Reactor for liquid phase fluorination reactions
    16.
    发明授权
    Reactor for liquid phase fluorination reactions 有权
    反应器用于液相氟化反应

    公开(公告)号:US09353028B2

    公开(公告)日:2016-05-31

    申请号:US14618500

    申请日:2015-02-10

    Abstract: The present invention relates to a hydrofluorinating process which comprises reacting a fluoroolefin with hydrogen fluoride in the liquid phase in the presence of a hydrofluorination catalyst in the reaction zone of a reactor, said reactor comprised of a reactor body having a length to diameter ratio of about 2:1 or greater; a stirred reaction zone containing said hydrofluorination catalyst, which may be prepared in situ, at least one inlet for supplying said hydrogen fluoride and fluoroolefin to the reaction zone and at least one outlet for recovering said fluoroalkane, said stirrer disposed in the reaction zone and comprising a plurality of blades fixedly attached to shaft drivable by a motor, said blades extending from about the bottom of the reaction zone to about the top of the reaction zone and said shaft extending on a longitudinal axis from the bottom of the reactor to the top of the reactor, said stirrer being rotated at a speed sufficient to promote a swirling of the liquid to effect the occurrence of hydrofluorination reaction and minimize overfluorination. The present invention also relates to said hydrofluorination reactor.

    Abstract translation: 本发明涉及一种氢氟化方法,其包括在反应器的反应区中在氟化氢催化剂存在下,在液相中使氟烯烃与氟化氢反应,所述反应器包括长径比为约 2:1或更大; 包含可以原位制备的所述氢氟化催化剂的搅拌反应区,至少一个用于将所述氟化氢和氟代烯烃供应到反应区的入口和用于回收所述氟烷烃的至少一个出口,所述搅拌器设置在反应区中并且包含 多个叶片固定地附接到由马达驱动的轴上,所述叶片从反应区域的底部延伸到反应区域的顶部,并且所述轴线在纵向轴线上从反应器底部延伸到顶部 反应器,所述搅拌器以足以促进液体旋转的速度旋转以实现氢氟化反应的发生并使过度氟化最小化。 本发明还涉及所述氢氟化反应器。

    METHOD FOR PROLONGING A CATALYST'S LIFE DURING HYDROFLUORINATION
    19.
    发明申请
    METHOD FOR PROLONGING A CATALYST'S LIFE DURING HYDROFLUORINATION 审中-公开
    在氢化过程中促进催化剂寿命的方法

    公开(公告)号:US20150152028A1

    公开(公告)日:2015-06-04

    申请号:US14604867

    申请日:2015-01-26

    Abstract: The invention provides an improved process to manufacture 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb) by reacting 2-chloro-3,3,3,-trifluoropropene (HCFO-1233xf) with hydrogen fluoride, in the presence of a fluorination catalyst, where by using 2-chloro-3,3,3,-trifluoropropene (HCFO-1233xf) of high purity, the need to add an oxidizing agent (typically chlorine) to keep the catalyst active can be avoided. The HCFC-244bb is then used as an intermediate in the production of 2,3,3,3-tetrafluoropropene-1 (HFO-1234yf).

    Abstract translation: 本发明提供了通过2-氯-3,3,3-三氟丙烯(HCFO-1233xf)与氟化氢反应制备2-氯-1,1,1,2-四氟丙烷(HCFC-244bb)的改进方法, 氟化催化剂的存在,其中通过使用高纯度的2-氯-3,3,3-三氟丙烯(HCFO-1233xf),可以避免添加氧化剂(通常为氯)以保持催化剂活性的需要 。 然后将HCFC-244bb用作生产2,3,3,3-四氟丙烯-1(HFO-1234yf)的中间体。

    METHOD FOR PRODUCING 2-CHLORO-3,3,3,-TRIFLUOROPROPENE (HCFC-1233xf)
    20.
    发明申请
    METHOD FOR PRODUCING 2-CHLORO-3,3,3,-TRIFLUOROPROPENE (HCFC-1233xf) 审中-公开
    生产2-氯-2,3,3, - 三氟硼酸(HCFC-1233xf)的方法

    公开(公告)号:US20150105595A1

    公开(公告)日:2015-04-16

    申请号:US14570283

    申请日:2014-12-15

    Abstract: The present invention relates to an improved method for manufacturing 2-chloro-3,3,3,-trifluoropropene (HCFC-1233xf) by reacting 1,1,2,3-tetrachloropropene, 1,1,1,2,3-pentachloropropane, and/or 2,3,3,3-tetrachloropropene with hydrogen fluoride, in a vapor phase reaction vessel in the presence of a vapor phase fluorination catalyst and stabilizer. HCFC-1233xf is an intermediate in the production of 2,3,3,3-tetrafluoropropene (HFO-1234yf) which is a refrigerant with low global warming potential.

    Abstract translation: 本发明涉及一种通过使1,1,2,3-四氯丙烯,1,1,1,2,3-五氯丙烷与1,1,3,3-四氯丙烯反应制备2-氯-3,3,3-三氟丙烯(HCFC-1233xf)的改进方法 ,和/或2,3,3,3-四氯丙烯与氟化氢在气相反应容器中在气相氟化催化剂和稳定剂存在下反应。 HCFC-1233xf是生产2,3,3,3-四氟丙烯(HFO-1234yf)的中间体,它是具有低全球变暖潜能的制冷剂。

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