System and method of controlling fuel cell system using a drain-purge valve
A system and method of controlling fuel cell system is provided that simultaneously drains condensation and purges hydrogen via single valve. In particular, condensate water is drained by opening a drain-purge valve at a point in time at which a production amount of the condensate water exceeds a capacity of a water trap. An opening time of the drain-purge valve is then determined depending on a hydrogen concentration of an anode side and a target hydrogen concentration after the draining the condensate water. Hydrogen is then purged by maintaining the drain-purge valve in a state in which it is opened for the determined opening time.
1. A method of controlling a fuel cell system, comprising:
draining, water from the fuel cell system by opening a drain-purge valve when a production amount of the water in the fuel cell system exceeds a capacity of a water trap;
determining, by a controller, an opening time, during which the drain-purge valve remains open after the draining has completed, depending on a hydrogen concentration of an anode side and a target hydrogen concentration; and
purging hydrogen by maintaining the drain-purge valve in an opened state for the determined opening time,
wherein the determining of the opening time of the drain-purge valve includes:
calculating a correction accumulated electric charge amount based on an output current of the fuel stack and a correction factor that becomes different depending on the output current;
calculating a hydrogen concentration depending on the calculated correction accumulated electric charge amount; and
determining the opening time according to the hydrogen concentration and a preset target hydrogen concentration,
wherein the correction factor is changed depending on an average current change rate and the average current change rate is determined depending on a comparison result between an average value of all current data and an average value of a preset number of current data measured last among all the current data.
2. The method of controlling a fuel cell system of claim 1 , wherein the draining of the water includes calculating a production amount of the water depending on rate of water generated which is calculated based on an average output current of a fuel cell stack.
3. The method of controlling a fuel cell system of claim 2 , wherein the average output current is an average value of a plurality of output current data measured over a preset period of time.
4. The method of controlling a fuel cell system of claim 3 , wherein the average output current is updated after a preset period of time.
5. The method of controlling a fuel cell system of claim 2 , wherein in the calculating of the production amount of the water, when a temperature of the fuel cell stack is different from a target operating temperature, the rate of water generated is calculated by multiplying a rate of water generated at the target temperature by a scale factor.
6. The method of controlling a fuel cell system of claim 1 , wherein the correction factor is changed to be less than a correction factor corresponding to the output current in the case in which the average current change rate increases and is changed to be greater than the correction factor corresponding to the output current when the average current change rate decreases.