Supercritical carbon dioxide power generation system utilizing plural heat sources

Patent metadata

Field	Value
Publication number	US-10273832-B2
Application number	US-201715407448-A
Country	US
Kind code	B2
Filing date	Jan 17, 2017
Priority date	Jan 15, 2016
Publication date	Apr 30, 2019
Grant date	Apr 30, 2019

Abstract

Disclosed herein is a supercritical carbon dioxide power generation system utilizing a plurality of heat sources, comprising: a pump for circulating a working fluid; a plurality of heat exchangers for heating the working fluid through an external heat source; a plurality of turbines driven by the working fluid heated through the heat exchangers; and a plurality of recuperators that allow the working fluid passed through the turbines and the working fluid passed through the pump to heat exchange with each other to cool the working fluid passed through the turbine, wherein the plurality of heat exchangers are sequentially disposed from a high temperature region at an inlet end into which waste heat gas stream is introduced up to a low temperature region at an outlet end through which the waste heat gas stream is discharged via a mediate temperature region.

First claim

What is claimed is:

1. A supercritical carbon dioxide power generation system utilizing a plurality of heat sources comprising:
a pump which circulates a working fluid,
a plurality of heat exchangers which heat the working fluid using an external heat source,
a plurality of turbines which are driven by the working fluid heated by the plurality of heat exchangers, and
a plurality of recuperators which perform heat exchange with each other to cool the working fluid passed through the plurality of turbines, the heat exchange being performed by using the working fluid passed through the plurality of turbines and the working fluid passed through the pump,
wherein the plurality of heat exchangers are sequentially disposed and distributed at a high temperature region, an intermediate temperature region and a low temperature region such that one or more heat exchangers to be used for circulating a corresponding flow path of the working fluid determined depending on a temperature of the working fluid are selected from among the plurality of heat exchangers, and
the high temperature region is located at an inlet into which a waste heat gas stream is introduced, and the low temperature region is located at an outlet through which the waste heat gas stream is discharged via the intermediate temperature region.

2. The supercritical carbon dioxide power generation system according to claim 1 , further comprising:
a valve disposed at a rear end of the pump to select the circulating flow path of the working fluid by
selectively supplying the working fluid to one or more selected from among the plurality of heat exchangers according to the temperature of the working fluid passed through the pump.

3. The supercritical carbon dioxide power generation system according to claim 1 , wherein the plurality of heat exchangers comprise:
a first heat exchanger disposed in the low temperature region;
a fourth heat exchanger disposed in the intermediate temperature region; and
a second heat exchanger, a third heat exchanger and a fifth heat exchanger, all of which are disposed in the high temperature region.

4. The supercritical carbon dioxide power generation system according to claim 3 ,
wherein the third, the fifth and the second heat exchangers are sequentially disposed from the high temperature region toward the intermediate temperature region.

5. The supercritical carbon dioxide power generation system according to claim 4 ,
wherein the working fluid is transferred to the first heat exchanger when the temperature of the working fluid passed through the pump is equal to or lower than a reference temperature, and
the working fluid is transferred to the fourth heat exchanger when the temperature of the working fluid is higher than the reference temperature.

6. The supercritical carbon dioxide power generation system according to claim 5 , wherein the plurality of recuperators comprise:
a first recuperator disposed between a rear end of a first turbine of the plurality of turbines and a front end of the pump; and
a second recuperator disposed between a rear end of the first recuperator and the front end of the pump.

7. The supercritical carbon dioxide power generation system according to claim 6 , wherein there is heat transfer between the working fluid having a temperature that is equal to or lower than the reference temperature and the waste heat gas stream in the first heat exchanger, and the working fluid is transferred to the first recuperator and absorbs heat from the working fluid passed through the first turbine, and is transferred to the second heat exchanger and there is a heat transfer between the working fluid and the waste heat gas stream.

8. The supercritical carbon dioxide power generation system according to claim 7 , wherein the working fluid passed through the second heat exchanger is transferred to the third heat exchanger and there is heat transfer between the working fluid and the waste heat gas stream, and the working fluid is transferred to any one of the plurality of turbines.

9. The supercritical carbon dioxide power generation system according to claim 8 , wherein the working fluid having the temperature which is higher than the reference temperature is transferred to the second recuperator and absorbs heat from the working fluid passed through the first recuperator, and is transferred to the fourth heat exchanger and there is heat transfer between the working fluid and the waste heat gas stream.

10. The supercritical carbon dioxide power generation system according to claim 9 , wherein the working fluid passed through the fourth heat exchanger is transferred to the fifth heat exchanger and there is heat transfer between the working fluid and the waste heat gas stream, and the working fluid is transferred to another of the plurality of turbines.

11. The supercritical carbon dioxide power generation system according to claim 10 , wherein the plurality of turbines comprise a high-pressure turbine driven by the working fluid supplied from any one of the third and the fifth heat exchangers and a low-pressure turbine driven by the working fluid supplied from another of the third and the fifth heat exchangers.

12. The supercritical carbon dioxide power generation system according to claim 11 , wherein the high-pressure turbine is connected to the third heat exchanger while the low pressure turbine is connected to the fifth heat exchanger.

13. The supercritical carbon dioxide power generation system according to claim 1 , wherein the inlet is an inlet end of the plurality of heat exchangers and the outlet is an outlet end of the plurality of heat exchangers.

Assignees

• Doosan Heavy Ind & Construction Co Ltd
• Doosan Heavy Ind Constr Co Ltd

Inventors

• CHA Song Hun
• Kim Hak Soo
• Kim Sang Hyeun
• Jang Jun Tae

Classifications

• F01K25/103 Primary

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

• F01K23/12

  the engines being mechanically coupled (F01K23/02 takes precedence) · CPC title

• F01K7/16

  the engines being only of turbine type (the engines using steam of critical or overcritical pressure F01K7/32; the engines being of extraction or non-condensing type F01K7/34) · CPC title

• F01K7/32

  the engines using steam of critical or overcritical pressure · CPC title