Acid gas absorbent, acid gas removal method, and acid gas removal device
    5.
    发明公开
    Acid gas absorbent, acid gas removal method, and acid gas removal device 审中-公开
    Säuregas吸收剂,SäuregasentfernungsverfahrenundSäuregasentfernungsvorrichtung

    公开(公告)号:EP2529824A1

    公开(公告)日:2012-12-05

    申请号:EP12169120.8

    申请日:2012-05-23

    IPC分类号: B01D53/14

    摘要: There is provided an acid gas absorbent having excellent performance of absorbing acid gas such as carbon dioxide, and an acid gas removal device and an acid gas removal method using the acid gas absorbent. An acid gas absorbent of an embodiment contains at least one type of tertiary amine compound represented by the following general formula (1).

    (In the above formula (1), the cycle A represents a cyclic structure whose carbon number is not less than 3 nor more than 8. R 1 ,R 2 and R 3 each represent an alkyl group whose carbon number is 1 to 4, and R 4 represents a hydroxyalkyl group. R 1 and R 2 are groups coupled to carbon atoms adjacent to a carbon atom forming the cycle A and coupled to a nitrogen atom.)

    摘要翻译: 提供一种具有优异吸收二氧化碳等酸性气体性能的酸性气体吸收剂,使用酸性气体吸收剂的酸性气体除去装置和酸性气体除去方法。 实施方案的酸性气体吸收剂含有至少一种由以下通式(1)表示的叔胺化合物。 (式(1)中,A为碳数为3以上8以上的环状结构。R 1,R 2,R 3各自为碳原子数为1〜4的烷基, 并且R 4表示羟烷基,R 1和R 2是与形成环A的碳原子相邻的碳原子连接并与氮原子偶合的基团。

    CARBON DIOXIDE RECOVERY APPARATUS AND CARBON DIOXIDE RECOVERY METHOD - ABSORBENT REGENERATION INVOLVING PHASE SEPARATION
    9.
    发明公开
    CARBON DIOXIDE RECOVERY APPARATUS AND CARBON DIOXIDE RECOVERY METHOD - ABSORBENT REGENERATION INVOLVING PHASE SEPARATION 审中-公开
    二氧化碳回收设备和二氧化碳回收过程 - 吸收性再生析相

    公开(公告)号:EP2933008A1

    公开(公告)日:2015-10-21

    申请号:EP15162089.5

    申请日:2015-03-31

    IPC分类号: B01D53/14 F23J15/00

    摘要: The CO 2 recovery apparatus 10A includes: an absorption tower 11 in which a discharge gas 21 is contacted with a second lean solution 22B to allow the second lean solution 22B to absorb CO 2 ; a temperature regulator 12 in which a first rich solution 23A discharged from the absorption tower is heated or cooled to allow the first rich solution 23A to be a solution in which a precipitate containing the reaction accelerator is dispersed; a phase separator 13 in which a second rich solution 23B passed through the temperature regulator 12 is separated into an amino group-containing compound rich phase 31 and a reaction accelerator rich phase 32; a regeneration tower 15 in which a third rich solution 23C is regenerated; and a solution mixing line L13A through which a reaction accelerator rich solution 34 is supplied to a first lean solution 22A discharged from the regeneration tower 15.

    摘要翻译: 的CO 2回收设备10A包括:吸收塔11,其中放电气体21与第二贫溶液22B,以允许第二贫溶液22B以吸收CO 2接触; 温度调节器12,其中从吸收塔排出的第一富溶液23A被加热或冷却,以允许第一富溶液23A是在其中将含有反应促进剂的沉淀物分散的溶液; 相分离器13,其中第二富溶液23B通过温度调节器12通过被分离成以含氨基的化合物富集相31和反应促进剂富集相32; 再生塔15,其中第三富液再生23C; 和溶液混合线L13A,通过该反应促进剂富溶液34被供给到从再生塔15日排出的第一贫溶液22A