REGENERABLE SORBENT CO2 SCRUBBER FOR SUBMARINE VESSELS
    7.
    发明公开
    REGENERABLE SORBENT CO2 SCRUBBER FOR SUBMARINE VESSELS 审中-公开
    CO2-WÄSCHERMIT EINEM REGENERIERBAREN SORPTIONSMITTELFÜRÜBERWASSERFAHRZEUGE

    公开(公告)号:EP3001831A1

    公开(公告)日:2016-04-06

    申请号:EP14788461.3

    申请日:2014-04-23

    IPC分类号: B63G8/36

    摘要: Systems, devices and methods for submarine CO2 scrubbing are disclosed. The system may comprise an assembly including a sorbent, a scrubbing inlet configured to receive a first airflow during an adsorption mode. The first airflow may comprise air received from a cabin of a submarine. The assembly may be configured to flow the first airflow over and/or through the sorbent during the adsorption mode such that the sorbent removes a portion of CO2 entrained in the first airflow. The system may also include a scrubbing outlet configured to expel the scrubbed first airflow from the assembly into the cabin. The system may include an outside air inlet configured to receive a second airflow comprising outside air during a regeneration mode. The system may include a regeneration air outlet in configured to expel the second airflow after the second airflow has flowed over and/or through the sorbent during the regeneration mode.

    摘要翻译: 公开了用于潜水二氧化碳洗涤的系统,装置和方法。 系统可以包括组件,其包括吸附剂,被配置为在吸附模式期间接收第一气流的洗涤入口。 第一气流可以包括从潜艇的舱室接收的空气。 组件可以被配置为在吸附模式期间使第一气流流过吸附剂和/或通过吸附剂,使得吸附剂除去夹带在第一气流中的一部分CO 2。 系统还可以包括洗涤出口,该洗涤出口构造成将洗涤的第一气流从组件排出到舱室中。 该系统可以包括被配置为在再生模式期间接收包含外部空气的第二气流的外部空气入口。 系统可以包括再生空气出口,其被配置成在再生模式期间在第二气流已经流过和/或通过吸附剂之后排出第二气流。

    CO2 recovery apparatus and method
    10.
    发明授权
    CO2 recovery apparatus and method 有权
    CO 2回收设备和方法

    公开(公告)号:EP2269711B1

    公开(公告)日:2012-06-20

    申请号:EP09178598.0

    申请日:2009-12-10

    IPC分类号: B01D53/14

    摘要: A CO 2 recovering apparatus includes a CO 2 absorber (16) that brings flue gas containing CO 2 into contact with CO 2 absorbent to reduce the CO 2 contained in the flue gas; and a regenerator (18) that reduces CO 2 contained in rich solvent absorbing CO 2 to regenerate the rich solvent, so that lean solvent that is the CO 2 absorbent having the CO 2 reduced in the regenerator (18) is reused in the CO 2 absorber (16). The CO 2 recovering apparatus further includes a controller that detects the difference between the gas temperature (T 1 ) of the flue gas guided into the entrance of the CO 2 absorber (16) and the gas temperature (T 2 ) of the gas exiting the CO 2 absorber (16), and the absorbent concentration (X (Vol%)) of the CO 2 absorbent; and controls to adjust the amount of water contained in the gas depending on the gas temperature difference between the gas entering and the gas exiting the CO 2 absorber (16) and to keep the absorbent concentration of the CO 2 absorbent within a set range (e.g., X 0 ±10% in a relative ratio).