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METHOD FOR COMBINING COAL LIQUEFACTION AND GASIFICATION PROCESSES

机译:煤液化与气化过程相结合的方法

摘要

Conversion of raw coal to distillate liquid and gaseous hydrocarbon products by solvent liquefaction in the presence of molecular hydrogen employing recycle of mineral residue is commonly performed at a higher thermal efficiency than conversion of coal to pipeline gas in a gasification process employing partial oxidation and methanation reactions. The prior art has disclosed a combination coal liquefaction-gasification process employing recycle of mineral residue in the liquefaction zone wherein all the normally solid dissolved coal produced in the liquefaction zone is passed to a gasification zone for conversion to hydrogen, where the amount of normally solid dissolved coal prepared and passed to the gasification zone is just sufficient to enable the gasification zone to produce the exact hydrogen requirement of the process. The present invention provides an unexpected improvement in the thermal efficiency of the combination process by utilizing formulas based on feed coal characteristics to calculate an amount of normally solid dissolved coal to be prepared in the liquefaction zone and passed to the gasification zone to enable the gasification zone to generate not only all of the hydrogen required by the liquefaction zone but also to produce synthesis gas for use as fuel in the liquefaction zone. It would have been expected that shifting some of the processing load from the ordinarily more efficient liquefaction zone to the ordinarily less efficient gasification zone would decrease process efficiency, but the present combination process unexpectedly achieves an overall efficiency increase by said shift.
机译:在分子氢存在下,采用溶剂残渣液化,利用矿物残渣的循环,将原煤转化为馏出的液态和气态烃产品,通常比在采用部分氧化和甲烷化反应的气化过程中,将煤转化为管道气的热效率更高。 。现有技术公开了一种组合煤液化气化方法,该方法利用液化区中的矿物残渣的再循环,其中将在液化区中产生的所有通常为固体的溶解煤通入气化区以转化为氢气,其中通常为一定量的固体。制备并传递到气化区的溶解煤正好足以使气化区产生过程中所需的确切氢气。本发明通过利用基于进料煤特性的公式来计算要在液化区中制备并通入气化区以使气化区的正常固体溶解煤的量,从而提供了组合工艺的热效率的出乎意料的改善。不仅产生液化区所需的所有氢,而且产生在液化区用作燃料的合成气。可以预期,将一些处理负荷从通常更有效的液化区转移到通常效率较低的气化区会降低处理效率,但是本发明的组合方法通过所述转移出乎意料地实现了整体效率的提高。

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