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<br />G <br />The initial small shafts will be retained and used for <br />ventilation, escape ways and mine dewatering. <br />The large-diameter production and service shafts will be <br />used for ventilation and to supply air for the retorting process. <br />Detailed descriptions of mine development plans are in- <br />cluded in Section III of the Modification to the DDP. <br />2. Description of In Situ Retorting <br />Retorts are created by mining out only enough shale to <br />provide a void fraction for rubbling the remaining shale by blasting and <br />to provide permeability for gas flow during operation. These in situ <br />retorts consist of groups or "clusters" of eight 200ft x 200-ft x 310-ft- <br />high rubble columns or chimneys. Undisturbed pillars function as control <br />partitions between operating retorts. <br />The processing of a cluster of retorts consists of several <br />steps. First, a retort within a cluster is kindled from the top by ex- <br />ternally fueled burners. When the temperature at the top of the retort <br />is sufficient to sustain reaction, the burners are shut off and a regulated <br />mixture of air and steam is drawn into and through the retort by exhaust <br />blowers on the surface. Residual organic material is combusted with the <br />air in the feed gas. The hot combustion gases flow down through the <br />retort and supply heat to the raw unretorted shale below. As the shale <br />is heated, the organic material or kerogen decomposes into oil vapor and <br />other gases that are carried along with the combustion gases while some <br />residual organic material remains in the rubble. Steam in the feed <br />gas acts as a diluent to the oxygen in the air to control the reaction <br />temperature and reacts with the residual organic material, forming <br />carbon monoxide and hydrogen to improve the heating value of the product <br />gas. Some of the mineral carbonates in the shale are also decomposed <br />to carbon dioxide gas and mineral oxides. At the same time, the oil and <br />some of the water vapor are condensed. Product liquids and gas leave <br />the bottom of the retort and move to the surface for further processing <br />as a product oil, produced fuel gas, and water. <br />As retorting progresses, the combustion and retorting zones <br />move slowly down through the in situ retort. Between 7 and 8 months are <br />required to process a cluster. When retorting is complete, the air and <br />steam feed are stopped and the in situ retort is closed off. The spent <br />shale remains underground with no need for surface disposal. <br />Surface process facilities consist only of oil/water separa- <br />tion equipment, exhaust blowers, a sulfur removal unit for treatment of <br />product gas, and boilers to produce process steam from fuel values in the <br />product gas. <br />-14- <br />