发明名称 Process for producing 1,3,3,3-tetrafluoropropene
摘要 According to the first characteristic of the present invention, there is provided a production process for 1,3,3,3-tetrafluoropropene including: the first step of reacting 1,1,1,3,3-pentachloropropane with hydrogen fluoride thereby obtaining 1-chloro-3,3,3-trifluoropropene; and the second step of reacting 1-chloro-3,3,3-trifluoropropene obtained in the first step with hydrogen fluoride in a gaseous phase in the presence of a fluorination catalyst. According to the second characteristic of the present invention, there is provided a dehydration process including bringing 1,3,3,3-tetrafluoropropene containing at least water into contact with zeolite.
申请公布号 US9051231(B2) 申请公布日期 2015.06.09
申请号 US200913119658 申请日期 2009.09.24
申请人 Central Glass Company, Limited 发明人 Sakyu Fuyuhiko;Yoshikawa Satoshi;Okamoto Satoru;Hibino Yasuo;Nishiguchi Yoshio
分类号 C07C17/20;C07C17/38 主分类号 C07C17/20
代理机构 Crowell & Moring LLP 代理人 Crowell & Moring LLP
主权项 1. A process for producing 1,3,3,3-tetrafluoropropene, comprising: a) a first step of reacting 1,1,1,3,3-pentachloropropane with hydrogen fluoride in a liquid phase and in the absence of the fluorination catalyst, within a reaction pressure range of 0.5 to 4.2 MPa, and within a reaction temperature range of 100° C. to 160° C., thereby obtaining 1-chloro-3,3,3-trifluoropropene, wherein 1,1,1,3,3-pentachloropropane and hydrogen fluoride are introduced into a reaction system while hydrogen chloride and 1-chloro-3,3,3-trifluoropropene generated from the reaction are extracted from the reaction system; and b) a second step of reacting 1-chloro-3,3,3-trifluoropropene obtained by the first step with hydrogen fluoride in a gaseous phase and in the presence of a fluorination catalyst.
地址 Ube-shi JP