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    • 87. 发明申请
    • PROCESS FOR MAKING HCFO-1233zd
    • 制造HCFO-1233zd的方法
    • WO2016182715A1
    • 2016-11-17
    • PCT/US2016/029112
    • 2016-04-25
    • HONEYWELL INTERNATIONAL INC.
    • WANG, HaiyouTUNG, Hsueh SungCOTTRELL, Stephen A.
    • C07C17/25C07C17/42C07C19/10
    • C07C17/25C07C21/18
    • Disclosed is a process for the production of 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd) which includes reacting a propane feedstock comprising tetrachlorofluoropropanes, trichlorodifluoropropanes, dichlorotrifluoropropanes, or a mixture thereof, in the presence of a solid catalyst. The process generally comprises the following four steps: (i) providing a propane feedstock comprising trichlorodifluoropropanes and dichlorotrifluoropropanes, (ii) reacting the feedstock in a vapor phase reactor in the presence of HF and in the presence of a solid catalyst under conditions effective to form a product stream comprising HCFO-1233zd and unconverted starting materials, (iii) recovering or removing HCl and HF, and (iv) isolating HCFO-1233zd(E), HCFO-1233zd(Z), or both.
    • 公开了一种生产1-氯-3,3,3-三氟丙烯(HCFO-1233zd)的方法,其包括在固体催化剂存在下使包含四氯氟丙烷,三氯二氟丙烷,二氯三氟丙烷或其混合物的丙烷原料反应。 该方法通常包括以下四个步骤:(i)提供包含三氯二氟丙烷和二氯三氟氟丙烷的丙烷原料,(ii)使反应物在气相反应器中在HF存在下和在固体催化剂存在下在有效形成的条件下反应 包含HCFO-1233zd和未转化的起始材料的产物流,(iii)回收或除去HCl和HF,和(iv)分离HCFO-1233zd(E),HCFO-1233zd(Z)或两者。
    • 89. 发明申请
    • A METHOD FOR MITIGATING HFC-245CB FORMATION DURING HCFO-1233XF HYDROFLUORINATION TO HCFC-244BB
    • 在HCFO-1233XF氢化HCFC-244BB中减缓HFC-245CB形成的方法
    • WO2014164611A1
    • 2014-10-09
    • PCT/US2014/023000
    • 2014-03-11
    • HONEYWELL INTERNATIONAL INC.
    • WANG, HaiyouMERKEL, Daniel C.TUNG, Hsueh SungKOPKALLI, Haluk
    • C07C17/25C07C17/42C07C19/08
    • C07C17/23C07C17/087C07C17/206C07C17/25C07C19/10C07C21/18
    • 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.
    • 本方法涉及在含氟氢化催化剂存在下,在2-氯-3,3,3-三氟丙烯和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,包括 :(a)在氢氟化催化剂存在下,在有效形成2-氯-1,1,1,2-四氟丙烷的条件下,使HF与足够量的2-氯-3,3,3-三氟丙烯反应,氢氟化催化剂 以足够的量存在以催化所述反应,形成的2-氯-1,1,1,2-四氟丙烷的转化率大于80%,1,1,1,2,2-五氟丙烷选择性降低 超过20%; 和(b)保持2-氯-1,1,1,2-四氟丙烷的转化率为约80%以上,1,1,1,2,2-五氟丙烷选择性为约20%,或 较少的是通过以小的增量将所述氢氟化催化剂加入到反应器中。