Controller for estimating relative humidity and condensed water, and method for controlling condensed water drain using the same
US-9343762-B2 · May 17, 2016 · US
US9728798B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9728798-B2 |
| Application number | US-201414532528-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 4, 2014 |
| Priority date | Nov 5, 2013 |
| Publication date | Aug 8, 2017 |
| Grant date | Aug 8, 2017 |
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A fuel cell system includes a fuel cell stack having a membrane electrode assembly and an internal reactant gas passage, a unit that detects or estimates an actual retained water quantity (R.W.Q.), and a power generation control unit having a normal-time mode, a normal-time drying mode and a stop-time drying mode. In the normal-time drying mode, the fuel cell stack is caused to generate electric power while being dried more than in the normal-time mode until the actual R.W.Q. is decreased to a target R.W.Q. In the stop-time drying mode, when the actual R.W.Q. is equal to or more than a flooding threshold at a time of detection of a system stop instruction, the fuel cell stack is caused to generate electric power while being dried more than in the normal-time drying mode until the actual R.W.Q. is decreased to a target R.W.Q.
Opening claim text (preview).
What is claimed is: 1. A control method for a fuel cell system equipped with: a fuel cell that has a membrane electrode assembly which includes an electrolyte membrane, and an internal reactant gas passage through which reactant gas supplied to and discharged from the membrane electrode assembly flows; a retained water quantity grasping unit that detects or estimates an actual retained water quantity which is a current quantity of retained water retained in the internal reactant gas passage; and a power generation control unit that controls power generation of the fuel cell, the control method comprising: a step of, when the actual retained water quantity is equal to or more than a flooding threshold, by means of the power generation control unit, causing the system to be actuated in a normal-time drying mode in which the fuel cell is caused to generate electric power while being dried more than in a normal-time mode in which the fuel cell is caused to normally generate electric power in response to a required load, until the actual retained water quantity is decreased to a normal-time target retained water quantity; and a step of, when the actual retained water quantity is equal to or more than the flooding threshold at a time of detection of a system stop instruction, by means of the power generation control unit, causing the system to be actuated in a stop-time drying mode in which the fuel cell is caused to generate electric power while being dried more than in the normal-time drying mode until the actual retained water quantity is decreased to a stop-time target retained water quantity that is set to be smaller than the normal-time target retained water quantity. 2. The control method for a fuel cell system, according to claim 1 , further comprising a step of, by means of the power generation control unit, raising a temperature of the fuel cell in the stop-time drying mode to be higher than in the normal-time drying mode. 3. The control method for a fuel cell system, according to claim 1 , further comprising a step of, by means of the power generation control unit, increasing a pressure of oxidant gas which flows through the fuel cell in the stop-time drying mode to be higher than in the normal-time drying mode. 4. The control method for a fuel cell system, according to claim 1 , further comprising a step of, by means of the power generation control unit, increasing a flow rate of oxidant gas which flows through the fuel cell in the stop-time drying mode to be higher than in the normal-time drying mode. 5. The control method for a fuel cell system, according to claim 1 , wherein the fuel cell system further comprises a fuel gas circulation passage which allows fuel gas discharged from the fuel cell to circulate therethrough, and a circulation quantity control unit that controls circulation quantity of the fuel gas circulating through the fuel gas circulation passage, the control method further comprising a step of, by means of the power generation control unit, causing the circulation quantity control unit to increase circulation quantity of the fuel gas in the normal-time drying mode and the stop-time drying mode. 6. The control method for a fuel cell system, according to claim 1 , further comprising a step of, by means of the power generation control unit, increasing a flow rate of fuel gas which flows through the fuel cell in the normal-time drying mode and the stop-time drying mode. 7. The control method for a fuel cell system, according to claim 1 , further comprising a step of, by means of the power generation control unit, setting a current value of the fuel cell in the stop-time drying mode to a stop-time current value, the stop-time current being consumable in a stopped state of a vehicle. 8. The control method for a fuel cell system, according to claim 1 , wherein a target moisture quantity that is set when detecting a system stop instructions and predicting that a next actuation of the system is a low-temperature actuation is smaller than a target moisture quantity that is set when detecting the system stop instructions and predicting that the next actuation of the system is not a low-temperature actuation. 9. The control method for a fuel cell system, according to claim 1 , wherein the fuel cell system further comprises an anode system that includes a fuel gas storage unit in which fuel gas is stored, a fuel gas supply passage through which fuel gas flows from the fuel gas storage unit toward the fuel cell, a fuel gas discharge passage through which fuel gas from the fuel cell flows, a fuel gas circulation passage which connects the fuel gas supply passage and the fuel gas discharge passage to each other and allows fuel gas to circulate therethrough, and a discharge valve which discharges gas in the fuel gas discharge passage to an outside of the system, the control method further comprising: a step of, by means of the retained water quantity grasping unit, detecting or estimating a quantity of anode system retained water retained in the anode system; and a step of, when a determination that the quantity of anode system retained water is equal to or more than the flooding threshold is made, by means of the power generation control unit, causing the system to be actuated in the normal-time drying mode or the stop-time drying mode.
of fuel cell stacks · CPC title
of fuel cell reactants · CPC title
Fuel cells in motive systems, e.g. vehicle, ship, plane · CPC title
Humidity; Ambient humidity; Water content · CPC title
during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells · CPC title
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