发明名称 FISCHER-TROPSCH SYNTHESIS PROCESS
摘要 A process for the conversion of synthesis gas to higher hydrocarbons by synthesis gas, at an elevated temperature and pressure, with a suspension of a particulate Fischer-Tropsch catalyst, in a system comprising at least one high shear mixing zone and a reactor vessel wherein the process comprises: (a) passing the suspension and the gaseous stream through the high shear mixing zone(s) wherein the gaseous stream is broken down into gas bubbles and/or irregularly shaped gas voids; (b) discharging suspension having gas bubbles and/or irregularly shaped gas voids dispersed therein from the high shear mixing zone(s) into the reactor vessel; and (c) maintaining the temperature of the suspension discharged into the reactor vessel at the desired reaction temperature by means of an internal heat exchanger positioned within the suspension in the reactor vessel characterized in that at least 5% of the exothermic heat of reaction is removed from the system by means of the internal heat exchanger. The remainder of the exothermic heat of reaction may be removed from the system by means of an external heat exchanger and/or through the introduction of a liquid coolant.
申请公布号 WO02096835(A3) 申请公布日期 2003.05.08
申请号 WO2002GB02307 申请日期 2002.05.17
申请人 BP EXPLORATION OPERATING COMPANY LIMITED;DAVY PROCESS TECHNOLOGY LIMITED;HENSMAN, JOHN, RICHARD;NEWTON, DAVID 发明人 HENSMAN, JOHN, RICHARD;NEWTON, DAVID
分类号 B01J3/00;B01J3/02;B01J8/22;C10G2/00 主分类号 B01J3/00
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