Renewable combined cycle low turbine boost
A method and system for cost effectively converting a feedstock using thermal plasma, or other styles of gassifiers, into to a feedwater energy transfer system. The feedstock can be any organic material, or fossil fuel. The energy transferred in the feedwater is converted into steam which is then injected into the low turbine of a combined cycle power plant. Heat is extracted from gas product issued by a gassifier and delivered to a power plant via its feedwater system. The gassifier is a plasma gassifier and the gas product is syngas. In a further embodiment, prior to performing the step of extracting heat energy, there is provided the further step of combusting the syngas in an afterburner. An air flow, and/or EGR flow is provided to the afterburner at a rate that is varied in response to an operating characteristic of the afterburner. The air flow to the afterburner is heated.
1. A method of extracting heat energy from a gassifier and delivering the heat energy to a combined cycle power plant low turbine, the method comprising the steps of:
extracting heat energy from a gas product issued by the gassifier; and
delivering the extracted heat energy to a feedwater system of a combined cycle power plant.
2. The method of claim 1 , wherein the gassifier is a plasma gassifier.
3. The method of claim 1 , wherein the gassifier is inductively heated.
4. The method of claim 1 , wherein the gassifier is inductively heated and plasma assisted.
5. The method of claim 1 , wherein the gas product is syngas.
6. The method of claim 5 , wherein prior to performing said step of extracting heat energy there is provided the further step of combusting the syngas in an afterburner.
7. The method of claim 6 , wherein there is further provided the step of supplying an air flow to the afterburner.
8. The method of claim 7 , wherein said step of supplying an air flow to the afterburner is performed in excess of stoichiometric to cool an outlet charge of the afterburner.
9. The method of claim 7 , wherein said step of supplying air flow to the afterburner is performed at an approximately stoichiometric level.
10. The method of claim 7 , wherein said step of supplying an air flow to the afterburner is performed at a variable flow rate.
11. The method of claim 10 , wherein there is provided the further step of varying the flow rate of the air flow in response to an air/fuel ratio.
12. The method of claim 10 , wherein there is provided the further step of varying the flow rate of the air flow in response to an afterburner temperature characteristic.
13. The method of claim 7 , wherein there is further provided the step of preheating the air flow to the afterburner to reclaim energy from the system.
14. The method of claim 5 , wherein prior to performing said step of extracting heat energy there is provided the further step of combusting the syngas in an afterburner.
15. The method of claim 14 , wherein there is provided the further step of varying the flow rate of the recirculated exhaust gas in response to an afterburner temperature characteristic.
16. The method of claim 1 , wherein the gassifier is a plasma gassifier, and there is further provided the step of cooling a plasma torch by using an incoming feedwater from the combined cycle power plant.
17. The method of claim 1 , wherein there is provided the further step of supplementing the extracted heat energy with a selectable one of a liquid and a gaseous fuel, and an oxidant.
18. The method of claim 1 , wherein there is provided the further step of reducing emissions by subjecting the gas product to a ceramic media filter.
19. A method of providing heat energy from a plasma gassifier to a power plant, the method comprising the steps of:
issuing a gas product from the plasma gassifier
delivering the gas product to a heat exchanger arrangement;
delivering feedwater from the power plant to the heat exchanger arrangement;
extracting heat energy from the gas product in the heat exchanger arrangement;
delivering the extracted heat energy to the feedwater from the power plant in the heat exchanger arrangement; and
returning the feedwater with the extracted heat energy in the form of steam to a low steam turbine of a combined cycle power plant.
20. The method of claim 19 , wherein the plasma gassifier is provided with a plasma torch, and there is provided the further step of cooling the plasma torch with the feedwater of the power plant.
21. The method of claim 19 , wherein prior to performing said step of delivering the gas product to the heat exchanger arrangement, there is provided the further step of combusting the syngas in an afterburner.
22. The method of claim 21 , wherein there is further provided the step of supplying an air flow to the afterburner.
23. The method of claim 22 , wherein said step of supplying an air flow to the afterburner is performed at a variable flow rate responsive to an operating condition of the afterburner.
24. The method of claim 21 , wherein there is provided the further step of injecting recirculated exhaust gas (EGR) into the afterburner.
25. The method of claim 24 , wherein said step of injecting recirculated exhaust gas (EGR) into the afterburner is performed at a variable flow rate that is responsive to an operating condition of the afterburner.
26. The method of claim 19 , wherein there is provided the further step of supplementing the heat energy extracted in said step of extracting heat energy from the gas product in the heat exchanger arrangement with a selectable one of a liquid and a gaseous fuel, and an oxidant.
27. A method of providing heat energy from a gassifier to a power plant,
the method comprising the steps of:
issuing a gas product from the gassifier, the gassifier being an inductively heated gassifier;
delivering the gas product to a heat exchanger arrangement;
delivering feedwater from the power plant to the heat exchanger arrangement;
extracting heat energy from the gas product in the heat exchanger arrangement;
delivering the extracted heat energy to the feedwater from the power plant in the heat exchanger arrangement; and
returning the feedwater with the extracted heat energy in the form of steam to a low steam turbine of a combined cycle power plant.
28. The method of claim 27 , wherein the gassifier is an inductively heated and plasma assisted gassifier.