Fuel cell with protection from pressure imbalance
US-11804608-B2 · Oct 31, 2023 · US
US12021278B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12021278-B2 |
| Application number | US-202318333996-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 13, 2023 |
| Priority date | Aug 21, 2018 |
| Publication date | Jun 25, 2024 |
| Grant date | Jun 25, 2024 |
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A fuel cell system includes a fuel cell. The fuel cell includes an anode having an anode inlet configured to receive anode feed gas, and an anode outlet configured to output anode exhaust. The fuel cell further includes a cathode having a cathode inlet and a cathode outlet. The fuel cell system further includes an anode blower configured to receive the anode exhaust and output a higher-pressure anode exhaust. The fuel cell system further includes an anode blower recycle line configured to receive a portion of the higher-pressure anode exhaust downstream from the anode blower and to output the portion of the higher-pressure anode exhaust upstream from the anode blower. The fuel cell system further includes a first valve disposed in the blower recycle line, the first valve configured to open when the anode of the fuel cell is under-pressurized.
Opening claim text (preview).
What is claimed is: 1. A fuel cell system, comprising: a fuel cell, comprising: an anode having an anode inlet configured to receive anode feed gas, and an anode outlet configured to output anode exhaust; and a cathode having a cathode inlet and a cathode outlet; a processing system configured to receive the anode exhaust from the anode outlet and to separate at least one of carbon dioxide or hydrogen from the anode exhaust to output processed anode exhaust; an anode blower having a blower inlet and a blower outlet, wherein the anode blower is downstream from the processing system and is configured to receive the processed anode exhaust at the blower inlet and output a higher-pressure anode exhaust at the blower outlet; a blower recycle line configured to receive a portion of the higher-pressure anode exhaust downstream from the anode blower and to output the portion of the higher-pressure anode exhaust upstream from the processing system and downstream from the anode outlet; and a first valve disposed in the blower recycle line, the first valve configured to open when the anode of the fuel cell is under-pressurized. 2. The fuel cell system of claim 1 , wherein the processing system separates carbon dioxide from the anode exhaust. 3. The fuel cell system of claim 1 , further comprising a second valve disposed in the blower recycle line, wherein the second valve is a pressure control valve configured to restrict an amount of the higher-pressure anode exhaust passing through the blower recycle line. 4. The fuel cell system of claim 1 , wherein: a first pressure differential is defined as a difference between a first pressure that is measured at one of the anode inlet or the anode outlet, and a second pressure measured at the cathode inlet; and the first valve is an automatic valve configured to open automatically when the first pressure differential drops below a pre-determined threshold amount. 5. The fuel cell system of claim 4 , further comprising a first pressure differential transmitter configured to measure and transmit the first pressure differential to a control system, wherein the control system is configured to send a signal to the first valve to open based on the first pressure differential transmitted from the first pressure differential transmitter. 6. The fuel cell system of claim 4 , further comprising: an anode exhaust line configured to receive anode exhaust from the anode; a vessel partially filled with water; a water seal downpipe extending away from the anode exhaust line and with at least a portion extending downward into the vessel, such that a water seal downpipe outlet is disposed in the water; and a vent defined in the vessel above a waterline, the vent configured to output anode exhaust. 7. The fuel cell system of claim 6 , wherein: a water level in the vessel is defined relative to a vertical position of the water seal downpipe outlet; and the water level provides a water seal pressure at the water seal downpipe outlet, such that anode exhaust is output through the vent when the first pressure differential is greater than the water seal pressure. 8. The fuel cell system of claim 4 , further comprising: an anode exhaust line configured to receive anode exhaust from the anode; a pressure relief line extending from the anode exhaust line; and a pressure relief valve disposed on the pressure relief line and configured to vent anode exhaust. 9. The fuel cell system of claim 8 , further comprising a heat sink disposed about the pressure relief line upstream from the pressure relief valve, the heat sink configured to absorb heat from anode exhaust. 10. The fuel cell system of claim 9 , further comprising a temperature sensor disposed between the heat sink and the pressure relief valve, the temperature sensor configured to measure a temperature of anode exhaust passing through the pressure relief valve. 11. The fuel cell system of claim 5 , further comprising a water seal comprising: an anode exhaust line configured to receive anode exhaust from the anode; a vessel partially filled with water; a water seal downpipe extending away from the anode exhaust line and with at least a portion extending downward into the vessel, such that a water seal downpipe outlet is disposed in the water; a reservoir partially filled with water and connected to a cathode inlet pipe such that a pressure over the reservoir is equal to a cathode inlet pressure; a water pipe connecting the vessel and the reservoir, the water pipe configured to permit water flow from the vessel to the reservoir during increases in an anode exhaust pressure and from the reservoir to the vessel during increases in the cathode inlet pressure; and a vent defined in the vessel above a waterline, the vent configured to output anode exhaust; wherein the water seal is configured to limit fuel cell anode pressure by having a water level adjusted by the cathode inlet pressure, thereby protecting the fuel cell system from anode over-pressurization by venting excess anode exhaust gas while maintaining a desired anode pressure during pressure upsets when the anode blower cannot maintain a desired anode-to-cathode pressure differential. 12. The fuel cell system of claim 5 , further comprising a differential pressure regulator configured to maintain a pressure at the anode outlet relative to a pressure at the cathode inlet by venting excess anode exhaust gas to atmosphere while maintaining a desired anode pressure during upsets when the anode blower cannot maintain a desired anode-to-cathode pressure differential, thereby protecting the fuel cell against anode over-pressurization. 13. A method of controlling pressure surge in a fuel cell system, comprising: receiving anode feed gas at an anode inlet; receiving cathode feed gas at a cathode inlet; outputting anode exhaust from an anode outlet; separating at least one of carbon dioxide or hydrogen from the anode exhaust using a processing system configured to receive the anode exhaust from the anode outlet and configured to output processed anode exhaust to a blower inlet of an anode blower; receiving the processed anode exhaust at the blower inlet; outputting higher-pressure anode exhaust from a blower outlet of the anode blower, wherein the higher-pressure anode exhaust has a higher pressure than the processed anode exhaust at the blower inlet; and receiving at least a portion of the higher-pressure anode exhaust at a blower recycle line configured to output the portion of the higher-pressure anode exhaust upstream from the processing system and downstream from the anode outlet. 14. The method of claim 13 , further comprising: measuring a first pressure at one of the anode inlet or the anode outlet; measuring a second pressure at the cathode inlet; determining a first pressure differential between the first pressure and the second pressure; opening a first valve disposed in the blower recycle line when the first pressure differential drops below a pre-determined pressure; passing a portion of the higher-pressure anode exhaust through the first valve; and receiving the portion of the higher-pressure anode exhaust from the blower recycle line at the blower inlet. 15. The method of claim 14 , further comprising passing a portion of the higher-pressure anode exhaust through a second valve disposed along the blower recycle line, wherein the second valve is configured to restrict an amount of the portion of the higher-pressure anode exhaust passing therethrough. 16. The method of claim 13 , further comprising: receiving anode exhaust at a
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by condensers, gas-liquid separators or filters · CPC title
Treatment of gaseous reactants or gaseous residues, e.g. cleaning · CPC title
of fuel cell reactants · CPC title
with recycling of the reactants (H01M8/04119, H01M8/04104 take precedence) · CPC title
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