发明名称 Liquid phase process for converting synthesis gas
摘要 In the synthesis of essentially linear saturated C5+ hydrocarbons from synthesis gas, the reactive gas phase circulating either as a downflow or as an upflow through a fixed bed catalytic reaction zone, an upflow of an inert liquid phase through said zone at a superficial flow rate of more than 0.01 cm/s, as compared to a downflow of liquid phase, increases the selectivity of the process to the formation of the desired C5+ cut.
申请公布号 US5786393(A) 申请公布日期 1998.07.28
申请号 US19960679256 申请日期 1996.07.12
申请人 INSTITUT FRANCAIS DU PETROLE 发明人 CHAUMETTE, PATRICK;BOUCOT, PIERRE;GALTIER, PIERRE
分类号 C07C1/06;C10G2/00;(IPC1-7):C07C27/00 主分类号 C07C1/06
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