CO2 power generation system

Patent metadata

Field	Value
Publication number	US-10309259-B2
Application number	US-201615348660-A
Country	US
Kind code	B2
Filing date	Nov 10, 2016
Priority date	Jun 15, 2016
Publication date	Jun 4, 2019
Grant date	Jun 4, 2019

Abstract

A CO2 power generation system includes a furnace to burn fuel, a turbine operated by a working fluid supplied thereto, the working fluid being heated by heat generated in the furnace, a recuperator exchanging heat with the working fluid passing through the turbine, a cooler to cool the working fluid passing through the recuperator, and a compressor to compress the working fluid passing through the cooler, wherein the working fluid passing through the compressor is circulated to the furnace, and the working fluid is supercritical CO2.

First claim

What is claimed is:

1. A CO 2 power generation system, comprising:
a furnace that burns fuel;
a turbine that is supplied with a working fluid of supercritical CO 2 heated by heat generated in the furnace;
a recuperator that exchanges heat with the working fluid passing through the turbine;
a first separator provided at a rear of the turbine so as to branch the working fluid passing through the turbine into the recuperator and the furnace;
a cooler that cools the working fluid passing through the recuperator; and
a compressor that compresses the working fluid passing through the cooler,
wherein the working fluid passing through the compressor is circulated to the furnace.

2. The CO 2 power generation system according to claim 1 , further comprising
a first mixer provided at a front of the cooler that mixes the working fluid discharged after heating air introduced into the furnace with the working fluid cooled by the recuperator, and that supplies the mixed working fluid to the cooler; and
a second separator provided at a discharge of the compressor that branches the working fluid passing through the compressor into the furnace and the recuperator.

3. The CO 2 power generation system according to claim 2 , wherein
the working fluid branched to the furnace by the first separator is cooled after heating the air introduced into the furnace, and is transferred out of the furnace,
the working fluid branched to the recuperator by the first separator is cooled by exchanging heat with a portion of the working fluid passing through the compressor,
a portion of the working fluid branched by the second separator is heated by the working fluid branched from the recuperator by the first separator, and
a remainder of the working fluid branched by the second separator is heated by depriving exhaust gas discharged from the furnace of heat.

4. The CO 2 power generation system according to claim 3 , wherein
the furnace includes
an economizer provided at a discharge end of the exhaust gas that recovers waste heat of the exhaust gas,
a reheater provided above a combustor of the furnace that heats the working fluid,
a superheater provided at an upper side of the furnace that heats the working fluid, and
a second mixer provided at a rear end of the recuperator that mixes the working fluid passing through the economizer with the working fluid heated while passing through the recuperator via the second separator,

the working fluid heated by depriving the exhaust gas of heat is heated by the economizer, and
the working fluid passing through the reheater is heated by the superheater and is then circulated to the turbine.

5. A CO 2 power generation system, comprising:
a furnace that burns fuel;
a turbine that is supplied with a working fluid of supercritical CO 2 heated by heat generated in the furnace;
a recuperator that exchanges heat with the working fluid passing through the turbine;
a first separator provided at a rear of the turbine that branches the working fluid passing through the turbine into the recuperator and the furnace;
a cooler that cools the working fluid passing through the recuperator; and
a compressor that compresses the working fluid passing through the cooler,
wherein a cycle from the furnace to the compressor is a closed loop.

6. The CO 2 power generation system according to claim 5 , wherein
the working fluid branched to the recuperator is cooled by exchanging heat with a portion of the working fluid passing through the compressor, and
the working fluid branched to the furnace is cooled after heating air introduced into the furnace; and
the first separator controls a flow rate of the working fluid such that a temperature of the working fluid passing through the recuperator after heat exchange of the working fluid is equal to a temperature of the working fluid after the working fluid heats the air introduced into the furnace.

7. The CO 2 power generation system according to claim 6 , further comprising
a first mixer provided at a front of the cooler that mixes the working fluid discharged after heating the air introduced into the furnace with the working fluid cooled by the recuperator, and that supplies the mixed working fluid to the cooler; and
a second separator provided at a discharge of the compressor that branches the working fluid passing through the compressor into the furnace and the recuperator, wherein
a portion of the working fluid branched by the second separator is heated by the working fluid branched from the recuperator by the first separator, and
a remainder of the working fluid branched by the second separator is heated by depriving exhaust gas discharged from the furnace of heat.

8. The CO 2 power generation system according to claim 7 , wherein the furnace includes
an economizer provided at a discharge of the exhaust gas that recovers waste heat of the exhaust gas;
a reheater provided above a combustor of the furnace that heats the working fluid;
a superheater provided at an upper side of the furnace that heats the working fluid; and
a second mixer provided at a rear of the recuperator that mixes the working fluid passing through the economizer with the working fluid heated while passing through the recuperator via the second separator.

9. The CO 2 power generation system according to claim 8 , wherein
the working fluid heated by depriving the exhaust gas of heat is heated by the economizer;
the second separator controls a flow rate of the working fluid such that a temperature of the working fluid after heat exchange of the working fluid in the recuperator via the second separator is equal to a temperature of the working fluid passing through the economizer; and
the working fluid passing through the reheater is heated by the superheater and is then circulated to the turbine.

10. A CO 2 power generation system, comprising:
a turbine that is operated by a working fluid of supercritical CO 2 ;
a recuperator that exchanges heat with the working fluid passing through the turbine;
a cooler that cools the working fluid passing through the recuperator;
a first compressor that compresses the working fluid passing through the cooler;
a second compressor that compresses a portion of the working fluid passing through the recuperator;
a separator provided at a rear of the recuperator that branches the working fluid passing through the turbine into the cooler and the second compressor; and
a furnace into which the working fluid passing through the first and second compressors is introduced to be heated by combustion heat,
wherein the working fluid is circulated to the turbine via the furnace.

11. The CO 2 power generation system according to claim 10 , further comprising a separator provided at a rear of the recuperator that branches the working fluid passing through the turbine into the cooler and the second compressor.

12. The CO 2 power generation system according to claim 10 , wherein
the working fluid branched to the cooler by the separator is cooled by the cooler, and is then transferred to the first compressor,
the working fluid branched to the second compressor by the separator is compressed by the second compressor, and is then transferred to the furnace,
the working fluid transferred to the recuperator via the turbine is cooled by exchanging heat with the working fluid compressed by the first compressor, and is then transferred to the separator, and
the working fluid compressed by the first compressor is recuperated in the recuperator by exchanging heat with the working fluid transferred to the recuperator via the turbine, and is then transferred to the furnace.

Assignees

• Doosan Heavy Ind Constr Co Ltd

Inventors

• Hwang Jeong Ho
• Kang Seung Gyu
• Lee Eung Chan

Classifications

• F05D2210/12

  gaseous, i.e. compressible · CPC title

• F05D2220/60

  making use of surplus or waste energy · CPC title

• F01K3/20 Primary

  with heating by combustion gases of main boiler · CPC title

• F01K11/02

  the engines being turbines · CPC title

• F02C1/10

  Closed cycles · CPC title