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Method for co-producing 2,3,3,3-tetrafluoropropene and trans-1,3,3,3-tetrafluoropropene

机译:共同制备2,3,3,3-四氟丙烯和反式1,3,3,3,3,3-四氟丙烯的方法

摘要

Disclosed is a method for co-producing 2,3,3,3-tetrafluoropropene and trans-1,3,3,3-tetrafluoropropene, comprising the following steps: preheating a mixture of 1,1,1,2,2-pentachloropropane and 1,1,1,3,3-pentachloropropane together with anhydrous hydrogen fluoride and simultaneously introducing into a first reactor to react in the presence of a catalyst La2O3—Cr2O3 to obtain a first reactor product; directly introducing the first reactor product into a second reactor without separation, and carrying out a catalytic fluorination reaction in the presence of a catalyst Ga2O3—Y2O3—Cr2O3 to obtain a second reactor product; and separating the second reactor product to obtain the products of 2,3,3,3-tetrafluoropropene and trans-1,3,3,3-tetrafluoropropene. The invention has such advantages that the process is simple and less equipment investment is required; used catalysts have good activity, high selectivity and long total life; and the ratio of the two products can be flexibly adjusted according to market demands.
机译:公开了一种共同生产2,3,3,3-四氟丙烯和反式-1,3,3,3-四氟丙烯的方法,包括以下步骤:预热1,1,1,2,2-五氯丙丙烷的混合物和1,1,1,3,3-五氯丙丙烷与无水氟化氢,并同时将第一反应器引入第一反应器中以在催化剂La 2 O 3 的存在下反应-CR <亚> 2 O 3 获得第一反应器产品;直接将第一反应器产物引入第二反应器而不分离,并在催化剂Ga 2 O 3 -y 2的存在下进行催化氟化反应 O 3 -cr 2 O 3 获得第二反应器产品;并将第二反应器产物分离以获得2,3,3,3-四氟丙烯和反式-1,3,3,3,3-四氟丙烯的产物。本发明具有这样的优势,即该过程简单,需要更少的设备投资;二手催化剂具有良好的活性,选择性高,寿命长;并且可以根据市场需求灵活地调整两种产品的比例。

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