会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明授权
    • System and method for recovering carbon dioxide from flue gas
    • 从废气中回收二氧化碳的系统和方法
    • US08647420B2
    • 2014-02-11
    • US13081925
    • 2011-04-07
    • Hiroshi TsuboneToyoshi NakagawaTakashi KamijoTsuyoshi OishiKatsufumi InoueOsamu Miyamoto
    • Hiroshi TsuboneToyoshi NakagawaTakashi KamijoTsuyoshi OishiKatsufumi InoueOsamu Miyamoto
    • B01D53/14
    • B01D53/1425B01D2257/504Y02C10/04Y02C10/06
    • [Problem] To provide a system for recovering carbon dioxide from flue gas, in which a reboiler in a regenerator can be compactly installed, and a method therefor, in facilities where CO2 or the like contained in flue gas is recovered.[Solving Means] To include an absorber 1006 that absorbs CO2 contained in flue gas 1002, a regenerator 1008 that strips CO2 from CO2 absorbent (rich solution) 1007 to regenerate absorbent, internal shells 101 provided at a bottom of the regenerator 1008 with a predetermined interval therebetween, into which regenerated CO2 absorbent is introduced by a feeding unit 102 from a bottom side thereof so that the CO2 absorbent overflows from an upper end of the internal shell thereof toward the bottom of the regenerator, and a reboiler that is inserted into the internal shells 101 in a direction orthogonal to a vertical axis and includes a heat-transfer tube 103 that reboils absorbent. Steam separated from CO2 absorbent reboiled by the heat-transfer tube 103 is transferred to an upper part of a regenerator, condensed absorbent is caused to overflow from an upper end of the internal shell and to be discharged from a bottom side of a regenerator, and the absorbent is fed to the absorber 1006 as regenerated CO2 absorbent (lean solution) 1009.
    • [问题]提供一种回收二氧化碳的方法,其中回收器中的再沸器可以紧凑地安装在其中,并且其方法在烟道气中包含二氧化碳等的设备中回收二氧化碳。 为了包括吸收烟道气1002中包含的CO 2的吸收器1006,从CO 2吸收剂(富溶液)1007中吸收CO 2以再生吸收剂的再生器1008,设置在再生器1008的底部的内部壳体101具有预定的 其中再生的CO 2吸收剂由进料单元102从其底侧引入其中,使得CO 2吸收剂从其内壳的上端向再生器的底部溢出,并且将再沸器插入到再生器 在与垂直轴正交的方向上具有内壳101,并且包括再吸收吸收剂的传热管103。 与由热传输管103再沸腾的CO 2吸收器分离的蒸汽被转移到再生器的上部,使冷凝的吸收剂从内壳的上端溢出并从再生器的底侧排出, 吸收剂作为再生的CO 2吸收剂(贫溶液)1009被供给到吸收器1006。
    • 2. 发明申请
    • SYSTEM AND METHOD FOR RECOVERING CARBON DIOXIDE FROM FLUE GAS
    • 从气体回收二氧化碳的系统和方法
    • US20110250120A1
    • 2011-10-13
    • US13081925
    • 2011-04-07
    • Hiroshi TsuboneToyoshi NakagawaTakashi KamijoTsuyoshi OishiKatsufumi InoueOsamu Miyamoto
    • Hiroshi TsuboneToyoshi NakagawaTakashi KamijoTsuyoshi OishiKatsufumi InoueOsamu Miyamoto
    • C01B31/20B01D53/14
    • B01D53/1425B01D2257/504Y02C10/04Y02C10/06
    • [Problem] To provide a system for recovering carbon dioxide from flue gas, in which a reboiler in a regenerator can be compactly installed, and a method therefor, in facilities where CO2 or the like contained in flue gas is recovered.[Solving Means] To include an absorber 1006 that absorbs CO2 contained in flue gas 1002, a regenerator 1008 that strips CO2 from CO2 absorbent (rich solution) 1007 to regenerate absorbent, internal shells 101 provided at a bottom of the regenerator 1008 with a predetermined interval therebetween, into which regenerated CO2 absorbent is introduced by a feeding unit 102 from a bottom side thereof so that the CO2 absorbent overflows from an upper end of the internal shell thereof toward the bottom of the regenerator, and a reboiler that is inserted into the internal shells 101 in a direction orthogonal to a vertical axis and includes a heat-transfer tube 103 that reboils absorbent. Steam separated from CO2 absorbent reboiled by the heat-transfer tube 103 is transferred to an upper part of a regenerator, condensed absorbent is caused to overflow from an upper end of the internal shell and to be discharged from a bottom side of a regenerator, and the absorbent is fed to the absorber 1006 as regenerated CO2 absorbent (lean solution) 1009.
    • [问题]提供一种回收二氧化碳的方法,其中回收器中的再沸器可以紧凑地安装在其中,并且其方法在烟道气中包含二氧化碳等的设备中回收二氧化碳。 为了包括吸收烟道气1002中包含的CO 2的吸收器1006,从CO 2吸收剂(富溶液)1007中吸收CO 2以再生吸收剂的再生器1008,设置在再生器1008的底部的内部壳体101具有预定的 其中再生的CO 2吸收剂由进料单元102从其底侧引入其中,使得CO 2吸收剂从其内壳的上端向再生器的底部溢出,并且将再沸器插入到再生器 在与垂直轴正交的方向上具有内壳101,并且包括再吸收吸收剂的传热管103。 与由热传输管103再沸腾的CO 2吸收器分离的蒸汽被转移到再生器的上部,使冷凝的吸收剂从内壳的上端溢出并从再生器的底侧排出, 吸收剂作为再生的CO 2吸收剂(贫溶液)1009被供给到吸收器1006。