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Process for recovery and reuse of ammonia in a liquid ammonia fabric treating system

机译:在液氨织物处理系统中回收和再利用氨的方法

摘要

The disclosure is directed to a system for the recovery of spent ammonia, in connection with the processing of fabrics and the like with liquid ammonia, and concerns particularly the elimination from the recovered ammonia of undesired water.PPEconomic processing of fabrics by liquid ammonia requires recovery and reuse of substantial quantities of ammonia. In the course of processing, the ammonia unavoidably becomes contaminated with water. Separation of water from ammonia on a laboratory level or, in any kind of batch processing is a theoretically simple matter and can be coped with by conventional differential evaporation techniques, or otherwise. However, in a continuously operating processing line where large quantities of anhydrous liquid ammonia are being used as the treating medium, water accumulates rapidly, not only from the fabric being processed, but also from a certain inevitable amount of air leakage in the system. Because so much of any given increment of the treating medium must be recycled, as compared to that actually "used up" in the treating process, water accumulates rapidly in the system and must be removed on a continuous basis. The specification discloses a unique and highly efficient procedure for removal of water by effecting condensation of water and ammonia vapors, constituting the process effluent, by feeding the effluent to a desuperheating vessel, where it is brought into direct contact with a body of low temperature liquid ammonia. This is done in conjunction with a preliminary low temperature condensation of the effluent in a non- contact heat exchange stage. The condensed body of liquid ammonia in the desuperheater vessel, including residual condensed water from the process effluent combined with re-liquefied ammonia, forms the feed supply of liquid ammonia solution to the process. The condensed water, which in the new process constitutes a portion of the feed supply, is applied to the fabric being treated, along with the liquid ammonia. Typically, some of the water is carried away with the processed fabric as a constituent of its moisture content. The remainder, which is driven off as steam in the process, is recycled.P PA key factor in the new process is that the re-liquefied ammonia, instead of being sent directly back to the process, is directed into the desuperheater vessel, there being combined with the condensed process effluent. The combined solution, containing a minor fraction of condensed residual water is then fed back to the process. In this manner, the total water fraction in the process solution may be kept a satisfactorily low level, typically on the order of two or three percent maximum, under extreme process conditions, and desirably much lower than that under more favorable process conditions.
机译:本发明涉及一种与用液态氨处理织物等有关的废氨的回收系统,尤其涉及从回收的氨中消除不希望有的水。液态氨制成的织物需要回收和再利用大量的氨。在处理过程中,氨不可避免地被水污染。在实验室水平或以任何分批处理方式从氨中分离水在理论上是简单的事情,并且可以通过常规的差动蒸发技术或其他方法来解决。然而,在连续操作的生产线中,其中大量的无水液态氨被用作处理介质,水不仅从被处理的织物而且从系统中不可避免的一定量的空气泄漏迅速积聚。由于与处理过程中实际“用完”的处理介质相比,任何给定增量的处理介质中的大部分必须被循环利用,因此水在系统中迅速积聚,必须连续去除。该说明书公开了一种独特且高效的去除水的程序,该方法通过将水和氨蒸气冷凝而构成工艺废水,方法是将废水进料至减温容器中,在该容器中与低温液体直接接触,从而使废水脱出。氨。这是在非接触式热交换阶段结合废水的初步低温冷凝完成的。减温器容器中的液态氨冷凝物,包括来自工艺废水的残留冷凝水和再液化的氨,构成了工艺中液态氨溶液的进料。在新工艺中,构成进料一部分的冷凝水与液氨一起被施加到​​被处理的织物上。典型地,一些水作为其水分含量的一部分被处理过的织物带走。在过程中作为蒸汽排出的其余部分被回收。

新过程的关键因素是将重新液化的氨直接送入过程中,而不是直接送回过程中。过热器容器与冷凝的过程废液合并。然后将包含少量冷凝残留水的合并溶液送回过程。以这种方式,在极端的工艺条件下,工艺溶液中的总水含量可以保持令人满意的低水平,通常最大为百分之二或三,并且比在更有利的工艺条件下理想地低得多。

著录项

  • 公开/公告号US4074969A

    专利类型

  • 公开/公告日1978-02-21

    原文格式PDF

  • 申请/专利权人 CLUETT PEABODY & CO. INC.;

    申请/专利号US19760679059

  • 发明设计人 JACKSON LAWRENCE;

    申请日1976-04-21

  • 分类号D06M1/24;F25J3/00;

  • 国家 US

  • 入库时间 2022-08-22 21:32:08

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