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    • 7. 发明申请
    • Configurations And Methods of SNG Production
    • SNG生产的配置和方法
    • US20090247653A1
    • 2009-10-01
    • US12295715
    • 2007-04-05
    • Ravi RavikumarGiorgio Sabbadini
    • Ravi RavikumarGiorgio Sabbadini
    • C07C27/00B01J7/00
    • C10L3/08Y02E20/18
    • SNG plants according to the inventive subject matter include one or more methanation reactors that produce a primary methanation product that is cooled to a temperature sufficient to condense water, which is removed in a separator. So produced dried methanation product is then split to provide a reflux stream to the methanation reactors and a feed stream to an adiabatic trim reactor. Most preferably, the plant comprises at least two methanation reactors that are operated in series, wherein the first reactor receives the recycle stream and wherein the second reactor receives a portion of the first methanation reactor effluent and a portion of the first methanation reactor feed.
    • 根据本发明主题的SNG设备包括一个或多个产生初级甲烷化产物的甲烷化反应器,该甲烷化反应器被冷却至足以冷凝水的温度,该水在分离器中除去。 然后分解所产生的干燥甲烷化产物以提供甲烷化反应器的回流和向绝热微调反应器的进料流。 最优选地,该植物包括至少两个串联操作的甲烷化反应器,其中第一反应器接收再循环流,并且其中第二反应器接收一部分第一甲烷化反应器流出物和一部分第一甲烷化反应器进料。