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公开(公告)号:US5565017A
公开(公告)日:1996-10-15
申请号:US428610
申请日:1995-04-25
CPC分类号: C01B13/0251 , B01D53/22 , B01D53/326 , F01K23/064 , C01B2210/0046 , Y02E20/18 , Y02P20/123 , Y02P20/131 , Y02P20/57
摘要: Oxygen is separated from air by a high temperature ion transport membrane which is integrated with a gas turbine system for energy recovery from the membrane nonpermeate stream. Air is compressed, heated in a first heating step, and passed through the feed side of a mixed conductor membrane zone to produce a high purity oxygen product on the permeate side of the membrane zone. Nonpermeate gas from the membrane zone is heated in a second heating step and passed through a hot gas turbine for power recovery. Water is added to the nonpermeate gas prior to the hot gas turbine to increase mass flow to the turbine and thus balance the mass flows of the air feed compressor and the expansion turbine. The operating temperatures of the membrane zone and the expansion turbine are independently maintained by controlling the rate of heat addition in the first and second heating steps and by controlling the rate of water addition, whereby the membrane zone and expansion turbine are thermally delinked for maximum oxygen recovery efficiency.
摘要翻译: 氧气通过与气体涡轮机系统集成的高温离子传输膜与空气分离,以从膜非渗透流中回收能量。 将空气压缩,在第一加热步骤中加热,并通过混合导体膜区域的进料侧,以在膜区域的渗透侧产生高纯度氧产物。 来自膜区的非渗透气体在第二加热步骤中被加热,并通过热燃气轮机进行动力回收。 在热燃气涡轮机之前将水加入到非渗透气体中,以增加到涡轮机的质量流量,从而平衡供气压缩机和膨胀涡轮机的质量流量。 通过控制第一和第二加热步骤中的加热速率并通过控制加水速率来独立地维持膜区和膨胀涡轮机的操作温度,由此膜区域和膨胀涡轮机对于最大氧气进行热脱水 恢复效率。
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公开(公告)号:US6030598A
公开(公告)日:2000-02-29
申请号:US93209
申请日:1998-06-08
IPC分类号: B01D53/04 , B01D53/047 , C01B13/10 , B01D53/02
CPC分类号: C01B13/10 , B01D53/047 , B01D2253/108 , B01D2256/14 , B01D2257/104 , B01D2257/106 , B01D2259/40056 , B01D2259/40079 , B01D2259/40081 , B01D2259/403 , B01D53/0423
摘要: An ozone containing gas stream is produced from oxygen by subjecting oxygen to an electric discharge and the ozone is then adsorbed on to a solid adsorbent, such as zeolite, the oxygen containing stream leaving the adsorbent is recycled to the ozonising process. Periodically, oxygen adsorbed on the adsorbent is desorbed by co-currently passing a purge gas over the adsorbent and the desorbed oxygen is also recycled to the ozoniser. Lastly ozone is desorbed from the adsorbent by a counter-current flow of purge gas and used in an ozone demanding process.
摘要翻译: 通过使氧进行放电,然后将臭氧吸附到诸如沸石的固体吸附剂上,由氧气产生含臭氧的气流,离开吸附剂的含氧流再循环到臭氧化过程中。 周期性地,吸附剂上吸附的氧气通过共同通过吹扫气体吸附在吸附剂上而解吸,并且解吸的氧也被再循环到臭氧发生器中。 最后,臭氧通过逆流净化气体从吸附剂中解吸并用于臭氧需求过程中。
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公开(公告)号:US5483806A
公开(公告)日:1996-01-16
申请号:US439802
申请日:1995-05-12
CPC分类号: F25B9/004
摘要: A refrigeration system using air as the refrigerant comprises a compressor which compresses air to 84 bar g. The compressed air is cooled first by cooling water and then by returning air in a plate-fin heat exchanger before being expanded to 59 bar g in an expander. The expanded air at -61.degree. C. is passed through indirect cooling coils in a cold store which it leaves at -45.degree. C. This air is then passed through the plate-fin heat exchanger before being recycled to the compressor. The refrigeration delivered is about 1.05 kw refrigeration/kw power input.
摘要翻译: 使用空气作为制冷剂的制冷系统包括将空气压缩至84巴g的压缩机。 首先通过冷却水冷却压缩空气,然后在膨胀器中膨胀至59巴g之前,通过在板翅式热交换器中返回空气。 在-61℃的膨胀空气在-45℃离开的冷库中通过间接冷却盘管。然后在将空气再循环到压缩机之前将该空气通过板翅式热交换器。 供应的制冷约为1.05 kw制冷/ kw功率输入。
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