发明名称 Method for producing synthetic natural gas
摘要 Process for producing synthetic natural gas (SNG) which is provided in an energy-efficient way at the inlet pressure into a downstream pipeline system. For this purpose, a synthesis gas containing carbon oxides and hydrogen is converted into a product gas rich in methane by multi-stage catalytic methanation in a main reaction zone and a post-reaction zone, wherein the adjustment of the target pressure is effected by compression before the main reaction zone and/or before or in the post-reaction zone.
申请公布号 US8759407(B2) 申请公布日期 2014.06.24
申请号 US201113812982 申请日期 2011.06.15
申请人 Lurgi GmbH 发明人 Walter Stefan
分类号 C07C27/00 主分类号 C07C27/00
代理机构 Norris McLaughlin & Marcus PA 代理人 Norris McLaughlin & Marcus PA
主权项 1. A process for producing a product gas stream rich in methane with a defined target pressure from a synthesis-gas fresh gas stream containing carbon oxides and hydrogen, comprising the following process steps: (a) providing a synthesis-gas fresh stream at an inlet pressure, (b) combining the synthesis-gas fresh gas stream with a recirculation stream to obtain a synthesis-gas feed stream, (c) heating up the synthesis-gas feed stream and supplying the same to a main reaction zone, (d) converting the heated synthesis-gas feed stream to an intermediate-product gas stream enriched in methane in a main reaction zone under methanation conditions, wherein the main reaction zone includes at least one catalyst bed containing a methanation catalyst, (e) withdrawing a partial stream of the intermediate-product gas stream rich in methane after the main reaction zone as recirculation stream, wherein the recirculation stream is recirculated before the main reaction zone by means of a cycle compressor and is combined with the synthesis-gas fresh gas stream to obtain the synthesis-gas feed stream, (f) supplying the fraction of the intermediate-product gas stream rich in methane remaining after step (e) to a post-reaction zone, (g) converting the intermediate-product gas stream supplied to the post-reaction zone under methanation conditions to a product gas stream rich in methane, wherein the post-reaction zone includes at least one catalyst bed containing a methanation catalyst, (h) withdrawing the product gas stream rich in methane from the post-reaction zone and adjusting the target pressure by means of a product compressor, wherein an additional compressor is provided upstream of the main reaction zone and/or the post reaction zone.
地址 Frankfurt am Main DE