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公开(公告)号:US09845281B2
公开(公告)日:2017-12-19
申请号:US15300566
申请日:2014-07-29
Applicant: Wanhua Chemical Group Co., Ltd.
Inventor: Junping Li , Haibo Chen , Lichang Zhang , Chunxian Cui , Yuan Li , Weiqi Hua , Jiansheng Ding , Junhua Zhang , Zhaokun Cheng
IPC: C07C67/26 , C08F220/06
CPC classification number: C07C67/26 , C07C69/54 , C08F220/06
Abstract: Hydroxyethyl (methyl)acrylate is prepared by a process of a combination of a three-stage tubular reactor and a tower reactor, wherein, firstly, a catalyst, a polymerization inhibitor and (methyl) acrylic acid are mixed until the solids are dissolved, then mixed with a part of ethylene oxide and thereafter enter into a first tubular reactor for a reaction, a reaction liquid flowing out from the first tubular reactor is mixed with a certain amount of ethylene oxide and enters into a second tubular reactor for a reaction, a reaction liquid flowing out from the second tubular reactor is then mixed with a certain amount of ethylene oxide and thereafter enters into a third tubular reactor, and a reaction liquid flowing out from the third tubular reactor is then passed through a stage of an adiabatic tower reactor and aged such that a product liquid is obtained from extraction.
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公开(公告)号:US20170183288A1
公开(公告)日:2017-06-29
申请号:US15300566
申请日:2014-07-29
Applicant: Wanhua Chemical Group Co., Ltd.
Inventor: Junping Li , Haibo Chen , Lichang Zhang , Chunxian Cui , Yuan Li , Weiqi Hua , Jiansheng Ding , Junhua Zhang , Zhaokun Cheng
IPC: C07C67/26 , C08F220/06
CPC classification number: C07C67/26 , C07C69/54 , C08F220/06
Abstract: Hydroxyethyl (methyl)acrylate is prepared by a process of a combination of a three-stage tubular reactor and a tower reactor, wherein, firstly, a catalyst, a polymerization inhibitor and (methyl) acrylic acid are mixed until the solids are dissolved, then mixed with a part of ethylene oxide and thereafter enter into a first tubular reactor for a reaction, a reaction liquid flowing out from the first tubular reactor is mixed with a certain amount of ethylene oxide and enters into a second tubular reactor for a reaction, a reaction liquid flowing out from the second tubular reactor is then mixed with a certain amount of ethylene oxide and thereafter enters into a third tubular reactor, and a reaction liquid flowing out from the third tubular reactor is then passed through a stage of an adiabatic tower reactor and aged such that a product liquid is obtained from extraction.
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