首页> 外国专利> Preparation of xylylenediamine comprises continuously hydrogenating phthalodinitrile over a heterogeneous catalyst in the presence of liquid ammonia, where a portion of reactor effluent is recycled continuously to the reactor inlet

Preparation of xylylenediamine comprises continuously hydrogenating phthalodinitrile over a heterogeneous catalyst in the presence of liquid ammonia, where a portion of reactor effluent is recycled continuously to the reactor inlet

机译:苯二甲胺的制备包括在液氨存在下,在非均相催化剂上连续氢化邻苯二甲腈,其中一部分反应器流出物连续循环到反应器入口

摘要

Preparation of xylylenediamine by continuously hydrogenating phthalodinitrile over a heterogeneous catalyst in a reactor, in which a portion of the reactor effluent is recycled as a liquid circulation stream continuously to the reactor inlet, comprises mixing phthalodinitrile by a mixing device with a stream of liquid ammonia (stream a) and a further stream that is removed at least as a sub-stream from the circulation stream around the hydrogenation reactor (stream b), or mixing of streams a and b, and conducting the resulting liquid mixture into the hydrogenation reactor. Preparation of xylylenediamine by continuously hydrogenating phthalodinitrile over a heterogeneous catalyst in the presence of liquid ammonia in a reactor, in which a portion of the reactor effluent is recycled as a liquid circulation stream continuously to the reactor inlet (circulation mode), comprises mixing phthalodinitrile, as melt or in solid form, by a mixing device with a stream of liquid ammonia (stream a) and a further stream that is drawn off at least as a sub-stream from the circulation stream around the hydrogenation reactor (stream b), or mixing of streams a and b, and conducting the resulting liquid mixture into the hydrogenation reactor.
机译:通过在反应器中的非均相催化剂上连续氢化邻苯二甲腈制备苯二甲胺,其中一部分反应器流出物作为液体循环流连续循环到反应器入口,包括通过混合装置将邻苯二甲腈与液氨流混合(物流a)和另外的物流,该物流至少作为子物流从围绕氢化反应器的循环物流中除去(物流b),或将物流a和b混合,并将得到的液体混合物导入氢化反应器中。通过在反应器中在液氨存在下在非均相催化剂上连续氢化邻苯二甲腈制备二甲苯二胺,其中将一部分反应器流出物作为液体循环流连续循环到反应器入口(循环方式),包括混合邻苯二甲腈,通过混合装置以熔融或固体形式与液态氨流(流a)和另一流至少作为子流从加氢反应器周围的循环流(流b)中抽出,或将料流a和b混合,并将所得的液体混合物导入氢化反应器中。

著录项

  • 公开/公告号DE102005058417A1

    专利类型

  • 公开/公告日2007-06-14

    原文格式PDF

  • 申请/专利权人 BASF AG;

    申请/专利号DE20051058417

  • 发明设计人 HUBER SABINE;DAHMEN KIRSTEN;RANDOLF HUGO;

    申请日2005-12-07

  • 分类号C07C209/48;C07C211/51;

  • 国家 DE

  • 入库时间 2022-08-21 20:29:35

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