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141. 发明申请

US20150075375A1 Mass Transfer Apparatus and Method for Separation of Gases 有权
公开(公告)号：US20150075375A1
公开(公告)日：2015-03-19
申请号：US14487235
申请日：2014-09-16
申请人： Savannah River Nuclear Solutions, LLC
发明人： Gerald C. Blount
IPC分类号： B01D53/18 , B01F3/04 , B01D53/14
CPC分类号： B01D53/1406 , B01D53/1425 , B01D53/1475 , B01D53/18 , B01D2011/005 , B01D2252/103 , B01D2259/40079 , B01F3/04248 , B01F3/04262 , E21B43/36 , Y02C10/06
摘要： A process and apparatus for separating components of a source gas is provided in which more soluble components of the source gas are dissolved in an aqueous solvent at high pressure. The system can utilize hydrostatic pressure to increase solubility of the components of the source gas. The apparatus includes gas recycle throughout multiple mass transfer stages to improve mass transfer of the targeted components from the liquid to gas phase. Separated components can be recovered for use in a value added application or can be processed for long-term storage, for instance in an underwater reservoir.

142. 发明授权

US08983791B2 Carbon dioxide separation recovery system and method of measuring amount of reboiler input heat 有权
标题翻译：二氧化碳分离回收系统及再沸器输入量测量方法
公开(公告)号：US08983791B2
公开(公告)日：2015-03-17
申请号：US13279041
申请日：2011-10-21
申请人： Yukio Ohashi , Takashi Ogawa , Hideo Kitamura , Haruhiko Hirata
发明人： Yukio Ohashi , Takashi Ogawa , Hideo Kitamura , Haruhiko Hirata
IPC分类号： B01D19/00 , G06F15/00 , F01K13/00 , B01D53/14
CPC分类号： F01K13/00 , B01D53/1425 , B01D53/1475 , B01D2252/103 , B01D2252/204 , B01D2258/0283 , B01D2259/65 , Y02C10/04 , Y02C10/06
摘要： According to one embodiment, a carbon dioxide separation recovery system includes an absorption tower that allows carbon dioxide to be absorbed to an absorption liquid, a regeneration tower that regenerates the absorption liquid, a reboiler that heats the absorption liquid of the regeneration tower, using a heating medium, and a measuring device that measures an amount of heat supplied to the absorption liquid from the heating medium. The measuring device includes a cooler that cools the heating medium discharged from the reboiler, and obtains the amount of heat that is supplied to the absorption liquid from the heating medium by subtracting an amount of heat that is retained by the heating medium cooled by the cooler and an amount of heat, which is removed from the heating medium in the cooler, from an amount of heat that is retained by the heating medium supplied to the reboiler.
摘要翻译：根据一个实施方案，二氧化碳分离回收系统包括吸收塔，其允许吸收二氧化碳，吸收液体再生的再生塔，再生塔的吸收液体加热的再沸器，使用加热介质和测量从加热介质供应到吸收液体的热量的测量装置。测量装置包括冷却从再沸器排出的加热介质的冷却器，并且通过减去由冷却器冷却的加热介质保持的热量来获得从加热介质供应到吸收液体的热量以及从冷却器中的加热介质中除去由供应到再沸器的加热介质保留的热量的热量。

143. 发明申请

US20150072393A1 FLUE GAS TREATMENT AND PERMEATE HARDENING 审中-公开
标题翻译： FLE气体处理和透气性硬化
公开(公告)号：US20150072393A1
公开(公告)日：2015-03-12
申请号：US14512452
申请日：2014-10-12
申请人： I.D.E. TECHNOLOGIES LTD.
发明人： Boris LIBERMAN
IPC分类号： B01D53/62 , B01D53/84
CPC分类号： B01D53/62 , B01D53/1475 , B01D53/75 , B01D53/84 , B01D2251/404 , B01D2252/103 , B01D2258/0283 , Y02A50/2342 , Y02A50/2358 , Y02C10/04 , Y02C10/06
摘要： Combining flue gas treatment, and in particular CO2 sequestration, with hardening of reverse osmosis (RO) permeate. Flue gas is compressed and injected into pressurized water, being either cooling water or RO permeate. The water with dissolved CO2 is either dispensed into the sea for biological fixation of the CO2 or, in the case of RO permeate, mixed with limestone to harden the product water.
摘要翻译：结合烟气处理，特别是二氧化碳封存，与反渗透（RO）渗透的硬化。烟气被压缩并注入加压水，即冷却水或RO渗透物。将溶解有CO2的水分配到海中进行生物固定二氧化碳，或者在RO渗透物的情况下，与石灰石混合以使产品水硬化。

144. 发明申请

US20150056115A1 COMPOUND INCLUDING ACTIVATED METAL AND LIGAND, CARBON DIOXIDE ABSORBENT INCLUDING THE COMPOUND, METHOD OF PREPARING THE CARBON DIOXIDE ABSORBENT, AND METHOD OF REMOVING CARBON DIOXIDE 审中-公开
标题翻译：包括活化金属和配体的化合物，包括该化合物的二氧化碳吸收剂，二氧化碳吸收剂的制备方法和除去二氧化碳的方法
公开(公告)号：US20150056115A1
公开(公告)日：2015-02-26
申请号：US14293001
申请日：2014-06-02
申请人： KOREA INSTITUTE OF ENERGY RESEARCH
发明人： Soon Kwan Jeong , Yeo Il Yoon , Sung Chan Nam , Soo Hyun Chol , Sung Ho Yoon , Dong Kook Park
IPC分类号： B01J31/22 , B01D53/86
CPC分类号： B01J31/1815 , B01D53/1475 , B01D53/1493 , B01D53/62 , B01D2252/2053 , B01D2258/0283 , B01J20/223 , B01J31/183 , B01J2531/0247 , B01J2531/26 , Y02A50/2342 , Y02C10/04 , Y02C10/06
摘要： Provided is a compound including an activated metal and a ligand, a carbon dioxide (CO2) absorbent including the compound, a method of preparing the CO2 absorbent, and a method of removing CO2.
摘要翻译：提供了包含活化金属和配体的化合物，包括该化合物的二氧化碳（CO 2）吸收剂，制备CO 2吸收剂的方法和除去CO 2的方法。

145. 发明授权

US08961665B2 Exhaust gas treatment system 有权
标题翻译：废气处理系统
公开(公告)号：US08961665B2
公开(公告)日：2015-02-24
申请号：US13604136
申请日：2012-09-05
申请人： Tatsuya Tsujiuchi , Shintaro Honjo , Takahito Yonekawa , Satoru Sugita , Motofumi Ito , Takashi Kamijo , Tatsuto Nagayasu , Takuya Okamoto
发明人： Tatsuya Tsujiuchi , Shintaro Honjo , Takahito Yonekawa , Satoru Sugita , Motofumi Ito , Takashi Kamijo , Tatsuto Nagayasu , Takuya Okamoto
IPC分类号： B01D53/14
CPC分类号： B01D53/1425 , B01D53/1475 , B01D2258/0283 , F23J15/04 , F23J2215/50 , F23J2219/40 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02E20/326
摘要： There is provided an exhaust gas treatment system including a CO2 recovery unit with further enhanced energy efficiency. The exhaust gas treatment system (1) includes: a CO2 recovery unit (10) including a CO2 absorption column (11), an absorbing solution regeneration column (16), a condensate supply pipeline (15) for supplying condensate, which contains CO2 absorbing solution discharged from the CO2 absorption column (11) to a bottom portion of the absorbing solution regeneration column (16), and a CO2 separation section (22) for performing heat exchange, via a heat exchanger (23), between the CO2 discharged from the absorbing solution regeneration column (16) and the condensate; and an exhaust gas heat exchanger (5) provided on a gas upstream side of the CO2 recovery unit (10) for performing heat exchange between exhaust gas before flowing into the CO2 recovery unit (10) and the condensate.
摘要翻译：提供了具有进一步提高的能量效率的CO 2回收单元的废气处理系统。废气处理系统（1）包括：CO 2回收单元（10），其包括CO 2吸收塔（11），吸收溶液再生塔（16），用于供应冷凝物的冷凝物供应管道（15），其包含CO 2吸收从吸收液体再生塔（16）的底部向CO 2吸收塔（11）排出的溶液和通过热交换器（23）进行热交换的CO 2分离部（22）之间，吸收溶液再生塔（16）和冷凝物; 以及设置在CO 2回收单元（10）的气体上游侧的用于在流入CO 2回收单元（10）和冷凝物之前进行排气之间的热交换的排气热交换器（5）。

146. 发明授权

US08952206B2 Formate based heat stable salt mitigation in physical solvent acid gas absorption processes 有权
标题翻译：物质溶剂酸性气体吸收过程中基于甲酸的热稳定盐减轻
公开(公告)号：US08952206B2
公开(公告)日：2015-02-10
申请号：US14239636
申请日：2012-08-24
申请人： Christophe R. Laroche
发明人： Christophe R. Laroche
IPC分类号： C07C41/34 , B01D53/14
CPC分类号： C07C41/34 , B01D53/1425 , B01D53/1456 , B01D2252/2021 , B01D2252/2025 , B01D2252/2026 , B01D2252/20452 , B01D2252/20463 , B01D2252/20468 , B01D2256/245 , B01D2257/302 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/406 , B01D2257/408 , B01D2257/504 , B01D2258/02 , Y02C10/06
摘要： There is described a process for reducing the concentration of formate based heat stable salts formed in a physical solvent acid gas absorption process (12) wherein acid gas contaminants such as hydrogen sulfide and carbon dioxide are removed from gas mixtures (30) which include these contaminants. The process comprises the step of contacting the physical solvent containing formate based heat stable salts (46) with a metallic and/or organometallic catalyst (52), preferably the catalyst comprises palladium, zinc, platinum, nickel, or rhodium, and/or salts thereof and/or oxides thereof. The process is particularly suited for physical solvents such as refrigerated methanol, dialkyl ethers of polyethylene glycols, N-methyl-2-pyrrolidones, propylene carbonate, blends of N-acetylmorpholine and N-formylmorpholine, 1,3-dimethyl-3,4,5,6-tetrahydro-2(1H)-pyrimidinone, and the like and particularly gas mixtures containing ammonia as a contaminant.
摘要翻译：描述了一种降低在物理溶剂酸性气体吸收过程（12）中形成的甲酸酯基热稳定盐的浓度的方法，其中从包括这些污染物的气体混合物（30）中除去诸如硫化氢和二氧化碳的酸性气体污染物。该方法包括使含有甲酸盐的热稳定盐（46）的物理溶剂与金属和/或有机金属催化剂（52）接触的步骤，优选地，催化剂包括钯，锌，铂，镍或铑，和/或和/或其氧化物。该方法特别适用于物理溶剂如冷冻甲醇，聚乙二醇二烷基醚，N-甲基-2-吡咯烷酮，碳酸亚丙酯，N-乙酰基吗啉和N-甲酰基吗啉的共混物，1,3-二甲基-3,4，特别是包含氨作为污染物的气体混合物。

147. 发明授权

US08945292B2 System for recovering acid gases from a gas stream 有权
标题翻译：从气流中回收酸性气体的系统
公开(公告)号：US08945292B2
公开(公告)日：2015-02-03
申请号：US13429212
申请日：2012-03-23
申请人： Judith Pauline Oppenheim , Anindra Mazumdar
发明人： Judith Pauline Oppenheim , Anindra Mazumdar
IPC分类号： B01D53/14 , B01D53/96 , B01D53/52
CPC分类号： B01D53/14 , B01D53/1406 , B01D53/1425 , B01D53/1462 , B01D53/52 , B01D53/96 , B01D2252/2026 , B01D2257/304 , B01D2257/504 , Y02C10/06 , Y02E20/16 , Y02E20/18
摘要： In one embodiment, a gas purification system is provided. The system includes a first section having a first solvent path and a first gas path. The first gas path is configured to flow a stripping gas to remove hydrogen sulfide (H2S) and carbon dioxide (CO2) from the first solvent path in a first vessel to produce a first gas mixture. The system also includes a second section having a second solvent path. The second solvent path is configured to flow a second solvent mixture to remove H2S from the first gas mixture and CO2 from the second solvent mixture within a second vessel. The second solvent mixture has a solvent saturated in CO2 at a first pressure, the second vessel is operated at a second pressure, and the first and second pressures are within approximately 20% of one another.
摘要翻译：在一个实施例中，提供了一种气体净化系统。该系统包括具有第一溶剂通道和第一气体通路的第一部分。第一气体路径被配置成流动汽提气体以从第一容器中的第一溶剂路径除去硫化氢（H 2 S）和二氧化碳（CO 2）以产生第一气体混合物。该系统还包括具有第二溶剂通路的第二部分。第二溶剂通道被配置为流动第二溶剂混合物以从第一气体混合物中除去H 2 S和在第二容器内从第二溶剂混合物中除去CO 2。第二溶剂混合物具有在第一压力下在CO 2中饱和的溶剂，第二容器在第二压力下操作，并且第一和第二压力彼此在大约20％内。

148. 发明授权

US08945279B2 Polymer-encapsulated carbon capture liquids that tolerate precipitation of solids for increased capacity 有权
标题翻译：聚合物包封的碳捕获液，能容忍固体的沉淀，以增加容量
公开(公告)号：US08945279B2
公开(公告)日：2015-02-03
申请号：US13661900
申请日：2012-10-26
申请人： Lawrence Livermore National Security, LLC
发明人： Roger D. Aines , William L. Bourcier , Christopher M. Spadaccini , Joshuah K. Stolaroff
IPC分类号： B01D53/02 , B01D53/14 , C09K3/00 , B82Y30/00
CPC分类号： B01D53/14 , B01D53/1475 , B01D2252/204 , B01D2257/504 , B82Y30/00 , C09K3/00 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02C10/08
摘要： A system for carbon dioxide capture from flue gas and other industrial gas sources utilizes microcapsules with very thin polymer shells. The contents of the microcapsules can be liquids or mixtures of liquids and solids. The microcapsules are exposed to the flue gas and other industrial gas and take up carbon dioxide from the flue gas and other industrial gas and eventual precipitate solids in the capsule.
摘要翻译：从烟道气和其他工业气体源捕获二氧化碳的系统利用具有非常薄的聚合物壳的微胶囊。微胶囊的内容物可以是液体或液体和固体的混合物。微胶囊暴露于烟气和其他工业气体，并从烟气和其他工业气体中吸收二氧化碳，并在胶囊中吸收最终的沉淀固体。

149. 发明授权

US08932547B2 Modular plant for removal of pollutants from flue gases produced by industrial processes 有权
标题翻译：用于从工业过程产生的烟道气中去除污染物的模块化设备
公开(公告)号：US08932547B2
公开(公告)日：2015-01-13
申请号：US12674223
申请日：2008-08-20
申请人： Tommaso Nardo , Antonio Maria Nardo , Angelo Basile , Fausto Gallucci
发明人： Tommaso Nardo , Antonio Maria Nardo , Angelo Basile , Fausto Gallucci
IPC分类号： B01D47/00 , C01B17/20 , C01B17/16 , C01B17/00 , C07C27/00 , G01D11/26 , B01D50/00 , B01D53/22 , C01B3/06 , E04H5/02 , B01D53/75 , C07C29/152 , B03C3/017 , B01D53/86 , B01D53/77
CPC分类号： E04H5/02 , B01D53/229 , B01D53/75 , B01D53/77 , B01D53/86 , B01D2251/404 , B01D2256/16 , B01D2257/2045 , B01D2257/2047 , B01D2257/302 , B01D2257/404 , B01D2257/504 , B01D2257/602 , B01D2257/7027 , B01J2219/0002 , B03C3/017 , C01B3/068 , C01B2203/0485 , C07C29/152 , Y02C10/04 , Y02C10/06 , Y02C10/10 , Y02E60/36 , Y02P20/152 , Y02P20/582 , Y02P30/30 , C07C31/04
摘要： The invention relates to a so-called zero emission ‘AST-CNR/ITM system’ modular plant for removal of pollutants from flue gases produced by industrial processes. The plant comprises prefabricated modular elements with programmed and automatic operation, easy to mount and assemble on site without undergoing expensive plant stoppage. Each module or ‘reaction tower’ comprises a plurality of sections vertically arranged on top of one another, which carry out the following functions: Removal of particulate matter with treatment and removal of chemical pollutants, such as heavy metals, chlorides, fluorides Treatment and removal of SOx Treatment and removal of NOx Capture of CO2 Production of hydrogen Production of methanol. The various sections may be combined according to the requirements of the plant and of the flue gases to be treated.
摘要翻译：本发明涉及用于从工业过程产生的烟道气中去除污染物的所谓零排放“AST-CNR / ITM系统”模块化设备。该工厂包括具有编程和自动操作的预制模块元件，易于现场安装和组装，而不会导致昂贵的工厂停机。每个模块或“反应塔”包括垂直布置在彼此顶部的多个部分，其具有以下功能：通过处理和去除化学污染物例如重金属，氯化物，氟化物来除去颗粒物质处理和去除的SOx处理和去除NOx捕获二氧化碳的生产氢气生产甲醇。可根据工厂的要求和待处理的烟气组合各部分。

150. 发明申请

US20150010452A1 CIRCULATING MOVING BED SYSTEM FOR CO2 SEPARATION, AND METHOD OF SAME 有权
标题翻译：循环用于二氧化碳分离的移动床系统及其方法
公开(公告)号：US20150010452A1
公开(公告)日：2015-01-08
申请号：US14325519
申请日：2014-07-08
申请人： TDA Research, Inc.
发明人： Jeannine Elizabeth Elliott , Robert James Copeland
IPC分类号： B01D53/96 , B01D53/62
CPC分类号： B01D53/06 , B01D2253/104 , B01D2257/504 , B01D2258/0283 , B01D2259/4009 , B01D2259/402 , B01D2259/4065 , Y02C10/04 , Y02C10/06 , Y02C10/08
摘要： A circulating moving bed and process for separating a carbon dioxide from a gas stream is disclosed. The circulating moving bed can include an adsorption reactor and a desorption reactor, and a sorbent that moves through the two reactors. The sorbent can enter the adsorptive reactor and one end and move to an exit point distal to its entry point, while a CO2 feed stream can enter near the distal point and move countercurrently through the sorbent to exit at a position near the entry point of the sorbent. The sorbent can adsorb the CO2 by concentration swing adsorption and adsorptive displacement. The sorbent can then transfer to a regeneration reactor and can move countercurrently against a flow of steam through the regeneration reactor. The sorbent can be regenerated and the carbon dioxide recaptured by desorbing the carbon dioxide from the sorbent using concentration swing desorption and desorptive displacement with steam.
摘要翻译：公开了一种循环移动床和用于从气流中分离二氧化碳的方法。循环移动床可以包括吸附反应器和解吸反应器，以及移动通过两个反应器的吸附剂。吸附剂可以进入吸附反应器并且一端移动到远离其入口点的出口点，而CO 2进料流可以进入远端附近并且逆流地通过吸附剂，以在接近入口处的入口附近的位置离开吸附剂吸附剂可通过浓度变化吸附和吸附位移吸附CO2。然后，吸附剂可以转移到再生反应器，并且可以逆流逆向通过再生反应器的蒸汽流。吸附剂可以再生，并且通过使用浓缩挥发解吸和用蒸汽解吸取代从吸附剂中解吸二氧化碳来重新捕获二氧化碳。

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