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1. 发明申请

WO2019115831A1 MASS TRANSFER SYSTEMS 审中-公开
公开(公告)号：WO2019115831A1
公开(公告)日：2019-06-20
申请号：PCT/EP2018/085300
申请日：2018-12-17
申请人： FJELL BIODRY AS
发明人： STRAND, Asbjørn , ROUT, Kumar Ranjan , CHEN, De
IPC分类号： B01D53/08 , B01D53/62 , B01D53/96 , B01D53/83
CPC分类号： B01D53/08 , B01D53/62 , B01D53/83 , B01D53/96 , B01D2251/606 , B01D2253/112 , B01D2253/1124 , B01D2255/2045 , B01D2257/504 , B01D2259/4009 , B01D2259/402
摘要： Disclosed herein is a gas capture system comprising: a gas inlet arranged to receive a gas flow into the system; a gas outlet arranged to provide a gas flow out of the system; a gas capture region for mass transfer between a gas and a sorbent of the gas; and a sorbent regeneration region for regenerating the sorbent by heating the sorbent so that the sorbent releases a gas; wherein: the gas capture region is arranged to receive sorbent from the sorbent regeneration region; the sorbent regeneration region is arranged to receive sorbent for regeneration from the gas capture region; the sorbent is a solid sorbent of carbon dioxide gas; and the gas capture region comprises: a sorbent inlet arranged to receive an input of sorbent into the gas capture region; a sorbent outlet arranged to provide an output of sorbent from the gas capture region; one or more mass transfer regions arranged between the sorbent inlet and the sorbent outlet such that, in use, the sorbent is retained within the one or more mass transfer regions as the sorbent moves through the mass transfer regions and the mass transfer between the gas and the sorbent occurs in the one or more mass transfer regions; a first gas chamber; and a second gas chamber, that is different from the first gas chamber; wherein the first gas chamber, second gas chamber and one or more mass transfer regions are arranged such that, in use, there is a flow path for gas that comprises gas flowing from the first gas chamber into one of the one or more mass transfer regions, the gas then flowing from said one of the mass transfer regions into the second gas chamber and the gas then flowing from the second gas chamber back into said one of the mass transfer regions.

2. 发明申请

WO2016122842A1 SEPARATION OF NITROGEN FROM HYDROCARBON GAS USING PYROLYZED SULFONATED MACROPOROUS ION EXCHANGE RESIN 审中-公开
标题翻译：使用磷酸化大型离子交换树脂从烃类气体中分离氮
公开(公告)号：WO2016122842A1
公开(公告)日：2016-08-04
申请号：PCT/US2016/012256
申请日：2016-01-06
申请人： DOW GLOBAL TECHNOLOGIES LLC
发明人： LIU, Junqiang , HAN, Chan , GOLTZ, H. Robert , RODGERS, Matthew L. , MATTEUCCI, Scott T. , KERN, Brandon J.
IPC分类号： B01D53/02 , B01D53/08 , B01J20/26 , B01J20/30 , C01B31/08 , B01J20/28
CPC分类号： B01D53/08 , B01D53/02 , B01D2253/206 , B01D2253/308 , B01D2256/24 , B01D2256/245 , B01D2257/102 , B01D2259/40094 , B01J20/20 , B01J20/267 , B01J20/28061 , B01J20/28064 , B01J20/2808 , B01J20/28085 , B01J20/28092 , B01J20/3078 , B01J20/3416 , B01J20/3441 , B01J2220/4812 , Y02C20/20
摘要： A method for separating N 2 from a hydrocarbon gas mixture containing N 2 comprising the steps of: i) providing a bed of adsorbent selective for N 2 ; ii) passing the hydrocarbon gas mixture through the bed of adsorbent to at least partially remove N 2 from the gas mixture to produce: (a) N 2 -loaded adsorbent and (b) N 2 -depleted hydrocarbon gas mixture; iii) recovering the N 2 -depleted hydrocarbon gas mixture; iv) regenerating the N 2 -loaded adsorbent by at least partially removing N 2 from the adsorbent; and v) sequentially repeating steps (ii) and (iii) using regenerated adsorbent from step (iv); wherein the adsorbent comprises a pyrolized sulfonated macroporous ion exchange resin.
摘要翻译：一种从含有N 2的烃气体混合物中分离N 2的方法，包括以下步骤：i）提供对N 2有选择性的吸附剂床; ii）使烃气体混合物通过吸附剂床至少部分地从气体混合物中除去N 2，以产生：（a）N2负载的吸附剂和（b）N 2耗尽的烃气体混合物; iii）回收耗尽N2的烃类气体混合物; iv）通过至少部分地从吸附剂中除去N 2来再生N 2负载的吸附剂; 和v）使用来自步骤（iv）的再生吸附剂顺序地重复步骤（ii）和（iii）; 其中所述吸附剂包括热解的磺化大孔离子交换树脂。

3. 发明申请

WO2016100111A1 MOVING BED TEMPERATURE SWING ADSORPTION PROCESS 审中-公开
标题翻译：移动床温度旋转吸附过程
公开(公告)号：WO2016100111A1
公开(公告)日：2016-06-23
申请号：PCT/US2015/065201
申请日：2015-12-11
申请人： UOP LLC
发明人： SADLER, Clayton C. , WEGERER, David A. , LIPPMAN, Matthew
IPC分类号： B01D53/06 , B01J8/12 , C10L3/10 , B01D53/86
CPC分类号： B01D53/0462 , B01D53/0438 , B01D53/0454 , B01D53/08 , B01D2253/104 , B01D2253/108 , B01D2255/102 , B01D2256/16 , B01D2256/24 , B01D2256/245 , B01D2257/2045 , B01D2257/2064 , B01D2257/2066 , B01D2257/80 , B01D2259/4009
摘要： Process for adsorbing a species from a feed gas stream. Feed gas stream is introduced to an adsorption zone having a sorbent. Species from the feed gas stream is adsorbed onto the sorbent at an adsorbing temperature to enrich the sorbent with the species and deplete the species from the feed gas stream. Species-lean product gas stream is output. Species-rich sorbent from the adsorption zone is passed to a regeneration zone. Regenerant gas at a regenerating temperature greater than the adsorbing temperature is introduced into the regeneration zone to strip the species from the species-rich sorbent. Regenerated sorbent from the regeneration zone passes to a cooling zone disposed below the regeneration zone. Regenerated sorbent is cooled at a cooling temperature below the regenerating temperature. Cooled sorbent is transferred to the adsorbent zone.
摘要翻译：从进料气流中吸附物质的方法。将进料气流引入具有吸附剂的吸附区。来自进料气流的物质在吸附温度下吸附到吸附剂上，以使物质富集吸附剂并从进料气流中消耗物质。输出物种贫产品气流。来自吸附区的物种丰富的吸附剂被传递到再生区。将再生温度大于吸附温度的再生气体引入再生区，以从物种丰富的吸附剂中剥离物质。来自再生区的再生吸附剂进入设置在再生区下方的冷却区。再生吸附剂在低于再生温度的冷却温度下冷却。冷却的吸附剂转移到吸附剂区域。

4. 发明申请

WO2016074980A1 PROCESS FOR CAPTURING CO2 FROM A GAS STREAM 审中-公开
标题翻译：从气体流中吸收二氧化碳的方法
公开(公告)号：WO2016074980A1
公开(公告)日：2016-05-19
申请号：PCT/EP2015/075511
申请日：2015-11-03
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. , SHELL OIL COMPANY
发明人： SPRACHMANN, Gerald , VAN MOSSEL, Gerardus, Antonius, Franciscus , DATHE, Hendrik , PROELL, Tobias , SCHÖNY, Gerhard
IPC分类号： B01D53/62 , B01D53/83 , B01J8/18 , B01D53/08
CPC分类号： B01D53/83 , B01D53/08 , B01D53/62 , B01D2252/204 , B01D2258/0283 , B01J8/189 , B01J8/26 , Y02A50/2342 , Y02C10/04 , Y02C10/08
摘要： The present invention relates to a process for capturing carbon dioxide from a gas stream. The gas stream is contacted with solid adsorbent particles in an adsorption zone. The adsorption zone has at least two beds of fluidized solid adsorbent particles, and the solid adsorbent particles are flowing downwards from bed to bed. The solid adsorbent particles comprise 15 to 75 weight% of organic amine compounds. The gas stream entering the adsorption zone has a dew point which is at least 5 °C below the forward flow temperature of the coolest cooling medium in the adsorption zone. Carbon dioxide enriched solid adsorbent particles are heated, and then regenerated. The desorption zone has at least two beds of fluidized solid adsorbent particles, and the stripping gas is steam. The regenerated particles are cooled and recycled to the adsorption zone.
摘要翻译：本发明涉及从气流中捕获二氧化碳的方法。气流与吸附区中的固体吸附剂颗粒接触。吸附区具有至少两个流化固体吸附剂颗粒床，固体吸附剂颗粒从床向下流动至床。固体吸附剂颗粒包含15至75重量％的有机胺化合物。进入吸附区的气流的露点比吸附区最冷的冷却介质的正向流动温度低至少5℃。将富含二氧化碳的固体吸附剂颗粒加热，然后再生。解吸区具有至少两个流化固体吸附剂颗粒床，汽提气体是蒸汽。将再生的颗粒冷却并再循环至吸附区。

5. 发明申请

WO2015183331A1 IMPROVED CO-CURRENT REGENERATION PROCESS FOR ADSORPTION MEDIA USED FOR RECOVERING CONDENSABLE COMPONENTS FROM A GAS STREAM 审中-公开
标题翻译：用于从气体流回收可混合组分的吸附媒质改进的同时再生过程
公开(公告)号：WO2015183331A1
公开(公告)日：2015-12-03
申请号：PCT/US2014/049795
申请日：2014-08-05
申请人： DOW GLOBAL TECHNOLOGIES LLC
发明人： LEISTER, Jonathan W. , BADHWAR, Ajay N. , DUGAS, Ross E. , GOLTZ, H. Robert , MATTEUCCI, Scott T.
IPC分类号： B01D53/04 , C10L3/10 , C10G5/02 , B01D53/08
CPC分类号： C10L3/101 , B01D53/04 , B01D53/08 , B01D2253/202 , B01D2256/245 , B01D2257/7022 , B01D2259/40088 , B01D2259/4009 , B01D2259/40094 , B01D2259/40098 , B01J20/3408 , B01J20/3416 , B01J20/3425 , B01J20/3433 , B01J20/3458 , B01J20/3483 , B01J20/3491 , C10G5/02 , C10L2290/06 , C10L2290/12 , C10L2290/36 , C10L2290/542 , C10L2290/543 , C10L2290/545
摘要： Disclosed is an improved process for recovering condensable components from a gas stream, in particular, heavier hydrocarbons from a gas stream. The present process uses solid adsorbent media to remove said heavier hydrocarbons wherein the adsorbent media is regenerated in a continuous fashion in a continuous adsorbent media co-current regeneration system using a stripping gas to provide a regenerated adsorbent media and a product gas comprising heavier hydrocarbons from a loaded adsorbent media.
摘要翻译：公开了一种用于从气流，特别是来自气流的较重烃回收可冷凝成分的改进方法。本发明方法使用固体吸附剂介质去除所述较重的烃，其中吸附介质在连续的吸附介质共流再生系统中以连续方式再生，使用汽提气体提供再生的吸附剂介质和包含较重烃的产物气体，加载的吸附剂介质。

6. 发明申请

WO2015153848A1 ENERGY EFFICIENT ETHANOL RECOVERY BY ADSORPTION 审中-公开
标题翻译：能源效率乙醇通过吸收回收
公开(公告)号：WO2015153848A1
公开(公告)日：2015-10-08
申请号：PCT/US2015/024019
申请日：2015-04-02
申请人： JOULE UNLIMITED TECHNOLOGIES, INC.
发明人： HETTENBACH, Kevin, William
IPC分类号： C07C29/88
CPC分类号： C07C29/76 , B01D53/08 , B01D2257/708 , C07C29/88 , C07C31/08
摘要： A method and system for recovering a volatile organic compound from a dilute aqueous phase. The method may include separating volatile organic compound from the aqueous phase by using carrier gas to generate a solvent-laden vapor stream, feeding a solvent-laden vapor stream to a mass of carbon adsorbent and enabling the solvent to be absorbed and separated from the solvent-laden vapor stream, releasing the absorbed volatile organic compound, and condensing the released volatile organic compound to form a condensate. The system may include a vapor phase source containing ethanol, at least one carbon bed containing a mass of coconut shell carbon, a steam source in fluid communication with the carbon bed, and a condenser in fluid communication with the carbon bed. The method and system may also utilize microbeads as an absorbent and may be configured so the capacity is scalable from lab scale to production scale.
摘要翻译：一种从稀水相中回收挥发性有机化合物的方法和系统。该方法可以包括通过使用载气分离挥发性有机化合物以产生含溶剂的蒸气流，将含溶剂的蒸气流供给到大量碳吸附剂，并使溶剂能够从溶剂中吸收和分离释放吸收的挥发性有机化合物，并将释放的挥发性有机化合物冷凝以形成冷凝物。该系统可以包括含有乙醇的气相源，至少一个含有大量椰子壳碳的碳床，与碳床流体连通的蒸汽源和与碳床流体连通的冷凝器。该方法和系统还可以使用微珠作为吸收剂，并且可以被配置为使得容量从实验室规模可扩展到生产规模。

7. 发明申请

WO2015142380A1 SEQUENTIAL REMOVAL OF NGLS FROM A NATURAL GAS STREAM 审中-公开
标题翻译：从天然气流顺序地去除NGLS
公开(公告)号：WO2015142380A1
公开(公告)日：2015-09-24
申请号：PCT/US2014/049784
申请日：2014-08-05
申请人： DOW GLOBAL TECHNOLOGIES LLC
发明人： MATTEUCCI, Scott T. , GOLTZ, H. Robert , BADHWAR, Ajay N. , SHURGOTT, Nicholas J. , LEISTER, Jonathan W.
IPC分类号： B01D53/04 , C07C7/13 , C10L3/10 , C10G5/02
CPC分类号： C10G5/02 , B01D15/1871 , B01D15/1885 , B01D15/203 , B01D53/04 , B01D53/0438 , B01D53/0462 , B01D53/047 , B01D53/08 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2253/202 , B01D2253/206 , B01D2253/306 , B01D2253/308 , B01D2253/31 , B01D2256/245 , B01D2257/302 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/406 , B01D2257/408 , B01D2257/504 , B01D2257/7022 , B01D2259/40094 , B01D2259/402 , B01D2259/403 , B01D2259/404 , B01D2259/4061 , B01D2259/4062 , B01D2259/4063 , B01D2259/4065 , B01D2259/4066 , B01D2259/4067 , B01D2259/41 , B01D2259/414 , C10L3/10 , C10L3/101 , C10L2290/12 , C10L2290/542 , Y02C10/08
摘要： Disclosed is a method of sequentially separating and recovering one or more NGLs (129, 229) from a natural gas feedstream (3). Specifically, a raw natural gas feedstream (3) is passed through two or more NGLs separation unit (100, 200) wherein each separation unit removes one or more NGLs from the natural gas feedstream to provide a methane-rich natural gas supply (205). Each separation unit employs an adsorption media and has an adsorption step and a media regeneration step wherein the regeneration step may be operated as a batch process, a semi-continuous process, or a continuous process. One embodiment of this method provides for the use of a different regenerable adsorbent media in each separation unit.
摘要翻译：公开了从天然气进料流（3）顺序地分离并回收一个或多个NGL（129,229）的方法。具体地说，原料天然气进料流（3）通过两个或更多个NGL分离单元（100,200），其中每个分离单元从天然气进料流中除去一个或多个NGL以提供富含甲烷的天然气供应（205）。每个分离单元采用吸附介质并具有吸附步骤和介质再生步骤，其中再生步骤可以作为间歇工艺，半连续工艺或连续工艺操作。该方法的一个实施方案提供了在每个分离单元中使用不同的可再生吸附剂介质。

8. 发明申请

WO2013042089A1 REMOVAL OF MERCURY EMISSIONS 审中-公开
标题翻译：拆除汞排放
公开(公告)号：WO2013042089A1
公开(公告)日：2013-03-28
申请号：PCT/IB2012/055042
申请日：2012-09-21
申请人： ALSTOM TECHNOLOGY LTD
发明人： LAFLESH, Richard, C. , IOVINO, John , KANG, Shin, G. , EDBERG, Carl, D. , COURNOYER, Raymond, W.
IPC分类号： B01D53/64 , B01D53/83
CPC分类号： B01D53/10 , B01D53/08 , B01D53/12 , B01D53/64 , B01D53/83 , B01D2253/102 , B01D2257/602 , F23J15/02 , F23J2215/60 , F23J2219/30
摘要： A system for removing gaseous pollutants, such as mercury from flue gases of a solid- fueled furnace (17), includes a sorbent mill (34) that receives superheated steam and a sorbent (28), such as activated carbon, in a partially agglomerated state, that processes the sorbent (28) by de-agglomerating and comminuting the sorbent (28). An educator (35) transports the processed sorbent (28) to a distributor (36) that injects it into the flue gases at a contact location having a temperature between 500º F and 900º F, whereupon the sorbent (28) adsorbs mercury from the flue gas. A particle collection device (24) removes the processed sorbent (28) having adsorbed mercury, from the flue gas.
摘要翻译：用于从固体燃料炉（17）的烟道气中除去气体污染物（例如汞）的系统包括接收过热蒸汽的吸附剂（34）和吸附剂（28），例如活性炭，部分聚集状态，其通过使吸附剂（28）脱附和粉碎来处理吸附剂（28）。教育者（35）将经处理的吸附剂（28）运送到分配器（36），分配器（36）将其注入到温度在500°F和900°F之间的接触位置处的烟道气中，于是吸附剂（28）从烟道中吸附汞加油站。颗粒收集装置（24）从烟道气中除去具有吸附的汞的经处理的吸附剂（28）。

9. 发明申请

WO2012136913A1 MÉLANGE D'UN ADSORBANT ET D'UN MATÉRIAU À CHANGEMENT DE PHASE À DENSITÉ ADAPTÉE 审中-公开
标题翻译：吸附剂的混合物和具有适应密度的相变材料
公开(公告)号：WO2012136913A1
公开(公告)日：2012-10-11
申请号：PCT/FR2012/050515
申请日：2012-03-13
申请人： L'AIR LIQUIDE,SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE , GUERET, Vincent , MONEREAU, Christian , PULLUMBI, Pluton
发明人： GUERET, Vincent , MONEREAU, Christian , PULLUMBI, Pluton
IPC分类号： B01D53/047 , C09K5/06
CPC分类号： B01J20/28011 , B01D53/02 , B01D53/047 , B01D53/0473 , B01D53/08 , B01D2253/102 , B01D2253/104 , B01D2253/108 , B01D2253/204 , B01D2253/304 , B01D2256/10 , B01D2256/12 , B01D2256/16 , B01D2256/22 , C09K5/063 , Y02C10/08
摘要： Agglomérat comprenant un premier matériau à changement de phase (MCP) et un constituant présentant une densité supérieure à 800 kg/m3 et formant le noyau dudit agglomérat.
摘要翻译：本发明涉及包含第一相变材料（PCM）和密度高于800kg / m 3并且形成所述附聚物的核心的成分的附聚物。

10. 发明申请

WO2012123200A1 VERFAHREN ZUR ADSORPTION VON GERUCHSEMISSIONEN AUS DER KAUTSCHUKVERARBEITUNG 审中-公开
标题翻译：吸附异味排放橡胶加工方法
公开(公告)号：WO2012123200A1
公开(公告)日：2012-09-20
申请号：PCT/EP2012/052373
申请日：2012-02-13
申请人： CONTINENTAL REIFEN DEUTSCHLAND GMBH , RECKER, Carla , THEUSNER, Martin
发明人： RECKER, Carla , THEUSNER, Martin
IPC分类号： B01D53/04 , B01D53/08
CPC分类号： B01D53/04 , B01D53/08 , B01D2253/102 , B01D2253/106 , B01D2253/1124 , B01D2257/708 , B01D2257/90 , B29B7/7495
摘要： Um ein Verfahren bereitzustellen, mit dem effektiv Geruchsemissionen, Aerosole und/oder Stäube aus der Abluft getrennt werden, wird folgendes Verfahren mit folgenden Schritten vorgeschlagen: a) Absaugen von Geruchsemissionen, Aerosolen und/oder Stäuben (2) mit einer Absauganlage (9), wobei die Geruchsemissionen, Aerosole und/oder Stäube (2) bei der Kautschukverarbeitung anfallen, b) Adsorption der Geruchsemissionen mit einem in der Absauganlage (9) angeordneten Filteranlage (4), wobei die Filteranlage (4) ein Adsorbens (5, 21, 8) für Geruchsemissionen und/oder Aerosole und/oder ein Filtermittel (12) für das Separieren von Stäuben umfasst, wobei das Adsorbens (5, 21, 8) die Geruchsemissionen hochwirksam aus der Abluft entfernt und für die Mischungsherstellung einsetzbar ist, c) Abführen von sauberer, geruchsfreier Luft (7) mit einem Fördermittel aus der Absauganlage (9), d) Abführen des beladenen Adsorbens (13) und der separierten Stäube aus der Absauganlage (9).
摘要翻译：提供一种方法，其从废气中分离有效气味排放，气雾剂和/或灰尘，包括以下步骤下面的步骤，提出了：1）的气味排放，气雾剂和/或粉剂（2）与抽吸系统（9）的提取，其中所述气味排放，（2）在橡胶加工得到的气雾剂和/或灰尘，b）用气味排放（在提取9）的吸附布置的过滤器设备（4），其中，所述过滤器单元（4）的吸附剂（5，21 8 ）包括用于气味排放和/或气雾剂和/或用于灰尘分离的过滤器装置（12），其中，所述吸附剂（5，21，8），气味排放是高度有效地从排气除去，可用于该混合物的制备中，c）中从吸干净，无异味的空气（7）的输送从抽吸单元装置（9）中，d）排出载货吸附剂（13）和分离的灰尘从抽吸系统（9）。

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