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    • 2. 发明公开
    • CO2 RECOVERY DEVICE AND OPERATION CONTROL METHOD OF CO2 RECOVERY DEVICE
    • CO2-RÜCKGEWINNUNGSVORRICHTUNGUND BETRIEBSSTEUERVERFAHRENFÜREINE CO2-RÜCKGEWINNUNGSVORRICHTUNG
    • EP2695662A1
    • 2014-02-12
    • EP11859860.6
    • 2011-08-25
    • Mitsubishi Heavy Industries, Ltd.
    • NAKAGAWA, Yosuke
    • B01D53/62C01B31/20
    • B01D53/1412B01D53/1475B01D53/62B01D2252/204B01D2257/504B01D2258/0283C01B32/50Y02C10/06Y02P20/152
    • A CO 2 recovering apparatus 10A according to this embodiment includes a cooling tower 11; a CO 2 absorber 12, a regenerator 13; an absorbing solution level meter 72 that measures the amount of liquid at a tower bottom of the CO 2 absorber 12; and a level controller 77 that performs automatic control or manual control for one or both of a supply amount of makeup water 76 and a condensation amount of water contained in an exhaust gas 15B based on the liquid amount of at the bottom of the CO 2 absorber 12 detected by the absorbing solution level meter 72. While the gas supply amount of the exhaust gas 15B is not changed, the level controller 77 is switched to the automatic control, and while the gas supply amount of the exhaust gas 15B is changed, the level controller 77 is switched to the manual control, thereby maintaining the supply amount of the makeup water 76 at a constant level.
    • 本实施方式的CO 2回收装置10A包括冷却塔11, CO 2吸收器12,再生器13; 吸收溶液液位计72,其测量CO 2吸收器12的塔底处的液体量; 以及水平控制器77,其基于CO 2吸收器的底部的液体量,对补充水76的供给量和排气15B中包含的水的冷凝量中的一个或两个进行自动控制或手动控制 当废气15B的气体供给量不改变时,电平控制器77切换到自动控制,而在排气15B的气体供给量改变的同时, 液位控制器77切换到手动控制,从而将补充水76的供给量保持在恒定水平。
    • 8. 发明公开
    • CO2 RECOVERY DEVICE AND CO2 RECOVERY METHOD
    • CO2回收装置和CO2回收方法
    • EP3187242A1
    • 2017-07-05
    • EP15819384.7
    • 2015-06-19
    • Mitsubishi Heavy Industries, Ltd.
    • NAKAGAWA, YosukeSHIMADA, DaisukeTSUJIUCHI, Tatsuya
    • B01D53/14B01D53/62C01B32/50B01D53/78F23J15/04
    • B01D53/1412B01D53/1425B01D53/1475B01D53/18B01D53/346B01D53/62B01D53/78B01D2252/20478B01D2256/22B01D2258/0283F23J15/04Y02A50/2342Y02C10/04Y02C10/06Y02E20/326
    • Provided are a CO 2 recovery unit and a CO 2 recovery method with which it is possible for a CO 2 recovery amount and/or a CO 2 recovery rate to be controlled with high accuracy towards a target value. This CO 2 recovery unit (1) is characterized by being equipped with: a CO 2 absorber (14) that causes CO 2 included in flue gas (11A) to be absorbed into a CO 2 -absorbing solution (13); a CO 2 -absorbing solution regenerator (15) which, by heating, regenerates the CO 2 -absorbing solution (13) that has absorbed the CO 2 ; a CO 2 recovery rate control unit which measures the CO 2 concentration in the flue gas (11A) and which, on the basis of the CO 2 concentration in the flue gas discharged from the CO 2 -absorbing solution (13) that has absorbed the CO 2 , changes the absorbing solution circulation amount and the amount of saturated steam (S) that is supplied to a regeneration heater (31); and a CO 2 recovery amount control unit which, in accordance with the CO 2 concentration of the flue gas (11A) and the flue gas flow rate, changes the circulation amount of the CO 2 -absorbing solution (13) and the amount of the saturated steam (S) supplied to the regeneration heater (31).
    • 本发明提供一种二氧化碳回收装置和二氧化碳回收方法,能够以高精度控制二氧化碳回收量和/或二氧化碳回收率,达到目标值。 该二氧化碳回收装置(1)的特征在于,具备:将吸收烟气(11A)中所含的二氧化碳吸收到二氧化碳吸收液(13)中的二氧化碳吸收器(14)。 CO 2吸收液再生器(15),其通过加热使吸收了CO 2的CO 2吸收液(13)再生; 测量废气(11A)中的二氧化碳浓度并且基于从已吸收二氧化碳的二氧化碳吸收溶液(13)排出的废气中的二氧化碳浓度的二氧化碳回收率控制单元改变 吸收液循环量和供给到再生加热器的饱和蒸汽量(S)。 以及CO2回收量控制单元,其根据烟气(11A)的CO2浓度和烟气流量,改变CO 2吸收溶液(13)的循环量和饱和蒸汽量( S)提供给再生加热器(31)。