首页> 外国专利> Process for recovery and reuse of liquid ammonia.Apparatus for processing of fabrics with liquid ammonia and system for recovery and reuse of ammonia is served for a treatment process with liquid ammonia

Process for recovery and reuse of liquid ammonia.Apparatus for processing of fabrics with liquid ammonia and system for recovery and reuse of ammonia is served for a treatment process with liquid ammonia

机译:液氨的回收和再利用方法。用液氨处理织物的设备和氨的回收和再利用系统用于液氨的处理过程。

摘要

From the exhaust gas continuously withdrawn from the treatment chamber (13) and containing NH3 gas, air and water vapour, the NH3 is continuously recovered and returned to the treatment process in a virtually anhydrous liquid form. The drawing illustrates a usable NH3 recovery plant. In the drawing (13) denotes treatment chamber; (27) denotes extraction line; (29) storage vessel for liquid NH3; (32) heat exchanger; (32a) denotes condensate water discharge line; (33) denotes cooling water feed line; (33a) denotes feed line for liquid ammonia; (34) denotes cooling water outlet line; (34a) denotes outlet line for liquid ammonia; (35) denotes outlet line for supercooled gases; (36) denotes saturation vessel; (37) denotes cold, liquid NH3; (38) denotes space for cooled gases; (39) denotes connection line between space (38) and suction side of a compressor (40); (40) denotes compressor; (41) denotes compressor drive motor; (42) denotes high pressure line for compressed gases; (43) denotes tube bundle condenser/heat exchanger; (44) denotes cooling water feed line; (45) denotes cooling water outlet line; (46) denotes high pressure line for liquid NH3; (47) denotes outflow line for uncondensed gases; (46) denotes NH3-cooled separator; (49) denotes condensate line to the saturation vessel (36); (50) denotes expansion valve; (51) denotes outlet line for liquid NH3; (52) denotes saturation vessel output line, leads via pump (53) and control valve (54) into the line (18) leading into the treatment chamber (13) with the treatment trough; (55 and 56) level sensors for controlling valve (57) in line (58) for the feed of liquid NH3 from the storage vessel (29) into the saturation vessel (36). The process enables the water content in the treatment agent to be kept continuously beneath 3%. IMAGE
机译:从连续地从处理室(13)排出的,含有NH3气体,空气和水蒸气的废气中,NH3被连续回收并以几乎无水的液体形式返回处理过程。该图说明了可用的NH3回收装置。图中的(13)表示处理室。 (27)表示提取线; (29)液态氨的储存容器; (32)热交换器; (32a)表示冷凝水排出管线; (33)是冷却水供给管线。 (33a)表示液氨的供给管线。 (34)是冷却水出口管线。 (34a)表示液氨的出口管线。 (35)表示过冷气体的出口管线; (36)是饱和容器。 (37)表示冷的液态NH3; (38)表示冷却气体的空间; (39)是空间(38)与压缩机(40)的吸入侧之间的连接线。 (40)是压缩机。 (41)是压缩机驱动电动机。 (42)是压缩气体的高压线。 (43)是管束冷凝器/热交换器。 (44)是冷却水供给管。 (45)为冷却水出口管线。 (46)表示液态NH3的高压管线; (47)表示未冷凝气体的流出管线; (46)表示NH3冷却的分离器; (49)表示到饱和容器(36)的冷凝水管线。 (50)表示膨胀阀; (51)表示液体NH3的出口管线; (52)是饱和容器的输出管路,通过泵(53)和控制阀(54)通向通过处理槽导入处理室(13)的管路(18)。 (55和56)液位传感器,用于控制管路(58)中的阀(57),以将液态NH3从存储容器(29)送入饱和容器(36)。该方法使处理剂中的水含量连续保持在3%以下。 <图像>

著录项

  • 公开/公告号TR19638A

    专利类型

  • 公开/公告日1979-09-04

    原文格式PDF

  • 申请/专利权人 CLUETT PEADODY & CO INC;

    申请/专利号TR19760019638

  • 发明设计人

    申请日1976-12-20

  • 分类号D06M11/00;C01C1/12;D06B9/06;D06B23/20;D06M11/61;D06M101/00;D06M101/02;D06M101/06;

  • 国家 TR

  • 入库时间 2022-08-22 20:31:59

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