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公开(公告)号：EP2659948A1
公开(公告)日：2013-11-06
申请号：EP11844393.6
申请日：2011-07-27
CPC分类号： B01D53/1425 , B01D53/1475 , B01D2259/65 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02E20/326
摘要： A CO2 recovery system according to the present invention includes: a CO 2 absorber (16) that brings a cooled CO 2 -containing exhaust gas (12) into contact with a CO 2 -absorbent (15) that absorbs CO 2 , thereby removing the CO 2 from the exhaust gas (12); an absorbent regenerator (18) that releases CO 2 from a CO 2 -absorbent that has absorbed CO 2 (rich solution) (17), thereby regenerating the absorbent (15); and a lean solution temperature-reduction unit (50) that recovers heat from a lean solution (15) discharged from the absorbent regenerator (18).
摘要翻译： 根据本发明的CO 2回收系统包括：CO 2吸收器（16），其使冷却的含CO 2排气（12）与吸收CO 2的CO 2吸收剂（15）接触，从而从排气中除去CO 2 气体（12）; 吸收再生器（18），其从已经吸收CO 2（富溶液）（17）的CO 2吸收剂释放CO 2，由此使吸收剂（15）再生; 以及从吸收再生器（18）排出的贫溶液（15）回收热量的贫溶液降温部（50）。
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2.发明公开
公开(公告)号：EP2612698A1
公开(公告)日：2013-07-10
申请号：EP11821465.9
申请日：2011-07-26
CPC分类号： B01D53/1425 , B01D53/1406 , B01D53/1468 , B01D53/1475 , Y02A50/2342 , Y02C10/06
摘要： In a reclaiming apparatus (106) that includes an airtight container (106a) as an absorbent storing unit that stores a part of an absorbent that absorbs CO 2 included in an exhaust gas and a heating unit that heats the absorbent stored in the airtight container (106a), a part of the absorbent stored in the airtight container (106a) is distributed, and a gaseous body is brought into counterflow contact with the absorbent that is distributed. As a result, since the gaseous body is brought into counterflow contact with a part of the absorbent stored in the absorbent storing unit, an absorbent component volatilizes and is separated from a degraded material, and the absorbent component can be extracted from the degraded material, whereby a loss of the absorbent can be reduced.
摘要翻译： 在一种回收设备（106）中，该回收设备（106）包括作为吸收剂储存单元的气密容器（106a），其存储吸收废气中包含的CO 2的吸收剂的一部分，以及加热容纳在密封容器中的吸收剂的加热单元 106a）中分配存储在气密容器（106a）中的吸收剂的一部分，并且使气体与分配的吸收剂逆流接触。 结果，由于气体与存储在吸收剂存储单元中的吸收剂的一部分进行逆流接触，所以吸收组分挥发并与劣化材料分离，并且可以从降解材料中提取吸收组分， 从而可以减少吸收剂的损失。
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3.发明公开CO2 RECOVERY DEVICE AND CO2 RECOVERY METHOD 审中-公开CO2-RÜCKGEWINNUNGSVORRICHTUNGUND CO2-RÜCKGEWINNUNGSVERFAHREN
公开(公告)号：EP2767328A1
公开(公告)日：2014-08-20
申请号：EP12831224.6
申请日：2012-09-10
发明人： TSUJIUCHI, Tatsuya , TANAKA, Hiroshi , NAGAYASU, Hiromitsu , HIRATA, Takuya , OISHI, Tsuyoshi , KAMIJO, Takashi , TATSUMI, Masahiko , YAGI, Yasuyuki , KAIBARA, Kazuhiko
CPC分类号： B01D53/1418 , B01D53/1425 , B01D53/1475 , B01D53/62 , B01D2252/204 , B01D2252/20478 , B01D2258/0283 , Y02A50/2342 , Y02C10/04 , Y02C10/06
摘要： The CO 2 recovery apparatus is provided with a CO 2 absorption portion 13A for absorbing CO 2 in a CO 2 -containing exhaust gas 11A by a CO 2 absorbing liquid 12, a water washing portion 13B provided on the upper portion side of the CO 2 absorption portion 13A so as to cool a CO 2 -removed exhaust gas and also recover the accompanying CO 2 absorbing liquid 12, a washing liquid circulation line L 1 for directly circulating a washing liquid 20 containing the CO 2 absorbing liquid 12 recovered in the water washing portion 13B from the top of the water washing portion 13B, an extraction line L 2 for extracting part of the washing liquid 20 containing the CO 2 absorbing liquid 12 as an extracted liquid 21 from the washing liquid circulation line L 1 , a concentration portion 22 for separating a gas component (water vapor) 24 from the extracted liquid 21 while concentrating the CO 2 absorbing liquid, and a concentrated liquid feed line L 3 for feeding a concentrated liquid 23 concentrated in the concentration portion 22 to the side of an absorbing liquid regeneration tower 14.
摘要翻译： CO 2回收装置设置有CO 2吸收部13A，其通过CO 2吸收液12吸收含CO 2的废气11A中的CO 2，设置在CO 2的上部侧的水洗部13B 吸收部13A，以冷却排出的二氧化碳的二氧化碳，还回收伴随的二氧化碳吸收液12，使回收在水中的含有二氧化碳吸收液12的洗涤液20直接循环的洗涤液循环管道L 1 从洗涤部分13B的顶部的清洗部分13B，提取管线L 2，用于从洗涤液循环管线L 1中提取含有作为提取液体21的CO 2吸收液体12的洗涤液20的一部分， 22，用于在浓缩CO 2吸收液体的同时从提取液体21中分离气体成分（水蒸气）24;以及浓缩液体供给管线L 3，其将浓缩液 浓缩部分22到吸收液体再生塔14的侧面。
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公开(公告)号：EP2719441A1
公开(公告)日：2014-04-16
申请号：EP12782974.5
申请日：2012-05-10
发明人： TANAKA, Hiroshi , NAGAYASU, Hiromitsu , HIRATA, Takuya , TSUJIUCHI, Tatsuya , OISHI, Tsuyoshi , KAMIJO, Takashi , TATSUMI, Masahiko , YAGI, Yasuyuki , KAIBARA, Kazuhiko
CPC分类号： C01B31/20 , B01D53/1418 , B01D53/1475 , B01D2258/0283 , C01B32/50 , Y02C10/04 , Y02C10/06 , Y02P20/152
摘要： A CO 2 recovery device includes: a CO 2 absorption unit (13A) for absorbing CO 2 , which is contained in a CO 2 -containing flue gas (11A), by a CO 2 absorbent (12); a washing unit (13B) for cooling a CO 2 -removed flue gas (11B) and recovering the accompanying CO 2 absorbent (12); a circulation line (L 1 ) for directly circulating wash water (20) from the top portion of the washing unit (13B); an extraction line (L 2 ) for extracting a part of the wash water (20) containing the CO 2 absorbent (12) as an extracted fluid (21); a first gas-liquid separation unit (22A) for separating a gas component (24) from the extracted fluid (21); a concentration unit (22B) for concentrating the CO 2 absorbent (12) contained in the extracted fluid (21) and separating the gas component (24); a concentrated fluid return line (L 3 ) through which a concentrated fluid (23), which is the concentrated CO 2 absorbent (12), returns to the CO 2 absorption unit (13A) provided below the washing unit (13B); and a gas inlet line (L 4 ) through which the separated gas component (24) is introduced into an absorber (13).
摘要翻译： 一种CO 2回收装置，其特征在于，具备：CO2吸收器（12），吸收包含在含有CO 2的排气（11A）中的CO 2的CO 2吸收器（13A）。 洗涤单元（13B），用于冷却除去CO 2的烟道气（11B）并回收伴随的CO 2吸收剂（12）; 循环管线（L1），用于从清洗单元（13B）的顶部直接循环洗涤水（20）; 提取管线（L2），用于提取含有CO 2吸收剂（12）作为提取液（21）的洗涤水（20）的一部分; 第一气液分离单元（22A），用于将气体成分（24）与提取液（21）分离; 浓缩装置（22B），用于浓缩提取流体（21）中所含的CO 2吸收剂（12）并分离气体组分（24）; 作为浓缩CO2吸收剂（12）的浓缩液（23）返回到设置在清洗单元（13B）的下方的CO 2吸收单元（13A）的浓缩液返回线路（L3）。 和将分离的气体组分（24）引入吸收器（13）中的气体入口管线（L4）。
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公开(公告)号：EP2659949A1
公开(公告)日：2013-11-06
申请号：EP11845355.4
申请日：2011-07-27
CPC分类号： B01D53/1425 , B01D53/1475 , B01D2252/204 , B01D2258/0283 , B01D2259/65 , Y02C10/04 , Y02C10/06 , Y02E20/326
摘要： A CO 2 recovery system according to the present invention includes: a cooling tower (14) that uses cooling water (13) to cool a CO 2 -containing exhaust gas (12) discharged from industrial equipment such as a boiler (11) or a gas turbine; a CO 2 absorber (16) that brings the cooled CO 2 -containing exhaust gas (12) into contact with a CO 2 -absorbent (15) that absorbs CO 2 , thereby removing the CO 2 from the exhaust gas (12); and a first absorbent regenerator (18-1) and a second absorbent regenerator (18-2) that release CO 2 from a CO 2 -absorbent that has absorbed CO 2 (rich solution) (17), thereby regenerating the CO 2 -absorbent (15). A second lean solution at the outlet of the second absorbent regenerator is subjected to vacuum flash vaporization, and the resulting vapor is inputted to the first absorbent regenerator.
摘要翻译： 根据本发明的CO 2回收系统包括：冷却塔（14），其使用冷却水（13）来冷却从诸如锅炉（11）的工业设备排出的含CO 2的废气（12） 燃气轮机; 使冷却的含CO 2的废气（12）与吸收CO 2的吸收剂（15）接触，从而从废气（12）除去CO 2的CO 2吸收器（16）。 以及从吸收了CO 2（富溶液）（17）的CO 2吸收剂中释放CO 2的第一吸收剂再生器（18-1）和第二吸收剂再生器（18-2），从而再生所述CO 2吸收剂 （15）。 在第二吸收性再生器的出口处的第二贫溶液经受真空闪蒸，并将所得蒸气输入到第一吸收性再生器。
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6.发明授权
公开(公告)号：EP1872846B1
公开(公告)日：2013-07-24
申请号：EP06731002.9
申请日：2006-04-03
发明人： MIMURA, Tomio , YAGI, Yasuyuki , OGURA, Kouki , IIJIMA, Masaki , TAKASHINA, Toru , TANAKA, Hiroshi , HIRATA, Takuya
IPC分类号： C07C209/90
CPC分类号： B01D53/1493 , B01D53/1462 , B01D53/526 , B01D2252/103 , B01D2252/20405 , B01D2252/2041 , B01D2252/20421 , B01D2252/20426 , B01D2252/20431 , B01D2252/20447 , B01D2252/20489 , B01D2252/504 , B01D2252/604 , B01D2256/24 , B01D2258/06 , C10L3/10 , Y02C10/06
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公开(公告)号：EP2327467A1
公开(公告)日：2011-06-01
申请号：EP09712867.2
申请日：2009-02-20
发明人： TANAKA, Hiroshi , TAKASHINA, Toru , OISHI, Tsuyoshi , IIJIMA, Masaki , MIMURA, Tomio , OGURA, Kouki , YAGI, Yasuyuki
CPC分类号： B01D53/1412 , B01D53/1475 , B01D53/62 , B01D2252/204 , B01D2256/22 , B01D2257/504 , B01D2258/0283 , B01D2259/652 , F23J15/04 , F23J2215/50 , F23J2219/40 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02E20/326
摘要： A CO 2 recovery apparatus according to the present invention includes: an absorber (1003) that brings CO 2 -containing flue gas (1001A) into counter-current contact with CO 2 absorbent (1002) to reduce CO 2 , and a regenerator (1005) that regenerates rich solution (1004) that has absorbed CO 2 , in which lean solution (1006) having CO 2 reduced in the regenerator (1005) is reused in the absorber (1003). The absorber (1003) further includes a CO 2 absorbing unit (1010) that recovers CO 2 contained in the flue gas (1001A), and the CO 2 absorbent (1002) that has absorbed CO 2 is extracted from a rich side of the CO 2 absorbing unit (1010) to exterior, cooled, and then supplied to a position nearer to a lean side of the absorber (1003) with respect to the position at which the CO 2 absorbent (1002) is extracted.
摘要翻译： 雅丁到本发明的CO 2回收设备，包括：一个吸收器（1003）做了带来含有CO 2的烟道气（1001A）成逆流接触用CO 2吸收剂（1002），以降低CO 2，和一个再生器（1005 ）做再生富溶液（1004）做了已吸收的CO 2，其中贫液（1006），其具有的CO 2在再生器（1005）减小在吸收器（1003）被再利用。 吸收器（1003）还包括CO 2吸收单元（1010）做了恢复其中所含的烟道气（1001A）中的CO 2，和CO 2吸收剂（1002）做了已吸收的CO 2从CO的浓侧提取 2吸收单元（1010）到外部，冷却，然后相对于提供到更近的位置到吸收器（1003）的稀侧到使CO 2吸收（1002）被提取的位置。
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8.发明授权
公开(公告)号：EP2279996B1
公开(公告)日：2015-12-23
申请号：EP08874481.8
申请日：2008-10-24
申请人： Mitsubishi Heavy Industries, Ltd. , The Kansai Electric Power Co., Inc. , Nippon Nyukazai Co., Ltd.
发明人： TSUJIUCHI, Tatsuya , TACHIBANA, Shinya , OISHI, Tsuyoshi , MIMURA, Tomio , YAGI, Yasuyuki , MITA, Hidehisa , ARAKI, Ryosuke , SAITO, Kenji
IPC分类号： C07C213/04 , C07C213/10 , C07C215/08
CPC分类号： C07C213/10 , C07C213/04 , C07C215/08
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9.发明公开3-COMPONENT ABSORBENT SOLUTION, AND CO2 AND/OR H2S REMOVAL DEVICE AND METHOD 审中-公开三，电子元件与CO2和/或H2S去除装置和方法的吸收液
公开(公告)号：EP2769759A1
公开(公告)日：2014-08-27
申请号：EP12842195.5
申请日：2012-10-17
CPC分类号： B01D53/526 , B01D53/1462 , B01D53/1493 , B01D53/62 , B01D2252/20405 , B01D2252/2041 , B01D2252/20426 , B01D2252/20431 , B01D2252/20447 , B01D2252/20484 , B01D2252/504 , Y02C10/04 , Y02C10/06
摘要： A first amine, which is a straight chain secondary monoamine, 2) a second amine, which is a cyclic secondary polyamine as a reaction accelerator, and 3) a third amine, which is an amine consisting of one selected from a cyclic amine group constituted from a secondary or tertiary amino group or a straight chain amine group with high steric hindrance are mixed to obtain an absorbent. By the synergistic effect thereof, absorption properties to CO 2 and/or H 2 S are excellent and the absorbed CO 2 or H 2 S emission properties during the regeneration of the absorbent become excellent. Therefore, the water vapor amount used during the regeneration of the absorbent in CO 2 recovery equipment can be reduced.
摘要翻译： 第一胺，所有这些是直链仲单胺，2）第二胺，所有这些是环状仲多胺作为反应促进剂，和3）第三胺，所有这些是胺由......组成一个由环状胺组中选择的构成 从一个仲或叔氨基基团或具有高空间位阻的直链胺基混合，得到吸水。 通过协同效应物，吸收特性为CO 2和/或H 2 S是优异的和吸收性变得良好的再生过程中吸收的CO 2或H 2 S的发光特性。 因此，在CO 2回收设备吸收剂的再生过程中使用的水蒸汽量可被减少。
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公开(公告)号：EP2540381A1
公开(公告)日：2013-01-02
申请号：EP11747084.9
申请日：2011-01-11
发明人： TSUJIUCHI, Tatsuya , NAGAYASU, Hiromitsu , HIRATA, Takuya , FUJIKAWA, Keiji , IMAI, Tetsuya , TANAKA, Hiroshi , OISHI, Tsuyoshi , TATSUMI, Masahiko , YAGI, Yasuyuki , KAIBARA, Kazuhiko
CPC分类号： B01D53/1425 , B01D53/1475 , B01D2252/204 , B01D2257/302 , B01D2258/0283 , F23G2207/104 , F23J15/006 , F23J15/04 , F23J15/06 , F23J2215/20 , F23J2219/40 , F23L7/002 , F23L15/04 , Y02A50/2342 , Y02C10/06 , Y02E20/326 , Y02E20/348
摘要： A CO 2 recovery unit includes an absorber that reduces CO 2 in flue gas (101) discharged from a combustion facility (50) by absorbing CO 2 by an absorbent, a regenerator that heats the absorbent having absorbed CO 2 to emit CO 2 , and regenerates and supplies the absorbent to the absorber, and a regenerating heater that uses steam (106) supplied from the combustion facility (50) for heating the absorbent in the regenerator and returns heated condensed water (106a) to the combustion facility (50). The CO 2 recovery unit further includes a condensed water/flue gas heat exchanger (57) that heats the condensed water (106a) to be returned from the regenerating heater to the combustion facility (50) by heat-exchanging the condensed water (106a) with the flue gas (101) in a flue gas duct (51) in the combustion facility (50).
摘要翻译： 甲CO 2回收单元包括：在吸收体那样通过在吸收性吸收CO 2通过从燃烧设备（50）排出的废气（101）中减少CO 2，再生器确实加热吸收剂具有吸收的CO 2以发射CO 2，和 再生和吸收供给到吸收器，和一个再生加热器那样使用从燃烧设备（50）供给的蒸汽（106），用于加热所述吸收剂在再生器中，并返回加热冷凝水（106A）到燃烧设备（50）。 的CO 2回收单元进一步包括：（57）那样进行加热的冷凝水（106A），以从再生加热器的燃烧设备（50）通过返回一个冷凝水/烟气热交换器进行热交换的冷凝水（106A） 与在燃烧设备（50）中的烟道气管道（51）的烟道气（101）。
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