Carbon dioxide recovery system and method

Patent metadata

Field	Value
Publication number	US-9243517-B2
Application number	US-201213437243-A
Country	US
Kind code	B2
Filing date	Apr 2, 2012
Priority date	Apr 6, 2011
Publication date	Jan 26, 2016
Grant date	Jan 26, 2016

Abstract

A carbon dioxide recovery system includes a high-pressure turbine 11 , an intermediate-pressure turbine 12 , a low-pressure turbine 13 , a main boiler 15 that generates steam 14 for driving these turbines, a carbon dioxide recovery unit 24 including a carbon dioxide absorber 21 that absorbs and reduces carbon dioxide in flue gas (emission gas) G emitted from the main boiler 15 using a carbon dioxide absorbent and an absorbent regenerator 23 that regenerates a carbon dioxide absorbent having absorbed the carbon dioxide using a regenerating superheater 22 to obtain a regenerated carbon dioxide absorbent, an auxiliary boiler 30 that generates saturated water vapor 31 to be supplied to the regenerating superheater 22 in the absorbent regenerator 23 , and a steam turbine 32 that is driven by steam from the auxiliary boiler 30.

First claim

The invention claimed is:

1. A carbon dioxide recovery system comprising:
a high-pressure turbine, an intermediate-pressure turbine, and a low-pressure turbine;
a main boiler that generates steam for driving these turbines and receives a first condensed water generated via these turbines;
a first steam line that supplies the steam sequentially to the high-pressure turbine, the intermediate-pressure turbine, and the low-pressure turbine and returns the first condensed water to the main boiler;
a carbon dioxide recovery unit including:
a carbon dioxide absorber having a carbon dioxide absorbent that absorbs and reduces carbon dioxide in flue gas emitted from the main boiler; and
an absorbent regenerator having a regenerating superheater that heats the carbon dioxide absorbent so as to regenerate the carbon dioxide absorbent;
an auxiliary boiler that is provided downstream of the regenerating superheater, receives a second condensed water generated via the regenerating superheater and generates saturated water vapor or almost-saturated water vapor to be supplied to the regenerating superheater in the absorbent regenerator;
a first steam turbine that is provided downstream of the auxiliary boiler, driven by steam from the auxiliary boiler, provided upstream of the regenerating superheater and emits turbine emission to the regenerating superheater; and
a second steam line that supplies the saturated water vapor or almost-saturated water vapor sequentially to the first steam turbine and the regenerating superheater and returns the second condensed water to the auxiliary boiler; wherein
a line for supplying carbon dioxide in flue gas emitted from the auxiliary boiler to the carbon dioxide absorber is provided.

2. The carbon dioxide recovery system according to claim 1 , further comprising:
a second steam turbine that is driven by steam from the auxiliary boiler and emits turbine emission to the regenerating superheater; and
a CO 2 compressor that is driven by the first steam turbine and compresses CO 2 emitted from the absorbent regenerator, wherein
the second steam turbine is provided parallel to the first steam turbine.

Assignees

• Iijima Masaki
• Mitsubishi Heavy Ind Ltd

Inventors

• Iijima Masaki

Classifications

• B01D53/1425

  Regeneration of liquid absorbents · CPC title

• Y02E20/185

  Cross-Sectional Technologies · mapped topic

• F01K17/04

  for specific purposes other than heating (F01K17/06 takes precedence) · CPC title

• B01D2258/0283

  Flue gases · CPC title

• F01K7/22 Primary

  the turbines having inter-stage steam heating · CPC title