REACTOR FOR LIQUID PHASE FLUORINATION REACTIONS
    81.
    发明申请
    REACTOR FOR LIQUID PHASE FLUORINATION REACTIONS 审中-公开
    液相荧光反应器的反应器

    公开(公告)号:WO2015120234A1

    公开(公告)日:2015-08-13

    申请号:PCT/US2015/014759

    申请日:2015-02-06

    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 hyrdofluorination 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。 本发明还涉及所述二氟化反应器。

    PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE
    84.
    发明申请
    PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE 审中-公开
    生产2,3,3,3-四氯丙烯的方法

    公开(公告)号:WO2013055726A1

    公开(公告)日:2013-04-18

    申请号:PCT/US2012/059441

    申请日:2012-10-10

    CPC classification number: C07C17/25 B01J19/02 B01J2219/0277 C07C21/18

    Abstract: The present invention relates, in part, to the discovery that the presence of impurities in a reactor for dehydrochlorinating HCFC-244bb to HFO-1234yf results in selectivity changeover from HFO-1234yf to HCFO-1233xf. By substantially removing such impurities, it is shown that the selectivity to HFO-1234yf via dehydrochlorination of HCFC-244bb is improved.

    Abstract translation: 本发明部分地涉及这样的发现,即将HCFC-244bb脱氯化氢反应成HFO-1234yf的反应器中的杂质的存在导致从HFO-1234yf到HCFO-1233xf的选择性转换。 通过基本上除去这些杂质,显示通过HCFC-244bb的脱氯化氢对HFO-1234yf的选择性得到改善。

    PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE
    85.
    发明申请
    PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE 审中-公开
    生产2,3,3,3-四氯丙烯的方法

    公开(公告)号:WO2013055722A1

    公开(公告)日:2013-04-18

    申请号:PCT/US2012/059437

    申请日:2012-10-10

    CPC classification number: C07C17/087 C07C17/206 C07C17/25 C07C21/18 C07C19/10

    Abstract: The present invention relates, in part, to the discovery that the presence of impurities in a reactor for dehydrochlorinating HCFC-244bb to HFO-1234yf results in a reduced conversion rate and/or a selectivity changeover from HFO-1234yf to HCFO-1233xf. By substantially removing such impurities, it is shown that the conversion rate may be improved and selectivity to HFO-1234yf via dehydrochlorination of HCFC-244bb is also improved.

    Abstract translation: 本发明部分地涉及以下发现,即将HCFC-244bb脱氯化氢反应到HFO-1234yf的反应器中的杂质的存在导致从HFO-1234yf到HCFO-1233xf的转化率和/或选择性转换的降低。 通过基本上除去这些杂质,可以看出可以提高转化率,并且通过HCFC-244bb的脱氯化氢还能改善对HFO-1234yf的选择性。

    PROCESS FOR PRODUCING TRANS-1233zd
    88.
    发明申请

    公开(公告)号:WO2012145188A3

    公开(公告)日:2012-10-26

    申请号:PCT/US2012/032830

    申请日:2012-04-10

    Abstract: Trans-1233zd, the trans-isomer of 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd) can be used as blowing agents, solvents, cleaning agents, as well as monomers of macromolecule compounds, and can be prepared through the dehydrochlorination of 1,1,1-trifluoro-3,3-dichloropropane (HCFC-243fa) with the help of a catalyst. The present invention is directed to an integrated process is proposed to produce trans-1233zd from 243fa, which is consisted of the following four major unit operations: (1) Catalytic dehydrochlorination of 243fa into trans/cis-1233zd, (2) HCl recovery, (3) Catalytic isomerization of cis-1233zd into trans-1233zzd, and (4) Isolation of trans-1233zd.

    PROCESS FOR PRODUCING TRANS-1233zd
    89.
    发明申请
    PROCESS FOR PRODUCING TRANS-1233zd 审中-公开
    生产TRANS-1233zd的方法

    公开(公告)号:WO2012145188A2

    公开(公告)日:2012-10-26

    申请号:PCT/US2012032830

    申请日:2012-04-10

    Abstract: Trans-1233zd, the trans-isomer of 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd) can be used as blowing agents, solvents, cleaning agents, as well as monomers of macromolecule compounds, and can be prepared through the dehydrochlorination of 1,1,1-trifluoro-3,3-dichloropropane (HCFC-243fa) with the help of a catalyst. The present invention is directed to an integrated process is proposed to produce trans-1233zd from 243fa, which is consisted of the following four major unit operations: (1) Catalytic dehydrochlorination of 243fa into trans/cis-1233zd, (2) HCl recovery, (3) Catalytic isomerization of cis-1233zd into trans-1233zzd, and (4) Isolation of trans-1233zd.

    Abstract translation: 反式1233zd,1-氯-3,3,3-三氟丙烯(HCFO-1233zd)的反式异构体可用作发泡剂,溶剂,清洗剂以及大分子化合物的单体,并可通过 借助催化剂对1,1,1-三氟-3,3-二氯丙烷(HCFC-243fa)进行脱氯化氢。 本发明涉及从243fa生产反式1233zd的综合方法,其由以下四个主要单元操作组成:(1)将243fa催化脱氯化氢转化成反式/顺式1233zd,(2)HCl回收, (3)顺式1233zd催化异构化为反式-1233zzd,(4)反式-1233zd的分离。

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