1) two molar ratio of concentrations, A1 and A2, are determined between the hydrogen and the carbon monoxide (H2/Co), A1 being the value of said ratio in the supply to the synthesis step b), and A2 being the value of said ratio in any one of the gaseous effluents obtained during steps b) to e);2) comparing ratios A1 and A2; and3) adjusting the concentrations of hydrogen and/or carbon monoxide in the synthesis gas to keep the difference between the two ratios A1 and A2 substantially constant."/> Fischer-Tropsch synthesis process with improved regulation
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Fischer-Tropsch synthesis process with improved regulation

机译:费-托合成工艺改进了调控

摘要

A process for the production of liquid hydrocarbons by the Fischer-Tropsch process comprises a step a) for generating a synthesis gas, a step b) for Fischer-Tropsch synthesis, a step c) for condensing the gaseous effluent obtained during step b), a step d) for separating the effluent condensed during step c) to obtain a gaseous effluent enriched in carbon monoxide and hydrogen, and a step e) for recycling at least a portion of the enriched gaseous effluent obtained during step d) to the Fischer-Tropsch synthesis step b), characterized in that:1) two molar ratio of concentrations, A1 and A2, are determined between the hydrogen and the carbon monoxide (H2/Co), A1 being the value of said ratio in the supply to the synthesis step b), and A2 being the value of said ratio in any one of the gaseous effluents obtained during steps b) to e);2) comparing ratios A1 and A2; and3) adjusting the concentrations of hydrogen and/or carbon monoxide in the synthesis gas to keep the difference between the two ratios A1 and A2 substantially constant.
机译:通过费-托法生产液态烃的方法包括:步骤a)产生合成气,步骤b)用于费-托合成,步骤c)冷凝在步骤b)中获得的气态流出物,步骤d)用于分离在步骤c)中冷凝的流出物以获得富含一氧化碳和氢气的气态流出物,以及步骤e)用于将在步骤d)中获得的至少一部分富集气态流出物再循环至Fischer-合成步骤b),其特征在于: 1)确定了氢气和一氧化碳之间的两个摩尔浓度比A 1 和A 2 (H 2 < / Sub> / Co),A 1 是在合成步骤b)的供应中的所述比率的值,A 2 是在任何一种情况下的所述比率的值步骤b)到e)中获得的一种气体排放物; 2)比较比率A 1 和A 2 ;和 3)调整合成气中氢和/或一氧化碳的浓度,以保持两个比率A 1 < / B>和A 2 基本恒定。

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