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    • 1. 发明申请
    • Process for the preparation of 1,1,1,3,3-pentafluoropropane and 1,1,1,3,3,3-hexafluoropropane
    • 制备1,1,1,3,3-五氟丙烷和1,1,1,3,3,3-六氟丙烷的方法
    • US20070123742A1
    • 2007-05-31
    • US10572627
    • 2004-10-13
    • Velliyur Nott RaoAllen Sievert
    • Velliyur Nott RaoAllen Sievert
    • C07C19/08
    • C07C17/23B01J23/002B01J23/26B01J27/12B01J37/26B01J2523/00C07C17/206C07C17/21C07C19/08C07C21/18C07C19/10B01J2523/27B01J2523/67
    • A process for the manufacture of CF3CH2CHF2 and CF3CH2CF3 is disclosed. The process involves (a) reacting HF and at least one halopropene of the formula CX3CCl═CClX (where each X is independently F or Cl) to produce a product including both CF3CCl═CF2 and CF3CHClCF3; (b) reacting CF3CCl═CF2 and CF3CHClCF3 produced in (a) with hydrogen to produce a product including both CF3CH2CHF2 and CF3CH2CF3; and (c) recovering CF3CH2CHF2 and CF3CH2CF3 from the product produced in (b). In (a), the CF3CCl═CF2 and CF3CHClCF3 are produced in the presence of a fluorination catalyst including a ZnCr2O4/crysta α-chromium oxide composition, a ZnCr2O4/crystalline α-chromium oxide composition which has been treated with a flourinating a agent, a zinc halide/α-chromium oxide composition and/or a zinc halideα-chromium oxide composition which has been treated with a fluorinating agent.
    • 用于制备CF 3 CH 2 CHF 2 CH 2和CF 3 CH 2的方法, SUB> CF 3 3 。 该方法包括(a)使HF和式CX 3 CCl-CClX(其中每个X独立地为F或Cl)的至少一种卤代丙烯反应,以产生包含CF 3 CCl-CF 2和CF 3 CHClCF 3; (b)使(a)中制备的CF 3 N 3 CCl-CF 2 H 2和CF 3 COClCF 3 N与氢 以产生包含CF 3 CH 2 CHF 2 CH 2和CF 3 CH 2 CH 2的化合物, CF 3 3; 和(c)回收CF 3 3 CH 2 CHF 2和CF 3 CH 2 2 / / SUB >(CF 3)3 。 在(a)中,CF 3 3 CCl-CF 2 CO 3和CF 3 CHClCF 3 3在存在下产生 的包含ZnCr 2 O 4 / SiO 2 /α-氧化铬组合物的氟化催化剂,ZnCr 2 O 4 O 3 已经用氟化剂处理过的已经用增稠剂,卤化锌/α-氧化铬组合物和/或卤化锌 - 铬 - 氧化铬组合物处理的结晶α-氧化铬组合物。
    • 8. 发明申请
    • Processes for the preparation of 2-chloro-1,1,1,2,3,3,3-heptafluoropropane, hexafluoropropene and 1,1,1,2,3,3,3-heptafluoropropane
    • 制备2-氯-1,1,1,2,3,3,3-七氟丙烷,六氟丙烯和1,1,1,2,3,3,3-七氟丙烷的方法
    • US20050222471A1
    • 2005-10-06
    • US10523223
    • 2003-08-21
    • Mario NappaVelliyur Nott RaoH. RosenfeldShekhar SubramoneyMunirpallam SubramanianAllen sievert
    • Mario NappaVelliyur Nott RaoH. RosenfeldShekhar SubramoneyMunirpallam SubramanianAllen sievert
    • B01J27/132B01J23/26B01J23/86B01J35/00B01J37/02B01J37/03B01J37/26C07B61/00C07C17/04C07C17/08C07C17/087C07C17/20C07C17/21C07C17/23C07C17/25C07C19/08C07C19/10C07C21/18
    • C07C19/08B01J23/26B01J23/866B01J35/002B01J37/0236B01J37/03B01J37/26C07C17/206C07C17/21C07C17/23C07C17/25C07C19/10C07C21/18
    • A process for the preparation of 2-chloro-1,1,1,3,3,3-heptafluoropropane is disclosed which involves (a) contacting a mixture comprising hydrogen fluoride, chlorine, and at least one starting material selected from the group consisting of halopropenes of the formula CX3CCl═CX2 and halopropanes of the formula the CX3CClYCX3, wherein each X is independently F or Cl, and Y is H, Cl or F (provided that the number of X and Y which are F totals no more than six) with a chlorofluorination catalyst in a reaction zone to produce a product mixture comprising CF3CClFCF3, HCl, HF, and underfluorinated halogenated hydrocarbon intermediates. The process is characterized by said chlorofluorination catalyst comprising at least one chromium-containing component selected from (i) a crystalline alpha-chromium oxide where at least 0.05 atom % of the chromium atoms in the alpha-chromium oxide lattice are replaced by nickel, trivalent cobalt or both nickel and trivalent cobalt, provided that no more than 2 atom % of the chromium atoms in the alpha-chromium oxide lattice are replaced by nickel and that the total amount of chromium atoms in the alpha-chromium oxide lattice that are replaced by nickel and trivalent cobalt is no more than 6 atom %, and (ii) a fluorinated crystalline oxide of (i). Also disclosed is a process for the manufacture of a mixture of HFC-227ea and hexafluoropropene by reacting a starting mixture comprising CFC-217ba and hydrogen in the vapor phase at an elevated temperature, optionally in the presence of a hydrogenation catalyst. This process involves preparing the CFC-217ba by the process described above.
    • 公开了一种制备2-氯-1,1,1,3,3,3-七氟丙烷的方法,其涉及(a)使包含氟化氢,氯和至少一种起始原料的混合物接触,所述起始材料选自 式CX 3 CCl-CX 2的卤代丙烯和下式的卤代丙烷CX 3 CClYCX 3 N, 其中每个X独立地为F或Cl,并且Y为H,Cl或F(条件是X和Y的总数不超过6的F数)与反应区中的氯氟化催化剂反应生成包含CF的产物混合物 3 CClFCF 3,HCl,HF和过氟化卤代烃中间体。 该方法的特征在于所述氯氟化催化剂包含至少一种含铬组分,其选自(i)α-氧化铬晶格中至少0.05原子%的铬原子被镍取代的结晶α-氧化铬,三价 钴或镍和三价钴,条件是α-铬氧化物晶格中不超过2原子%的铬原子被镍代替,并且α-氧化铬晶格中的铬原子的总量被 镍和三价钴不超过6原子%,和(ii)(i)的氟化结晶氧化物。 还公开了通过在升高的温度下,任选地在氢化催化剂存在下,使包含CFC-217ba和氢的起始混合物在气相中反应制备HFC-227ea和六氟丙烯的混合物的方法。 该方法包括通过上述方法制备CFC-217ba。