发明名称 |
Process for separating hydrocarbon compounds |
摘要 |
Disclosed herein are processes for producing and separating ethane and ethylene. In some embodiments, an oxidative coupling of methane (OCM) product gas comprising ethane and ethylene is introduced to a separation unit comprising two separators. Within the separation unit, the OCM product gas is separated to provide a C2-rich effluent, a methane-rich effluent, and a nitrogen-rich effluent. Advantageously, in some embodiments the separation is achieved with little or no external refrigeration requirement. |
申请公布号 |
US9527784(B2) |
申请公布日期 |
2016.12.27 |
申请号 |
US201514820460 |
申请日期 |
2015.08.06 |
申请人 |
SILURIA TECHNOLOGIES, INC. |
发明人 |
Weinberger Sam;Edwards Justin Dwight;Wolfenbarger Julian;Vuddagiri Srinivas R.;Rahmim Iraj Isaac |
分类号 |
C07C2/84;C07C2/82;C10G27/04;C10G29/20;C10G31/06;F25J3/02 |
主分类号 |
C07C2/84 |
代理机构 |
Wilson Sonsini Goodrich & Rosati |
代理人 |
Wilson Sonsini Goodrich & Rosati |
主权项 |
1. A process for producing hydrocarbon compounds via oxidative coupling of methane (OCM), comprising:
combining a feedstock gas comprising methane with an oxygen-containing gas comprising oxygen to produce a combined gas; bringing the combined gas in contact with an OCM catalyst in an OCM reactor to generate an OCM reactor effluent stream that includes ethylene and unreacted methane; separating the OCM reactor effluent stream into at least a first stream, a second stream, and a third stream; expanding at least a portion of the first stream substantially isentropically to produce an expanded first stream and expanding at least a portion of the third steam substantially isentropically to produce an expanded third stream; directing the expanded first stream and the second stream to a separations unit to separate at least a portion of a mixture of the expanded first stream and the second stream into a first effluent stream comprising ethylene and a second effluent stream comprising unreacted methane, wherein the separations unit is operated at a first temperature that is less than 25° C. and at a first pressure that is greater than 1 atmosphere; and separating at least a portion of the second effluent stream and at least a portion of the expanded third stream in an additional separations unit to provide a methane-rich effluent and a nitrogen-rich effluent. |
地址 |
San Francisco CA US |