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Process and device for carrying off free and combined ammonia from aqueous solutions containing both components

机译:从含有两种成分的水溶液中排出游离氨和合并氨的方法和装置

摘要

1. Process for stripping free and combined ammonia from aqueous solutions containing these two components, in which the combined ammonia is liberated by treatment with caustic soda and the free ammonia is stripped from the solution with steam and/or exhaust vapours and in which the process is carried out in columns fitted with suitable internals, characterized by the use of the following process features : a) The treatment of the ammoniacal feed solution is carried out in a single column consisting of three sections, of which the first (top) section and the second section below it are connected by a plate which is permeable to gas and liquid while the second and third sections are separated from each other by an impermeable plate : b) the ammoniacal feed solution is introduced at the head of the column into the first section of the same and after passing through the first section is divided into two component streams of which one component steam flows directly into the second section below while the other component stream is fed directly into the third section of the column via a by-pass line, in which the stripping vapour is introduced into the third and second sections of the column and the caustic soda is also fed into the second section, and c) the vapours rising in the third section of the column are introduced via a by-pass line into the second or the first sections of the same, while the regenerated solution leaving the third section of the column is transferred for re-use and the solution leaving the second section is rejected from the process after appropriate waste water treatment.
机译:1.从含有这两种成分的水溶液中汽提游离和合并的氨的方法,其中通过用苛性钠处理释放合并的氨,并用蒸汽和/或废气将游离的氨从溶液中汽提,并且其中该方法在装有合适内件的塔中进行,其特征在于使用以下工艺特征:a)氨水进料溶液的处理在由三部分组成的单个塔中进行,其中第一(顶部)部分和下方的第二部分通过一块可透过气体和液体的板连接,而第二部分和第三部分通过一块不可渗透的板彼此隔开:b)将氨的进料溶液从塔顶引入第一部分相同部分并经过第一部分后分成两部分,其中一股蒸汽直接流入第二部分b当另一组分流通过旁路管线直接进料到塔的第三部分时,汽提蒸气被引入到塔的第三和第二部分中,并且苛性钠也被进料到第二部分中c)在塔的第三部分中上升的蒸气通过旁路管线引入到塔的第二或第一部分中,而离开塔的第三部分的再生溶液则被转移再利用经过适当的废水处理后,离开第二部分的溶液将从工艺中剔除。

著录项

  • 公开/公告号EP0103674A3

    专利类型

  • 公开/公告日1985-08-21

    原文格式PDF

  • 申请/专利权人 KRUPP KOPPERS GMBH;

    申请/专利号EP19830104711

  • 发明设计人 RIZZON JOHN;DIEMER PETER DR. DIPL.-ING.;

    申请日1983-05-13

  • 分类号C01C1/10;C02F1/58;B01D19/00;B01D3/14;

  • 国家 EP

  • 入库时间 2022-08-22 08:02:57

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