IP Library Granted Patent US 12,172,124
Granted Patent B2
US 12,172,124 · App. 17/633,413 · Granted Dec 24, 2024

Carbon dioxide recovery system and carbon dioxide recovery method

Inventors: Tomoki Noborisato (Kanagawa, JP); Takashi Kamijo (Kanagawa, JP)
Assignee: MITSUBISHI HEAVY INDUSTRIES, LTD.
B01D53/1425B01D53/1412B01D53/1418B01D53/1475B01D53/185C01B32/50F23J15/04F23J2900/15027
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Quick Facts
Patent No.
US 12,172,124
App. No.
17/633,413
Granted
Dec 24, 2024
Kind
B2
Abstract

A carbon dioxide recovery system includes: a plurality of absorption towers each disposed for each of a plurality of combustion equipments for absorbing carbon dioxide in an exhaust gas discharged from each of the plurality of combustion equipments into an absorption liquid by bringing the exhaust gas into contact with the absorption liquid; and at least one regeneration tower communicating with each of the plurality of absorption towers, for recovering carbon dioxide from a CO 2 rich absorption liquid which is the absorption liquid flowing out of each of the plurality of absorption towers. The regeneration tower is smaller in number than the absorption towers.

Claims (22)

1. A carbon dioxide recovery system, comprising:

absorption towers each disposed for each of combustion equipments for absorbing carbon dioxide in an exhaust gas discharged from the each of the combustion equipments into an absorption liquid by bringing the exhaust gas into contact with the absorption liquid;

ducts that each connect the combustion equipments with corresponding ones of the absorption towers;

at least one regeneration tower communicating with each of the absorption towers, for recovering carbon dioxide from a CO 2 rich absorption liquid that is the absorption liquid flowing out of each of the absorption towers; and

CO 2 rich absorption liquid supply pipes that each connect the absorption towers with the at least one regeneration tower and supply the CO 2 rich absorption liquid from the absorption towers to the at least one regeneration tower, wherein

the regeneration tower is smaller in number than the absorption towers,

a distance between each of the combustion equipments and a corresponding one of the absorption towers provided for each of the combustion equipments is shorter than a distance between each of the combustion equipments and the regeneration tower, and

outer diameters of the ducts are larger than outer diameters of the CO 2 rich absorption liquid supply pipes.

2. The carbon dioxide recovery system according to claim 1 , further comprising:

CO 2 lean absorption liquid supply pipes for supplying, to each of the absorption towers, a CO 2 lean absorption liquid, which is obtained by removing carbon dioxide from the CO 2 rich absorption liquid by the regeneration tower, as the absorption liquid contacting the exhaust gas in each of the absorption towers; and

a flow control part for controlling a flow rate of the CO 2 lean absorption liquid flowing through each of the CO 2 lean absorption liquid supply pipes, wherein

the flow control part controls the flow rate of the CO 2 lean absorption liquid flowing through each of the CO 2 lean absorption liquid supply pipes such that a carbon dioxide concentration in the CO 2 rich absorption liquid flowing out of each of the absorption towers is not less than a preset lower limit concentration.

3. The carbon dioxide recovery system according to claim 1 , further comprising:

a carbon dioxide flow rate acquisition part for acquiring a flow rate of carbon dioxide flowing into the regeneration tower; and

a heat medium flow control part for controlling a flow rate of a heat medium supplied to the regeneration tower in order to heat the CO 2 rich absorption liquid in the regeneration tower, wherein

the heat medium flow control part controls the flow rate of the heat medium based on a value detected by the carbon dioxide flow rate acquisition part.

4. A carbon dioxide recovery method, comprising:

a step of absorbing carbon dioxide in an exhaust gas discharged from each of combustion equipments into an absorption liquid by individually bringing the exhaust gas into contact with the absorption liquid in each of absorption towers provided for combustion equipments, respectively, wherein the exhaust gas discharged from each of the combustion equipments; and

a step of recovering carbon dioxide in at least one regeneration tower after merging CO 2 rich absorption liquids each of which is the absorption liquid absorbing carbon dioxide, wherein

the at least one regeneration tower is smaller in number than the absorption towers,

a distance between each of the combustion equipments and a corresponding one of the absorption towers provided for each of the combustion equipments is shorter than a distance between each of the combustion equipments and the at least one regeneration tower, and

outer diameters of ducts that each connect the combustion equipments with corresponding ones of the absorption towers are larger than outer diameters of CO 2 rich absorption liquid supply pipes that each supply the CO 2 rich absorption liquids from the absorption towers to the at least one regeneration tower.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 17, 2023
From: MHI ENGINEERING, LTD.
To: MITSUBISHI HEAVY INDUSTRIES, LTD.
Reel/Frame 065245/0620 →
CHANGE OF NAME Recorded Oct 17, 2023
From: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
To: MHI ENGINEERING, LTD.
Reel/Frame 065245/0643 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 2, 2022
From: NOBORISATO, TOMOKI; KAMIJO, TAKASHI
To: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
Reel/Frame 059146/0292 →
Priority Claims (1)
JP 2019-196885 · Oct 30, 2019 · national
Continuity (1)
Related Publication 20220288527A1 · Sep 15, 2022
Cited By (1)
US 12,480,444