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    • 3. 发明授权
    • Process for the manufacture of 1,1,1,3,3-pentafluoropropene, 2-chloro-pentafluoropropene and compositions comprising saturated derivatives thereof
    • 用于制备1,1,1,3,3-五氟丙烯,2-氯 - 五氟丙烯的方法和包含其饱和衍生物的组合物
    • US06548720B2
    • 2003-04-15
    • US10061002
    • 2002-01-30
    • William H. ManogueV. N. Mallikarjuna RaoAllen Capron SievertSteven H. Swearingen
    • William H. ManogueV. N. Mallikarjuna RaoAllen Capron SievertSteven H. Swearingen
    • C07C1700
    • C07C19/08B01J23/868B01J27/12B01J27/132B01J37/0009B01J37/06C07C17/00C07C17/087C07C17/21C07C17/23C07C17/354C07C17/38C07C43/12Y02P20/582C07C21/18
    • A process is disclosed for producing the pentfluropropenes of the formula CF3CX═CF2, where X is H or Cl. The process involves hydrodehalogenating CF3CCl2CF3 with hydrogen at an elevated temperature in the vapor phase over a catalyst comprising an elemental metal, metal oxide, metal halide and/or metal oxyhalide (the metal being copper, nickel, chromium and the halogen of said halides and said oxyhalides being fluorine and/or chlorine. Processes for producing the hydrofluorocarbons CF3CH2CHF2, CF3CHFCF3 and CF3CH2CF3 are also disclosed which involve (a) hydrodehalogenating CF3CCl2CF3 with the hydrogen as indicated above to produce a product comprising CF3CCl═CF2, CF3CH═CF2, HCl and HF; and (b) either reacting the CF3CCl═CF2 and/or CF3CH═CF2 produced in (a) in the vapor phase with hydrogen to produce CF3CH2CHF2, reacting CF3CCl═CF2 produced in (a) with HF to produce CF3CHFCF3, or reacting the CF3CH═CF2produced in (a) with HF to produce CF3CH2CF3. Azeotrope compositions of CF3CHFCH3 with HF, and a process for recovering HF from a product mixture comprising HF and CF3CHFCF3 are also disclosed. Also disclosed are compositions and a process for producing compositions comprising (c1) CF3CHFCF3, CF3CH2CF3 or CHF2CH2CF3 and (c2) at least one saturated halogenated hydrocarbon and/or ether having the formula: CnH2n+2−a−bClaFbOc wherein n is an integer from 1 to 4, a is an integer from 0 to 2n+1, b is an integer from 1 to 2n+2−a, and c is 0 or 1, provided that when c is 1 then n is an integer from 2 to 4, and provided that component (c2) does not include the selected component (c1) compound, wherein the molar ratio of component (c2) to component (c1) is between about 1:99 and a molar ratio of HF to component (c1) in an azeotrope or azeotrope-like composition of component (c1) with HF. The process involves (A) combining (i) the azeotropic composition with (ii) the fluorination precursor to component (c2); and (B) reacting a sufficient amount of the HF from the azeotrope or azeotrope-like composition(i) with precursor component (ii) to provide a composition containing components (c1) and (c2) in the desired ratio. The compositions include at least two (c1) compounds, at least one of which is an ether.
    • 公开了制备式CF 3 C X = CF 2的五氟丙烯的方法,其中X是H或Cl。 该方法包括在气相中在升高的温度下在含有元素金属,金属氧化物,金属卤化物和/或金属卤氧化物(金属为铜,镍,铬和所述卤化物的卤素和所述卤化物的催化剂)的催化剂中用氢气脱氢CF 3 CCl 2 CF 3 还公开了用于制备氢氟烃CF 3 CH 2 CHF 2,CF 3 CHFCF 3和CF 3 CH 2 CF 3的方法,其涉及(a)如上所述用氢气将CF 3 CCl 2 CF 3加氢脱卤以产生包含CF 3 CCl = CF 2,CF 3 CH = CF 2,HCl和HF的产物 将(a)中产生的CF 3 CCl = CF 2和/或CF 3 CH = CF 2与氢气反应以产生CF 3 CH 2 CHF 2,使(a)中制备的CF 3 CCl = CF 2与HF反应产生CF 3 CHFCF 3,或使 CF3CH = CF2,在HF中产生CF 3 CH 2 CF 3,CF 3 CHFCH 3与HF的共沸组合物,以及从含有HF和CF 3 CHFCF 3的产物混合物中回收HF的方法也被公开 。 还公开了组合物和制备组合物的方法,其包含(c1)CF 3 CHFCF 3,CF 3 CH 2 CF 3或CHF 2 CH 2 CF 3和(c2)至少一种具有下式的饱和卤代烃和/或醚:CnH2n + 2-a-bClaFbOc其中n是 如图1〜图4所示,a为0〜2n + 1的整数,b为1〜2n + 2-a的整数,c为0或1,条件是当c为1时,n为2〜4的整数 ,并且条件是组分(c2)不包括选择
    • 6. 发明授权
    • Processes for the purification and use of 2-chloro-1,1,1,2,3,3,3-heptafluoropropane and zeotropes thereof with HF
    • US06677493B1
    • 2004-01-13
    • US09283449
    • 1999-04-01
    • Ralph Newton MillerV. N. Mallikarjuna RaoSteven H. Swearingen
    • Ralph Newton MillerV. N. Mallikarjuna RaoSteven H. Swearingen
    • C07C1908
    • C07C21/18C01B7/195C07C17/206C07C17/23C07C17/38C07C19/08C07C19/10Y02P20/582
    • A process is disclosed for the separation of a mixture of HF and CF3CClFCF3. The process involves placing the mixture in a separation zone at a temperature of from about −30° C. to about 100° C. and at a pressure sufficient to maintain the mixture in the liquid phase, whereby an organic-enriched phase comprising less than 50 mole percent HF is formed as the bottom layer and an HF-enriched phase comprising more than 90 mole percent HF is formed as the top layer. The organic-enriched phase can be withdrawn from the bottom of the separation zone and subjected to distillation in a distillation column to recover essentially pure CF3CClFCF3. The distillate comprising HF and CF3CClFCF3 can be removed from the top of the distillation column while essentially pure CF3CClFCF3 can be recovered from the bottom of the distillation column. The HF-enriched phase can be withdrawn from the top of the separation zone and subjected to distillation in a distillation column. The distillate comprising HF and CF3CClFCF3 can be removed from the top of the distillation column while essentially pure HF can be recovered from the bottom of the distillation column. If desired, the two distillates can be recycled to the separation zone. Also disclosed are compositions of hydrogen fluoride in combination with an effective amount of CF3CClFCF3 to form an azeotrope or azeotrope-like composition with hydrogen fluoride. Included are compositions containing from about 38.4 to 47.9 mole percent CF3CClFCF3. Also disclosed are processes for producing 1,1,1,2,3,3,3-heptafluoro-propane. One process uses a mixture comprising HF and CF3CClFCF3 and is characterized by preparing essentially pure CF3CClFCF3 as indicated above, and reacting the CF3CClFCF3 with hydrogen. Another process uses an azeotropic composition as described above, and reacts the CF3CClFCF3 with hydrogen in the presence of HF. Also disclosed is a process for producing hexafluoropropene. This process is characterized by preparing essentially pure CF3CClFCF3 as indicated above, and dehalogenating the CF3CClFCF3.