Process for the manufacture of halogenated propanes containing
end-carbon fluorine
    1.
    发明授权
    Process for the manufacture of halogenated propanes containing end-carbon fluorine 有权
    制造含有末端碳氟的卤代丙烷的方法

    公开(公告)号:US6066769A

    公开(公告)日:2000-05-23

    申请号:US155841

    申请日:1998-10-06

    摘要: A process is disclosed for producing a compound of the formula: CF.sub.3 CHXCF.sub.3-z Y.sub.2 where X and Y are independently selected from the group consisting of H and Cl, and z is 0 or 1. The process involves (1) contacting CCl.sub.3 CHXCC.sub.3-z Y.sub.z,CCl.sub.2-z .dbd.CXCC.sub.3, and/or CCl.sub.2 CX.dbd.CC.sub.3-z Y.sub.z starting material, with hydrogen fluoride at a temperature of less than 200.degree. C. to produce a fluorination product of said starting material which includes at least 90 mole percent total of C.sub.3 HXY.sub.z Cl.sub.6-z-x F.sub.x saturated compounds and C.sub.3 XY.sub.z Cl.sub.5-z-y F.sub.y olefinic compounds, wherein x is an integer from 1 to 6-z and y is an integer from 1 to 5-z, (the fluorination product including no more than about 40 mole percent of the desired product, CF.sub.3 CHXCF.sub.3-z Y.sub.z); (2) contacting saturated compounds and olefinic compounds produced in (1) with hydrogen fluoride in the vapor phase at a temperature of from 200.degree. C. to about 400.degree. C. in the presence of a fluorination catalyst; and (3) reacting a sufficient amount of said compounds, wherein x is an integer from 1 to 5-z and olefinic compounds produced in (1) with hydrogen fluoride in the vapor phase at a temperature of from 200.degree. C. to about 400.degree. C. in the presence of a vapor phase fluorination catalyst to provide an overall selectivity to CF.sub.3 CHXCF.sub.3-z Y.sub.z of at least about 90 percent based upon the amount of starting material reacted with HF in (1) and (2).

    摘要翻译: PCT No.PCT / US97 / 06013 371 1998年10月6日第 102(e)日期1998年10月6日PCT 1997年4月4日PCT PCT。 WO97 / 37956 PCT公开号 日期1997年10月16日公开了制备下式化合物的方法:CF 3 CHXCF 3 -ZY 2其中X和Y独立地选自H和Cl,z是0或1.该方法包括(1) CCl 3 CHXCC 3 -ZYz,CCl 2 -Z = CXCC 3和/或CCl 2 C X = CCl 3 -ZYz起始原料,在低于200℃的温度下加入氟化氢,以产生所述原料的氟化产物,其包含至少90摩尔% 总共C3HXYzCl6-z-xFx饱和化合物和C3XYzCl5-z-yFy烯属化合物,其中x是1至6-z的整数,y是1至5-z的整数(氟化产物不超过约 40摩尔%的所需产物,CF 3 CHXCF 3 -ZYz); (2)在氟化催化剂存在下,将温度为200℃至约400℃的气相中的(1)中产生的饱和化合物和烯烃化合物与氟化氢接触; 和(3)将足量的所述化合物(其中x是1至5-z的整数)和(1)中制备的烯烃化合物与气相中的氟化氢在200℃至约400℃的温度下反应 在气相氟化催化剂的存在下,基于在(1)和(2)中与HF反应的原料的量,提供至少约90%的CF 3 CHXCF 3 -ZYz的总体选择性。

    Processes for producing 2,3,3,3-tetrafluoropropene, a process for producing 1-chloro-2,3,3,3-pentafluoropropane and azeotropic compositions of 1-chloro-2,3,3,3-tetrafluoropropene with HF

    公开(公告)号:US07906693B2

    公开(公告)日:2011-03-15

    申请号:US12442955

    申请日:2007-10-31

    IPC分类号: C07C17/00 C07C19/08

    摘要: A process is disclosed for making CH2═CFCF3. The process involves contacting CH2ClCF2CF3 with H2 in a reaction zone in the presence of a catalyst including a catalytically effective amount of palladium supported on a support selected from chromium oxide, fluorinated chromium oxide, chromium fluoride, aluminum oxide, aluminum fluoride and/or fluorinated alumina, to produce CH2═CFCF3. The mole ratio of H2 to the CH2ClCF2CF3 fed to the reaction zone is between about 1:1 and about 4:1. Also disclosed is another process for making CH2═CFCF3 that involves (a) reacting CH2ClCF2CF3 with H2 in the presence of a catalytically effective amount of hydrogenation catalyst to form CH3CF2CF3; and (b) dehydrofluorinating CH3CF2CF3 from (a) to form CH2═CFCF3; and another process for making CH2═CFCF3 that involves (1) dehydrofluorinating CH2ClCF2CF3 in the presence of a catalytically effective amount of dehydrofluorination catalyst to form CHCl═CFCF3; and (2) hydrogenating CHCl═CFCF3 from (1) in the presence of a hydrogenation catalyst including a catalytically effective amount of palladium supported on a support selected from chromium oxide, fluorinated chromium oxide, chromium fluoride, aluminum oxide, aluminum fluoride and/or fluorinated alumina to form CH2═CFCF3. Also disclosed is a process for making CH2ClCF2CF5. This process involves reacting CH2ClF with CF2═CF2 in a reaction zone in the presence of a catalytically effective amount of an aluminum halide composition having a bulk formula of AlClxBryF3-x-y wherein the average value of x is 0 to 3, the average value of y is 0 to 3-x, provided that the average values of x and y are not both 0. Also disclosed is an azeotropic composition including CF3CF═CHCl and HF.

    PROCESSES FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE, A PROCESS FOR PRODUCING 1-CHLORO-2,3,3,3-PENTAFLUOROPROPANE AND AZEOTROPIC COMPOSITIONS OF 1-CHLORO-2,3,3,3-TETRAFLUOROPROPENE WITH HF

    公开(公告)号:US20100076231A1

    公开(公告)日:2010-03-25

    申请号:US12442955

    申请日:2007-10-31

    IPC分类号: C07C17/25 C07C17/278

    摘要: A process is disclosed for making CH2═CFCF3. The process involves contacting CH2ClCF2CF3 with H2 in a reaction zone in the presence of a catalyst including a catalytically effective amount of palladium supported on a support selected from chromium oxide, fluorinated chromium oxide, chromium fluoride, aluminum oxide, aluminum fluoride and/or fluorinated alumina, to produce CH2═CFCF3. The mole ratio of H2 to the CH2ClCF2CF3 fed to the reaction zone is between about 1:1 and about 4:1. Also disclosed is another process for making CH2═CFCF3 that involves (a) reacting CH2ClCF2CF3 with H2 in the presence of a catalytically effective amount of hydrogenation catalyst to form CH3CF2CF3; and (b) dehydrofluorinating CH3CF2CF3 from (a) to form CH2═CFCF3; and another process for making CH2═CFCF3 that involves (1) dehydrofluorinating CH2ClCF2CF3 in the presence of a catalytically effective amount of dehydrofluorination catalyst to form CHCl═CFCF3; and (2) hydrogenating CHCl═CFCF3 from (1) in the presence of a hydrogenation catalyst including a catalytically effective amount of palladium supported on a support selected from chromium oxide, fluorinated chromium oxide, chromium fluoride, aluminum oxide, aluminum fluoride and/or fluorinated alumina to form CH2═CFCF3. Also disclosed is a process for making CH2ClCF2CF5. This process involves reacting CH2ClF with CF2═CF2 in a reaction zone in the presence of a catalytically effective amount of an aluminum halide composition having a bulk formula of AlClxBryF3-x-y wherein the average value of x is 0 to 3, the average value of y is 0 to 3-x, provided that the average values of x and y are not both 0. Also disclosed is an azeotropic composition including CF3CF═CHCl and HF.

    Tetrafluoropropene Production Processes
    10.
    发明申请
    Tetrafluoropropene Production Processes 有权
    四氟丙烯生产工艺

    公开(公告)号:US20090127496A1

    公开(公告)日:2009-05-21

    申请号:US12301070

    申请日:2007-06-22

    IPC分类号: C09K5/00 C07C17/25

    摘要: A process is disclosed for the manufacture of CF3CF═CH2 and CF3CH═CHF. The process involves dehydrofluorinating CF3CHFCH2F in the presence of a dehydrofluorination catalyst to produce a product mixture comprising CF3CF═CH2 and CF3CH═CHF, and recovering said CF3CF═CH2 and CF3CH═CHF from the product mixture.The present invention also provides a composition comprising (a) the Z-isomer of CF3CH═CHF and (b) HF; wherein the HF is present in an effective amount to form an azeotropic combination with the Z—CF3CH═CHF.

    摘要翻译: 公开了用于制造CF 3 CF-CH 2和CF 3 CH-CHF的方法。 该方法包括在脱氟化氢催化剂的存在下对CF 3 CHFCH 2 F进行脱氟化氢,以产生包含CF 3 CF-CH 2和CF 3 CH-CHF的产物混合物,并从产物混合物回收所述CF 3 CF-CH 2和CF 3 CH-CHF。 本发明还提供一种组合物,其包含(a)CF 3 CH-CHF的Z-异构体和(b)HF; 其中HF以有效量存在以与Z-CF 3 CH-CHF形成共沸组合。