Heat recovery from an electrochemical hydrogen separation system

1. An electrochemical hydrogen separation (EHS) system, comprising:

an EHS cell comprising:

an anode;

a cathode; and

a cooling plate disposed proximate at least one of the anode or the cathode, the cooling plate configured to receive water and configured to output steam or a mixture of water and steam; and

a liquid-vapor separator (LVS) configured to receive the steam or the mixture of water and steam from the cooling plate and to separate water and steam;

wherein the LVS is configured to output water to the cooling plate.

2. The system of claim 1 , further comprising a saturator configured to receive steam from the LVS;

wherein the LVS is configured to output steam to the saturator.

3. The system of claim 2 , wherein the saturator is configured to receive water from the LVS.

4. The system of claim 3 , further comprising a heat exchanger configured to heat water from the saturator and output heated water to the saturator.

5. The system of claim 1 , wherein the cooling plate is configured to transfer heat from at least one of the anode or the cathode to the water passing through the cooling plate.

6. The system of claim 5 , wherein a temperature of the cooling plate is controlled by controlling a pressure in the LVS.

7. The system of claim 1 , further comprising a heater configured to receive and heat water from the LVS; and

wherein the cooling plate is configured to receive heated water from the LVS.

8. The system of claim 7 , wherein the cooling plate is configured to transfer heat from at least one of the anode or the cathode to the water passing through the cooling plate.

9. The system of claim 1 , wherein at least one of the anode or the cathode is configured to receive a current and electrochemically separate hydrogen from other gases.

10. A method of operating an electrochemical hydrogen separator (EHS) system, comprising:

passing water through a cooling plate disposed proximate at least one of an anode or a cathode in an EHS;

transferring heat from at least one of the anode or the cathode, through the cooling plate, to the water in the cooling plate;

vaporizing at least a portion of the water in the cooling plate into steam;

outputting a mixture of water and steam from the cooling plate;

receiving the mixture of water and steam from the cooling plate at a liquid-vapor separator (LVS); and

separating steam and water in the LVS.

11. The method of claim 10 , further comprising feeding water from the LVS to the cooling plate.

12. The method of claim 10 , further comprising mixing steam from the LVS with feed gas for a fuel cell; and

feeding a mixture of steam and feed gas to a saturator.

13. The method of claim 12 , wherein prior to being fed to the saturator, the mixture of steam and feed gas has a steam-to-carbon ratio less than 2.0.

14. The method of claim 13 , further comprising:

feeding steam from the LVS to the saturator; and

feeding water from the LVS to the saturator.

15. The method of claim 14 , further comprising vaporizing water from the saturator in a first heat exchanger;

outputting steam from the first heat exchanger to the saturator; and

mixing steam from the first heat exchanger with the mixture of steam and feed gas.

16. The method of claim 15 , wherein the mixture of steam and feed gas in the saturator has a steam-to-carbon ratio of approximately 2.0.

17. A method of operating an electrochemical hydrogen separator (EHS) system, comprising:

passing water through a cooling plate disposed proximate at least one of an anode or a cathode in an EHS;

transferring heat from the water through the cooling plate to at least one of the anode or the cathode;

receiving water from the cooling plate at a liquid-vapor separator (LVS);

heating water from the LVS in a heater; and

receiving water from the heater at the cooling plate.

18. The method of claim 17 , further comprising separating steam and water in the LVS; and

outputting steam from the LVS.

19. The method of claim 17 , further comprising feeding at least a portion of the water from the LVS to a saturator.

20. The method of claim 17 , further comprising introducing make-up water to the system upstream from the heater.