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    • 1. 发明授权
    • Neutralization of reaction mixtures obtained by Beckman rearrangement of
cyclohexanone oxime
    • 通过Beckman重排环己酮肟获得的反应混合物中和
    • US4806638A
    • 1989-02-21
    • US109405
    • 1987-10-19
    • Uwe BrandRuediger SchmitzErnst DeukerHugo Fuchs
    • Uwe BrandRuediger SchmitzErnst DeukerHugo Fuchs
    • C07D201/04C07D201/16
    • C07D201/16
    • Reaction mixtures obtained by Beckmann rearrangement of cyclohexanone oxime with sulfuric acid or oleum are neutralized by a process which comprises the following steps:(a) mixing the reaction mixture with recycled ammonium sulfate mother liquor whose concentration is chosen so that no solid ammonium sulfate is precipitated during the neutralization,(b) neutralization by feeding gaseous ammonia which contains water or an aqueous ammonium sulfate solution in finely divided liquid form through a plurality of nozzle orifices into the solution of the reaction mixture in the ammonium sulfate mother liquor at elevated temperatures,(c) separation of crude lactam from the aqueous ammonium sulfate solution,(d) evaporation of the ammonium sulfate solution under reduced pressure and with separation of the crystalline ammonium sulfate from the ammonium sulfate mother liquor and(e) recycling of the ammonium sulfate mother liquor to stage a).
    • 通过包含以下步骤的方法中和通过Beckmann重排环己酮肟与硫酸或发烟硫酸得到的反应混合物:(a)将反应混合物与其浓度选择为不使固体硫酸铵沉淀的再循环硫酸铵母液混合 在中和期间,(b)通过将高分子液体形式的含有水或硫酸铵水溶液的气态氨通过多个喷嘴孔送入反应混合物在硫酸铵母液的溶液中,在升高的温度下中和(b) c)将粗内酰胺与硫酸铵水溶液分离,(d)在减压下蒸发硫酸铵溶液,并从硫酸铵母液中分离结晶硫酸铵,和(e)将硫酸铵母液 到a)。
    • 8. 发明授权
    • Preparation of .epsilon.-caprolactam by catalytic rearrangement of
cyclohexanone-oxime
    • 通过催化重排环己酮 - 肟制备ε-己内酰胺
    • US4248782A
    • 1981-02-03
    • US78031
    • 1979-09-24
    • Hugo FuchsUwe BrandPeter Horn
    • Hugo FuchsUwe BrandPeter Horn
    • C07D201/04
    • C07D201/04Y02P20/52
    • In a process for the preparation of .epsilon.-caprolactam by catalytic rearrangement of cyclohexanone-oxime in the gas phase at from 230.degree. to 450.degree. C. over a supported catalyst, containing boron trioxide, in a fluidized bed, wherein the catalyst is removed from the fluidized bed at the rate at which it becomes spent and is treated, in a fluidized state, with gases containing molecular oxygen at from 600.degree. to 900.degree. C., after which boron trioxide or boric acid is added to the fluidized catalyst, at from 300.degree. to 900.degree. C., before the catalyst is returned to the fluidized bed, the improvement that boron trioxide or boric acid of particle size from 0.05 to 1.5 mm is fed to the fluidized catalyst at one or more points.
    • 在通过在230℃至450℃的气相中催化重排环己酮 - 肟在含有三氧化硼的载体催化剂的流化床中制备ε-己内酰胺的方法,其中将催化剂从 流化床以其流失的速率以流化状态处理含有分子氧的气体在600-900℃,之后将三氧化硼或硼酸加入到流化催化剂中,在 在催化剂返回到流化床之前,从300℃升至900℃,改善将粒径为0.05-1.5mm的三氧化硼或硼酸以一个或多个点进料到流化催化剂中。
    • 9. 发明授权
    • Continuous extraction of caprolactam from crude lactam
    • 从内酰胺连续提取己内酰胺
    • US4154729A
    • 1979-05-15
    • US848210
    • 1977-11-03
    • Hugo FuchsUwe BrandKlaus Kartte
    • Hugo FuchsUwe BrandKlaus Kartte
    • C07D201/16
    • C07D201/16
    • In a process for the continuous extraction of caprolactam from crude lactam by means of benzene in counter-current, in which crude lactam is fed into the upper part of an extraction zone and benzene into the lower part, a solution of caprolactam in benzene is taken off at the top and an aqueous solution containing impurities is taken off at the bottom, the improvement that water is additionally fed into the upper part of the extraction zone and a part of the aqueous solution, containing impurities, obtained at the bottom of the extraction zone is recycled into the extraction zone. Caprolactam is used for the manufacture of nylon.
    • 在将粗制内酰胺进料到提取区上部并进入下部的苯中,通过逆流中的苯从粗制内酰胺连续提取己内酰胺的方法,将己内酰胺在苯中的溶液 在底部取出含有杂质的水溶液,改善了将水另外进料到提取区的上部,并将部分含有杂质的水溶液在提取物的底部获得 区域被回收到提取区域。 己内酰胺用于制造尼龙。