Solid oxide fuel cell system and method of stopping the same
A solid oxide fuel cell system includes: a fuel cell unit including a solid oxide fuel cell and a mixer, the solid oxide fuel cell including an anode gas passage and a cathode gas passage, the mixer mixing an anode off gas discharged from the anode gas passage and a cathode off gas discharged from the cathode gas passage; a power-generating raw material supply device operative to supply a power-generating raw material to the fuel cell unit; a combustible gas passage, which extends from the power-generating raw material supply device to a downstream end of the anode gas passage; an oxidizing gas supply device operative to supply an oxidizing gas to the cathode gas passage; and a controller operative to, after electric power generation by the fuel cell unit is stopped, control the power-generating raw material supply device to supply the power-generating raw material in a volume more than or equal to a volume of the combustible gas passage to the combustible gas passage, and concurrently control the oxidizing gas supply device to supply the oxidizing gas to the cathode gas passage.
1. A solid oxide fuel cell system comprising:
a fuel cell unit including a solid oxide fuel cell and a mixer, the solid oxide fuel cell including an anode gas passage and a cathode gas passage, the mixer mixing an anode off gas discharged from the anode gas passage and a cathode off gas discharged from the cathode gas passage;
a power-generating raw material supply device operative to supply a power-generating raw material to the fuel cell unit;
a combustible gas passage, which extends from the power-generating raw material supply device to a downstream end of the anode gas passage;
an oxidizing gas supply device operative to supply an oxidizing gas to the cathode gas passage; and
a controller operative to, after electric power generation by the fuel cell unit is stopped, control the power-generating raw material supply device to supply the power-generating raw material in a volume more than or equal to a volume of the combustible gas passage to the combustible gas passage, and concurrently control the oxidizing gas supply device to supply the oxidizing gas to the cathode gas passage.
2. The solid oxide fuel cell system according to claim 1 , wherein
the controller controls the oxidizing gas supply device such that a volume of the oxidizing gas supplied to the cathode gas passage after the electric power generation by the fuel cell unit is stopped is more than or equal to a volume of the cathode gas passage.
3. The solid oxide fuel cell system according to claim 2 , wherein
the controller controls the oxidizing gas supply device such that the supply of the oxidizing gas to the cathode gas passage is continued after the supply of the power-generating raw material to the combustible gas passage is stopped after the electric power generation by the fuel cell unit is stopped.
4. The solid oxide fuel cell system according to claim 1 , wherein
the mixer includes an ignitor operative to ignite and combust a mixed gas of the anode off gas and the cathode off gas, and
the controller controls the ignitor to ignite and combust the mixed gas of the anode off gas and the cathode off gas after the electric power generation by the fuel cell unit is stopped.
5. The solid oxide fuel cell system according to claim 4 , comprising an oxidizing gas passage, which extends from the oxidizing gas supply device to a downstream end of the cathode gas passage and through Which the oxidizing gas flows, wherein
the controller, in an operation stop process of the solid oxide fuel cell system, controls the oxidizing gas supply device to supply the oxidizing gas through the oxidizing gas passage, controls the power-generating raw material supply device to intermittently supply the power-generating raw material through the combustible gas passage, and controls the ignitor to ignite a combustible gas that is discharged to the mixer intermittently in accordance with the intermittent supply of the power-generating raw material.
6. The solid oxide fuel cell system according to claim 5 , wherein
the fuel cell unit includes a reformer operative to reform the power-generating raw material to generate a hydrogen-containing gas, and
the controller controls the oxidizing gas supply device and the power-generating raw material supply device to supply the power-generating raw material to the fuel cell unit intermittently while supplying the oxidizing gas to the fuel cell unit, such that a temperature of the reformer is lower than temperatures at which thermal decomposition of the power-generating raw material occurs.
7. The solid oxide fuel cell system according to claim 6 , wherein
the controller controls the oxidizing gas supply device and the power-generating raw material supply device to start supplying the power-generating raw material to the fuel cell unit while supplying the oxidizing gas to the fuel cell unit when the temperature of the reformer has decreased below the temperatures at which thermal decomposition of the power-generating raw material occurs and reached a lower limit temperature for water to exist as steam.
8. The solid oxide fuel cell system according to claim 5 , wherein
the controller controls the oxidizing gas supply device and the power-generating raw material supply device to supply the power-generating raw material to the fuel cell unit intermittently while supplying the oxidizing gas to the fuel cell unit, such that a temperature of the solid oxide fuel cell is lower than temperatures at which thermal decomposition of the power-generating raw material occurs.
9. The solid oxide fuel cell system according to claim 5 , wherein
the fuel cell unit includes a reformer operative to reform the power-generating raw material to generate a hydrogen-containing gas, and
the controller controls the oxidizing gas supply device and the power-generating raw material supply device to supply the power-generating raw material to the fuel cell unit intermittently while supplying the oxidizing gas to the fuel cell unit, such that a temperature of the reformer and a temperature of the solid oxide fuel cell are lower than temperatures at which thermal decomposition of the power-generating raw material occurs.
10. The solid oxide fuel cell system according to claim 1 , wherein
the fuel cell unit includes a hydrodesulfurizer operative to remove a sulfur compound from the power-generating raw material supplied from the power-generating raw material supply device.
11. The solid oxide fuel cell system according to claim 10 , wherein
the hydrodesulfurizer is heated by exhaust heat generated as a result of combusting a mixed gas of the anode off gas and the cathode off gas.
12. The solid oxide fuel cell system according to claim 10 , wherein
the controller controls the oxidizing gas supply device and the power-generating material supply device to start supplying the power-generating raw material to the fuel cell unit while supplying the oxidizing gas to the fuel cell unit when a temperature of the hydrodesulfurizer has decreased below temperatures at which thermal decomposition of the power-generating raw material occurs and reached a lower limit temperature for water to exist as steam.
13. A method of stopping a solid oxide fuel cell system, the method comprising:
stopping electric power generation by a fuel cell unit including a solid oxide fuel cell;
in a case where a passage extending from a power-generating raw material supply device to a downstream end of an anode gas passage of the solid oxide fuel cell serves as a combustible gas passage, after the electric power generation by the fuel cell unit is stopped, supplying a power-generating raw material in a volume more than or equal to a volume of the combustible gas passage to the combustible gas passage, and concurrently supplying an oxidizing gas to a cathode gas passage of the solid oxide fuel cell; and
mixing an anode off gas discharged from the anode gas passage and a cathode off gas discharged from the cathode gas passage, and combusting the mixed gas.
14. The method of stopping a solid oxide fuel cell system according to claim 13 , wherein
after the electric power generation by the fuel cell unit is stopped and when the supply of the power-generating raw material to the combustible gas passage is started, a temperature of the solid oxide fuel cell is not lower than 100° C. and not higher than 400° C.