Regenerative thermodynamic power generation cycle systems, and methods for operating thereof
A regenerative closed loop thermodynamic power generation cycle system is presented. The system includes a high-pressure expander to deliver an exhaust stream. A conduit is fluidly coupled to the high-pressure expander, which is configured to split the exhaust stream from the high-pressure expander into a first exhaust stream and a second exhaust stream. The system further includes a first low-pressure expander and a second low-pressure expander. The first low-pressure expander is coupled to a pressurization device through a turbocompressor shaft, and fluidly coupled to receive the first exhaust stream. The second low-pressure expander is coupled to the high-pressure expander and an electrical generator through a turbogenerator shaft, and fluidly coupled to receive the second exhaust stream. A method for operating the regenerative closed loop thermodynamic power generation cycle system is also presented.
1. A method for operating a regenerative closed loop thermodynamic power generation cycle system, comprising:
delivering an exhaust stream from a high-pressure expander;
splitting the exhaust stream from the high-pressure expander to a first exhaust stream and a second exhaust stream;
directing the first exhaust stream to a first low-pressure expander, wherein the first low-pressure expander is coupled to a pressurization device through a turbocompressor shaft;
directing the second exhaust stream to a second low-pressure expander, wherein the second low-pressure expander is coupled to the high-pressure expander and an electrical generator through a turbogenerator shaft; and
delivering a pressurized fluid stream above a critical point of a working fluid from the pressurization device and providing the pressurized fluid stream to the high-pressure expander.
2. The method of claim 1 , further comprising heating the exhaust stream before splitting the exhaust stream to the first exhaust stream and the second exhaust stream.
3. The method of claim 1 , further comprising heating the pressurized fluid stream before supplying the pressurized fluid stream to the high-pressure expander.
4. The method of claim 1 , further comprising delivering a third exhaust stream from the first low-pressure expander and a fourth exhaust stream from the second low-pressure expander and regeneratively supplying each of the third exhaust stream and the fourth exhaust stream to one or more heat exchangers.
5. The method of claim 4 , further comprising supplying the third exhaust stream and the fourth exhaust stream to a precooler through the one or more heat exchangers.
6. The method of claim 5 , further comprising receiving a cooled fluid stream from the precooler to supply the cooled fluid stream to the pressurization device.
7. The method of claim 1 , wherein splitting the exhaust stream from the high pressure expander comprises controlling a flow ratio of the first exhaust stream to the second exhaust stream.
8. A regenerative closed loop thermodynamic power generation cycle system, comprising:
a high-pressure expander to deliver an exhaust stream,
a conduit fluidly coupled to the high-pressure expander, and configured to split the exhaust stream into a first exhaust stream and a second exhaust stream;
a first low-pressure expander coupled to a pressurization device through a turbocompressor shaft, and fluidly coupled to receive the first exhaust stream; and
a second low-pressure expander coupled to the high-pressure expander and an electrical generator through a turbogenerator shaft, and fluidly coupled to receive the second exhaust stream, wherein the pressurization device is fluidly coupled to the high-pressure expander to supply a pressurized fluid stream above a critical point of a working fluid to the high-pressure expander.
9. The thermodynamic power generation cycle system of claim 8 , wherein the thermodynamic power generation cycle system forms a closed flow path for the working fluid.
10. The thermodynamic power generation cycle system of claim 9 , wherein the working fluid comprises carbon dioxide.
11. The thermodynamic power generation cycle system of claim 8 , wherein the pressurization device comprises a first compressor and a second compressor coupled to each other.
12. The thermodynamic power generation cycle system of claim 8 , wherein the pressurization device is fluidly coupled to the high-pressure expander through one or more heat exchangers.
13. The thermodynamic power generation cycle system of claim 12 , wherein the one or more heat exchangers comprise a first heat exchanger and a second heat exchanger fluidly coupled to each other.
14. The thermodynamic power generation cycle system of claim 12 , further comprising a first heat source fluidly coupled between the one or more heat exchangers and the high-pressure expander.
15. The thermodynamic power generation cycle system of claim 12 , wherein the one or more heat exchangers are further fluidly coupled to the first low-pressure expander and the second low-pressure expander to receive a third exhaust stream and a fourth exhaust stream.
16. The thermodynamic power generation cycle system of claim 8 , further comprising a second heat source fluidly coupled between the high-pressure expander and the conduit to receive the exhaust stream from the high-pressure expander and deliver a heated exhaust stream to the conduit.
17. The thermodynamic power generation cycle system of claim 8 , further comprising a pressure regulating valve to control a flow ratio of the first exhaust stream to the second exhaust stream.
18. The thermodynamic power generation cycle system of claim 8 , further comprising a precooler fluidly coupled to the pressurization device to supply a cooled fluid stream to the pressurization device.