Hydrogen generator, fuel cell system, and method for operating hydrogen generator
View Patent ↗The possibility of carbon deposition from a raw material gas is made lower than before in a pressure compensating operation carried out after stopping the stop process of a hydrogen generator and a fuel cell system including the hydrogen generator. The hydrogen generator includes: a raw material supply unit ( 102, 103 ) configured to function to block supply of a raw material; a steam supply unit ( 104, 105 ) configured to function to block supply of steam; a reformer 108 including a reforming catalyst 109 and configured to generate a hydrogen-containing gas by using the raw material supplied from the raw material supply unit and the steam supplied from the steam supply unit; a closing unit 116 configured to block at least a gas passage provided downstream of the reformer; and a controller 140 configured to execute a pressure compensating operation in which: during stop of the hydrogen generator, with hydrogen contained in the reformer, the supply of the raw material from the raw material supply unit and the supply of the steam from the steam supply unit are blocked, and the closing unit is closed; and to compensate a pressure decrease in the reformer due to a temperature decrease in the reformer after the closing of the closing unit, with the hydrogen contained in the reformer, the steam is supplied from the steam supply unit to the reformer.
1. A method for operating a hydrogen generator including a steam supply unit and a reformer including a reforming catalyst and configured to generate a hydrogen-containing gas by using a raw material and steam, the method comprising steps of:
(a) executing a sealing operation in which during stop of the hydrogen generator, with hydrogen contained in the reformer, communication between a gas passage containing at least the reforming catalyst and atmosphere is blocked to seal the reformer; and
(b) executing a pressure compensating operation in which, in order to compensate a pressure decrease in the reformer due to a temperature decrease in the reformer after the sealing operation, with the hydrogen contained in the reformer, the steam is supplied from the steam supply unit to the reformer.
2. The method according to claim 1 , further comprising a step of (c), in order to compensate the pressure decrease in the reformer due to the temperature decrease in the reformer after the sealing operation,
in a case where a temperature of the reforming catalyst is a temperature at which carbon in the raw material deposits on a surface of the reforming catalyst when the raw material flows through the reforming catalyst, executing a first pressure compensating operation of supplying the steam to the reformer in a state where the communication between the gas passage containing at least the reforming catalyst and atmosphere is blocked, and
in a case where the temperature of the reforming catalyst is a temperature at which the carbon in the raw material does not deposit on the surface of the reforming catalyst when the raw material flows through the reforming catalyst, executing a second pressure compensating operation of supplying the raw material to the reformer in a state where the communication between the gas passage containing at least the reforming catalyst and atmosphere is blocked.
3. The method according to claim 1 , wherein the step (b) is executed each time the temperature decrease in the reformer proceeds.
4. The method according to claim 1 , wherein:
the steam supply unit includes an evaporator configured to evaporate water, and
the method further comprises a step of:
(c) supplying the water to the evaporator for generation of the steam, an amount of the steam compensating at least the pressure decrease in the reformer due to the temperature decrease in the reformer.
5. A method for operating a hydrogen generator including a steam supply unit and a reformer including a reforming catalyst and configured to generate a hydrogen-containing gas by using a raw material and steam, the method comprising steps of:
(a) executing a sealing operation in which during stop of the hydrogen generator, with hydrogen contained in the reformer, communication between a gas passage containing at least the reforming catalyst and atmosphere is blocked to seal the reformer;
(b) executing a pressure compensating operation in which, in order to compensate a pressure decrease in the reformer due to a temperature decrease in the reformer after the sealing operation, with the hydrogen contained in the reformer, the steam is supplied from the steam supply unit to the reformer; and
(c) releasing to atmosphere a part of pressure of the steam supplied to the reformer, by discharging from the reformer a part of gas containing the steam, in the pressure compensating operation in the step (b).
6. The method according to claim 5 , wherein:
the hydrogen generator further includes a discharge passage through which the part of gas discharged in the step (c) flows, and
the method further comprises a step of:
(d) cooling the discharge passage in the pressure compensating operation in the step (b).
7. The method according to claim 5 , wherein:
the hydrogen generator further includes:
a discharge passage through which the part of gas discharged in the step (c) flows;
a combustor communicating with the discharge passage and configured to heat the reformer; and
an air supply unit configured to supply combustion air to the combustor, and
the method further comprises a step of:
(e) operating the air supply unit in the pressure compensating operation in the step (b).
8. The method according to claim 1 , wherein the step (b) is performed in a state where the hydrogen exists in the reformer, an amount of the hydrogen corresponding to an amount necessary to inhibit steam oxidation of the reforming catalyst.
9. The method according to claim 1 , wherein the step (b) is performed in a state where the communication between the gas passage containing at least the reforming catalyst and atmosphere is blocked.
10. The method according to claim 5 , further comprising a step of (f), in order to compensate the pressure decrease in the reformer due to the temperature decrease in the reformer after the sealing operation,
in a case where a temperature of the reforming catalyst is a temperature at which carbon in the raw material deposits on a surface of the reforming catalyst when the raw material flows through the reforming catalyst, executing a first pressure compensating operation of supplying the steam to the reformer in a state where the communication between the gas passage containing at least the reforming catalyst and atmosphere is blocked, and
in a case where the temperature of the reforming catalyst is a temperature at which the carbon in the raw material does not deposit on the surface of the reforming catalyst when the raw material flows through the reforming catalyst, executing a second pressure compensating operation of supplying the raw material to the reformer in a state where the communication between the gas passage containing at least the reforming catalyst and atmosphere is blocked.
11. The method according to claim 5 , wherein the step (b) is executed each time the temperature decrease in the reformer proceeds.
12. The method according to claim 5 , wherein:
the steam supply unit includes an evaporator configured to evaporate water, and
the method further comprises a step of:
(f) supplying the water to the evaporator for generation of the steam, an amount of the steam compensating at least the pressure decrease in the reformer due to the temperature decrease in the reformer.
13. The method according to claim 5 , wherein the step (b) is performed in a state where the hydrogen exists in the reformer, an amount of the hydrogen corresponding to an amount necessary to inhibit steam oxidation of the reforming catalyst.
14. The method according to claim 5 , wherein the step (b) is performed in a state where the communication between the gas passage containing at least the reforming catalyst and atmosphere is blocked.