发明名称 STEAM REFORMING
摘要 The endothermic reaction of a hydrocarbon feedstock with steam and/or carbon dioxide is carried out using a double-tube reactor (123, 140). In one preferred form of the reactor the catalyst (142) is present as a coating on the outside of the inner tube (140). In another form inner tubes are mounted in one tube plate (136) and the outer tubes in a second tube plate (126) and the tube plates are disposed across a cylindrical shell (110) so as to define a heat exchange zone (124) (provided with a heat source) a reactants feed zone (134) and a products offtake zone (148). The heat source is preferably a burner (116), to be fed with the product (118) of the endothermic reaction, followed by a secondary reforming catalyst (113). The apparatus makes possible processes for making raw hydrogen-containing gases with advantageous internal heat recovery.
申请公布号 DE3480192(D1) 申请公布日期 1989.11.23
申请号 DE19843480192 申请日期 1984.03.14
申请人 IMPERIAL CHEMICAL INDUSTRIES PLC 发明人 PINTO, ALWYN;TWIGG, MARTYN VINCENT
分类号 C01B3/38;B01J8/02;B01J8/06;B01J12/00;B01J19/24;C01B3/02 主分类号 C01B3/38
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