CO2 recovery apparatus and CO2 recovery method

Patent metadata

Field	Value
Publication number	US-9421491-B2
Application number	US-201214235636-A
Country	US
Kind code	B2
Filing date	Sep 10, 2012
Priority date	Sep 13, 2011
Publication date	Aug 23, 2016
Grant date	Aug 23, 2016

Abstract

The CO 2 recovery apparatus is provided with a CO 2 absorption portion for absorbing CO 2 in a CO 2 -containing exhaust gas by a CO 2 absorbing liquid, a water washing portion provided on the upper portion side of the CO 2 absorption portion so as to cool a CO 2 -removed exhaust gas and also recover the accompanying CO 2 absorbing liquid, a washing liquid circulation line for directly circulating a washing liquid containing the CO 2 absorbing liquid recovered in the water washing portion, an extraction line for extracting part of the washing liquid containing the CO 2 absorbing liquid as an extracted liquid from the washing liquid circulation line, a concentration portion for separating a gas component (water vapor) from the extracted liquid while concentrating the CO 2 absorbing liquid, and a concentrated liquid feed line for feeding a concentrated liquid concentrated in the concentration portion to the side of an absorbing liquid regeneration tower.

First claim

The invention claimed is:

1. A CO 2 recovery apparatus comprising:
a CO 2 absorption tower for bringing a CO 2 -containing exhaust gas and a CO 2 absorbing liquid into contact with each other so as to remove CO 2 and make a purified exhaust gas; and
an absorbing liquid regeneration tower for separating CO 2 from the CO 2 absorbing liquid which has absorbed CO 2 so as to regenerate the CO 2 absorbing liquid,
wherein a lean solution from which CO 2 has been removed in the absorbing liquid regeneration tower is reused in the CO 2 absorption tower, and
wherein the CO 2 absorption tower comprises:
a CO 2 absorption portion for absorbing CO 2 in the CO 2 -containing exhaust gas by the CO 2 absorbing liquid,
a water washing portion for cooling a CO 2 -removed exhaust gas by a washing liquid and for recovering the CO 2 absorbing liquid which accompanies the CO 2 -removed exhaust gas, the water washing portion being provided downstream of the CO 2 absorption portion;
a washing liquid circulation line for supplying the washing liquid containing the CO 2 absorbing liquid recovered in the water washing portion to a side of a top of the water washing portion so as to circulate and wash the washing liquid;
an extraction line for extracting a part of the washing liquid containing the CO 2 absorbing liquid as an extracted liquid from the washing liquid circulation line;
a concentration portion for concentrating the CO 2 absorbing liquid while separating a gas component from the extracted liquid so as to produce a concentrated liquid;
a separation drum for separating a CO 2 gas accompanied by water vapor from an upper portion of the absorbing liquid regeneration tower so as to produce a condensed water; and
a concentrated liquid feed line for connecting between the concentration portion and the upper portion of the absorbing liquid regeneration tower and feeding the concentrated liquid from the concentration portion directly to the upper portion of the absorbing liquid regeneration tower.

2. The CO 2 recovery apparatus according to claim 1 , further comprising a gas exhaust line for merging the gas component into the purified exhaust gas exhausted from the CO 2 absorption tower.

3. The CO 2 recovery apparatus according to claim 1 , further comprising a cooling tower for cooling the CO 2 -containing exhaust gas so as to set a temperature (T 2 ) of the purified exhaust gas exhausted from the CO 2 absorption tower lower than a temperature (T 1 ) of the CO 2 -containing exhaust gas containing CO 2 cooled in the cooling tower (T 1 >T 2 ), the cooling tower being provided upstream of the CO 2 absorption tower.

4. The CO 2 recovery apparatus according to claim 1 wherein a water is supplied to the water washing portion from an outside or an inside of a system.

5. A CO 2 recovery method for using a CO 2 absorption tower for removing CO 2 by bringing a CO 2 -containing exhaust gas and a CO 2 absorbing liquid into contact with each other so as to remove CO 2 and an absorbing liquid regeneration tower for regenerating the CO 2 absorbing liquid by separating CO 2 from the CO 2 absorbing liquid absorbing CO 2 so as to reuse a lean solution from which CO 2 has been removed in the absorbing liquid regeneration tower in the CO 2 absorption tower,
the CO 2 recovery method comprising:
downstream of the CO 2 absorption tower, cooling a CO 2 -removed exhaust gas with a washing liquid and recovering the CO 2 absorbing liquid accompanied by CO 2 -removed exhaust gas;
supplying the washing liquid containing CO 2 absorbing liquid recovered in a water washing portion to a side of a top of the water washing portion so as to circulate and wash the washing liquid;
extracting a part of the washing liquid containing the CO 2 absorbing liquid as an extracted liquid;
concentrating the CO 2 absorbing liquid contained in the extracted liquid as a concentrated liquid;
separating a CO 2 gas accompanied by water vapor from the absorbing the absorbing liquid regeneration tower so as to produce a condensed water; and
feeding the concentrated liquid directly to an upper portion of the absorbing liquid regeneration tower.

Assignees

• Tsujiuchi Tatsuya
• Tanaka Hiroshi
• Nagayasu Hiromitsu
• Hirata Takuya
• Oishi Tsuyoshi
• Kamijo Takashi
• Tatsumi Masahiko
• Yagi Yasuyuki
• Kaibara Kazuhiko
• Mitsubishi Heavy Ind Ltd
• Kansai Electric Power Co

Inventors

• Tsujiuchi Tatsuya
• Tanaka Hiroshi
• Nagayasu Hiromitsu
• Hirata Takuya
• Oishi Tsuyoshi
• Kamijo Takashi
• Tatsumi Masahiko
• Yagi Yasuyuki
• Kaibara Kazuhiko

Classifications

• B01D53/62

  Carbon oxides · CPC title

• B01D2252/204

  Amines · CPC title

• B01D2252/20478

  Alkanolamines · CPC title

• Y02C10/06

  Cross-Sectional Technologies · mapped topic

• B01D2258/0283

  Flue gases · CPC title