholite. Dawsonite is a mineral found in the <br />lease azea which could be subject to solution mining using essentially the same process that <br />American Soda proposes to use. However, as we set forth in some detail below, American <br />Soda's lease stipulations prevent recovery of this resource. At a minimum, the DMG should be <br />testing for dawsonite and chemicals related to dawsonite (especially aluminum / alumina <br />chemistry's) since this mineral is a protected resource and indication that destructive distillation <br />of oil shale is in progress. <br />FURTHER DETAIL RELATED TO COMMENT ABOVE <br />LITERATURE SEARCH <br />The following is an excerpt from the article "Soluble-Salt Processes for In-Situ Recovery of <br />Hydrocarbons From Oil Shale", Journal Of Petroleum Technology September 1977, pg.1079 <br />"In addition to halite and narholite, dawsonite [NaAI(OI-n2C0~] is also present in the target <br />region in average concentrations of about 5 percent. Dawsonite is not very soluble in <br />water. I[ decomposes when heated, giving off C02, aad reacts in an aqueous environment <br />with silica (SiO~ to give various insoluble alumina silicates, the most common of which is <br />enalcite (NaA1SiZ0~." <br />