System and method using solar thermal energy for power, cogeneration and/or poly-generation using supercritical brayton cycles
US-2016047361-A1 · Feb 18, 2016 · US
US11098615B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11098615-B2 |
| Application number | US-201715711606-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 21, 2017 |
| Priority date | Sep 22, 2016 |
| Publication date | Aug 24, 2021 |
| Grant date | Aug 24, 2021 |
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Methods and systems of power generation that integrate SCO2 Brayton and Rankin steam power cycles with fossil fuel combustion, One such method involves combusting a fuel material with an oxidizer material in a combustor to produce heat and a combustion exhaust. At least a portion of the combustion exhaust and a first portion of heat produced by the combustion processing are fed to a SCO2 Brayton power cycle to produce power and a second exhaust. At least a portion of the second exhaust and a second portion of heat produced by the combustion processing are feed to a steam Rankine power cycle to produce additional power and a third exhaust.
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What is claimed is: 1. A method for generating power, the method comprising: combusting a fuel material with an oxidizer material in a combustor to produce heat and a combustion exhaust; separating the heat from the combustor into a first portion of heat produced by the combustion and a second portion of heat produced by the combustion; feeding at least a portion of the combustion exhaust and the first portion of heat directly to a SCO 2 Brayton power cycle to produce power and a second exhaust; feeding at least a portion of the second exhaust to a steam Rankine power cycle to produce heated steam and a third exhaust; feeding the second portion of heat directly to the steam Rankine power cycle to produce higher temperature steam from the heated steam; and introducing the higher temperature steam into a turbine to produce additional power. 2. The method of claim 1 wherein the fuel material comprises a fossil fuel material. 3. The method of claim 2 wherein the fossil fuel material is coal or natural gas. 4. The method of claim 1 wherein the feeding of the at least a portion of the combustion exhaust and the first portion of the heat to the SCO 2 Brayton power cycle to produce the power and the second exhaust comprises: introducing high temperature SCO2 into a SCO2 turbine to produce the power and a high temperature SCO2 turbine exhaust; and recouping at least a portion of a heat from the high temperature SCO2 turbine exhaust. 5. The method of claim 4 wherein the high temperature SCO2 is formed by a method comprising: introducing SCO2 into heat exchange communication with the at least a portion of the combustion exhaust to form heated SCO2; and introducing the heated SCO2 into heat exchange communication with the first portion of heat produced to form the high temperature SCO2. 6. The method of claim 4 wherein heat from the high temperature SCO2 turbine exhaust is recouped in the form of SCO2 at a temperature of at least 900° F. 7. The method of claim 6 wherein the SCO2 at a temperature of at least 900° F. is heated to a temperature of up to 1300° F. prior to introduction into the SCO2 turbine. 8. The method of claim 7 wherein the SCO2 at a temperature of at least 900° F. is heated in part by heat exchange communication with the combustion exhaust. 9. The method of claim 8 wherein the SCO2 at a temperature of at least 900° F. is heated by a method comprising: introducing the SCO2 at a temperature of at least 900° F. into heat exchange communication with the at least a portion of the combustion exhaust to form heated SCO2; and introducing the heated SCO2 into heat exchange communication with the first portion of heat produced to form the high temperature SCO2. 10. The method of claim 1 wherein the turbine expands the higher temperature steam at high temperature and high pressure to produce the additional power and a steam product at lower temperature and lower pressure; and repressurizing and reheating the steam product to at least in part to form the heated steam by heat exchange communication with the second exhaust. 11. The method of claim 10 wherein the heated steam is produced at least in part by heat exchange communication with the second exhaust. 12. The method of claim 1 wherein the second portion of heat produced does not feed through the SCO 2 Brayton power cycle. 13. The method of claim 1 , further comprising: heating a turbine steam discharge produced by the turbine with a second part of the second portion of heat to produce a reheated steam; and introducing the reheated steam into a second turbine to produce a second additional power. 14. A method for generating power, the method comprising: combusting a fuel material with an oxidizer material in a fluidized bed combustor to produce combustion heat and a combustion exhaust; heating SCO2 with at least a portion of the combustion exhaust in a first convective heat exchanger of a SCO2 Brayton power cycle to form heated SCO2 and a second exhaust; further heating the heated SCO2 with a first portion of the combustion heat in a first in-bed heat exchanger to form higher temperature SCO2; introducing the higher temperature SCO2 into a first turbine to produce power and a turbine SCO2 discharge; recycling the turbine SCO2 discharge from the turbine back to the first convective heat exchanger; feeding at least a portion of the second exhaust to a second convective heat exchanger of a steam Rankine power cycle to produce heated steam and a third exhaust; further heating the heated steam with a second portion of the combustion heat in a second in-bed heat exchanger of the steam Rankine power cycle to produce higher temperature steam; introducing the higher temperature steam into a second turbine to produce additional power and a turbine steam discharge; and recycling the turbine steam discharge from the second turbine back to the second convective heat exchanger. 15. The method of claim 14 wherein the second portion of the combustion heat does not feed through the SCO 2 Brayton power cycle.
Heat transfer, e.g. cooling · CPC title
Carbon dioxide (F01K25/065 takes precedence) · CPC title
using industrial or other waste gases · CPC title
Combustion apparatus characterised by means creating a distinct flow path for flue gases or for non-combusted gases given off by the fuel · CPC title
Combustors or associated equipment · CPC title
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