IP Library Granted Patent US 12,017,178
Granted Patent B2
US 12,017,178 · App. 17/439,221 · Granted Jun 25, 2024

Absorption solvent regeneration device, CO2 recovery device, and method for modifying absorption solvent regeneration device

Inventors: Yoshiki Sorimachi (Kanagawa, JP); Takashi Kamijo (Kanagawa, JP); Shinya Kishimoto (Kanagawa, JP)
Assignee: MITSUBISHI HEAVY INDUSTRIES, LTD.
B01D53/1425B01D53/1475B01D53/1493B01D53/62B01D53/96B01D2257/504
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 12,017,178
App. No.
17/439,221
Granted
Jun 25, 2024
Kind
B2
Abstract

An absorption solvent regeneration device includes: a regenerator for regenerating an absorption solvent by separating CO 2 from the absorption solvent which has absorbed CO 2 ; a main rich solvent line for supplying the absorption solvent which has absorbed CO 2 to the regenerator; a regeneration reboiler for heating an absorption solvent extracted from the regenerator; a reboiler line configured to extract the absorption solvent stored in the regenerator and return the absorption solvent to the regenerator via the regeneration reboiler; a branch rich solvent line branching from the main rich solvent line and connected to a portion of the reboiler line downstream of the regeneration reboiler; and a heating part for heating the absorption solvent flowing through the branch rich solvent line, the heating part being disposed on the branch rich solvent line.

Claims (23)

1. An absorption solvent regeneration device, comprising:

a regenerator for regenerating an absorption solvent by separating CO 2 from the absorption solvent which has absorbed CO 2 ;

a main rich solvent line for supplying the absorption solvent which has absorbed CO 2 to the regenerator;

a regeneration reboiler for heating an absorption solvent extracted from the regenerator;

a reboiler line configured to extract the absorption solvent stored in the regenerator and return the absorption solvent to the regenerator via the regeneration reboiler;

a branch rich solvent line branching from the main rich solvent line for supplying a portion of the absorption solvent to a portion of the reboiler line downstream of the regeneration reboiler; and

a heating part for heating the absorption solvent flowing through the branch rich solvent line, the heating part being disposed on the branch rich solvent line.

2. The absorption solvent regeneration device according to claim 1 ,

wherein the regeneration reboiler is configured such that a flow of the absorption solvent discharged from the regeneration reboiler to the reboiler line is a two-phase flow.

3. The absorption solvent regeneration device according to claim 1 , further comprising a steam supply line for supplying steam for heating the absorption solvent to the regeneration reboiler,

wherein the heating part includes a heat exchanger configured to exchange heat between condensed water of steam after heating the absorption solvent in the regeneration reboiler and the absorption solvent flowing through the branch rich solvent line.

4. The absorption solvent regeneration device according to claim 1 , further comprising a valve for regulating a flow rate of the absorption solvent in the branch rich solvent line, the valve being disposed in the branch rich solvent line.

5. A CO 2 recovery device, comprising:

an absorber configured to cause CO 2 in a flue gas to be absorbed by an absorption solvent by bringing the flue gas containing CO 2 and the absorption solvent into contact; and

the absorption solvent regeneration device according to claim 1 ,

wherein the main rich solvent line is configured to supply the absorption solvent which has absorbed CO 2 in the absorber to the regenerator.

6. A method for modifying an absorption solvent regeneration device, the absorption solvent regeneration device including:

a regenerator for regenerating an absorption solvent by separating CO 2 from the absorption solvent which has absorbed CO 2 ;

a main rich solvent line for supplying the absorption solvent which has absorbed CO 2 to the regenerator;

a regeneration reboiler for heating an absorption solvent extracted from the regenerator; and

a reboiler line configured to extract the absorption solvent stored in the regenerator and return the absorption solvent to the regenerator via the regeneration reboiler;

the method comprising a step of additionally installing a branch rich solvent line branching from the main rich solvent line for supplying a portion of the absorption solvent to a portion of the reboiler line downstream of the regeneration reboiler, and a heating part for heating the absorption solvent flowing through the branch rich solvent line, the heating part being disposed in the branch rich solvent line.

7. The method for modifying an absorption solvent regeneration device according to claim 6 , further comprising a step of installing, in the branch rich solvent line, a valve for regulating a flow rate of the absorption solvent in the branch rich solvent line.

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 Nov 11, 2021
From: SORIMACHI, YOSHIKI; KAMIJO, TAKASHI; KISHIMOTO, SHINYA
To: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
Reel/Frame 058091/0146 →
Priority Claims (1)
JP 2019-052031 · Mar 20, 2019 · national
Continuity (1)
Related Publication 20220161184A1 · May 26, 2022