PROCESS FOR SEPARATING HYDROGEN FLUORIDE FROM ORGANIC FEEDSTOCKS
    131.
    发明申请
    PROCESS FOR SEPARATING HYDROGEN FLUORIDE FROM ORGANIC FEEDSTOCKS 有权
    从有机饲料中分离氟化氢的方法

    公开(公告)号:US20090287027A1

    公开(公告)日:2009-11-19

    申请号:US12464666

    申请日:2009-05-12

    IPC分类号: C07C19/08

    摘要: Provided is a process for purifying an organic feedstock comprising (a) distilling a raw organic feedstock comprising hydrogen fluoride, 2-chloro-1,1,1,2-tetrafluoropropane, and 2-chloro-3,3,3-trifluoropropene to produce a first distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a first bottoms stream rich in hydrogen fluoride; (b) cooling said first distillate stream to produce an intermediate composition comprising an organic layer rich in 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene, and an acid layer rich in hydrogen fluoride; and, optionally but preferably, (c) distilling said organic layer to produce a second distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a second bottoms stream comprising a purified organic feedstock substantially free of hydrogen fluoride.

    摘要翻译: 提供了一种纯化有机原料的方法,其包括(a)蒸馏包含氟化氢,2-氯-1,1,1,2-四氟丙烷和2-氯-3,3,3-三氟丙烯的原始有机原料以产生 包含2-氯-1,1,1,2-四氟丙烷,2-氯-3,3,3-三氟丙烯和氟化氢的类共沸组合物的第一蒸馏物流和富含氟化氢的第一塔底物流 ; (b)冷却所述第一馏出物流以产生包含富含2-氯-1,1,1,2-四氟丙烷和2-氯-3,3,3-三氟丙烯的有机层和富含酸层的中间组合物 在氟化氢中; 和(c)蒸馏所述有机层以产生包含2-氯-1,1,1,2-四氟丙烷,2-氯-3,3,3-四氯丙烷的类共沸组合物的第二馏出物流, 三氟丙烯和氟化氢,以及包含基本上不含氟化氢的纯化有机原料的第二塔底物流。

    Processes for geometric isomerization of halogenated olefins
    133.
    发明授权
    Processes for geometric isomerization of halogenated olefins 有权
    卤代烯烃几何异构化方法

    公开(公告)号:US07563936B2

    公开(公告)日:2009-07-21

    申请号:US11588466

    申请日:2006-10-27

    IPC分类号: C07C17/00

    CPC分类号: C07C17/358 C07C21/18

    摘要: Disclosed are processes for the conversion of isomerizable halogenated C2-C6 olefins from one geometric form to a more preferred geometric form. Preferred process aspects involve converting C2-C6 olefin in a cis-form to a trans-form under conditions effective to convert at least about 50 percent, and even more preferably at least about 70 percent, of the cis-form compound to the trans-form compound. In preferred embodiments the C2-C6 olefin comprises tetrafluoropropene, with cis-1,3,3,3 tetrafluoropropene (cis-HFO-1234ze) being converted, preferably at high conversion rates and high selectivity, to trans-1,3,3,3 tetrafluoropropene (trans-HFO-1234ze). In preferred embodiments the conditions effective to achieve the desired high levels of conversion and selectivity include exposing the feed to a metal based catalyst selected from the group consisting of halogentated metal oxides, Lewis acid metal halides, zero-valent metals, and combinations of these, preferably under reaction conditions, including reaction temperature and residence time, effective to convert at least about 5% of the cis-form of the compound to other compounds and to further achieve a selectivity to the trans-form of the compound of at least about 70%.

    摘要翻译: 公开了将可异构化的卤代C 2 -C 6烯烃从一种几何形式转化为更优选的几何形式的方法。 优选的方法方面涉及在有效将至少约50%,甚至更优选至少约70%的顺式形式化合物转化成反式 - 形式的条件下,将顺式C2-C6烯烃转化为反式 - 形成化合物。 在优选的实施方案中,C2-C6烯烃包括四氟丙烯,顺式-1,3,3,3四氟丙烯(顺式-HFO-1234ze)优选以高转化率和高选择性转化成反式1,3,3,3-四氟丙烯, 3四氟丙烯(反式HFO-1234ze)。 在优选的实施方案中,有效实现期望的高水平转化率和选择性的条件包括将进料暴露于金属基催化剂中,所述催化剂选自卤化金属氧化物,路易斯酸金属卤化物,零价金属及其组合, 优选在反应条件下,包括反应温度和停留时间,有效地将至少约5%的顺式化合物转化为其它化合物,并进一步实现化合物的反式形式至少约70的选择性 %。

    Process for manufacture of fluorinated olefins
    134.
    发明授权
    Process for manufacture of fluorinated olefins 有权
    氟化烯烃的制造方法

    公开(公告)号:US07560602B2

    公开(公告)日:2009-07-14

    申请号:US11588464

    申请日:2006-10-27

    IPC分类号: C07C17/00 C07C17/10

    摘要: A process for the production of fluorinated olefins, preferably fluorinated propenes, by contacting a feed stream containing a fluorinated olefin and hydrogen with a first amount of catalyst to produce the hydrofluorocarbon, wherein a first exit stream contains unreacted fluorinated olefin and hydrogen; contacting the first exit stream with a second amount of catalyst to produce a hydrofluorocarbon, wherein the second amount of catalyst is preferably greater than the first amount of catalyst; and contacting the hydrofluorocarbon with a catalyst for dehydrohalogenation to produce a product stream of fluorinated olefin.

    摘要翻译: 通过使包含氟化烯烃和氢气的进料流与第一量催化剂接触以产生氢氟烃来生产氟化烯烃,优选氟化丙烯的方法,其中第一出口流含有未反应的氟化烯烃和氢; 使第一出口流与第二量的催化剂接触以产生氢氟烃,其中第二量的催化剂优选大于第一量的催化剂; 并将氢氟烃与用于脱卤化氢的催化剂接触以产生氟化烯烃的产物流。

    MANUFACTURE OF 1,1,1,2,3,3-HEXAFLUORORPROPANE AND 1,1,1,2-TETRAFLUOROPROPANE VIA CATALYTIC HYDROGENATION
    135.
    发明申请
    MANUFACTURE OF 1,1,1,2,3,3-HEXAFLUORORPROPANE AND 1,1,1,2-TETRAFLUOROPROPANE VIA CATALYTIC HYDROGENATION 有权
    1,1,1,2,3,3-十六烷基丙烷和1,1,1,2-四氢呋喃的制备通过催化氢化

    公开(公告)号:US20090131727A1

    公开(公告)日:2009-05-21

    申请号:US12264735

    申请日:2008-11-04

    IPC分类号: C07C17/354

    摘要: A process for producing hydrofluorocarbon compounds represented by the following formula: CF3CHFCHm+1Fn wherein m is 0 or 2; n is 0 or 2; and m+n=2. The process has the step of contacting, i.e., reacting, hydrogen with a precursor compound represented by the following formula: CF3CF═CHmFn wherein m is 0 or 2; n is 0 or 2; and m+n=2. The contact is carried out in the presence of a solid catalyst and in the presence or absence of an inert gas. The catalyst is selected from the group consisting of: Fe, Co, Ni, Cu, Cr, Ru, Rh, Ag, Re, Os, Ir, Pt, Au, Sn, and any combinations thereof. For the hydrogenation of 1234yf to 254eb, Pd can also be used as catalyst in addition to the other above-referenced metals. These metals are preferably supported on a carrier such as activated carbon.

    摘要翻译: 由下式表示的氢氟烃化合物的制造方法:&lt;直线式公式说明=“In-line formula”end =“lead”?> CF3CHFCHm + 1Fn <?in-line-formula description =“In-line 式“end =”tail“?>其中m为0或2; n为0或2; m + n = 2。 该方法具有使氢与由下式表示的前体化合物接触,即使其反应的步骤:<?in-line-formula description =“In-line Formulas”end =“lead”?> CF 3 CF-CHmFn < in-line-formula description =“In-line formula”end =“tail”?>其中m为0或2; n为0或2; m + n = 2。 该接触在固体催化剂存在下和在惰性气体存在或不存在下进行。 催化剂选自:Fe,Co,Ni,Cu,Cr,Ru,Rh,Ag,Re,Os,Ir,Pt,Au,Sn及其任何组合。 对于1234yf至254eb的氢化,除了其它上述金属之外,Pd也可用作催化剂。 这些金属优选负载在载体如活性炭上。

    PROCESS FOR THE PRODUCTION OF HFO TRANS-1234ze FROM HFC-245fa
    136.
    发明申请
    PROCESS FOR THE PRODUCTION OF HFO TRANS-1234ze FROM HFC-245fa 有权
    从HFC-245fa生产HFO TRANS-1234ze的方法

    公开(公告)号:US20080051611A1

    公开(公告)日:2008-02-28

    申请号:US11775318

    申请日:2007-07-10

    IPC分类号: C07C19/00

    摘要: This invention relates a process for the manufacture of the HFO trans-1,3,3,3-tetrafluoropropene (HFO trans-1234ze). More particularly, the invention pertains to a process for the manufacture of the HFO trans-1234ze by first dehydrofluorinating 1,1,1,3,3-pentafluoropropane to thereby produce a mixture of cis-1,3,3,3-tetrafluoropropene, trans-1,3,3,3-tetrafluoropropene and hydrogen fluoride. Then optionally recovering hydrogen fluoride and then recovering trans-1,3,3,3-tetrafluoropropene.

    摘要翻译: 本发明涉及制备HFO反式-1,3,3,3-四氟丙烯(HFO trans-1234ze)的方法。 更具体地说,本发明涉及通过首先使1,1,1,3,3-五氟丙烷脱氟化氢来制造HFO反式 - 1234ze的方法,从而产生顺式-1,3,3,3-四氟丙烯, 反式-1,3,3,3-四氟丙烯和氟化氢。 然后任选地回收氟化氢,然后回收反式-1,3,3,3-四氟丙烯。

    Process for manufacture of fluorinated olefins
    137.
    发明申请
    Process for manufacture of fluorinated olefins 有权
    氟化烯烃的制造方法

    公开(公告)号:US20070179324A1

    公开(公告)日:2007-08-02

    申请号:US11588464

    申请日:2006-10-27

    IPC分类号: C07C21/18

    摘要: A process for the production of fluorinated olefins, preferably fluorinated propenes, by contacting a feed stream containing a fluorinated olefin and hydrogen with a first amount of catalyst to produce the hydrofluorocarbon, wherein a first exit stream contains unreacted fluorinated olefin and hydrogen; contacting the first exit stream with a second amount of catalyst to produce a hydrofluorocarbon, wherein the second amount of catalyst is preferably greater than the first amount of catalyst; and contacting the hydrofluorocarbon with a catalyst for dehydrohalogenation to produce a product stream of fluorinated olefin.

    摘要翻译: 通过使包含氟化烯烃和氢气的进料流与第一量催化剂接触以产生氢氟烃来生产氟化烯烃,优选氟化丙烯的方法,其中第一出口流含有未反应的氟化烯烃和氢; 使第一出口流与第二量的催化剂接触以产生氢氟烃,其中第二量的催化剂优选大于第一量的催化剂; 并将氢氟烃与用于脱卤化氢的催化剂接触以产生氟化烯烃的产物流。

    Continuous process for preparing halogenated compounds
    139.
    发明授权
    Continuous process for preparing halogenated compounds 有权
    连续制备卤化物的方法

    公开(公告)号:US07102041B2

    公开(公告)日:2006-09-05

    申请号:US11007036

    申请日:2004-12-08

    申请人: Hsueh Sung Tung

    发明人: Hsueh Sung Tung

    IPC分类号: C07C21/18 C07C17/26

    摘要: A process for preparing a haloalkane comprising: (a) contacting a haloalkane starting material with an alkene in the presence of an effective amount of a catalyst complex under conditions effective to facilitate an addition reaction and to form a product stream comprising a haloalkane product from the addition reaction, wherein the catalyst complex has a boiling point higher than that of the haloalkane product; and (b) recovering the haloalkane product from the product stream.

    摘要翻译: 一种制备卤代烷烃的方法,包括:(a)在有效促进加成反应的条件下,在有效量的催化剂配合物的存在下,使卤代烷烃原料与烯烃接触,并形成含有来自 加成反应,其中催化剂络合物的沸点高于卤代烷产物的沸点; 和(b)从产物流中回收卤代烷烃产物。