发明名称 1, 3, 3, 3-tetrafluoropropene preparation process
摘要 Disclosed is an HFO-1234ze preparation process. The present invention is realized by loading two fluorination catalysts into the same reactor, and controlling the temperature in each section. The preparation process of the present invention is of moderate reaction condition, stable catalyst activity, and simple process.
申请公布号 US9458070(B2) 申请公布日期 2016.10.04
申请号 US201314653510 申请日期 2013.12.17
申请人 SINOCHEM MODERN ENVIRONMENTAL PROTECTION CHEMICALS (XI'AN) CO., LTD.;Sinochem Lantian Co., Ltd. 发明人 Xu Lei;Yang Gang;Yang Huie;Chen Shukang;Zhao Zhixia
分类号 C07C17/25;C07C17/383;C07C17/20 主分类号 C07C17/25
代理机构 Osha Liang LLP 代理人 Osha Liang LLP
主权项 1. A method for preparing 1,1,3-Tetrafluorontopene (HFO-1234ze), characterized in that the method comprises the following steps: (1) charging a reactor with a fluorination catalyst in two sections, wherein the first section of the fluorination catalyst is controlled at a temperature of 200-300° C., and the second section of the fluorination catalyst is controlled at a temperature of 350-450° C.; and (2) introducing a gasified HF with 1,1,1,3,3-pentachloropropane (HCC-240fa) and/or 1,1,3,3-tetrachloro-prop-1-ene (HCO- 1230za) into the reactor, passing through the first section of the fluorination catalyst and then through the second section of the fluorination catalyst, wherein a molar ratio of HF to the total organic phase is from 5:1 to 20:1, a contact time for the reaction is 1-30 seconds, and a reaction pressure is 0.1-1.2 MPa, forming a product stream; and (3) passing the product stream through a distillation tower; wherein: a stream containing HFO-1234ze and HCl is formed at the top of the distillation tower and the stream is further treated to remove acid and water and distilled to produce HFO-1234ze;a material stream containing 1-chloro-3,3,3-trifluoropropene (HCFC-1233zd), 1,1,1,3,3-pentafluoropropane(HFC-245fa) and HF is formed in a pot at the bottom of the distillation tower; andthe pressure in the distillation tower is 0.1 -0.6 MPa, a temperature at the top of the tower is −30-10° C. and the temperature in the pot at the bottom of the distillation tower 40-80° C.
地址 Shaanxi CN