发明名称 METHOD FOR THE PRODUCTION OF ETHYLENE OXIDE
摘要 A method for the production of ethylene oxide wherein the partial pressure of water vapor at the inlet of the reactor is at least about 8 kPa using a high purity carrier comprising alpha-alumina, a promoting amount of at least one Group IA metal, and a promoting amount of rhenium.
申请公布号 US2016016924(A1) 申请公布日期 2016.01.21
申请号 US201414773784 申请日期 2014.03.12
申请人 DOW TECHNOLOGY INVESTMENTS LLC 发明人 Zhang Liping;McAdon Mark H.;Frank Ernest R.
分类号 C07D301/10;C07C29/132 主分类号 C07D301/10
代理机构 代理人
主权项 1. A method of producing ethylene oxide comprising: a) providing to a reactor a reactor inlet gas mixture comprising ethylene, oxygen, one or more gas phase promoters, water and carbon dioxide, wherein the one or more gas phase promoters are organic chlorides, the components of the gas mixture subsequently being contacted within the reactor under epoxidation reaction conditions with a catalyst comprising a catalytically effective amount of silver supported on a high purity carrier, a promoting amount of at least one Group IA metal, and a promoting amount of rhenium; b) yielding from the reactor a reactor outlet gas mixture comprising ethylene oxide, ethylene, oxygen, water and carbon dioxide; c) providing at least a portion of the reactor outlet gas mixture to an ethylene oxide absorber to produce an ethylene oxide stream and a treated gas stream comprising water and carbon dioxide; d) providing at least a portion of the treated gas stream to a carbon dioxide absorber unit; e) operating the carbon dioxide absorber unit to produce a recycle gas stream comprising carbon dioxide and water; and f) combining at least a portion of the recycle gas stream from the carbon dioxide absorber unit with fresh feeds comprising oxygen and ethylene and at least a portion of a remaining portion, if any, of the treated gas stream, to form the reactor inlet gas mixture, wherein:(i) a partial pressure of water vapor at the reactor inlet is at least about 8 kPa; and(ii) the partial pressure of water vapor at the reactor inlet is continuously maintained at at least about 8 kPa over a period corresponding to the production of at least 250 kmole of ethylene oxide per cubic meter of catalyst.
地址 Midland MI US