Electrochemical cell having a cascade seal configuration and hydrogen reclamation
An electrochemical cell includes a pair of bipolar plates and a membrane electrode assembly between the bipolar plates. The electrochemical cell further includes a first seal defining a high pressure zone, wherein the first seal is located between the bipolar plates and configured to contain a first fluid within the high pressure zone. Further, the electrochemical cell includes a second seal defining an intermediate pressure zone, wherein the second seal is located between the bipolar plates and configured to contain a second fluid within the intermediate pressure zone. The first seal is configured to leak the first fluid into the intermediate pressure zone when the first seal unseats.
1. An electrochemical cell comprising:
a pair of bipolar plates;
a membrane electrode assembly, wherein the membrane electrode assembly comprises an anode, a cathode, and a proton exchange membrane disposed therebetween;
a first seal located between the bipolar plates and configured to partially define a high pressure zone; and
a pair of flow structures having gas diffusion layers, wherein the flow structures are positioned between the bipolar plates on each side of the membrane electrode assembly;
wherein at least one of the bipolar plates includes a first component and a second component and the first component and the second component define a void that houses the flow structures and the membrane electrode assembly.
2. The electrochemical cell of claim 1 , further comprising a second seal located between the bipolar plates and configured to partially define an intermediate pressure zone.
3. The electrochemical cell of claim 2 , further comprising a third seal located between the bipolar plates and configured to partially define a low pressure zone.
4. The electrochemical cell of claim 3 , wherein the first seal is contained within the second seal and the second seal is contained within the third seal.
5. The electrochemical cell of claim 3 , wherein the thickness of the third seal is greater than the second seal and the thickness of the second seal is greater than the first seal.
6. The electrochemical cell of claim 3 , wherein the high pressure zone is configured to contain high pressure hydrogen, the intermediate pressure zone is configured to contain lower pressure hydrogen, and the low pressure zone is configured to contain coolant fluid.
7. The electrochemical cell of claim 2 , wherein a pressure of a fluid in the low pressure zone is monitored and a rise in the pressure indicates an unseating of at least the second seal, and wherein the electrochemical cell is configured to shut down before the third fluid reaches a pressure at which the third seal unseats.
8. The electrochemical cell of claim 2 , wherein the first seal, the second seal, and the third seal within the pair of bipolar plates are configured to remain seated when a closing force being applied to the pair of bipolar plates is greater than the opening force within the pair of bipolar plates.
9. The electrochemical cell of claim 1 , wherein the first seal is formed from at least one of silicone, ethylenepropylene-diene-monomer (EPDM), fluoroelastomer, nitrile rubber (Buna-N), polytetrafluoroethylene (PTFE), polysulfone, polyetherimide, polychenylene sulfide, polyether ether ketone (PEEK), polyimide, polyethylene terephthalate (PET), polyethylene naphthalate (PEN), high-density polyethylene (HDPE), polyurethane, neoprene, acetal, nylon, polybutylene terephthalate, and acrylonitrile-butadiene rubber (NBR).
10. The electrochemical cell of claim 1 , wherein the first seal is a knife-edge type seal.
11. The electrochemical cell of claim 1 , wherein the electrochemical cell is at least one of a hydrogen fuel cell, hydrogen purifier, hydrogen expander, and hydrogen compressor.
12. The electrochemical cell of claim 1 , wherein the first seal has a generally rectangular cross-section.
13. The electrochemical cell of claim 4 , wherein the first seal is configured to unseat before the second seal or the third seal when a closing force applied to the pair of bipolar plates approaches an opening force within the pair of bipolar plates, which causes a first separation of the pair of bipolar plates.
14. The electrochemical cell of claim 13 , wherein the second seal is configured to unseat when the closing force further approaches the opening force causing a second separation of the pair of bipolar plates.