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IMPROVED FISCHER-TROPSCH SYNTHESIS PROCESS THROUGH CONTROL OF THE PARTIAL PRESSURE OF WATER IN THE REACTION ZONE
IMPROVED FISCHER-TROPSCH SYNTHESIS PROCESS THROUGH CONTROL OF THE PARTIAL PRESSURE OF WATER IN THE REACTION ZONE
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机译:通过控制反应区中水的分压来改进FISCHER-TROPSCH合成过程
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摘要
The subject of the invention is a process for the synthesis of hydrocarbons from a feedstock of the synthesis gas type in which said synthesis gas is brought into contact with a catalyst in a reactor under Fischer-Tropsch synthesis conditions and in which the partial pressure of water is controlled to keep it below a critical value ppH2O limit defined by the formula: ppH2O limit = exp (-7751 / d pT) .P s (T) where T is the reaction temperature in K, dp is the average pore diameter of the catalyst in nm, determined by nitrogen adsorption-desorption (BJH method), P s (T) is the saturation vapor pressure of water at temperature T, in bar .
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机译:本发明的主题是从合成气类型的原料合成烃的方法,其中使所述合成气在费-托合成条件下在反应器中与催化剂接触,并且其中水的分压将其控制为保持在以下公式定义的临界值ppH2O极限以下:ppH2O极限= exp(-7751 / d pT).P s(T)其中T是反应温度(单位:K),dp是反应的平均孔径通过氮吸附-脱附(BJH方法)确定的以纳米为单位的催化剂,P s(T)是温度T下水的饱和蒸气压,单位为bar。
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