Carbon dioxide capturing system and method of operating the same

Patent metadata

Field	Value
Publication number	US-9815016-B2
Application number	US-201514744285-A
Country	US
Kind code	B2
Filing date	Jun 19, 2015
Priority date	Dec 5, 2014
Publication date	Nov 14, 2017
Grant date	Nov 14, 2017

Abstract

In one embodiment, a carbon dioxide capturing system includes an absorber to discharge an absorption liquid having absorbed carbon dioxide, a regenerator to discharge the absorption liquid having released the carbon dioxide, a first line to introduce the absorption liquid discharged from the absorber to the regenerator, a second line to introduce the absorption liquid discharged from the regenerator to the absorber, and a heat exchanger to exchange heat between absorption liquids flowing in the first and second lines. The system further includes a bypass line to branch from the first line between the absorber and the heat exchanger and introduce the absorption liquid to the regenerator without passing through the heat exchanger, a valve on the bypass line, an instrument to measure a value indicating a state of the regenerator, and a controller to control a degree of opening of the valve based on the measured value.

First claim

The invention claimed is:

1. A carbon dioxide capturing system comprising:
an absorber configured to bring a gas containing carbon dioxide into contact with an absorption liquid capable of absorbing the carbon dioxide, and to discharge the absorption liquid having absorbed the carbon dioxide;
a regenerator configured to cause the absorption liquid discharged from the absorber to release the carbon dioxide, and to discharge the absorption liquid having released the carbon dioxide;
a first absorption liquid line configured to introduce the absorption liquid discharged from the absorber to the regenerator;
a second absorption liquid line configured to introduce the absorption liquid discharged from the regenerator to the absorber;
a heat exchanger configured to exchange heat between the absorption liquid flowing in the first absorption liquid line and the absorption liquid flowing in the second absorption liquid line;
a bypass line configured to branch from the first absorption liquid line between the absorber and the heat exchanger, and to introduce the absorption liquid to the regenerator without passing through the heat exchanger;
at least one absorption liquid valve provided on the bypass line;
at least one measuring instrument configured to measure a value that indicates a state of the regenerator; and
a controller configured to control a degree of opening of the absorption liquid valve, based on the value measured by the measuring instrument,
wherein the measuring instrument is configured to measure at least one of a flow rate of a gas discharged from the regenerator and a pressure in the regenerator.

2. The system of claim 1 , wherein the measuring instrument is further configured to measure a temperature in the regenerator.

3. The system of claim 1 , wherein the controller controls the degree of opening of the absorption liquid valve such that a flow rate of the absorption liquid introduced from the bypass line to the regenerator is 80% or less of a flow rate of the absorption liquid discharged from the absorber to the first absorption liquid line.

4. The system of claim 1 , wherein
the at least one absorption liquid valve includes first to Nth absorption liquid valves where N is an integer of two or more,
the at least one measuring instrument includes first to Nth measuring instruments, and
the controller controls a degree of opening of a Kth absorption liquid valve, based on a value measured by a Kth measuring instrument where K is an integer satisfying 1≦K≦N.

5. The system of claim 1 , further comprising:
a cooler configured to cool the absorption liquid flowing in the bypass line; and
a refrigerant valve configured to regulate a flow rate of a refrigerant in the cooler,
wherein the controller controls a degree of opening of the refrigerant valve, based on the value measured by the measuring instrument.

6. The system of claim 1 , further comprising:
a cooler configured to cool the absorption liquid flowing in the second absorption liquid line; and
a refrigerant valve configured to regulate a flow rate of a refrigerant in the cooler,
wherein the controller controls a degree of opening of the refrigerant valve, based on the value measured by the measuring instrument.

7. The system of claim 1 , further comprising:
a gas line configured to introduce the gas containing the carbon dioxide to the absorber; and
a gas valve configured to regulate a flow rate of the gas flowing in the gas line,
wherein the controller controls a degree of opening of the gas valve, based on the value measured by the measuring instrument.

8. The system of claim 1 , further comprising a heater configured to heat the regenerator,
wherein the controller controls an input heat amount to the heater, based on the value measured by the measuring instrument.

9. The system of claim 1 , further comprising a cooling module configured to extract the absorption liquid from the absorber, cool the extracted absorption liquid, and return the cooled absorption liquid to the absorber,
wherein the controller controls operation of the cooling module, based on the value measured by the measuring instrument.

10. A method of operating a carbon dioxide capturing system, the system comprising:
an absorber configured to bring a gas containing carbon dioxide into contact with an absorption liquid capable of absorbing the carbon dioxide, and to discharge the absorption liquid having absorbed the carbon dioxide;
a regenerator configured to cause the absorption liquid discharged from the absorber to release the carbon dioxide, and to discharge the absorption liquid having released the carbon dioxide;
a first absorption liquid line configured to introduce the absorption liquid discharged from the absorber to the regenerator;
a second absorption liquid line configured to introduce the absorption liquid discharged from the regenerator to the absorber; and
a heat exchanger configured to exchange heat between the absorption liquid flowing in the first absorption liquid line and the absorption liquid flowing in the second absorption liquid line,
the method comprising:
measuring a value that indicates a state of the regenerator with at least one measuring instrument;
controlling, based on at least one of a flow rate of a gas discharged from the regenerator and a pressure in the regenerator, a degree of opening of at least one absorption liquid valve provided on a bypass line that branches from the first absorption liquid line between the absorber and the heat exchanger and introduces the absorption liquid to the regenerator without passing through the heat exchanger; and
introducing the absorption liquid discharged from the absorber to the regenerator through the first absorption liquid line and the bypass line.

Assignees

• Toshiba Kk
• Toshiba Plant Systems & Services Corp

Inventors

• Udatsu Mitsuru
• Kashimoto Satoru
• Hodotsuka Masatoshi
• Kitamura Hideo
• Oohashi Yukio
• Saito Satoshi

Classifications

• B01D53/1475

  Removing carbon dioxide · CPC title

• B01D2259/65

  Employing advanced heat integration, e.g. Pinch technology · CPC title

• B01D2258/0283

  Flue gases · CPC title

• B01D53/18 Primary

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title

• B01D53/1425

  Regeneration of liquid absorbents · CPC title