Carbon dioxide recovery system and carbon dioxide recovery method

Patent metadata

Field	Value
Publication number	US-12172124-B2
Application number	US-202017633413-A
Country	US
Kind code	B2
Filing date	Aug 3, 2020
Priority date	Oct 30, 2019
Publication date	Dec 24, 2024
Grant date	Dec 24, 2024

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.

First claim

The invention claimed is:

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.

Assignees

• Mitsubishi Heavy Ind Ltd

Inventors

• Noborisato Tomoki
• Kamijo Takashi

Classifications

• F23J2900/15027

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