Complex supercritical CO2 generation system

Patent metadata

Field	Value
Publication number	US-10309262-B2
Application number	US-201715698518-A
Country	US
Kind code	B2
Filing date	Sep 7, 2017
Priority date	Jan 16, 2017
Publication date	Jun 4, 2019
Grant date	Jun 4, 2019

Abstract

The present invention relates to a complex supercritical CO 2 generation system capable of increasing the heat exchange efficiency to improve a system output. According to the present invention, a complex generation system of a bottoming cycle and a topping cycle is configured, a flow rate of a cold side outlet of a bottoming cycle recuperators provided in parallel is branched to be supplied to a recuperator of a topping cycle provided in series, thereby increasing heat exchange efficiency of the topping cycle.

First claim

What is claimed is:

1. A complex supercritical CO 2 generation system, comprising:
a bottoming cycle including
a compressor that compresses a working fluid,
a lower heat exchanger unit having a plurality of heat exchangers that are supplied with heat from an external heat source to heat the working fluid,
a lower turbine unit having a plurality of turbines that are driven by the working fluid,
a lower recuperator unit having a plurality of recuperators that are installed in parallel to each other and exchange heat between the working fluid having passed through the lower turbine unit and the working fluid having passed through the compressor to cool the working fluid having passed through the lower turbine unit, and
a pre-cooler that cools the working fluid primarily cooled by the lower recuperator unit and supplies the pre-cooled working fluid to the compressor; and

a topping cycle including
an upper heat exchanger unit that is supplied with the heat from the external heat source to heat the working fluid,
an upper turbine unit that is driven by the working fluid, and
an upper recuperator unit having a plurality of recuperators that are installed in series with each other and exchange heat between the working fluid having passed through the upper turbine unit and the working fluid supplied from the bottoming cycle to cool the working fluid having passed through the upper turbine unit, the working fluid cooled by the upper recuperator unit being supplied to the bottoming cycle,

wherein the bottoming cycle and the topping cycle share the compressor and the pre-cooler of the bottoming cycle.

2. The complex supercritical CO 2 generation system of claim 1 , wherein the bottoming cycle branches the working fluid at a downstream end of the compressor and supplies the branched working fluid to the topping cycle and the topping cycle recuperates the working fluid branched from the bottoming cycle using the upper recuperator unit and then supplies the recuperated working fluid to the upper turbine unit.

3. The complex supercritical CO 2 generation system of claim 2 , wherein some of the working fluid recuperated by a cold side recuperator among the recuperators of the lower recuperator unit in the bottoming cycle is branched and supplied to the topping cycle, and the topping cycle recuperates the working fluid branched from the bottoming cycle using a cold side recuperator among the recuperators of the upper recuperator unit, mixes the recuperated working fluid with the working fluid supplied from the cold side recuperator of the bottoming cycle to the topping cycle, and supplies the mixed working fluid to a hot side recuperator among the recuperators of the upper recuperator unit.

4. The complex supercritical CO 2 generation system of claim 3 , wherein the working fluid supplied to the hot side recuperator through the cold side recuperator of the topping cycle is recuperated by the hot side recuperator, reheated by a high temperature heater, and then supplied to the upper turbine unit, and the working fluid expanded by passing through the upper turbine unit is cooled by sequentially passing through the hot side recuperator and the cold side recuperator of the upper recuperator unit and then supplied to an upstream end of the pre-cooler of the bottoming cycle.

5. The complex supercritical CO 2 generation system of claim 4 , wherein the lower heat exchanger unit of the bottoming cycle includes a low temperature heater and a mid-temperature heater that exchange heat with low temperature and mid-temperature waste heat gases, the upper heat exchanger unit of the topping cycle includes the high temperature heater that exchanges heat with high temperature waste heat gas, and the waste heat gas sequentially passes through the high temperature heater, the mid-temperature heater, and the low temperature heater.

6. The complex supercritical CO 2 generation system of claim 5 , wherein the bottoming cycle further includes a first separator that branches the working fluid compressed by the compressor to the low temperature heater and the lower recuperator unit, respectively, a second separator that branches the working fluid branched to the lower recuperator unit to a hot side recuperator and a cold side recuperator, respectively, among the plurality of recuperators of the lower recuperator unit, and a third separator that is provided between the first separator and the compressor to branch the working fluid compressed by the compressor to the topping cycle and the first separator, respectively.

7. The complex supercritical CO 2 generation system of claim 6 , wherein the lower turbine unit of the bottoming cycle includes a first turbine and a second turbine, the working fluid recuperated by the hot side recuperator of the lower recuperator unit is supplied to the second turbine, some of the working fluid recuperated by the cold side recuperator of the lower recuperator unit is supplied to the topping cycle and some thereof is branched to be supplied to the mid-temperature heater, the working fluid branched to the mid-temperature heater is mixed with the working fluid heated by the low temperature heater to be supplied to the mid-temperature heater, and the working fluid supplied to the mid-temperature heater is heated by the mid-temperature heater and then supplied to the first turbine.

8. The complex supercritical CO 2 generation system of claim 2 , wherein the working fluid supplied to a hot side recuperator through a cold side recuperator of the topping cycle is recuperated by the hot side recuperator, reheated by the upper heat exchanger unit, and then supplied to the upper turbine unit, and the working fluid expanded by passing through the upper turbine unit is cooled by sequentially passing through the hot side recuperator and the cold side recuperator and then supplied to an upstream end of the pre-cooler of the bottoming cycle.

9. The complex supercritical CO 2 generation system of claim 8 , wherein the topping cycle further includes a separator that branches some of the working fluid cooled by sequentially passing through the hot side recuperator and the cold side recuperator, a second compressor that compresses the working fluid branched from the separator, and a mixer that is provided at a downstream end of the second compressor and the working fluid branched from the bottoming cycle and supplied to the cold side recuperator of the topping cycle and the working fluid having passed through the second compressor are mixed with each other by the mixer of the topping cycle to be supplied to the hot side recuperator.

10. The complex supercritical CO 2 generation system of claim 9 , wherein the lower heat exchanger unit of the bottoming cycle includes a low temperature heater and a mid-temperature heater that exchange heat with low temperature and mid-temperature waste heat gases, the upper heat exchanger unit of the topping cycle includes a high temperature heater that exchanges heat with high temperature waste heat gas, and the waste heat gas sequentially passes through the high temperature heater, the mid-temperature heater, and the low temperature heater.

11. The complex supercritical CO 2 generation system of claim 10 , wherein the bottoming cycle further includes a first separator that branches the working fluid compressed by the compressor to the low temperature heater and the lower recuperator unit, respectively, a second separator that branches the working fluid branched to the lower recuperator unit to a hot side recuperator and a cold side recuperator, respectively, among the recuperators of the lower recuperator unit, and a third separator that is provided between the first separator and the compre

Assignees

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

Inventors

• Bak Byoung Gu
• Kang Seung Gyu
• Hwang Jeong Ho
• Lee Eung Chan
• Jeong Cheol Rae

Classifications

• F02C1/04

  the working fluid being heated indirectly {(in a fluidised-bed combustor F02C3/205)} · 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

• F01K25/103 Primary

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

• F02C1/10

  Closed cycles · CPC title