Methods and systems for starting and stopping a closed-cycle turbomachine
The present disclosure relates to methods for starting and rapidly decelerating a turbomachine in a power generation system that utilizes a supercritical fluid in a closed cycle.
1. In a system for generating power utilizing a closed cycle with a working fluid, when the working fluid is in a supercritical state, the closed cycle including a turbomachine comprising a supercritical fluid compressor connected via a shaft to a supercritical fluid turbine, a method for starting the turbomachine comprising the steps of:
a) charging a mass of working fluid that is not in the supercritical state in the closed cycle up to a starting mass that is greater than a design operating mass, wherein the design operating mass is the mass of working fluid in the closed cycle when operating at steady-state design point conditions;
b) heating the working fluid; and
c) venting a discharge mass of working fluid from the closed cycle at a location in the closed cycle that is on an exhaust side of the supercritical fluid turbine.
2. The method of claim 1 , wherein the heating step further comprises heating the working fluid such that the working fluid is at or above the critical point of the working fluid prior to the venting step.
3. The method of claim 1 , wherein the heating step further comprises heating the working fluid such that the working fluid at an inlet of the supercritical fluid compressor is at or above the critical point of the working fluid prior to the venting step.
4. The method of claim 1 , wherein the heating step further comprises heating the working fluid to within a predetermined temperature range of a critical temperature of the working fluid prior to the venting step.
5. The method of claim 4 , wherein the predetermined temperature range is within 10 to 15 degrees Kelvin (° K) of the critical temperature of the working fluid.
6. The method of claim 4 , wherein the predetermined temperature range is within 5 to 10 degrees Kelvin (° K) of the critical temperature of the working fluid.
7. The method of claim 4 , wherein the predetermined temperature range is within 2 to 5 degrees Kelvin (° K) of the critical temperature of the working fluid.
8. The method of claim 4 , wherein the predetermined temperature range is within 1 to 2 degrees Kelvin (° K) of the critical temperature of the working fluid.
9. The method of claim 4 , wherein the predetermined temperature range is within 0.2 to 1 degrees Kelvin (° K) of the critical temperature of the working fluid.
10. The method of claim 1 , wherein venting the discharge mass reduces the mass of working fluid in the closed cycle from the starting mass to the design operating mass.
11. The method of claim 10 , wherein the venting step further comprises venting a second discharge mass of working fluid from the closed cycle that reduces the mass of working fluid in the closed cycle to an amount that is less than the design operating mass.
12. The method of claim 1 , wherein venting the discharge mass reduces the mass of working fluid in the closed cycle to an amount that is less than the starting mass but greater than the design operating mass.
13. The method of claim 1 , wherein the venting step further comprises controlling the rate at which the discharge mass is vented from the closed supercritical fluid cycle.
14. The method of claim 1 , wherein the turbomachine further comprises a supercritical fluid power turbine positioned along the closed cycle at a location that is on the exhaust side of the supercritical fluid turbine.
15. The method of claim 14 , further comprising a step of controlling a flow direction of the working fluid through the closed cycle.
16. The method of claim 15 , wherein the controlling the working fluid flow direction step is performed by one or more fluidic diodes.
17. The method of claim 15 , wherein the controlling the working fluid flow direction step is performed by one or more nozzles of the power turbine.
18. The method of claim 1 , wherein the discharge mass of working fluid is vented into a containment vessel.
19. The method of claim 1 , wherein the discharge mass of working fluid is vented to atmosphere.
20. The method of claim 1 , wherein the heating step further comprises transferring heat from a Thermal Energy Storage (TES) to the working fluid such that a temperature of the working fluid in the closed cycle is maintained above a critical temperature of the working fluid.
21. The method of claim 1 , wherein the working fluid is carbon dioxide.