Electrochemical cell having a cascade seal configuration and hydrogen reclamation

US9567679B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9567679-B2
Application numberUS-201414192006-A
CountryUS
Kind codeB2
Filing dateFeb 27, 2014
Priority dateFeb 28, 2013
Publication dateFeb 14, 2017
Grant dateFeb 14, 2017

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

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.

First claim

Opening claim text (preview).

What is claimed is: 1. An electrochemical cell comprising: a pair of bipolar plates and a membrane electrode assembly located between the pair of bipolar plates, wherein the membrane electrode assembly comprises an anode, a cathode, and a proton exchange membrane disposed therebetween; 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; 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; 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 the first seal is configured to leak the first fluid into the intermediate pressure zone when the first seal unseats; and wherein at least one of the bipolar plates includes a first component and a second component and has a cascade seal configuration arranged between the first component and the 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 third seal defining a low pressure zone configured to contain a third fluid within the low pressure zone, wherein the second seal is configured to leak the second fluid into the low pressure zone when the second seal unseats. 3. The electrochemical cell of claim 2 , wherein the first seal is contained within the second seal and the second seal is contained with the third seal. 4. The electrochemical cell of claim 2 , wherein the first fluid is at a higher pressure than the second fluid and the second fluid is at a higher pressure than the third fluid. 5. The electrochemical cell of claim 2 , wherein the first seal, the second seal, and the third seal have a generally rectangular cross-section. 6. The electrochemical cell of claim 2 , 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. 7. The electrochemical cell of claim 2 , wherein the first fluid is high pressure hydrogen, the second fluid is lower pressure hydrogen, and the third fluid is coolant fluid. 8. The electrochemical cell of claim 2 , wherein the third fluid is nitrogen and the low pressure zone includes a nitrogen blanket surrounding the electrochemical cell configured to detect a leak of at least one of the first fluid and the second fluid from within the electrochemical cell. 9. The electrochemical cell of claim 2 , wherein the pressure of the third fluid 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. 10. 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, preventing the leaking of the first fluid, the second fluid, and the third fluid, when a closing force being applied to the pair of bipolar plates is greater than the opening force within the pair of bipolar plates. 11. The electrochemical cell of claim 2 , wherein the first seal is configured to unseat before the second seal or the third seal causing the first fluid to leak past the first seal into the intermediate pressure zone 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. 12. The electrochemical cell of claim 11 , wherein the second seal is configured to unseat causing the second fluid to leak past the second seal into the low pressure zone when the closing force further approaches the opening force causing a second separation of the pair of bipolar plates. 13. The electrochemical cell of claim 11 , wherein the first fluid that leaks into the intermediate pressure zone combines with the second fluid and is recycled and the second fluid that leaks into the low pressure zone combines with the third fluid and flows out of the electrochemical cell and is reclaimed. 14. The electrochemical cell of claim 2 , further comprising a pair of ancillary seals located outside the first seal and inside the second seal, wherein the pair of ancillary seals defines two ancillary high pressure zones in fluid communication with the high pressure zone. 15. An electrochemical cell comprising: a pair of bipolar plates and a membrane electrode assembly located between the pair of bipolar plates; 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; a high pressure zone located between the bipolar plates containing a first fluid; an intermediate pressure zone located between the bipolar plates containing a second fluid; and a low pressure zone containing a third fluid; wherein the electrochemical cell is configured to transition between a first configuration, a second configuration, and a third configuration based on at least one of a closing force applied to the bipolar plates and an opening force produced by a pressure of at least one of the first fluid, second fluid, and third fluid; and wherein at least one of the bipolar plates includes a first component and a second component and has a cascade seal configuration arranged between the first component and the second component, and the first component and the second component define a void that houses the flow structures and the membrane electrode assembly. 16. The electrochemical cell of claim 15 , wherein the first configuration provides substantially no leaking of fluid between the high pressure zone, the intermediate pressure zone, and the low pressure zone; the second configuration provides leaking of a portion of the first fluid from the high pressure zone to the intermediate pressure zone; and the third configuration provides leaking of a portion of first fluid from the high pressure zone to the intermediate pressure zone and leaking of a portion of second fluid from the intermediate pressure zone to the low pressure zone. 17. The electrochemical cell of claim 16 , further comprising a hydrogen reclamation apparatus in fluid communication with the low pressure zone of the electrochemical cell, wherein the hydrogen reclamation apparatus is configured to reclaim the portion of second fluid leaked into the low pressure zone and reintroduce the reclaimed second fluid into the intermediate pressure zone of the electrochemical cell, and where the pressure of the third fluid in the low pressure zone is monitored, and a rise in the pressure of the third fluid engages the hydrogen reclamation apparatus. 18. The electrochemical cell of claim 15 , wherein the high pressure zone is contained within the intermediate pressure zone and the intermediate pressure zone is contained within the low pressure zone. 19. The electrochemical cell of claim 15 , further comprising a first seal configured to contain the first fluid in the high pressure zone, a second seal configured to contain the second fluid in the intermediate pressure zone, and a third seal configured to contain the third fluid in the low pressure zone. 20

Assignees

Inventors

Classifications

  • Fuel cells · CPC title

  • Chemistry & Metallurgy · mapped topic

  • H01M8/006Primary

    Flat · CPC title

  • C25B9/206Primary

    Chemistry & Metallurgy · mapped topic

  • by electrolytic decomposition of the electrolytic solution or the formed water product · CPC title

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What does patent US9567679B2 cover?
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 de…
Who is the assignee on this patent?
Nuvera Fuel Cells Inc, Nuvera Fuel Cells Llc
What technology area does this patent fall under?
Primary CPC classification H01M8/006. Mapped technology areas include Electricity.
When was this patent published?
Publication date Tue Feb 14 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 2 related publications on this page (citations in our corpus or others sharing the same primary CPC).