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31. 发明申请

WO2004043564A3 MOVING BED ADSORBER/DESORBER AND LOW FLOW (HIGH YIELD) DESORBER DEVICES AND THEIR METHODS OF USE 审中-公开
标题翻译：移动床ADDORBER / DESORBER AND LOW FLOW（HIGH YIELD）DESORBER DEVICES及其使用方法
公开(公告)号：WO2004043564A3
公开(公告)日：2004-07-08
申请号：PCT/US0335785
申请日：2003-11-06
申请人： CHEMICAL RECOVERY INTERNATIONA
发明人： DAI XIANG FENG DI
IPC分类号： B01D53/06 , B01D53/08
CPC分类号： B01D53/08 , B01D53/0446 , B01D53/261 , B01D2253/20 , B01D2253/202 , B01D2257/7022 , B01D2257/708 , B01D2257/80 , B01D2259/40088 , B01D2259/4009 , B01D2259/402
摘要： A Moving bed adsorber/desorber apparatus (10) contains an adsorbent bed (12) having adsorbent material (14) moving over a series of vane members (70) and a fluid inlet assembly (24) that passes feed between vane members (70) and through the moving adsorbent material (14). An adsorbent material bed thickness regulator (30) is positionned a spaced distance from vane members (70) to regulate the depht of adsorbent material (14). The adsorbent material (14) can be divised into two or more sloped passageways (20), which allow the contamined fee fluid (22) to flow through separate arrays of vane members (70).
摘要翻译：移动床吸附器/解吸器装置（10）包含吸附床（12），吸附床（12）具有在一系列叶片构件（70）上移动的吸附材料（14）和通过叶片构件（70）之间的进料通过的流体入口组件（24）并通过移动的吸附剂材料（14）。吸附材料床层调节器（30）与叶片构件（70）间隔开定位，以调节吸附材料（14）的深度。吸附材料（14）可以分成两个或更多个倾斜的通道（20），这允许被检查的费用流体（22）流过分离的叶片构件阵列（70）。

32. 发明申请

WO0235623A8 SYSTEMS AND PROCESSES FOR PROVIDING HYDROGEN TO FUEL CELLS 审中-公开
标题翻译：向氢燃料电池提供氢的系统和工艺
公开(公告)号：WO0235623A8
公开(公告)日：2003-10-30
申请号：PCT/CA0101523
申请日：2001-10-26
申请人： QUESTAIR TECHNOLOGIES INC , KEEFER BOWIE , SAWADA JAMES A , JOHANNES ERIK P , ROY SURAJIT , BROWN MICHAEL J
发明人： KEEFER BOWIE G , SAWADA JAMES A , JOHANNES ERIK P , ROY SURAJIT , BROWN MICHAEL J
IPC分类号： C01B3/32 , B01D53/047 , B01D53/08 , B01J4/00 , B01J20/18 , C01B3/38 , C01B3/40 , C01B3/48 , C01B3/56 , H01M8/00 , H01M8/04 , H01M8/06 , H01M8/10
CPC分类号： B01D53/06 , B01D53/047 , B01D53/261 , B01D2253/102 , B01D2253/108 , B01D2256/16 , B01D2257/502 , B01D2257/80 , B01D2258/0208 , B01D2259/40001 , B01D2259/40005 , B01D2259/402 , B01D2259/4541 , C01B3/38 , C01B3/386 , C01B3/56 , C01B2203/00 , C01B2203/0233 , C01B2203/025 , C01B2203/0283 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0883 , C01B2203/1076 , C01B2203/1211 , C01B2203/1223 , C01B2203/1229 , C01B2203/1241 , C01B2203/1288 , C01B2203/146 , C01B2203/147 , C01B2203/82 , H01M8/04022 , H01M8/04029 , H01M8/04156 , H01M8/0612 , H01M8/0662 , Y02C10/08 , Y02P20/128 , Y02P20/129 , Y02P20/52
摘要： A process and system for providing a hydrogen-containing gas stream to a fuel cell anode that includes providing a hydrogen-containing gas stream that includes carbon monoxide, introducing the hydrogen-containing gas stream into a pressure swing adsorption module that includes at least one carbon monoxide-selective adsorbent to produce a purified hydrogen-containing gas stream, and introducing the purified hydrogen-containing gas stream to the fuel cell anode. The pressure swing adsorption module can also include a second adsorbent and/or catalyst. Also disclosed is a fuel cell system coupled to an internal combustion engine and a fuel cell system that utilizes fuel cell waste heat for vaporizing a hydrocarbon/water mixture.
摘要翻译：一种用于向燃料电池阳极提供含氢气体流的方法和系统，其包括提供包含一氧化碳的含氢气体流，将含氢气流引入变压吸附模块，所述变压吸附模块包括至少一个碳一氧化碳选择性吸附剂以产生纯化的含氢气流，并将纯化的含氢气体流引入燃料电池阳极。变压吸附模块还可以包括第二吸附剂和/或催化剂。还公开了一种联接到内燃机和燃料电池系统的燃料电池系统，其利用燃料电池废热来蒸发烃/水混合物。

33. 发明申请

WO2002085497A1 METHOD FOR REGENERATION OF A LIMESTONE BED FOR FLUE GAS CLEANING 审中-公开
标题翻译：用于再生用于气体清洁的石灰石床的方法
公开(公告)号：WO2002085497A1
公开(公告)日：2002-10-31
申请号：PCT/SE2002/000373
申请日：2002-03-04
申请人： FAGERSTA INTERVEX AB , TIBERG, Lars
发明人： TIBERG, Lars
IPC分类号： B01D53/08
CPC分类号： B01D53/83 , B01D53/508 , F23J2215/20 , F23J2219/60
摘要： Combustion plants burning fuels that contain sulphur must clean the flue gases from sulphur oxides for environmental reasons. This can be done by leading the flue gases through a limestone bed where calcium carbonate is transformed to calcium sulphate (gypsum). According to the invention, a portion of the limestone bed (17) is fed out, cleaned in two steps and reused. In a first cleaning step, powdery material is separated in a sieve (42) and in a second step the surface of the limestone is worn off in a tumbler (43) with water addition. The cleaned limestone and the powdery material from the second step is introduced again to the bed. The powdery material worn off in the tumbler consists mainly of limestone and gypsumg.
摘要翻译：由于环境原因，燃烧含有硫的燃料的燃烧工厂必须清洁硫氧化物的烟道气。这可以通过引导烟道气通过石灰石床来完成，其中碳酸钙被转化为硫酸钙（石膏）。根据本发明，一部分石灰石床（17）被送出，以两个步骤清洁并重复使用。在第一清洁步骤中，将粉末材料在筛子（42）中分离，并且在第二步骤中，石灰石的表面在添加水的滚筒（43）中磨损。将清洁的石灰石和来自第二步的粉末状材料再次引入床中。在滚筒上磨损的粉状材料主要由石灰石和石膏组成。

34. 发明申请

WO00013782A1 FLUID DISTRIBUTOR-MIXER-EXTRACTOR AND RELATED METHOD 审中-公开
标题翻译：流体分配器 - 混合器 - 提取器及相关方法
公开(公告)号：WO00013782A1
公开(公告)日：2000-03-16
申请号：PCT/FR1999/002065
申请日：1999-08-30
IPC分类号： G01N30/02 , B01D11/00 , B01D15/02 , B01D15/18 , B01D53/08 , B01F3/08 , B01F5/00 , B01F5/02 , B01F5/06 , B01F5/10 , B01J8/04 , C07B61/00 , C07C7/12 , C07C15/08 , C07C17/12 , G01N30/60
CPC分类号： B01J8/0492 , B01D15/1842 , B01D53/0423 , B01D53/0446 , B01D2215/023 , B01D2257/7027 , B01D2259/402 , B01F5/0601 , B01F15/0264 , B01J8/0453 , C07C7/12 , C07C15/08
摘要： The invention concerns a device (DME) or panel for collecting, distributing, mixing or extracting several fluids, at least one main fluid and two secondary fluids, comprising at least: means for collecting a main fluid (3, 9); at least two injection and/or extraction lines (6, 7) for allowing through secondary fluids; at least two mixing chambers (11a, 11b) communicating with the injection and/or extraction lines through orifices or passages (6I, 7I); at least means for redistributing (12, 4) the fluid coming from said mixing chambers; means (5a, 5b) for separating the collecting and redistributing means; the extraction lines (6, 7) are arranged one above the other and the mixing chambers (11a, 11b) are arranged on either side of the lines and symmetrically relative to the orifices operating the injection. The invention is useful for praxylene separation on mobile simulated bed.
摘要翻译：本发明涉及用于收集，分配，混合或提取多种流体的装置（DME）或面板，至少一个主流体和两个次流体，至少包括：用于收集主流体（3,9）的装置; 用于允许通过第二流体的至少两个注入和/或提取管线（6,7）通过孔或通道（6I，7I）与注射和/或提取管线连通的至少两个混合室（11a，11b）; 至少用于重新分配（12,4）来自所述混合室的流体的装置; 用于分离收集和再分配装置的装置（5a，5b）; 提取管线（6,7）一个一个地布置，并且混合室（11a，11b）布置在管线的任一侧上并且相对于操作喷射的孔对称地布置。本发明可用于移动模拟床上的丙烯分离。

35. 发明申请

WO1994008697A1 METHOD FOR FLUE-GAS CLEANING 审中-公开
标题翻译：用于气体清洁的方法
公开(公告)号：WO1994008697A1
公开(公告)日：1994-04-28
申请号：PCT/SE1993000861
申请日：1993-10-20
申请人： SVENSKA ENERGINÄT MILJÖTEKNIK AB , LÜNING, Björn
发明人： SVENSKA ENERGINÄT MILJÖTEKNIK AB
IPC分类号： B01D53/08
CPC分类号： B01D53/08 , B01D53/0431 , B01D53/0462 , B01D53/508 , B01D2251/404 , B01D2251/606 , B01D2257/302 , B01D2258/0283
摘要： In a method for cleaning SOx-polluted flue gases from a combustion process, the flue gases are, in a gas-cleaning zone (20), passed through a gas-cleaning bed (22) of an SOx-absorbing substance which, once polluted and heated by the flue gases, is circulated out of and back to the gas-cleaning zone (20) in a circulation path which passes through a cooling zone (30), where the substance is directly contacted with a cooling medium in order to be cooled, and a separating zone (40), where sulphur pollutants are removed. The gas-cleaning bed (22) is gradually displaced into the cooling zone (30) where it instead forms a cooling bed (32) through which the cooling medium is passed. The bed is displaced through a channel (21, 50, 31) of annular cross section, such that the substance is fed as a tubular body (22, 53, 32) through the channel running through the gas-cleaning zone (20) as well as the cooling zone (30). The flue gases and the cooling medium are passed substantially radially through the bed in the gas-cleaning zone (20) and the cooling zone (30), respectively.
摘要翻译：在用于清洁来自燃烧过程的SO x污染烟道气的方法中，废气在气体清洁区（20）中通过吸收SO x的物质的气体清洁床（22），其一旦被污染并被烟道气加热，在通过冷却区（30）的循环路径中循环回到气体清洁区（20），在该循环路径中物质与冷却介质直接接触，以便于和分离区（40），其中硫污染物被去除。气体清洁床（22）逐渐移入冷却区（30），在冷却区（30）中形成冷却介质通过的冷却床（32）。床通过环形横截面的通道（21,50,31）移动，使得物质通过穿过气体清洁区（20）的通道作为管状体（22,53,32）供给，如以及冷却区（30）。废气和冷却介质基本上径向通过气体清洁区（20）和冷却区（30）中的床。

36. 发明申请

WO1990009839A1 FLUIDISED BED REACTOR WITH OBLIQUE FLOW THROUGH THE BED 审中-公开
标题翻译：流化床反应器具有通过床的OBLIQUE流动
公开(公告)号：WO1990009839A1
公开(公告)日：1990-09-07
申请号：PCT/EP1990000197
申请日：1990-02-07
申请人： BERGWERKSVERBAND GMBH , WÜNNENBERG, Wolfgang
发明人： BERGWERKSVERBAND GMBH
IPC分类号： B01D53/08
CPC分类号： B01D46/38 , B01D46/34 , B01D53/0446 , B01D53/08 , B01J8/12
摘要： Fluidised bed reactors with oblique flow through the bed, in which the bulk material runs through the reactor from top to bottom and is laterally restricted by main louvres between which the gas is fed in, whereby a gas-permeable retaining and guiding component (14) for bulk material particles is allocated to each louvre unit (17) of the louvre (23) on the downstream side. A secondary louvre unit (15, 19) may also be fitted in front of each main louvre unit (17).

37. 发明申请

WO1988003434A1 REACTOR WITH MOVING LAYER FOR THE REMOVAL OF UNDESIRABLE GASEOUS COMPONENTS FROM GASES 审中-公开
标题翻译：具有移动层的反应器，用于从气体中去除不可接受的气体组分
公开(公告)号：WO1988003434A1
公开(公告)日：1988-05-19
申请号：PCT/EP1987000639
申请日：1987-10-28
申请人： BERGWERKSVERBAND GMBH , BRÜGGENDICK, Hermann , WEBER, Raimond , RICHTER, Ekkehard , KNOPPIK, Berthold
发明人： BERGWERKSVERBAND GMBH
IPC分类号： B01D53/08
CPC分类号： B01J8/12 , B01D53/0446 , B01D53/08 , B01D2257/302 , B01D2257/404
摘要： In a reactor having a moving layer for the removal of undesirable gaseous components from gases, the gases pass diagonally through a downward moving layer of granular adsorption agents. The moving layer is isolated from the gas chambers by shutters and the reactor is narrower in the proximity of the inlet and outlet of adsorption agents, forming a distribution chamber and a discharge chamber for the granular adsorption agents. The distribution chamber (4) and the discharge chamber (5) are further provided on one of their sides with shutters (3, 3a), so that the gas chambers (11, 12) extend over the whole area of the shutters (3, 3a). A gas and adsorption agent conduit (6) is arranged on one side of the distribution chamber (4).
摘要翻译：在具有用于从气体中除去不需要的气体组分的移动层的反应器中，气体通过对角地通过向下移动的颗粒吸附剂层。移动层通过百叶窗与气室隔离，反应器在吸附剂入口和出口附近较窄，形成用于颗粒吸附剂的分配室和排放室。分配室（4）和排放室（5）还在其一侧上设置有闸门（3,3a），使得气室（11,12）在快门的整个区域上延伸，图3a）。气体和吸附剂导管（6）设置在分配室（4）的一侧。

38. 发明申请

WO1984003844A1 SEQUENCED MODULAR BED CAROUSEL DEHUMIDIFIER 审中-公开
标题翻译：顺序模块化卡车除湿器
公开(公告)号：WO1984003844A1
公开(公告)日：1984-10-11
申请号：PCT/US1984000485
申请日：1984-04-02
申请人： BRY-AIR, INC. , LEONARD, David, M.
发明人： BRY-AIR, INC.
IPC分类号： B01D53/08
CPC分类号： F24F3/1423 , B01D53/0431 , B01D53/06 , B01D53/261 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2253/116 , B01D2257/80 , B01D2259/40081 , B01D2259/4009 , F24F2203/1004 , F24F2203/1012 , F24F2203/1036 , F24F2203/1052 , F24F2203/1068 , F24F2203/108 , F24F2203/1096
摘要： In dehumidifying systems which produce a controlled humidity environment in an enclosed volume using a circular desiccant bed system, a problem encountered is that sections of the desiccant bed cannot be absolutely isolated with respect to a section in process use and a section subjected to heated reactivating air flow. A co-mingling of process air and heated reactivating air may occur due to sealing problems and imbalances between the two air streams. The invention utilizes a carousel ring (2) mounted in a box frame (1), with a plurality of axial modular desiccant beds (2a through 2g) which are separated from each other by angular dividers (11a through 11e). A sector divider (53, 54) is provided within the carousel to separate process air flow (98) and regeneration air flow (96) and to provide isolated process and regeneration chambers for air flow through groups of individual beds. The modular beds are cyclically shifted by an indexed linear actuator (6) in a process-reactivating-process cycle as the carousel ring rotates about central axle (4).
摘要翻译：在使用圆形干燥剂床系统在封闭体积中产生受控湿度环境的除湿系统中，遇到的问题是干燥剂床的部分不能相对于工艺用途的部分和经受加热的再生空气的部分绝对分离流。由于密封问题和两个空气流之间的不平衡，可能会发生过程空气和加热的再生空气的共混。本发明利用安装在盒框架（1）中的转盘环（2），其中多个轴向模块式干燥剂床（2a至2g）通过角度分隔器（11a至11e）相互分离。扇形分隔器（53,54）设置在转盘内以分离工艺空气流（98）和再生空气流（96），并提供隔离的过程和再生室，用于通过各组单独的床的气流。当转盘环绕中心轴（4）旋转时，模块化床在处理再活化处理循环中由分度线性致动器（6）循环移位。

39. 发明申请

WO2023079071A1 A DEVICE AND METHOD FOR PURIFYING EXHAUST GAS FROM A COMBUSTION PROCESS 审中-公开
公开(公告)号：WO2023079071A1
公开(公告)日：2023-05-11
申请号：PCT/EP2022/080806
申请日：2022-11-04
申请人： GROCHOWSKI, Horst
发明人： FRANZISKUS, Eddy-John
IPC分类号： B01D53/08 , B01D53/83
摘要： Embodiments of the present disclosure provide a device for purifying exhaust gas of a combustion process. The device comprises at least one multi-stage purification module, and each multi-stage purification module includes three or more purification modules, adsorption and/or absorption agent conveying pipeline systems, and intermediate plates between two adjacent purification modules. The purification modules are arranged in a sequentially stacked manner in the vertical direction, and can perform the purification of exhaust gas independently of each other. The adsorption and/or absorbent conveying pipeline system pentrates each multi-stage purification module, and is used to supply fresh adsorption and/or absorbent, and to discharge the used adsorption and/or absorbent from the purification module. The above device has the advantages of small floor space, high working efficiency and high flexibility.

40. 发明申请

WO2023067046A1 CO2 CAPTURE METHOD USING A COUNTERCURRENT MOVING BED REACTOR 审中-公开
公开(公告)号：WO2023067046A1
公开(公告)日：2023-04-27
申请号：PCT/EP2022/079177
申请日：2022-10-20
申请人： CONSEJO SUPERIOR DE INVESTIGACIONES CIENTÍFICAS (CSIC)
发明人： ABANADES GARCIA, Juan Carlos , ALVAREZ CRIADO, Yolanda
IPC分类号： B01D53/62 , B01D53/83 , B01D53/08
摘要： This invention discloses a method to capture CO2 from a gas using Ca-containing porous solids composed of Ca(OH)2 and/or CaO, arranged in a packed bed to contact with the gas. The method is characterized by the use of a carbonator reactor operated in a countercurrent moving bed mode. Such configuration provides the conditions to generate an autothermal central region in the reactor at optimum carbonation temperature between 600-700°C when using Ca-containing stones, pellets or extruded bricks with effective diameters or thickness between 1-10 cm and solid residence times between 1 to 20 hours, when treating gases with CO2 content between 2-25%v. In another embodiment, the method provides optimum conditions for efficient CO2 capture from gases with CO2 content below 2%v, including ambient air, at temperatures below 100°C and relative humidity between 80-100%, to achieve maximum carbonation conversion with solid residence times between 20 to 200 hours.

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