Carbon dioxide recovery apparatus and carbon dioxide recovery method

Patent metadata

Field	Value
Publication number	US-9339762-B2
Application number	US-201414310676-A
Country	US
Kind code	B2
Filing date	Jun 20, 2014
Priority date	Mar 6, 2012
Publication date	May 17, 2016
Grant date	May 17, 2016

Abstract

In one embodiment, a carbon dioxide recovery apparatus includes a heat exchanger which heats a first rich liquid, a flow divider which divides the first rich liquid heated by the heat exchanger into a second rich liquid and a third rich liquid, a first release device which heats the second rich liquid and discharges a first semi-lean liquid, a second release device which heats the third rich liquid and discharges a second semi-lean liquid, and a regeneration tower which heats the first and second semi-lean liquids to generate a lean liquid. The first release device heats the second rich liquid, using the lean liquid. The second release device heats the third rich liquid, using a carbon dioxide-containing steam discharged at the regeneration tower. The heat exchanger heats the first rich liquid, using the lean liquid which has passed through the first release device.

First claim

What is claimed is:

1. A carbon dioxide recovery method comprising:
bringing carbon dioxide-containing gas into contact with an absorbing liquid for absorbing carbon dioxide and generating a first rich liquid having the absorbed carbon dioxide;
heating the first rich liquid;
dividing the heated first rich liquid into a second rich liquid and a third rich liquid;
heating the second rich liquid and generating a first semi-lean liquid in which carbon dioxide-containing steam is released;
heating the third rich liquid and generating a second semi-lean liquid in which carbon dioxide-containing steam is released; and
heating the first semi-lean liquid and the second semi-lean liquid in a regeneration tower, releasing remaining carbon dioxide-containing steam, and generating a lean liquid, thereby reducing heat exchange duty,
wherein
the first rich liquid is heated before being divided into a second rich liquid and a third rich liquid,
a portion of the first rich liquid is divided before the first rich liquid is heated,
the second rich liquid is heated by a first carbon dioxide release device, using the lean liquid discharged from the regeneration tower as a heat source,
the third rich liquid and the portion of the first rich liquid are heated by a second carbon dioxide release device, using carbon dioxide-containing steam discharged at the regeneration tower as a heat source, and
the first rich liquid is heated, using the lean liquid after heating the second rich liquid as a heat source.

2. The carbon dioxide recovery method according to claim 1 , wherein a flow rate of the portion of the first rich liquid and a flow rate of the third rich liquid are equivalent to each other.

Assignees

• Toshiba Kk

Inventors

• Kitamura Hideo
• Saito Satoshi
• Udatsu Mitsuru

Classifications

• B01D53/1475 Primary

  Removing carbon dioxide · CPC title

• B01D53/96 Primary

  Regeneration, reactivation or recycling of reactants · CPC title

• B01D2259/65

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

• F23J2215/50

  Carbon dioxide · CPC title

• F23J2219/40

  Sorption with wet devices, e.g. scrubbers · CPC title