Patent Application
20150118589
The present invention relates to a solid oxide fuel cell system. More particularly, the present invention relates to a solid oxide fuel cell system including a reformer configured to generate a hydrogen-containing gas by using humidified air and a raw material.
Patent Literature 1 discloses a fuel cell system including a condenser which condenses a steam contained in a gas discharged from an anode to generate liquid water (FIG. 3). This fuel cell system may be configured as a solid oxide fuel cell system (column 4: line 52-56).
Patent Literature 2 discloses a solid oxide fuel cell system including an oxidation (oxidization) air humidification means which humidifies partial oxidation air which is supplied to a partial oxidation unit so that its temperature becomes equal to or higher than a dew point of 80 degrees C. by causing the partial oxidation air to contact humidification water heated by utilizing exhaust heat generated in a solid oxide fuel cell (abstract, FIG. 1). The partial oxidation unit generates a reducing gas containing hydrogen by causing a desulfurized fuel gas to go through partial oxidation in the presence of an oxidation catalyst (claim 1). The humidification water is supplied from a clean water supply source. The water discharged from the humidification means is stored in a hot water storage tank (FIG. 1).
Patent Literature 1: U.S. Pat. No. 7,858,256 specification
Patent Literature 2: Japanese Laid-Open Patent Application Publication No. 2005-317489
In an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise, it was difficult for a conventional fuel cell system to supply electric power stably.
The present invention addresses the above described problem associated with a prior art, and an object is to provide a fuel cell system which is capable of supplying electric power more stably than a conventional fuel cell system is, in an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise.
Another object of the present invention is to supply reforming water stably while efficiently utilizing energy, in a solid oxide fuel cell system in which a moisture contained in a gas discharged from the solid oxide fuel cell system is recovered and used for reforming a raw material.
According to an aspect of the present invention, there is provided a solid oxide fuel cell system comprising a reformer configured to generate a hydrogen-containing gas by using a raw material and water; a solid oxide fuel cell including an anode and a cathode, and configured to generate electric power by using the hydrogen-containing gas supplied from the reformer to the anode and air supplied to the cathode; a heat radiator configured to radiate heat from at least one of an anode off-gas discharged from the anode and a combustion exhaust gas generated by combusting the anode off-gas to generate condensed water; a condensed water circulating passage configured to circulate the condensed water supplied from the heat radiator; a condensed water tank provided on the condensed water circulating passage and configured to store the condensed water therein; a condensed water pump provided on the condensed water circulating passage and configured to circulate the condensed water; and a condensed water/off-gas heat exchanger provided on the condensed water circulating passage and configured to exchange heat between the condensed water and an off-gas discharged from the solid oxide fuel cell; wherein at least a part of the water supplied to the reformer is the condensed water.
According to an aspect of the present invention, it becomes possible to achieve an advantage that reforming water can be supplied stably while efficiently utilizing energy, in a solid oxide fuel cell system in which a moisture contained in a gas discharged from the solid oxide fuel cell system is recovered and used for reforming a raw material.
According to another aspect of the present invention, it becomes possible to achieve an advantage that electric power can be supplied more stably than in a conventional example, in an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise.
The inventors intensively studied to supply reforming water stably while efficiently utilizing energy, in a fuel cell system in which a moisture contained in a gas discharged from a fuel cell system is recovered and used for reforming a raw material, and as a result, found out the followings.
In a case where the moisture contained in the gas discharged from the fuel cell system is stored as condensed water, germs and others may breed within a condensed water passage, and cause a problem such as clogging of a pump which supplies the condensed water to a reformer. The problem such as clogging may lead to a situation in which the reforming water is supplied unstably.
In light of the above, the inventors conceived that a condensed water pump circulates the condensed water in a condensed water circulating passage, and a condensed water/off-gas heat exchanger for exchanging heat between the condensed water and an off-gas discharged from a solid oxide fuel cell is provided in order to heat the condensed water by the off-gas. In this configuration, breeding of the germs and the like can be suppressed by heating the condensed water, and exhaust heat energy can be efficiently utilized by heating the condensed water by the off-gas.
Also, the inventors intensively studied to develop a solid oxide fuel cell system which is capable of supplying electric power more stably than a conventional solid oxide fuel cell system is, in an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise to about 50 degrees C., and they found out the followings.
In a case where water supply cannot depend on infrastructure, the water may be recovered from an off-gas discharged from a fuel cell. In the solid oxide fuel cell system, the dew point of an anode off-gas is as high as, for example, about 80 degrees C. Therefore, if the condensed water can be recovered from the anode gas, the condensed water with a sufficient amount can be recovered even when the air temperature is as high as, for example, 50 degrees C.
However, in a case where the recovered condensed water is supplied by a pump and the like to an evaporator and the evaporator evaporates the water as in a conventional method, there is a need for a pump which is capable of supplying the water with a small amount stably to the evaporator. Such a pump is expensive and maintenance of the pump is difficult.
Under the above circumstances, the inventors conceived that the condensed water is heated by the off-gas discharged from the fuel cell, the resulting hot water is circulated to humidify the air, and the humidified air is supplied to the reformer, instead of evaporating the water and supplying the evaporated water to the reformer. In this configuration, the supply amount of the steam can be controlled properly based on the temperature, circulation amount and the like of the condensed water. Therefore, it becomes possible to supply electric power more stably than in a conventional example, in an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise to about 50 degrees C. Note that the raw material may be humidified in addition to the air.
According to Embodiment 1, there is provided a solid oxide fuel cell system comprising a reformer configured to generate a hydrogen-containing gas by using a raw material and water; a solid oxide fuel cell including an anode and a cathode, and configured to generate electric power by using the hydrogen-containing gas supplied from the reformer to the anode and air supplied to the cathode; a heat radiator configured to radiate heat from at least one of an anode off-gas discharged from the anode and a combustion exhaust gas generated by combusting the anode off-gas to generate condensed water; a condensed water circulating passage configured to circulate the condensed water supplied from the heat radiator; a condensed water tank provided on the condensed water circulating passage and configured to store the condensed water therein; a condensed water pump provided on the condensed water circulating passage and configured to circulate the condensed water; and a condensed water/off-gas heat exchanger provided on the condensed water circulating passage and configured to exchange heat between the condensed water and an off-gas discharged from the solid oxide fuel cell; wherein at least a part of the water supplied to the reformer is the condensed water.
In this configuration, in a fuel cell system in which a moisture contained in a gas discharged from the fuel cell system is recovered and used for reforming the raw material, breeding of germs and the like can be reduced by heating the condensed water. In addition, exhaust heat energy can be efficiently utilized by heating the condensed water by the off-gas. Thus, the reforming water can be supplied stably while efficiently utilizing the energy.
“off-gas discharged from the solid oxide fuel cell” includes a cathode off-gas discharged from the cathode, an anode off-gas discharged from the anode, a combustion gas generated by combusting the cathode off-gas and the anode off-gas, etc.
An oxidizing (oxidant) gas used for combusting the anode off-gas in “combustion exhaust gas generated by combusting the anode off-gas” may be, for example, the air, or the cathode off-gas.
[System Configuration]
In the example of
The reformer 10 is configured to generate a hydrogen-containing gas by using a raw material and water. In the example of
The raw material may be, for example, a gas containing an organic compound composed of at least carbon and hydrogen, such as a LPG gas, a propane gas, a butane gas, or a city gas containing methane as a major component, coal oil, alcohol, etc. In a case where a liquid raw material such as the coal oil or alcohol is used, it may be heated and vaporized before being supplied to the reformer 10.
In the reformer 10, for example, steam reforming may take place by using the raw material and a steam.
In the reformer 10, for example, oxidative steam reforming may take place by using hydrocarbon contained in the raw material, water and oxygen contained in the humidified air. In the case of using the oxidative steam reforming, the reforming easily proceeds in terms of heat balance, and the size of the reformer 10 can be made smaller than that in the case of using the steam reforming. In addition, even when a sulfur compound is contained in the raw material, it is easily converted into SO2 and the catalyst within the stack is less likely to be poisoned.
The reformer 10 is configured in such a manner that a reforming catalyst is filled into a container, for example. As the reforming catalyst, for example, an alumina carrier impregnated with at least one of platinum and rhodium may be used. The reforming catalyst is not particularly limited. For example, various catalysts may be used so long as they allow at least one of the steam reforming and the oxidative steam reforming to proceed.
The solid oxide fuel cell 12 is a solid oxide fuel cell including an anode 14 and a cathode 16, and generates electric power by using a hydrogen-containing gas supplied from the reformer 10 to the anode 14 and the air supplied to the cathode 16. In the example of
The unit fuel cells may have a known configuration using, for example, yttria-stabilized zirconia (YSZ) as an electrolyte and the like. As the material of the unit fuel cell, zirconia doped with yttrium or scandium, or a lanthanum gallate based solid electrolyte may be used. In the unit fuel cell including the yttria-stabilized zirconia, the power generation reaction takes place in a temperature range of, for example, about 600 degrees C. to about 1000 degrees C., although this depends on the thickness of the electrolyte.
The electric power generated by the power generation in the solid oxide fuel cell 12 is supplied to an outside load through a terminal which is not shown. The outside load may be, for example, a device constituting a base station of a cellular phone.
The heat radiator 17 is configured to radiate heat from an anode off-gas discharged from the anode 14 to generate condensed water. In the example of
In general, the dew point of the anode off-gas is as high as 80 degrees C. When the anode off-gas is cooled to about 50 degrees C., the condensed water with a sufficient amount is obtained. Therefore, the radiator 17 may be configured in such a manner that for example, even in an environment in which an air temperature is high and infrastructure for supplying clean water is inadequate, the condensed water may cover the total amount of the water used to generate the hydrogen-containing gas with a required amount. In other words, the solid oxide fuel cell system 90 may be configured as an oxidative steam reforming solid oxide fuel cell system which allows the water to be self-sustainable even in a high-temperature area. The term “allows the water to be self-sustainable” means that the solid oxide fuel cell system is able to continue to operate by using the water obtained by using the raw material and the like, without depending on the water supplied from outside.
The heat radiator 17 may generate the condensed water by radiating heat from a combustion exhaust gas generated by combusting the anode off-gas discharged from the anode 14. In this case, the heat radiator 17 is provided on a combustion exhaust gas passage. In general, the dew point of the combustion exhaust gas is as high as about 70 degrees. When the combustion exhaust gas is cooled to about 50 degrees C., the condensed water with a sufficient amount is obtained.
The heat radiator 17 may be configured in any way provided that it is able to cool at least one of the anode off-gas and the combustion exhaust gas. The gas may be directly cooled by atmospheric air, or may be cooled in such a manner that the gas is caused to exchange heat with a cooling medium such as a circulated antifreezing fluid and the cooling medium is cooled by the atmospheric air in a radiator and the like. As the heat radiator 17, for example, a shell and tube heat exchanger may be used.
The condensed water circulating passage 20 is configured to circulate the condensed water supplied from the heat radiator 17. In the example of
The condensed water tank 22 is provided on the condensed water circulating passage 20 and is configured to store the condensed water therein. In the example of
The condensed water tank 22 may be provided with a water supply mechanism for supplying the clean water from clean water infrastructure located outside the solid oxide fuel cell system 90 to the condensed water tank 22 at start-up. The condensed water tank 22 may be provided with a water drain mechanism for discharging the water from the condensed water tank 22 to outside the solid oxide fuel cell system 90 during non-use.
The condensed water pump 24 is provided on the condensed water circulating passage 20 to circulate the condensed water. When the condensed water pump 24 is activated, the condensed water stored in the condensed water tank 22 is circulated through the condensed water circulating passage 20. Specifically, the condensed water taken out of the condensed water tank 22 is circulated in such a manner that the condensed water flows through the condensed water/off-gas heat exchanger 26 and a humidifier 28 in this order and is returned to the condensed water tank 22. The off-gas discharged from the solid oxide fuel cell is in a sufficiently high temperature state and therefore can be utilized to heat and sterilize the condensed water. By circulating the condensed water by using the condensed water pump 24, for example, the condensed water is heated and sterilized in the condensed water/off-gas heat exchanger 26 on a regular basis, and thus breeding of the germs can be suppressed. This makes it possible to reduce a possibility of clogging of the condensed water circulating passage 20, the reforming water pump 27, and the like, a failure (e.g. float gets stuck in an unmovable state) of a water level meter attached to the condensed water tank 22, etc.
As the condensed water pump 24, for example, a plunger pump, a magnet pump, etc., may be used. The minimum discharge amount of the condensed water pump 24 may be a predetermined value which is equal to or more than 50 g/minute. The minimum discharge amount of the condensed water pump 24 may be a predetermined value which is equal to or more than 100 g/minute. The maximum discharge amount of the condensed water pump 24 may be a predetermined value which is equal to or less than 1000 g/minute. Specifically, for example, the minimum discharge amount of the condensed water pump 24 may be 100 g/minute, while the maximum discharge amount of the condensed water pump 24 may be 800 g/minute.
The condensed water/off-gas heat exchanger 26 is provided on the condensed water circulating passage 20 and configured to exchange heat between the condensed water and the off-gas discharged from the solid oxide fuel cell 12. Since the temperature of the off-gas discharged from the solid oxide fuel cell 12 is high, the condensed water can be heated efficiently to a level at which the condensed water can be sterilized by utilizing the off-gas.
In the example of
An ion exchange device (ion exchange resin) may be provided on the condensed water circulating passage 20. Specifically, for example, the ion exchange device (ion exchange resin) may be provided on a portion of the condensed water circulating passage 20, which portion is from the condensed water tank 22 to the condensed water/off-gas heat exchanger 26.
The reforming water pump 27 is provided on a reforming water passage 61 and configured to supply the condensed water to the reformer 10. Although in the example of
As the reforming water pump 27, for example, a plunger pump, a gear pump, a magnet pump, etc., may be used. The maximum discharge amount of the reforming water pump 27 may be a predetermined value which is equal to or less than 30 g/minute. The maximum discharge amount of the reforming water pump 27 may be a predetermined value which is equal to or less than 10 g/minute. The maximum discharge amount of the reforming water pump 27 may be a predetermined value which is equal to or less than 5 g/minute. Specifically, for example, the minimum discharge amount of the reforming water pump 27 may be 0 g/minute, while the maximum discharge amount of the reforming water pump 27 may be 30 g/minute. The maximum discharge amount of the reforming water pump 27 may be equal to or more than 1 g/minute or equal to or more than 5 g/minute.
In a case where the amount of the reforming water supplied to the reformer 10 is small, the capacity of the reforming water pump 27 is also small, and hence clogging and the like is more likely to occur in the reforming water pump 27. In the configuration of the present embodiment, by circulating the condensed water by using the condensed water pump 24, for example, the condensed water is heated and sterilized in the condensed water/off-gas heat exchanger 26 on a regular basis, and thus breeding of the germs can be suppressed. Therefore, clogging and the like of the reforming water pump 27 is less likely to occur, even if the capacity of the reforming water pump 27 is small.
The means (condensed water supply unit) which supplies the condensed water to the reformer 10 is not limited to the reforming water pump 27, and another condensed water supply unit may be used. Any condensed water supply unit may be used so long as it is able to supply the condensed water to the reformer 10. As the condensed water supply unit, for example, the humidifier 28 described in Embodiment 2, etc., as well as the reforming water pump 27, may be used. Or, the condensed water supply unit may be a reforming water passage configured to automatically supply the condensed water to the reformer by a gravitational force.
The cathode gas passage 68 and the cathode off-gas passage 70 may be provided with a cathode air heat exchanger which exchanges heat between the air flowing through the cathode gas passage 68 and the cathode off-gas flowing through the cathode off-gas passage 70. In this configuration, the cathode off-gas heats the air up to a predetermined temperature (e.g., 700 degrees C.) before the air is supplied to the cathode. Since the temperature of the air to be supplied to the cathode is raised in advance, for example, a temperature gradient within the stack becomes small, and a problem such as a cracking which would be caused by a thermal stress can be mitigated.
Modified examples of Embodiment 2 to Embodiment 9 may also be applied to Embodiment 1.
A solid oxide fuel cell system of Embodiment 2 is the solid oxide fuel cell system of Embodiment 1, in which the reformer is configured to generate the hydrogen-containing gas by using humidified air and the raw material, and the heat radiator is configured to radiate heat from the anode off-gas discharged from the anode, the solid oxide fuel cell system of Embodiment 2 further comprising a humidifier provided on the condensed water circulating passage and configured to humidify the air by using the condensed water to generate the humidified air to be supplied to the reformer.
According to Embodiment 2, there is provided a solid oxide fuel cell system comprising a reformer configured to generate a hydrogen-containing gas by using humidified air and a raw material; a solid oxide fuel cell including an anode and a cathode, and configured to generate electric power by using the hydrogen-containing gas supplied from the reformer to the anode and air supplied to the cathode; an anode off-gas heat radiator configured to radiate heat from an anode off-gas discharged from the anode to generate condensed water; a condensed water circulating passage configured to circulate the condensed water supplied from the anode off-gas heat radiator; a condensed water tank provided on the condensed water circulating passage and configured to store the condensed water therein; a condensed water pump provided on the condensed water circulating passage and configured to circulate the condensed water; a condensed water/off-gas heat exchanger provided on the condensed water circulating passage and configured to exchange heat between the condensed water and an off-gas discharged from the solid oxide fuel cell; and a humidifier provided on the condensed water circulating passage and configured to humidify the air by using the condensed water to generate the humidified air to be supplied to the reformer.
In this configuration, it becomes possible to supply electric power more stably than in a conventional example, in an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise to about 50 degrees C.
“off-gas discharged from the solid oxide fuel cell” includes a cathode off-gas discharged from the cathode, an anode off-gas discharged from the anode, a combustion gas generated by combusting the cathode off-gas and the anode off-gas, etc.
In the above solid oxide fuel cell system, the off-gas used for heat exchange in the condensed water/off-gas heat exchanger may be the cathode off-gas discharged from the cathode.
In this configuration, the condensed water can be heated by using the cathode off-gas.
In the above solid oxide fuel cell system, the minimum discharge amount of the condensed water pump may be equal to or more than 50 g/minute.
In this configuration, since a general pump can be used, manufacturing cost can be significantly reduced.
In the above solid oxide fuel cell system, the minimum discharge amount of the condensed water pump may be equal to or more than 100 g/minute. The maximum discharge amount of the condensed water pump may be equal to or less than, for example, 1000 g/minute.
[System Configuration]
In the example of
The reformer 10 is configured to generate the hydrogen-containing gas by using the humidified air and the raw material. In the example of
The raw material may be, for example, a gas containing an organic compound composed of at least carbon and hydrogen, such as a LPG gas, a propane gas, a butane gas, or a city gas containing methane as a major component, coal oil, alcohol, etc. In a case where the liquid raw material such as the coal oil or alcohol is used, it may be heated and vaporized before being supplied to the reformer 10. In the reformer 10, for example, oxidative steam reforming may take place by using hydrocarbon contained in the raw material, water and oxygen contained in the humidified air. In the case of using the oxidative steam reforming, the reforming easily proceeds in terms of heat balance, and the size of the reformer 10 can be made smaller than that in the case of using the steam reforming. In addition, even when a sulfur compound is contained in the raw material, it is easily converted into SO2 and the catalyst within the stack is less likely to be poisoned.
The reformer 10 is configured in such a manner that the reforming catalyst is filled into the container, for example. As the reforming catalyst, for example, the alumina carrier impregnated with platinum may be used. The reforming catalyst is not particularly limited. For example, various catalysts may be used so long as they allow the oxidative steam reforming to proceed.
The solid oxide fuel cell 12 is a solid oxide fuel cell including the anode 14 and the cathode 16, and generates electric power by using the hydrogen-containing gas supplied from the reformer 10 to the anode 14 and the air supplied to the cathode 16. In the example of
The unit fuel cells may have a known configuration using, for example, yttria-stabilized zirconia (YSZ) as an electrolyte and the like. As the material of the unit fuel cell, zirconia doped with yttrium or scandium, or a lanthanum gallate based solid electrolyte may be used. In the unit fuel cell including the yttria-stabilized zirconia, the power generation reaction takes place in a temperature range of, for example, about 600 degrees C. to about 1000 degrees C., although this depends on the thickness of the electrolyte.
The electric power generated by the power generation in the solid oxide fuel cell 12 is supplied to the outside load through the terminal which is not shown. The outside load may be, for example, the device constituting the base station of the cellular phone.
The anode off-gas heat radiator 18 is configured to radiate heat from the anode off-gas discharged from the anode 14 to generate the condensed water. In the example of
In general, the dew point of the anode off-gas is as high as 80 degrees C. When the anode off-gas is cooled to about 50 degrees C., the condensed water with a sufficient amount is obtained. Therefore, the anode off-gas heat radiator 18 may be configured in such a manner that for example, even in an environment in which an air temperature is high and infrastructure for supplying clean water is inadequate, the condensed water may cover the total amount of the water used to generate the hydrogen-containing gas with a required amount. In other words, the solid oxide fuel cell system 100 may be configured as the oxidative steam reforming solid oxide fuel cell system which allows the water to be self-sustainable even in a high-temperature area. The term “allows the water to be self-sustainable” means that the solid oxide fuel cell system is able to continue to operate by using the water obtained by using the raw material and the like, without depending on the water supplied from outside.
The anode off-gas heat radiator 18 may be configured in any way provided that it is able to cool the anode off-gas. The anode off-gas may be directly cooled by atmospheric air, or may be cooled in such a manner that the anode off-gas is caused to exchange heat with the cooling medium such as the circulated antifreezing fluid and the cooling medium is cooled by the atmospheric air in the radiator and the like. As the anode off-gas heat radiator 18, for example, the shell and tube heat exchanger may be used.
The condensed water circulating passage 20 is configured to circulate the condensed water supplied from the anode off-gas heat radiator 18. In the example of
The condensed water tank 22 is provided on the condensed water circulating passage 20 and is configured to store the condensed water therein. In the example of
The condensed water tank 22 may be provided with a water supply mechanism for supplying the clean water from clean water infrastructure located outside the solid oxide fuel cell system 100 to the condensed water tank 22 during start-up. The condensed water tank 22 may be provided with a water drain mechanism for discharging the water from the condensed water tank 22 to outside the solid oxide fuel cell system 100 during non-use.
The condensed water pump 24 is provided on the condensed water circulating passage 20 to circulate the condensed water. When the condensed water pump 24 is activated, the condensed water stored in the condensed water tank 22 is circulated through the condensed water circulating passage 20. Specifically, the condensed water taken out of the condensed water tank 22 is circulated in such a manner that the condensed water flows through the condensed water/off-gas heat exchanger 26 and the humidifier 28 in this order and is returned to the condensed water tank 22. By circulating the condensed water by using the condensed water pump 24, for example, the condensed water is heated and sterilized in the condensed water/off-gas heat exchanger 26 on a regular basis, and thus breeding of the germs can be suppressed. Therefore, clogging and the like of the condensed water circulating passage 20 is less likely to occur.
As the condensed water pump 24, for example, a plunger pump, a magnet pump, etc., may be used. The minimum discharge amount of the condensed water pump 24 may be a predetermined value which is equal to or more than 50 g/minute. The minimum discharge amount of the condensed water pump 24 may be a predetermined value which is equal to or more than 100 g/minute. The maximum discharge amount of the condensed water pump 24 may be a predetermined value which is equal to or less than 1000 g/minute. Specifically, for example, the minimum discharge amount of the condensed water pump 24 may be 100 g/minute, while the maximum discharge amount of the condensed water pump 24 may be 800 g/minute.
The condensed water/off-gas heat exchanger 26 is provided on the condensed water circulating passage 20 and configured to exchange heat between the condensed water and the off-gas discharged from the solid oxide fuel cell 12. In the example of
As the condensed water/off-gas heat exchanger 26, for example, a plate heat exchanger, a double-pipe heat exchanger, etc., may be used.
An ion exchange device (ion exchange resin) may be provided on the condensed water circulating passage 20. Specifically, for example, the ion exchange device (ion exchange resin) may be provided on a portion of the condensed water circulating passage 20, which portion is from the condensed water tank 22 to the condensed water/off-gas heat exchanger 26.
The humidifier 28 is provided on the condensed water circulating passage 20 and configured to humidify the air by using the condensed water to generate the humidified air to be supplied to the reformer 10. The air is supplied to the humidifier 28 through an air passage 62. The air passage 62 may be provided with an air supply unit such as a blower. In the example of
The cathode gas passage 68 and the cathode off-gas passage 70 may be provided with a cathode air heat exchanger which exchanges heat between the air flowing through the cathode gas passage 68 and the cathode off-gas flowing through the cathode off-gas passage 70. In this configuration, the cathode off-gas heats the air up to a predetermined temperature (e.g., 700 degrees C.) before the air is supplied to the cathode. Since the temperature of the air to be supplied to the cathode is raised in advance, for example, a temperature gradient within the stack becomes small, and a problem such as a cracking which would be caused by a thermal stress can be mitigated.
[Operation]
Hereinafter, the exemplary operation of the solid oxide fuel cell system of Embodiment 2 will be described. The following description is merely an example of the operation, and specific numeric values and the like may be suitably changed. In the following example, it is supposed that the cathode air heat exchanger (not shown) is provided to exchange heat between the air supplied to the cathode and the cathode off-gas.
It is supposed that the power generation output of the fuel cell is 1500 W, fuel utilization efficiency Uf is 75%, the raw material is LPG having a composition in which propane (C3H8) is 50% and butane (C4H10) is 50%. When an average composition is expressed as a chemical formula CnHm, it is C3.5H9.
When the conversion rate of hydrocarbon is 100%, the reaction formula of the oxidative steam reforming is as follows:
CnHm+αO2+βH2OaCO+bCO2+cH2+dH2O (1)
where O/C=2 α/n, S/C=β/n. a, b, c, and d are varied depending on the composition of the hydrogen-containing gas, the characteristics of the reformer, reforming temperature, etc. O of O/C does not include oxygen atoms originating in water (H2O), but include only oxygen atoms originating in oxygen (O2).
Hereinafter, a case where O/C=0.8, and S/C=1.2 (α=1.4, β=4.2) will be described. To perfectly combust of 1 mole of C3.5H9, 5.75 mole of O2 is required. When α=1.4, the supply amount of O2 corresponding to 1 mole of C3.5H9 is 1.4 mole according to the formula (1). Therefore, λ=1.4/5.75≈0.24 is derived. The value of O/C and the value of S/C are not limited to the above, but may be any values so long as the solid oxide fuel cell system can operate.
The temperature of the condensed water stored in the condensed water tank 22 is about 60 degrees C. Specifically, for example, the condensed water pump 24 sends the condensed water to the condensed water/off-gas heat exchanger 26 at a flow rate of 500 g/minute. The condensed water is heated up to about 85 degrees C. for about 900 W by the cathode off-gas discharged from the cathode air heat exchanger.
The heated condensed water is supplied to the humidifier 28. The humidifier 28 is supplied with water of 7.7 g/minute and humidifies the air. At this time, energy of about 350 W is deprived from the condensed water as evaporation latent heat of the water. Therefore, the temperature of the air discharged from the humidifier 28 and the temperature of the condensed water discharged from the humidifier 28 become about 75 degrees C. The humidified air is mixed with the fuel gas and a mixture of the fuel gas and the humidified air is supplied to the reformer 10. The condensed water discharged from the humidifier 28 is cooled by the pipe, the radiator, etc., and is stored in the condensed water tank 22 as the hot water with 60 degrees C.
The reformer 10 causes the oxidative steam reforming to proceed by using the humidified air and the raw material to generate the hydrogen-containing gas. The composition of an unreformed gas which is the mixture of the humidified air and the raw material is suitable for the oxidative steam reforming. Since O/C=0.8, and S/C=1.2, the oxidative steam reforming proceeds suitably in the reformer 10.
Even when a pulsation occurs in the discharge amount of the condensed water pump 24, the temperature of the cathode off-gas, the flow rate of the cathode off-gas, etc., the temperature of the condensed water in the condensed water circulating passage 20 is less likely to rapidly change because of the high heat capacity of the water, and O/C and S/C of the unreformed gas are stable. Therefore, carbon is less likely to be deposited in the reformer 10.
A solid oxide fuel cell system of the present example is the solid oxide fuel cell system of Embodiment 2, in which the off-gas used for heat exchange in the condensed water/off-gas heat exchanger is the anode off-gas discharged from the anode.
In this configuration, it becomes possible to supply electric power more stably than in a conventional example, in an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise to about 50 degrees C. In addition, the condensed water can be heated by using the anode off-gas.
The condensed water/off-gas heat exchanger 26 is provided on the condensed water circulating passage 20 and configured to exchange heat between the condensed water and the off-gas discharged from the solid oxide fuel cell 12. In the present modified example, the condensed water/off-gas heat exchanger 26 is provided on the anode off-gas passage 64 connected to the anode 14 As the condensed water/off-gas heat exchanger 26, for example, a plate heat exchanger, a double-pipe heat exchanger, etc., may be used.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 100A of the present modified example may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
In the present modified example, it becomes possible to supply electric power more stably than in a conventional example, in an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise to about 50 degrees C. In addition, the condensed water can be heated by using the anode off-gas.
Embodiment 2 and the present modified example may be combined. That is, both of the heat exchange between the condensed water and the anode off-gas and the heat exchange between the condensed water and the cathode off-gas may be performed.
A solid oxide fuel cell system of Embodiment 3 is the solid oxide fuel cell system of Embodiment 2 or the modified example of Embodiment 2, which further comprise a condensed water heat radiator provided on the condensed water circulating passage in a location which is downstream of the humidifier and upstream of the condensed water tank and configured to radiate heat from the condensed water.
In this configuration, for example, it becomes possible to reduce a possibility that the condensed water is re-evaporated in the condensed water tank and a steam flows back. Or, for example, the air can be humidified more effectively by raising the temperature of the humidifier.
As exemplarily shown in
The condensed water heat radiator 30 is provided on the condensed water circulating passage 20 in a location which is downstream of the humidifier 28 and upstream of the condensed water tank 22 and configured to radiate heat from the condensed water. For example, the heat may be radiated from the condensed water in such a manner that the condensed water is cooled by atmospheric air, in the radiator and the like. As the condensed water heat radiator 30, for example, a fin and tube heat exchanger, and the like may be used.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 200 of Embodiment 3 may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
In the solid oxide fuel cell system 200, the condensed water discharged from the humidifier 28 is cooled in the condensed water heat radiator 30 and then supplied to the condensed water tank 22. In this configuration, a temperature difference between the humidifier 28 and the condensed water tank 22 can be increased. Therefore, for example, it becomes possible to reduce a possibility that the condensed water is re-evaporated in the condensed water tank 22 and a steam flows back toward the cathode off-gas 70. Or, for example, the air can be humidified more effectively by raising the temperature of the humidifier 28
Modified example of Embodiment 2 may also be applied to Embodiment 3.
A solid oxide fuel cell system of Embodiment 4 is the solid oxide fuel cell system of Embodiment 2, the modified example of Embodiment 2, or Embodiment 3, which further comprises a bypass air passage configured to bypass the humidifier such that unhumidified air is supplied to the reformer, and a first switch configured to perform switching between a state in which the air is supplied to the reformer through the humidifier and a state in which the air is supplied to the reformer through the bypass air passage.
In this configuration, a start-up time can be reduced.
The phrase “perform switching between a state in which the air is supplied to the reformer through the humidifier and a state in which the air is supplied to the reformer through the bypass air passage” is meant to include a case where ON/OFF switching is performed to select a state in which all of the air is supplied to the reformer through the humidifier or a state in which all of the air is supplied to the reformer through the bypass air passage, and a case where a ratio between the flow rate of the air supplied to the reformer through the humidifier and the flow rate of the air supplied to the reformer through the bypass air passage is changed.
As exemplarily shown in
The bypass air passage 72 is configured to bypass the humidifier 28 such that unhumidified air is supplied to the reformer. In the example of
The first switch 33 is configured to perform switching between a state in which the air is supplied to the reformer through the humidifier 28 and a state in which the air is supplied to the reformer through the bypass air passage 72. In the example of
The first switch 33 opens the first on-off valve 32 and closes the second on-off valve 34 during, for example, a normal operation such that the air is supplied to the reformer 10 through the humidifier 28 without flowing through the bypass air passage 72. The first switch 33 closes the first on-off valve 32 and opens the second on-off valve 34 during, for example, start-up such that the air is supplied to the reformer 10 through the bypass air passage 72 without flowing through the humidifier 28. The first on-off valve 32 and the second on-off valve 34 may be on-off valves which are capable of selecting a fully open state or a fully closed state, or may be, for example, flow control valves which are capable of continuously controlling their opening degrees.
The first switch 33 may not necessarily include the first on-off valve 32 and the second on-off valve 34, but may be constituted by, for example, a three-way valve.
The first switch 33 may be controlled by, for example, a control unit. In this case, the control unit may be configured as in the control unit of modified example of the present embodiment, and will not be described in detail.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 300 of Embodiment 4 may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
During start-up, it is necessary to increase the temperatures of the reformer 10, the solid oxide fuel cell 12, and others. If partial oxidation reforming which generates a greater amount of heat than the oxidative steam reforming does can proceed in the reformer 10 during start-up, then the start-up time can be reduced. In the present embodiment, during start-up, the first switch 33 causes the air to be supplied to the reformer 10 through the bypass air passage 72 and thus the unhumidified air is supplied to the reformer 10. Thus, during start-up, the partial oxidation reforming can proceed in the reformer 10, and a heat generation amount can be increased. As a result, the start-up time can be reduced.
For example, at a time point when the temperatures of the reformer 10, the solid oxide fuel cell 12, and others reach temperatures at which the power generation operation is enabled, the first switch 33 causes the air to be supplied to the reformer 10 through the humidifier 28, so that the humidified air is supplied to the reformer 10. Such control enables the oxidative steam reforming to proceed in the reformer and the hydrogen-containing gas to be generated efficiently during the power generation operation.
Modified examples of Embodiment 2 and Embodiment 3 may also be applied to Embodiment 4.
A solid oxide fuel cell system according to a modified example of Embodiment 4 is the solid oxide fuel cell system of Embodiment 2, the modified example of Embodiment 2, Embodiment 3, or Embodiment 4, which further comprises a control unit configured to deactivate the condensed water pump during start-up.
In this configuration, the start-up time can be reduced.
As exemplarily shown in
The control unit 36 is configured to deactivate the condensed water pump 24 during start-up. The control unit 36 may be communicatively coupled to the condensed water pump 24. It is sufficient that the control unit 36 has a control function. The control unit 36 includes a processor section (not shown), and a storage section (not shown) for storing control programs. As examples of the processor section, there are MPU, and CPU. As examples of the storage section, there are memories. The control unit may be constituted by a single control unit which performs centralized control but may be a plurality of control units which cooperate with each other to perform distributed control.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 300A according to the modified example of Embodiment 4 may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
In the present modified example, as in Embodiment 4, the partial oxidation reforming which generates a greater amount of heat than the oxidative steam reforming does can proceed in the reformer 10 during start-up, and thus the start-up time can be reduced. In the present embodiment, during start-up, the control unit 36 deactivates the operation of the condensed water pump 24. In a state in which the condensed water pump 24 is deactivated, heating of the condensed water in the condensed water/off-gas heat exchanger 26 does not progress, so that the temperature of the condensed water in the condensed water circulating passage 20 becomes lower that than in a case where the condensed water pump 24 is activated. Because of this, humidification of the air in the humidifier 28 does not progress easily, and the unhumidified air is supplied to the reformer 10. Thus, during start-up, the partial oxidation reforming can proceed in the reformer 10, and a heat generation amount can be increased. As a result, the start-up time can be reduced.
For example, at a time point when the temperatures of the reformer 10, the solid oxide fuel cell 12, and others reach temperatures at which the power generation operation is enabled, the control unit 36 starts the operation of the condensed water pump 24, so that the humidified air is supplied to the reformer 10. Such control enables the oxidative steam reforming to proceed in the reformer and the hydrogen-containing gas to be generated efficiently during the power generation operation.
The present modified example may also be applied to Embodiment 3 and Embodiment 4.
A solid oxide fuel cell system according to Embodiment 5 is the solid oxide fuel cell system of Embodiment 2, the modified example of Embodiment 2, Embodiment 3, Embodiment 4, or the modified example of Embodiment 4, which further comprises a combustor configured to combust the anode off-gas and the cathode off-gas to generate a combustion gas, wherein the off-gas used for heat exchange in the condensed water/off-gas heat exchanger is a combustion gas discharged from the combustor.
In this configuration, the dew point of the air discharged from the humidifier can be increased.
As exemplarily shown in
The combustor 38 is configured to combust the anode off-gas and the cathode off-gas to generate the combustion gas. In the example of
In the solid oxide fuel cell system 400, the condensed water/off-gas heat exchanger 26 is provided on the combustion gas passage 76. The condensed water/off-gas heat exchanger 26 is configured to exchange heat between the condensed water and the combustion gas discharged from the combustor 38.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 400 of Embodiment 5 may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
In the solid oxide fuel cell system 400, since the combustor 38 combusts the anode off-gas and the cathode off-gas, the temperature of the off-gas (combustion gas) supplied to the condensed water/off-gas heat exchanger 26 can be increased. The amount of heat exchanged in the condensed water/off-gas heat exchanger 26 can be increased, and the temperature of the condensed water discharged from the condensed water/off-gas heat exchanger 26 can be increased. This makes it possible to reduce the size of the heat exchanger while realizing a desired heat exchange amount or increase the dew point of the air discharged from the humidifier 28.
Modified examples of Embodiment 2, Embodiment 3, and Embodiment 4 may also be applied to Embodiment 5. The present embodiment may be combined with Embodiment 2 or the modified example of Embodiment 2. For example, both of the heat exchange between the condensed water and the cathode off-gas and the heat exchange between the condensed water and the combustion gas may take place. Or, both of the heat exchange between the condensed water and the anode off-gas and the heat exchange between the condensed water and the combustion gas may take place. Or, all of the heat exchange between the condensed water and the cathode off-gas, the heat exchange between the condensed water and the anode off-gas, and the heat exchange between the condensed water and the combustion gas may take place.
A solid oxide fuel cell system according to Embodiment 6 is the solid oxide fuel cell system of Embodiment 2, the modified example of Embodiment 2, Embodiment 3, Embodiment 4, the modified example of Embodiment 4, or Embodiment 5, wherein the anode off-gas heat radiator is configured to exchange heat between a liquid cooling medium and the anode off-gas to radiate heat from the anode off-gas, the solid oxide fuel cell system comprising: a water storage amount detector configured to detect an amount of water stored in the condensed water tank; a cooling medium circulating passage configured to circulate the cooling medium; a cooling medium pump provided on the cooling medium circulating passage and configured to circulate the cooling medium; a cooling medium heat radiator provided on the cooling medium circulating passage and configured to exchange heat between the cooling medium and atmospheric air to radiate heat from the cooling medium; and a control unit configured to control a discharge amount of the cooling medium pump based on a result of detection of the water storage amount detector.
In this configuration, the generation amount of the condensed water can be controlled properly based on the amount of water stored in the condensed water tank.
As exemplarily shown in
In the present embodiment, the anode off-gas heat radiator 18 is configured to exchange heat between the liquid cooling medium and the anode off-gas to radiate heat from the anode off-gas.
The water storage amount detector 40 is configured to detect the amount of water stored in the condensed water tank. Specifically, for example, the water storage amount detector 40 may be constituted by a water level sensor, etc.
The cooling medium circulating passage 78 is configured to circulate the cooling medium. In the example of
As the cooling medium, for example, water, an antifreeze liquid, and the like may be used.
The cooling medium pump 42 is provided on the cooling medium circulating passage 78 and configured to circulate the cooling medium. When the cooling medium pump 42 is activated, the cooling medium is circulated through the cooling medium circulating passage 78. Specifically, the cooling medium discharged from the cooling medium pump 42 is circulated in such a manner that the cooling medium flows through the anode off-gas heat radiator 18 and the cooling medium heat radiator 44 in this order and is returned to the cooling medium pump 42.
As the cooling medium pump 42, for example, a plunger pump, a magnet pump, etc., may be used.
The cooling medium heat radiator 44 is provided on the cooling medium circulating passage 78, and configured to exchange heat between the cooling medium and the atmospheric air to radiate heat from the cooling medium. For example, the heat may be radiated from the cooling medium in such a manner that the cooling medium is cooled by atmospheric air, in the radiator and the like. As the cooling medium heat radiator 44, for example, a fin and tube heat exchanger, and the like may be used.
The control unit 36 is configured to control the discharge amount of the cooling medium pump 42 based on a result of detection of the water storage amount detector 40. The control unit 36 may be communicatively connected to the water storage amount detector 40 and to the cooling medium pump 42. The configuration of the control unit 36 may be the same as that of the modified example of Embodiment 4, except for the above, and will not be described in detail repeatedly.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 500 according to the modified example of Embodiment 6 may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
In the present embodiment, the control unit 36 is configured to control the discharge amount of the cooling medium pump 42 based on a result of detection of the water storage amount detector 40. In this configuration, the generation amount of the condensed water can be controlled properly based on the amount of water stored in the condensed water tank 22.
Specifically, for example, when the amount of water stored in the condensed water tank 22 is small, the discharge amount of the cooling medium pump 42 is increased to increase the heat exchange amount in the anode off-gas heat radiator 18. Such control can increase the cooling amount of the anode off-gas and increase the generation amount of the condensed water.
Or, for example, when the amount of water stored in the condensed water tank 22 is large, the discharge amount of the cooling medium pump 42 is decreased to decrease the heat exchange amount in the anode off-gas heat radiator 18. Such control can decrease cooling amount of the anode off-gas and decrease the generation amount of the condensed water.
As described above, in the present embodiment, the generation amount of the condensed water can be controlled properly based on the amount of water stored in the condensed water tank 22.
Modified examples of Embodiment 2, Embodiment 3, Embodiment 4, and Embodiment 5 may also be applied to Embodiment 6.
A solid oxide fuel cell system according to Embodiment 7 is the solid oxide fuel cell system of Embodiment 2, the modified example of Embodiment 2, Embodiment 3, Embodiment 4, the modified example of Embodiment 4, Embodiment 5 or Embodiment 6, wherein the condensed water circulating passage includes a heat exchanger bypass passage configured to circulate the condensed water such that the condensed water does not flow through the condensed water/off-gas heat exchanger, and a second switch configured to perform switching between circulation of the condensed water through the condensed water/off-gas heat exchanger and circulation of the condensed water through the heat exchanger bypass passage.
The phrase “perform switching between circulation of the condensed water through the condensed water/off-gas heat exchanger and circulation of the condensed water through the heat exchanger bypass passage” is meant to include a case where ON/OFF switching is performed to select circulation of all of the condensed water through the condensed water/off-gas heat exchanger or circulation of all of the condensed water through the heat exchanger bypass passage, and a case where a ratio between the flow rate of the condensed water circulated through the condensed water/off-gas heat exchanger and the flow rate of the condensed water circulated through the heat exchanger bypass passage is changed.
In this configuration, the dew point of the air discharged from the humidifier can be controlled easily.
As exemplarily shown in
The heat exchanger bypass passage 80 is configured to circulate the condensed water such that the condensed water does not flow through the condensed water/off-gas heat exchanger 26. In the example of
The second switch 47 is configured to perform switching between circulation of the condensed water through the condensed water/off-gas heat exchanger 26 and circulation of the condensed water through the heat exchanger bypass passage 80.
In the example of
In a case where the temperature of the condensed water to be supplied to the humidifier 28 is increased, for example, the second switch 47 opens the third on-off valve 46 and closes the fourth on-off valve 48, so that the condensed water is circulated through the condensed water/off-gas heat exchanger 26 without flowing through the heat exchanger bypass passage 80.
In a case where the temperature of the condensed water to be supplied to the humidifier 28 is decreased, the second switch 47 closes the third on-off valve 46 and opens the fourth on-off valve 48, so that the condensed water is circulated through the heat exchanger bypass passage 80 without flowing through the condensed water/off-gas heat exchanger 26.
The third on-off valve 46 and the fourth on-off valve 48 may be on-off valves which are capable of selecting a fully open state or a fully closed state, or may be, for example, flow control valves which are capable of continuously controlling their opening degrees. In this configuration, by changing the ratio between the flow rate of the condensed water circulated through the condensed water/off-gas heat exchanger 26 and the flow rate of the condensed water circulated through the heat exchanger bypass passage 80, the temperature of the condensed water to be supplied to the humidifier 28 can be controlled more effectively.
The second switch 47 may not necessarily include the third on-off valve 46 and the fourth on-off valve 48, but may be constituted by, for example, a three-way valve. Or, the second switch unit 47 may be constituted by only one of the third on-off valve 46 and the fourth on-off valve 48.
The second switch 47 may be controlled by, for example, a control unit. In this case, the control unit may be configured as in the control unit of the modified example of Embodiment 4, and will not be described in detail repeatedly.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 600 of Embodiment 7 may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
In the present embodiment, since the second switch 47 controls the heating amount of the condensed water in the condensed water/off-gas heat exchanger 26, the temperature of the condensed water to be supplied to the humidifier 28 can be easily controlled. Therefore, the dew point of the air discharged from the humidifier 28 can be controlled easily.
Modified examples of Embodiment 2, Embodiment 3, Embodiment 4, Embodiment 5, and Embodiment 6 may also be applied to Embodiment 7.
A solid oxide fuel cell system according to Embodiment 8 is the solid oxide fuel cell system of Embodiment 2, the modified example of Embodiment 2, Embodiment 3, Embodiment 4, the modified example of Embodiment 4, Embodiment 5, Embodiment 6, or Embodiment 7, wherein the condensed water circulating passage include a humidifier bypass passage configured to circulate the condensed water such that the condensed water does not flow through the humidifier, and a third switch configured to perform switching between circulation of the condensed water through the humidifier and circulation of the condensed water through the humidifier bypass passage.
The phrase “perform switching between circulation of the condensed water through the humidifier and circulation of the condensed water through the humidifier bypass passage” is meat to include a case where ON/OFF switching is performed to select circulation of all of the condensed water through the humidifier or circulation of all of the condensed water through the humidifier bypass passage, and a case where a ratio between the flow rate of the condensed water circulated through the humidifier and the flow rate of the condensed water circulated through the humidifier bypass passage is changed.
In this configuration, the dew point of the air discharged from the humidifier can be controlled easily.
As exemplarily shown in
The humidifier bypass passage 82 is configured to circulate the condensed water such that the condensed water does not flow through the humidifier 28. In the example of
The third switch 51 is configured to perform switching between circulation of the condensed water through the humidifier 28 and circulation of the condensed water through the humidifier bypass passage 82.
In the example of
In a case where the flow rate of the condensed water to be supplied to the humidifier 28 is increased, for example, the third switch 51 opens the fifth on-off valve 50 and closes the sixth on-off valve 52, so that the condensed water is circulated through the humidifier 28 without flowing through the humidifier bypass passage 82.
In a case where the flow rate of the condensed water to be supplied to the humidifier 28 is decreased, for example, the third switch 51 closes the fifth on-off valve 50 and opens the sixth on-off valve 52, so that the condensed water is circulated through the humidifier bypass passage 82 without flowing through the humidifier 28.
The fifth on-off valve 50 and the sixth on-off valve 52 may be on-off valves which are capable of selecting a fully open state or a fully closed state, or may be, for example, flow control valves which are capable of continuously controlling their opening degrees. In this configuration, by changing the ratio between the flow rate of the condensed water circulated through the humidifier 28 and the flow rate of the condensed water circulated through the humidifier bypass passage 82, the flow rate of the condensed water to be supplied to the humidifier 28 can be controlled more effectively.
The third switch 51 may not necessarily include the fifth on-off valve 50 and the sixth on-off valve 52, but may be constituted by, for example, a three-way valve. Or, the third switch unit 51 may be constituted by only one of the fifth on-off valve 50 and the sixth on-off valve 52.
The third switch 51 may be controlled by, for example, a control unit. In this case, the control unit may be configured as in the control unit of the modified example of Embodiment 4, and will not be described in detail repeatedly.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 700 of Embodiment 8 may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
In the present embodiment, since the third switch 51 controls the flow rate of the condensed water to be supplied to the humidifier 28, the dew point of the air discharged from the humidifier 28 can be controlled easily.
Modified examples of Embodiment 2, Embodiment 3, Embodiment 4, Embodiment 5, Embodiment 6, and Embodiment 7 may also be applied to Embodiment 8.
A solid oxide fuel cell system according to Embodiment 9 is the solid oxide fuel cell system of Embodiment 2, the modified example of Embodiment 2, Embodiment 3, Embodiment 4, the modified example of Embodiment 4, Embodiment 5, Embodiment 6, Embodiment 7, or Embodiment 8, which further comprises an ion concentration detector configured to detect an ion concentration of the condensed water stored in the condensed water tank, a notification unit, and a control unit configured to cause the notification unit to output an alarm based on a result of detection of the ion concentration detector.
In this configuration, it becomes possible to reduce a possibility that salt and the like is deposited in the humidifier and the heat exchanger.
As exemplarily shown in
The ion concentration detector 54 is configured to detect the ion concentration of the condensed water stored in the condensed water tank 22. As the ion concentration detector 54, for example, an electric conductivity meter including a sensor placed inside the condensed water tank 22, etc., may be used.
As the notification unit 56, for example, a buzzer, a transmitter which wirelessly transmits an alarm signal, etc., may be used.
The control unit 36 causes the notification unit 56 to output the alarm based on a result of detection of the ion concentration detector 54. The control unit 36 may be communicatively connected to the ion concentration detector 54 and to the notification unit 56. For example, in a case where the ion concentration detected by the ion concentration detector 54 is equal to or higher than 20 mS, the control unit 36 causes the notification unit 56 to output the alarm. When the alarm is output, the control unit 36 may discharge the condensed water stored in the condensed water tank 22 to outside the solid oxide fuel cell system 800 and supply to the condensed water tank 22 the clean water supplied from clean water infrastructure located outside the solid oxide fuel cell system 800. The configuration of the control unit 36 may be the same as that of the modified example of Embodiment 4, except for the above, and will not be described in detail repeatedly.
Except for the above, the system configuration and operation of the solid oxide fuel cell system 800 according to Embodiment 9 may be the same as those of the solid oxide fuel cell system 100 of Embodiment 2. Therefore, in
In the present embodiment, the ion concentration detector 54, the notification unit 56 and the control unit 36 can reduce a possibility that the ion concentration of the water within the condensed water circulating passage 20 is increased excessively. Therefore, it becomes possible to reduce a possibility that salt and the like is deposited in the humidifier 28, the condensed water/off-gas heat exchanger 26, etc.
Modified examples of Embodiment 2, Embodiment 3, Embodiment 4, Embodiment 5, Embodiment 6, Embodiment 7, and Embodiment 8 may also be applied to Embodiment 9.
Numeral improvements and alternative embodiments of the present invention will be obvious to those skilled in the art in view of the foregoing description. Accordingly, the description is to be construed as illustrative only, and is provided for the purpose of teaching those skilled in the art the best mode of carrying out the present invention. The details of the structure and/or function may be varied substantially without departing from the spirit of the present invention.
An aspect of the present invention is useful as a solid oxide fuel cell system which is capable of supplying electric power more stably than in a conventional solid oxide fuel cell system, in an environment in which infrastructure for supplying clean water is inadequate and an air temperature tends to rise.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2012-145875 | Jun 2012 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2013/002561 | 4/16/2013 | WO | 00 |
