IP Library Granted Patent US 8,052,948
Granted Patent B2
US 8,052,948 · App. 11/896,731 · Granted Nov 8, 2011

CO

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Quick Facts
Patent No.
US 8,052,948
App. No.
11/896,731
Granted
Nov 8, 2011
Kind
B2
Abstract

A CO 2 recovery system includes an absorption tower and a regeneration tower. CO 2 rich solution is produced in the absorption tower by absorbing CO 2 from CO 2 -containing gas. The CO 2 rich solution is conveyed to the regeneration tower where lean solution is produced from the rich solution by removing CO 2 . A compressor compresses CO 2 that is removed from the rich solution and discharged through a head of the regeneration tower. Heat is generated while the compressor compresses the CO 2 . A heat supplying unit supplies the heat to the regeneration tower for heating the lean solution.

Claims (26)

1. A CO 2 recovery system including

an absorption tower that

receives CO 2 -containing gas and CO 2 -absorbing solution, and

causes the CO 2 -containing gas to come in contact with the CO 2 -absorbing solution to produce CO 2 rich solution, and

a regeneration tower that

receives the rich solution and

produces lean solution from the rich solution by removing CO 2 from the rich solution, wherein semi-lean solution is produced as an intermediate product before producing the lean solution from the rich solution,

the CO 2 recovery system comprising:

a condenser that receives CO 2 removed from the rich solution and discharged through a head of the regeneration tower, and that condenses water vapor released along with the CO 2 into water;

a separation drum that receives the CO 2 from the condenser and separates the water from the CO 2 ;

two or more compressors that compress the CO 2 from the separation drum, wherein heat is generated while each compressor compresses the CO 2 ;

a heat supplying unit that supplies the heat to the regeneration tower for heating any one of the lean solution and the semi-lean solution;

a bifurcated path through which any one of a part of the lean solution extracted from a portion of bottom of the regeneration tower and the semi-lean solution extracted from a midcourse of the regeneration tower bifurcates and passes;

a circulating path suitable for extracting any one of the part of the lean solution and the semi-lean solution through the bifurcated path, heat-exchanging with compression heat that is generated when CO 2 gas, which is released from a head of the regeneration tower is compressed by each compressor, and supplying again any one of the heated part of the lean solution and the semi-lean solution to the regeneration tower therethrough; and

at least two heat exchangers that are located on intersections between the bifurcated path and a path suitable for conveying the CO 2 gas discharged from the top of the regeneration tower capable of transferring the heat to any one of the part of the lean solution or the semi-lean solution, wherein the condenser, the separation drum, the compressors, and the heat exchangers are located on the CO 2 gas conveying path.

2. A CO 2 recovery method comprising:

causing CO 2 -containing gas to come in contact with CO 2 -absorbing solution to produce CO 2 rich solution in an absorption tower,

conveying the rich solution to a regeneration tower, and

producing a lean solution from the rich solution by removing CO 2 from the rich solution in the regeneration tower, wherein semi-lean solution is produced as an intermediate product before producing the lean solution from the rich solution

receiving the CO 2 removed from the rich solution and discharged through a head of the regeneration tower, and condensing water vapor released along with the CO 2 into water;

receiving the CO 2 after water vapor is condensed and separating the water from the CO 2 ;

compressing, using two or more compressors, the CO 2 from which the water is separated, wherein heat is generated at the compressing;

transferring the heat to any one of a part of the lean solution extracted from a portion of bottom of the regeneration tower and a part of the semi-lean solution extracted from a midcourse of the regeneration tower;

bifurcating any one of the part of the lean solution and the semi-lean solution so as to be flowed into a bifurcated path;

exchanging heat between any one of the part of the lean solution and the semi-lean solution on a circulating path and a path suitable for conveying the CO 2 gas from the head of the regeneration tower, wherein the circulating path is a path suitable for extracting any one of the part of the lean solution and the semi-lean solution through the bifurcated path, heat-exchanging with compression heat that is generated when CO 2 gas, which is released from the head of the regeneration tower, is compressed by each compressor and supplying again any one of the heated part of the lean solution and the semi-lean solution to the regeneration tower therethrough; and

returning any one of the part of the lean solution and the semi-lean solution heated in the transferring to the regeneration tower to supply heat to the regeneration tower for heating.

Assignments (4)
CHANGE OF NAME Recorded Dec 14, 2023
From: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
To: MHI ENGINEERING, LTD.
Reel/Frame 066014/0774 →
NUNC PRO TUNC ASSIGNMENT Recorded Dec 14, 2023
From: MHI ENGINEERING, LTD.
To: MITSUBISHI HEAVY INDUSTRIES, LTD.
Reel/Frame 066014/0870 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 12, 2018
From: MITSUBISHI HEAVY INDUSTRIES, LTD.
To: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
Reel/Frame 047054/0898 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 20, 2007
From: IIJIMA, MASAKI
To: MITSUBISHI HEAVY INDUSTRIES, LTD.; THE KANSAI ELECTRIC POWER CO., INC.
Reel/Frame 020138/0498 →