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A COST-EFFECTIVE CATALYST FOR GASIFICATION OF POWDER RIVER BASIN COAL

机译:一种成本效益高的粉状流域煤气化催化剂

摘要

The present invention generally relates to a catalytic gasification of coal. Catalytic gasification of a Wyodak low-sulfur sub-bituminous coal from the Powder River Basin of Wyoming was investigated using an inexpensive sodium carbonate catalyst applied via incipient wetness impregnation. Experiments in an atmospheric pressure fixed-bed laboratory gasifier were performed to evaluate the effects of reaction temperature, feed gas steam content, and Na2CO3 loading on the catalytic gasification of the Wyodak coal. The temperature range investigated (700-900°C) was selected with consideration of the Na2CO3 melting point (850°C) to reduce the loss by volatilization of sodium. Sodium was found to be active during both pyrolysis and gasification steps. The catalyst was most cost-effective at addition levels of approximately 3 wt%. The random pore model provided a good fit to the conversion versus time data collected under both the catalytic and the uncatalytic conditions.
机译:本发明一般涉及煤的催化气化。使用廉价的碳酸钠催化剂通过初湿浸渍法对怀俄明州粉河盆地的Wyodak低硫次烟煤进行了催化气化研究。在大气压固定床实验室气化炉上进行了实验,以评估反应温度,原料气蒸汽含量和Na 2 CO 3 负载量对催化气化的影响。 Wyodak煤炭。考虑Na 2 CO 3 熔点(850°C)来选择要研究的温度范围(700-900°C),以减少钠挥发引起的损失。发现钠在热解和气化步骤中均具有活性。在约3重量%的添加水平下,该催化剂是最具成本效益的。随机孔模型提供了在催化和非催化条件下收集的转化率与时间数据的良好拟合。

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