(a) reacting HF with sufficient amount of 2-chloro-3,3,3-trifluoropropene in the presence of a hydrofluorination catalyst under conditions effective to form 2-chloro-1,1,1,2-tetrafluoropropane, the hydrofluorination catalyst being present in sufficient amounts to catalyze said reaction and the 2-chloro-1,1,1,2-tetrafluoropropane being formed with both a conversion of greater than 80% and a 1,1,1,2,2-pentafluoropropane selectivity lower than 20%; and(b) maintaining the 2-chloro-1,1,1,2-tetrafluoropropane being formed with both a conversion of about 80% or more and a 1,1,1,2,2-pentafluoropropane selectivity of about 20% or less by adding said hydrofluorination catalyst to the reactor in small increments."/> Method for mitigating HFC-245cb formation during HCFO-1233xf hydrofluorination to HCFC-244bb
首页> 外国专利> Method for mitigating HFC-245cb formation during HCFO-1233xf hydrofluorination to HCFC-244bb

Method for mitigating HFC-245cb formation during HCFO-1233xf hydrofluorination to HCFC-244bb

机译:减轻HCFO-1233xf加氢氟化为HCFC-244bb时HFC-245cb形成的方法

摘要

The present process relates to a method for minimizing the formation of 1,1,1,2,2-pentafluoropropane in a liquid phase reaction of 2-chloro-3,3,3-trifluoropropene and HF in the presence of a hydrofluorination catalyst comprising:(a) reacting HF with sufficient amount of 2-chloro-3,3,3-trifluoropropene in the presence of a hydrofluorination catalyst under conditions effective to form 2-chloro-1,1,1,2-tetrafluoropropane, the hydrofluorination catalyst being present in sufficient amounts to catalyze said reaction and the 2-chloro-1,1,1,2-tetrafluoropropane being formed with both a conversion of greater than 80% and a 1,1,1,2,2-pentafluoropropane selectivity lower than 20%; and(b) maintaining the 2-chloro-1,1,1,2-tetrafluoropropane being formed with both a conversion of about 80% or more and a 1,1,1,2,2-pentafluoropropane selectivity of about 20% or less by adding said hydrofluorination catalyst to the reactor in small increments.
机译:本发明涉及一种在氢氟酸催化剂存在下,在2-氯-3,3,3-三氟丙烯与HF的液相反应中使1,1,1,2,2-五氟丙烷的形成最小化的方法,所述方法包括: : (a)在有效形成2-氯-1,1,1,2-的条件下,在氢氟化催化剂存在下,HF与足够量的2-氯-3,3,3-三氟丙烯反应-四氟丙烷,氢氟化催化剂的存在量足以催化所述反应,并且形成的2-氯-1,1,1,2-四氟丙烷的转化率均大于80%,且1,2,1,1,2, 2-五氟丙烷的选择性低于20%;和 (b)维持形成的2-氯-1,1,1,2-四氟丙烷的转化率均达到或超过约80%通过将所述氢氟化催化剂以小增量加入到反应器中,得到的1,1,1,2,2-五氟丙烷选择性约为20%或更低。

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