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51. 发明公开

EP2212402A4 METHOD AND SYSTEM FOR THE SMALL-SCALE PRODUCTION OF LIQUIFIED NATURAL GAS (LNG) FROM LOW-PRESSURE GAS 有权
标题翻译：方法和系统LPG（液化天然气）来自按照低压气体生产常设小尺度
公开(公告)号：EP2212402A4
公开(公告)日：2014-04-23
申请号：EP08847848
申请日：2008-11-05
申请人： VANDOR DAVID , GREENBERG RALPH
发明人： VANDOR DAVID , GREENBERG RALPH
IPC分类号： F25J1/00 , F25J1/02
CPC分类号： F25J1/0227 , F25J1/0022 , F25J1/0025 , F25J1/0035 , F25J1/0037 , F25J1/004 , F25J1/0045 , F25J1/0202 , F25J1/023 , F25J1/0231 , F25J1/0242 , F25J1/0254 , F25J1/0277 , F25J1/0278 , F25J1/0281 , F25J1/0283 , F25J1/0288 , F25J2230/04 , F25J2230/22 , F25J2230/30 , F25J2245/02 , F25J2245/90 , F25J2270/906 , F25J2290/62

52. 发明公开

EP2500565A1 SUPERCRITICAL AIR ENERGY STORAGE SYSTEM 有权
标题翻译：超滤器润滑脂系统
公开(公告)号：EP2500565A1
公开(公告)日：2012-09-19
申请号：EP10827783.1
申请日：2010-08-31
申请人： Institute Of Engineering Thermophysics, Chinese Academy Of Sciences
发明人： CHEN, Haisheng , TAN, Chunqing , LIU, Jia , XU, Yujie
IPC分类号： F03G7/06
CPC分类号： F03G7/06 , F01K3/004 , F01K5/02 , F01K7/22 , F25J1/0012 , F25J1/0037 , F25J1/0045 , F25J1/0228 , F25J1/0251 , F25J3/04018 , F25J3/04054 , F25J3/04084 , F25J3/04187 , F25J3/04193 , F25J3/04309 , F25J3/044 , F25J3/04581 , F25J3/04842 , F25J2205/24 , F25J2230/04 , F25J2230/08 , F25J2230/30 , F25J2240/10 , F25J2240/90 , F25J2245/90 , Y02E60/15
摘要： Disclosed is an energy storage system using supercritical air, comprising compressor units (1, 3), heat exchanger and storage device (2, 4), a throttle valve (5), a cryogenic tank (6), a cryogenic pump (8), expander units (9, 10), a generator (11), a driver unit (12), and a plurality of pipes. There are several advantages of this invention, including high energy density, high efficiency, no storage cycle and geographical conditions restriction, easy implementation with all kinds of power stations, environment friendliness and capability of recycling low to medium temperature waste heat and so on.
摘要翻译：公开了一种使用超临界空气的能量存储系统，包括压缩机单元（1,3），热交换器和存储装置（2,4），节流阀（5），低温罐（6），低温泵（8），膨胀机组（9,10），发电机（11），驱动单元（12）和多个管道。本发明有几个优点，包括高能量密度，高效率，无储存循环和地理条件限制，易于实施各种发电站，环境友好和回收中低温余热等能力。

53. 发明公开

EP2381198A1 Method for separating carbon dioxide from flue gas of combustion plants 有权转让
标题翻译：一种用于二氧化碳从烟气从焚烧厂分离过程
公开(公告)号：EP2381198A1
公开(公告)日：2011-10-26
申请号：EP10004249.8
申请日：2010-04-21
申请人： Alstom Technology Ltd
发明人： Stallmann, Olaf
IPC分类号： F25J3/06 , F25J3/02 , B01D53/00 , C01B31/20
CPC分类号： F25J1/0027 , B01D53/002 , B01D2257/504 , B01D2258/0283 , F25J3/0266 , F25J3/067 , F25J2200/02 , F25J2200/40 , F25J2200/70 , F25J2200/76 , F25J2205/04 , F25J2210/70 , F25J2215/04 , F25J2220/82 , F25J2230/04 , F25J2230/30 , F25J2230/32 , F25J2235/80 , F25J2240/90 , F25J2260/80 , F25J2270/02 , F25J2270/06 , F25J2270/80 , F25J2290/62 , Y02C10/12 , Y02E20/326
摘要： Method for producing liquid CO 2 of combustion flue gases wherein the flue gas (3) is compressed in a first compressor (1), subsequently cooled in a first cooler (5)and partially condensed in at least two separation stages (9,21), wherein the at least two separation stages (9,21) are cooled by expanded offgas (23) and expanded liquid CO 2 (3.1,3.3), and wherein the first cooler (5) is supplied with chilled water from the first separation stage.

54. 发明授权

EP2050999B1 System to cold compress an air stream using natural gas refrigeration 无效
标题翻译：系统用于通过天然气冷却的空气流的冷压缩
公开(公告)号：EP2050999B1
公开(公告)日：2011-02-23
申请号：EP08166447.6
申请日：2008-10-13
申请人： Air Products and Chemicals, Inc.
发明人： Dee, Douglas Paul , Herron, Donn Michael , Choe, Jung Soo
IPC分类号： F17C9/04 , F25J3/04
CPC分类号： F25J3/04412 , F25J1/0015 , F25J1/0221 , F25J1/0234 , F25J3/04018 , F25J3/04157 , F25J3/04224 , F25J3/04266 , F25J3/04351 , F25J2210/62 , F25J2230/02 , F25J2230/04 , F25J2270/904

55. 发明授权

EP1476708B1 COOLING PROCESS AND APPARATUS FOR COOLING A FLUID USING COOLANT WATER 无效
标题翻译：冷却器和方法用于冷却液使用水冷却
公开(公告)号：EP1476708B1
公开(公告)日：2010-01-27
申请号：EP03739608.2
申请日：2003-02-12
申请人： L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude
发明人： KLEIN, Eric, P.
IPC分类号： F28D21/00 , F28C1/00 , F25J3/00
CPC分类号： F28D21/0012 , F25J3/04018 , F25J3/04157 , F25J3/04775 , F25J2205/02 , F25J2205/32 , F25J2205/34 , F25J2230/04 , F25J2245/02 , F25J2270/90 , F25J2280/02 , F28C1/00 , Y02B30/566

56. 发明公开

EP2050999A1 System to cold compress an air stream using natural gas refrigeration 无效
标题翻译：系统zur Kaltkomprimierung eines Luftstroms mitKühlungdurch Erdgas
公开(公告)号：EP2050999A1
公开(公告)日：2009-04-22
申请号：EP08166447.6
申请日：2008-10-13
申请人： Air Products and Chemicals, Inc.
发明人： Dee, Douglas Paul , Herron, Donn Michael , Choe, Jung Soo
IPC分类号： F17C9/04 , F25J3/04
CPC分类号： F25J3/04412 , F25J1/0015 , F25J1/0221 , F25J1/0234 , F25J3/04018 , F25J3/04157 , F25J3/04224 , F25J3/04266 , F25J3/04351 , F25J2210/62 , F25J2230/02 , F25J2230/04 , F25J2270/904
摘要： An air stream (100) is compressed in multiple stages (3a, 3b, 3c) using refrigeration derived from a refrigerant (166, 168) comprising natural gas for inter-stage cooling (4b, 4c). The possibility of natural gas leaking into the air stream is reduced by use of an intermediate cooling medium ("ICM") to transfer (4) the refrigeration from the refrigerant to the inter-stage air stream (102, 104). The compressed air stream can be fed to a cryogenic air separation unit (1) that includes an LNG-based liquefier unit (2) from which a cold natural gas stream is withdrawn for use as said refrigerant.
摘要翻译：空气流（100）利用来自包含用于级间冷却的天然气（4b，4c）的制冷剂（166,168）的制冷而在多级（3a，3b，3c）中被压缩。通过使用中间冷却介质（“ICM”）将天然气泄漏到空气流中的可能性降低，从而将（4）制冷从制冷剂转移到级间空气流（102,104）。压缩空气流可以被供给到低温空气分离单元（1），所述低温空气分离单元（1）包括LNG基液化器单元（2），冷的天然气流从该液化器单元（2）被抽出用作所述制冷剂。

57. 发明公开

EP1869385A2 PROCEDE ET INSTALLATION INTEGRES D'ADSORPTION ET DE SEPARATION CRYOGENIQUE POUR LA PRODUCTION DE CO2 有权
标题翻译：集成工艺和集成系统的低温吸附及其制备分离CO2
公开(公告)号：EP1869385A2
公开(公告)日：2007-12-26
申请号：EP06726290.7
申请日：2006-03-30
申请人： L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude
发明人： DUBETTIER-GRENIER, Richard , LOCKWOOD, Frederick , GUERET, Vincent
IPC分类号： F25J3/02 , F25J3/08
CPC分类号： F25J3/067 , B01D53/04 , B01D2256/22 , B01D2259/40001 , B01D2259/416 , C01B32/50 , F25J1/0027 , F25J1/004 , F25J1/0087 , F25J1/0095 , F25J1/0208 , F25J1/021 , F25J1/0221 , F25J3/0219 , F25J3/0223 , F25J3/0266 , F25J3/04181 , F25J3/04612 , F25J3/062 , F25J3/0625 , F25J2205/02 , F25J2205/40 , F25J2205/60 , F25J2205/70 , F25J2210/04 , F25J2210/12 , F25J2210/70 , F25J2220/80 , F25J2220/82 , F25J2220/84 , F25J2230/04 , F25J2230/30 , F25J2230/32 , F25J2230/80 , F25J2240/82 , F25J2240/90 , F25J2245/02 , F25J2245/90 , F25J2260/02 , F25J2260/80 , F25J2270/04 , F25J2270/12 , F25J2270/14 , F25J2270/60 , F25J2270/80 , F25J2270/90 , F25J2270/902 , F25J2270/904 , F25J2270/906 , F25J2290/62 , Y02C10/12 , Y02P20/125 , Y02P20/152
摘要： The invention concerns integrated method and installation using an adsorption unit (3) and a cryogenic unit (9), wherein a feeding gas containing CO2 is conveyed to an adsorption unit (3) where it is separated into a first flow enriched in CO2 (6) and a first flow depleted in CO2 (5), the first flow enriched in CO2 being conveyed to the cryogenic unit (9) where it is separated into a second flow rich in CO2 (11) and a second flow depleted in CO2 (10). The first flow enriched in CO2 (6) derived from the adsorption unit (3) is sent to homogenizing means (17), such as a storage volume or the like, for attenuating the cyclic variations of flow rate, of composition and/or of gas pressure, then subjected to at least one intermediate compression step (7) prior to its input into the cryogenic unit (9). The first flow enriched in CO2 (6) exiting the adsorption unit (3) contains between 40 and 95 %, preferably between 60 and 85 % of CO2.
摘要翻译：该方法涉及在接收（3）含有二氧化碳的40至95百分比的吸收单元中从二氧化碳（6）富集的流。二氧化碳被朝向气体均化单元（17），用于衰减的压力周期性变化发送，流量和/或气体成分和在中间压缩阶段进行（7）中的二氧化碳的在低温单元中的条目（前 9）。因此独立claimsoft被包括用于在用于从气体供给含有二氧化碳生产二氧化碳的集成安装。

58. 发明公开

EP1860393A1 Method and apparatus for the reliquefaction of a vapour 有权
标题翻译： Verfahren und Vorrichtung zurRückverflüssigungeines Gasstromes
公开(公告)号：EP1860393A1
公开(公告)日：2007-11-28
申请号：EP06352012.6
申请日：2006-05-23
申请人： Cryostar SAS
发明人： Fuchs, Vincent
IPC分类号： F25J1/02 , F17C9/00
CPC分类号： F25J1/0204 , F17C2221/033 , F17C2223/0161 , F17C2223/033 , F17C2250/0439 , F17C2265/03 , F17C2265/034 , F17C2265/037 , F17C2270/0105 , F25J1/0025 , F25J1/0045 , F25J1/005 , F25J1/0072 , F25J1/0208 , F25J1/0277 , F25J1/0288 , F25J2205/30 , F25J2220/62 , F25J2230/04 , F25J2230/08 , F25J2230/60 , F25J2245/02
摘要： Vapour boiled off from a liquefied natural gas storage tank (10) is compressed in vapour compression stages (40) and (42). The resulting compressed vapour is condensed in a condenser (46) and the condensate returned to the tank (10). The condenser (46) is cooled by means of a working fluid, for example nitrogen, flowing in a Brayton cycle (60). The Brayton cycle includes a heat exchanger (86) which removes heat of compression from the compressed natural gas vapour upstream of its passage through the condenser (46). In addition a part of the working fluid is withdrawn from a region of the Brayton cycle (60) intermediate the working fluid outlet from the condenser (46) and the working fluid inlet to the heat exchanger (86) and the withdrawn working fluid flows through another heat exchanger (88) in which it removes heat of compression from the natural gas vapour intermediate the compression stage (40) and the compression stage (42). The withdrawn working fluid is returned to the Brayton cycle (60).
摘要翻译：从液化天然气储罐（10）中蒸出的蒸汽在蒸汽压缩级（40）和（42）中被压缩。所得的压缩蒸汽在冷凝器（46）中冷凝，冷凝物返回到罐（10）。冷凝器（46）通过在布雷顿循环（60）中流动的工作流体例如氮气来冷却。布雷顿循环包括热交换器（86），该热交换器（86）从其通过冷凝器（46）的通道的压缩天然气蒸气中除去压缩热。此外，一部分工作流体从位于来自冷凝器（46）的工作流体出口之间的布雷顿循环（60）的区域和到热交换器（86）的工作流体入口的区域中被排出，并且抽出的工作流体流过另一个热交换器（88），其在压缩级（40）和压缩级（42）之间从天然气蒸汽中除去压缩热。撤回的工作流体返回到布雷顿循环（60）。

59. 发明公开

EP1776553A1 PROCESS AND APPARATUS FOR THE LIQUEFACTION OF CARBON DIOXIDE 审中-公开
标题翻译：方法和装置液化二氧化碳
公开(公告)号：EP1776553A1
公开(公告)日：2007-04-25
申请号：EP05758151.4
申请日：2005-07-14
申请人： Statoil ASA , Sinvent AS , Orkla Engineeering , Teekay Norway AS
发明人： ASPELUND, Audun , KROGSTAD, Henrik , SANDVIK, Tor, Erling
IPC分类号： F25J1/00 , F25J1/02 , F25J3/02 , F25J3/08 , C01B31/20
CPC分类号： F25J1/0042 , F25J1/0027 , F25J1/004 , F25J1/0045 , F25J1/0202 , F25J1/0208 , F25J2205/04 , F25J2205/66 , F25J2220/80 , F25J2220/82 , F25J2230/04 , F25J2230/30 , F25J2245/90 , F25J2270/90
摘要： Apparatus for carbon dioxide liquefaction comprising a flow channel for carbon dioxide passage from an inlet port to an outlet port. The channel comprises a plurality of compressors ( 2, 5, 8 ) and coolers ( 4, 7, 9, 10, 13 ) arranged in series with an expansion chamber ( 14, 15 ) in said flow channel downstream of the final compressor ( 8 ) and cooler ( 9, 10, 13 ). The apparatus also comprises a recirculation channel ( 16 ) arranged to return gaseous carbon dioxide from said expansion chamber ( 15 ) into said flow channel ( 3 ) upstream of said final compressor ( 8 ) and cooler ( 9, 10, 13 ).

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