发明名称 |
CO2 RECOVERY APPARATUS AND CO2 RECOVERY METHOD |
摘要 |
A CO2 recovery apparatus provided with a CO2 absorption tower for making a purified exhaust gas and an absorbing liquid regeneration tower for regenerating a CO2 absorbing liquid by separating CO2 from the CO2 absorbing liquid, in which a lean solution removed of CO2 in the absorbing liquid regeneration tower is reused in the CO2 absorption tower, a cooling tower for cooling the CO2-containing exhaust gas containing CO2 is provided on the upstream flow side of the CO2 absorption tower so as to set a temperature (T2) of the purified exhaust gas exhausted from the CO2 absorption tower lower than a temperature (T1) of the CO2-containing exhaust gas containing CO2 cooled in the cooling tower (T1>T2), and a condensed water made by condensing water vapor discharged from the absorbing liquid regeneration tower is evaporated in an evaporation portion. |
申请公布号 |
US2014245888(A1) |
申请公布日期 |
2014.09.04 |
申请号 |
US201214236294 |
申请日期 |
2012.09.10 |
申请人 |
Tsujiuchi Tatsuya;Tanaka Hiroshi;Nagayasu Hiromitsu;Hirata Takuya;Oishi Tsuyoshi;Kamijo Takashi;Tatsumi Masahiko;Yagi Yasuyuki;Kaibara Kazuhiko |
发明人 |
Tsujiuchi Tatsuya;Tanaka Hiroshi;Nagayasu Hiromitsu;Hirata Takuya;Oishi Tsuyoshi;Kamijo Takashi;Tatsumi Masahiko;Yagi Yasuyuki;Kaibara Kazuhiko |
分类号 |
B01D53/14 |
主分类号 |
B01D53/14 |
代理机构 |
|
代理人 |
|
主权项 |
1. A CO2 recovery apparatus comprising:
a CO2 absorption tower for bringing a CO2-containing exhaust gas containing CO2 and a CO2 absorbing liquid into contact with each other so as to remove CO2 and make a purified exhaust gas; and an absorbing liquid regeneration tower for separating CO2 from the CO2 absorbing liquid which has absorbed CO2 so as to regenerate the CO2 absorbing liquid, wherein a lean solution from which CO2 has been removed in the absorbing liquid regeneration tower is reused in the CO2 absorption tower, wherein a cooling tower for cooling the CO2-containing exhaust gas containing CO2 is provided on a side of an upstream flow of the CO2 absorption tower and a temperature (T2) of the purified exhaust gas exhausted from the CO2 absorption tower is set to be lower than a temperature (T1) of the CO2-containing exhaust gas containing CO2 cooled in the cooling tower (T1>T2), and wherein an evaporation portion is configured to evaporate a condensed water made by condensing water vapor discharged from the absorbing liquid regeneration tower to outside. |
地址 |
Tokyo JP |