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公开(公告)号:US07549400B2
公开(公告)日:2009-06-23
申请号:US11633758
申请日:2006-12-05
IPC: F22G1/00
CPC classification number: F22D1/38 , F01K3/185 , F22B1/18 , F22B37/00 , F22G1/16 , F23C9/00 , F23C2202/20 , F23L7/005 , F23L7/007 , Y02E20/344
Abstract: A method of heating process streams fed to a boiler incorporating an oxygen transport membrane device that includes an oxygen-containing stream and a boiler feed water stream. The membrane device separates oxygen to support combustion of a fuel and generate heat to raise the steam. Heat is recovered and process streams are heated by separately heating portions of the oxygen-containing stream and the boiler feed water stream with a retentate stream produced from the oxygen separation and a flue gas stream generated from the combustion. The flow rate of the portion of the oxygen-containing stream heated by the retentate stream is greater than that heated by the flue gas stream to help minimize heat transfer area and thus, fabrication costs. Also, water is condensed from the flue gas stream during the heat exchange involved in the heat recovery to increase thermodynamic efficiency.
Abstract translation: 一种加热工艺物流的方法,该方法加入到包含含氧物流和锅炉给水流的氧传输膜装置的锅炉中。 膜装置分离氧气以支持燃料的燃烧并产生热量以升高蒸汽。 回收热量,通过用氧气分离产生的滞留物流和从燃烧产生的烟道气分别加热含氧流和锅炉给水流的一部分来加热工艺流。 由滞留物流加热的部分含氧流的流量大于由烟气流加热的部分的流速,以帮助最小化传热面积,从而最小化制造成本。 此外,在热回收期间涉及的热交换中,水从烟道气流中冷凝以提高热力学效率。
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公开(公告)号:US20080141715A1
公开(公告)日:2008-06-19
申请号:US11639569
申请日:2006-12-15
Applicant: Vijayaraghavan Srinivasan Chakravarthy , Amitabh Gupta , Alan T.Y. Cheng
IPC: F25J3/00
CPC classification number: A61L2/022 , F17C2221/014 , F17C2260/044
Abstract: A system and method for sterilizing a cryogen is provided. In the disclosed embodiment a liquid cryogen is first vaporized and subsequently compressed prior to undergoing sterilization using biological filters. The compressed, sterilized cryogen vapor is then pre-cooled, preferably with the cryogen being vaporized, to produce a partially condensed, cool, sterile cryogen stream and then further condensed using the liquid cryogen to produce a sterilized liquid cryogen.
Abstract translation: 提供了一种用于对冷冻剂灭菌的系统和方法。 在所公开的实施方案中,液体冷冻剂首先在使用生物过滤器进行灭菌之前蒸发并随后压缩。 然后将经压缩的灭菌的冷冻剂蒸气预先冷却,优选在冷冻剂被蒸发的情况下,产生部分冷凝的,冷却的无菌制冷剂流,然后使用液体冷冻剂进一步冷凝以产生无菌液体冷冻剂。
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公开(公告)号:US20090308073A1
公开(公告)日:2009-12-17
申请号:US12374646
申请日:2007-07-25
Applicant: Dante Patrick Bonaquist , Minish Mahendra Shah , Vijayaraghavan Srinivasan Chakravarthy , Monica Zanfir , Raymond Francis Drnevich , Stefan Laux
Inventor: Dante Patrick Bonaquist , Minish Mahendra Shah , Vijayaraghavan Srinivasan Chakravarthy , Monica Zanfir , Raymond Francis Drnevich , Stefan Laux
CPC classification number: F23L7/007 , F01K13/00 , F01K25/10 , F22B1/16 , F23C9/00 , F23L2900/07005 , F25J3/04527 , F25J3/04533 , F25J3/04551 , F25J3/04557 , F25J3/04593 , F25J2230/22 , F25J2240/70 , Y02E20/344
Abstract: The present invention relates to a system for carrying out oxygen-enhanced combustion in an industrial process wherein the industrial process, an oxygen supply system or a source of oxygen, a heat recovery network, and an alternative Rankine cycle system based on a working fluid other than steam are integrated to achieve improved throughput and efficiency, and a method for oxygen-enhanced combustion in an industrial process using said system. Examples of industrial processes include cement production, steel reheat applications, glass production, aluminum and copper melting, as well as any industrial process that uses process heater, furnaces where combustion is carried out using an oxidant stream with oxygen content higher’ than that in ambient air and up to 100%.
Abstract translation: 本发明涉及一种用于在工业过程中进行增氧燃烧的系统,其中工业过程,氧供应系统或氧源,热回收网络和基于工作流体的替代兰金循环系统 比蒸汽整合以实现提高的产量和效率,以及使用所述系统的工业过程中的氧增强燃烧的方法。 工业过程的实例包括水泥生产,钢再热应用,玻璃生产,铝和铜熔化,以及使用工艺加热器的任何工业过程,使用氧气流进行燃烧的氧化剂流,其氧含量高于环境中的氧含量 空气高达100%。
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公开(公告)号:US07421856B2
公开(公告)日:2008-09-09
申请号:US11154630
申请日:2005-06-17
Applicant: Vijayaraghavan Srinivasan Chakravarthy , Richard John Jibb , Michael James Lockett , John Henri Royal
Inventor: Vijayaraghavan Srinivasan Chakravarthy , Richard John Jibb , Michael James Lockett , John Henri Royal
IPC: F25J3/00
CPC classification number: F25J5/002 , F25J3/04412 , F25J2235/50 , F25J2250/04 , F25J2250/20 , F25J2290/12 , Y10S62/903
Abstract: A cryogenic air separation system wherein nitrogen vapor from a higher pressure column and oxygen liquid from a lower pressure column each pass down through a once-through main condenser in heat exchange relation and some but not all of the oxygen liquid is vaporized such that the oxygen liquid and vapor exit the condenser in a liquid to vapor mass flowrate ratio within the range of from 0.05 to 0.5 whereby the need for a recirculation pump to ensure avoidance of oxygen boiling to dryness is eliminated.
Abstract translation: 一种低温空气分离系统,其中来自较高压力塔的氮气蒸汽和来自低压塔的氧气液体各自以热交换关系通过直通主冷凝器,并且部分但不是全部的氧液体被蒸发,使得氧气 液体和蒸汽以0.05至0.5的液体与蒸汽质量流量比离开冷凝器,由此消除了需要一个循环泵,以确保避免氧气沸腾至干燥。
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公开(公告)号:US20080127911A1
公开(公告)日:2008-06-05
申请号:US11633758
申请日:2006-12-05
IPC: F22B31/08
CPC classification number: F22D1/38 , F01K3/185 , F22B1/18 , F22B37/00 , F22G1/16 , F23C9/00 , F23C2202/20 , F23L7/005 , F23L7/007 , Y02E20/344
Abstract: A method of heating process streams fed to a boiler incorporating an oxygen transport membrane device that includes an oxygen-containing stream and a boiler feed water stream. The membrane device separates oxygen to support combustion of a fuel and generate heat to raise the steam. Heat is recovered and process streams are heated by separately heating portions of the oxygen-containing stream and the boiler feed water stream with a retentate stream produced from the oxygen separation and a flue gas stream generated from the combustion. The flow rate of the portion of the oxygen-containing stream heated by the retentate stream is greater than that heated by the flue gas stream to help minimize heat transfer area and thus, fabrication costs. Also, water is condensed from the flue gas stream during the heat exchange involved in the heat recovery to increase thermodynamic efficiency.
Abstract translation: 一种加热工艺物流的方法,该方法加入到包含含氧物流和锅炉给水流的氧传输膜装置的锅炉中。 膜装置分离氧气以支持燃料的燃烧并产生热量以升高蒸汽。 回收热量,通过用氧气分离产生的滞留物流和从燃烧产生的烟道气分别加热含氧流和锅炉给水流的一部分来加热工艺流。 由滞留物流加热的部分含氧流的流量大于由烟气流加热的部分的流速,以帮助最小化传热面积,从而最小化制造成本。 此外,在热回收期间涉及的热交换中,水从烟道气流中冷凝以提高热力学效率。
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公开(公告)号:US06666046B1
公开(公告)日:2003-12-23
申请号:US10259357
申请日:2002-09-30
IPC: F25B4100
CPC classification number: F25B9/006 , F25B9/02 , F25B40/00 , F25B2400/23 , F25B2500/01 , F25J1/0022 , F25J1/0055 , F25J1/0092 , F25J1/0212 , F25J1/0248 , F25J1/0258 , F25J1/0259 , F25J1/0262
Abstract: A refrigeration system particularly useful with a multicomponent refrigerant fluid wherein the refrigerant fluid is cooled in an upward leg of a first vertically oriented heat exchanger section and further cooled in a downward leg of a second vertically oriented heat exchanger section prior to refrigeration generation and serial recycle flow through the two heat exchanger sections.
Abstract translation: 一种特别适用于多组分制冷剂流体的制冷系统,其中制冷剂流体在第一垂直取向的热交换器部分的向上的腿部中被冷却,并且在制冷生成和连续循环之前在第二垂直取向的热交换器部分的下端进一步冷却 流过两个热交换器部分。
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