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1.发明公开PROCEDE DE CAPTURE DU DIOXYDE DE CARBONE PAR CRYO-CONDENSATION 审中-公开KOHLENDIOXIDGEWINNUNGSVERFAHREN UNTER VERWENDUNG VON KRYOKONDENSATION
公开(公告)号：EP2379968A1
公开(公告)日：2011-10-26
申请号：EP09803847.4
申请日：2009-12-14
CPC分类号： B01D53/002 , B01D2257/504
摘要： Disclosed is a method for producing at least one gas having a low CO
2 concentration and one or more primary fluids having a high CO
2 concentration from a fluid which is to be treated and contains CO
2 and at least one compound that is more volatile than CO
2 .
Said method comprises the following steps: a) the fluid to be treated is subjected to a first cooling process using heat exchange without the fluid undergoing a change of state; b) at least some of the fluid to be treated and cooled in step a) is cooled a second time such that a solid is obtained which contains mainly CO
2 and at least the gas having a low CO
2 concentration; and c) a step in which at least some of said solid is liquefied such that the one or more primary fluids having a high CO
2 concentration are obtained. The disclosed method is characterized in that at least part of the first cooling process in step a) is carried out by heating at least some of the one or more primary fluids having a high CO
2 concentration.摘要翻译： 本发明涉及一种在流体中捕获二氧化碳的方法，其包含至少一种比二氧化碳CO 2更易挥发的化合物，例如甲烷CH 4，氧气O 2，氩气Ar，氮气N 2，一氧化碳CO，氦He和/或氢气 H2。
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2.发明公开PROCÉDÉ DE CAPTURE DE C02 PAR CRYO-CONDENSATION SOLIDE DANS UNE TURBINE 审中-公开PROCÉDÉDE CAPTURE DE CO 2 PAR冷凝固体齿轮涡轮机
公开(公告)号：EP2379199A1
公开(公告)日：2011-10-26
申请号：EP09803854.0
申请日：2009-12-14
CPC分类号： B01D53/002 , B01D2257/504 , C10L3/10 , F23J2900/15061 , F25J3/0219 , F25J3/0223 , F25J3/0252 , F25J3/0257 , F25J3/0261 , F25J3/0266 , F25J3/0295 , F25J3/04533 , F25J3/04539 , F25J3/04545 , F25J3/04557 , F25J3/04563 , F25J3/04612 , F25J3/04836 , F25J3/0625 , F25J3/0655 , F25J3/067 , F25J3/0695 , F25J2205/04 , F25J2205/10 , F25J2205/20 , F25J2205/32 , F25J2205/34 , F25J2210/04 , F25J2210/14 , F25J2210/70 , F25J2220/80 , F25J2230/08 , F25J2230/30 , F25J2230/32 , F25J2235/80 , F25J2240/02 , F25J2245/42 , F25J2260/44 , F25J2270/02 , F25J2270/04 , F25J2270/06 , F25J2270/14 , F25J2270/58 , F25J2270/80 , F25J2270/88 , F25J2290/42 , Y02C10/12
摘要： The invention relates to a method for producing at least one gas lean in CO
2 and one or more primary fluids rich in CO
2 from a fluid to be processed that contains CO
2 and at least one compound more volatile than CO
2 , implementing: a) a first cooling of the fluid to be processed by heat exchange without state modification; b) a second cooling of a at least a portion of the fluid to be processed cooled during step a) in order to obtain at least one solid mainly containing CO
2 and at least one gas lean in CO
2 ; and c) a step including the liquefaction and/or sublimation of at least a portion of said solid in order to obtain said one or more CO
2 -rich primary fluids; wherein the method is characterised in that step b) is carried out in at least one expansion turbine, the solid being formed inside said turbine.摘要翻译： 本发明涉及一种用于从含有CO 2和至少一种比CO 2更易挥发的化合物的待处理流体中产生至少一种CO 2贫气和一种或多种富含CO 2的主流体的方法，其实施：a ）通过热交换对待处理流体进行第一次冷却而不进行状态修改; b）对在步骤a）期间冷却的至少一部分待处理流体进行第二次冷却，以获得至少一种主要含有CO 2和至少一种贫CO 2气体的固体; 和c）包括至少一部分所述固体液化和/或升华以获得所述一种或多种富CO 2主流体的步骤; 其中该方法的特征在于，步骤b）在至少一个膨胀涡轮机中进行，该固体形成在所述涡轮机内。
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公开(公告)号：EP2379971A1
公开(公告)日：2011-10-26
申请号：EP09803851.6
申请日：2009-12-14
CPC分类号： B01D53/002 , B01D2257/504 , C10L3/10 , F23J2900/15061 , F25J3/0219 , F25J3/0223 , F25J3/0252 , F25J3/0257 , F25J3/0261 , F25J3/0266 , F25J3/0295 , F25J3/04533 , F25J3/04539 , F25J3/04545 , F25J3/04557 , F25J3/04563 , F25J3/04612 , F25J3/04836 , F25J3/0625 , F25J3/0655 , F25J3/067 , F25J3/0695 , F25J2205/04 , F25J2205/10 , F25J2205/20 , F25J2205/32 , F25J2205/34 , F25J2210/04 , F25J2210/14 , F25J2210/70 , F25J2220/80 , F25J2230/08 , F25J2230/30 , F25J2230/32 , F25J2235/80 , F25J2240/02 , F25J2245/42 , F25J2260/44 , F25J2270/02 , F25J2270/04 , F25J2270/06 , F25J2270/14 , F25J2270/58 , F25J2270/80 , F25J2270/88 , F25J2290/42 , Y02C10/12
摘要： Disclosed is a method for producing chilled water, at least one gas having a low CO
2 concentration, and one or more primary fluids having a high CO
2 concentration from a fluid which is to be treated and contains CO
2 and at least one compound that is more volatile than CO
2 , and from industrial water. Said method comprises the following steps: a) the fluid to be treated is separated into at least the gas having a low CO
2 concentration (44) and the primary fluids having a high CO
2 concentration; and b) the industrial water is chilled by exchanging heat with a fraction of the gas having a low CO
2 concentration, said fraction not amounting to zero, such that the chilled water is obtained. The disclosed method is characterized in that the heat exchange in step b) takes place in a direct-contact tower.-
公开(公告)号：EP2379971B1
公开(公告)日：2014-02-12
申请号：EP09803851.6
申请日：2009-12-14
CPC分类号： B01D53/002 , B01D2257/504 , C10L3/10 , F23J2900/15061 , F25J3/0219 , F25J3/0223 , F25J3/0252 , F25J3/0257 , F25J3/0261 , F25J3/0266 , F25J3/0295 , F25J3/04533 , F25J3/04539 , F25J3/04545 , F25J3/04557 , F25J3/04563 , F25J3/04612 , F25J3/04836 , F25J3/0625 , F25J3/0655 , F25J3/067 , F25J3/0695 , F25J2205/04 , F25J2205/10 , F25J2205/20 , F25J2205/32 , F25J2205/34 , F25J2210/04 , F25J2210/14 , F25J2210/70 , F25J2220/80 , F25J2230/08 , F25J2230/30 , F25J2230/32 , F25J2235/80 , F25J2240/02 , F25J2245/42 , F25J2260/44 , F25J2270/02 , F25J2270/04 , F25J2270/06 , F25J2270/14 , F25J2270/58 , F25J2270/80 , F25J2270/88 , F25J2290/42 , Y02C10/12
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5.发明公开PROCÉDÉ DE CAPTURE DU CO2 PAR CRYO-CONDENSATION 审中-公开VERFAHREN ZUR CO2-RÜCKGEWINNUNGMITTELS KRYOKONDENSATION
公开(公告)号：EP2379970A1
公开(公告)日：2011-10-26
申请号：EP09803850.8
申请日：2009-12-14
CPC分类号： B01D53/002 , B01D2257/504 , C10L3/10 , F23J2900/15061 , F25J3/0219 , F25J3/0223 , F25J3/0252 , F25J3/0257 , F25J3/0261 , F25J3/0266 , F25J3/0295 , F25J3/04533 , F25J3/04539 , F25J3/04545 , F25J3/04557 , F25J3/04563 , F25J3/04612 , F25J3/04836 , F25J3/0625 , F25J3/0655 , F25J3/067 , F25J3/0695 , F25J2205/04 , F25J2205/10 , F25J2205/20 , F25J2205/32 , F25J2205/34 , F25J2210/04 , F25J2210/14 , F25J2210/70 , F25J2220/80 , F25J2230/08 , F25J2230/30 , F25J2230/32 , F25J2235/80 , F25J2240/02 , F25J2245/42 , F25J2260/44 , F25J2270/02 , F25J2270/04 , F25J2270/06 , F25J2270/14 , F25J2270/58 , F25J2270/80 , F25J2270/88 , F25J2290/42 , Y02C10/12
摘要： Disclosed is a method for producing at least one gas having a low CO
2 concentration and one or more primary fluids having a high CO
2 concentration from a fluid which is to be treated and contains CO
2 and at least one compound that is more volatile than CO
2 . Said method comprises the following steps: a) the fluid to be treated is subjected to a first cooling process using heat exchange without the fluid undergoing a change of state; b) at least some of the fluid to be treated and cooled in step a) is cooled a second time such that a solid is obtained which contains mainly CO
2 and at least the gas having a low CO
2 concentration; and c) a step in which at least some of said solid is liquefied and/or sublimed such that the one or more primary fluids having a high CO
2 concentration are obtained. The disclosed method is characterized in that at least some of the cold required for the first cooling process and/or the second cooling process is supplied by one or more refrigeration cycles, each of which includes at least one quasi isentropic expansion of a gas.摘要翻译： 本发明涉及一种在流体中捕获二氧化碳的方法，其包含至少一种比二氧化碳CO 2更易挥发的化合物，例如甲烷CH 4，氧气O 2，氩气Ar，氮气N 2，一氧化碳CO，氦He和/或氢气 H2。
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公开(公告)号：EP2379969A1
公开(公告)日：2011-10-26
申请号：EP09803848.2
申请日：2009-12-14
发明人： JALLAIS, Simon , LOCKWOOD, Frédérick , TRANIER, Jean-Pierre , WAGNER, Marc , WEBER, Claire , RAVEX, Alain
CPC分类号： B01D53/002 , B01D2257/504
摘要： The invention relates to a method for producing at least one gas lean in CO
2 and one or more fluids rich in CO
2 from a fluid to be processed including CO
2 and at least one compound more volatile than CO
2 , wherein said method comprises: a) cooling, by cryocondensation, at least a portion of said fluid to be processed in at least one container so as to obtain at least one solid mainly containing CO
2 and at least said gas lean in CO
2 ; b) extracting at least a portion of the solid produced during step a) from said container; and c) liquefying and/or subliming a at least a portion of said solid extract during step b) in order to obtain one or more fluids rich in CO
2 ; characterised in that the time intervals during which step b) is implemented are included in the time intervals during which said step a) is implemented.
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