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    • 21. 发明授权
    • Toluene diamine from non-washed dinitrotoluene
    • 来自未洗涤二硝基甲苯的甲苯二胺
    • US4224249A
    • 1980-09-23
    • US38976
    • 1979-05-14
    • Nance D. KunzThomas A. JohnsonBarton Milligan
    • Nance D. KunzThomas A. JohnsonBarton Milligan
    • C07B61/00B01J29/00C07C67/00C07C209/00C07C209/36C07C211/51C07C85/11C07C85/26
    • C07C209/36
    • This invention relates to an improvement in a process for preparing toluene diamine. The improvement resides in a process which is capable of permitting reduction of dinitrotoluene to toluene diamine without prior alkaline treatment for removal of nitrocresols in the dinitrotoluene. In carrying out the improvement the feed dinitrotoluene is water washed to remove HNO.sub.3 to a level below 6000 ppm, and the catalytic conversion of dinitrotoluene to toluene diamine is done continuously. Dinitrotoluene is charged to a reaction vessel containing a liquid carrier and reduced with hydrogen at constant pressure, the dinitrotoluene being added at a rate to maintain a concentration of dinitrotoluene of 0.0001 to 25% by weight of the total reactor contents while the hydrogenation catalyst is maintained at a level from about 0.1 to 3% based on the weight of reactor contents.
    • 本发明涉及一种制备甲苯二胺的方法的改进。 改进之处在于能够允许将二硝基甲苯还原成甲苯二胺而不经过碱性处理除去二硝基甲苯中的硝基甲酚。 在进行改进时,将进料二硝基甲苯进行水洗以除去HNO 3至低于6000ppm的水平,并连续进行二硝基甲苯向甲苯二胺的催化转化。 将二硝基甲苯加入到含有液体载体的反应容器中并在恒定压力下用氢气还原,二硝基甲苯的加入速率使二硝基甲苯的浓度保持在总反应器内容物的0.0001至25重量%,同时保持氢化催化剂 基于反应器内容物的重量为约0.1至3%的水平。