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公开(公告)号:US11312823B2
公开(公告)日:2022-04-26
申请号:US16622964
申请日:2018-06-26
申请人: DIC Corporation
发明人: Masaya Kadoki , Saori Nara , Taku Ibaraki , Hideki Watanabe , Satoshi Inoue
IPC分类号: C08G75/0259 , C08G75/0213 , C08G75/0254 , C08J3/20 , C08J5/00
摘要: Provided is a method for producing a polyarylene sulfide resin, the method including subjecting a dihaloaromatic compound and a sulfidizing agent to a polymerization reaction in the presence of an aliphatic cyclic compound having a ring openable by hydrolysis, in which corrosion of a production apparatus is suppressed. More particularly, provided is a method for producing a polyarylene sulfide resin, the method including a dehydration step (1) in which a water-containing sulfidizing agent and an aliphatic cyclic compound having a ring openable by hydrolysis are heated in the presence of a dihaloaromatic compound to a liquid temperature in the range of 90° C. or higher and 170° C. or lower under the atmospheric pressure, and then dehydration is performed while maintaining the liquid temperature and reducing the pressure to a pressure in the range of 30 [kPa abs] or higher and 80 [kPa abs] or lower to thus obtain a mixture.
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公开(公告)号:US20210147630A1
公开(公告)日:2021-05-20
申请号:US16622964
申请日:2018-06-26
申请人: DIC Corporation
发明人: Masaya Kadoki , Saori Nara , Taku Ibaraki , Hideki Watanabe , Satoshi Inoue
IPC分类号: C08G75/0259 , C08G75/0254 , C08G75/0213 , C08J5/00 , C08J3/20
摘要: Provided is a method for producing a polyarylene sulfide resin, the method including subjecting a dihaloaromatic compound and a sulfidizing agent to a polymerization reaction in the presence of an aliphatic cyclic compound having a ring openable by hydrolysis, in which corrosion of a production apparatus is suppressed. More particularly, provided is a method for producing a polyarylene sulfide resin, the method including a dehydration step (1) in which a water-containing sulfidizing agent and an aliphatic cyclic compound having a ring openable by hydrolysis are heated in the presence of a dihaloaromatic compound to a liquid temperature in the range of 90° C. or higher and 170° C. or lower under the atmospheric pressure, and then dehydration is performed while maintaining the liquid temperature and reducing the pressure to a pressure in the range of 30 [kPa abs] or higher and 80 [kPa abs] or lower to thus obtain a mixture.
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