Method and system for gas initiated natural circulation vertical heat recovery steam generator
US-2016312997-A1 · Oct 27, 2016 · US
US9982881B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9982881-B2 |
| Application number | US-201514693137-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 22, 2015 |
| Priority date | Apr 22, 2015 |
| Publication date | May 29, 2018 |
| Grant date | May 29, 2018 |
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The present disclosure is directed to a method and a system employing a gas introduced into the system as a startup operation for a natural circulation vertical heat recovery steam generator (HRSG) to initiate natural circulation of a fluid within the system. More specifically, the present disclosure is directed to a method and a system employing a gas introduced into an outlet header of an evaporator, into an outlet header of an evaporator and into one or more risers near the outlet header of the evaporator, or into one or more risers near the outlet header of the evaporator, to initiate natural circulation of a fluid in a desired system direction from the evaporator directly into a steam drum.
Opening claim text (preview).
The invention claimed is: 1. A vertical heat recovery steam generator system comprising: a gas turbine arranged to initiate a flow of hot gas upon start up; a steam drum; one or more downcomers; an evaporator with a plurality of evaporator tubes arranged perpendicular to the flow of hot gas; one or more risers; and a gas flow connector assembly fluidly connected to the one or more risers, for gas flow connector assembly introduction of a gas other than steam into the system prior to the start up of the gas turbine to reduce an average density of a fluid therein to thereby initiate natural circulation flow of the fluid therein in a direction from the one or more risers directly to the steam drum. 2. The system of claim 1 , wherein the gas flow connector assembly comprises a check valve and an isolation valve. 3. The system of claim 1 , wherein a pressure flow control valve controls flow of the gas to the gas flow connector assembly and into the system. 4. The system of claim 1 , wherein the gas flow connector assembly introduces the gas into the one or more risers at, near or adjacent to a header outlet of the evaporator. 5. The system of claim 4 , wherein the gas flow connector assembly introduces gas into the header outlet of the evaporator. 6. The system of claim 1 , wherein the introduction of gas into the system lowers the average fluid density of fluid in the one or more risers. 7. The system of claim 1 , wherein the introduction of gas into the system is ended when a fluid pressure in the steam drum increases to a preset value, with introduction of the gas being controlled by a pressure flow control valve. 8. The system of claim 1 , further comprising: a secondary gas flow connector assembly configured for introduction of a secondary gas into the system to reduce the average density of the fluid in the system to initiate natural circulation flow of the fluid therein, for flow circulation in the direction from the one or more risers directly to the steam drum; wherein the secondary gas flow connector assembly is configured to introduce the secondary gas at a secondary location that is different than a location at which the gas flow connector assembly introduces the gas other than steam. 9. A method for startup of a vertical heat recovery steam generator system comprising: introducing, prior to start up of an associated gas turbine, via a gas flow connector assembly, a gas other than steam into one or more risers, a header outlet of an evaporator, or both to lower the average fluid density of a fluid therein to initiate natural circulation fluid flow in a flow direction from the one or more risers, to a steam drum, to one or more downcomers, to the evaporator and back to the one or more risers. 10. The method of claim 9 , wherein the gas is introduced to initiate natural circulation fluid flow in a cold, warm or hot startup of the system. 11. The method of claim 9 , wherein the gas is air or nitrogen. 12. The method of claim 9 , wherein the fluid is water. 13. The method of claim 9 , wherein the evaporator comprises a plurality of evaporator tubes arranged horizontally, perpendicular to a flow of hot gas. 14. The method of claim 9 , wherein the gas flow connector assembly comprises a check valve to prevent back flow of fluid from a circulation loop into a gas system, and an isolation valve to isolate the gas system from the circulation loop. 15. The method of claim 9 , further comprising the step of: introducing via a secondary gas flow connector assembly a secondary gas, at a secondary location different than a location at which the gas flow connector assembly introduces the gas, into one or more risers, a header outlet of an evaporator or both so as to lower the average fluid density of the fluid therein to initiate natural circulation fluid flow in the flow direction from the one or more risers, to a steam drum, to one or more downcomers, to the evaporator and back to the one or more risers. 16. A vertical heat recovery steam generator system comprising: a steam drum; one or more downcomers; an evaporator with a plurality of evaporator tubes arranged perpendicular to a flow of hot gas; one or more risers having an inlet end and an outlet end, the outlet end fluidly coupled to the steam drum; a header having a header inlet fluidly coupled to the outlet end of the plurality of evaporator tubes, and a header outlet fluidly coupled to the inlet end of the one or more risers; a gas flow connector assembly configured to introduce a gas into the system at the one or more risers to reduce an average density of a fluid therein to initiate natural circulation flow of a fluid therein, for flow circulation in a direction from the one or more risers directly to the steam drum; and a secondary gas flow connector assembly configured to introduce a secondary gas into the system at the header outlet to reduce the average density of the fluid in the system to initiate natural circulation flow of the fluid therein, for flow circulation in the direction from the one or more risers directly to the steam drum. 17. The vertical heat recovery steam generator system of claim 16 , wherein both the gas flow connector assembly and the secondary gas flow connector assembly are configured to introduce the gas and the secondary gas, respectively, prior to start up of an associated gas turbine.
during the starting-up periods, i.e. during the periods between the lighting of the furnaces and the attainment of the normal operating temperature of the steam boilers · CPC title
of combined-circulation type, i.e. in which convection circulation due to the difference in specific gravity between cold and hot water is promoted by additional measures, e.g. by injecting pressure-water temporarily · CPC title
using the exhaust gases of gas-turbines · CPC title
Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT] · CPC title
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