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公开(公告)号：EP2162202A1
公开(公告)日：2010-03-17
申请号：EP08769709.0
申请日：2008-05-23
申请人： L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude , Air Liquide Medical Systems S.A.
CPC分类号： B01D53/22 , B01D53/228 , B01D63/02 , B01D71/32 , B01D2256/18 , C01B23/0042 , C01B23/0047 , C01B2210/0037 , C01B2210/0045 , C01B2210/0046 , C01B2210/0051
摘要： Xe exhaled from a patient is recovered with a polymeric membrane.
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公开(公告)号：EP3612302A1
公开(公告)日：2020-02-26
申请号：EP17835781.0
申请日：2017-12-29
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公开(公告)号：EP3612301A1
公开(公告)日：2020-02-26
申请号：EP17835780.2
申请日：2017-12-29
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公开(公告)号：EP3316992A1
公开(公告)日：2018-05-09
申请号：EP16736719.2
申请日：2016-06-28
申请人： Air Liquide Advanced Technologies U.S. LLC , L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude , Saudi Arabian Oil Company
发明人： KULKARNI, Sudhir S. , BEERS, Karl S. , BLLAGUET, Jean-Pierre R. , VAIDYA, Milind M. , DUVAL, Sebastien A.
CPC分类号： B01D63/02 , B01D53/22 , B01D53/228 , B01D63/043 , B01D63/10 , B01D2053/224 , B01D2313/04 , B01D2313/20 , B01D2313/23 , B01D2319/04 , C01B17/167
摘要： A gas separation membrane module includes a seal between a higher pressure gas and a lower pressure gas. The seal includes a compressible sealing member in between sealing surfaces. At least one of the sealing surfaces has corrosion-resistant cladding provided over either low alloy steel or high alloy steel. The cladding reduce the possibility of a seal failure due to corrosion of low alloy or high alloy steel exposed to acid gases or condensed moisture containing acid gases dissolved therein while at the same not requiring that all surfaces of the membrane module exposed to acid gases be provided with cladding.
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5.发明公开PROCÉDÉ D'ÉPURATION DE BIOGAZ PAR MEMBRANE(S) À TEMPÉRATURE NÉGATIVE 审中-公开PROCÉDÉD'ÉPURATIONDE BIOGAZ PAR MEMBRANE（S）ÀTEMPÉRATURENÉGATIVE
公开(公告)号：EP3189123A1
公开(公告)日：2017-07-12
申请号：EP15759897.0
申请日：2015-08-12
发明人： BIGEARD, Sarah , GARNAUD, Delphine , HASSE, David J. , KULKARNI, Sudhir S. , SANDERS, Edgar , ZICK, Golo
CPC分类号： B01D53/229 , B01D53/002 , B01D53/226 , B01D53/227 , B01D53/26 , B01D53/265 , B01D2256/245 , B01D2257/504 , B01D2257/80 , B01D2258/05 , C10L3/104 , C10L3/106 , C10L2290/06 , C10L2290/08 , C10L2290/548 , F25J3/08 , F25J2205/80 , F25J2215/60 , F25J2220/66 , F25J2220/68 , F25J2230/30 , F25J2270/08 , Y02C10/10
摘要： The invention relates to a method for membrane permeation of a gas flow including methane and carbon dioxide, wherein said gas flow is cooled to a temperature of 0°C to -60°C before being fed into a membrane separation unit.
摘要翻译： 本发明涉及用于包括甲烷和二氧化碳的气流的膜渗透的方法，其中所述气流在供入膜分离单元之前被冷却至0℃至-60℃的温度。
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公开(公告)号：EP2624935A1
公开(公告)日：2013-08-14
申请号：EP11770978.2
申请日：2011-10-06
CPC分类号： B01D53/229 , B01D53/1475 , B01D53/226 , B01D71/64 , B01D2257/504 , B01D2311/04 , B01D2311/06 , B01D2311/08 , B01D2311/103 , B01D2311/106 , B01D2311/13 , B01D2311/25 , B01D2311/2669 , B01D2311/2673 , B01D2317/022 , C10L3/104 , F25J3/0209 , F25J3/0233 , F25J3/0266 , F25J3/029 , F25J3/061 , F25J3/0635 , F25J3/067 , F25J3/069 , F25J2200/02 , F25J2200/30 , F25J2205/04 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2215/04 , F25J2220/82 , F25J2230/30 , F25J2235/80 , F25J2245/02 , Y02C10/06 , Y02C10/10 , Y02C10/12 , Y02E50/346 , Y10S62/928
摘要： A process for efficiently removing carbon dioxide from a hydrocarbon containing feed stream utilizing a membrane separation unit in conjunction with a heat exchanger and a carbon dioxide separation unit wherein the streams obtained in the carbon dioxide separation unit are utilized to provide the cooling effect in the heat exchanger.
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7.发明公开PROCESS AND APPARATUS FOR THE SEPARATION OF A STREAM CONTAINING CARBON DIOXIDE, WATER AND AT LEAST ONE LIGHT IMPURITY INCLUDING A SEPARATION STEP AT SUBAMBIENT TEMPERATURE 审中-公开方法和装置分裂的流程从二氧化碳，水和至少一种光污染，包括分步在温度在室温下
公开(公告)号：EP2872841A1
公开(公告)日：2015-05-20
申请号：EP13736558.1
申请日：2013-07-11
发明人： DARDE, Arthur , DUBETTIER-GRENIER, Richard , HASSE, David J. , KULKARNI, Sudhir S. , LECLERC, Mathieu , TERRIEN, Paul
CPC分类号： B01D53/229 , B01D53/002 , B01D53/22 , B01D53/261 , B01D2256/22 , B01D2258/0283 , B01D2259/40001 , B01D2259/40086 , F23J15/04 , F23J2215/50 , F23J2219/40 , F25J3/0223 , F25J3/0266 , F25J3/0625 , F25J3/067 , F25J2200/02 , F25J2200/40 , F25J2200/70 , F25J2205/04 , F25J2205/40 , F25J2205/66 , F25J2205/70 , F25J2205/80 , F25J2210/04 , F25J2210/70 , F25J2220/80 , F25J2220/82 , F25J2230/30 , F28C3/08 , Y02C10/12
摘要： In a process for the separation of a stream containing carbon dioxide, water and at least one light impurity including a separation step at subambient temperature, the feed stream (1,3) is compressed in a compressor (C1, C2, C3) comprising at least two stages to form a compressed feed stream (7), the compressed feed stream is purified in an adsorption unit (A1,A2) to remove water and form a dried compressed stream (9, 11), the dried compressed stream or a stream derived therefrom is cooled to a subambient temperature and separated by partial condensation and/or distillation in a separation apparatus (19, 31), liquid enriched in carbon dioxide (37, 43) is removed from the separation apparatus, the adsorption unit is regenerated using a regeneration gas (25, 53) and the regeneration gas is formed by separating, by permeation in a permeation unit (21, 51), the dried compressed stream (9) or a gas (19) derived therefrom, the permeate of the permeation unit constituting the regeneration gas.
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公开(公告)号：EP2872841B1
公开(公告)日：2018-10-03
申请号：EP13736558.1
申请日：2013-07-11
发明人： DARDE, Arthur , DUBETTIER-GRENIER, Richard , HASSE, David J. , KULKARNI, Sudhir S. , LECLERC, Mathieu , TERRIEN, Paul
CPC分类号： B01D53/229 , B01D53/002 , B01D53/22 , B01D53/261 , B01D2256/22 , B01D2258/0283 , B01D2259/40001 , B01D2259/40086 , F23J15/04 , F23J2215/50 , F23J2219/40 , F25J3/0223 , F25J3/0266 , F25J3/0625 , F25J3/067 , F25J2200/02 , F25J2200/40 , F25J2200/70 , F25J2205/04 , F25J2205/40 , F25J2205/66 , F25J2205/70 , F25J2205/80 , F25J2210/04 , F25J2210/70 , F25J2220/80 , F25J2220/82 , F25J2230/30 , F28C3/08 , Y02C10/12
摘要： In a process for the separation of a stream containing carbon dioxide, water and at least one light impurity including a separation step at subambient temperature, the feed stream (1,3) is compressed in a compressor (C1, C2, C3) comprising at least two stages to form a compressed feed stream (7), the compressed feed stream is purified in an adsorption unit (A1,A2) to remove water and form a dried compressed stream (9, 11), the dried compressed stream or a stream derived therefrom is cooled to a subambient temperature and separated by partial condensation and/or distillation in a separation apparatus (19, 31), liquid enriched in carbon dioxide (37, 43) is removed from the separation apparatus, the adsorption unit is regenerated using a regeneration gas (25, 53) and the regeneration gas is formed by separating, by permeation in a permeation unit (21, 51), the dried compressed stream (9) or a gas (19) derived therefrom, the permeate of the permeation unit constituting the regeneration gas.
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公开(公告)号：EP3145606B1
公开(公告)日：2018-08-01
申请号：EP15716304.9
申请日：2015-03-27
发明人： BEASSE, Gregoire , KULKARNI, Sudhir S. , KOSURI, Madhava R. , LECLERC, Mathieu , BOURHY-WEBER, Claire
CPC分类号： F25J3/0266 , B01D3/00 , B01D3/145 , B01D19/0031 , B01D53/002 , B01D53/22 , B01D53/228 , B01D53/229 , B01D61/362 , B01D71/48 , B01D71/52 , B01D71/56 , B01D71/70 , B01D71/80 , B01D2256/22 , B01D2257/404 , B01D2259/4516 , B01D2311/04 , B01D2311/08 , B01D2311/13 , B01D2311/2669 , B01D2323/30 , C01B32/50 , F25J2200/02 , F25J2200/04 , F25J2200/40 , F25J2200/70 , F25J2205/02 , F25J2205/30 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2210/70 , F25J2215/80 , F25J2220/82 , F25J2220/84 , F25J2230/30 , F25J2230/80 , F25J2235/80 , F25J2245/02 , F25J2270/02 , F25J2270/04 , Y02C10/12 , Y02P20/145 , Y02P20/152 , Y02P70/34
摘要： A process for separating carbon dioxide from a fluid containing carbon dioxide, NO2, and at least one of oxygen, argon, and nitrogen comprises the steps of separating at least part of the fluid into a carbon dioxide enriched stream, a carbon dioxide depleted stream comprising CO2 and at least one of oxygen, argon, and nitrogen and a NO2 enriched stream and recycling said NO2 enriched stream upstream of the separation step.
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公开(公告)号：EP3316991A1
公开(公告)日：2018-05-09
申请号：EP16736355.5
申请日：2016-06-28
申请人： Air Liquide Advanced Technologies U.S. LLC , L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude , Saudi Arabian Oil Company
发明人： KULKARNI, Sudhir S. , BEERS, Karl S. , BLLAGUET, Jean-Pierre R. , VAIDYA, Milind M. , DUVAL, Sebastien A.
CPC分类号： B01D63/02 , B01D53/22 , B01D53/228 , B01D63/043 , B01D63/10 , B01D2053/224 , B01D2313/04 , B01D2313/20 , B01D2313/23 , B01D2319/04 , C01B17/167
摘要： A gas separation membrane module includes a seal between a higher pressure gas and a lower pressure gas. The seal includes a compressible sealing member in between sealing surfaces. At least one of the sealing surfaces has corrosion-resistant cladding provided over either low alloy steel or high alloy steel. The cladding reduce the possibility of a seal failure due to corrosion of low alloy or high alloy steel exposed to acid gases or condensed moisture containing acid gases dissolved therein while at the same not requiring that all surfaces of the membrane module exposed to acid gases be provided with cladding.
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