| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 1 | 隔热系统 | CN200780043951.5 | 2007-11-13 | CN101542187B | 2011-06-08 | R·J·吉布; J·H·罗亚尔 |
| 一种隔热系统，其在容器内阻止从周围环境到位于容器内的设备的热泄漏，该设备在低温下操作。该隔热系统包括填充容器的散装隔热材料和位于容器内的隔热层，该隔热层处在设备与容器之间。与散装隔热材料相比，隔热层具有更低的热导率。设备的一部分外部区域比设备的其余外部区域更靠近容器的相对容器壁区域。隔热层的尺寸定成仅隔热设备的该一部分外部区域避免通过相对容器壁区域的热泄漏。隔热层可由气凝胶形成。 | ||||||
| 2 | 隔热布置 | CN200780043951.5 | 2007-11-13 | CN101542187A | 2009-09-23 | R·J·吉布; J·H·罗亚尔 |
| 一种隔热布置，其在容器内阻止从周围环境到位于容器内的设备的热泄漏，该设备在低温下操作。该隔热布置包括填充容器的散装隔热材料和位于容器内的隔热层，该隔热层处在设备与容器之间。与散装隔热材料相比，隔热层具有更低的热导率。设备的一部分外部区域比设备的其余外部区域更靠近容器的相对容器壁区域。隔热层的尺寸定成仅隔热设备的该一部分外部区域避免通过相对容器壁区域的热泄漏。隔热层可由气凝胶形成。 | ||||||
| 3 | 热交换器组合件和结合有该组合件的低温蒸馏设备 | CN200580045642.2 | 2005-12-23 | CN101095022A | 2007-12-26 | P·卡瓦涅; A·吉亚尔; P·勒博; D·古尔丹; M·瓦格纳; F·茹达斯; J-M·佩龙; B·索尼耶; D·阿弗鲁; I·瑙德; I·莱沃 |
| 热交换器组合件，包括至少一个第一热交换器主体和一个第二热交换器主体(5，7)，每一个热交换器主体是板式热交换器类型并包括：多个具有基本上相似轮廓的金属板，这些金属板沿着第一方向或长度和第二方向或宽度延伸，沿着第三方向或厚度彼此间隔地、相互平行地设置；以及密封装置，该密封装置与上述板一起限定扁平通道，形成至少一个第一类型的通道和至少一个第二类型的通道，分配于每一个通道的密封装置形成一个流体进口和一个流体出口，其特征在于，由至少一个第一热交换器主体的宽度和厚度限定的侧面与由至少一个第二热交换器主体的宽度和厚度限定的侧面至少部分地相对配置，这两侧面由绝热材料(I)分隔开。 | ||||||
| 4 | 换热器和包含该换热器的气体分离单元的安装方法 | CN201380048485.5 | 2013-08-29 | CN104641197B | 2017-08-04 | F·克雷萨克; B·达维迪安; F·戴尔科索; S·德绍特; J-P·特拉尼耶; M·瓦格纳 |
| 本发明涉及一种换热器(1)，包括:平行的板(2)，限定用于加热或冷却流体的通路；在板(2)之间延伸并限定通路的间隔件；以及覆盖所述板(2)并且包括防火热绝缘层的单个壳体。 | ||||||
| 5 | 换热器和包含该换热器的气体分离单元的安装方法 | CN201380048485.5 | 2013-08-29 | CN104641197A | 2015-05-20 | F·克雷萨克; B·达维迪安; F·戴尔科索; S·德绍特; J-P·特拉尼耶; M·瓦格纳 |
| 本发明涉及一种换热器(1)，包括:平行的板(2)，限定用于加热或冷却流体的通路；在板(2)之间延伸并限定通路的间隔件；以及覆盖所述板(2)并且包括防火热绝缘层的单个壳体。 | ||||||
| 6 | 热交换器组合件和结合有该组合件的低温蒸馏设备 | CN200580045642.2 | 2005-12-23 | CN100590374C | 2010-02-17 | P·卡瓦涅; A·吉亚尔; P·勒博; D·古尔丹; M·瓦格纳; F·茹达斯; J-M·佩龙; B·索尼耶; D·阿弗鲁; I·瑙德; I·莱沃 |
| 热交换器组合件，包括至少一个第一热交换器主体和一个第二热交换器主体(5，7)，每一个热交换器主体是板式热交换器类型并包括：多个具有基本上相似轮廓的金属板，这些金属板沿着第一方向或长度和第二方向或宽度延伸，沿着第三方向或厚度彼此间隔地、相互平行地设置；以及密封装置，该密封装置与上述板一起限定扁平通道，形成至少一个第一类型的通道和至少一个第二类型的通道，分配于每一个通道的密封装置形成一个流体进口和一个流体出口，其特征在于，由至少一个第一热交换器主体的宽度和厚度限定的侧面与由至少一个第二热交换器主体的宽度和厚度限定的侧面至少部分地相对配置，这两侧面由绝热材料(I)分隔开。 | ||||||
| 7 | Cryogenic separation unit | JP2007548812 | 2005-12-23 | JP4991561B2 | 2012-08-01 | アベル、ダビッド; カバーニュ、パトリス; ギラール、アリン; グルディン、ダニエル; ジューダ、フレデリック; スルニール、ベルナール; ヌードゥ、イザベル; ペイロン、ジャン−マルク; ル・ボット、パトリック; レウォン、イバン; ワグネール、マルク |
| A heat exchanger assembly has two series of heat exchangers (1, 2) stacked in the vertical direction. The two series of heat exchangers have an insulating material (I) placed between them. A heat exchange assembly comprises at least one first and one second heat exchange body (5, 7), each being of the plate heat exchanger type, comprising metal plates of similar contour extending along a first dimension or length and a second dimension or width, spaced from and arranged in parallel rows to one another along a third dimension or thickness and a sealing means bounding flattened passages with the the plates, forming at least one passage of a first type and at least one passage of a second type. The sealing means allocates to each passage releasing one fluid inlet and one fluid outlet, one inlet (El) of the first body being connected to a first delivery line for a fluid to be cooled (D AIR MP) and one outlet (S1) of the first body being connected to a first collecting line for cooled fluid (C AIR MP), another inlet of the first body being connected to a first delivery line (DNR) for fluid to be heated and another outlet of the first body being connected to a first collecting line for heated fluid (CNR), one inlet of the second body being connected to a delivery line for fluid to be cooled (Dl AIR HP, D2 AIR HP) and one outlet of the second body being connected to a collecting line for cooled fluid (C1 AIR HP, C2 AIR HP), another inlet of the second body being connected to a delivery line for fluid to be heated (DNR') and another outlet of the second body being connected to a collecting line for heated fluid (CNR'). One side bounded by a width and a thickness of at least one first heat exchange body is located at least partially opposite a side bounded by a width and a thickness of at least one second heat exchange body, the two sides being separated by insulating material (I). An independent claim is indluced for an apparatus for the cryogenic separation of a gas mixture, comprising a stripping unit, a heat exchange assembly as above, and a system of columns, means for conveying the gas mixture to the stripping unit, means for conveying the stripped gas mixture to the assembly of heat exchangers to be cooled at least in one of the first and second heat exchanger bodies (5, 7) to at least one pressure, means for conveying at least some gas mixture cooled in at least one of the first and second heat exchanger bodies to the system of columns, and means (DNR, DNR') for conveying at least one product from the system of columns to each of the first and second series of heat exchanger bodies. | ||||||
| 8 | Insulation arrangement | US14734244 | 2015-06-09 | US10048003B2 | 2018-08-14 | Richard John Jibb; John Henri Royal |
| An arrangement of insulation within a container to prevent heat leakage from the ambient to an apparatus located within the container that operates at a cryogenic temperature. The arrangement of insulation includes bulk insulation filling the container and an insulation layer that is located within the container, between the apparatus and the container. The insulation layer as opposed to the bulk insulation has a lower thermal conductivity. An exterior region of the apparatus is situated closer to an opposite container wall region of the container than remaining exterior regions of the apparatus. The insulation layer is sized to only insulate the exterior region of the apparatus from heat leakage from the opposite container wall region. The insulation layer can be formed of an aerogel. | ||||||
| 9 | LNG system with warm nitrogen rejection | US10785808 | 2004-02-24 | US20050183452A1 | 2005-08-25 | Paul Hahn; Phillip Ritchie; Jame Yao; Rong-Jwyn Lee; Anthony Eaton; William Low |
| Natural gas liquefaction system employing an enhanced nitrogen removal system capable of removing nitrogen from a relatively warm natural gas stream. | ||||||
| 10 | Dephlegmator system and process | US09663477 | 2000-09-15 | US06349566B1 | 2002-02-26 | Lee Jarvis Howard; Howard Charles Rowles; Randy James Nickel; Gene Anthony Lucadamo; Bruce Moodie Hill |
| Dephlegmator system without headers, collectors, or distributors at the bottom end of feed circuits in plate and fin exchangers operating in condensing or rectifying service. Each dephlegmator is installed within a pressure vessel, thereby eliminating the need for headers, collectors, or distributors at the bottom end of the feed circuits. In an alternative embodiment of the invention, upper and lower segments of the pressure vessel are isolated by a mid-vessel seal between the vessel and dephlegmator walls, and headers or collectors are not required at the upper and lower ends of the feed circuits. | ||||||
| 11 | Heat interchanger | US61843945 | 1945-09-25 | US2508247A | 1950-05-16 | GIAUQUE WILLIAM F |
| 12 | PURIFYING CRYOGENIC FLUIDS | US15195337 | 2016-06-28 | US20170003071A1 | 2017-01-05 | Patrick N. Gutelius; James R. Parys |
| A cryogenic fluid purification device comprising: a first container defining an interior region; a second container defining an interior region in fluid communication with the interior region of the first container; and a cryogenic fluid in contact with an exterior of the second container. | ||||||
| 13 | LOW-DENSITY SOLID-STATE INSULATION FOR CRYOGENIC SERVICE | US13712156 | 2012-12-12 | US20140158926A1 | 2014-06-12 | Paul YAMARICK |
| A cryogenic insulation system including a low density low conductivity insulation material for cryogenic service, wherein the low conductivity insulation material is essentially free of hydrocarbon residue. A method for producing a low density low conductivity insulation material for cryogenic service, comprising: exposing the low density low conductivity insulation material to at least one of an elevated temperature or a reduced pressure, for a length of time sufficient to reduce the hydrocarbon residue to less than 1000 ppm. | ||||||
| 14 | ASSEMBLY OF HEAT EXCHANGERS AND A CRYOGENIC DISTILLATION APPARATUS INCORPORATING THE SAME | US11813165 | 2005-12-23 | US20090211295A1 | 2009-08-27 | Patrice Cavagne; Alain Guillard; Patrick Le Bot; Daniel Gourdain; Marc Wagner; Frederic Judas; Jean-Marc Peyron; Bernard Saulnier; David Averous; Isabelle Naude; Ivan Lewon |
| Heat exchange assembly comprising at least one first and one second heat exchange body (5, 7), each body being of the plate heat exchanger type, comprising a plurality of metal plates of substantially similar contour extending along a first dimension or length and a second dimension or width, spaced from and arranged in parallel rows to one another along a third dimension or thickness and sealing means bounding flattened passages with the said plates, forming at least one passage of a first type and at least one passage of a second type, the sealing means allocated to each passage releasing one fluid inlet and one fluid outlet, characterized in that one side bounded by a width and a thickness of at least one first heat exchange body is located at least partially opposite a side bounded by a width and a thickness of at least one second heat exchange body, the two sides being separated by insulating material (I). | ||||||
| 15 | Insulation arrangement | US11605697 | 2006-11-30 | US20080127674A1 | 2008-06-05 | Richard John Jibb; John Henri Royal |
| An arrangement of insulation within a container to prevent heat leakage from the ambient to an apparatus located within the container that operates at a cryogenic temperature. The arrangement of insulation includes bulk insulation filling the container and an insulation layer that is located within the container, between the apparatus and the container. The insulation layer as opposed to the bulk insulation has a lower thermal conductivity. An exterior region of the apparatus is situated closer to an opposite container wall region of the container than remaining exterior regions of the apparatus. The insulation layer is sized to only insulate the exterior region of the apparatus from heat leakage from the opposite container wall region. The insulation layer can be formed of an aerogel. | ||||||
| 16 | Heat exchanger column | US09852361 | 2001-05-09 | US20020166656A1 | 2002-11-14 | Lee Jarvis Howard; Howard Charles Rowles; Randy James Nickel; Gene Anthony Lucadamo; Bruce Moodie Hill |
| Plate-and-fin core-type heat exchangers are installed within pressure vessels in a manner which eliminates the need for distributors, collectors, headers, nozzles, and manifolds at the feed inlet, the processed gas outlet, or both the feed inlet and the processed gas outlet of each exchanger core. The heat exchangers can be installed in parallel or in series within a single pressure vessel. Alternatively, the heat exchangers can be installed in pressure vessels which are arranged in series such that multiple liquid product streams can be obtained. The heat exchangers preferably are operated in the condensing mode in which feed gas is cooled and partially condensed. The operation of the heat exchangers is characterized by the cocurrent flow of the condensate and uncondensed feed gas, preferably in the vertical or near-vertical direction. In an alternative embodiment, the heat exchangers are operated such that a feed fluid is cooled without phase change. | ||||||
| 17 | Containment enclosure | US09719762 | 2000-12-14 | US06360545B1 | 2002-03-26 | Peter G. Goldstone; Rodney J. Allam |
| A containment enclosure (1) for a cryogenic unit (2) has a chamber (7) in which the cryogenic unit (2) is located. A chamber wall (4, 5, 6) includes thermally insulating bricks (10, 11) for thermally insulating the cryogenic unit (2) in the chamber (7). The chamber wall (4, 5, 6) is impermeable to liquid leaking from the cryogenic unit (2). A sump (30) is provided for receiving any liquid leaking from the cryogenic unit (2). Withdrawing means (31) are provided for withdrawing liquid from the sump (30) through an open uppermost end of the sump (30). | ||||||
| 18 | Thermal insulation construction | US41023164 | 1964-11-10 | US3361284A | 1968-01-02 | SOTIRI LUKA; KORDYBAN EUGENE S; REKAWEK JAN F |
| 19 | Low temperature gas decomposition plant | US83167959 | 1959-08-04 | US3107992A | 1963-10-22 | ALFONS SELLMAIER |
| 20 | CONDUIT SEAL ASSEMBLY | EP14875259.5 | 2014-12-11 | EP3087299B1 | 2018-06-06 | DAVIES, Paul R.; THOMAS, Emery Jay; HARRIS, James L. |
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