发明名称 |
Oxidative Coupling of Methane Implementations for Olefin Production |
摘要 |
The present disclosure provides oxidative coupling of methane (OCM) systems for small scale and world scale production of olefins. An OCM system may comprise an OCM subsystem that generates a product stream comprising C2+ compounds and non-C2+ impurities from methane and an oxidizing agent. At least one separations subsystem downstream of, and fluidically coupled to, the OCM subsystem can be used to separate the non-C2+ impurities from the C2+ compounds. A methanation subsystem downstream and fluidically coupled to the OCM subsystem can be used to react H2 with CO and/or CO2 in the non-C2+ impurities to generate methane, which can be recycled to the OCM subsystem. The OCM system can be integrated in a non-OCM system, such as a natural gas liquids system or an existing ethylene cracker. |
申请公布号 |
US2015210610(A1) |
申请公布日期 |
2015.07.30 |
申请号 |
US201514592668 |
申请日期 |
2015.01.08 |
申请人 |
Siluria Technologies, Inc. |
发明人 |
Rafique Humera A.;Vuddagiri Srinivas;Harraz Hatem;Radaelli Guido;Scher Erik C.;McCormick Jarod;Iyer Rahul;Duggal Suchia;Cizeron Joel;Hong Jin Ki |
分类号 |
C07C2/84;C07C1/04;C07C1/12;B01J19/24;B01J23/00 |
主分类号 |
C07C2/84 |
代理机构 |
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代理人 |
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主权项 |
1. An oxidative coupling of methane (OCM) system, comprising:
(a) an OCM subsystem that (i) takes as input a feed stream comprising methane (CH4) and a feed stream comprising an oxidizing agent, and (ii) generates from said methane and said oxidizing agent a product stream comprising C2+ compounds and non-C2+ impurities; and (b) at least one separations subsystem downstream of, and fluidically coupled to, said OCM subsystem, wherein said separations subsystem comprises a first heat exchanger, a de-methanizer unit downstream of said first heat exchanger, and a second heat exchanger downstream of said de-methanizer unit, wherein
(1) said first heat exchanger cools said product stream,(2) said de-methanizer unit accepts said product stream from said first heat exchanger and generates an overhead stream comprising methane and at least a portion of said non-C2+ impurities, and a bottoms stream comprising at least a portion of said C2+ compounds, and(3) at least a portion of said overhead stream is cooled in said second heat exchanger and is subsequently directed to said first heat exchanger to cool said product stream. |
地址 |
San Francisco CA US |