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.
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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 |
代理机构 |
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代理人 |
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主权项 |
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地址 |
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