Process for perhalofluorinated butanes and hexanes
    32.
    发明授权
    Process for perhalofluorinated butanes and hexanes 失效
    全氟化丁烷和己烷的方法

    公开(公告)号:US06207869B1

    公开(公告)日:2001-03-27

    申请号:US09519791

    申请日:2000-03-07

    Abstract: The instant invention relates to producing perhalofluorobutanes and perhalofluorohexanes, more particularly it relates to their production by utilizing tetrafluoroethylene (hereinafter referred to as “TFE”) and chlorotrifluoro-ethylene (hereinafter referred to as “CTFE”) with selected perhalofluoroethanes containing 2 to 4 nonfluorine halogen and 2 to 4 fluorine substituents in the presence of a polyvalent metal halide such as an aluminum chloride or chlorofluoride as catalyst.

    Abstract translation: 本发明涉及生产全氟全氟代丁烷和全卤代己烷,更具体地说,涉及其使用四氟乙烯(以下称为“TFE”)和氯三氟乙烯(以下称为“CTFE”)的制备方法,该选择性全卤代乙烷含有2-4个非氟 卤素和2至4个氟取代基在多价金属卤化物如氯化铝或氯氟化物作为催化剂存在下进行。

    Mixed fluorination catalyst
    34.
    发明授权
    Mixed fluorination catalyst 有权
    混合氟化催化剂

    公开(公告)号:US06184172B2

    公开(公告)日:2001-02-06

    申请号:US09195455

    申请日:1998-11-18

    Abstract: Mixed fluorination catalyst comprising one or more nickel and chromium oxides, halides and/or oxyhalides deposited on a support composed of aluminium fluoride or of a mixture of aluminium fluoride and alumina, characterized in that the weight of nickel/weight of chromium ratio is between 0.08 and 0.25, preferably between 0.1 and 0.2.

    Abstract translation: 包含沉积在由氟化铝或氟化铝和氧化铝的混合物组成的载体上的一种或多种镍和铬氧化物,卤化物和/或氧卤化物的混合氟化催化剂,其特征在于镍/铬的重量比为0.08 和0.25,优选在0.1和0.2之间。

    Perhalofluorinated butanes and hexanes
    35.
    发明授权
    Perhalofluorinated butanes and hexanes 失效
    全氟化丁烷和己烷

    公开(公告)号:US6066768A

    公开(公告)日:2000-05-23

    申请号:US738117

    申请日:1996-10-25

    Abstract: The instant invention relates to producing perhalofluorobutanes and perhalofluorohexanes, more particularly it relates to their production by utilizing tetrafluoroethylene (hereinafter referred to as "TFE") and chlorotrifluoro-ethylene (hereinafter referred to as "CTFE") with selected perhalofluoroethanes containing 2 to 4 nonfluorine halogen and 2 to 4 fluorine substituents in the presence of a polyvalent metal halide such as an aluminum chloride or chlorofluoride as catalyst.

    Abstract translation: 本发明涉及生产全氟全氟代丁烷和全卤代己烷,更具体地说,涉及其使用四氟乙烯(以下称为“TFE”)和氯三氟乙烯(以下称为“CTFE”)的制备方法,该选择性全卤代乙烷含有2-4个非氟 卤素和2至4个氟取代基在多价金属卤化物如氯化铝或氯氟化物作为催化剂存在下进行。

    Process for preparing 1,1,1,2-tetrafluoroethane
    36.
    发明授权
    Process for preparing 1,1,1,2-tetrafluoroethane 失效
    制备1,1,1,2-四氟乙烷的方法

    公开(公告)号:US6037508A

    公开(公告)日:2000-03-14

    申请号:US209942

    申请日:1998-12-11

    CPC classification number: C07C17/206 B01J23/26 B01J27/125 C07C17/21

    Abstract: 1,1,1,2-tetrafluoroethane (134a) is prepared by reacting, in the gas phase, trichloroethylene with 1,1,1-trifluorochloroethane (133a) and hydrofluoric acid with trichloroethylene/133a molar ratios ranging from 5/95 to 50/50, in the presence of a catalyst consisting of Cr.sub.2 O.sub.3 carried on AlF.sub.3.The process provides 134a yields higher than 90% and permits an exceptionally long life of the catalyst. In this way it is possible to realize a continuous process by recycling the unreacted trichloroethylene and 133a, thereby making up for the relatively low global conversion of the reagents.

    Abstract translation: 1,1,1,2-四氟乙烷(134a)是通过在气相中使三氯乙烯与1,1,1-三氟氯乙烷(133a)和三氟乙烯/ 133a摩尔比为5/95至50的氢氟酸反应制备的 / 50,在由AlF3承载的Cr2O3组成的催化剂存在下。 该方法提供134a产率高于90%并且允许催化剂的使用寿命特别长。 以这种方式,可以通过再循环未反应的三氯乙烯和133a来实现连续的方法,从而弥补了试剂的相对低的全局转化率。

    Method for producing 3,3-dichloro-1,1,1-triflouroacetone
    38.
    发明授权
    Method for producing 3,3-dichloro-1,1,1-triflouroacetone 失效
    3,3-二氯-1,1,1-三氟丙酮的制备方法

    公开(公告)号:US5905174A

    公开(公告)日:1999-05-18

    申请号:US60180

    申请日:1998-04-15

    CPC classification number: C07C45/82 B01J27/08 B01J27/125 C07C45/63 C07C45/83

    Abstract: The invention relates to a method for producing 3,3-dichloro-1,1,1-trifluoroacetone. This method includes a step of fluorinating pentachloroacetone by hydrogen fluoride in the presence of a fluorination catalyst. This fluorination may be conducted in a liquid phase in the presence of an antimony compound as the fluorination catalyst. Alternatively, the fluorination may be conducted in a gas phase in the presence of a fluorination catalyst which may be a fluorinated alumina or at least one compound of at least one metal selected from Al, Cr, Mn, Ni, and Co. The method is suited to an industrial scale production of 3,3-dichloro-1,1,1-trifluoroacetone. The invention further relates to another method for producing 3,3-dichloro-1,1,1-trifluoroacetone. This method includes a step of purifying a crude 3,3-dichloro-1,1,1-trifluoroacetone by a distillation in the presence of water, thereby to produce 3,3-dichloro-1,1,1-trifluoroacetone which is substantially free of organic matters other than 3,3-dichloro-1,1,1-trifluoroacetone. This crude 3,3-dichloro-1,1,1-trifluoroacetone may be the reaction products of the fluorination of pentachloroacetone in a gas phase. Due to the provision of the another method, 3,3-dichloro-1,1,1-trifluoroacetone can be produced with high yield.

    Abstract translation: 本发明涉及一种生产3,3-二氯-1,1,1-三氟丙酮的方法。 该方法包括在氟化催化剂存在下用氟化氢氟化五氯丙酮的步骤。 该氟化可以在作为氟化催化剂的锑化合物的存在下在液相中进行。 或者,氟化可以在可以是氟化氧化铝或至少一种选自Al,Cr,Mn,Ni和Co的至少一种金属的化合物的氟化催化剂的存在下在气相中进行。该方法是 适合工业规模生产3,3-二氯-1,1,1-三氟丙酮。 本发明还涉及制备3,3-二氯-1,1,1-三氟丙酮的另一种方法。 该方法包括在水存在下通过蒸馏纯化粗制3,3-二氯-1,1,1-三氟丙酮的步骤,从而产生3,3-二氯-1,1,1-三氟丙酮,其基本上 不含3,3-二氯-1,1,1-三氟丙酮以外的有机物。 该粗的3,3-二氯-1,1,1-三氟丙酮可以是五氯丙酮在气相中氟化的反应产物。 由于提供另一种方法,可以高产率制备3,3-二氯-1,1,1-三氟丙酮。

    Alkylation process and catalyst therefor
    39.
    发明授权
    Alkylation process and catalyst therefor 失效
    烷基化方法及其催化剂

    公开(公告)号:US5254793A

    公开(公告)日:1993-10-19

    申请号:US9504

    申请日:1993-01-25

    Abstract: A composition of matter, which is an effective alkylation catalyst composition, is prepared by a method comprising heating, at a temperature of about 40.degree.-90.degree. C., (a) aluminum chloride, (b) boron phosphate, (c) alumina and/or silica, and (d) at least one chlorinated hydrocarbon (preferably CCl.sub.4), and subsequently separating the formed solid from the chlorinated hydrocarbon. The thus-prepared catalyst composition is employed in the alkylation of C.sub.2 -C.sub.7 alkane(s) with C.sub.2 -C.sub.7 alkene(s).

    Abstract translation: 通过以下方法制备作为有效的烷基化催化剂组合物的物质组成:在约40-90℃的温度下加热(a)氯化铝,(b)磷酸氢硼,(c)氧化铝 和/或二氧化硅,和(d)至少一种氯化烃(优选CCl 4),随后将形成的固体与氯化烃分离。 由此制备的催化剂组合物用于与C 2 -C 7烯烃的C 2 -C 7烷烃的烷基化。

    Hydrotreating catalyst
    40.
    发明授权
    Hydrotreating catalyst 失效
    加氢处理催化剂

    公开(公告)号:US4900711A

    公开(公告)日:1990-02-13

    申请号:US172267

    申请日:1988-03-23

    Abstract: A hydrotreating catalyst is described which comprises at least one Group VI metal, metal oxide, or metal sulfide, at least one Group VIII metal, metal oxide, or metal sulfide, and a halogen supported on a carrier wherein(A) the catalyst comprises from about 10% to about 35% by weight of combined metal and the atomic ratio of the Group VIII metal to Group VI metal is in the range of from about 0.5:1 to about 2:1;(B) the catalyst contains from about 0.5 to about 10% by weight of halogen;(C) the carrier comprises from about 10 to about 50% by weight of silica and from about 40 to about 90% of alumina; and(D) the catalyst is characterized as having a median pore radius of from about 20 to about 90 Angstroms, and a surface area of from about 90 to about 230 m.sup.2 /g.The catalyst is useful in the production of lubricating oils from crude lubricating oil stocks. Hydrotreating processes using the catalysts of the invention result in the production of oils having increased viscosity indexes, reduced aromatic content and improved stability. The nitrogen and sulfur content of the oils also are reduced through the use of the catalyst in the hydrogenation process.

    Abstract translation: 描述了一种加氢处理催化剂,其包含至少一种第Ⅵ族金属,金属氧化物或金属硫化物,至少一种第Ⅷ族金属,金属氧化物或金属硫化物,和负载在载体上的卤素,其中(A)催化剂包含 约10重量%至约35重量%的组合金属,并且第Ⅷ族金属与Ⅵ族金属的原子比在约0.5:1至约2:1的范围内; (B)催化剂含有约0.5至约10重量%的卤素; (C)载体包含约10至约50重量%的二氧化硅和约40至约90重量%的氧化铝; 和(D)催化剂的特征在于中值孔半径为约20至约90埃,表面积为约90至约230m 2 / g。 该催化剂可用于从原油润滑油原料生产润滑油。 使用本发明的催化剂的加氢处理方法导致具有增加的粘度指数,降低的芳香族含量和改进的稳定性的油的生产。 通过在氢化过程中使用催化剂,还可以减少油中的氮和硫含量。

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