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公开(公告)号:US3847567A
公开(公告)日:1974-11-12
申请号:US39108273
申请日:1973-08-27
Applicant: EXXON RESEARCH ENGINEERING CO
CPC classification number: C10J3/54 , C07C1/00 , C07C2527/232 , C10J2300/093 , C10J2300/0959 , C10J2300/0966 , C10J2300/0973 , C10J2300/0986 , C10J2300/1662 , C10J2300/1807 , C10J2300/1823 , C10J2300/1853 , C10J2300/1884 , C10J2300/1892 , C10K1/004 , C10K1/005 , C10L3/08 , C10L3/102 , C10L3/106 , Y10S585/943 , C07C9/04
Abstract: Methane is produced by the thermoneutral reaction of steam with coal or other carbonaceous material in a hydrogasification zone containing an alkali metal catalyst and sufficient hydrogen to suppress competing endothermic reactions. The gas taken overhead from the gasifier is subjected to steam reforming and then processed for the removal of acid constituents, hydrogen which is recycled to the hydrogasification zone, and carbon monoxide which is used as fuel for the steam reformer.
Abstract translation: 在包含碱金属催化剂和足够的氢气的加氢气化区中,通过蒸汽与煤或其它碳质材料的热中和反应生成甲烷,以抑制相互竞争的吸热反应。 对来自气化器的塔顶气体进行蒸汽重整,然后处理以去除酸组分,再循环到加氢气化区的氢气和用作蒸汽重整器的燃料的一氧化碳。