JP2010272343A - Fuel cell system - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a fuel cell system that is advantageous to suppress freezing of a drain section farther downstream than a condensed water tank in which the condensed water is stored. <P>SOLUTION: The system includes a fuel cell 1; the condensed water tank 30 for storing the condensed water generated in accordance with a power generation operation of the fuel cell 1; the drain section 32 for discharging surplus water in the condensed water tank 30 to the outside; a hot water storage system 130 that has a hot-water storage vessel 131 for storing the hot water heated by the heat generated accompanying the power generation operation of the fuel cell 1; a hot-water passage 50 capable of supplying heat energy of the hot water in the hot-water storage system 130 to the drain section 32, and a hot-water valve 52. When there is a possibility that the drain section 32 may be frozen, or when the drain part 32 is frozen, the control part 5 makes the hot-water valve 52 released and supplies the heat energy of the hot water in thehot-water storage system 130 to the drain section 32 via the hot-water passage 50, and suppress freezing of the drain section 32. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to a fuel cell system having a hot water storage system for storing hot water generated by power generation.

  The fuel cell system includes a fuel cell that performs a power generation operation using an anode fluid and a cathode fluid, a condensed water tank that stores condensed water generated during the power generation operation of the fuel cell, and discharges excess water in the condensed water tank to the outside. And a hot water storage system having a hot water storage tank for storing hot water heated by heat generated by the power generation operation of the fuel cell. If the drain part freezes, the excess water collected in the system will not be discharged, the water in the condensate tank overflows from the condensate tank, enters the parts in the housing, etc., and the power generation operation of the system is stopped. is there.

  Furthermore, Patent Document 1 discloses a fuel cell system in which a heater for preventing freezing is provided on the entire bottom of the casing. According to this, it is considered that freezing in the vicinity of the drain portion is suppressed by the heat generated by the heater. Further, in claim 9 of Patent Document 1, when there is a possibility that the water supply passage for supplying fresh water to the hot water storage tank may freeze, the hot water of the hot water storage tank is continuously supplied to the condensed water tank by supplying hot water from the hot water storage passage. By reducing the level of the hot water, the hot water storage tank is continuously replenished with fresh water via the water supply passage. According to this apparatus, when there is a possibility that the water supply passage may freeze, fresh water is continuously supplied from the water supply passage to the hot water storage tank, so that fresh water continuously flows in the water supply passage. to continue. Therefore, freezing in the water supply passage is suppressed by continuous water flow.

JP 2005-259494 A

  According to the technique according to Patent Document 1 described above, although the freezing in the vicinity of the drain portion is suppressed by the heat generated by the heater provided at the bottom of the housing, there is a limit to the prevention of the drain portion from freezing. Furthermore, according to the technique according to claim 9 of Patent Document 1, as described above, a system is adopted in which hot water stored in a hot water tank is supplied to a condensed water tank. Here, the condensed water stored in the condensed water tank is condensed water obtained by condensing water vapor, has an extremely low impurity concentration, has a high pure water content, and has improved water vapor reforming in the reformer. Used for quality reactions.

  In contrast, hot water stored in a hot water storage tank is basically tap water supplied from a water pipe and used as hot water for home use or business use. It is not water with high purity, containing a large amount of various ions such as chlorine ions, iron ions, silica ions and the like. For this reason, when warm water is supplied to a condensed water tank, there exists a possibility that the purity of the water stored in the condensed water tank may fall large. In this case, the lifetime of the ion exchanger that removes the aforementioned ions from the condensed water is reduced.

  The present invention has been made in view of the above circumstances, and is advantageous for suppressing freezing of the drain portion of the condensed water tank in which condensed water accumulates even if the temperature is lowered, and is stored in the condensed water tank. It is an object of the present invention to provide a fuel cell system that is advantageous in ensuring the cleanliness of condensed water.

  A fuel cell system according to the present invention is provided with a fuel cell that performs a power generation operation using an anode fluid and a cathode fluid, a condensate water tank that stores condensate generated during the power generation operation of the fuel cell, and a downstream of the condensate water tank. A drain part for discharging excess water in the condensed water tank to the outside, a hot water storage system having a hot water storage tank for storing hot water heated by the heat generated by the power generation operation of the fuel cell, a hot water storage system and a drain part Hot water passage that can connect and supply hot water from a hot water storage system to the drain portion, a hot water valve that can open and close the hot water passage, and when the drain portion is likely to freeze, or when the drain portion is frozen, A controller that suppresses freezing of the drain part of the condensate water tank by supplying the thermal energy of the hot water of the hot water storage system to the drain part via the hot water passage. Comprising.

  “Supplying the hot energy of hot water in the hot water storage system to the drain part via the hot water passage” means that the hot water in the hot water storage system and the drain part are heated in addition to supplying the hot water in the hot water system directly to the drain part. This includes the case where the heat energy is indirectly supplied to the drain part through heat exchange through the exchanger. According to the present invention, when there is a possibility that the drain part is frozen or when the drain part is frozen, the control part opens the hot water valve and supplies the thermal energy of the hot water of the hot water storage system to the drain part. As a result, the temperature of the drain portion rises and the freezing of the drain portion is suppressed.

  Further, according to the present invention, hot water in the hot water storage system is supplied to the drain part to suppress freezing of the drain part, but is not supplied to the condensed water tank that stores condensed water. Therefore, the cleanliness of the condensed water stored in the condensed water tank is ensured satisfactorily. Therefore, even when the condensed water stored in the condensed water tank is used as the reformed water, it is possible to suppress the ions that lower the purity of the water from being supplied to the ion exchanger.

  According to the present invention, when there is a possibility that the drain part is frozen or when the drain part is frozen, the control part opens the hot water valve and drains the thermal energy of the hot water in the hot water storage system via the hot water passage. Supply to the department. Thereby, the temperature of the drain part of a condensed water tank rises, and freezing of a drain part is suppressed.

  According to the present invention, hot water in the hot water storage system is supplied to the drain portion to suppress freezing of the drain portion, but is not supplied to the tank for storing condensed water. Therefore, the cleanliness of the condensed water stored in the condensed water tank is ensured satisfactorily. Therefore, even when the condensed water stored in the condensed water tank is used as the reforming water, it is possible to suppress impurity ions that reduce the purity of the water from being supplied to the ion exchanger. In this case, the life of the ion exchanger is suppressed from being shortened in an unexpected short period, and deterioration of the reformer, the piping connected to the reformer, and the electrolyte of the fuel cell can be suppressed, and these lifetimes can be extended. Can contribute.

1 is an overall system diagram of a fuel cell system according to Embodiment 1. FIG. 10 is a flowchart executed by a control unit according to the second embodiment. FIG. 10 is a system diagram of the entire fuel cell system according to Embodiment 3. 10 is a flowchart executed by a control unit according to the third embodiment. FIG. 10 is a system diagram of a fuel cell system according to Embodiment 4. FIG. 10 is a system diagram of a fuel cell system according to Embodiment 6.

  According to a preferred embodiment of the present invention, the first temperature sensor for detecting the temperature of the cathode gas or the outside air before being supplied to the fuel cell is provided, and the controller detects the temperature detected by the first temperature sensor. When it is lower than the first threshold, the hot water valve can be opened. In this case, warm water is supplied to the drain part, and the drain part is warmed to prevent freezing. The first temperature sensor can detect the temperature of the cathode gas in the housing before being supplied to the cathode gas transport source as the temperature of the cathode gas before being supplied to the fuel cell. As parameters for determining whether or not there is a possibility of the drain portion being frozen, in addition to the cathode gas and the outside air temperature, the temperature of the condensed water tank or the drain portion itself disposed in the housing and the surrounding temperature are the first temperature. The sensor may detect it. The term “periphery” refers to a region having a temperature substantially equal to the temperature of the drain portion, and a plan area range (including the drain portion) that is a predetermined multiple (within 7 times) of the projected area of the drain portion in plan view. .

  According to a preferred embodiment of the present invention, either the first temperature sensor for detecting the temperature of the cathode gas or the outside air before being supplied to the fuel cell or the drain temperature sensor for detecting the temperature of the drain part is provided. Yes. In this case, when the temperature detected by the first temperature sensor is lower than the first threshold or when the condition that the temperature detected by the drain temperature sensor is lower than the second threshold is satisfied, The hot water valve can be opened to supply hot water to the drain part. It is avoided that cold water is supplied to the drain part. The temperature of the drain part includes the temperature of the drain part itself and the temperature around the drain part. Examples of the temperature of the cathode gas before being supplied to the fuel cell detected by the first temperature sensor include the temperature of air before being sucked into the cathode gas transport source in the housing.

  According to a preferred embodiment of the present invention, either the first temperature sensor for detecting the temperature of the cathode gas or the outside air before being supplied to the fuel cell or the drain temperature sensor for detecting the temperature of the drain part is provided. In addition, a hot water temperature sensor for detecting the temperature of the hot water in the hot water storage system is provided. In this case, the control unit satisfies the condition that the temperature detected by the first temperature sensor is lower than the first threshold value, or the temperature detected by the drain temperature sensor is lower than the second threshold value, and When the condition that the temperature detected by the hot water temperature sensor is higher than the third threshold is satisfied, the hot water valve can be opened to supply hot water to the drain portion. Supply of low-temperature hot water to the drain part is suppressed, and excessive freezing of the drain part is suppressed.

  According to a preferred embodiment of the present invention, a hot water temperature sensor for detecting the temperature of hot water in the hot water storage system is provided, and the control unit is configured such that when the temperature detected by the first temperature sensor is lower than the first threshold value, and When the temperature detected by the hot water temperature sensor is higher than the third threshold value, the hot water valve can be opened to supply hot water to the drain part. In this case, supply of low-temperature warm water to the drain part is suppressed, and excessive freezing of the drain part is suppressed.

  According to a preferred embodiment of the present invention, there is provided a reforming section for generating an anode fluid supplied to the anode of the fuel cell from a fuel material by a reforming reaction. In this case, when there is a possibility that the drain part is frozen, or when the drain part is frozen, the control unit causes the condensed water stored in the condensed water tank to be supplied to the reforming unit as reformed water, The water level in the condensed water tank can be lowered as much as possible. In this case, the flow rate of the drain water discharged from the condensed water tank to the drain portion is reduced, excessive freezing of the drain portion is suppressed, and the drain portion is easily thawed with thermal energy.

  According to a preferred embodiment of the present invention, a reforming section for generating an anode fluid supplied to the anode of a fuel cell from a fuel material by a reforming reaction, and heating the reforming section so that the reforming section is suitable for the reforming reaction. A burner is provided. In this case, when there is a possibility that the drain part is frozen or when the drain part is frozen, the control part is supplied to the flow rate of combustion air burned by the burner and / or the cathode of the fuel cell. Increase the flow rate of cathode gas. When the flow rate of the combustion air burned by the burner increases, the flow rate of the exhaust gas discharged from the burner to the outside increases. In this specification, the flow rate means a flow rate per unit time.

  When the flow rate of the cathode gas supplied to the cathode of the fuel cell is increased, the flow rate of the cathode off gas discharged from the cathode to the outside increases. As a result, the amount of moisture taken out by the exhaust gas or the cathode off gas increases. Therefore, the flow rate of the condensed water generated in the entire system decreases, the flow rate of the condensed water stored in the condensed water tank decreases, and the water level of the condensed water tank decreases. Therefore, the flow rate of the drain water discharged from the condensed water tank to the drain portion is reduced, excessive freezing of the drain portion is suppressed, and the drain portion is easily thawed.

  According to the preferable form of this invention, it is preferable that the heat exchanger which can exchange heat with a drain part and gives the thermal energy of warm water to a drain part is provided in the warm water channel | path.

(Embodiment 1)
Hereinafter, Embodiment 1 of the present invention will be described with reference to FIGS. 1 and 2.

(overall structure)
In FIG. 1, a fuel cell system 100 (hereinafter also simply referred to as a system) is a stationary device installed in a general household, a business store, a building, or the like, and has a cooling passage 10 through which a coolant such as cooling water flows. The battery stack 1 includes a main cooling circuit 2 that cools the stack 1 by flowing a cooling liquid through the cooling passage 10 of the stack 1, and a housing 6 having a storage chamber 60 for storing them. The housing 6 includes an outside air inlet 62 that takes in outside air, and a first temperature sensor 63 that detects the temperature T3 of the outside air taken in from the outside air inlet 62. The membrane electrode assembly of the stack 1 is an ion conductive membrane sandwiched between an anode (fuel electrode) and a cathode (oxidant electrode) (for example, a solid polymer type such as a fluorocarbon type or a hydrocarbon type, or an inorganic material type) Electrolyte sheet) and may be a sheet type or a tube type.

  According to the present embodiment, as shown in FIG. 1, the outlet temperature sensor 21, the heater 29, the first heat exchanger 22, the first heat exchanger 22, the outlet 10 p to the inlet 10 i of the cooling passage 10 of the stack 1 in the main cooling circuit 2. One pump 23 (first transport source), an anode condenser 24, and an inlet temperature sensor 20 are provided in series. The heater 29 warms the coolant when the temperature of the coolant flowing through the main cooling circuit 2 is excessively low, such as when the stack 1 is started. During steady operation of the stack 1, the heater 29 is basically turned off.

  When the first pump 23 is actuated, the cooling water of the main cooling circuit 2 receives heat at the anode condenser 24, passes through the inlet temperature sensor 20, flows from the inlet 10 i of the stack 1 to the cooling passage 10, and receives heat from the stack 1, It is discharged from the outlet 10p through the cooling passage 10, and further flows through the temperature sensor 21, the heater 29, and the first heat exchanger 22 in this order. For this reason, the heat generated when the stack 1 generates power is recovered in the cooling water of the main cooling circuit 2. Further, the heat of the anode gas generated in the reformer 70 is recovered in the cooling water of the main cooling circuit 2 through the anode condenser 24. The cooling water for the main cooling circuit 2 is a liquid having a low electrical conductivity.

  The anode gas supply system 7 that supplies anode gas (for example, fuel such as hydrogen-containing gas) to the anode that is the fuel electrode of the stack 1 will be described. The anode gas supply system 7 includes a reformer 70 having a reforming unit 70a and a burner 71 that heats the reforming unit 70a so as to be suitable for the reforming reaction, and an air pump 72 that supplies combustion air to the burner 71 ( Combustion air carrier source), fuel pump 73 (fuel carrier source) for supplying fuel (hydrocarbon gas such as natural gas) to the reformer 70a and burner 71, outlet 70p of the reformer 70 and the stack 1 And an anode gas passage 76 (fuel passage) that connects the anode inlet to the anode inlet 24 via an anode condenser 24 and an anode inlet valve 75.

Here, the anode gas mainly containing hydrogen generated in the reformer 70 is supplied to the anode (fuel electrode) of the stack 1 through the anode gas passage 76. A CO reduction unit 77 is provided on the outlet side of the reformer 70. The CO reduction unit 77 includes a CO shift unit 78 having a catalyst that promotes a shift reaction that reduces the concentration of CO contained in the anode gas generated by the reformer 70 by the shift reaction of Formula (1); The CO gas contained in the anode gas that has passed through the shift unit 78 is oxidized by the equation (2) to form a CO oxidation unit 79 having a catalyst that promotes an oxidation reaction that further reduces the CO concentration. CO is not preferred because it affects the performance of the stack 1 catalyst.
Formula (1): CO + H ₂ O → H ₂ + CO ₂ (exothermic reaction)
Formula (2): CO + 1 / 2O ₂ → CO ₂ (exothermic reaction)
A cathode gas supply system 8 that supplies a cathode gas (for example, an oxidant gas such as an oxygen-containing gas such as air) to the cathode that is the oxidant electrode of the stack 1 will be described. The cathode gas supply system 8 includes a cathode gas passage 80 (oxidant passage) connected to the cathode inlet of the stack 1, a pump 81 (cathode gas conveyance source) provided in the cathode gas passage 80, and a humidifier 82. The humidifier 82 includes a humidification path 82a, a moisture absorption path 82b, and a moisture holding member 82c that partitions the humidification path 82a and the moisture absorption path 82b. When the pump 81 is actuated, the cathode gas, which is air, is humidified by the humidifying passage 82 a of the humidifier 82 and then supplied to the cathode (oxidant electrode) of the stack 1.

  As shown in FIG. 1, a cathode inlet valve 85 (cathode inlet opening / closing portion) for opening and closing the cathode inlet side of the stack 1 is provided in the cathode gas passage 80. A cathode outlet valve 87 (cathode outlet opening / closing part) for opening and closing the cathode outlet side of the stack 1 is provided in the cathode offgas passage 96.

  The anode off gas discharge system 90 will be described. Off-gas means a gas that has undergone a power generation reaction in the stack 1. As shown in FIG. 1, the anode offgas discharge system 90 includes an anode offgas passage 91 that connects the anode outlet of the anode of the stack 1 and the burner 71, an anode outlet valve 92 provided in the anode offgas passage 91, and an anode offgas passage. And an anode off-gas condenser 93 provided at 91. Here, since the anode off-gas discharged from the anode outlet of the stack 1 contains a combustible component, the anode off-gas condenser 93 reduces the moisture, and then supplies the burner 71 to burn.

  The cathode offgas discharge system 95 will be described. As shown in FIG. 1, the cathode gas discharge system 95 is provided in the cathode offgas passage 96 and the cathode offgas passage 96 through which the cathode offgas discharged from the cathode outlet of the stack 1 flows through the moisture absorption passage 82 b of the humidifier 82. A cathode off-gas condenser 97. Here, the cathode off-gas discharged from the cathode outlet of the stack 1 is further exhausted by the moisture absorption path 82b of the humidifier 82 and the cathode off-gas condenser 97 to be exhausted.

  As shown in FIG. 1, the exhaust heat recovery system 120 includes a second pump 122 (water conveyance source), an anode offgas condenser 93, a cathode offgas condenser 97, a combustion exhaust heat exchanger 125, and a second heat exchanger 127. A circulation circuit 128 that circulates is provided. When the second pump 122 is activated, cooling water (refrigerant) circulates in the circulation circuit 128, and the heat of the anode offgas condenser 93, the cathode offgas condenser 97, and the combustion exhaust heat exchanger 125 is recovered. Thereby, the cooling water flowing through the circulation circuit 128 is heated.

  The hot water storage system 130 will be described. As shown in FIG. 1, the hot water storage system 130 is sequentially disposed in the hot water storage tank 131 for storing hot water, the hot water storage circuit 132 that connects the discharge port 131p of the hot water storage tank 131 and the suction port 131i of the hot water storage tank 131, and the hot water storage circuit 132. The third pump 133 (water transport source), the second heat exchanger 127, the first heat exchanger 22, the hot water supply passage 131m for discharging the hot water in the hot water storage tank 131 toward the hot water consumption section, and the hot water supply passage 131m When hot water is used for hot water supply, a replenishment passage 135 (such as a water pipe) that automatically supplies new water (tap water) to the hot water tank 131 by opening a valve (not shown) is provided.

  When the third pump 133 is activated, the water flowing through the hot water storage circuit 132 is heated through the second heat exchanger 127 and the first heat exchanger 22 and returns to the hot water tank 131. That is, the heat recovered by the exhaust heat recovery system 120 is recovered as hot water in the hot water storage circuit 132 by the second heat exchanger 127. The heat recovered in the main cooling circuit 2 is recovered as hot water in the hot water storage circuit 132 by the first heat exchanger 22. The control unit 5 includes an input processing circuit that receives a signal such as a temperature signal, a CPU, a memory, and an output processing circuit, and includes pumps 23, 122, 133, 81, 72, 73, 74, and a valve 75. , 92, 85, 87, and control signals for controlling the heater 29 are output.

  Now, the main part will be described. As shown in FIG. 1, a condensed water tank 30 that stores condensed water generated by the power generation reaction of the stack 1 is provided at the lower part of the housing 6. The condensed water tank 30 is disposed below the anode off-gas condenser 93, the cathode off-gas condenser 97, the condenser 24, and the combustion exhaust heat exchanger 125 in the gravity direction. The condensed water tank 30 (hereinafter also referred to as the tank 30) is provided on the bottom side of the housing 6, and receives the condensed water generated by these condensers 93, 97, 24 and the combustion exhaust heat exchanger 125. To collect. The tank 30 stores these condensed water. A drain portion 32 that discharges excess water stored in the tank 30 to the outside of the housing 6 is provided downstream of the tank 30. The drain part 32 is provided downstream of the tank 30 and leads out the water overflowing from the outlet 30p of the tank 30, a collecting part 32b provided at the tip of the leading pipe 32a, and extends from the collecting part 32b. And a drain pipe 32c that is formed by a drain hose or the like that is open to the atmosphere. A part of the drain pipe 32c is located outside the housing 6 and is easily frozen. The collecting portion 32b and the drain pipe 32c are located below the water outlet 30p of the tank 30 in the gravity direction. Therefore, the water in the collecting portion 32b is prevented from flowing back to the water outlet 30p of the tank 30. When the flow rate of the condensed water generated in the system is compared with the flow rate of the reforming water, the flow rate of the condensed water per unit time is larger than the flow rate of the reforming water. For this reason, surplus condensed water stored in the tank 30 is discharged to the outside as drain water through the water outlet 30p, the outlet pipe 32a, the collecting portion 32b, and the drain pipe 32c. For this reason, it is requested | required that the drainage of the drain part 32 is ensured.

  A reforming water supply system 4 that connects the tank 30 and the reforming device 70 is provided. The reforming water supply system 4 includes a reforming water supply passage 40 that connects the tank 30 and the reforming device 70, and a water pump 41 and a water purifier 42 that are provided in the reforming water supply passage 40. The water purifier 42 has a water purifying material such as an ion exchange resin, and purifies condensed water to increase the purity. Thus, the reformed water used in the reformer 70 has a high purity. If the concentration of impurities contained in the reformed water is high, the reformer 70, its piping, and consequently the electrolyte membrane of the stack 1 are likely to deteriorate. The water purifier 42 is provided with a first heater 43f for preventing freezing. The tank 30 is provided with a second heater 43s for preventing freezing.

  As shown in FIG. 1, a hot water passage 50 that connects the hot water storage circuit 132 of the hot water storage system 130 and the gathering portion 32 b of the drain portion 32 of the tank 30 is provided in a state branched from the branch portion 132 m of the hot water storage circuit 132. The hot water passage 50 and the collecting portion 32b of the drain portion 32 are disposed below the water level of the hot water tank 131 so that water pressure acts. The branch part 132m is disposed downstream of the heat exchanger 127 that heats the water with the heat recovered by the exhaust heat recovery system 120 and the heat exchanger 22 that heats the water with the heat recovered by the stack 1 and the condenser 24. The hot water heated by the heat exchanger 127 and the heat exchanger 22 is supplied to the drain part 32 through the hot water passage 50. For this reason, hot water as high as possible can be supplied to the drain part 32.

  The hot water passage 50 is provided with a hot water valve 52 that opens and closes the hot water passage 50. The inlet port 52 i of the hot water valve 52 is connected to the hot water passage 50, and the outlet port 52 p is connected to the collecting portion 32 b of the drain portion 32. In some cases, the hot water valve 52 may be a three-way valve. A hot water temperature sensor 67 for detecting the temperature T4 of the hot water in the hot water storage circuit 132 is provided. The hot water temperature sensor 67 is located downstream of the heat exchangers 127 and 22 and upstream of the branch part 132m, and detects the temperature of the hot water just before being heated by the heat exchangers 127 and 22 and flowing into the hot water passage 50. To do. For this reason, the hot water temperature sensor 67 is advantageous for detecting the hot water temperature immediately before flowing into the drain part 32.

  According to the present embodiment, the control unit 5 opens the hot water valve 52 when there is a possibility that the drain part 32 may freeze in a cold region or in winter, or when the drain part 32 is frozen. Thereby, the hot water of the hot water storage circuit 132 of the hot water storage system 130 is supplied to the collecting portion 32 b of the drain portion 32 via the hot water passage 50 without being supplied to the tank 30. In this case, warm water may be supplied continuously or intermittently. The drain part 32 may be supplied to a part other than the collecting part 32b. Thereby, the temperature of the drain part 32 of the tank 30 rises, and the freezing of the drain part 32 is suppressed. Hot water is discharged from the drain part 32 to the outside. Since the height of the water outlet 30p is higher than that of the drain part 32, it is possible to prevent the warm water (tap water or the like) supplied to the drain part 32 from flowing back into the tank 30.

  Here, if the hot water valve 52 is opened, even if the pump 133 is not driven, it is based on the water pressure of the hot water storage circuit 132, the water pressure of the hot water stored in the hot water storage tank 13, the water pressure of the supply passage 135, and the like. Thus, the hot water in the hot water storage circuit 132 flows toward the drain portion 32. Of course, if the pump 133 is driven, warm water can be supplied to the drain part 32 more positively.

  According to this embodiment, the hot water of the hot water storage circuit 132 of the hot water storage system 130 is supplied to the collecting portion 32b of the drain portion 32 of the tank 30 (located downstream of the tank 30 and below the weight direction). The freezing of the drain part 32 is suppressed. In this case, the hot water in the hot water storage circuit 132 is water stored in the hot water storage tank 131, and is hot water obtained by heating the tap water supplied to the hot water storage tank 131 through the replenishment passage 135, chlorine ions for sterilization, It differs from pure water that contains ions such as iron ions and silicon compounds at a considerable concentration and does not contain impurities.

  The hot water in the hot water storage circuit 132 is not supplied to the tank 30 itself that requires high cleanliness, but is supplied to the collecting portion 32b that is downstream from the water outlet 30p of the tank 30 and has a low height position. Therefore, the hot water does not flow back to the tank 30 and the cleanliness of the condensed water stored in the tank 30 is ensured satisfactorily. Therefore, even when the condensed water stored in the tank 30 is used as reforming water in the reforming device 70, it is suppressed that ions that lower the purity of the water are supplied to the ion exchanger 42. The In this case, the ion exchanger 42 is prevented from having a short life in an unexpected short time, and the electrolyte membrane of the fuel cell, the reformer 70, the piping of the reformer 70, etc. assembled in the stack 1 are ionized. Therefore, it is possible to contribute to the extension of the service life.

(Embodiment 2)
Since this embodiment basically has the same configuration and the same operation and effect as those of the first embodiment, FIG. 1 is applied mutatis mutandis. Hereinafter, the description will focus on the different parts. As described above, the first temperature sensor 63 that detects the temperature of the outside air serving as the cathode gas is provided in the outside air inlet 62 of the housing 6. When the temperature detected by the first temperature sensor 63 is lower than the first threshold value Tf, the control unit 5 opens the warm water valve 52 because the drain unit 32 may be frozen. As a result, the hot water of the hot water storage circuit 132 of the hot water storage system 130 is supplied to the collecting portion 32b of the tank 30, the temperature of the collecting portion 32b rises, and the temperature of the outlet portion 32a and the drain pipe 32c rises. Is suppressed. Regardless of whether the pump 133 is driven or not, if the hot water valve 52 is opened, the hot water storage circuit 132 connected to the hot water tank 131 and the hot water in the hot water passage 50 are supplied to the drain portion 32.

  FIG. 2 shows an example of a flowchart executed by the control unit 5. As shown in FIG. 2, when the main routine is being executed, the interrupt routine is executed as a freeze release routine at regular intervals. In the interrupt routine, the control unit 5 determines whether or not the cathode gas temperature T3 detected by the first temperature sensor 63 is lower than a first threshold Tf (for example, 4 ° C.) (step S102). If the temperature T3 of the cathode gas (outside air) is lower than the first threshold value Tf (for example, 4 ° C.) (YES in step S102), the drain part 32 may be frozen in the near future or is frozen.

  Therefore, the control unit 5 determines whether or not the temperature T4 of the hot water is higher than a third threshold value Tt (for example, 60 ° C.) (step S104). If the temperature T4 of the drain part 32 is higher than the third threshold value Tt (for example, 60 ° C.) (YES in Step S104), the control part 5 opens the hot water valve 52 for a predetermined time Ty (Steps S106, S108). When the predetermined time Ty has elapsed, the hot water valve 52 is closed to stop the hot water (step S110). The predetermined time Ty can be appropriately selected according to the installation environment of the system, the season, and the like, and can be within a range of, for example, 20 seconds to 10 minutes.

  Also in this embodiment, the hot water in the hot water storage system 130 is supplied to the drain portion 32 of the tank 30 to suppress freezing of the drain portion 32, but the hot water is not directly supplied to the tank 30 itself. Therefore, the cleanliness of the condensed water (reformed water) stored in the tank 30 is ensured satisfactorily. Therefore, even when the condensed water stored in the tank 30 of the tank 30 is used as the reformed water in the reformer 70, chlorine ions, iron ions, and silicon compound ions that reduce the purity of the water are present. Supply to the ion exchanger 42 is suppressed. In this case, the lifetime of the ion exchanger 42 is suppressed from being shortened in an unexpected short period, which can contribute to the extension of the life of the reformer 70 assembled in the stack 1. As a result, it is possible to contribute to extending the life of the electrolyte membrane of the fuel cell to which the anode gas formed by the reformer 70 is supplied.

(Embodiment 3)
FIG. 3 shows a third embodiment. The present embodiment has basically the same configuration and the same function and effect as the first and second embodiments. Hereinafter, the description will focus on the different parts. As shown in FIG. 3, a first temperature sensor 63 that detects the temperature T <b> 3 of the cathode gas formed by the outside air is provided at the outside air inlet 62 of the housing 6. A drain temperature sensor 65 for detecting the temperature T5 of the drain part 32 is provided in the drain part 32. Although the drain temperature sensor 65 detects the temperature of the drain pipe 32c, the temperature of the collecting portion 32b or the outlet pipe 32a may be detected. Furthermore, a hot water temperature sensor 67 for detecting the temperature T4 of the hot water flowing through the hot water storage circuit 132 is provided.

  When the temperature T5 of the drain part 32 detected by the drain temperature sensor 65 is lower than the second threshold value Ts, the control unit 5 determines that the temperature T4 of hot water detected by the hot water temperature sensor 67 is lower than the third threshold value Tt. When it is high, the warm water valve 52 is opened. If the environmental temperature is low enough to freeze the drain part 32, the hot water temperature may also be lowered. However, since warm water is higher than 3rd threshold value Tt, it has sufficient defrosting capability. Therefore, the hot water in the hot water storage circuit 132 of the hot water storage system 130 is supplied to the collecting portion 32 b of the drain portion 32 of the tank 30 through the hot water passage 50. As a result, the temperature of the collective portion 32 of the drain portion 32 rises. Further, the temperature of the drain pipe 32c and the outlet pipe 32a is increased by heat transfer or the like, and freezing of the drain portion 32 is suppressed. In this case, when the temperature T4 of the warm water detected by the warm water temperature sensor 67 is higher than the third threshold value Tt, the control unit 5 opens the warm water valve 52 and supplies the warm water to the drain unit 32, but the warm water temperature sensor When the temperature T4 of the hot water detected at 67 is equal to or lower than the third threshold value Tt, the freezing release force of the hot water is low, so the control unit 5 closes the hot water valve 52 and does not supply the hot water to the drain unit 32. For this reason, when the freezing release force of the water in the hot water passage 50 is not sufficient due to the reason that the water in the hot water storage tank 131 is cold water, the water is not supplied to the drain part 32. Therefore, there is an advantage that excessive freezing of the drain part 32 is suppressed.

  FIG. 4 shows an example of a flowchart executed by the control unit 5. As shown in FIG. 4, when the main routine is being executed, the interrupt routine is executed at regular intervals. In the interrupt routine, the controller 5 determines whether or not the temperature T5 of the drain 32 detected by the drain temperature sensor 65 is lower than a second threshold Ts (for example, 0 ° C.) (step S302). If the temperature T5 of the drain part 32 is lower than the second threshold Ts (for example, 0 ° C.) (YES in step S302), the drain part 32 may be frozen or it is frozen.

  Therefore, the control unit 5 determines whether or not the temperature T4 of the hot water in the hot water passage 50 of the hot water storage system 130 detected by the hot water temperature sensor 67 is a high temperature that exceeds a third threshold value Tt (for example, 60 ° C.) (step). S304). If the temperature T4 of the hot water exceeds a third threshold value Tt (for example, 60 ° C.) (YES in step S304), the hot water has a high freezing release force.

  For this reason, the control part 5 opens the warm water valve 52, supplies warm water to the drain part 32 (step S306), and makes the warm water supply time count (step S308). Thereby, the drain part 32 is gradually warmed with warm water. If the temperature T5 of the drain part 32 becomes higher than the second threshold value Ts2 (for example, 10 ° C.) (YES in step S310), the drain part 32 is thawed. Therefore, the controller 5 closes the hot water valve 52 (step S312), stops the supply of hot water, stops the time count of the hot water supply time Tm, and returns to the main routine.

  Even if the hot water supply time Tm to the drain part 32 is not less than a predetermined time (for example, 1 minute), if the temperature T5 of the drain part 32 is not more than the second threshold value Ts2 (for example, 10 ° C.) (NO in step S314). It is estimated that the temperature T5 of the drain part 32 is not sufficient and the drain part 32 is insufficiently thawed. Therefore, the control unit 5 closes the hot water valve 52 to temporarily stop the supply of hot water to the drain unit 32 (step S316) and stop the time count of the hot water supply time Tm (step S318). This is to prevent excessive freezing in the drain part 32.

  Thereafter, the controller 5 supplies the water in the tank 30 to the reformer 70 via the purifier 42 by increasing the number of revolutions (drive amount) per unit time of the water pump 41 (reformed water transport source). A reforming water increasing operation is performed to increase the amount of reforming water per unit time within a permissible range of the system for a predetermined time Tx (steps S320 and S322). As a result, the water level of the condensed water stored in the tank 30 is reduced, the flow rate of water overflowing from the tank 30 to the drain part 32 side via the outlet pipe 32a is reduced, and excessive freezing of the drain part 32 is suppressed. Here, at the predetermined time Tx, it is expected that the drain part 32 is thawed by heat transfer from the hot water supplied to the drain part 32.

  Here, the following parallel operation may be executed in conjunction with the reforming water increasing operation. That is, as a parallel operation, the control unit 5 increases the flow rate of the combustion air supplied to the burner 71 within a predetermined time Tx and an allowable range of the system. In this case, since the flow rate of the exhaust gas discharged from the combustion exhaust heat exchanger 125 to the outside increases, the amount of moisture taken out by the exhaust gas increases. Further, as a parallel operation, the control unit 5 increases the flow rate of the cathode gas supplied to the cathode of the stack 1 within a predetermined time Tx and an allowable range of the system. In this case, since the flow rate of the cathode offgas discharged from the cathode offgas condenser 97 to the outside increases, the amount of moisture taken out by the cathode offgas increases. As a result, due to the parallel operation described above, the overall flow rate of the condensed water condensed in the system is lowered, and consequently, the level of the condensed water stored in the tank 30 is lowered and discharged from the tank 30 to the drain portion 32. The flow rate of drain water decreases, and the flow rate of water overflowing from the tank 30 to the drain part 32 is suppressed. The flow rate means a flow rate per unit time. The allowable range refers to a range in which fluctuations are allowed to such an extent that the system does not greatly affect the power generation output when the system is performing power generation operation such as rated operation.

  As described above, when the time for executing the process of lowering the water level of the tank 30 has elapsed for the predetermined time Tx, the control unit 5 opens the hot water valve 52 again (step S324), and the hot water in the hot water storage circuit 132 is supplied to the drain unit 32. Supply. Even if the drain part 32 is frozen, it is expected that the drain part 32 is thawed by heat transfer from the hot water.

  Then, as described above, the control unit 5 counts the hot water supply time Tm2 for supplying hot water to the drain unit 32 (step S326). Further, the controller 5 determines whether or not the temperature T5 of the drain part 32 exceeds the second threshold value Ts2 (for example, 10 ° C.) (step S328), and the temperature of the drain part 32 heated by the hot water is determined. If T5 is higher than the second threshold value Ts2 (for example, 10 ° C.) (YES in step S328), the drain part 32 has been thawed. For this reason, the controller 5 closes the hot water valve 52 (step S330), stops the supply of hot water, stops the time count, and further stops the reforming water increasing process (step S332). Return to the routine. When the parallel operation for increasing the flow rates of the combustion air and the cathode gas is performed in parallel, the control unit 5 cancels the increase in the flow rates.

  Even if the hot water supply time Tm2 from the time when the hot water valve 52 is opened again has passed a predetermined time (for example, 1 minute), the temperature T5 of the drain portion 32 is not more than the second threshold value Ts2 (for example, 10 ° C.) (step S340). NO), since it is presumed that the drain part 32 has not been thawed, the control part 5 stops the system (step S342) and warns the user or maintenance person to that effect. This is because if the power generation operation is continued with the drainage from the drain part 32 being restricted, water may overflow from the tank 30 and water may enter components in the system.

(Embodiment 4)
FIG. 5 shows a fourth embodiment. The present embodiment has basically the same configuration and the same function and effect as the above-described embodiment. Hereinafter, the description will focus on the different parts. The stack 1 is formed of a solid oxide fuel cell (SOFC), and the operating temperature is, for example, in the range of 400 to 1000 ° C. and in the range of 500 to 800 ° C., depending on the electrolyte material. As can be understood from the comparison between FIG. 1 and FIG. 5, although the reformer 70 is provided, the main cooling circuit for cooling the stack 1, the anode offgas condenser, and the cathode offgas condenser are eliminated. Furthermore, the CO shift part 78 and the CO oxidation part 79 are also abolished. This is because CO can also be an anode gas.

  As shown in FIG. 5, a reforming water supply system 4 that connects the tank 30 and the reforming device 70 is provided. The reforming water supply system 4 includes a reforming water supply passage 40 that connects the tank 30 and the reforming device 70, and a water pump 41 and a water purifier 42 that are provided in the reforming water supply passage 40. The water purifier 42 has a water purifying material such as an ion exchange resin, and purifies condensed water to increase the purity. The water purifier 42 is provided with a first heater 43f for preventing freezing. The tank 30 is provided with a second heater 43s for preventing freezing. When there is a risk of freezing, the heaters 43f and 43s generate heat.

  The anode off gas after the power generation reaction discharged from the anode of the stack 1 is supplied to the burner 71 of the reformer 70 through the passage 13. Cathode off-gas (off-air) after the power generation reaction discharged from the cathode of the stack 1 is supplied to the burner 71 through the passage 14. After the anode off gas is recombusted with the cathode off gas, it is discharged to the outside through the passage 15 and the combustion exhaust heat exchanger 125 as exhaust gas.

  As shown in FIG. 5, the hot water storage system 130 is sequentially arranged in the hot water storage tank 131 that stores hot water, the hot water storage circuit 132 that connects the discharge port 131p of the hot water storage tank 131 and the suction port 131i of the hot water storage tank 131, and the hot water storage circuit 132. The third pump 133 (water conveyance source) and the combustion exhaust heat exchanger 125 are provided. The condensed water is caused to flow to the condensed water tank 30 through the condensed water passage 125k branched from the passage for exhausting the exhaust gas led out from the combustion exhaust heat exchanger 125 to the outside. The hot water storage circuit 132 is provided with a hot water temperature sensor 67 for detecting the temperature T4 of the hot water flowing therethrough. When the third pump 133 is actuated, the water flowing through the hot water storage circuit 132 flows through the combustion exhaust heat exchanger 125 and further exchanges heat with the hot exhaust gas from the burner 71, so that it is heated to become hot water, and the hot water storage tank 131. Return to For this reason, the heat of exhaust gas is collect | recovered by the hot water storage tank 131 as warm water.

  As shown in FIG. 5, a hot water passage 50 that connects the hot water storage circuit 132 of the hot water storage system 130 and the drain portion 32 of the tank 30 is provided in a state branched from the branch portion 132 m of the hot water storage circuit 132. The branch portion 132m is located downstream of the heat exchanger 125 that has recovered the heat of the high-temperature exhaust gas in the hot water storage circuit 132, and the hot water heated by the heat exchange 125 is drained through the hot water passage 50 to the drain portion 32. To supply. For this reason, hot water as high as possible can be supplied to the drain part 32.

  The hot water passage 50 is provided with a hot water valve 52 that opens and closes the hot water passage 50. The inlet port 52 i of the hot water valve 52 is connected to the hot water passage 50, and the outlet port 52 p is connected to the collecting portion 32 b of the drain portion 32. In the hot water storage circuit 132. A hot water temperature sensor 67 for detecting the temperature T4 of the hot water flowing through this is provided. The hot water temperature sensor 67 is located downstream of the heat exchanger 125 and upstream of the branch part 132m, and detects the temperature of the hot water just before being heated by the heat exchanger 125 and flowing into the hot water passage 50.

  The hot water passage 50 is provided with a hot water valve 52 that opens and closes the hot water passage 50. The inlet port 52 i of the hot water valve 52 is connected to the hot water passage 50, and the outlet port 52 p is connected to the collecting portion 32 b of the drain portion 32. A drain temperature sensor 65 that detects the temperature of the drain portion 32 is provided. The drain temperature sensor 65 can detect the temperature of the surface of the drain pipe 32c or the inside of the drain pipe 32c, for example.

  According to this embodiment, when there is a possibility that the drain part 32 may freeze in a cold region or winter, or when the drain part 32 is frozen, the control part 5 opens the hot water valve 52 to store hot water. The hot water of the circuit 132 is supplied to the hot water passage 50 and eventually to the drain part 32. Thereby, the temperature of the collection part 32b and the drain pipe 32c of the tank 30 rises, and the freezing of the drain part 32 is suppressed by extension. In this case, the pump 133 (hot water transport source) is preferably transported, but the hot water in the hot water storage circuit 132 may be supplied to the drain part 32 by gravity.

  Here, when the temperature T5 of the drain pipe 32c detected by the drain temperature sensor 65 is lower than the second threshold Ts (for example, 0 ° C.), the temperature T4 of the hot water detected by the hot water temperature sensor 67 is the third threshold. When the temperature is higher than Tt3 (for example, 30 ° C.), the control unit 5 opens the hot water valve 52 and sends the hot water to the drain pipe 32c. Thereby, the hot water of the hot water storage circuit 132 of the hot water storage system 130 is supplied to the drain pipe 32 c of the drain portion 32 through the hot water passage 50. As a result, the temperature of the drain pipe 32c rises, and freezing of the collecting portion 32b and the outlet pipe 32a is suppressed by heat transfer.

  In this case, when the temperature T4 of the warm water detected by the warm water temperature sensor 67 is higher than a third threshold value Tt3 (for example, 30 ° C.), the warm water valve 52 is opened and the warm water is supplied to the drain portion 32. When the temperature T4 of the hot water detected at 67 is lower than the third threshold value Tt3 (for example, 30 ° C.), the hot water does not have the thawing capability, so the hot water valve 52 is closed and the hot water is not supplied to the drain part 32. . Thus, when the water in the hot water tank 131 is cold water and the water in the hot water passage 50 is cold, it is not supplied to the drain part 32. Therefore, excessive freezing of the collective portion 32b of the drain portion 32 and / or the drain pipe 32c is suppressed. Also in this embodiment, the hot water in the hot water supply passage 131m may be supplied to the drain portion 32 by gravity or a pump (not shown).

(Embodiment 5)
This embodiment has basically the same configuration and the same function and effect as the embodiment shown in FIG. Hereinafter, the description will focus on the different parts. A hot water supply passage 131m led out from the upper part of the hot water storage tank 131 toward the hot water consumption section is provided. When the drain part 32 is frozen, when there is a possibility of freezing, the hot water itself of the hot water supply passage 131m may be supplied to the drain part 32. In this case, a valve such as a three-way valve provided in the hot water supply passage 131m is operated, and the warm hot water stored in the upper part of the hot water tank 131 is supplied to the collecting portion 32b and / or the drain pipe 32c of the drain portion 32 Is done. Alternatively, the thermal energy of hot water flowing through the hot water supply passage 131m may be given to the collecting portion 32b and / or the drain pipe 32c of the drain portion 32 by a heat exchanger (not shown).

(Embodiment 6)
FIG. 6 shows a sixth embodiment. The present embodiment has basically the same configuration and the same function and effect as the first embodiment. Hereinafter, the description will focus on the different parts. As shown in FIG. 6, a heat exchanger 500 that can exchange heat with the drain portion 32 is provided in the hot water passage 50. When the drain part 32 may be frozen or when the drain part 32 is frozen, the controller 5 opens the hot water valve 52. As a result, the hot water of the hot water storage circuit 132 of the hot water storage system 130 (hot water heated by the heat exchangers 127 and 22) flows to the heat exchanger 500 through the hot water passage 50 and is further returned to the hot water storage circuit 132. The heat exchanger 500 exchanges heat with the drain part 32 to give warm water thermal energy to the gathering part 32 b of the drain part 32. For this reason, the temperature of the drain part 32 of the tank 30 rises, and the freezing of the drain part 32 is suppressed. Since warm water is not discarded from the drain pipe 32c, consumption of warm water is reduced. The heat exchanger 500 may exchange heat with the drain pipe 32c to give warm water thermal energy to the drain pipe 32c. A structure that suppresses freezing of the drain portion 32 by exchanging heat energy of hot water in this way may be applied to all the embodiments. The present invention may be applied to a solid oxide fuel cell system.

  (Others) The system 100 is not limited to the arrangement and structure of the system shown in FIG. 1, and the arrangement and structure can be changed as appropriate. The humidifier does not necessarily have to be mounted. The condensers 93, 97, and 24 shown in FIG. 1 may be provided as necessary. The pump 81 and the air pump 72 may be a fan, a blower, or a compressor. The fuel pump 73 may be a fan, a blower, or a compressor. The water pump 74 may be a fan, a blower, or a compressor. The reforming fuel supplied to the reforming apparatus is not limited to gas such as city gas or biogas, but may be liquid fuel such as kerosene, methanol, dimethyl ether, and gasoline. The combustion fuel supplied to the burner is not limited to gas, and may be liquid fuel such as kerosene, methanol, dimethyl ether, gasoline, or solid fuel.

  The present invention is not limited to the embodiments described above and shown in the drawings, and can be implemented with appropriate modifications within a range not departing from the gist. Structures and functions specific to one embodiment can be applied to other embodiments. The following technical idea can be understood from the description of the present specification.

  [Additional Item 1] A fuel cell that performs a power generation operation using an anode fluid and a cathode fluid, a tank that stores condensed water generated during the power generation operation of the fuel cell, and a drain portion that discharges excess water in the tank to the outside And a hot water storage system having a hot water storage tank for storing hot water heated by heat generated by the power generation operation of the fuel cell, and the hot water storage system and the drain section, and the thermal energy of the hot water of the hot water storage system A fuel cell system comprising a hot water passage capable of supplying water to a drain portion and a hot water valve capable of opening and closing the hot water passage.

  The present invention can be applied to, for example, stationary, vehicle, electrical equipment, electronic equipment, and portable fuel cell systems.

  In the figure, 1 is a stack (fuel cell), 10 is a cooling passage, 2 is a main cooling circuit, 30 is a condensed water tank, 32 is a drain part, 32a is a lead-out pipe, 32b is a collecting part, 32c is a drain pipe, Reformed water supply system, 41 is a water pump, 42 is a water purifier, 5 is a control unit, 50 is a hot water passage, 52 is a hot water valve, 6 is a housing, 60 is a storage chamber, 62 is an outside air inlet, and 63 is First temperature sensor, 65 drain temperature sensor, 67 hot water temperature sensor, 7 anode gas supply system, 70 reforming device, 70a reforming unit, 71 burner, 76 anode gas passage, 77 CO reduction , 78 is a CO shift unit, 78 is a CO oxidation unit, 80 is a cathode gas passage, 81 is a pump (cathode gas carrier source), 82 is a humidifier, 85 is a cathode inlet valve (inlet opening / closing unit), and 87 is a cathode outlet. Valve, 91 is anode Fugasu passage 96 is cathode off-gas passage, 75 an anode inlet valve, 92 is an anode outlet valve, 130 hot water storage system, 131 hot water storage tank, 132 is a hot water storage circuit, 133 denotes a third pump.

Claims (5)

  A fuel cell that performs a power generation operation using an anode fluid and a cathode fluid, a condensate water tank that stores condensate generated during the power generation operation of the fuel cell, and a surplus in the condensate water tank that is provided downstream of the condensate water tank A drain part that discharges the water of the fuel to the outside, a hot water storage system having a hot water storage tank that stores hot water heated by the heat generated during the power generation operation of the fuel cell, the hot water storage system and the drain part, and When a hot water passage that can supply hot water of a hot water storage system to the drain portion, a hot water valve that can open and close the hot water passage, and the drain portion may freeze, or when the drain portion is frozen, By opening the hot water valve and supplying thermal energy of hot water of the hot water storage system to the drain part through the hot water passage, A fuel cell system and a control unit to suppress the freezing of serial drain portion. In Claim 1, either the 1st temperature sensor which detects the temperature of cathode gas before supplying to the fuel cell or outside air, and the drain temperature sensor which detects the temperature of the drain part are provided,
When the temperature of the cathode gas or the outside air detected by the first temperature sensor is lower than the first threshold, or the temperature of the drain detected by the drain temperature sensor is lower than the second threshold. A fuel cell system that opens the hot water valve when a condition of low is satisfied. In Claim 1, either the 1st temperature sensor which detects the temperature of cathode gas before supplying to the fuel cell or outside air, and the drain temperature sensor which detects the temperature of the drain part are provided, Furthermore, a hot water temperature sensor for detecting the temperature of the hot water in the hot water storage system is provided,
When the temperature of the cathode gas or the outside air detected by the first temperature sensor is lower than the first threshold, or the temperature of the drain detected by the drain temperature sensor is lower than the second threshold. A fuel cell system that opens the warm water valve when a condition that the temperature is low is satisfied and a condition that the temperature of the warm water detected by the warm water temperature sensor is higher than a third threshold is satisfied. In one of Claims 1-3, the reforming part which generates the anode fluid supplied to the anode of the above-mentioned fuel cell from the fuel raw material by reforming reaction is provided,
When there is a possibility that the drain part is frozen, or when the drain part is frozen, the control part uses the condensed water stored in the condensed water tank as reformed water to the reforming part. A fuel cell system that increases the amount of water to be supplied and decreases the amount of water stored in the condensed water tank. 4. The reforming unit according to claim 1, wherein an anode fluid supplied to an anode of the fuel cell is generated from a fuel raw material by a reforming reaction, and the reforming unit is suitable for the reforming reaction. A burner for heating the reforming section is provided;
When there is a possibility that the drain part is frozen, or when the drain part is frozen, the control part is connected to the flow rate of combustion air burned by the burner and / or the cathode of the fuel cell. A fuel cell system that increases the flow rate of supplied cathode gas.

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