发明名称 CONTINUOUS LOW-TEMPERATURE PROCESS TO PRODUCE TRANS-1-CHLORO-3,3,3-TRIFLUOROPROPENE
摘要 Disclosed is process for the production of (E) 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd(E)) by conducting a continuous reaction without the use of a catalyst. Also disclosed is an integrated system including one or more reactors for producing hydrofluoro olefins, particularly 1233zd(E). The manufacturing process includes six major unit operations: (1) a fluorination reaction of HCC-240fa (in continuous or semi-batch mode) using HF with simultaneous removal of by-product HCl and the product 1233zd(E); (2) recycle of unreacted HCC-240fa and HF together with under-fluorinated by-products back to (1); (3) separation and purification of by-product HCl; (4) separation of excess HF back to (1); (5) purification of final product, 1233zd(E); and (6) isomerization of by-product 1233zd(Z) to 1233zd(E) to maximize the process yield.
申请公布号 US2014206910(A1) 申请公布日期 2014.07.24
申请号 US201414195899 申请日期 2014.03.04
申请人 Honeywell International Inc. 发明人 Pokrovski Konstantin A.;Merkel Daniel C.;Tung Hsueh Sung
分类号 C07C17/20;C07C17/358 主分类号 C07C17/20
代理机构 代理人
主权项 1. A method for the production of (E) 1-chloro-3,3,3-trifluoropropene without the use of a catalyst comprising the steps of; (a) operating one or more agitated reaction vessels, each vessel in succession converting a portion of the original reactants fed to the first of the reaction vessels, with all of the reaction vessels being run simultaneously and operating in a continuous fashion; (b) conducting, in each of the reaction vessels, a series of fluorination reactions of a starting material selected from the group consisting of 1,1,1,3,3-pentachloropropane, 1,1,1,3,3-pentachloropropane, 1,1,3,3-tetrachloropropene, and 1,3,3,3-tetrachloropropene, and any mixtures thereof, using HF with simultaneous removal of by-product HCl and the product (E) 1-chloro-3,3,3-trifluoropropene; (c) recycling at least a portion of any unreacted starting material and HF together with any under-fluorinated by-products back to step (b); (d) separating and purifying by-product HCl; (e) separating excess HF back to step (b); (f) purifying the desired product, (E) 1-chloro-3,3,3-trifluoropropene; and (g) isomerization any by-product (Z) 1-chloro-3,3,3-trifluoropropene to (E) 1-chloro-3,3,3-trifluoropropene to maximize the process yield.
地址 Morristown NJ US