Process for the preparation of fluorinated alkanes from alkenes
    32.
    发明授权
    Process for the preparation of fluorinated alkanes from alkenes 失效
    从烯烃制备氟化烷烃的方法

    公开(公告)号:US4937398A

    公开(公告)日:1990-06-26

    申请号:US290129

    申请日:1988-12-27

    IPC分类号: C07C17/02 C07C17/04 C07C19/08

    CPC分类号: C07C17/02 C07C17/04

    摘要: The present invention provides a process for the preparation of luorinated alkanes. The process comprises the step of: reacting an alkene with carbon having fluorine absorbed therein at a temperature and for a time sufficient to form fluorinated alkanes. The alkene used is not perhalogenated at the double-bonded carbons. Preferably, the alkene used is vinylidene fluoride or ethylene.The process produces products such as 1,1,1,2-tetrafluoroethane (known in the art as 134a) which may be used as a refrigerant and 1,1,1-trifluoroethane (known in the art as R143a) and 1,2-difluoroethane (known in the art as R152) which may be used as blowing agents or solvents.

    摘要翻译: 本发明提供了一种制备罗氏化烷烃的方法。 该方法包括以下步骤:在足以形成氟化烷烃的温度和时间下使烯烃与其中吸收有氟的碳反应。 所用的烯烃在双键碳上不是全卤代的。 优选使用的烯烃是偏二氟乙烯或乙烯。 该方法产生可用作制冷剂的1,1,1,2-四氟乙烷(本领域已知的134a)和1,1,1-三氟乙烷(本领域已知的R143a)和1,2 二氟乙烷(本领域已知为R152),其可用作发泡剂或溶剂。

    High energy density battery with cathode composition
    33.
    发明授权
    High energy density battery with cathode composition 失效
    具有阴极组成的高能量密度电池

    公开(公告)号:US4548881A

    公开(公告)日:1985-10-22

    申请号:US699765

    申请日:1985-02-08

    CPC分类号: H01M4/5835 H01M6/16

    摘要: A cell which employs an active metal anode such as lithium and a liquid organic electrolyte that is improved by the use of a cathode comprised of carbon fluoride chloride is described.The cathode comprises a carbon fluoride chloride of the general formula (C.sub.y F.sub.x Cl.sub.z).sub.n wherein y is 1 to 2, x is greater than 0 to 1.2, z is .ltoreq.0.1 and n defines the number of repeating units occurring in the carbon fluoride chloride molecule of high molecular weight. The resulting battery has improved discharge and shelf-life characteristics.

    摘要翻译: 描述了使用通过使用由氟化碳氟化物构成的阴极改善的活性金属阳极例如锂和液体有机电解质的电池。 阴极包含通式为(CyFxClz)n的氟化碳氟化物,其中y为1至2,x大于0至1.2,z为<= 0.1,n为在氟化碳氯化物中存在的重复单元数 高分子量分子。 所得的电池具有改善的放电和保质期特性。

    Production of fluorocarbons employing two catalyst zones
    34.
    发明授权
    Production of fluorocarbons employing two catalyst zones 失效
    生产采用两个催化剂区的碳氟化合物

    公开(公告)号:US4088704A

    公开(公告)日:1978-05-09

    申请号:US761161

    申请日:1977-01-21

    IPC分类号: C07C17/00 C07C17/15 C07C17/10

    摘要: Highly chlorinated hydrocarbons having one to three carbons such as CCl.sub.4, C.sub.2 Cl.sub.6 and C.sub.3 Cl.sub.8 are reacted with HF in the presence of a fluorination catalyst such as gamma aluminum fluoride. The effluent is reacted with unhalogenated or underhalogenated hydrocarbons having 1 to 3 carbons, such as CH.sub.4, CH.sub.3 Cl, C.sub.2 H.sub.5 Cl, C.sub.2 H.sub.6, CH.sub.2 .dbd.CHCl and CFCl.dbd.CCl.sub.2, and O.sub.2 in the presence of an oxychlorination catalyst, such as cupric chloride with alkali halide or alkaline earth halide promoters on alpha aluminum fluoride. Fluorocarbons having 1 to 3 carbons such as CCl.sub.2 F.sub.2, C.sub.2 Cl.sub.3 F.sub.3 and C.sub.2 Cl.sub.2 F.sub.4 are separated from the effluent. Preferably, highly chlorinated materials are recycled onto the fluorination catalyst and underhalogenated materials are recycled onto the oxychlorination catalyst.

    摘要翻译: 在氟化催化剂如γ-氟化铝的存在下,将具有一至三个碳的高氯代烃如CCl4,C2Cl6和C3Cl8与HF反应。 将流出物与具有1至3个碳原子的未卤化或卤代烃反应,例如CH 4,CH 3 Cl,C 2 H 5 Cl,C 2 H 6,CH 2 = CHCl和CFCl = CCl 2,和O 2在氧氯化催化剂如氯化铜与碱 卤化物或碱土卤化物助剂在α氟化铝上。 具有1至3个碳的碳氟化合物如CCl 2 F 2,C 2 Cl 3 F 3和C 2 Cl 2 F 4与流出物分离。 优选地,将高度氯化的材料再循环到氟化催化剂上,并将卤代化物质再循环到氧氯化催化剂上。

    Separation and recovery of molybdenum values from uranium process waste
    40.
    发明授权
    Separation and recovery of molybdenum values from uranium process waste 失效
    从铀工艺废物中分离和回收钼值

    公开(公告)号:US4584184A

    公开(公告)日:1986-04-22

    申请号:US612282

    申请日:1984-05-21

    摘要: A method for treating process waste consisting of uranium hexafluoride, UF.sub.6, molybdenum hexafluoride, MoF.sub.6 and molybdenum oxytetrafluoride, MoOF.sub.4 is provided wherein the foregoing mixture is hydrolyzed in an aqueous solution of ammonium carbonate and ammonium hydroxide. The resulting mother liquor is digested at 60.degree.-80.degree. C. to drive off carbon dioxide and convert the ammonium uranyl carbonate, (NH.sub.4).sub.4 UO.sub.2 (CO.sub.3).sub.3 to ammonium diuranate, (NH.sub.4).sub.2 U.sub.2 O.sub.7. The pH is maintained above 9 to prevent premature precipitation of the molybdenum values as molybdic acid or uranyl molybdate.The ammonium diuranate which forms as a yellow solid is filtered, slurried in aqueous ammonium hydroxide, filtered and dried. The yield is quantitative. Pyrolysis results in conversion of the diuranate salt to uranium oxide, U.sub.3 O.sub.8, of suitable purity to be recycled in the uranium hexafluoride production process. The combined filtrates which contain the molybdenum values and ammonium fluoride by-product are diluted, and stirred, with 95% ethanol to precipitate white, crystalline, ammonium molybdate, (NH.sub.4).sub.2 MoO.sub.4. The ammonium fluoride remains soluble. The ammonium molybdate is filtered, dried and calcined at 600.degree. C. for 2 hours to yield molybdenum trioxide, MoO.sub.3 in >90% yield and essentially free of uranium contamination. Fluoride contamination in either of the reprocessed materials is minimal.

    摘要翻译: 一种用于处理由六氟化铀,UF 6,六氟化钼,MoF 6和四氟化钼组成的处理废物的方法,其中上述混合物在碳酸铵和氢氧化铵的水溶液中水解。 将得到的母液在60°-80℃下消化以除去二氧化碳,并将碳酸铀酸铵(NH4)4UO2(CO3)3转化成二氢铀酸铵(NH4)2U2O7。 pH值保持在9以上,以防止钼值过早沉淀为钼酸或钼酸铀。 过滤形成黄色固体的二异氰酸铵,在氢氧化铵水溶液中浆化,过滤并干燥。 产量是定量的。 热解导致将二铀酸盐转化为具有合适纯度的氧化铀U3O8,以在六氟化铀生产过程中再循环。 将含有钼值和氟化铵副产物的合并滤液稀释,并用95%乙醇搅拌,沉淀出白色,结晶,钼酸铵(NH 4)2 OO 4。 氟化铵保持溶解。 将钼酸铵过滤,干燥并在600℃下煅烧2小时,得到三氧化钼,MoO 3> 90%产率,基本上不含铀污染物。 任何一种后处理材料中的氟化物污染最小。