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 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, 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 of the 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 provided the further step of injecting recirculated exhaust gas into the afterburner.
8. The method of claim 7 , wherein there is provided the further step of varying the flow rate of the recirculated exhaust gas in response to the afterburner temperature characteristic.
9. The method of claim 6 , wherein there is further provided the step of supplying an air flow to the afterburner.
10. The method of claim 9 , 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.
11. The method of claim 9 , wherein said step of supplying air flow to the afterburner is performed at an approximately stoichiometric level.
12. The method of claim 9 , wherein said step of supplying an air flow to the afterburner is performed at a variable flow rate.
13. The method of claim 12 , wherein there is provided the further step of varying the flow rate of the air flow in response to an air/fuel ratio.
14. The method of claim 12 , wherein there is provided the further step of varying the flow rate of the air in response to an afterburner temperature characteristic.
15. A system for providing heat energy from a gasifier to a power plant, the system comprising:
a gasifier configured to issue a gas product; and
a heat exchanger, wherein the heat exchanger receives the gas product, extracts heat energy from the gas product, and delivers the heat energy to a feedwater of the power plant.
16. The system of claim 15 , wherein the gassifier is a plasma gasifier and is provided with a plasma torch.
17. The system of claim 16 , wherein the plasma torch is configured to be cooled with the feedwater of the power plant.
18. The system of claim 15 , further comprising a ceramic media filter configured to receive the gas product and to reduce emissions associated with the gas product.
19. A method of extracting heat energy from a gassifier and delivering the heat energy to a combined cycle power plant, 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 makeup water of the combined cycle power plant.
20. The method of claim 19 , wherein the gas product is syngas.