Preparation of 1,1,1,3-tetrafluoropropene( 1234ze )
    1.
    发明公开
    Preparation of 1,1,1,3-tetrafluoropropene( 1234ze ) 有权
    Herstellung von 1,1,1,3-四氟丙烯(1234ze)

    公开(公告)号:EP0974571A2

    公开(公告)日:2000-01-26

    申请号:EP99305781.9

    申请日:1999-07-21

    CPC classification number: C07C17/25 C07C21/18

    Abstract: Disclosed is a process for the preparation of cis/trans 1,1,1,3-tetrafluoro-2-propene (1234 ze) which comprises (a) contacting 1,1,1,3,3-pentafluoropropane (245fa) with an alkaline solution, preferably an aqueous or alcoholic solution of a base such as KOH, NaOH, Ca(OH) 2 or Mg(OH) 2 , or with a chromium-based catalyst, such as fluorided Cr 2 O 3 or fluorided Cr/Ni/Alf 3 , and (b) recovering cis/trans 1,1,1,3-tetrafluoro-2-propene from the reaction mixture.

    Abstract translation: 公开了一种制备顺式/反式1,1,1,3-四氟-2-丙烯(1234 ze)的方法,其包括(a)使1,1,1,3,3-五氟丙烷(245fa)与 碱性溶液,优选碱如KOH,NaOH,Ca(OH)2或Mg(OH)2的水溶液或醇溶液,或与铬基催化剂如氟化Cr 2 O 3或氟化Cr / Ni / Alf 3, 和(b)从反应混合物中回收顺/反1,1,1,3-四氟-2-丙烯。

    Gas phase fluorination of 1,1,3,3-tetrachloro-2-propene
    6.
    发明公开
    Gas phase fluorination of 1,1,3,3-tetrachloro-2-propene 失效
    在气相1,1,3,3- -Tetrachloro -2-丙烯的氟化

    公开(公告)号:EP0919527A1

    公开(公告)日:1999-06-02

    申请号:EP98304230.0

    申请日:1998-05-28

    CPC classification number: C07C17/00 C07C17/21 C07C21/18 C07C19/08

    Abstract: A process for the fluorination of 1230za is provided, wherein 1230za is contacted with HF in the gas phase in the presence of an aluminum fluoride or chromium-based fluorination catalyst under conditions sufficient to produce a reaction mixture containing 1233zd, 1234ze and 245fa. 245fa is a known foam blowing agent and refrigerant, while 1233zd and 1234ze are known intermediates useful for preparing 245fa.

    Process for the production of 1,1,1-trifluoroethane
    9.
    发明公开
    Process for the production of 1,1,1-trifluoroethane 失效
    生产1,1,1-三氟乙烷的方法

    公开(公告)号:EP0714874A1

    公开(公告)日:1996-06-05

    申请号:EP95114300.7

    申请日:1995-09-12

    CPC classification number: C07C17/206 B01J27/125 B01J27/128 C07C19/08

    Abstract: Process for synthesizing 1,1,1-trifluoroethane (143a) in the gaseous phase by reacting 1,1-defluoro-1-chloroethane in gaseous phase in the presence of a Cr catalyst. The process may be run isothermally or adiabatically, without co-feeding air or other oxygen containing gas, in the presence or absence of a Ni, Co, Zn or Mn cocatalyst for the Cr catalyst. The catalyst may be unsupported or supported with a support preferably selected from activated carbon, alumina and fluorided alumina. The formation of olefin byproduct can be kept to less than 10 ppm in accordance with the process of the invention.

    Abstract translation: 通过使1,1-二氟-1-氯乙烷在气相中在Cr催化剂存在下反应合成气相中的1,1,1-三氟乙烷(143a)的方法。 该方法可以在存在或不存在用于Cr催化剂的Ni,Co,Zn或Mn助催化剂的情况下等温或绝热地运行,而无需共同进料空气或其它含氧气体。 所述催化剂可以不被载体或载体优选选自活性炭,氧化铝和氟化氧化铝。 根据本发明的方法,可以将烯烃副产物的形成保持在小于10ppm。

    1,1,1-Trifluoroethane synthesis using a supported lewis acid
    10.
    发明公开
    1,1,1-Trifluoroethane synthesis using a supported lewis acid 失效
    上支持使用路易斯酸1,1,1-三氟乙烷的制备

    公开(公告)号:EP0712826A1

    公开(公告)日:1996-05-22

    申请号:EP95113522.7

    申请日:1995-08-29

    CPC classification number: C07C17/206 C07C19/08

    Abstract: Process for synthesizing 1,1,1-trifluoroethane (143a) in the gaseous phase by reacting 1,1-difluoro-1-chloroethane in gaseous phase in the presence of a catalyst selected from the SbV, TiIV,and SnIV salts. The process may be run without co-feeding chlorine gas as a coactivator, in the presence or absence of an impurity selected from HCl and 141b. The catalyst may be unsupported or supported on activated carbon. The formation of olefin byproduct was not detected when the process of the invention was conducted under the conditions described.

    Abstract translation: 过程用于通过从SBV,TiIV和SnIV盐的催化剂的存在下在气相中起反应的1,1-二氟-1-氯乙烷在气相中合成1,1,1-三氟乙烷(143A)。 该过程可以在没有共进料的氯气作为共活化剂运行,在从盐酸和141b选择的杂质的存在或不存在。 该催化剂可以是未负载或负载在活性炭上。 烯烃副产物的形成没有检测到什么时候所述的条件下什么进行的本发明的方法。

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