CO2 recovery device and CO2 recovery method

Patent metadata

Field	Value
Publication number	US-11229873-B2
Application number	US-201816771118-A
Country	US
Kind code	B2
Filing date	Dec 26, 2018
Priority date	Dec 27, 2017
Publication date	Jan 25, 2022
Grant date	Jan 25, 2022

Abstract

A CO 2 recovery device includes: an absorption tower configured to bring an emission gas including CO 2 in contact with an absorbent solution, to remove the CO 2 from the emission gas, and to thereby generate a rich solution corresponding to the absorbent solution having absorbed the CO 2 ; a regeneration tower configured to regenerate the absorbent solution by removing the CO 2 from the rich solution; a heat exchanger configured to carry out heat exchange between the rich solution and the absorbent solution which is higher in temperature than the rich solution and from which the CO 2 is removed; an absorbent-solution delivery pipe configured to deliver the absorbent solution subjected to the heat exchange in the heat exchanger to the absorption tower; and a bypass pipe configured to deliver the rich solution before the heat exchange to the absorbent-solution delivery pipe.

First claim

The invention claimed is:

1. A CO 2 recovery device comprising:
an absorption tower configured to bring an emission gas including CO 2 in contact with an absorbent solution, to remove the CO 2 from the emission gas, and to thereby generate a rich solution corresponding to the absorbent solution having absorbed the CO 2 ;
a regeneration tower configured to regenerate the absorbent solution by removing the CO 2 from the rich solution;
a heat exchanger configured to carry out heat exchange between the rich solution and the absorbent solution which is higher in temperature than the rich solution and from which the CO 2 is removed;
an absorbent-solution delivery pipe configured to deliver the absorbent solution subjected to the heat exchange in the heat exchanger to the absorption tower;
a bypass pipe configured to deliver the rich solution before the heat exchange to the absorbent-solution delivery pipe; and
a control device configured to control a bypass control valve attached to the bypass pipe to increase its opening when a liquid level of the absorbent solution accumulated in a base of the regeneration tower is below a predetermined level.

2. The CO 2 recovery device according to claim 1 , wherein
when a first pressure applied to the rich-solution delivery pipe configured to deliver the rich solution to the heat exchanger exceeds a predetermined solution, the control device is configured to increase the opening of the bypass control valve attached to the bypass pipe and to thereby deliver the rich solution before the heat exchange to the absorbent-solution delivery pipe.

3. The CO 2 recover device according to claim 1 , further comprising:
a rich-solution delivery pipe configured to deliver the rich solution to the regeneration tower; and
a rich-solution control valve configured to adjust a flow rate of the rich solution, which is disposed adjacent to the regeneration tower rather than the heat exchanger configured to carry out the heat exchange between the rich solution flowing through the rich-solution delivery pipe and the absorbent solution, wherein
the control device is configured to control the rich-solution control valve to increase its opening according to a reduction of the liquid level when the liquid level is above the predetermined level.

4. A CO 2 recovery method for a CO 2 recovery device, comprising:
bringing an emission gas including CO 2 in contact with an absorbent solution, removing the CO 2 from the emission gas, and thereby generating a rich solution in an absorption tower;
regenerating the absorbent solution by removing the CO 2 from the rich solution in a regeneration tower;
carrying out by a heat exchanger a heat exchange between the rich solution and the absorbent solution which is higher in temperature than the rich solution and from which the CO 2 is removed;
delivering by an absorbent-solution delivery pipe the absorbent solution subjected to the heat exchange in the heat exchanger to the absorption tower;
delivering the rich solution before the heat exchange to the absorbent-solution delivery pipe through a bypass pipe; and
controlling a bypass control valve attached to the bypass valve to increase its opening when the liquid level of the absorbent solution accumulated in a base of the regeneration tower is below a predetermined level.

5. The CO 2 recovery method according to claim 4 , further comprising:
when a first pressure applied to the absorbent-solution delivery pipe configured to deliver the rich solution before the heat exchange exceeds a predetermined threshold, increasing the opening of the bypass control valve attached to the bypass pipe when the first pressure exceeds a predetermined threshold, thus delivering the rich solution before the heat exchange to the absorbent-solution delivery pipe.

6. The CO 2 recovery method according to claim 4 , further comprising:
delivering by a rich-solution delivery pipe the rich solution to the regeneration tower;
adjusting a flow rate of the rich solution using a rich-solution control valve, which is disposed adjacent to the regeneration tower rather than the heat exchanger configured to carry out the heat exchange between the absorbent solution and the rich solution flowing through the rich-solution delivery pipe; and
controlling the rich-solution control valve to increase its opening according to a reduction of the liquid level when the liquid level is above the predetermined level.

Assignees

• Mitsubishi Heavy Ind Eng Ltd

Inventors

• Nakagawa Yosuke
• Shimada Daisuke
• Tsujiuchi Tatsuya

Classifications

• Y02C20/40

  of CO2 · CPC title

• B01D53/346

  Controlling the process · CPC title

• B01D53/96

  Regeneration, reactivation or recycling of reactants · CPC title

• B01D53/1412 Primary

  Controlling the absorption process · CPC title

• C01B32/50

  Carbon dioxide · CPC title