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    • 1. 发明专利
    • Co2 recovery apparatus and method
    • 二氧化碳回收装置和方法
    • JP2006232596A
    • 2006-09-07
    • JP2005047857
    • 2005-02-23
    • Kansai Electric Power Co Inc:TheMitsubishi Heavy Ind Ltd三菱重工業株式会社関西電力株式会社
    • KAMIJO TAKASHIIIJIMA MASAKIMIMURA TOMIOYAGI YASUYUKI
    • C01B32/50B01D53/14B01D53/62
    • B01D53/1425B01D53/1475F23J2219/40F23J2219/80Y02C10/06
    • PROBLEM TO BE SOLVED: To provide a CO
      2 recovery apparatus and a recovery method with improved energy efficiency.
      SOLUTION: The CO
      2 recovery apparatus has a CO
      2 absorption tower where flue gas containing CO
      2 is brought into contact with a CO
      2 absorption liquid to remove CO
      2 from the flue gas, and a regeneration tower where CO
      2 is removed from the rich solution which is the CO
      2 absorption liquid with CO
      2 absorbed therein to regenerate a lean solution which is a CO
      2 absorption liquid without absorption of CO
      2 , so as to reuse the lean solution from which CO
      2 is removed in the regeneration tower again in the absorption tower; wherein the apparatus is provided with a flow passage for extracting a semi-lean solution, temperature rising and returning, so as to extract at least a part of the semi-lean solution prepared by allowing a part of CO
      2 to emit from the rich solution injected into the regeneration tower from the upper part of the regeneration tower, from the regeneration tower, to elevate the temperature of the solution by heat exchange with a high temperature flue gas in a flue of an industrial equipment such as a boiler and a gas turbine, and to return the solution to the regeneration tower at a position lower than the semi-lean solution extraction position of the tower.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种具有改善的能量效率的CO 2 回收装置和回收方法。 解决方案:CO 2 回收装置具有CO 2 SB吸收塔,其中含有CO 2 的烟道气与CO 吸收液从烟道气中除去CO 2 ,从富CO溶液中除去CO SB SB2的再生塔,CO 吸收有CO 2 的SB SB吸附液再生贫CO 2 SB吸收液,而不吸收CO 2 / SB>,以便再次在吸收塔中重新利用在再生塔中除去CO 2 的贫溶液; 其中所述装置设置有用于提取半贫溶液,升温和返回的流动通道,以便提取通过使一部分CO 2
    • 3. 发明专利
    • Co2 recovery device and method
    • 二氧化碳回收装置和方法
    • JP2014033991A
    • 2014-02-24
    • JP2012176131
    • 2012-08-08
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社Kansai Electric Power Co Inc:The関西電力株式会社
    • TANAKA YUJINAGAYASU HIROTSUGUHIRATA TAKUYAOISHI GOJIKAMIJO TAKASHI
    • B01D53/62B01D53/14C01B32/50
    • B01D53/1425B01D53/1475B01D53/18B01D53/62B01D53/78B01D2252/204B01D2258/0283C01B32/50Y02C10/04Y02C10/06Y02P20/152
    • PROBLEM TO BE SOLVED: To provide a COrecovery device and method capable of reducing concentration of COabsorption liquid released while remaining in a decarboxylation exhaust gas.SOLUTION: A COrecovery device is provided for recovering and removing COin a COcontaining exhaust gas 11A containing the COin a COabsorption tower 13 using a COabsorption liquid 12. In the device, the COabsorption tower 13 includes:a COabsorbing section 13A for absorbing the COin the COcontaining exhaust gas; a main washing section 13C provided in the gas stream slip stream side of the COabsorbing section 13A and recovering the COabsorption liquid by a cleaning water 20 accompanying the COremoving exhaust gas, while cooling it, by the cleaning water 20; and a preliminary washing section 13B provided between the COabsorbing section 13A and the washing section 13C. A portion 20a of the cleaning water 20 containing the circulating COabsorption liquid is extracted in the main washing section 13C, and preliminarily washed in the preliminary washing section 13B. Also, the preliminary cleaning water is merged with the COabsorption liquid 12, while being made to directly flow down to the COabsorbing section 13A side.
    • 要解决的问题:提供一种能够在残留在脱羧废气中时减少释放的CO吸收液的浓度的COrecovery装置和方法。解决方案:提供一种COrecovery装置,用于回收和除去含有CO的CO含量废气11A的COin CO吸收 塔13使用CO吸收液12.在该装置中,CO吸收塔13包括:用于吸收CO含有废气的CO吸收部13A; 主洗涤部分13C,设置在CO吸收部分13A的气流滑流侧,并通过清洁水20在伴随排气的清洁水20中冷却CO回收液; 以及设置在CO吸收部13A和洗涤部13C之间的预备洗涤部13B。 含有循环的CO吸收液的清洗水20的部分20a在主洗涤部13C中被提取,并在预备清洗部13B中预先清洗。 此外,预先清洗水与CO吸收液12合并,直接向下流到CO吸收部13A侧。
    • 4. 发明专利
    • Carbon dioxide collection device and method
    • 二氧化碳收集装置和方法
    • JP2013039573A
    • 2013-02-28
    • JP2012248840
    • 2012-11-12
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社Kansai Electric Power Co Inc:The関西電力株式会社
    • KAMIJO TAKASHIIIJIMA MASAKIYONEKAWA TAKAHITOMIMURA TOMIOYAGI YASUYUKI
    • B01D53/14B01D53/34B01D53/62C01B32/50
    • Y02A50/2342Y02C10/04Y02C10/06Y02P20/124Y02P20/152Y02P20/57
    • PROBLEM TO BE SOLVED: To provide a COcollection device and method further improving energy efficiency.SOLUTION: The COcollection device has an absorption tower 13 for removing COby bringing a CO-containing gas 11 into contact with a CO-absorbing liquid 12, and a regeneration tower 15 for regenerating a CO-rich solution 14, wherein at the regeneration tower 15, a lean solution 16 in which CO2 is removed is reused in the absorption tower 13. Besides, the device is provided with: a regeneration heater 18 which extracts outside the lean solution 16 collected in the vicinity of the bottom of the tower 15 to perform a heat exchange by a high-temperature steam 17; and a heat exchanger 21 using a steam-condensed water, which is provided in a rich solution-feeding pipe 20 for feeding the rich solution 14 from the absorption tower 13 to the tower 15 and heats the rich solution 14 by utilizing the remaining heat of the steam-condensed water 19 from the heater 18.
    • 要解决的问题:提供一种进一步提高能量效率的CO 2 收集装置和方法。 解决方案:CO 2 收集装置具有一个吸收塔13,用于通过使一个CO 2 =“POST”> 2 的气体11与CO 2 吸收液体12接触,再生塔SB再生CO 2 富溶液14,其中在再生塔15处,其中除去CO 2的贫溶液16在吸收塔13中重新使用。此外,该装置设置有:再生加热器18 其在塔15的底部附近收集的贫溶液16外部提取,以通过高温蒸汽17进行热交换; 以及使用蒸汽冷凝水的热交换器21,其设置在富溶液供给管20中,用于将富溶液14从吸收塔13供给塔15,并通过利用剩余的热量加热富溶液14 来自加热器18的蒸汽冷凝水19.版权所有(C)2013,JPO&INPIT
    • 6. 发明专利
    • Co2 recovery device, and co2 recovery method
    • 二氧化碳回收装置和二氧化碳回收方法
    • JP2012236166A
    • 2012-12-06
    • JP2011107695
    • 2011-05-12
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社Kansai Electric Power Co Inc:The関西電力株式会社
    • TANAKA YUJINAGAYASU HIROTSUGUHIRATA TAKUYATSUJIUCHI TATSUYAOISHI GOJIKAMIJO TAKASHITATSUMI MASAHIKOYAGI YASUYUKIKAIHARA KAZUHIKO
    • B01D53/62B01D53/14B01D53/58C01B32/50C02F1/20
    • C01B31/20B01D53/1418B01D53/1475B01D2258/0283C01B32/50Y02C10/04Y02C10/06Y02P20/152
    • PROBLEM TO BE SOLVED: To provide a COrecovery device and COrecovery method, with which concentration of basic amine compounds discharged while remaining in decarbonation exhaust gas can be more reduced.SOLUTION: The COrecovery device includes a COabsorption unit 13A where COin CO-containing exhaust gas 11A is absorbed by COabsorption fluid 12, a water washing unit 13B where CO-removed exhaust gas 11B is cooled and further the COabsorption fluid 12 entrained in the gas 11B is recovered, a circulation line Lfor directly circulating washing water 20 from a top of the water washing unit 13B, an extraction line Lfor extracting a part of the washing water 20 including the COabsorption fluid 12 as extraction fluid 21, a first gas-fluid separation unit 22A for separating gas components 24 from the extraction fluid 21, a concentrating unit 22B which concentrates the COabsorption fluid 12 in the extraction fluid 21 and separates the gas components 24, a concentrated fluid returning line Lwhich returns concentrated fluid 23 obtained by concentrating the COabsorption fluid 12 to a COabsorption unit 13A side below the water washing unit 13B, and a gas inlet line Lfor introducing separated gas components 24 into an absorption tower 13.
    • 要解决的问题:提供CO 2 恢复装置和CO 2 恢复方法,其基本浓度 在脱碳废气中排出的胺化合物可以进一步降低。 解决方案:CO 2 恢复装置包括CO 2 吸收单元13A,其中CO 2 吸收流体12被吸收液体12吸收,> 2 单元13B,其中CO 2 - 移动废气11B被冷却,并且进一步夹带在气体11B中的CO 2 吸收流体12 回收,用于从洗涤单元13B的顶部直接循环洗涤水20的循环管线L 1 ,提取管线L 2 < SB>,用于提取包括作为萃取流体21的CO 2 吸收流体12的洗涤水20的一部分,用于将气体成分24从 萃取液21,浓缩单元22B,其将CO 吸收流体12集中在萃取流体21中并分离气体组分24,浓缩物 流体返回管线L 3 ,其返回通过将CO 2 吸收流体12浓缩到CO SB SB =“POST”> 2 吸收单元13A侧,以及用于将分离的气体成分24引入吸收塔的气体入口管线L 4 13.版权所有(C)2013,JPO&INPIT
    • 8. 发明专利
    • Co2 recovery device and co2 recovery method
    • 二氧化碳回收装置和二氧化碳回收方法
    • JP2013059727A
    • 2013-04-04
    • JP2011199883
    • 2011-09-13
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社Kansai Electric Power Co Inc:The関西電力株式会社
    • TSUJIUCHI TATSUYATANAKA YUJINAGAYASU HIROTSUGUHIRATA TAKUYAOISHI GOJIKAMIJO TAKASHITATSUMI MASAHIKOYAGI YASUYUKIKAIHARA KAZUHIKO
    • B01D53/62B01D53/14B01D53/34C01B32/50
    • B01D53/1418B01D53/1425B01D53/1475B01D53/62B01D2252/204B01D2252/20478B01D2258/0283Y02A50/2342Y02C10/04Y02C10/06
    • PROBLEM TO BE SOLVED: To provide a COrecovery device and a COrecovery method which can further reduce the concentration of amine compounds remained in a decarbonated exhaust gas and discharged.SOLUTION: The COrecovery device is provided with: a COabsorption unit 13A that absorbs COin CO-containing exhaust gas 11A by means of a CO-absorbing liquid 12; a water cleaning unit 13B that is provided to the top of the COabsorption unit 13A, cools the CO-eliminated exhaust gas, and recovers the associated CO-absorbing liquid 12; a cleaning liquid circulation line Lthat directly circulates a cleaning liquid 20 containing the CO-absorbing liquid 12 recovered at the water cleaning unit 13B, from the apex of the water cleaning unit 13B; an extraction line Lthat extracts a portion of the cleaning liquid 20 containing the CO-absorbing liquid 12 as an extraction liquid 21 from the cleaning liquid circulation line L; a concentration unit 22 that concentrates the CO-absorbing liquid while separating the gaseous component (water vapor) 24 from the extraction liquid 21; and a concentrated liquid feed line Lthat feeds the concentrated liquid 23 resulting from concentrating at the concentration unit 22 to an absorbing liquid regeneration tower 14 side.
    • 要解决的问题:提供一种CO 2 恢复装置和CO 2 恢复方法,其可以进一步减少 胺化合物的浓度保持在脱碳废气中并排出。

      解决方案:CO 2 恢复装置具有:吸收CO 2 的CO 2 的废气气体11A中的“=”POST“> 2 液体12; 设置在CO 2 吸收单元13A的顶部的水清洁单元13B冷却CO 2 气体,并回收相关的CO 2 吸收液体12; 直接循环包含在水中回收的CO 2 吸收液12的清洗液20的清洗液循环管线L 1 清洁单元13B,从水清洁单元13B的顶点; 萃取管线L 2 ,提取含有作为萃取液的CO SB SB = 2 / SB吸收液体12的清洗液20的一​​部分 21从清洗液循环管路L 1 ; 浓缩单元22,其将CO气体成分(水蒸气)24与提取液21分离,同时浓缩CO 2 吸收液; 以及将浓缩单元22浓缩而产生的浓缩液23供给到吸收液再生塔14侧的浓缩液体供给管线L