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    • 72. 发明授权
    • Preparation of 3-aminomethyl-3,5,5-trimethylcyclohexylamine
    • 3-氨基甲基-3,5,5-三甲基环己胺的制备
    • US5756845A
    • 1998-05-26
    • US608485
    • 1996-02-28
    • Guido VoitTom WitzelBoris BreitscheidelWolfgang HarderHermann LuykenAxel PaulKarl-Heinz RossPeter Wahl
    • Guido VoitTom WitzelBoris BreitscheidelWolfgang HarderHermann LuykenAxel PaulKarl-Heinz RossPeter Wahl
    • B01J23/46B01J23/75B01J23/755C07B61/00C07C209/48C07C211/36
    • C07C209/48C07C2101/14
    • A process for the preparation of 3-aminomethyl-3,5,5-trimethylcyclohexylamine from 3-cyano-3,5,5-trimethylcyclohexanone which requires three spatially separated reaction spaces, in order to carry out the following three steps in sequence: a) reacting the 3-cyano-3,5,5-trimethylcyclohexanone with excess ammonia on acidic metal-oxide catalysts in a first reaction space at from 20.degree. to 150.degree. C. and from 50 to 300 bar, b) hydrogenating the resultant reaction products using hydrogen in a second reaction space in the presence of excess ammonia and preferably liquid ammonia on hydrogenation catalysts, optionally using basic components or on neutral or basic supports at from 50.degree. to 100.degree. C. and at from 50 to 300 bar, and c) hydrogenating the resultant reaction products in the presence of hydrogen and also ammonia in a third reaction space on hydrogenation catalysts, optionally using basic components or on neutral or basic supports at from 110.degree. to 160.degree. C. and at from 150 to 300 bar.These three steps in sequence provide a substantially complete reaction of the original 3-cyano-3,3,5-trimethylcyclohexanone reactant with a yield of 96% of the desired diamino product in which the cis-content of the diamine is 70%.
    • 从3-氰基-3,5,5-三甲基环己酮制备3-氨基甲基-3,5,5-三甲基环己胺的方法,其需要三个空间分离的反应空间,以便按顺序进行以下三个步骤:a )在20至150℃和50至300巴的第一反应空间中使3-氰基-3,5,5-三甲基环己酮与过量的氨在酸性金属氧化物催化剂上反应,b)将所得反应物氢化 在氢化催化剂存在下,在过量氨和优选液氨存在下在第二反应空间中使用氢的产物,任选使用碱性组分或在中性或碱性载体上在50至100℃和50至300巴条件下,以及 c)在氢化催化剂的第三反应空间中,在氢气和氨的存在下氢化所得反应产物,任选使用碱性组分或在中性或碱性载体上在110至160℃和150至300b ar。 这三个步骤依次提供原始3-氰基-3,3,5-三甲基环己酮反应物的基本上完全的反应物,其中二胺的顺式含量为70%的所需二氨基产物的产率为96%。
    • 75. 发明授权
    • Method for producing dinitriles
    • 生产二腈的方法
    • US07816551B2
    • 2010-10-19
    • US10586500
    • 2005-01-27
    • Tim JungkampRobert BaumannMichael BartschGerd HaderleinHermann LuykenJens Scheidel
    • Tim JungkampRobert BaumannMichael BartschGerd HaderleinHermann LuykenJens Scheidel
    • C07C253/10
    • C07C253/10C07C255/04
    • An adiponitrile/methylglutaronitrile preparation process includes distilling a reaction stream to obtain stream 3 depleted in pentenenitriles (bottom product) and stream 4 enriched in pentenenitriles (top product); extracting stream 3 obtaining stream 6 enriched with extractant (top product) and stream 7 depleted in extractant (bottom product); distilling stream 6 obtaining stream 8 comprising the catalyst (bottom product) and stream 9 comprising the extractant (top product); distilling stream 7 obtaining stream 10 (bottom product) and stream 11 comprising the extractant (top product); distilling stream 10 obtaining stream 12 comprising catalyst degradation products, at least one promotor, adiponitrile and methylglutaronitrile (bottom product) and stream 13 comprising pentenenitriles (top product); distilling stream 12 obtaining stream 14 comprising catalyst degradation products and the promotor(s) (bottom product) and stream 15 comprising adiponitrile and methylglutaronitrile (top product); distilling stream 15 obtaining stream 16 comprising adiponitrile (bottom product) and stream 17 comprising methylglutaronitrile (top product).
    • 己二腈/甲基戊二腈的制备方法包括蒸馏反应物流以获得贫饱和腈(最终产物)的流3和富含戊烯腈的流4(顶部产物); 提取物流3获得富集萃取剂(顶部产物)的流6和耗尽萃取剂(底部产物)的料流7; 蒸馏流6获得包含催化剂(底部产物)的流8和包含萃取剂的流9(顶部产物); 蒸馏流7获得流10(底部产物)和包含萃取剂(顶部产物)的料流11; 蒸馏流10获得包含催化剂降解产物的流12,至少一种促进剂,己二腈和甲基戊二腈(底部产物)和包含戊烯腈(顶部产物)的料流13; 蒸馏流12获得包含催化剂降解产物和促进剂(底部产物)的流14和包含己二腈和甲基戊二腈(顶部产物)的料流15; 蒸馏流15获得包含己二腈(底部产物)的流16和包含甲基戊二腈(顶部产物)的料流17。