Patent Publication Number: US-2016240874-A1

Title: Fuel cell generator and method for operating fuel cell generator

Description:
TECHNICAL FIELD 
     The present invention relates to a fuel cell generator and a method for operating a fuel cell generator and, for example, relates to a fuel cell generator capable: of self-repairing damage in a cell stack and a method for operating the fuel cell generator. 
     BACKGROUND ART 
     In the related art, a solid oxide fuel cell (SOFC) in which multiple fuel cells (power generation elements) including a fuel electrode, a solid electrolyte, and an air electrode sequentially stacked together therein are disposed on the exterior surface of cylindrical base body tube has been proposed (for example, refer to Patent Document 1). In addition, a solid oxide fuel cell in which multiple fuel cells including a fuel electrode, a solid electrolyte, and an air electrode sequentially stacked together therein are provided on a planar base body plate (for example, refer to Patent Document 2) and a solid oxide fuel cell in which multiple fuel cells including a fuel electrode, a solid electrolyte, and an air electrode sequentially stacked together therein are provided on a base body tube having an elliptical sectional shape (for example, refer to Patent Document 3) have been proposed. 
     RELATED ART DOCUMENT 
     Patent Document 
     [Patent Document 1] JP-A-2007-109598 
     [Patent Document 2] JP-A-2003-272658 
     [Patent Document 3] JP-A-2013-211106 
     SUMMARY OF THE INVENTION 
     Problem That the Invention is to Solve 
     Meanwhile, in the fuel electrode in an ordinary solid oxide fuel cell, since nickel (Ni) is used, when an oxidizing atmosphere of an oxygen partial pressure or higher at which nickel (Ni) oxidizes is formed in the fuel electrode, nickel (Ni) in the fuel electrode oxidizes and thus turns into nickel oxide (NiO) and thus there are cases in which the volume of the fuel electrode expands and thus damaged portions (for example, fissures and the like) are generated in the fuel cell. When damaged portions are generated in the fuel cell, a certain amount of oxidizing gas leaks from the air electrode toward the fuel electrode and thus the damaged portions in the fuel cell enlarge and there are cases in which secondary damage develops in peripheral cell stacks in a cartridge. Therefore, there has been a demand for a fuel cell generator capable of repairing damaged portions even in a case in which the fuel cell is damaged. 
     The present invention has been made in consideration of the above-described circumstances and an object of the present invention is to provide a fuel cell generator capable of reducing or repairing damage in damaged portions for itself even in a case in which a fuel cell is damaged and a method for operating the fuel cell generator. 
     Means for Solving the Problem 
     A fuel cell generator of the present invention includes a fuel cell main body formed by disposing multiple power generation elements, in which a fuel electrode, a solid electrolyte, and an air electrode are sequentially stacked together, at predetermined intervals, the multiple power generation elements being connected to each other through an interconnector; a fuel gas supply unit that supplies fuel gas to the fuel electrode; an oxidizing gas supply unit that supplies oxidizing gas to the air electrode; and a repairing particle supply unit that supplies repairing particles that repair a damaged portion to the damaged portion in at least one of the interconnector and the solid electrolyte. 
     According to the fuel cell generator, even in a case in which damaged portions such as fissures are generated in the interconnector and the solid electrolyte of the fuel cell base body, the repairing particles are supplied to the damaged portions and thus it is possible to repair the damaged portions in the interconnector and the solid electrolyte. Therefore, even in a case in which the power generation element is damaged due to the generation of fissures and the like, it is possible to realize a fuel cell generator capable of reducing or repairing damage of the damaged portions for itself. 
     In the fuel cell generator of the present invention, the repairing particle supply unit preferably supplies the repairing particles to the fuel gas. With this configuration, even in a case in which damaged portions such as fissures are generated in the interconnector and the solid electrolyte of the fuel cell base body, the repairing particles supplied to the fuel gas are supplied to the damaged portions together with the fuel gas and thus it is possible to repair the damaged portions in the interconnector and the solid electrolyte. 
     In the fuel cell generator of the present invention, the repairing particle supply unit is preferably a repairing particle layer provided on the surface of a base body provided with the power generation element. With this configuration, the repairing particles included in the repairing particle: layer near the damaged portions in the interconnector and the solid electrolyte of the fuel cell main body having a temperature that is increased due to the leakage of the fuel gas are supplied to the damaged portions and thus it becomes possible to efficiently repair the damaged portions. 
     The fuel cell generator of the present invention preferably includes a control unit that controls the supplied amount of the repairing particles on the basis of an increase in the temperature of the fuel cell base body, the concentration of the fuel gas discharged from the fuel cell base body, the voltage drop of the fuel cell base body, and the concentration of oxygen in the oxidizing gas discharged from the fuel cell base body. With this configuration, the supplied amount of the repairing particles is controlled on the basis of the temperature of the fuel cell base body, the concentration of the fuel gas, the voltage drop of the fuel cell base body, and the concentration of oxygen in the air discharged from the fuel cell base body, which vary depending on the damage, to the power generation element, and thus it becomes possible to efficiently supply the repairing particles depending on the generation of damage in the power generation element. and the degree of the damage. 
     In the fuel cell generator of the present invention, the repairing particles are preferably at least partially gasified at a temperature that is equal to or higher than the temperature of the interconnector or the solid electrolyte during the repairing operation of the fuel cell main body through which the damaged portions are repaired. With this configuration, the repairing particles supplied to the power generation element in the fuel cell generator base body together with the fuel gas are gasified in the fuel cell base body and thus it becomes possible to supply the repairing particles to the damaged portions in a gaseous state as a volatile component. In addition, the repairing particles as the volatile component supplied to the damaged portions are precipitated in a solid form on the basis of the difference in the oxygen partial pressure between the fuel electrode and the air electrode. As a result, it is possible to supply the repairing particles to the damaged portions through a porous ceramic member or the like and thus it becomes possible to efficiently repair the damaged portions. 
     In the fuel cell generator of the present invention, the repairing particles are preferably at least partially melted at a temperature that is equal to or higher than the temperature of the interconnector or the solid electrolyte during the repairing operation of the fuel cell main body through which the damaged portions are repaired. With this configuration, the repairing particles supplied to the power generation element in the fuel cell generator base body together with the fuel gas are melted in the damaged portions having a temperature that is increased to the operation temperature or higher of the fuel cell main body due to the leakage of the fuel gas and thus it becomes possible to reduce the leakage of the fuel gas from the damaged portions. In addition, the temperatures of the damaged portions are decreased due to the reduction of the leakage of the fuel gas from the damaged portions and the repairing particles change to a solid and thus it becomes possible to efficiently repair the damaged portions. 
     In the fuel cell generator of the present invention, the average particle diameter of the repairing particles is preferably 2.5 μm or less. With this configuration, the repairing particles efficiently accompany the fuel gas and it becomes possible to efficiently supply the repairing particles to the damaged portions. 
     In the fuel cell generator of the present invention, the repairing particles preferably include at least one selected from a group consisting of sodium carbonate, sodium chloride, zinc oxide, sodium fluoride, and sodium silicate. With this configuration, the temperature for the melting or decomposition and precipitation of the repairing particles falls into an appropriate range and thus it becomes possible to efficiently prevent the damaged portions. 
     In the fuel cell generator of the present invention, the base body is preferably a base body tube forming a cylindrical shape. With this configuration, the balance between the disposition of the fuel cell and the supply of the fuel gas and the air gas efficiently improves and thus it becomes possible to efficiently generate power. 
     A method for operating a fuel cell generator of the present invention includes a first step of measuring at least one of an increase in the temperature of a fuel cell base body, the concentration of fuel gas discharged from the fuel cell base body, the voltage drop of the fuel cell base body, and the concentration of oxygen in oxidizing gas discharged from the fuel cell base body; and a second step of controlling the amount of repairing particles repairing a damaged portion supplied to the damaged portion in at least one of an interconnector and a solid electrolyte in a power generation element of the fuel cell main body on the basis of at least one measurement value of the measured increase in the temperature, the measured concentration of the fuel gas, the measured voltage drop, and the measured concentration of oxygen. 
     According to the method for operating a fuel cell generator, the supplied amount of the repairing particles is controlled on the basis of the temperature of the fuel cell base body, the concentration of the fuel gas, the voltage drop of the fuel cell base body, and the concentration of oxygen in the air discharged from the fuel cell base body, which vary depending on the damage to the power generation element, and thus, even in a case in which damaged portions such as fissures are generated in the interconnector and the solid electrolyte of the fuel cell base body, the repairing particles are efficiently supplied and the damaged portions in the interconnector and the electrolyte can be repaired. Therefore, even in a case in which the power generation element is damaged due to the generation of fissures, it is possible to realize a method for operating a fuel cell generator which is capable of reducing or repairing damage of the damaged portions for itself. 
     In the method for operating a fuel cell generator of the present invention, it is preferable that, in a case in which the measurement value exceeds a predetermined threshold value, the supply of the repairing particles is initiated or continued and, in a case in which the measurement value is equal to or lower than the predetermined threshold value, the supply of the repairing particles is stopped. With this method, it becomes possible to appropriately supply the repairing particles depending on the generation of damaged portions in the interconnector and the solid electrolyte of the fuel cell base body. 
     In the method for operating a fuel cell generator of the present invention, it is preferable that, in the first step, the supply of the repairing particles is initiated in advance before the initiation of the operation of the fuel cell main body and, in the second step, in a case in which the measurement value exceeds the predetermined threshold value, the supplied amount of the repairing particles is increased and, in a case in which the measurement value is equal to or lower than the predetermined threshold value, the supplied amount of the repairing particles is decreased. With this method, it is possible to supply the repairing particles to the interconnector, the solid electrolyte, and the like of the fuel cell main body at all times and thus it becomes possible to efficiently prevent the generation of the damaged portions. 
     In the method for operating a fuel cell generator of the present invention, it is preferable that, in the second step, in a case in which the measurement value exceeds the predetermined threshold value, the power generation of the fuel cell main body is stopped so as to initiate or continue the supply of the repairing particles and, furthermore, the method includes a third step of, in a state in which the power generation of the fuel cell main body is stopped, measuring at least one of an increase in the temperature of the fuel cell base body, the concentration of the fuel gas discharged from the fuel cell base body, the voltage drop of the fuel cell base body, and the concentration of oxygen in oxidizing gas discharged from the fuel cell base body; and a fourth step of initiating or continuing the supply of the repairing particles in a case in which at least one measurement value of an increase in the temperature of the fuel cell base body, the concentration of the fuel as discharged from the fuel cell base body, the voltage drop of the fuel cell base body, and the concentration of oxygen in oxidizing gas discharged from the fuel cell main body in a state in which the power generation of the fuel cell main body is stopped exceeds the predetermined threshold value, and stopping the supply of the repairing particles in a case in which the measurement value is equal to or lower than the predetermined threshold value. With this method, even in a case in which the damaged portions such as fissures in the interconnector and the solid electrolyte are large, it is possible to prevent an excessive increase in the temperature of a fuel cell module and thus it becomes possible to efficiently reduce or repair damage for itself using the repairing particles. 
     In the method for operating a fuel cell generator of the present invention, it is preferable that, in the first step, the supply of the repairing particles is initiated in advance before the initiation of the operation of the fuel cell base body. With this method, it is possible to supply the repairing particles to the interconnector, the solid electrolyte, and the like of the fuel cell main body at all times and thus it becomes possible to efficiently prevent the generation of the damaged portions. 
     Advantage of the Invention 
     According to the present invention, it is possible to realize a fuel cell generator capable of reducing or repairing damage in damaged portions for itself and a method for operating the fuel cell generator. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  is a schematic configuration view of a fuel cell generator according to a first embodiment of the present invention. 
         FIG. 2  is a schematic configuration view of a fuel cell module according to the first embodiment of the present invention. 
         FIG. 3  is a schematic sectional view of a cell tube according to the first embodiment of the present invention. 
         FIG. 4  is a schematic sectional view of the cell tube according to the first embodiment of the present invention. 
         FIG. 5A  is a flowchart illustrating an example of the operation conditions of the fuel cell generator according to the first embodiment of the present invention. 
         FIG. 5B  is a flowchart illustrating another example of the operation conditions of the fuel cell generator according to the first embodiment of the present invention. 
         FIG. 5C  is a flowchart illustrating still another example of the operation conditions of the fuel cell generator according to the first embodiment of the present invention. 
         FIG. 5D  is a flowchart illustrating far still another example of the operation conditions of the fuel cell generator according to the first embodiment of the present invention. 
         FIG. 6  is a schematic sectional view of a cell tube according to a second embodiment of the present invention. 
         FIG. 7  is a schematic sectional view of a cell tube according to a third embodiment of the present invention. 
         FIG. 8  is a schematic sectional view of another cell tube according to the third embodiment of the present invention. 
         FIG. 9  is a schematic sectional view illustrating another example of the cell tube according to the third embodiment of the present invention. 
         FIG. 10  a schematic sectional view illustrating still another example of the cell tube according to the third embodiment of the present invention. 
     
    
    
     BEST MODE FOR CARRYING OUT THE INVENTION 
     Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings. Meanwhile, the present invention is not limited to the respective embodiments described below and can be carried out in an appropriately-modified manner. In addition, the respective embodiments described below can be carried out in an appropriate combination. In addition, constituent elements common to the respective embodiments will be given the same reference numbers and the description thereof will not be repeated. 
     First Embodiment 
       FIG. 1  is a schematic configuration view of a fuel cell generator  1  according to a first embodiment of the present invention. As illustrated in  FIG. 1 , the fuel cell generator  1  includes a fuel cell module  10  made up of solid oxide fuel cell (SOFC), an air supply unit (oxidizing gas supply unit)  11  that supplies air (oxidizing gas) to the fuel cell module  10 , a fuel supply unit  12  that supplies fuel gas to the fuel cell module  10 , a repairing particle supply unit  14  that supplies repairing particles to the fuel gas, and a control unit  15  that controls the respective units in the fuel cell generator  1 . 
     The air supply unit  11  supplies air G 1  as oxidizing gas to an air supply chamber  108  (not illustrated in  FIG. 1 , refer to  FIG. 2 ) in the fuel cell module  10 . The air supply unit  11  and the air supply chamber  108  are connected to each other through an air supply flow path R 1 . In the air supply flow path R 1 , an air flow rate meter  30  that measures the flow rate of air flowing through the air supply flow path R 1  is provided. The oxidizing gas may be gas containing approximately 15% to 30% of oxygen and the air supply unit  11  may supply, in addition to air, a gas mixture of combustion exhaust gas and air, a gas mixture of oxygen and air, or the like to the fuel cell module  10  as the oxidizing gas. 
     The fuel supply unit  12  supplies fuel gas G 2  to a fuel supply chamber  106  (not illustrated in  FIG. 1 , refer to  FIG. 2 ) in the fuel cell module  10 . The fuel supply unit  12  and the fuel supply chamber  106  are connected to each other through a fuel supply flow path R 2 . Liquefied natural gas (LNG), hydrocarbon gas such as hydrogen (H 2 ) and carbon monoxide (CO) or methane (CE 4 ), or gas produced using a gasification facility of a carbonaceous raw material such as coal is supplied as the fuel gas G 2 . 
     The repairing particle supply unit  14  supplies repairing particles  14   a  to the fuel as G 2 , which is supplied to the fuel cell module  10  from the fuel supply unit  12 , through a repairing particle supply flow path R 4 . The repairing particles  14   a  are significantly affected by a buoyant force rather than gravitational settling and, in order to suspend the repairing particle in the fuel as C 2 , the ordinary upper limit of the particle diameter is, for example, PM2.5 in terms of the particle diameter of a suspended substance in the air. In addition, the repairing particles  14   a  are made up of the submicron particles of the repairing particles  14   a  having an average particle diameter of 2.5 μm or less. In addition, the lower limit value of the average particle diameter of the repairing particles  14   a  is, for example, 1 nm or more. The repairing particles  14   a  are supplied to the inside of the fuel cell module  10  together with the fuel gas G 2  and repair damaged portions (for example, fissures and the like) generated in fuel cells  110  (not illustrated in  FIG. 1 , refer to  FIG. 2 ) in the fuel cell module  10 . 
     The repairing particles  14   a  contain the submicron particles and are thus likely to agglomerate together. When the repairing particles are suspended in carrier gas after removing adsorbed water vapor and the like through preheating and neutralization and then are diluted before being supplied to the inside of the fuel cell module  10 , it is possible to prevent the agglomeration. In addition, when gas is circulated through voids among the particles through fluidized agglomerate so as to drag the particles, the particles are put into a zero-gravity state so as to change all of the particles to behave like liquid, and then the repairing particles  14   a  are supplied, it becomes possible to prevent the agglomeration. 
     The repairing particles  14   a  are at least partially gasified at a temperature that is equal to or higher than the temperature (for example, 800° C. to 950 C.) of an interconnector or a solid electrolyte during the repairing operation of the fuel cell module  10 . Therefore, the repairing particles  14   a  are gasified in the fuel cells  110 , reach the damaged portions, and are precipitated in a solid form due to the difference in the oxygen partial pressure between a fuel electrode and an air electrode, whereby it becomes possible to block fissures and the like generated in the damaged portions. In addition, when the amount of gas leakage in the damaged portions is reduced, the temperature decreases, a molten substance changes to a solid, and it becomes possible to reduce and repair damage in the damaged portions. Meanwhile, the repairing operation mentioned herein refers not only to a repairing operation carried out during the power generation of the fuel cell module  10 , the details of which will be described below, but also to a repairing operation carried out using the repairing particles  14   a  under maintenance conditions in which the power generation of the fuel cell module  10  is stopped. 
     As the repairing particles  14   a,  a substance which at least partially changes to a liquid or a gas at the temperature of the interconnector or the solid electrolyte during the repairing operation of a power generation unit  105  (not illustrated in  FIG. 1 , refer to  FIG. 2 ) in the fuel cell module  10  and has a vapor pressure is used. As the repairing particles  14   a,  it is possible to use typical metal elements or compounds of a transition metal element and a typical non-metal element. The repairing particles  14   a  are preferably substances which are oxidized in an oxidizing atmosphere and change the phase from gas to solid in a reducing atmosphere. Examples of the repairing particles  14   a  include NaCl, EnCl 2 , and the like. In addition, as the repairing particles  14   a,  when a eutectic reaction is used by mixing multiple compounds of a typical metal element, a transition metal element, and a typical non-metal element, it is also possible to use a mixture of KCl-NaCl or the like having a melting point that is decreased to be lower than that of a sole compound. A substance having a low reactivity with a material configuring the cell stack of the fuel cell module  10  is preferred. The repairing particles  14   a  are preferably, for example, at least one selected from a group consisting of sodium carbonate (NaCO 3 ), sodium chloride (NaCl), zinc chloride (ZnCl 2 ), sodium fluoride (NaF), and sodium silicate. 
     Examples of a method for producing the repairing particles  14   a  include a method for producing the repairing particles  14   a  having a submicron (several hundred nanometers) size by crushing the repairing particles synthesized using a solid phase method, a liquid phase method, or a gas phase method. In the solid phase method, it becomes possible to obtain the repairing particles  14   a  having a submicron size by crushing the repairing particles  14   a  using a ball mill or the like after the synthesis of the repairing particles  14   a.  In the liquid phase method, it becomes possible to obtain the nano-sized repairing particles  14   a  using a coprecipitation method, a sol-gel method, a liquid-phase reduction method, a hydrothermal method, or the like. In addition, in the gas phase method, it becomes possible to obtain the nano-sized repairing particles  14   a  using an electric furnace method, a chemical flame method, a laser method, a thermal plasma method, or the like. Among these, the repairing particles  14   a  are preferably produced using the liquid phase method from the viewpoint of the manufacturing costs, qualities, and the like. In addition, the average particle diameter of the repairing particles  14   a  is preferably 1 μm or less. Meanwhile, in the present embodiment, the average particle diameter refers to the average particle diameter (the 50% diameter in the volume-based volume fraction) measured using a measurement method based on JIS R 1629 “Determination of particle size distributions for fine ceramic raw powders by laser diffraction and scattering method”. 
     In addition, the fuel cell generator  1  includes a voltage meter  40  that measures the voltage of a current in the fuel cell module  10 , a first temperature sensor  41  and a second temperature sensor  42  provided in the air supply flow path R 1 , a third temperature: sensor  43  provided in a power generation chamber  105  in the fuel cell module:  10 , an oxygen concentration meter  44  provided in an air discharge flow path R 5  in the fuel cell module  10 , and a gas concentration meter  45  provided in a fuel gas discharge flow path R 6  in the fuel cell module  10 . 
     The voltage meter  40  measures the voltage of a current obtained through the power generation of the fuel cell module  10 . The first temperature sensor  41  is provided in the air supply flow path R 1 . The first temperature sensor  41  measures the temperature of air flowing through the air supply flow path R 1 . The second temperature sensor  42  is provided downstream of the converging portion of a supply flow path for fuel gas for combustion R 3  connected to the air supply flow path R 1 . The second temperature sensor  42  measures the temperatures of air and fuel gas for combustion which are mixed together downstream of the air supply flow path R 1 . 
     The third temperature sensor  43  measures the temperature of the power generation chamber  105  in the fuel cell module  10 . The oxygen concentration meter  44  measures the concentration of oxygen in the air discharged from the fuel cell module  10 . The gas concentration meter  45  measures the concentration of the fuel gas in the fuel as G 2  discharged from the fuel cell module  10 . 
     To a control unit  15 , the air flow rate meter  30 , the voltage meter  40 , the first temperature sensor  41 , the second temperature sensor  42 , the third temperature sensor  43 , the oxygen concentration meter  44 , and the gas concentration meter  45 , which have been described, are connected. The control unit  15  controls the respective units in the fuel cell generator during the initiation operation and the power generation operation of the fuel cell module  10 . In addition, the control unit  15  controls the supplied amount of the repairing particles  14   a  that are supplied to the fuel gas G 2  from the repairing particle supply unit  14  through a control valve  33 . 
       FIG. 2  is a schematic configuration view of the fuel cell module  10 . As illustrated in  FIG. 2 , the fuel cell module  10  includes a casing  101 , multiple cell tubes  102  that are disposed in the casing  101  and are formed into a substantially cylindrical shape, an upper tube plate  103   a  supporting the upper end portions of the cell tubes  102 , a lower tube plate  103   b  supporting the lower end portions of the cell tubes  102 , and an upper adiabatic body  104   a  and a lower adiabatic body  104   b  disposed between the upper and lower tube plates  103   a  and  103   b.    
     The casing  101  includes a trunk case  101   a  and an upper case  101   b  and a lower case  101   c  provided at both ends of the trunk case  101   a.  The cell tubes  102  are stored in an interior storage space of the casing  101 . 
     The upper tube plate  103   a  is a plate-like member disposed on one side (upper side) of the casing  101  in the shaft direction. The lower tube plate  103   b  is a plate-like member disposed on the other side (lower side) of the casing  101  in the shaft direction. In a space partitioned by the upper case  101   b  and the upper tube plate  103   a  of the casing  101 , the fuel supply chamber  106  is formed. In a space partitioned by the lower case  101   c  and the lower tube plate  103   b  of the casing  101 , a fuel discharge chamber  107  is formed. The opening ends of the cell tubes  102  on one side are disposed in the fuel supply chamber  106  and the opening ends of the cell tubes  102  on the other side are disposed in a fuel discharge chamber  107 . 
     The upper adiabatic body  104   a  is disposed on one side (upper side) of the casing  101  in the shaft direction. The upper adiabatic body  104   a  is formed into a blanket shape or a board shape using an adiabatic material. The lower adiabatic body  104   b  is disposed on the other side (lower side) of the casing  101  in the shaft direction. The lower adiabatic body  104   b  is formed into a blanket shape or a board shape using an adiabatic material. In the respective adiabatic bodies  104   a  and  104   b,  holes  111   a  and  111   b,  through which the cell tubes  102  are inserted, are formed respectively. The holes  111   a  and  111   b  are formed to have a diameter that is larger than the diameter of the cell tube  102 . In a space sandwiched by the upper adiabatic body  104   a  and the lower adiabatic body  104   b,  the power generation chamber  105  is formed. In addition, in a space between the lower tube plate  103   b  and the lower adiabatic body  104   b,  an air supply chamber  108  is formed and in a space between the upper tube plate  103   a  and the upper adiabatic body  104   a,  an air discharge chamber  109  is formed. The fuel cells  110  in the cell tube  102   s  are disposed so as to be located only in the power generation chamber  105 . 
       FIG. 3  is a schematic sectional view of the cell tube  102 . As illustrated in  FIG. 3 , the cell tube  102  includes a base body tube  102   a  forming a cylindrical shape and the fuel cell  110  which serves as a power generation element provided on the outer circumferential surface of the base body tube  102   a.  The base body tube  102   a  is a porous ceramic cylindrical tube. Inside the base body tube  102   a,  the fuel gas G 2  flows. In addition, the base body tube  102   a  is porous and thus guides the fuel gas G 2  flowing therein to the outer circumferential surface of the base body tube  102   a.    
     The fuel cell  110  of the present embodiment is configured by stacking a fuel electrode  111 , a solid electrolyte  112 , an interconnector  114 , and an air electrode  113  together. The fuel electrode  111  is provided on one surface of the solid electrolyte  112 . The air electrode  113  is provided in on the other surface of the solid electrolyte  112 . The fuel electrode  111  is in contact with the outer circumferential surface of the base body tube  102   a.  The air electrode  113  includes active metal. The air electrode  113  has a function (combustion through a catalytic action) that contributes to a combustion reaction using the active metal included therein. 
     In addition, the multiple fuel cells  110  are disposed along the shaft direction of the base body tube  102   a  at predetermined intervals. In the multiple fuel cells  110 , the fuel electrode  111  of one of the adjacent fuel cells  110  and the air electrode  113  of the other of the adjacent fuel cells  110  are connected to each other through the interconnector  114 . The fuel cells  110  configured as described above generate power at a high temperature of, for example, 800° C. to 950° C. during the power generation operation of the fuel well generator  1 . 
     The base body tube  102   a  is a ceramic cylinder and includes an iron group metal having an internal reforming function (for example, Ni), an iron group metal oxide (for example, NiO), an alloy and an alloy oxide thereof. The base body tube  102   a  is, for example, a mixture of Ni and CSZ (calcia stabilized zirconia (CaO stabilized ZrO 2 )). In addition, the base body tube  102   a  forms a fuel passage with the inner circumferential surface. The base body tube  102   a  is configured using a porous material and transmits the fuel gas flowing through the fuel passage to the fuel electrode  111 . The base body tube  102   a  can be made to be porous by adjusting the particle diameters of the mixture or mixing a pore material in. 
     The fuel electrode  111  is configured using, for example, a mixture of Ni and YSZ (yttrium stabilized zirconia (Y 2 O 3  stabilized ZrO 2 )). The fuel electrode  111  is electrically conductive and is a porous material. The solid electrolyte  112  is stacked on the surface of the fuel electrode  111  opposite to the base body tube  102   a  and is formed so as to be present up to a portion between the fuel electrode and another fuel electrode  111  adjacent to each other in the shaft direction of the base body tube  102   a.  The fuel electrode  111  is configured using an oxide of a compound material between Ni and a zirconia-based electrolytic material, which is, for example, Ni-YSZ. In the fuel electrode  111 , Ni, which is a component of the fuel electrode  111 , has a catalytic action with respect to the fuel gas G 2 . This catalytic action causes a reaction of the fuel gas G 2  supplied through the base body tube  103 , for example, a gas mixture of methane (CH 4 ) and water vapor, and reforms the fuel gas into hydrogen (H 2 ) and carbon monoxide (CO). In addition, the fuel electrode  111  makes the hydrogen (H 2 ) and the carbon monoxide (CO) obtained through the reforming electrochemically react with oxygen ions supplied through the solid electrolyte  112  near the interface with the solid electrolyte  112  so as to generate water (H 2 O) and carbon dioxide (CO 2 ). The fuel cells  110  generate power using electrons discharged from the oxygen ions. 
     The solid electrolyte  112  is configured using, for example, YSZ (yttrium stabilized zirconia (Y 2 O 3  stabilized ZrO 2 )). A dense material is used in order to prevent the contact between the fuel electrode gas and the air electrode gas. As the solid electrolyte  112 , YSZ having airtightness so that gas does not easily pass therethrough and high oxygen ion conductivity at a high temperature is mainly used. The solid electrolyte  112  moves oxygen ions (O 2− ) generated in the air electrode  113  to the fuel electrode  111 . 
     The air electrode  113  is configured using, for example, at least one porous conductive ceramic such as a LaMnO 3 -based material, a LaFeO 3 -based material, and a LaCoO 3 -based material. The air electrode  113  dissociates oxygen in air G 1 , which serves as an oxidizing gas being supplied, so as to generate oxygen ions (O 2− ) near the interface with the solid electrolyte  112 . In addition, the air electrode  113  has a function (combustion through a catalytic action) that contributes to a combustion reaction. When the fuel gas G 2  is supplied to the air electrode  113 , the fuel gas G 2  catalytically combusts in the air electrode  113 . The air electrode  113  is catalyst having a power generation function and is also a catalyst having a combustion function including an oxidation reaction. 
     The interconnector  114  is configured using a conductive perovskite oxide expressed by M 1-x L x TiO 3  (M represents an alkaline-earth metal element and L represents a lanthanoid element) such as SrTiO 3  and is made of a dense material in order to prevent the leakage of gas. The interconnector  114  is made of a dense film so as to prevent the fuel gas G  2  and the air G 1  from being mixed together. In addition, the interconnector  114  has stable electric conductivity in both an oxidizing atmosphere and a reducing atmosphere. The interconnector  114  electrically connects, in the fuel cells  110  adjacent to each other, the air electrode  113  in one fuel cell  110  and the fuel electrode  111  in the other fuel cell  110  and connects the fuel cells  110  adjacent to each other in series. 
     In order to configure the cell tube  102 , in the fuel cells  110  adjacent to each other in the shaft direction of the base body tube  102   a,  the fuel electrode  111  in one fuel cell  110  and the air electrode  113  in the other fuel cell  110  are connected to each other through the interconnector  114 . In addition, the fuel electrode  111  is partially coated with the solid electrolyte  112  and is partially coated with the interconnector  114 . In addition, the cell tube  102  is sintered in a state in which the fuel electrode  111 , the solid electrolyte  112 , the interconnector  114 , and the air electrode  113  are stacked on the exterior surface of the base body tube  102   a.    
     Here, the overall operation of the fuel cell module  10  will be described. The fuel cell module  10  carries out an initiation operation through which the fuel cells  110  are heated to a predetermined temperature and then carries out a power generation operation through which power is generated in the fuel cells  110 . When the fuel cell module  10  carries out the power generation operation, the air G 1  into the air supply chamber  108  in the fuel cell module  10 . This air G 1  is supplied to the inside of the power generation chamber  105  through the gaps between the holes  111   b  in the lower adiabatic body  104   b  and the cell tube  102 . On the other hand, the fuel gas G 2  flows into the fuel supply chamber  106 . This fuel gas G 2  is supplied to the inside of the power generation chamber  105  through the inside of the base body tube  102   a  in the cell tube  102 . Here, the air G 1  and the fuel gas G 2  flow in the mutually opposite directions on the inner circumferential surface and the outer circumferential surface of the cell tube  102 . 
     The fuel gas G 2  flowing inside the base body tube  102   a  passes through fine holes in the base body tube  102   a  and reaches the fuel electrode  111 . The fuel gas G 2  is reformed into water vapor using the active metal included in the fuel electrode  111 . Hydrogen generated through the water vapor reforming passes through fine holes in the fuel electrode  111  and reaches the solid electrolyte  112 . On the other hand, the air G 1  flows along the outside of the base body tube  102   a  (the air electrode  113 ). Oxygen in the air ionizes while passing through fine holes in the air electrode  113  or after reaching the solid electrolyte  112 . The ionized oxygen passes through the solid electrolyte  112  and reaches the fuel electrode  111 . The oxygen ions that have passed through the solid electrolyte  112  react with the fuel gas G 2 . The fuel cell module  10  generates power due to the potential difference generated by the above-described cell reaction. 
     In addition, the fuel gas G 2  that is used for power generation in the power generation chamber  105  and thus has a high temperature exchanges heat with the air G 1  that is to he used for power generation in the air supply chamber  108 . In addition, the air G 1  that is used for power generation in the power generation chamber  105  and thus has a hide temperature exchanges heat with the fuel as G 2  that is to be used for power generation in the air discharge chamber  109 . 
     In addition, after the fuel gas G 2  and the air G 1  that have been used for power generation are cooled through the heat exchange, the fuel gas G 2  flows into the fuel discharge chamber  107  and is discharged outside the fuel cell module  10  from the fuel discharge chamber  107 . The air G 1  is discharged outside the fuel cell module  10  from the air discharge chamber  109 . 
     Next, a repairing operation of the fuel cell  110  in the fuel cell generator  1  according the present invention will he described.  FIG. 4  is a schematic sectional view of the cell tube  102  according to the present embodiment. 
     As illustrated in  FIG. 4 , during the operation of the fuel cell generator  1 , the fuel gas G 2  is supplied to the inside of the base body tube  102   a,  remaining fuel gas and water are generated, and the air G 1  flows outside the base body tube  1   02   a.  Here, in a case in which there are defective portions such as pinholes in the solid electrolyte  112 , which is a dense film, and the interconnector  114  in the fuel cell  110 , there are cases in which oxygen contained in the air G 1  intrudes into the fuel electrode  111  through the defective portions due to the leakage caused by the differential pressure between the fuel electrode  111  and the air electrode  113  and the diffusion caused by the difference in the concentration of oxygen between the fuel electrode  111  and the air electrode  113 , nickel (Ni) in the fuel electrode  111  oxidizes and thus turns into nickel oxide (NiO), and the volume of a partial region of the fuel electrode  111  expands. In this case, there are cases in which compressive stress is generated in another region of the fuel electrode  111  and thus a tensile stress is generated on the inner surfaces of the electrolyte  112 , the interconnector  114 , and the base body tube  102   a,  when the generated tensile stress is greater than the fracture stress, fissures and the like are generated, and thus damaged portions X are generated. 
     In the present embodiment, the repairing particles  14   a  are supplied to the fuel cells  110  together with the fuel gas G 2  flowing inside the base body tube  102   a.  The supplied repairing particles  14   a  are at least partially gasified at the temperature or higher (for example, 800° C. to 950° C.) of the interconnector  114  or the solid electrolyte  112  during the repairing operation. In addition, the gasified repairing particles  14   a  pass through the base body tube  102   a  configured using a porous ceramic material or the like and reach the damaged portions X in the fuel cells  102 . Furthermore, the damaged portions X are in a state in which the oxygen partial pressure in the fuel is higher than that in the fuel electrode  111  in a reducing atmosphere due to the leakage of oxygen from the air electrode  113  caused by the differential pressure between the fuel electrode  111  and the air electrode  113  and the diffusion of oxygen caused by the difference in the concentration of oxygen between the fuel electrode  111  and the air electrode  113 , and the gasified repairing particle component of the repairing particles  14   a  that have reached the damaged portions X is oxidized at the oxygen partial pressure of the damaged portions X and is precipitated in a solid form. Therefore, it is possible to at least partially block the damaged portions X, which serve as the routes for the leakage of oxygen from the air electrode  113  to the fuel electrode  111 , with the precipitated solid and the leakage amount of oxygen is reduced. 
     Next, a method for operating a fuel cell according to the present embodiment will be described in detail with reference to  FIGS. 5A and 5B .  FIG. 5A  is a flowchart illustrating an example of the method for operating the fuel cell according to the present embodiment. As illustrated in  FIG. 5A , first, the control unit  15 , after an ordinary operation of the fuel cell generator  1  (Step ST 10 ), determines whether or not a variety of measurement values related to an increase in the temperature of the fuel cell module  10  measured using the third temperature sensor  43  (for example, 25° C.), the concentration of the fuel gas in the fuel gas discharged from the fuel cell module  10  measured using the gas concentration meter  45 , the voltage drop of the fuel cell module  10  measured using the voltage meter  40 , and the concentration of oxygen in the air discharged from the fuel cell module  10  measured using the oxygen concentration meter  44  are equal to or lower than the predetermined threshold values (Step ST 11 ). In addition, in a case in which the variety of measurement values are equal to or lower than the predetermined threshold values (Step ST 11 : Yes), the control unit  15  continues the ordinary operation of the fuel cell module  10 . In addition, in a case in which the variety of measurement values exceed the predetermined threshold values (Step ST 11 : No), the control unit  15  initiates the supply of the repairing particles  14   a  from the repairing particle supply unit  14  to the fuel cell module  10  (Step ST 12 ). Therefore, the repairing particles  14   a  are gasified, reach the damaged portions X, and are precipitated as illustrated in  FIG. 4  and thus the fuel cell module  10  becomes capable of repairing fissure and the like in the damaged portions X. The repairing particles  14   a  that do not contribute to the repair are precipitated in a low-temperature section other than the fuel cells  110 . Therefore, the repairing particles are collected by installing a filter at the pipe in the fuel outlet or collected by accelerating the condensation from a gas phase using a cooling trap. 
     In addition, the control unit  15 , again, determines whether or not the variety of measured measurement values are equal to or lower than the predetermined threshold values and, in a case in which the variety of measurement values are equal to or lower than the predetermined threshold values (Step ST 13 : Yes), the supply of the repairing particles  14   a  from the repairing particle supply unit  14  is stopped so as to continue the ordinary operation of the fuel cell module  10  (Step ST 14 ). Here, the control unit  15  may make only the fuel gas G 2  flow for a predetermined time without conducting electricity after the end of the supply of the repairing particles. Therefore, the repairing particles  14   a  remaining in the fuel cell module  10  can be discharged and thus it becomes possible to clean the fuel cell module  10 . In addition, in a case in which the variety of re-measured measurement values exceed the predetermined threshold values (Step ST 13 : No), the control unit  15  continues the supply of the repairing particles  14   a  from the repairing particle supply unit  14  and operates the fuel cell module  10  (Step ST 12 ). 
       FIG. 5B  is a flowchart illustrating another example of the method for operating the fuel cell generator according to the present embodiment. In the example illustrated in  FIG. 5B , in a case in which a variety of measurement values measured using the third temperature sensor  43 , the gas concentration meter  45 , the voltage meter  40 , and the oxygen concentration meter  44  exceed the predetermined threshold values (Step ST 11 : No), the control unit  15  stops the supply of the air G 1  and the fuel gas G 2  to the fuel cell module  10  so as to stop the power generation of the fuel cell module  10  (Step ST 15 ). Therefore, even in a case in which the damaged portions X such as fissures and the like in the interconnector  114 , the solid electrolyte  112 , and the like are large, it is possible to prevent an excessive increase in the temperature of the fuel cell module  10  and thus it becomes possible to efficiently repair and reduce damage for itself using the repairing particles  14   a.  After the repairing operation of the damaged portions X, the control unit  15  reinitiates the supply of the air G 1  and the fuel gas G 2  to the fuel cell module  10  so as to initiate power generation (Step ST 16 ) and then operates the fuel cell module  10  in an ordinary manner. 
       FIG. 5C  is a flowchart illustrating still another example of the method for operating the fuel cell according to the present embodiment. In the example illustrated in  FIG. 5C , first, the control unit  15  initiates the supply of the repairing particles  14   a  from the repairing particle supply unit  14  to the fuel cell module  10  before the initiation of the operation (Step ST 21 ). Subsequently, the control unit  15  initiates the ordinary operation of the fuel cell module  10  in a state in which the supply of the repairing particles  14   a  from the repairing particle supply unit  14  to the fuel cell module  10  is continued (Step ST 22 ). Next, the control unit  15  determines whether or not a variety of measurement values related to an increase in the temperature of the fuel cell module  10  measured using the third temperature sensor  43  (for example, 25° C., the concentration of the fuel gas in the fuel gas discharged from the fuel cell module  10  measured using the gas concentration meter  45 , the voltage drop of the fuel cell module  10  measured using the voltage meter  40 , and the concentration of oxygen in the air discharged from the fuel cell module  10  measured using the oxygen concentration meter  44  are equal to or lower than the predetermined threshold values (Step ST 23 ) In addition, in a case in which the variety of measurement values exceed the predetermined threshold values (Step ST 23 : No), the supplied amount of the repairing particles  14   a  from the repairing particle supply unit  14  to the fuel cell module  10  is increased (Step ST 24 ). Therefore, the repairing particles  14   a  are gasified, reach the damaged portions X, and are precipitated as illustrated in  FIG. 4  and thus the fuel cell module  10  becomes capable of repairing fissures and the like in the damaged portions X. The repairing particles  14   a  that do not contribute to the repair are precipitated in a low-temperature section other than the fuel cells  110 . Therefore, the repairing particles are collected by installing a filter at the pipe in the fuel outlet or collected by accelerating the condensation from a as phase using a cooling trap. In addition, in a case in which the variety of measurement values are equal to or lower than the predetermined threshold values (Step ST 23 : Yes), the control unit  15  decreases the supplied amount of the repairing particles  14   a  from the repairing particle supply unit  14  and continues the ordinary operation of the fuel cell module  10  (Step ST 25 ). Therefore, the method for operating the fuel cell can supply the repairing particles  14   a  to the interconnector  114 , the solid electrolyte  112 , and the like in the fuel cell module  10  at all times and thus it becomes possible to efficiently prevent the generation of the damaged portions X. 
       FIG. 5D  is a flowchart illustrating far still another example of the method for operating the fuel cell according to the present embodiment. In the example illustrated in  FIG. 5D , first, the control unit  15  initiates the supply of the repairing particles  14   a  from the repairing particle supply unit  14  to the fuel cell module  10  before the initiation of the operation (Step ST 31 ). Subsequently, the control unit  15  operates the fuel cell module  10  in an ordinary manner in a state in which the repairing particles  14   a  are supplied to the fuel cell module  10  from the repairing particle supply unit  14  (Step ST 32 ). Next, in a case in which a variety of measurement values measured using the third temperature sensor  43 , the gas concentration meter  45 , the voltage: meter  40 , and the oxygen concentration meter  44  exceed the predetermined threshold values (Step ST 33 : No), the control unit  15  stops the supply of the air G 1  and the fuel gas G 2  to the fuel cell module  10  and stops the power generation of the fuel cell Module  10  (Step ST 34 ). Therefore, even in a case in which the damaged portions X such as fissures and the like in the interconnector  114 , the solid electrolyte  112 , and the like are large, it is possible to prevent an excessive increase in the temperature of the fuel cell module  10  and thus it becomes possible to efficiently reduce and repair damage for itself using the repairing particles  14   a.    
     Next, the control unit  15  continues the supply of the repairing particles  14   a  to the fuel cell module  10  in a state in which the power generation of the fuel cell module  10  is stopped (Step ST 35 ). Here, in a case in which the damaged portions X such as fissures and the like in the interconnector  114 , the solid electrolyte  112 , and the like are large, the control unit  15  may use the repairing particles  14   a  that are at least partially melted at a high temperature with respect to the interconnector  114  or the solid electrolyte  112  (for example, 800° C. to 950° C.) during the repairing operation of the fuel cell module  10  according to a second embodiment, the details of which will be described below. Therefore, it is possible to jointly use two kinds of repairing particles  14   a  having different properties and thus it becomes possible to efficiently repair the damaged portions X. Next, the control unit  15  determines whether or not a variety of measurement values related to an increase in the temperature of the fuel cell module  10  measured using the third temperature sensor  43  (for example, 25° C.) the concentration of the fuel gas in the fuel gas discharged from the fuel cell module  10  measured using the gas concentration meter  45 , the voltage drop of the fuel cell module  10  measured using the voltage meter  40 , and the concentration of oxygen in the air discharged from the fuel cell module  10  measured using the oxygen concentration meter  44  are equal to or lower than the predetermined threshold values (Step ST 36 ). In addition, in a case in which the variety of measurement values exceed the predetermined threshold values (Step ST 36 : No), the control unit  15  continues the supply of the repairing particles  14   a  from the repairing particle supply unit  14  to the fuel cell module  10  (Step ST 34 ). In addition, in a case in which the variety of measurement values are equal to or lower than the predetermined threshold values (Step ST 36 : Yes), the control unit  15  stops the supply of the repairing particles  14   a  to the fuel cell module  10  from the repairing particle supply unit  14  so as to end the repairing operation (Step ST 37 ). Subsequently, the control unit  15 , after the repairing operation of the damage portions X, reinitiates the supply of the it G 1  and the fuel gas G 2  to the fuel cell module  10  so as to initiate power generation (Step ST 38 ) and then operates the fuel cell module  10  in an ordinary manner. Therefore, in the method for operation the fuel cell, it is possible to supply the repairing particles  14   a  to the interconnector  114 , the solid electrolyte  112 , and the like in the fuel cell module  10  at all times from before the initiation of the ordinary operation of the fuel cell module  10  to after the completion of the repairing operation of the fuel cell module  10  and thus it becomes possible to efficiently prevent the generation of the damaged portions X. 
     As described above, according to the present embodiment, even in a case in which fissures are generated in the fuel cells  110  in the fuel cell module  10 , the repairing particles  14   a  supplied to the fuel gas G 2  are supplied to the fuel cells  110  together with the fuel gas G 2  and thus it is possible to repair the damaged portions X such as fissures generated in the fuel cells  110 . Therefore, even in a case in which the fuel cells  110  are damaged due to the generation of fissures, it is possible to realize the fuel cell generator  1  capable of reducing or repairing damage of the damaged portions for itself. 
     Second Embodiment 
     Next, the second embodiment of the present invention will be described. Meanwhile, in the following description, differences from the above-described first embodiment will be mainly described and the repetition of the description will be avoided. 
       FIG. 6  is a schematic sectional view of the cell tube  102  according to the present embodiment. As illustrated in  FIG. 6 , in the present embodiment, the repairing particles  14   a  that are at least partially melted at a high temperature with respect to the interconnector  114  or the solid electrolyte  112  (for example, 800° C. to 950° C.) during the repairing operation of the fuel cell module  10  are used as the repairing particles  14   a.  Therefore, even in a case in which fissure portions  102   ax  are generated in the base body tube  102   a,  the repairing particles  14   a  are melted near the damaged portions  102 X in the fuel electrode  111  having a temperature that is increased due to the leakage of gas, the molten repairing particles  14   a  intrude toward the fuel electrode  111  from the fissure portions  102   ax  in the base body tube  102   a  and reach the damaged portions X. Therefore, the molten repairing particles  14   a  serve as resistance to the leakage of gas from the damaged portions X caused by a surface tension or the differential pressure between the fuel and the air and thus the amount of gas leakage is slowly decreased. In addition, the temperatures near the damaged portions X are decreased in response to the reduction of the amount of gas leakage and thus it becomes possible to fully block the damaged portions X through the solidification of the molten substance of the repairing particles  14   a.    
     In the present embodiment, the repairing particles  14   a  are preferably a compound of a typical metal element, a transition metal element, and a typical non-metal element which is at least partially melted at the temperature of the interconnector  114  or the solid electrolyte  112  during the repairing operation of the power generation unit in the fuel cell module  10 . Examples of the repairing particles  14   a  include caicia silicate (CaSi 2 ), sodium fluoride (NaF), and the like having a melting point of approximately 1000° C. In addition, it is also possible to use SrO—ZnO—P 2 O 5 , PbO—CrO 3 —WO 3 , and the like which are mixtures having a melting point that is decreased to be lower than that of a sole compound by mixing multiple compounds of a typical metal element, a transition metal element, and a typical non-metal element and causing a eutectic reaction. 
     As described above, according to the present embodiment, since the repairing particles  14   a  having higher melting point than the interconnector  114  or the solid electrolyte  112  during the repairing operation of the fuel cell module  10  are used, the repairing particles  14   a  are melted near the damaged portions X in the fuel cells  110  having a temperature that is increased due to gas leakage and reach the damaged portions X. Therefore, it becomes possible to block the damaged portions X and thus it becomes possible to efficiently reduce and repair damage in the damaged portions X for itself. 
     Third Embodiment 
     Next, a third embodiment will be described. Meanwhile, in the following description, differences from the above-described first embodiment will be mainly described and the repetition of the description will be avoided. 
       FIG. 7  is a schematic sectional view of the cell tube  102  according to the present embodiment. As illustrated in  FIG. 7 , in the present embodiment, the repairing particles  14   a  are applied onto the interior wall of the base body tube  102   a  in advance so as to provide a repairing particle layer (repairing particle supply chamber)  140  including the repairing particles  14   a.  Therefore, in a case in which the fissure portions  102   ax  are generated on the interior wall of the base body tube  102   a  and the damaged portions X are generated in the fuel cells  110  as illustrated in  FIG. 8 , the repairing particles  14   a  in the repairing particle layer  140  intrude into the damaged portions X through the fissure portions  102   ax  and thus it becomes possible to repair the damaged portions X in the same manner as in the first and second embodiments. The repairing particle layer  140  preferably includes a pore-forming material and the like so as to transmit gas. In addition, the repairing particle layers  140  are preferably particles that are not melted at the operation temperature of the fuel cell module  10  but are melted or gasified at the temperature of the interconnector  114  or the solid electrolyte  112  during the repairing operation. Furthermore, the repairing particle layer  140  preferably has a linear expansion. coefficient (thermal expansion rate) similar to the linear expansion coefficient of a cell stack. 
     In the present embodiment, as the repairing particles  14   a,  it is possible to use the same particles as in the second embodiment. In addition, as the repairing particles  14   a,  a substance that at least partially turns into liquid or gas at the temperature of the interconnector  114  or the solid electrolyte  112  during the repairing operation so as to have a vapor pressure may also be used. Examples of the above-described substance include substances, such as sodium fluoride (NaF), that are compounds of a typical metal element, a transition metal element, and a typical non-metal element, are oxidized in an oxidizing atmosphere, and change the phase from gas to solid in a reducing atmosphere. In addition, a substance having a melting point that is decreased to be lower than that of a sole compound by mixing multiple compounds of a typical metal element, a transition metal element, and a typical non-metal element and causing a eutectic reaction may also be used. 
     In the method for manufacturing the repairing particle layer  140 , a pore-forming material for forming pores among the repairing particles  14   a,  purified water, and a dispersing material are mixed together and are kneaded using a kneader, thereby producing a slurry. In addition, it is possible to provide the repairing particle. layer  140  by applying the obtained slurry to the inside of the base body tube  102   a  in a cell stack after the firing of the air electrode or a cell stack after a reducing step through dipping or the like. Examples of the pore-forming material include acrylic particles and styrene particles. In addition, as the dispersing material, it is possible to use a dispersing material for ceramics (product name: POIZ532A manufactured by KAO Corporation) or the like. In addition, the film thickness during the application of the slurry of the repairing particles  14   a  can be appropriately controlled using the viscosity, yield value, surface tension, and the like of the slurry. 
     As described above, according to the present embodiment, since the repairing particles  14   a  are supplied to the damaged portions X generated in the fuel cells  110  from the repairing particle layer  140  provided in advance on the interior wall of the base body tube  102   a,  even in a case in which the damaged portions X are generated in the fuel cells  110 , it becomes possible to repair the damaged portions X for itself. 
     Meanwhile, in the present embodiment, the repairing particles  14   a  may be supplied from the repairing particle layer  140  provided in the cell tube  102  and, as illustrated in  FIGS. 9 and 10 , similar to the first and second embodiments, the repairing particles  14   a  may be supplied from the repairing particle supply unit  14  to the fuel cell as necessary. Therefore, even in a case in which the damaged layers in the damaged portions X are insufficiently reduced due to the insufficient supplied amount of the repairing particles  14   a  supplied from the repairing particle layer  140 , it becomes possible to reduce and repair damage in the damaged portions X in the interconnector  114  and the solid electrolyte  112  for itself using the repairing particles  14   a  supplied from the repairing particle supply unit  14  together with the fuel gas. In addition, since it also becomes possible to supply the repairing particles  14   a  that are different from the repairing particles  14   a  provided in advance in the repairing particle layer  140 , it also becomes possible to efficiently repair the damaged portions X which cannot be sufficiently repaired using the repairing particles  14   a  in the repairing particle layer  140 . 
     Meanwhile, in the respective embodiments described above, an example in which the base body of the fuel cell  110  is the cylindrical base body tube  102   a  has been described; however, as the base body, it is possible to use not only the cylindrical base body tube  102   a  but also base bodies having a variety of shapes such as a planar base body tube and a flat-cylindrical base body tube. In addition, the interconnector  114  may be connected in series or in parallel. 
     In addition, in the respective embodiments described above, an example in which the fuel cells  110  in the fuel cell module  10  are provided on the base body has been described; however, in the fuel cell module  10 , the fuel cells  110  do not need to be provided on the base body at all times and a plurality of the fuel cells  110  having the fuel electrode  111 , the solid electrolyte  112 , and the air electrode  113  sequentially laminated may be disposed adjacent to each other. 
     DESCRIPTION OF REFERENCE NUMERALS AND SIGNS 
       1  FUEL CELL GENERATOR 
       10  FUEL CELL MODULE 
       11  AIR SUPPLY UNIT 
       12  FUEL SUPPLY UNIT 
       13  SUPPLY UNIT FOR FUEL FOR COMBUSTION 
       14  REPAIRING PARTICLE SUPPLY UNIT 
       14   a  REPAIRING PARTICLE 
       15  CONTROL UNIT 
       30  AIR FLOW RATE METER 
       31  FLOW RATE METER OF FUEL GAS FOR COMBUSTION 
       32  FLOW RATE ADJUSTMENT VALVE 
       40  VOLTAGE METER 
       41  FIRST TEMPERATURE SENSOR 
       42  SECOND TEMPERATURE SENSOR 
       43  THIRD TEMPERATURE SENSOR 
       44  OXYGEN CONCENTRATION METER 
       45  GAS CONCENTRATION METER 
       101  CASING 
       102  CELL TUBE 
       102   a  BASE BODY TUBE 
       105  POWER GENERATION CHAMBER 
       106  FUEL SUPPLY CHAMBER 
       107  FUEL DISCHARGE CHAMBER 
       108  AIR SUPPLY CHAMBER 
       109  AIR DISCHARGE CHAMBER 
       110  FUEL CELL 
       111  FUEL ELECTRODE 
       112  SOLID ELECTROLYTE 
       113  AIR ELECTRODE 
       114  INTERCONNECTOR 
       140  REPAIRING PARTICLE LAYER 
     R 1  AIR SUPPLY FLOW PATH 
     R 2  FUEL SUPPLY FLOW PATH 
     R 4  REPAIRING PARTICLE SUPPLY FLOW PATH 
     R 5  AIR DISCHARGE FLOW PATH 
     R 6  FUEL GAS DISCHARGE FLOW PATH 
     G 1  AIR 
     G 2  FUEL GAS