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    • 35. 发明授权
    • Processes for hydrofluorination of 2-chloro-3,3,3-trifluoropropene to 2-chloro-1,1,1,2-tetrafluoropropane
    • 将2-氯-3,3,3-三氟丙烯氢氟化为2-氯-1,1,1,2-四氟丙烷的方法
    • US08916733B2
    • 2014-12-23
    • US12484588
    • 2009-06-15
    • Daniel C. MerkelRobert C. JohnsonHsueh Sung Tung
    • Daniel C. MerkelRobert C. JohnsonHsueh Sung Tung
    • C07C19/08C07C17/00C07C17/08C07C17/087
    • C07C17/087C07C19/10
    • A process for making 2-chloro-1,1,1,2-tetrafluoropropane. The process has the step of contacting 2-chloro-3,3,3-trifluoropropene with hydrogen fluoride in the presence of a catalyst having about 25 to about 99.9 mole percent antimony pentachloride and about 0.1 to about 75 mole percent of a metal of a Lewis acid under conditions sufficient to form the 2-chloro-1,1,1,2-tetrafluoropropane. There is a second process for making 2-chloro-1,1,1,2-tetrafluoropropane. The process has the step of hydrofluorinating about 75 to about 99.9 mole percent 2-chloro-3,3,3-trifluoropropene and about 0.1 to about 25 mole percent of one or more other hydrocarbons having at least one chlorine atom in the presence of a catalyst of fluorinated antimony pentachloride under conditions sufficient to form the 2-chloro-1,1,1,2-tetrafluoropropane. There is yet another process for hydrofluorinating 2-chloro-3,3,3-trifluoropropene to 2-chloro-1,1,1,2-tetrafluoropropane. The process has the step of contacting the 2-chloro-3,3,3-trifluoropropene with hydrogen fluoride in the presence of a vapor phase catalyst under conditions sufficient to form the 2-chloro-1,1,1,2-tetrafluoropropane.
    • 制备2-氯-1,1,1,2-四氟丙烷的方法。 该方法具有在催化剂存在下使2-氯-3,3,3-三氟丙烯与氟化氢接触的步骤,该催化剂具有约25至约99.9摩尔%的五氯化锑和约0.1至约75摩尔%的金属 路易斯酸在足以形成2-氯-1,1,1,2-四氟丙烷的条件下进行。 制备2-氯-1,1,1,2-四氟丙烷的第二种方法。 该方法具有在存在下存在下,将约75-约99.9摩尔%的2-氯-3,3,3-三氟丙烯和约0.1-约25摩尔%的一种或多种其它具有至少一个氯原子的烃氢氟化的步骤 在足以形成2-氯-1,1,1,2-四氟丙烷的条件下的氟化五氯化锑催化剂。 还有将2-氯-3,3,3-三氟丙烯氢氟化为2-氯-1,1,1,2-四氟丙烷的另一种方法。 该方法具有在气相催化剂存在下,在足以形成2-氯-1,1,1,2-四氟丙烷的条件下使2-氯-3,3,3-三氟丙烯与氟化氢接触的步骤。
    • 36. 发明授权
    • Method for producing fluorinated organic compounds
    • 氟化有机化合物的制备方法
    • US08455704B2
    • 2013-06-04
    • US13287199
    • 2011-11-02
    • Robert C. JohnsonHsueh S. TungDaniel C. Merkel
    • Robert C. JohnsonHsueh S. TungDaniel C. Merkel
    • C07C17/00
    • C07C17/25C07C17/04C07C17/087C07C17/204C07C17/206C07C17/21C07C17/23C07C21/18C07C19/01C07C19/10C07C19/08C07C21/073
    • Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CF3CF═CH2 (1234yf). In certain preferred embodiments the processes comprise first exposing a compound of Formula (IA) C(X)2═CClC(X)3  (IA) where each X is independently F, Cl or H, preferably CCl2═CClCH2Cl, to one or more sets of reaction conditions, but preferably a substantially single set of reaction conditions, effective to produce at least one chlorofluoropropane, preferably in accordance with Formula (IB): CF3CClX′C(X′)3  Formula (IB) where each X′ is independently F, Cl or H, and then exposing the compound of Formula (IB) to one or more sets of reaction conditions, but preferably a substantially single set of reaction conditions, effective to produce a compound of Formula (II) CF3CF═CHZ  (II) where Z is H, F, Cl, I or Br.
    • 公开了用于制备氟化烯烃的方法,优选适于商业化CF 3 CF = CH 2(1234yf)。 在某些优选实施方案中,该方法包括首先将式(IA)C(X)2 = CClC(X)3(IA)的化合物暴露于其中每个X独立地为F,Cl或H,优选CCl 2 = CClCH 2 Cl, 反应条件组,但优选基本上单一组的反应条件,有效产生至少一种氯氟丙烷,优选按照式(IB):CF 3 CClX'C(X')3式(IB),其中每个X'独立地为F ,然后将式(IB)化合物暴露于一组或多组反应条件,但优选基本上单一组的反应条件,有效地制备式(II)化合物,CF 3 CF = CHZ(II) 其中Z是H,F,Cl,I或Br。
    • 37. 发明申请
    • PROCESSES FOR HYDROFLUORINATION OF 2-CHLORO-3,3,3-TRIFLUOROPROPENE TO 2-CHLORO-1,1,1,2-TETRAFLUOROPROPANE
    • 将2-氯代-3,3,3-三氟苯酚氢化成2-氯-1,1,1,2-四氢呋喃的方法
    • US20090312585A1
    • 2009-12-17
    • US12484588
    • 2009-06-15
    • Daniel C. MerkelRobert C. JohnsonHsueh Sung Tung
    • Daniel C. MerkelRobert C. JohnsonHsueh Sung Tung
    • C07C19/08
    • C07C17/087C07C19/10
    • A process for making 2-chloro-1,1,1,2-tetrafluoropropane. The process has the step of contacting 2-chloro-3,3,3-trifluoropropene with hydrogen fluoride in the presence of a catalyst having about 25 to about 99.9 mole percent antimony pentachloride and about 0.1 to about 75 mole percent of a metal of a Lewis acid under conditions sufficient to form the 2-chloro-1,1,1,2-tetrafluoropropane. There is a second process for making 2-chloro-1,1,1,2-tetrafluoropropane. The process has the step of hydrofluorinating about 75 to about 99.9 mole percent 2-chloro-3,3,3-trifluoropropene and about 0.1 to about 25 mole percent of one or more other hydrocarbons having at least one chlorine atom in the presence of a catalyst of fluorinated antimony pentachloride under conditions sufficient to form the 2-chloro-1,1,1,2-tetrafluoropropane. There is yet another process for hydrofluorinating 2-chloro-3,3,3-trifluoropropene to 2-chloro-1,1,1,2-tetrafluoropropane. The process has the step of contacting the 2-chloro-3,3,3-trifluoropropene with hydrogen fluoride in the presence of a vapor phase catalyst under conditions sufficient to form the 2-chloro-1,1,1,2-tetrafluoropropane.
    • 制备2-氯-1,1,1,2-四氟丙烷的方法。 该方法具有在催化剂存在下使2-氯-3,3,3-三氟丙烯与氟化氢接触的步骤,该催化剂具有约25至约99.9摩尔%的五氯化锑和约0.1至约75摩尔%的金属 路易斯酸在足以形成2-氯-1,1,1,2-四氟丙烷的条件下进行。 制备2-氯-1,1,1,2-四氟丙烷的第二种方法。 该方法具有在存在下存在下,将约75-约99.9摩尔%的2-氯-3,3,3-三氟丙烯和约0.1-约25摩尔%的一种或多种其它具有至少一个氯原子的烃氢氟化的步骤 在足以形成2-氯-1,1,1,2-四氟丙烷的条件下的氟化五氯化锑催化剂。 还有将2-氯-3,3,3-三氟丙烯氢氟化为2-氯-1,1,1,2-四氟丙烷的另一种方法。 该方法具有在气相催化剂存在下,在足以形成2-氯-1,1,1,2-四氟丙烷的条件下使2-氯-3,3,3-三氟丙烯与氟化氢接触的步骤。