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    • 1. 发明授权
    • Process for obtaining coarsely crystalline pure ammonium sulfate
    • 获得粗结晶纯硫酸铵的方法
    • US4138472A
    • 1979-02-06
    • US844647
    • 1977-10-25
    • Gerald NeubauerGerard Van WauweJosef BeullensUwe BrandHugo FuchsKlaus Kartte
    • Gerald NeubauerGerard Van WauweJosef BeullensUwe BrandHugo FuchsKlaus Kartte
    • C01C1/242C01C1/248
    • C01C1/242C01C1/248
    • A process for obtaining coarsely crystalline pure ammonium sulfate from reaction mixtures which have been obtained by Beckmann rearrangement of cyclohexanone-oxime with sulfuric acid or oleum, by neutralizing the mixtures with ammonia at an elevated temperature, with the addition of recycled ammonium sulfate mother liquor, the concentration being so chosen that during the neutralization no solid ammonium sulfate precipitates, separating the crude caprolactam from the ammonium sulfate solution, crystallizing ammonium sulfate by evaporating the ammonium sulfate solution under reduced pressure, separating off the crystallized ammonium sulfate and recycling the mother liquor to the neutralization stage. The neutralization is carried out at from 80.degree. to 115.degree. C. under autogenous pressure and the ammonium sulfate solution obtained after separating off the crude lactam is evaporated under a pressure of from 200 to 600 mm Hg while cooling to from 72.degree. to 101.degree. C.
    • 从反应混合物中获得粗结晶纯硫酸铵的方法,其通过用硫酸或发烟硫酸重整环己酮 - 肟,通过在升高的温度下用氨中和混合物,再加入回收的硫酸铵母液, 浓度如此选择,使得在中和期间没有固体硫酸铵沉淀,将粗己内酰胺与硫酸铵溶液分离,通过在减压下蒸发硫酸铵溶液使硫酸铵结晶,分离结晶的硫酸铵并将母液再循环至 中和阶段。 中和在自生压力下在80〜115℃进行,分离出内酰胺后得到的硫酸铵溶液在200〜600mmHg的压力下蒸发,同时冷却至72〜101℃。 C。
    • 3. 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。
    • 6. 发明授权
    • Partial dehydration of cyclohexanone oxime
    • 环己酮肟部分脱水
    • US3941838A
    • 1976-03-02
    • US438167
    • 1974-01-30
    • Hugo FuchsRudolph GathKurt KahrKlaus Kartte
    • Hugo FuchsRudolph GathKurt KahrKlaus Kartte
    • B01D20060101C07C20060101C07C131/04
    • C07C249/14
    • A process for the partial dehydration of cyclohexanone oxime by treatment with aqueous solutions of inorganic salts, wherein the crude cyclohexanone oxime is extracted, above its melting point, with a concentrated ammonium salt solution and/or hydroxylammonium salt solution in countercurrent in an extraction column and the salt solution is then separated from the partly dehydrated cyclohexanone oxime, reconcentrated by evaporation and recycled to the oxime dehydration process. The cyclohexanone oxime melt which has been dehydrated to water contents of about 4 to 6% by weight is treated with a heated inert gas above its melting point and the off-gas is washed to remove entrained cyclohexanone oxime.
    • 一种通过用无机盐的水溶液处理来环己酮肟部分脱水的方法,其中将粗环己酮肟在其熔点以上提取,浓缩的铵盐溶液和/或羟基铵盐溶液在提取塔中逆流, 然后将盐溶液与部分脱水的环己酮肟分离,通过蒸发浓缩并再循环至肟脱水过程。 已经脱水至约4〜6重量%的含水量的环己酮肟熔体用高于其熔点的加热惰性气体处理,并将废气洗涤以除去夹带的环己酮肟。