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公开(公告)号：US20140193319A1
公开(公告)日：2014-07-10
申请号：US14150005
申请日：2014-01-08
CPC分类号： B01D53/62 , B01D53/1406 , B01D53/1475 , B01D53/501 , B01D53/502 , B01D53/64 , B01D53/80 , B01D2251/304 , B01D2251/404 , B01D2251/604 , B01D2252/102 , B01D2252/103 , B01D2258/0233 , B01D2258/025 , B01D2258/0283 , F23J2215/50 , Y02C10/06
摘要： The present invention relates to a method and system for cleaning a process gas containing carbon dioxide and contaminants, by bringing the process gas into direct contact with an alkaline solution or slurry, and capturing in the alkaline solution or slurry at least a part of the contaminants of the process gas; and bringing the process gas, depleted in contaminants, into direct contact with a cooling liquid to form a cooled process gas; wherein said alkaline solution or slurry is separate from the cooling liquid.
摘要翻译： 本发明涉及一种通过使工艺气体与碱性溶液或浆料直接接触并且在碱性溶液或淤浆中捕获至少一部分污染物来清洗含有二氧化碳和污染物的工艺气体的方法和系统 的工艺气体; 并将耗尽污染物的工艺气体与冷却液直接接触以形成冷却的工艺气体; 其中所述碱性溶液或浆液与冷却液分开。
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2.发明申请ARRANGEMENT AND PROCESS FOR INTEGRATED FLUE GAS TREATMENT AND SODA ASH PRODUCTION 审中-公开一体化烟气处理和SODA ASH生产的安排和流程公开(公告)号：US20150239744A1
公开(公告)日：2015-08-27
申请号：US14630037
申请日：2015-02-24
IPC分类号： C01D7/12
CPC分类号： C01D7/126 , B01D53/62 , B01D2251/404 , B01D2258/0283 , C01D7/18
摘要： The arrangement of a flue gas treatment system by carbonation-calcination loop and soda ash production system by Solvay process has CaO and heat for use in the soda ash production system extracted from the flue gas treatment system.
摘要翻译： 通过碳酸化 - 煅烧回路和苏打灰生产系统的烟道气处理系统通过Solvay方法的排列具有CaO和热量，用于从烟气处理系统中提取的纯碱生产系统。
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3.发明申请公开(公告)号：US20150368157A1
公开(公告)日：2015-12-24
申请号：US14742102
申请日：2015-06-17
CPC分类号： C01F11/06 , B01D53/62 , B01D53/83 , B01D2251/404 , B01D2251/602 , B01D2257/504 , B01D2258/0283 , B01J6/002 , B01J8/0055 , B01J8/087 , B01J8/10 , B01J8/1809 , B01J2208/0038 , B01J2208/00513 , B01J2208/00752 , C01B32/50 , C04B7/434 , C04B7/44 , C04B7/4438 , F23G5/20 , F27B7/02 , F27B7/2016 , F27B2007/025 , F27D17/004 , F27D17/008 , Y02C10/04 , Y02C10/08 , Y02P20/152
摘要： A method for calcination of a carbon dioxide rich sorbent (containing CaCO3) includes combusting in a furnace a fuel with an oxidizer, supplying heat transfer (HT) solids into the furnace and heating them, transferring the HT solid particles from the furnace to a reactor having a rotatable container, supplying a carbon dioxide rich solid sorbent (containing CaCO3) into the rotatable container, rotating the rotatable container for mixing the solid particles and the carbon dioxide rich solid sorbent for transferring heat from the solid particles to the carbon dioxide rich solid sorbent and generating carbon dioxide and carbon dioxide lean solid sorbent (mainly CaO), discharging the carbon dioxide and the carbon dioxide lean solid sorbent from the rotatable container and the subsequent classification of the HT solids from the lean sorbent.
摘要翻译： 用于煅烧富含二氧化碳的吸附剂（含有CaCO 3）的方法包括在炉中将燃料与氧化剂一起燃烧，向炉内供应传热（HT）固体并加热，将HT固体颗粒从炉中转移到反应器 具有可旋转的容器，将富含二氧化碳的固体吸附剂（含有CaCO 3）供应到可旋转的容器中，使可旋转的容器旋转，用于混合固体颗粒和富含二氧化碳的固体吸附剂，用于将热量从固体颗粒转移到富含二氧化碳的固体 吸附剂和产生二氧化碳和二氧化碳贫固体吸附剂（主要是CaO），从可旋转容器中排出二氧化碳和二氧化碳贫固体吸附剂，随后从贫吸附剂分类HT固体。
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公开(公告)号：US20140112857A1
公开(公告)日：2014-04-24
申请号：US14056486
申请日：2013-10-17
CPC分类号： B01D53/62 , B01D53/83 , B01D53/96 , B01D2251/404 , B01D2251/604 , B01D2257/504 , B01D2258/0283 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02C10/08
摘要： The system includes a first reactor configured to discharge CO2 depleted process gas. The first reactor having a first and a second portion of particulate sorbent material having captured CO2. A second reactor is arranged to receive the first portion of particulate sorbent material and is configured to release CO2 from the particulate sorbent material by decarbonation, return the first portion of particulate sorbent material to the first reactor, and discharge a CO2 rich gas stream. A third reactor is arranged to receive the second portion of particulate sorbent material and is configured to supply water to the second portion of particulate sorbent material to hydrate at least a part of a remaining portion of calcium oxide of the second portion of particulate sorbent material to form calcium hydroxide, and return the second portion of particulate sorbent material to the first reactor.
摘要翻译： 该系统包括被配置为排出二氧化碳贫化处理气体的第一反应器。 第一反应器具有第一和第二部分具有捕获的CO 2的颗粒状吸附剂材料。 第二反应器被布置成接收颗粒状吸附剂材料的第一部分，并且被配置为通过脱碳从颗粒状吸附剂材料释放CO 2，将颗粒状吸附剂材料的第一部分返回到第一反应器，并排出富CO2气流。 第三反应器被布置成接收颗粒状吸附剂材料的第二部分，并且被配置为向颗粒状吸附剂材料的第二部分供应水以将至少一部分剩余部分的颗粒状吸附剂材料的第二部分的氧化钙水合至 形成氢氧化钙，并将颗粒状吸附剂材料的第二部分返回到第一反应器。
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公开(公告)号：US20160051925A1
公开(公告)日：2016-02-25
申请号：US14854515
申请日：2015-09-15
IPC分类号： B01D53/14
CPC分类号： B01D53/1493 , B01D53/14 , B01D53/1406 , B01D53/1475 , B01D53/58 , B01D2252/102 , B01D2252/103 , B01D2257/406 , B01D2257/504 , B01D2258/025 , B01D2258/0283 , B01D2258/0291 , Y02A50/2342 , Y02A50/2346 , Y02C10/06
摘要： A method for capturing ammonia present in combustion flue gas subjected to carbon dioxide removal using a water wash unit included in a chilled ammonia process. The method includes combining a CO2 loaded liquid and a wash water liquid to form a CO2 enriched wash water liquid that is then brought into contact with the combustion flue gas.
摘要翻译： 使用包含在冷冻氨方法中的水洗单元捕获在二氧化碳除去过程中存在的燃烧烟道气中的氨的方法。 该方法包括将经CO 2加载的液体和洗涤水液体组合以形成富含CO 2的洗涤水液体，然后与燃烧烟道气接触。
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公开(公告)号：US20150017081A1
公开(公告)日：2015-01-15
申请号：US14499726
申请日：2014-09-29
CPC分类号： B01D53/83 , B01D45/12 , B01D53/62 , B01D53/82 , B01D53/96 , B01D2251/402 , B01D2251/404 , B01D2257/504 , B01J8/24 , C01B32/60 , C01F11/18 , F27B15/16 , Y02C10/04 , Y02P20/152
摘要： The present invention relates to a method for capturing carbon dioxide CO2 by carbonation in a circulating fluidized bed (CFB) carbonation reactor wherein temperature profile is adjusted by recirculation of solid fractions of metal oxide MeO and metal carbonate MeCO3 to the CFB carbonation reactor. Also a system recirculating the metal oxide MeO and metal carbonate MeCO3 is provided by the invention.
摘要翻译： 本发明涉及在循环流化床（CFB）碳酸化反应器中通过碳酸化捕获二氧化碳CO 2的方法，其中通过将金属氧化物MeO和金属碳酸盐MeCO 3的固体部分再循环到CFB碳酸化反应器来调节温度分布。 本发明还提供了再循环金属氧化物MeO和金属碳酸盐MeCO 3的体系。
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