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公开(公告)号：EP3378551A1
公开(公告)日：2018-09-26
申请号：EP17192157.0
申请日：2017-09-20
IPC分类号： B01D53/04 , B01D53/047 , B01D53/26 , B01D53/28 , F24F3/14
CPC分类号： B01J20/18 , B01D53/04 , B01D53/0407 , B01D53/047 , B01D53/261 , B01D53/263 , B01D53/28 , B01D2253/108 , B01D2253/304 , B01D2253/308 , B01D2253/3425 , B01D2257/80 , B01J20/28004 , B01J20/28045 , B01J20/28085 , F24F3/1411
摘要： A gas separator of an arrangement includes: a honeycomb base having a plurality of through holes juxtaposed and made apart from one another by partition walls extending between a first face and a second face; and porous aggregates of inorganic material particles filled in the through holes and each having a third face and a fourth face. The porous aggregates each include pores passing from the third face to the fourth face among the inorganic material particles, and air permeability of the porous aggregates from the third faces to the fourth faces is not less than 1 x 10 -14 m 2 nor more than 1 x 10 -11 m 2 .
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公开(公告)号：EP3377194A1
公开(公告)日：2018-09-26
申请号：EP16806352.7
申请日：2016-11-15
发明人： RAVIKOVITCH, Peter I. , SHOLL, David , KAMAKOTI, Preeti , PAUR, Charanjit , STROHMAIER, Karl G. , FANG, Hanjun , KULKARNI, Ambarish R. , AWATI, Rohan V.
IPC分类号： B01D53/04 , B01D53/047 , B01D53/62
CPC分类号： B01D53/0462 , B01D53/02 , B01D53/047 , B01D53/0476 , B01D2253/1085 , B01D2253/34 , B01D2253/3425 , B01D2257/504 , B01J20/18 , B01J20/3491 , C10L3/104 , C10L2290/12 , C10L2290/542 , Y02C10/08
摘要： Methods of designing zeolite materials for adsorption of CO2. Zeolite materials and processes for CO2 adsorption using zeolite materials.
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3.发明公开
公开(公告)号：EP3344370A1
公开(公告)日：2018-07-11
申请号：EP16757411.0
申请日：2016-08-10
发明人： MARSHALL, Bennett, D. , KELLEY, Bruce, T. , NAGAVARAPU, Ananda, K. , DECKMAN, Harry, W. , JOHNSON, Robert, A. , RAMKUMAR, Shwetha , OELFKE, Russell, H.
IPC分类号： B01D53/04 , B01D53/047 , B01D53/26 , C10L3/10
CPC分类号： B01D53/0423 , B01D53/0462 , B01D53/0473 , B01D53/261 , B01D2253/3425 , B01D2256/245 , B01D2257/304 , B01D2257/504 , B01D2257/80 , B01D2259/40009 , B01D2259/40045 , B01D2259/40054 , C10L3/104 , C10L3/106 , C10L2290/543 , Y02C10/08
摘要： Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to treat the pipeline quality natural gas to form a stream that complies with liquefied natural gas (LNG) specifications. The process may involve a combined TSA and PSA process, which is utilized to remove contaminants from the feed stream.
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公开(公告)号：EP3104955A4
公开(公告)日：2017-12-27
申请号：EP15749024
申请日：2015-02-12
申请人： ENVERID SYSTEMS INC
发明人： MEIRAV UDI , BIRAN ISRAEL , MERUHAM ASAEL , JACOBI JACOB
CPC分类号： B01D53/0415 , B01D53/0446 , B01D53/0462 , B01D2253/102 , B01D2253/116 , B01D2253/20 , B01D2253/304 , B01D2253/34 , B01D2253/3425 , B01D2257/11 , B01D2257/302 , B01D2257/404 , B01D2257/502 , B01D2257/504 , B01D2257/708 , B01D2257/91 , B01D2258/06 , B01D2259/40086 , B01D2259/40088 , B01D2259/4009 , B01D2259/4508 , B01D2259/4566 , F24F13/28 , Y02C10/08
摘要： A regenerable air scrubbing system comprises of an air flow assembly with replaceable cartridges arranged in a parallel orientation and designed for easy insertion and removal of the cartridges. The cartridge design enhances the contact area, reduces the pressure drop, and readily allows the design of similar assemblies with different airflow throughputs using the same cartridge, while facilitating easy replacement of the sorbent in the field. The cartridge can be partitioned into smaller compartments, improving the mechanical properties of the cartridge and the uniformity of the sorbent distribution.
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公开(公告)号：EP3225308A1
公开(公告)日：2017-10-04
申请号：EP17163127.8
申请日：2017-03-27
申请人： NGK Insulators, Ltd.
发明人： YAMAZAKI, Satoshi , HAYASE, Toru , MORIMOTO, Kenji
IPC分类号： B01J35/04 , B01J29/80 , B01J29/08 , B01J29/14 , B01J29/40 , B01J29/46 , B01J29/70 , B01J29/76 , B01J35/02 , B01J35/10 , B01J37/00 , B01D53/86
CPC分类号： B01J29/85 , B01D53/02 , B01D53/0407 , B01D53/9413 , B01D2253/108 , B01D2253/311 , B01D2253/3425 , B01D2255/502 , B01D2255/504 , B01D2255/91 , B01D2255/912 , B01D2257/404 , B01D2257/702 , B01J21/04 , B01J21/12 , B01J29/084 , B01J29/146 , B01J29/40 , B01J29/46 , B01J29/7007 , B01J29/7015 , B01J29/7215 , B01J29/723 , B01J29/7615 , B01J29/763 , B01J29/80 , B01J35/0006 , B01J35/023 , B01J35/04 , B01J35/1033 , B01J35/1052 , B01J35/1095 , B01J37/0018 , B01J37/04 , B01J37/082 , B01J37/30 , B01J2229/183 , B01J2229/186 , B01J2229/42 , B28B3/20 , B28B11/243 , B28B2003/203
摘要： The manufacturing method includes a step of mixing a coarse particle zeolite, a fine particle zeolite, and a raw material of an inorganic bonding material to prepare a zeolite raw material; a step of forming the prepared zeolite raw material into a honeycomb shape to prepare a honeycomb formed body; and a step of firing the prepared honeycomb formed body to prepare the honeycomb structure. In the step of preparing the zeolite raw material, as the coarse particle zeolite, a chabazite type zeolite is used in which an average particle diameter is 2 µm or more and 6 µm or less, the fine particle zeolite is used in which an average particle diameter is 0.02 µm or more and smaller than 2 µm, the raw material of the inorganic bonding material which includes at least basic aluminum lactate is used, and 10 to 35 parts by mass of basic aluminum lactate as the raw material of the inorganic bonding material is added to 100 parts by mass of a total mass of the coarse particle zeolite and the fine particle zeolite, to prepare the zeolite raw material.
摘要翻译： 该制造方法包括：将粗粒沸石，微粒沸石和无机接合材料的原料混合而制备沸石原料的工序; 将制备的沸石原料成形为蜂窝形状以制备蜂窝成形体的步骤; 以及煅烧所制备的蜂窝成形体以制备蜂窝结构的步骤。 在制备沸石原料的步骤中，作为粗粒沸石，使用平均粒径为2μm以上且6μm以下的菱沸石型沸石，其中使用平均粒子 其直径为0.02μm以上且小于2μm，使用至少含有碱性乳酸铝的无机粘结材料的原料，作为无机粘结材料的原料使用10〜35质量份的碱性乳酸铝 添加到粗粒沸石和微粒沸石的总质量100质量份中，制备沸石原料。
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6.发明公开CARBON-DIOXIDE RECOVERY APPARATUS, AND CARBON-DIOXIDE RECOVERY METHOD 审中-公开KOHLENDIOXIDWIEDERGEWINNUNGSVORGHHTUNG UND KOHLENDIOXIDWIEDERGEWINNUNGSVERFAHREN
公开(公告)号：EP3106216A4
公开(公告)日：2017-09-27
申请号：EP14881848
申请日：2014-10-15
发明人： YOSHIKAWA KOUHEI , KANEEDA MASATO , NAKAMURA HIDEHIRO , SHIRASAKA TOSHIAKI , KITAMURA KENETSU , ENOMOTO KAZUHIRO
CPC分类号： B01D53/0438 , B01D53/0423 , B01D53/0462 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2253/1122 , B01D2253/1124 , B01D2253/204 , B01D2253/3425 , B01D2257/504 , B01D2259/40009 , B01D2259/40086 , B01D2259/40088 , B01D2259/4009 , B01J20/06 , B01J20/34 , C01B32/50 , Y02C10/04 , Y02C10/08 , Y02P20/152 , Y02P20/57
摘要： In the step of regenerating a carbon dioxide capturing material, the amount of a regeneration gas to be supplied to a carbon dioxide recovery column is reduced to offer higher energy efficiency and to shorten the time taken to perform the regeneration step. A carbon dioxide recovery apparatus includes a carbon dioxide sorbing column, a heating unit, and first, second, and third channels. The carbon dioxide sorbing column contains a carbon dioxide capturing material. The heating unit heats the carbon dioxide capturing material. A carbon-dioxide-containing gas is introduced via the first channel into the carbon dioxide sorbing column. The regeneration gas is introduced via the second channel into the carbon dioxide sorbing column. A gaseous mixture containing a gas desorbed from the carbon dioxide capturing material is recovered via the third channel. In the apparatus, the heating unit preheats the carbon dioxide capturing material, and then the regeneration gas is introduced into the carbon dioxide sorbing column to recover carbon dioxide from the carbon dioxide capturing material.
摘要翻译： 在再生二氧化碳捕获材料的步骤中，要供应到二氧化碳回收塔的再生气体的量减少以提供更高的能量效率并且缩短执行再生步骤所花费的时间。 二氧化碳回收设备包括二氧化碳吸收塔，加热单元以及第一，第二和第三通道。 吸收二氧化碳的塔含有二氧化碳捕集材料。 加热单元加热二氧化碳捕获材料。 含二氧化碳的气体通过第一通道引入二氧化碳吸收塔。 再生气体通过第二通道引入二氧化碳吸收塔。 含有从二氧化碳捕获材料解吸的气体的气体混合物通过第三通道回收。 在该装置中，加热单元预热二氧化碳捕获材料，然后将再生气体引入二氧化碳吸收塔中以从二氧化碳捕获材料回收二氧化碳。
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公开(公告)号：EP3081909A1
公开(公告)日：2016-10-19
申请号：EP15163346.8
申请日：2015-04-13
申请人： Carl Freudenberg KG
发明人： Stahl, Ulrich
CPC分类号： F15D1/025 , B01D53/00 , B01D53/04 , B01D53/0446 , B01D2253/102 , B01D2253/3425 , B01D2257/702 , B01D2259/4508 , B01D2259/4566 , B01J20/20 , B01J20/28045 , F02M35/0218 , F02M35/02441 , F02M35/10314 , F24F13/28 , G01F1/6842 , G01F15/00 , G01F15/125
摘要： Eine Anordnung, umfassend eine Leitung (1) und einen Strömungsgleichrichter (2), wobei der Strömungsgleichrichter (2) in die Leitung (1) eingebaut ist, um einem strömenden Gas nach Durchströmen des Strömungsgleichrichters (2) auf einer Abströmseite (3) innerhalb der Leitung (1) ein vergleichmäßigtes Strömungsprofil zu verleihen, ist im Hinblick auf die Aufgabe, eine Anordnung anzugeben, welche bei teilearmem und kompaktem Aufbau erlaubt, ein strömendes Gas einerseits im Hinblick auf sein Strömungsprofil zu vergleichmäßigen und andererseits Bestandteile eines Gases zu adsorbieren, dadurch gekennzeichnet, dass der Strömungsgleichrichter (2) als Wabenkörper ausgebildet ist, der eine Vielzahl von Kanälen (5) aufweist, die von einander durch Kanalwände (6) abgetrennt sind, wobei der Wabenkörper aus Aktivkohle gefertigt ist oder Aktivkohle aufweist.
摘要翻译： 一种具有线路和流量整流器的装置，其中流动整流器安装在管路中，以便在流经气流在流经线路内的流出侧上通过流动气体之后，使流动气体均匀流动， 旨在提出具有紧凑结构并且包括少量部件并且一方面允许流动气体在其流动廓线方面被均匀化的结构的目的，另一方面允许 要吸附的气体的组分的特征在于，流动整流器被构造为具有通过通道壁彼此分离的多个通道的蜂窝体元件，由此蜂窝体元件由活性炭制成，或者 含有活性炭。
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公开(公告)号：EP2609982B1
公开(公告)日：2016-03-16
申请号：EP12194744.4
申请日：2012-11-29
发明人： Fujioka, Yuji
CPC分类号： B01D53/06 , B01D53/261 , B01D2253/108 , B01D2253/3425 , B01D2257/708 , B01D2257/80 , B01D2257/90 , B01D2258/0258 , B01D2259/40088 , F24F3/1423 , F24F2203/1012 , F24F2203/108 , F28D19/042 , F28F2265/02
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9.发明公开VERWENDUNG EINES WABENFÖRMIGEN FILTERELEMENTS ZUR ADSORPTION VON KOHLENWASSERSTOFFEN 审中-公开VERWENDUNG EINESWABENFÖRMIGENFILTERELEMENTS ZUR吸收哇哇哇哇哇哇
公开(公告)号：EP2946827A1
公开(公告)日：2015-11-25
申请号：EP15167053.6
申请日：2015-05-11
申请人： Carl Freudenberg KG
发明人： Felber, Uwe , Stößer, Thomas , Stahl, Ulrich , Wolff, Thomas, Dr.
CPC分类号： B60H3/0658 , B01D46/2429 , B01D53/04 , B01D2253/102 , B01D2253/304 , B01D2253/3425 , B01D2258/06 , B01D2259/4508 , B01D2259/4566 , B01J20/20 , B01J20/28045 , B60H2003/0691
摘要： Eine Verwendung eines Filterelements (1), umfassend einen Körper (2) der Material (3) aufweist, welches zur Adsorption von Gasen und Dämpfen geeignet ist, wobei der Körper (2) als Wabenkörper ausgebildet ist, ist im Hinblick auf die Aufgabe, einen weitgehend abgeschlossenen Raum problemlos mit gefilterter Zuluft zu versorgen, wobei die Zuluft von Schadstoffen nahezu vollständig befreit ist, die in Aerosolen, Gasen, Flüssigkeitströpfchen oder festen Partikeln vorliegen, und wobei ein konstruktiv einfach aufgebautes Filterelement verwendet wird, dadurch gekennzeichnet, dass das Filterelement (1) verwendet wird, um einen zumindest teilweise abgeschlossenen Raum mit gefilterter Zuluft zu versorgen, wobei die Zuluft von Schadstoffen befreit ist, die in Aerosolen, Gasen, Flüssigkeitströpfchen oder festen Partikeln vorliegen.
摘要翻译： 使用具有适于吸附气体和蒸气的材料的本体的过滤元件，本体为蜂窝体，其目的是向基本上封闭的室提供过滤后的入口空气 以无故障的方式，入口空气几乎完全免除以气溶胶，气体，液滴或固体颗粒形式存在的污染物，以及使用简单结构的过滤元件，其中过滤元件用于供应 将入口空气过滤到至少部分封闭的室，所述入口空气不含存在气溶胶，气体，液滴或固体颗粒形式的污染物。
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10.发明公开
公开(公告)号：EP2747872A1
公开(公告)日：2014-07-02
申请号：EP12754178.7
申请日：2012-08-23
申请人： Corning Incorporated
CPC分类号： B01D53/0446 , B01D53/0438 , B01D53/06 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2253/204 , B01D2253/342 , B01D2253/3425 , B01D2256/16 , B01D2256/245 , B01D2257/304 , B01D2257/504 , B01D2258/0283 , B01D2258/05 , B01D2258/06 , B01D2259/40003 , B01D2259/40086 , Y02C10/08
摘要： High volumetric-efficiency thermally integrated systems for captur¬ ing a target gas from a process gas stream include a monolithic body (10) and a distribution system. The monolithic body (10) includes a first plurality of channels (25) and a second plurality of channels (35) each having sorbent surfaces that reversibly adsorb the target gas. The channels are in thermal communication such that heat from an exothermic adsorption of target gas in one plurality of channels is used by an endothermic desorption of target gas from the other plu¬ rality of channels. Methods for separating a target gas from a process gas stream include switching the high volumetric-efficiency thermal¬ ly integrated systems between a first state and a second state. In the first state, the first plurality of channels (25) undergoes desorption while the second (35) undergoes adsorption. In the second state, the second plurality of channels (35) undergoes desorption while the first plurality (25) undergoes adsorption.
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