Fuel cell system
View Patent ↗This cathode-side humidification tank 1038 also functions as a coolant tank. The water in the cathode-side humidification tank 1038 cools the fuel cell 1030 and returns to the cathode-side humidification tank 1038 . In the foregoing situations where the fuel cell 1030 is low in temperature, such as during the startup of the fuel cell system 1100 , the coolant warmed by the heat exchanger HEX 05 can also be supplied to the fuel cell 1030 to warm up the fuel cell 1030 . Moreover, a coolant channel 1040 for supplying a coolant to a cooling plate 1036 provided in the fuel cell 1030 is in connection with a heat exchanger HEX 06 which is formed in an anode-side humidification tank 1042 . Consequently, the coolant even plays the role of maintaining the cathode-side humidification tank 1038 and the anode-side humidification tank 1042 in almost the same temperatures.
1. A fuel cell system comprising:
a fuel cell stack including a laminate formed by combining a membrane electrode assembly composed of an electrolyte membrane, an anode jointed to one side of the electrolyte membrane, and a cathode joined to the other side of the electrolyte membrane, with a fuel channel plate having a fuel channel for supplying a fuel to the anode, an oxidant channel plate having an oxidant channel for supplying an oxidant to the cathode, and a heat-medium channel plate having a heat-medium channel for a heat medium to flow through;
a unit which cools the heat medium exhausted from the fuel cell stack before puffing the heat medium into the fuel cell stack for circulation;
a fuel humidifying unit which humidifies the fuel by heat exchange with the heat medium;
an oxidant humidifying unit which humidifies the oxidant by heat exchange with the heat medium; and
a control unit which stops power generation of the fuel cell in a system stopping process while continuing the circulation of the heat medium until a predetermined cooling stop condition holds.
2. The fuel cell system according to claim 1 , wherein
the control unit adjusts an amount of circulation of the heat medium so that a difference between a temperature of the heat medium exhausted from the fuel cell stack and a temperature of the heat medium put into the fuel cell stack falls within a predetermined range during a period in the system stopping process until the predetermined cooling stop condition holds.
3. The fuel cell system according to claim 1 , wherein
the control unit determines the cooling stop condition to be that a temperature of the heat medium exhausted from the fuel cell stack falls below a value determined as a function of outside air temperature.
4. The fuel cell system according to claim 1 , wherein
the control unit determines the cooling stop condition to be that a predetermined time elapses since the system stopping process is started.
5. A method for operating a fuel cell system comprising a reforming unit which reforms a raw fuel into a hydrogen-containing fuel, and a fuel cell which generates electric power from the fuel,
the method comprising supplying the fuel including carbon monoxide of a concentration higher than the concentration in a normal operation to the fuel cell when starting the fuel cell system.
6. The method for operating a fuel cell system according to claim 5 , comprising starting power generation of the fuel cell at a temperature lower than a normal power generation temperature of the fuel cell.
7. A method for operating a fuel cell system having a reforming unit which reforms a raw fuel into a hydrogen-containing fuel and a fuel cell which generates electric power from the fuel,
the method comprising: when stopping the fuel cell system,
supplying the fuel including carbon monoxide of a concentration higher than the concentration in a normal operation to the fuel cell;
cooling the fuel cell to a temperature lower than a normal power generation temperature of the fuel cell; and
stopping power generation of the fuel cell, following the cooling of the cell.