发明名称 Optimizing the production rate of slurry bubble reactors by using large gas flow rates and moderate single pass conversion.
摘要 A gas-agitated multiphase reactor system that is effective for enabling maximum reactor productivity or minimizing reactor volume comprising at least two stages with or without recycle, wherein inlet gas superficial velocity is at least 20 cm/sec at Fischer-Tropsch synthesis, yielding a total syngas conversion of greater than about 90%, while syngas conversion in each reactor is less than 60%. More specifically, the total reactor volume is held to a minimum such that minimum reactor volume is less than 0.02 cubic meters total reactor volume/(kg C<SUB>5+</SUB>/hr production).
申请公布号 ZA200400281(B) 申请公布日期 2005.01.14
申请号 ZA20040000281 申请日期 2004.01.14
申请人 CONOCOPHILLIPS COMPANY 发明人 JIANPING ZHANG;HAROLD A. WRIGHT
分类号 B01J8/18;B01J8/22;C10G2/00 主分类号 B01J8/18
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