Carbon dioxide recovery method and carbon-dioxide-recovery-type steam power generation system

Patent metadata

Field	Value
Publication number	US-9416683-B2
Application number	US-201414229572-A
Country	US
Kind code	B2
Filing date	Mar 28, 2014
Priority date	Oct 22, 2010
Publication date	Aug 16, 2016
Grant date	Aug 16, 2016

Abstract

According to one embodiment, a carbon-dioxide-recovery-type steam power generation system comprises a boiler that produces steam and generates an exhaust gas, a first turbine that is rotationally driven by the steam, an absorption tower allows carbon dioxide contained in the exhaust gas to be absorbed into an absorption liquid, a regeneration tower that discharges the carbon dioxide gas from the absorption liquid supplied from the absorption tower, a condenser that removes moisture from the carbon dioxide gas, discharged from the regeneration tower, by condensing the carbon dioxide gas using cooling water, a compressor that compresses the carbon dioxide gas from which the moisture is removed by the condenser, and a second turbine that drives the compressor. The steam produced by the cooling water recovering the heat from the carbon dioxide gas in the condenser is supplied to the first turbine or the second turbine.

First claim

What is claimed is:

1. A carbon-dioxide-recovery-type steam power generation system, comprising:
a boiler that produces steam and generates an exhaust gas by combusting fuel;
a first turbine that is connected to a generator and is rotationally driven by the steam supplied from the boiler;
an absorption tower that is supplied with the exhaust gas from the boiler and allows carbon dioxide contained in the exhaust gas to be absorbed into an absorption liquid;
a regeneration tower that is supplied with the absorption liquid absorbing the carbon dioxide from the absorption tower, discharges a carbon dioxide gas from the absorption liquid, and discharges the carbon dioxide gas;
a reboiler that heats the absorption liquid from the regeneration tower and supplies the generated steam to the regeneration tower;
a condenser that removes moisture from the carbon dioxide gas, discharged from the regeneration tower, by condensing the carbon dioxide gas using a cooling medium;
a compressor that compresses the carbon dioxide gas from which the moisture is removed by the condenser; and
a second turbine that drives the compressor,
wherein steam produced by the cooling medium recovering the heat from the carbon dioxide gas in the condenser is supplied to the first turbine or the second turbine.

2. The carbon-dioxide-recovery-type steam power generation system according to claim 1 , further comprising:
a steam condenser that produces the cooling medium by cooling and condensing exhaust steam from the second turbine.

3. The carbon-dioxide-recovery-type steam power generation system according to claim 1 , further comprising:
a temperature decreasing unit that decreases the temperature of the steam from the first turbine and supplies the steam to the reboiler,
wherein the cooling medium recovers the heat from the carbon dioxide gas in the condenser, and thereafter, recovers the heat from the steam from the first turbine in the temperature decreasing unit.

4. The carbon-dioxide-recovery-type steam power generation system according to claim 3 , further comprising:
a control unit that measures the temperature of the steam decreased in temperature by the temperature decreasing unit and controls the flow rate of the cooling medium supplied to the condenser based on the measurement result.

5. The carbon-dioxide-recovery-type steam power generation system according to claim 1 , further comprising:
a cooler to which a part of the cooling medium is supplied and which cools the carbon dioxide gas compressed by the compressor,
wherein the steam produced by cooling the carbon dioxide gas in the cooler is supplied to the second turbine.

6. The carbon-dioxide-recovery-type steam power generation system according to claim 1 ,
wherein the boiler includes a superheater generating main steam and a reheater generating reheat steam,
the first turbine includes a high-pressure turbine rotationally driven by the main steam supplied thereto, an intermediate-pressure turbine rotationally driven by the reheat steam supplied thereto, and a low-pressure turbine rotationally driven by the exhaust steam supplied thereto from the intermediate-pressure turbine,
the cooling medium is a part of a condensate produced by cooling and condensing the exhaust steam from the low-pressure turbine, and
the steam produced in the condenser is supplied to the low-pressure turbine.

7. The carbon-dioxide-recovery-type steam power generation system according to claim 1 ,
wherein the cooling medium is a part of a condensate produced by cooling and condensing the exhaust steam from the first turbine, and
the steam produced in the condenser is supplied to the second turbine.

8. A carbon dioxide recovery method, comprising:
producing steam, which drives a turbine, and generating an exhaust gas by combusting fuel;
allowing carbon dioxide, which is contained in the exhaust gas, to be absorbed into an absorption liquid;
emitting a carbon dioxide gas by heating the absorption liquid absorbing the carbon dioxide and discharging the carbon dioxide gas;
cooling the discharged carbon dioxide gas using a cooling medium and removing moisture from the carbon dioxide gas by condensing the moisture;
compressing the carbon dioxide gas, from which moisture is removed, using a compressor; and
supplying steam generated by the cooling medium recovering heat at the time of condensing the moisture from the carbon dioxide gas to a driving turbine driving the compressor or the turbine.

9. The carbon dioxide recovery method according to claim 8 ,
wherein the cooling medium is produced by cooling and condensing an exhaust steam from the driving turbine.

10. The carbon dioxide recovery method according to claim 8 ,
wherein the steam from the turbine is used as a heat source of the absorption liquid and a heat source of the steam generated by the cooling medium recovering heat at the time of condensing the moisture.

11. The carbon dioxide recovery method according to claim 10 ,
wherein the temperature of the steam decreased in temperature by a temperature decreasing unit is measured, and the flow rate of the cooling medium is controlled based on the temperature measurement result.

12. The carbon dioxide recovery method according to claim 8 ,
wherein a part of the cooling medium is used to cool the carbon dioxide gas compressed by the compressor.

13. The carbon dioxide recovery method according to claim 8 ,
wherein the cooling medium is a part of a condensate generated by cooling and condensing the exhaust steam from the turbine, and
the steam generated by the cooling medium recovering heat at the time of condensing the moisture is supplied to the turbine.

14. The carbon dioxide recovery method according to claim 8 ,
wherein the cooling medium is a part of a condensate generated by cooling and condensing the exhaust steam from the turbine, and
the steam generated by the cooling medium recovering heat at the time of condensing the moisture is supplied to the driving turbine.

Assignees

• Toshiba Kk

Inventors

• Murakami Yuya
• Okita Nobuo
• Takahashi Takeo
• Takayanagi Mikio
• Suga Takeo
• Sasanuma Takeshi
• Kiyokuni Toshihisa
• Kitamura Hideo

Classifications

• F01K25/06

  using mixtures of different fluids (plants using mixtures of steam and gas F01K21/04) · CPC title

• Y02C10/06

  Cross-Sectional Technologies · mapped topic

• F01K13/00 Primary

  General layout or general methods of operation of complete plants · CPC title

• F01K25/103

  Carbon dioxide (F01K25/065 takes precedence) · CPC title

• Y02E20/14

  Combined heat and power generation [CHP] · CPC title