Process for the preparation of phosphorus oxybromide
    3.
    发明授权
    Process for the preparation of phosphorus oxybromide 失效
    制备氧溴化磷的方法

    公开(公告)号:US3917803A

    公开(公告)日:1975-11-04

    申请号:US37153873

    申请日:1973-06-19

    Applicant: HOECHST AG

    CPC classification number: C01B25/00 C01B25/10

    Abstract: The invention relates to a process for the preparation of phosphorus oxybromide from phosphorus tribromide and oxygen in the presence of nitrogen oxides in an organic solvent. The phosphorus oxybromide is separated by crystallization or vacuum distillation.

    Abstract translation: 本发明涉及在有机溶剂中在氮氧化物存在下由三溴化磷和氧气制备三溴氧磷的方法。 通过结晶或真空蒸馏分离氧溴化磷。

    Process for the manufacture of nitrous oxide
    4.
    发明授权
    Process for the manufacture of nitrous oxide 失效
    硝酸氧化物的制造工艺

    公开(公告)号:US3656899A

    公开(公告)日:1972-04-18

    申请号:US3656899D

    申请日:1970-03-27

    Applicant: HOECHST AG

    CPC classification number: C01B21/22

    Abstract: To produce N2O, ammonium nitrate is decomposed in an aqueous, chloride-containing solution in nitric acid while an ammonia atmosphere is maintained above the reaction mixture. The preferred temperature range of the solution is 110*-125* C. The atmosphere of ammonia is maintained by introducing at least part of the required ammonia into the gas volume of the reaction vessel. The decomposition of the ammonium nitrate and the formation of N2O is enhanced by the presence of catalytically active ions of manganese, copper, cerium, lead, bismuth, cobalt and nickel; manganese, especially in its bivalent form, being preferred.

    Abstract translation: 为了产生N2O,硝酸铵在含硝酸的含氯化物溶液中分解,同时氨气氛保持在反应混合物上方。 溶液的优选温度范围为110°-125℃。通过将至少部分所需氨引入反应容器的气体体积来维持氨的气氛。 锰,铜,铈,铅,铋,钴和镍的催化活性离子的存在增强了硝酸铵的分解和N2O的形成; 优选锰,特别是其二价形式。

    Fluorinated tertiary amino ethers
    5.
    发明授权
    Fluorinated tertiary amino ethers 失效
    氟化泰坦尼治亚

    公开(公告)号:US3882178A

    公开(公告)日:1975-05-06

    申请号:US38686173

    申请日:1973-08-09

    Applicant: HOECHST AG

    CPC classification number: C25B3/08 C23C2/02

    Abstract: Tetrafluoro-ethylene can be added to monoamines having oxyethyl or oxypropyl groups in aprotic polar solvents in the presence of alkali metals. The new monoamines obtained having the radicals tetrafluoro-ethyloxy-ethyl or tetrafluoro-ethyl-oxy-propyl are electrolyzed in anhydrous hydrofluoric acid, thus forming new monoamines in which all or nearly all hydrogen atoms of the starting compounds are replaced by fluorine.

    Abstract translation: 在碱金属存在下,四氟乙烯可以加入非质子极性溶剂中具有氧乙基或氧丙基的单胺。 获得的具有四氟乙氧基 - 乙基或四氟 - 乙基 - 氧基 - 丙基基团的新单胺在无水氢氟酸中电解,从而形成新的单胺,其中起始化合物的全部或几乎全部氢原子被氟取代。

    Process for the manufacture of condensed aluminum phosphates
    6.
    发明授权
    Process for the manufacture of condensed aluminum phosphates 失效
    稠化磷酸铝的制造工艺

    公开(公告)号:US3650683A

    公开(公告)日:1972-03-21

    申请号:US3650683D

    申请日:1969-05-09

    Applicant: HOECHST AG

    CPC classification number: C01B25/38

    Abstract: The preparation of condensed aluminum phosphates containing phosphorus pentoxide and aluminum trioxide in a molar ratio within the range of from 1.1 : 1 to 3 : 1 is carried out by reacting water-soluble alkali metal polyphosphates with watersoluble aluminum salts and water and subjecting them to a heat treatment.

    Abstract translation: 通过使水溶性碱金属多磷酸盐与水溶性铝盐和水反应,将摩尔比在1.1:1至3:1范围内的五氧化二磷和三氧化二铝的缩合磷酸铝的制备进行, 进行热处理。

    PROCESS FOR THE RECOVERY OF ANTIMONY PENTACHLORIDE FROM CATALYST SOLUTIONS

    公开(公告)号:CA958520A

    公开(公告)日:1974-12-03

    申请号:CA127864

    申请日:1971-11-17

    Applicant: HOECHST AG

    Abstract: 1377084 Antimony pentachloride FARBWERKE HOECHST AG 17 Nov 1971 [6 March 1971] 53472/71 Heading C1A Antimony is recovered as the pentachloride from solutions containing antimony as chloride and/or fluoride, hydrocarbons substituted with chlorine or both chlorine and fluorine and inorganic impurities, by converting any antimony fluorides in the solution to antimony chlorides, distilling off halogenated hydrocarbons to concentrate the solution, establishing the solution at a temperature of at least 60‹ C. to decompose any SbCl 5 in the solution into SbCl 3 and chlorine, separating residual halogenated hydrocarbons and any other organic impurities by extracting with an organic solvent, oxidizing with chlorine the antimony trichloride so obtained to antimony pentachloride and separating the latter from the inorganic impurities. The initial solution may be a spent catalyst solution, obtained in the fluorination of halogenated hydrocarbons using SbCl 5 as catalyst, and generally containing chlorinated or fluorochlorinated hydrocarbons, inorganic and organic impurities, e.g. FeCl 3 and hexachloroethane and antimony chlorides and fluorides (SbF 3 and SbF 5 ). The latter are converted into antimony chlorides by heating the solution suitably at 40‹-130‹ C., the antimony fluorides reacting with chlorinated hydrocarcarbons present and if desired additionally added chlorinated hydrocarbon, e.g. CCl 4 . Halogenated hydrocarbons are distilled off simultaneously or subsequently and the concentrated solution is heated at e.g. 80‹-300‹ C. to decompose SbCl 5 present, the liberated chlorine being used in the rechiorination step. Organic impurities, e.g. fluorinated and chlorinated hydrocarbons, e.g. C 2 Cl 6 are then solvent extracted preferably by contacting with a halogenated hydrocarbon, suitably that obtained in the preceding distillation, at an elevated temperature of up to 100‹ C. and then cooling to not less than 10‹ C. Rechlorination of the SbCl 3 is preferably effected 60‹-150‹ C. at 0-4 atmospheres gauge and the resulting pentachloride separated from inorganic impurities, e.g. FeCl 3 by distillation under reduced pressure.

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