发明名称 ETHYLENE-TO-LIQUIDS SYSTEMS AND METHODS
摘要 Integrated systems are provided for the production of higher hydrocarbon compositions, for example liquid hydrocarbon compositions, from methane using an oxidative coupling of methane system to convert methane to ethylene, followed by conversion of ethylene to selectable higher hydrocarbon products. Integrated systems and processes are provided that process methane through to these higher hydrocarbon products.
申请公布号 US2016368834(A1) 申请公布日期 2016.12.22
申请号 US201615076436 申请日期 2016.03.21
申请人 Siluria Technologies, Inc. 发明人 Nyce Greg;Czerpak Peter;Faz Carlos;McCormick Jarod;Michalak William;Patel Bipinkumar;Radaelli Guido;Rappold Tim A.;Runnebaum Ron;Scher Erik C.;Zhang Aihua;Cizeron Joel
分类号 C07C2/12 主分类号 C07C2/12
代理机构 代理人
主权项 1. A system, comprising: an ethylene-to-liquids (ETL) reactor that (i) receives an olefin feed stream at a first temperature, said olefin feed stream comprising (1) ethylene (C2H4) at a concentration of at least about 0.5 mole percent (mol %), (2) C2H4 and propylene (C3H6) at a combined concentration of at most about 10 mol %, and (3) carbon monoxide (CO) or carbon dioxide (CO2), and (ii) as part of an ETL process, facilitates conversion of C2H4 to higher hydrocarbon products with the aid of an ETL catalyst to yield a product stream comprising said higher hydrocarbon products that is at a second temperature which is higher than said first temperature, wherein said ETL process liberates heat; and a separations module in fluid communication with said ETL reactor that recovers from said product stream a liquid stream comprising said higher hydrocarbon products, wherein said higher hydrocarbon products include (i) at least 5 compounds having 5 different carbon numbers, said 5 carbon numbers selected from 4 through 20, wherein each of said at least 5 carbon numbers is at a concentration of at least 5 weight percent (wt %) of said liquid stream, and (ii) a paraffin compound, an isoparaffin compound, and a naphthene compound, wherein during use, at least about 80% of said heat liberated in said ETL process provides a difference between said first temperature and said second temperature of between about 50° C. and about 150° C.
地址 San Francisco CA US