Hydrogen-containing water generating electrode and hydrogen-containing water generating device
US-2015368816-A1 · Dec 24, 2015 · US
US10000855B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10000855-B2 |
| Application number | US-201514790045-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 2, 2015 |
| Priority date | Jul 2, 2014 |
| Publication date | Jun 19, 2018 |
| Grant date | Jun 19, 2018 |
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A multi-stack electrochemical hydrogen compressor (EHC) system is provided. The EHC system may have two or more EHC stacks, wherein each EHC stack includes at least one electrochemical cell and a power supply. The EHC system may also have a controller in communication with the power supply of each EHC stack, wherein the controller is configured to reduce total energy consumption of the EHC system by independently controlling the power supply of each EHC stack.
Opening claim text (preview).
What is claimed is: 1. A multi-stack electrochemical hydrogen compressor (EHC) system, comprising: two or more EHC stacks, wherein each EHC stack comprises; at least one electrochemical cell; and a power supply; a controller in communication with the power supply of each EHC stack; wherein the controller is configured to reduce total energy consumption of the EHC system by independently controlling the power supply of each EHC stack; a water distribution circuit configured to circulate water through each EHC stack; a coolant distribution circuit configured to circulate coolant through each EHC stack; and at least one sensor is disposed in the coolant distribution circuit at the outlet of each stack and is configured to generate a signal indicative of the coolant temperature at the outlet of the stack; at least one sensor disposed in the coolant distribution circuit, configured to generate a signal indicative of the coolant temperature at the inlet of each stack; wherein the EHC system is configured such that a coolant distribution through each stack is determined based on a temperature differential of the coolant through each stack. 2. The EHC system of claim 1 , wherein the controller is configured to control the power supply of each EHC stack including matching the power of each stack, while maintaining a total current flow to the system based on a desired hydrogen throughput. 3. The EHC system of claim 2 , wherein the controller is configured to control the power supply of each EHC stack by substantially matching the heat generation by each stack. 4. The EHC system of claim 1 , wherein the controller is configured to control the power supply of each EHC stack by substantially matching the electrical potential applied to each EHC stack while optimizing the current distribution applied to each EHC stack. 5. The EHC system of claim 4 , wherein a best performing EHC stack is configured to be the highest temperature stack and a worst performing EHC stack is configured to be the lowest temperature stack. 6. The EHC system of claim 1 , wherein the controller is further configured to increase stack durability by controlling the power such that the heat load of each stack is substantially equal. 7. The EHC system of claim 1 , wherein the sensors are configured to generate a signal indicative of the temperature difference across each EHC stack; wherein the controller is configured such that the temperature difference of each stack is utilized in determining a power distribution of the power supplies. 8. A method of controlling a multi-stack electrochemical hydrogen compressor (EHC) system having two or more EHC stacks, comprising: directing a gas stream containing hydrogen to the two or more EHC stacks; supplying power to the two or more EHC stacks from independent power supplies; and controlling the power independently supplied to each EHC stack; circulating water through each EHC stack; circulating coolant through each EHC stack; detecting the temperature of the coolant exiting each stack; detecting the temperature of the coolant entering each stack; calculating a temperature differential of the coolant through each stack; determining a coolant flow distribution through each stack based on the temperature differential of the coolant through each stack. 9. The method of claim 8 , wherein controlling the power reduces total energy consumption of the EHC system. 10. The method of claim 9 , wherein controlling the power includes matching the power of each EHC stack, while maintaining a total current to the system sufficient to meet a desired throughput of hydrogen. 11. The method of claim 10 , wherein controlling the power further comprises substantially matching heat load from each EHC stack. 12. The method of claim 8 , wherein controlling the power includes reducing a total power consumed by the system by substantially matching the electrical potential applied to each EHC stack while optimizing the current distribution applied to each EHC stack. 13. The method of claim 8 , wherein controlling the power includes supplying the most current to a best performing EHC stack of the system such that it is the highest temperature stack while supplying the least current to a worst performing EHC stack of the system such that it is the lowest temperature stack. 14. The method of claim 8 , wherein controlling the power includes substantially balancing the heat load of all the stacks in order increase stack durability. 15. The method of claim 8 , further comprising: detecting a temperature difference across each EHC stack; wherein controlling the power independently includes utilizing the temperature difference of each stack in determining a power distribution of the from the independent power supplies.
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