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    • 1. 发明申请
    • FISCHER-TROPSCH SYNTHESIS PROCESS AND SYSTEM
    • FISCHER-TROPSCH合成过程和系统
    • US20130116348A1
    • 2013-05-09
    • US13809104
    • 2011-07-08
    • Yulin ShiXiuzhang WuLei GongQuan LinYijun LvYifeng BuHongxue Wang
    • Yulin ShiXiuzhang WuLei GongQuan LinYijun LvYifeng BuHongxue Wang
    • C10G2/00
    • C10G2/32C10G2/332C10G2/34C10G2/342C10G2300/4006C10G2300/4012C10K1/005
    • The present invention relates to a Fischer-Tropsch synthesis process and system. The process comprises: a) introducing a feedstock gas containing CO and H2 into a first stage Fischer-Tropsch synthesis reactor to carry out a Fischer-Tropsch synthesis reaction; b) separating products of the first stage Fischer-Tropsch synthesis reaction, to separate water from the unconverted tail gas and to obtain hydrocarbon products and the unconverted tail gas; c) introducing the unconverted tail gas obtained in Step b) into a second stage Fischer-Tropsch synthesis reactor to carry out a Fischer-Tropsch synthesis reaction; d) separating products of the second stage Fischer-Tropsch synthesis reaction, to separate water from the unconverted tail gas, with a portion of the unconverted tail gas of the second stage Fischer-Tropsch synthesis reaction being returned to the second stage Fischer-Tropsch synthesis reactor for recycle reactions. The process and system are suitable for large-scale industrialized production.
    • 本发明涉及费 - 托合成方法和系统。 该方法包括:a)将含有CO和H 2的原料气体引入第一级费 - 托合成反应器中以进行费 - 托合成反应; b)分离第一阶段费 - 托合成反应的产物,从未转化的尾气中分离水并获得烃产物和未转化的尾气; c)将步骤b)中获得的未转化的尾气引入第二级费 - 托合成反应器中以进行费 - 托合成反应; d)分离第二级费 - 托合成反应的产物,从未转化的尾气分离出水,第二级费 - 托合成反应的未转化尾气的一部分返回到第二级费 - 托合成 反应器用于再循环反应。 该工艺和系统适用于大规模工业化生产。