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Modeling and operating conditions optimization of Fischer-Tropsch synthesis in a fixed-bed reactor

机译:固定床反应器中费-托合成的建模和操作条件优化

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摘要

The effect of a range of operation variables such as pressure, low temperature and H2/CO molar feed ration the catalytic performance of 80%Co/20%Ni/30 wt% La2O3/1 wt% Cs catalyst was investigated. It was found that the optimum operating conditions is a H2/CO = 2/1 molar feed ratio at 260 °C temperature and 2 bar pressure. Reaction rate equations were derived on the basis of the Langmuir-Hinshelwood-Hougen-Watson (LHHW) type models for the Fischer-Tropsch reactions. The activation energy obtained was 59.69 kJ/mol for optimal kinetic model.
机译:研究了一系列操作变量(例如压力,低温和H2 / CO摩尔进料比)对80%Co / 20%Ni / 30 wt%La2O3 / 1 wt%Cs催化剂的催化性能的影响。发现最佳的操作条件是在260℃的温度和2巴的压力下H2 / CO = 2/1的摩尔进料比。反应速率方程是基于费休反应的Langmuir-Hinshelwood-Hougen-Watson(LHHW)类型模型得出的。对于最佳动力学模型,获得的活化能为59.69 kJ / mol。

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