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    • 19. 发明申请
    • CO2 RECOVERING APPARATUS AND METHOD
    • 二氧化碳回收装置和方法
    • US20100322842A1
    • 2010-12-23
    • US12633410
    • 2009-12-08
    • Masaki IijimaHiroshi TanakaYoshiki SorimachiKouki OguraMasahiko TatsumiYasuyuki Yagi
    • Masaki IijimaHiroshi TanakaYoshiki SorimachiKouki OguraMasahiko TatsumiYasuyuki Yagi
    • C01B31/20B01D53/14
    • B01D53/1412B01D53/1475B01D53/77B01D2251/80B01D2257/504Y02C10/06
    • A CO2 recovering apparatus includes a CO2 absorber that brings flue gas containing CO2 into contact with CO2 absorbent to reduce the CO2 contained in the flue gas; and a regenerator that reduces CO2 contained in rich solvent absorbing CO2 to regenerate the rich solvent, so that lean solvent that is the CO2 absorbent having the CO2 reduced in the regenerator is reused in the CO2 absorber. The CO2 recovering apparatus further includes a controller that detects a difference between a gas temperature (T1) of the flue gas guided into an entrance of the CO2 absorber and a gas temperature (T2) of the gas exiting the CO2 absorber, and an absorbent concentration (X (Vol %)) of the CO2 absorbent; and controls to adjust an amount of water contained in the gas depending on the gas temperature difference between the gas entering and the gas exiting the CO2 absorber and to keep an absorbent concentration of the CO2 absorbent within a set range (e.g., X0±10% in a relative ratio).
    • CO 2回收装置包括CO 2吸收器,其将含有CO 2的烟道气与CO 2吸收剂接触以减少烟道气中所含的CO 2; 以及再生器,其减少富含溶剂的CO 2中包含的CO以再生富溶剂,使得在再生器中减少的CO 2吸收剂的贫溶剂在CO 2吸收器中再次使用。 CO 2回收装置还包括控制器,该控制器检测引导到CO 2吸收器的入口的烟道气的气体温度(T1)与离开CO 2吸收器的气体的气体温度(T2)之间的差异,以及吸收剂浓度 (X(vol%)); 并且根据气体进入和离开CO 2吸收器的气体之间的气体温度差来控制气体中所含的水量,并且将CO 2吸收剂的吸收剂浓度保持在设定范围内(例如,X 0±10% 相对比例)。