Systems and methods for reducing noncondensable gas buildup in coolant systems
Systems reduce noncondensable gasses within coolant systems with a recombiner into which the fluid coolant flows. Flow through the recombiner may be opposite that of a heat exchanger. The recombiner includes a catalyst that combines or degrades the noncondensable gasses, such as a Group 9-11 transition metal that speeds reaction of noncondensable gasses. The catalyst may be a liner, plate, aggregate, et. with openings through which all coolant must flow. The recombiner may be insulated to prevent heat exchange and condensation and may be tilted from a vertical to enhance draining and fluid flow. The entire system may be passive without any operator intervention or moving structures. Systems can be made from isolation condenser systems in nuclear power plants in an isolation condenser pool by adding a recombiner to existing coolant systems. Systems may also be made by including a recombiner with new isolation condensers.
1. A system for removing noncondensable gasses from coolant, the system comprising:
a condenser having an upper volume configured to receive a coolant having at least a part condensable vapor, a lower volume configured to return the coolant, and a plurality of heat exchange tubes connecting the upper and lower volumes so as to permit the coolant to flow in the tubes from the upper volume to the lower volume while condensing the vapor in the coolant; and
a recombiner connected between the upper volume and the lower volume, wherein the recombiner defines a flow path outside of the condenser, wherein the flow path is out of the lower volume, through the recombiner, and into the upper volume, and wherein the recombiner includes a catalytic material in the flow path configured to remove noncondensable gasses flowing into the recombiner from the lower volume.
2. The system of claim 1 , wherein the recombiner further includes an insulator configured to prevent condensation of the coolant.
3. The system of claim 1 , wherein the catalytic material is at least one of platinum and palladium.
4. The system of claim 1 , wherein the catalytic material lines the flow path of the recombiner.
5. The system of claim 1 , wherein the catalytic material is a plate with openings that spans the flow path of the recombiner.
6. The system of claim 1 , wherein the plurality of heat exchange tubes are aligned in parallel between the upper volume and the lower volume, and wherein the recombiner is angled between the upper volume and the lower volume so as to not be parallel with the heat exchange tubes.
7. The system of claim 1 , wherein the upper volume is an isolation condenser upper drum, and wherein the lower volume is an isolation condenser lower drum, the system further comprising:
an isolation condenser pool surrounding the condenser and the recombiner.
8. The system of claim 7 , further comprising:
a steam supply line configured to carry the coolant to the condenser; and
a condensate return line configured to carry the coolant from the condenser when condensed.
9. The system of claim 1 , wherein the system includes no powered pump or fan.
10. The system of claim 1 , further comprising:
a relief line connected to the upper volume and configured to provide steam as the coolant; and
a condensate return line connected to the lower volume and configured to return water condensed from the steam, wherein the condenser is one of a plurality of isolation condensers immersed in an isolation condenser pool.
11. The system of claim 10 , wherein the flow path is an insulated flow path through the isolation condenser pool.
12. The system of claim 10 , wherein the catalytic material is at least one of platinum and palladium.
13. The system of claim 10 , wherein the catalytic material lines an internal flow path of the recombiner.
14. The system of claim 10 , wherein the catalytic material is a plate with openings that spans an internal flow path of the recombiner.
15. The system of claim 10 , wherein the plurality of heat exchange tubes are substantially vertical, and wherein the flow path is angled with respect to the vertical.
16. The system of claim 10 , further comprising:
a boiling water nuclear reactor pressure vessel connected to the relief line and the condensate return line, wherein the relief line connects to the vessel vertically above where the condensate return line connects to the vessel.
17. A method of forming the system of claim 1 , the method comprising:
connecting the recombiner between the upper and lower volumes of the condenser, wherein the condenser has previously been installed in an isolation condenser pool in a nuclear power plant.
18. The method of claim 17 , wherein the connecting is performed while the isolation condenser pool is drained below the recombiner.
19. The method of claim 17 , wherein the connecting is performed during a maintenance outage of the nuclear power plant.
20. The method of claim 17 , wherein the recombiner is insulated from the isolation condenser pool.