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    • 31. 发明授权
    • Preparation of amines and aminonitriles
    • 胺和氨基腈的制备
    • US5789621A
    • 1998-08-04
    • US693983
    • 1996-08-08
    • Werner SchnurrGuido VoitKlemens FlickRolf-Hartmuth Fischer
    • Werner SchnurrGuido VoitKlemens FlickRolf-Hartmuth Fischer
    • B01J23/78B01J23/94B01J27/187B01J27/28B01J38/10C07B43/04C07B61/00C07C20060101C07C209/48C07C209/52C07C211/12C07C211/35C07C253/30C07C255/24C07C209/02
    • C07C209/48C07C209/52
    • A process for preparing an NH.sub.2 -containing compound by hydrogenating a compound containing at least one unsaturated carbon-nitrogen bond with hydrogen in the presence of a catalyst at temperatures not below room temperature and elevated hydrogen partial pressure in the presence or absence of a solvent which process includes the following steps: a) using a catalyst comprising a cobalt- and/or iron-containing catalyst, and b) after the conversion based on the compound to be hydrogenated and/or the selectivity based on the desired product has or have dropped below a defined value or the amount of an unwanted by-product has risen beyond a defined value, interrupting the hydrogenation by stopping the feed of the compound to be hydrogenated and of the solvent, if used, c) treating the catalyst at from 150.degree. to 400.degree. C. with hydrogen using a hydrogen pressure within the range from 0.1 to 30 MPa and a treatment time within the range from 2 to 48 h, and d) subsequently continuing the hydrogenation of the compound containing at least one unsaturated carbon-nitrogen bond.
    • 在催化剂存在下,在不低于室温和升高的氢分压的情况下,在存在或不存在溶剂的情况下,通过氢化含有至少一个不饱和碳 - 氮键的化合物与氢气来制备含NH 2的化合物的方法, 方法包括以下步骤:a)使用包含含钴和/或含铁催化剂的催化剂,和b)基于待氢化的化合物转化后,和/或基于所需产物的选择性具有或已经下降 低于定义的值或不想要的副产物的量已经超过定义的值,如果使用,则通过停止待氢化化合物的进料和溶剂的中断氢化,c)在150℃下处理催化剂 在氢气压力为0.1〜30MPa,处理时间为2〜48h的范围内,使氢气变为400℃,d)随后继续进行水压 该化合物含有至少一个不饱和碳 - 氮键。
    • 32. 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%。