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公开(公告)号：EP2715260B1
公开(公告)日：2020-08-19
申请号：EP12731086.0
申请日：2012-05-29
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公开(公告)号：EP2619455B1
公开(公告)日：2015-01-14
申请号：EP11773062.2
申请日：2011-09-12
CPC分类号： B01D53/00 , B01D53/002 , B01D2257/504 , F04B13/02 , F04B15/08 , F04B2015/0818 , F25J3/0266 , F25J2200/02 , F25J2200/70 , F25J2205/04 , F25J2210/70 , F25J2220/82 , F25J2230/24 , F25J2230/32 , F25J2230/80 , F25J2240/90 , F25J2245/02 , F25J2260/80 , F25J2270/02 , F25J2280/20 , Y02C10/12
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公开(公告)号：EP2761035A1
公开(公告)日：2014-08-06
申请号：EP12769635.9
申请日：2012-09-28
CPC分类号： F27D17/002 , C21B5/06 , C21B7/002 , C21B13/02 , C21B2100/04 , C21B2100/24 , C21B2100/282 , C21B2100/44 , C21B2100/60 , C21B2100/62 , C21C2100/02 , C21C2100/04 , F25J3/0223 , F25J3/0252 , F25J3/0261 , F25J3/0266 , F25J2205/40 , F25J2205/80 , F25J2210/04 , F25J2230/30 , F25J2245/02 , Y02C10/12 , Y02P10/122 , Y02P10/126 , Y02P10/128 , Y02P10/132 , Y02P10/216 , Y02P10/265 , Y02P10/283
摘要： Ironmaking method and installation with recirculation of exhaust gas as a reduction gas and whereby part of the exhaust gas is purged upstream and/or downstream of a CO/CO 2 separation unit, said purged exhaust gas being subjected to a water gas shift reaction for H 2 generation.
摘要翻译： 炼铁方法和通过废气再循环作为还原气体并且由此部分排气在CO / CO 2分离单元的上游和/或下游被清除的装置，所述排出的废气经受水煤气变换反应H 2代。
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4.发明公开PROCEDE ET APPAREIL DE LIQUEFACTION D'UN GAZ OU REFROIDISSEMENT D'UN GAZ D'ALIMENTATION A PRESSION SUPERCRITIQUE 审中-公开方法和装置气体液体或用于冷却超临界压力的气体USE
公开(公告)号：EP2697583A2
公开(公告)日：2014-02-19
申请号：EP12722405.3
申请日：2012-04-12
发明人： DARDE, Arthur , TRAVERSAC, Xavier
CPC分类号： F25J1/00 , F25J1/0027 , F25J1/004 , F25J1/0042 , F25J1/0045 , F25J1/0202 , F25J1/0262 , F25J1/0263 , F25J1/0264 , F25J3/067 , F25J2210/70 , F25J2220/82 , F25J2230/30 , F25J2230/42 , F25J2245/02 , F25J2270/02 , F25J2270/80 , Y02C10/12
摘要： The invention relates to a method for liquefying a feed gas or cooling a feed gas at supercritical pressure, in which the feed gas mixed with a cycle gas is condensed or cooled in order to form a supercritical gas or liquid at the first pressure, the liquid at the first pressure is cooled in a first heat exchanger (E2), the cooled liquid is removed from the first exchanger and expanded up to a second pressure that is lower than the first pressure in order to form an expanded flow, at least one portion of the expanded flow is cooled in a second heat exchanger, the expanded flow is removed from the second heat exchanger (E2), said flow is split into at least two portions, including a first portion and a second portion, the first portion of the expanded flow constituting the liquefied product, the second portion and preferably a third portion being vaporised in the second heat exchanger and the thus-formed at least one cycle gas is then mixed with the feed gas and compressed in a compressor, before or after being mixed with the feed gas.
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5.发明授权PROCÉDÉ ET APPAREIL DE REFROIDISSEMENT D'UN DÉBIT CONTENANT AU MOINS 35% DE DIOXYDE DE CARBONE ET DU MERCURE 有权PROCÉDÉET APPAREIL DE REFROIDISSEMENT D'UNDÉBITCONTENTANT AU MOINS 35％DE DIOXYDE DE CARBONE ET DU MERCURE
公开(公告)号：EP2872298B1
公开(公告)日：2017-08-30
申请号：EP13747447.4
申请日：2013-07-12
发明人： BRIGLIA, Alain , DARDE, Arthur , GRANADOS, Ludovic , LECLERC, Mathieu , LOCKWOOD, Frederick , TRAVERSAC, Xavier
IPC分类号： B25J1/00
CPC分类号： B01D5/0075 , F25J3/0223 , F25J3/0266 , F25J3/0295 , F25J5/002 , F25J5/005 , F25J2200/02 , F25J2200/70 , F25J2205/04 , F25J2205/20 , F25J2205/40 , F25J2205/60 , F25J2205/66 , F25J2210/04 , F25J2210/70 , F25J2215/04 , F25J2220/80 , F25J2220/82 , F25J2220/84 , F25J2230/30 , F25J2230/32 , F25J2230/80 , F25J2235/80 , F25J2250/02 , F25J2280/20 , F25J2280/40 , F25J2290/44 , F25J2290/90 , Y02C10/12
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公开(公告)号：EP2872839A1
公开(公告)日：2015-05-20
申请号：EP13739640.4
申请日：2013-07-12
发明人： DARDE, Arthur , DUBETTIER-GRENIER, Richard , LOCKWOOD, Frederick , TERRIEN, Paul , TRANIER, Jean-Pierre , TRAVERSAC, Xavier
CPC分类号： F25J1/0027 , C01B32/55 , F25J1/004 , F25J1/0045 , F25J1/0202 , F25J1/0245 , F25J3/0625 , F25J3/067 , F25J2205/20 , F25J2210/06 , F25J2210/70 , F25J2220/82 , F25J2230/80 , F25J2235/80 , F25J2245/02 , F25J2270/02 , F25J2270/08 , F25J2270/80 , F25J2280/02 , F25J2290/62 , Y02C10/12 , Y02P20/152
摘要： In a process for storing liquid rich in carbon dioxide in solid form and subsequently releasing liquid containing mainly carbon dioxide, a solid (13) containing mainly carbon dioxide is formed from at least part of the liquid (1) with or without using indirect heat exchange means, storing the solid containing mainly carbon dioxide ,the process steps including subsequently causing at least part of the solid containing mainly carbon dioxide to melt forming a liquid containing mainly carbon dioxide, by direct contact with an auxiliary gas (11) rich in carbon dioxide, wherein the auxiliary gas is at least partially liquefied to form liquid containing mainly carbon dioxide by heat exchange with the melting solid and removing at least part of the liquid (7) containing mainly carbon dioxide.
摘要翻译： 在用于在固体形式的二氧化碳储存液体丰富和随后释放主要含有二氧化碳，固体（13）主要含有二氧化碳从该液体（1）使用或不使用间接热交换的至少一部分上形成液体的方法 手段，存储所述固体主要含有二氧化碳，则处理步骤，包括用在富含二氧化碳的辅助气体（11）随后使固体主要含二氧化碳的至少一部分以熔化形成主要含有二氧化碳的液体，通过直接接触 ，worin辅助气体被至少部分液化，以形成液体通过与固体熔化热交换主要含有二氧化碳和除去（7）主要含有二氧化碳的液体的至少一部分。
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7.发明公开PROCÉDÉ ET APPAREIL DE SÉPARATION D'UN GAZ RICHE EN DIOXYDE DE CARBONE PAR DISTILLATION 审中-公开方法及器具的富含二氧化碳的气体通过蒸馏分离
公开(公告)号：EP2773442A1
公开(公告)日：2014-09-10
申请号：EP12787799.1
申请日：2012-10-23
发明人： DARDE, Arthur , TRAVERSAC, Xavier
CPC分类号： F25J1/0027 , B01D53/002 , B01D2257/504 , F25J3/0266 , F25J2200/02 , F25J2200/40 , F25J2200/70 , F25J2210/70 , F25J2215/04 , F25J2220/82 , F25J2230/04 , F25J2230/80 , F25J2250/30 , F25J2270/04 , F25J2270/80 , Y02C10/12
摘要： In a process for separating a gas rich in carbon dioxide by distillation, the gas rich in carbon dioxide is cooled in a heat exchanger (3) and is sent to a distillation column (5), a gas (6) depleted in carbon dioxide is withdrawn from the top of the column and a liquid (7) enriched in carbon dioxide is withdrawn from the bottom of the column, a gas enriched in carbon dioxide is compressed in a compressor (17) down to a first pressure and at least one portion of the gas enriched in carbon dioxide originating from the compressor is expanded from the first pressure to a second pressure lower than the first pressure, for example the pressure of the column, and the expanded gas is used to heat the bottom of the column.
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公开(公告)号：EP2552827A1
公开(公告)日：2013-02-06
申请号：EP11714362.8
申请日：2011-03-16
发明人： DARDE, Arthur , VALENTIN, Solène , COURT, Philippe , TRANIER, Jean-Pierre , TRAVERSAC, Xavier , TERRIEN, Paul
CPC分类号： C01B3/38 , C01B3/48 , C01B3/56 , C01B2203/0233 , C01B2203/0288 , C01B2203/043 , C01B2203/046 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , Y02C10/04 , Y02P20/129 , Y02P30/30
摘要： The present invention relates to a method for producing hydrogen, with reduced carbon dioxide emissions, from a hydrocarbon mixture. In said method, the hydrocarbon mixture is reformed (2) so as to produce a synthetic gas that is cooled (4) then treated in a (HT) shift reactor (6) so as to be enriched with H
2 and CO
2 . Optionally dried (10), said mixture is treated in a PSA hydrogen purification unit (12) in order to produce hydrogen. The residue is treated by means of partial condensation with a view to capturing CO
4 (20) before said residue is sent as fuel to reforming (28). According to the invention, the CO
2 emissions in the fumes are reduced by converting the carbon monoxide, from the synthetic gas that has not reacted during the high-temperature shift reaction, into carbon dioxide via a second shift reaction (23) downstream from the PSA. The CO
2 emissions are moreover reduced by capturing the thus-generated additional CO
2 (27) prior to sending it as fuel.-
9.发明授权PROCÉDÉ ET APPAREIL DE SÉPARATION D'UN MÉLANGE CONTENANT DU DIOXYDE DE CARBONE PAR DISTILLATION 有权PROCÉDÉET APPAREIL DESÉPARATIOND'UNMÉLANGE现在DU DUOXYDE DE CARBONE PAR蒸馏
公开(公告)号：EP2932177B1
公开(公告)日：2017-09-06
申请号：EP13711091.2
申请日：2013-03-05
CPC分类号： F25J1/0027 , F23L7/007 , F25J3/0223 , F25J3/0252 , F25J3/0266 , F25J2200/02 , F25J2200/04 , F25J2200/40 , F25J2200/70 , F25J2200/78 , F25J2205/04 , F25J2205/30 , F25J2210/04 , F25J2210/70 , F25J2220/82 , F25J2220/84 , F25J2230/30 , F25J2235/80 , F25J2240/90 , F25J2245/02 , F25J2270/02 , F25J2270/80 , Y02C10/12
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10.发明授权PROCEDE DE PRODUCTION D'UN FLUIDE ENRICHI EN DIOXYDE DE CARBONE A PARTIR D'UN GAZ RESIDUAIRE D'UNE UNITE SIDERURGIQUE 有权过程流程ENRICHI EN DIOXYDE DE CARBONE A PARTIR D'UN GAZ RESIDUAIRE D'UNE UNITE SIDERURGIQUE
公开(公告)号：EP2648825B1
公开(公告)日：2017-08-02
申请号：EP11801803.5
申请日：2011-12-01
发明人： BRIGLIA, Alain , DE CAYEUX, Olivier , DUBETTIER-GRENIER, Richard , GUILLARD, Alain , TRAVERSAC, Xavier , SZAMLEWSKI, Christophe
IPC分类号： B01D53/047 , C21B5/06 , C21B7/00 , B01D53/00
CPC分类号： B01D53/047 , B01D53/002 , B01D53/0407 , B01D53/62 , B01D53/77 , B01D2253/102 , B01D2253/108 , B01D2253/20 , B01D2256/20 , B01D2257/504 , B01D2258/025 , B01D2259/40001 , B01D2259/416 , C01B32/50 , C21B5/06 , C21B2100/02 , C21B2100/04 , C21B2100/26 , C21B2100/282 , C21B2100/60 , F25J3/0223 , F25J3/0261 , F25J3/0266 , F25J3/0295 , F25J2205/40 , F25J2205/60 , F25J2205/64 , F25J2210/04 , F25J2215/04 , F25J2220/82 , F25J2230/30 , F25J2240/40 , F25J2245/02 , F25J2280/02 , F25J2290/62 , Y02C10/08 , Y02C10/12 , Y02P10/122 , Y02P10/126 , Y02P10/128 , Y02P10/132 , Y02P10/265 , Y02P10/283 , Y02P20/152
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