Hydrogen consumption measuring method for fuel cell system
US-2017301931-A1 · Oct 19, 2017 · US
US12438170B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12438170-B2 |
| Application number | US-202217957368-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 30, 2022 |
| Priority date | Mar 8, 2022 |
| Publication date | Oct 7, 2025 |
| Grant date | Oct 7, 2025 |
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The present disclosure generally relates to systems and methods for operating a shutdown process in a fuel cell system including connecting a passive electrical load to a fuel cell stack in the fuel cell system before initiating the shutdown process, disconnecting a DC-DC converter by a system controller, initiating nitrogen blanketing after a current passing through the DC-DC converter is reduced to about zero, ensuring water content in the fuel cell stack is about zero, and sending a signal to the system controller to initiate the shutdown process.
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What is claimed is: 1. A method of operating a fuel cell system comprising: connecting a passive electrical load to a fuel cell stack comprising a membrane, an anode and a cathode, disconnecting a DC-DC converter by a system controller, initiating nitrogen blanketing after a current through the DC-DC converter is reduced to about zero, ensuring water content in the fuel cell stack is about zero, sending a signal to the system controller to initiate a shutdown process, and initiating the shutdown process in the fuel cell system, wherein the passive electrical load is configured to be connected during fuel cell system shutdown and disconnected during normal operation of the fuel cell system and the passive load is not a parasitic load when the fuel cell system is operating normally. 2. The method of claim 1 , wherein ensuring water content in the fuel cell stack is about zero further comprises by passing humidification of the fuel cell system by a humidification system. 3. The method of claim 1 , wherein ensuring water content in the fuel cell stack is about zero further comprises increasing air supply to the fuel cell stack and drying the membrane in the fuel cell stack. 4. The method of claim 1 , further comprising shutting down an air compressor, wherein air passes through the compressor before entering the cathode of the fuel cell stack. 5. The method of claim 1 , further comprising recirculating fuel while operating a recirculation pump at an operating speed of about 20% to about 50% of a maximum operating speed of the recirculation pump or blower. 6. The method of claim 5 , further comprising determining the operating speed of the recirculation pump based on a cell voltage balance across the fuel cell stack. 7. The method of claim 1 , further comprising closing an inlet air valve, wherein the fuel cell stack comprises the inlet air valve at a cathode inlet of the cathode and an exhaust air valve at a cathode outlet of the cathode. 8. The method of claim 7 , further comprising sealing the cathode inlet, and regulating the exhaust air valve to utilize oxygen deficient air in the fuel cell stack for pressure regulation at the cathode. 9. The method of claim 1 , wherein initiating nitrogen blanketing comprises regulating an anode pressure by a control valve, wherein the control valve controls hydrogen supply to the fuel cell stack. 10. The method of claim 9 , further comprising adjusting the anode pressure to minimize differential pressure across the membrane in the fuel cell stack, wherein the anode pressure is below ambient pressure. 11. The method of claim 9 , further comprising: setting the anode pressure equal to a cathode pressure, implementing a discharge resistor, and waiting for an average fuel cell voltage in the fuel cell stack to drop below about 0.026 V. 12. The method of claim 9 , further comprising: keeping a fuel supply valve open, and adjusting the anode pressure by toggling the control valve. 13. The method of claim 11 , further comprising: reducing a hydrogen supply pressure to about 20 kPa more than an ambient pressure, and depressurizing a hydrogen supply line up to the control valve. 14. The method of claim 13 , further comprising depressurizing the hydrogen supply line up to a fuel supply valve. 15. The method of claim 13 , further comprising turning off the control valve after a target vacuum is present at the anode. 16. The method of claim 15 , wherein the control valve is an electronically actuated control valve, a proportional control valve, a mechanical regulator, or an injector. 17. A fuel cell system comprising: a fuel cell stack comprising a membrane, and anode, and a cathode, a system controller configured to receive a signal to initiate shutdown of the fuel cell system, wherein the system controller is configured to disconnect a DC-DC converter, initiate nitrogen blanketing, and ensure water content in the fuel cell stack is about zero by performing a stack freeze operation, and a passive electrical load configured to connect to the fuel cell stack before the system controller receives the signal to initiate the shutdown, wherein the passive electrical load is not a parasitic load. 18. The fuel cell system of claim 17 , further comprising an inlet air valve at a cathode inlet of the cathode and an exhaust air valve at a cathode outlet of the cathode, wherein the cathode inlet is sealed and the exhaust air valve is controlled to regulate pressure at the cathode. 19. The fuel cell system of claim 17 , further comprising a physical or virtual sensing system to measure pressure in the anode or the cathode. 20. The fuel cell system of claim 17 , further comprising a proportional control valve, wherein the proportional control valve is turned off when the system controller detects an increase in anode pressure.
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