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公开(公告)号：US4605679A
公开(公告)日：1986-08-12
申请号：US734188
申请日：1985-05-15
CPC分类号： B01J37/0203 , B01J23/75 , B01J23/8913 , B01J23/894 , B01J37/14 , B01J37/18 , C07C1/0445 , C07C2521/04 , C07C2523/10 , C07C2523/12 , C07C2523/46 , C07C2523/75
摘要： Synthesis gas comprising carbon monoxide and hydrogen is converted to a liquid hydrocarbon by contacting the synthesis gas under conversion conditions with a catalyst prepared by subjecting a cobalt carbonyl-impregnated alumina or silica support to an activation procedure at a temperature not exceeding 500.degree. C. comprising, in sequence, (A) reduction in hydrogen, (B) oxidation in an oxygen-containing gas, and (C) reduction in hydrogen.
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公开(公告)号：US4729981A
公开(公告)日：1988-03-08
申请号：US869705
申请日：1986-06-02
CPC分类号： C07C1/0445 , B01J23/75 , B01J23/894 , B01J37/14 , B01J37/18 , C07C2521/04 , C07C2523/10 , C07C2523/12 , C07C2523/46 , C07C2523/75
摘要： Catalyst for synthesis gas conversion in which a gas comprising carbon monoxide and hydrogen is converted to a liquid hydrocarbon is prepared by subjecting cobalt or nickel on a refractory metal oxide support to an activation procedure at a temperature of from about 100.degree. to about 450.degree. C. comprising, in sequence, (A) reduction in hydrogen, (B) oxidation in an oxygen-containing gas, and (C) reduction in hydrogen.
摘要翻译： 将含有一氧化碳和氢气的气体转化为液态烃的合成气转化催化剂是通过将钴或镍在难熔金属氧化物载体上进行活化程序制备的，该活化程序在约100至约450℃ （A）还原氢，（B）含氧气体中的氧化，和（C）氢的还原。
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公开(公告)号：US4670414A
公开(公告)日：1987-06-02
申请号：US876730
申请日：1986-06-20
CPC分类号： C07C1/0445 , B01J23/75 , B01J23/894 , B01J37/14 , B01J37/18 , C07C2521/04 , C07C2523/10 , C07C2523/12 , C07C2523/46 , C07C2523/75
摘要： Synthesis gas comprising carbon monoxide and hydrogen is converted to a liquid hydrocarbon by contacting the synthesis gas under conversion conditions with a catalyst prepared by subjecting a cobalt carbonyl-impregnated alumina or silica support to an activation procedure at a temperature not exceeding 500.degree. C. comprising, in sequence, (A) reduction in hydrogen, (B) oxidation in an oxygen-containing gas, and (C) reduction in hydrogen.
摘要翻译： 包含一氧化碳和氢的合成气体通过使转化条件下的合成气与通过在不超过500℃的温度下使羰基浸渍的氧化铝或二氧化硅载体进行活化程序制备的催化剂而转化为液体烃，包括 ，（A）氢的还原，（B）含氧气体中的氧化，和（C）氢的还原。
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公开(公告)号：US4605676A
公开(公告)日：1986-08-12
申请号：US734189
申请日：1985-05-15
CPC分类号： C07C1/0445 , B01J23/75 , B01J23/83 , B01J23/894 , B01J37/14 , B01J37/18 , C07C2521/04 , C07C2521/06 , C07C2523/10 , C07C2523/12 , C07C2523/46 , C07C2523/75
摘要： Synthesis gas comprising carbon monoxide and hydrogen is converted to a liquid hydrocarbon by contacting the synthesis gas under conversion conditions with a catalyst prepared by subjecting cobalt or nickel on a refractory metal oxide support to an activation procedure at a temperature below 500.degree. C. comprising, in sequence, (A) reduction in hydrogen, (B) oxidation in an oxygen-containing gas, and (C) reduction in hydrogen.
摘要翻译： 包含一氧化碳和氢的合成气体通过使转化条件下的合成气与在难熔金属氧化物载体上的钴或镍在低于500℃的温度下进行活化程序制备的催化剂而转化为液体烃， （A）氢的还原，（B）含氧气体中的氧化，和（C）氢的还原。
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