WO2014123020A1 - Fuel cell system - Google Patents

Fuel cell system Download PDF

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Publication number
WO2014123020A1
WO2014123020A1 PCT/JP2014/051640 JP2014051640W WO2014123020A1 WO 2014123020 A1 WO2014123020 A1 WO 2014123020A1 JP 2014051640 W JP2014051640 W JP 2014051640W WO 2014123020 A1 WO2014123020 A1 WO 2014123020A1
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WIPO (PCT)
Prior art keywords
fuel
fuel cell
generating member
container
cell system
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PCT/JP2014/051640
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French (fr)
Japanese (ja)
Inventor
誉之 岡野
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コニカミノルタ株式会社
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Publication of WO2014123020A1 publication Critical patent/WO2014123020A1/en

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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N5/00Analysing materials by weighing, e.g. weighing small particles separated from a gas or liquid
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04201Reactant storage and supply, e.g. means for feeding, pipes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • H01M8/0625Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the present invention provides a fuel cell system comprising a fuel generating member that generates a fuel gas by a chemical reaction, and a fuel cell unit that generates power by a reaction between an oxidant gas containing oxygen and a fuel gas supplied from the fuel generating member.
  • a fuel cell system comprising a fuel generating member that generates a fuel gas by a chemical reaction, and a fuel cell unit that generates power by a reaction between an oxidant gas containing oxygen and a fuel gas supplied from the fuel generating member.
  • a fuel cell typically includes a solid polymer electrolyte membrane using a solid polymer ion exchange membrane, a solid oxide electrolyte membrane using yttria-stabilized zirconia (YSZ), a fuel electrode (anode) and an oxidizer electrode.
  • the one sandwiched from both sides by the (cathode) has a single cell configuration.
  • a fuel gas channel for supplying a fuel gas (for example, hydrogen) to the fuel electrode and an oxidant gas channel for supplying an oxidant gas (for example, oxygen or air) to the oxidant electrode are provided. Electric power is generated by supplying the fuel gas and the oxidant gas to the fuel electrode and the oxidant electrode, respectively.
  • Fuel cells are not only energy-saving because of the high efficiency of power energy that can be extracted in principle, but they are also a power generation system that is excellent in the environment, and are expected as a trump card for solving energy and environmental problems on a global scale.
  • Patent Documents 1 and 2 disclose a secondary battery type fuel cell system that combines a solid oxide fuel cell and a hydrogen generation member (iron) that generates hydrogen by an oxidation reaction and can be regenerated by a reduction reaction. It is disclosed.
  • the hydrogen generating member (iron) generates hydrogen by an oxidation reaction with water during the power generation operation of the system, and is oxidized during the charging operation of the system. Regenerated by a reduction reaction with hydrogen.
  • the secondary battery type fuel cell system disclosed in Patent Document 1 does not detect the ratio (remaining amount of iron) in which the hydrogen generating member is not oxidized, the remaining amount of iron is reduced.
  • over-discharge may occur if electricity is continuously supplied to the load.
  • overcharging may occur if charging continues even though iron oxide is reduced and the amount of remaining iron is increasing. If overdischarge or overcharge occurs, the solid oxide fuel cell may be deteriorated or damaged.
  • the secondary battery type fuel cell system disclosed in Patent Document 2 includes a weight measuring unit that measures the weight of an object to be measured, and a vibration that calculates the frequency component most emphasized in the output signal of the weight measuring unit.
  • the frequency calculation unit measures the weight of the measurement object. Then, the oxidation state of the hydrogen generating member is identified from the weight of the object to be measured, and the ratio (remaining amount of iron) in which the hydrogen generating member is not oxidized is determined from the identified oxidation state.
  • the weight measuring unit is the object to be measured.
  • the weight As the weight, the weight of the entire container including the solid oxide fuel cell and the hydrogen generating member is measured. Therefore, for example, when the ratio of the weight of the hydrogen generating member to the weight of the entire container is small, the change in the weight of the hydrogen generating member is small relative to the weight of the entire container, and there is a problem that the detection accuracy of the remaining amount of iron is lowered. .
  • the weight of the hydrogen generating member and the secondary battery type fuel cell system varies greatly depending on the use of the fuel cell system (portable fuel cell, household fuel cell cogeneration, power generation facility, etc.). If the weight of the solid oxide fuel cell is 10 kg, the total is 20 kg. On the other hand, the weight change due to the oxidation-reduction reaction of the hydrogen generating member becomes a slight change of several grams when the chemical reaction gradually progresses, and the change of several grams is accurately measured with a measuring instrument measuring 20 kg. It is difficult to do. In addition, the change in weight during power generation / charging is generated not only by the hydrogen generating member but also by the chemical reaction of the electrode on the solid oxide fuel cell side. Therefore, when the weight of the entire container including the solid oxide fuel cell and the hydrogen generating member is measured, factors other than the hydrogen generating member are included in the weight change, and the weight change of the hydrogen generating member alone is accurately measured. It becomes difficult to do.
  • Patent Document 3 discloses a hydrogen generation method capable of generating and storing hydrogen using oxidation / reduction of an iron material.
  • the state of oxidation / reduction of the iron material is calculated by cooling the water vapor generated by the reduction of the iron material into water and reading the total weight of the water.
  • the total flow rate of the generated hydrogen gas is calculated by reading with a flow meter.
  • the temperature of the piping is insufficient, water vapor is condensed outside the target place (water tank), and thus there is a problem that the total weight of the generated water cannot be measured accurately.
  • the flow meter is usually calibrated to show a correct value for a certain gas type and a certain gas composition, and does not show an accurate value when the composition of the passing gas changes. Therefore, for example, when the amount of reaction with water vapor changes depending on the remaining amount of iron material and the composition of the gas passing through the flow meter changes, there is a problem that the total flow rate of the generated hydrogen gas cannot be measured accurately.
  • an object of the present invention is to provide a fuel cell system capable of accurately detecting the oxidation state of a fuel generating member.
  • a fuel cell system comprises a fuel generating member that generates fuel gas by an oxidation reaction, an oxidant gas containing oxygen, and a fuel gas supplied from the fuel generating member. Gas is generated between a fuel cell unit that generates power, a first container that houses the fuel generation member, a second container that houses the fuel cell unit, and a fuel electrode of the fuel generation member and the fuel cell unit.
  • a pipe provided between the first container and the second container so as to circulate, A weight measuring unit for measuring the weight of the entire first container including the fuel generating member; and a detecting unit for detecting an oxidation state of the fuel generating member based on a measurement result of the weight measuring unit, wherein the pipe is
  • the first container A structure having a movable portion that moves in the direction of change of position.
  • the pipe since the pipe has the movable part that moves in the direction of change of the position of the first container, the first container corresponding to the weight change of the entire first container including the fuel generating member.
  • the change in position is not hindered by the piping.
  • the weight measuring unit measures the weight of the entire first container without being affected by the weight of the fuel cell unit or the second container, the ratio of the weight of the fuel generating member to the measurement result of the weight measuring unit is growing.
  • the weight of the fuel generating member can be accurately grasped. Therefore, it is possible to accurately detect the oxidation state of the fuel generating member based on the measurement result of the weight measuring unit.
  • FIG. 1 is a diagram showing a schematic configuration of a fuel cell system according to a first embodiment of the present invention. It is a figure which shows the fuel cell system which concerns on 1st Embodiment of this invention when the weight of a fuel generation member increases. It is a figure which shows the modification of the fuel cell system which concerns on 1st Embodiment of this invention. It is a figure which shows the other modification of the fuel cell system which concerns on 1st Embodiment of this invention. It is a figure which shows schematic structure of the fuel cell system which concerns on 2nd Embodiment of this invention. It is a figure which shows the fuel cell system which concerns on 2nd Embodiment of this invention when the weight of a fuel generation member increases. It is a figure which shows schematic structure of the fuel cell system which concerns on 3rd Embodiment of this invention. It is a figure which shows the fuel cell system which concerns on 3rd Embodiment of this invention when the weight of a fuel generation member increases.
  • FIG. 1 shows a schematic configuration of the fuel cell system according to the first embodiment of the present invention.
  • the fuel cell system according to the present embodiment includes a fuel generating member 1 that generates a fuel gas by an oxidation reaction, and a fuel cell that generates power by a reaction between an oxidant gas containing oxygen and a fuel gas supplied from the fuel generating member 1.
  • the pipe 5 has a bellows-like pipe 6 which is a movable part.
  • the pipe 5 is made of stainless steel including the bellows-like pipe 6.
  • the fuel cell system detects the oxidation state of the fuel generating member 1 based on the spring balance 7 that measures the weight of the entire container 3 including the fuel generating member 1 and the measurement result of the spring balance 7.
  • a detection unit 8 and a remaining amount indicator 9 are provided.
  • a heater for adjusting the temperature, a temperature sensor for detecting the temperature, or the like may be provided around the fuel generating member 1 or the fuel cell unit 2.
  • a pump, a blower or the like for forcibly flowing the gas is connected to the pipe 5, a pipe for supplying air as an oxidant gas to the oxidant electrode 2 ⁇ / b> C of the fuel cell unit 2, and an oxidant of the fuel cell unit 2 You may arrange
  • a pump, a blower or the like is provided between the bellows-like pipe 6 and the container 4 in order to avoid a pump or a blower being included in the measurement object of the spring balance 7. Is desirable.
  • the fuel generating member 1 for example, a fuel generating member made of a fine particle compressed body whose base material (main component) is iron can be used.
  • the fuel cell unit 2 has, for example, a MEA (Membrane Electrode Assembly) structure in which a solid electrolyte that transmits O 2 ⁇ is sandwiched and a fuel electrode and an oxidant electrode are formed on both sides.
  • MEA Membrane Electrode Assembly
  • FIG. 1 illustrates a structure in which only one MEA is provided, a plurality of MEAs may be provided, or a plurality of MEAs may be stacked.
  • a fuel generating member made of a fine particle compact whose base material (main component) is iron is used as the fuel generating member 1
  • a solid oxide fuel cell unit is used as the fuel cell unit 2
  • hydrogen is used as the fuel gas. The case where it is used will be described.
  • the fuel cell unit 2 is electrically connected to an external load (not shown) during power generation of the fuel cell system according to the present embodiment.
  • the following reaction (1) occurs at the fuel electrode 2B during power generation of the fuel cell system according to the present embodiment.
  • the fuel cell unit 2 performs a power generation operation. Further, as can be seen from the above equation (1), during the power generation operation of the fuel cell system according to the present embodiment, H 2 is consumed and H 2 O is generated on the fuel electrode 2B side.
  • the fuel generating member 1 consumes H 2 O generated on the fuel electrode 2B side of the fuel cell unit 2 during power generation of the fuel cell system according to the present embodiment by an oxidation reaction expressed by the following equation (4).
  • the fuel cell unit 2 When the fuel cell system according to this embodiment is charged, the fuel cell unit 2 is connected to an external power source (not shown).
  • an electrolysis reaction shown in the following equation (5) which is the reverse reaction of the above equation (3), occurs, and H 2 on the fuel electrode 2B side.
  • O is consumed and H 2 is generated, and the fuel generating member 1 undergoes a reduction reaction represented by the following equation (6), which is the reverse reaction of the oxidation reaction represented by the above equation (4).
  • H 2 produced on the 2B side is consumed and H 2 O is produced.
  • the fuel generating member 1 is oxidized by the oxidation reaction shown in the above formula (4) during power generation of the fuel cell system according to this embodiment, and the weight increases. For example, when 3 mol of Fe is oxidized to 1 mol of Fe 3 O 4 , the weight changes from about 168 g to about 232 g, and the weight increases by about 64 g. On the other hand, the fuel generating member 1 is reduced (regenerated) by the reduction reaction shown in the above equation (6) when the fuel cell system according to this embodiment is charged, and the weight is reduced.
  • the oxidation state of the fuel generating member 1 can be detected from the weight change of the fuel generating member 1. Since the battery remaining amount of the fuel cell system according to the present embodiment is determined by the amount of fuel gas that can be generated from the fuel generating member 1, the oxidation state of the fuel generating member 1 is the battery remaining amount of the fuel cell system according to the present embodiment. It becomes an indicator to show.
  • a method for detecting the oxidation state of the fuel generating member 1 there is a method for detecting based on the total power generation amount of the fuel cell unit 2, but this is an indirect measurement method, and the fuel generating member as in this embodiment. Measuring the weight change of 1 gives a more accurate result.
  • the spring balance 7 measures the weight of the entire container 3 including the fuel generation member 1, and the detection unit 8 determines the measurement result of the spring balance 7 and the oxidation state of the fuel generation member 1.
  • the oxidation state of the fuel generating member 1 is detected on the basis of the measurement result of the spring balance 7 using a data table indicating the relationship between the spring balance 7 and a calculation formula indicating the relationship between the measurement result of the spring balance 7 and the oxidation state of the fuel generating member 1 To do.
  • the detecting unit 8 determines that the ratio of oxidation of the fuel generating member 1 is equal to or greater than the threshold value, the detecting unit 8 turns on the remaining amount indicator 9 indicating that the remaining amount of iron in the fuel generating member 1 is small, and the fuel generating member 1 When it is determined that the oxidation ratio of 1 is less than the threshold, the remaining amount indicator 9 is turned off.
  • an LED or the like can be used as the remaining amount indicator 9.
  • the bellows-like pipe 6 moves in the direction of change of the position of the container 3. For example, when the weight of the fuel generating member 1 increases, as shown in FIG. 2, the position of the container 3 changes downward, and accordingly, the bellows-like pipe 6 also moves downward. For this reason, the change of the position of the container 3 according to the weight change of the whole container 3 including the fuel generating member 1 is not hindered by the pipe 5.
  • the spring balance 7 measures the weight of the entire container 3 without being affected by the weight of the fuel cell unit 2 or the container 4, the ratio of the weight of the fuel generating member 1 to the measurement result of the spring balance 7 is It becomes large, and even a slight change in weight can be accurately measured, and the change in weight of the fuel generating member can be accurately grasped. Therefore, the oxidation state of the fuel generating member 1 can be accurately detected based on the measurement result of the spring balance 7.
  • the spring balance 7 is installed on the lower side of the container 3. However, the spring balance 7 is installed on the upper side of the container 3 as shown in FIG. You may make it the form which hangs.
  • the spring balance 7 has the same structure as a general weight scale using a lever spring as disclosed in, for example, Japanese Patent Application Laid-Open No. 8-86686, for example, a measurement object installation surface of the spring balance 7 is used.
  • a measurement object installation surface of the spring balance 7 is used.
  • the weight of the entire container 3 including the fuel generating member 1 can be accurately measured.
  • the fuel generating member 1 and the fuel cell unit 2 are arranged side by side in the horizontal direction, but the fuel generating member 1 and the fuel cell unit 2 are arranged in the vertical direction. May be.
  • the container 4 is supported by a column 10, and the spring balance 7 is not affected by the weight of the fuel cell unit 2 or the container 4. What is necessary is just to enable it to measure the weight of the whole container 3 containing the generating member 1.
  • the bellows-like pipe 6 may be located at any position between the container 3 and the container 4, but the position closer to the container 3 is less affected by the weight of the pipe 5. The weight of the fuel generating material 1 can be measured more accurately. Further, when the movable part is near the container 3, it is easier to replace when the fuel generating member 1 is deteriorated.
  • the movable part is configured only in a part of the piping, but may be configured over a wider range of the piping, or may be configured in almost all of the piping. Also good.
  • the weight change of the fuel generating member 1 is accurately detected, Based on the result, the oxidation state of the fuel generating member 1 can be accurately detected.
  • a container 3 is not provided in the connection part of the pipe 5 and the container 3 instead of providing a movable part on the pipe 5 like this embodiment. It is also conceivable to provide a slide portion that can change the position according to the weight change. However, with this configuration, there is a high possibility that gas will flow out from the slide portion.
  • the gas flows out, the gas is mixed in from the outside, which leads to a decrease in power generation / charging efficiency.
  • the configuration of the present embodiment since the movable part on the pipe 5 is only deformed, it becomes easy to maintain the sealing property between the container 3 and the container 4, and the power generation / charging efficiency is maintained. be able to.
  • FIG. 5 shows a schematic configuration of a fuel cell system according to the second embodiment of the present invention.
  • the fuel cell system according to the present embodiment has the same configuration as that of the fuel cell system according to the first embodiment, except that a flexible resin pipe 11 is used as a movable part instead of the bellows-like pipe 6.
  • the resin pipe 11 moves in the direction of change of the position of the container 3. For example, when the weight of the fuel generating member 1 increases, as shown in FIG. 6, the position of the container 3 changes downward, and accordingly, the bellows-like pipe 6 also moves downward.
  • the fuel cell system according to the present embodiment can accurately detect the oxidation state of the fuel generating member 1 based on the measurement result of the spring balance 7 as in the fuel cell system according to the first embodiment.
  • the temperature of the resin pipe 11 is adjusted at the time of charging / discharging of the fuel cell system, considering that the resin pipe 11 has lower heat resistance than the metal pipe. From the viewpoint of heat resistance, about 200 ° C. or lower is preferable, and if the temperature becomes too low, water vapor may be condensed in the resin pipe 11, and therefore, about 120 ° C. or higher is preferable.
  • a cooler may be disposed in the pipe 11.
  • a material of piping if it is a flexible material, it will not be restricted to resin.
  • FIG. 7 shows a schematic configuration of the fuel cell system according to the third embodiment of the present invention.
  • the fuel cell system according to the present embodiment has the same configuration as that of the fuel cell system according to the first embodiment, except that the sliding joint 12 is used as a movable part instead of the bellows-like pipe 6.
  • the sliding joint 12 includes a stainless-made small-diameter pipe portion 12A, a stainless-steel large-diameter pipe portion 12B having a diameter larger than that of the small-diameter pipe portion 12A, and a packing 12C.
  • the small-diameter pipe portion 12A and the large-diameter pipe portion 12B include It is arranged on the same axis, and the packing 12C is fixed to the large-diameter pipe portion 12B and is provided in the gap between the small-diameter pipe portion 12A and the large-diameter pipe portion 12B. With such a configuration, the slip joint 12 can be expanded and contracted in the axial direction of the small-diameter pipe portion 12A and the large-diameter pipe portion 12B while ensuring gas sealing performance.
  • the sliding direction of the sliding joint 12 is one-dimensional, in the fuel cell system according to the present embodiment, the sliding direction of the sliding joint 12 is aligned with the direction of change of the container position. It moves in the direction of change of position. For example, when the weight of the fuel generating member 1 increases, as shown in FIG. 8, the position of the container 3 changes downward, and the slip joint 12 expands and moves downward accordingly.
  • the fuel cell system according to the present embodiment can accurately detect the oxidation state of the fuel generating member 1 based on the measurement result of the spring balance 7 as in the fuel cell system according to the first embodiment.
  • the temperature of the sliding joint 12 is adjusted during charging / discharging of the fuel cell system. From the viewpoint of heat resistance, about 200 ° C. or lower is preferable, and if the temperature is too low, water vapor may be condensed in the slip joint 12, and therefore, about 120 ° C. or higher is preferable. In temperature control, the same configuration as in the second embodiment can be considered.
  • the spring balance 7 is used as the weight measuring unit.
  • a weight sensor using a strain gauge may be used instead of the spring balance 7.
  • a solid oxide electrolyte is used as the electrolyte membrane 2A of the fuel cell unit 2, and water is generated on the fuel electrode 2B side during power generation. According to this configuration, water is generated on the side where the fuel generating member 1 is provided, which is advantageous for simplification and miniaturization of the apparatus.
  • a solid polymer electrolyte that allows hydrogen ions to pass through can be used as the electrolyte membrane 2A of the fuel cell unit 2.
  • a flow path for propagating this water to the fuel generation unit 1 may be provided.
  • a movable part similar to the movable part of the pipe 5 may be provided in the flow path for propagating water generated on the oxidant electrode 2 ⁇ / b> C side of the fuel cell part 2 to the fuel generation part 1.
  • one fuel cell unit 2 performs both power generation and water electrolysis.
  • a fuel cell for example, a solid oxide fuel cell dedicated to power generation
  • a water electrolyzer for example, water
  • a solid oxide fuel cell dedicated for electrolysis may be connected to the fuel generating member 1 in parallel on the gas flow path.
  • a movable part similar to the movable part of the pipe 5 may be provided also in the pipe provided between the container containing the water electrolyzer and the container 3 containing the fuel generating member 1.
  • the fuel gas of the fuel cell unit 2 is hydrogen, but a reducing gas other than hydrogen such as carbon monoxide or hydrocarbon may be used as the fuel gas of the fuel cell unit 2.
  • the pipe 5 may include both the bellows-like pipe 6 and the resin pipe 11.
  • the modifications described in the above embodiments may be applied to other embodiments as long as there is no contradiction.

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Abstract

This fuel cell system is provided with: a fuel generating member that generates fuel gas via an oxidation reaction; a fuel cell unit that generates power via a reaction between an oxidant gas containing oxygen and fuel gas supplied from the fuel generating member; a first container that accommodates the fuel generating member; a second container that accommodates the fuel cell unit; pipes that are disposed between the first container and the second container in such a manner that gas flows between the fuel generating member and a fuel electrode of the fuel cell unit; a weight measuring unit that measures the weight of the entire first container, including the fuel generating member, in association with changes in the position of the first container due to changes in the weight of the entire first container, including the fuel generating member; and a detection unit that detects the oxidation state of the fuel generating member on the basis of the measurement results of the weight measuring unit. The pipes have movable sections that are able to move in the position change direction of the first container.

Description

燃料電池システムFuel cell system
 本発明は、化学反応により燃料ガスを発生する燃料発生部材と、酸素を含む酸化剤ガスと前記燃料発生部材から供給される燃料ガスとの反応により発電を行う燃料電池部とを備える燃料電池システムに関する。 The present invention provides a fuel cell system comprising a fuel generating member that generates a fuel gas by a chemical reaction, and a fuel cell unit that generates power by a reaction between an oxidant gas containing oxygen and a fuel gas supplied from the fuel generating member. About.
 燃料電池は、典型的には、固体ポリマーイオン交換膜を用いた固体高分子電解質膜、イットリア安定化ジルコニア(YSZ)を用いた固体酸化物電解質膜等を、燃料極(アノード)と酸化剤極(カソード)とで両側から挟み込んだものを1つのセル構成としている。そして、燃料極に燃料ガス(例えば水素)を供給する燃料ガス流路と、酸化剤極に酸化剤ガス(例えば酸素や空気)を供給する酸化剤ガス流路とが設けられ、これらの流路を介して燃料ガス、酸化剤ガスがそれぞれ燃料極、酸化剤極に供給されることにより発電が行われる。 A fuel cell typically includes a solid polymer electrolyte membrane using a solid polymer ion exchange membrane, a solid oxide electrolyte membrane using yttria-stabilized zirconia (YSZ), a fuel electrode (anode) and an oxidizer electrode. The one sandwiched from both sides by the (cathode) has a single cell configuration. A fuel gas channel for supplying a fuel gas (for example, hydrogen) to the fuel electrode and an oxidant gas channel for supplying an oxidant gas (for example, oxygen or air) to the oxidant electrode are provided. Electric power is generated by supplying the fuel gas and the oxidant gas to the fuel electrode and the oxidant electrode, respectively.
 燃料電池は、原理的に取り出せる電力エネルギーの効率が高いため、省エネルギーになるだけでなく、環境に優れた発電方式であり、地球規模でのエネルギーや環境問題解決の切り札として期待されている。 Fuel cells are not only energy-saving because of the high efficiency of power energy that can be extracted in principle, but they are also a power generation system that is excellent in the environment, and are expected as a trump card for solving energy and environmental problems on a global scale.
特表平11-501448号公報Japanese National Patent Publication No. 11-501448 特開2012―47693号公報JP 2012-47693 A 特開2008―150256号公報JP 2008-150256 A
 特許文献1及び特許文献2には、固体酸化物型燃料電池と、酸化反応により水素を発生し、還元反応により再生可能な水素発生部材(鉄)とを組み合わせた2次電池型燃料電池システムが開示されている。上記2次電池型燃料電池システムでは、システムの発電動作時に水素発生部材(鉄)が水との酸化反応により水素を発生し、システムの充電動作時に酸化している水素発生部材(酸化鉄)が水素との還元反応により再生される。 Patent Documents 1 and 2 disclose a secondary battery type fuel cell system that combines a solid oxide fuel cell and a hydrogen generation member (iron) that generates hydrogen by an oxidation reaction and can be regenerated by a reduction reaction. It is disclosed. In the above secondary battery type fuel cell system, the hydrogen generating member (iron) generates hydrogen by an oxidation reaction with water during the power generation operation of the system, and is oxidized during the charging operation of the system. Regenerated by a reduction reaction with hydrogen.
 しかしながら、特許文献1で開示されている2次電池型燃料電池システムは、水素発生部材の酸化反応をしていない割合(鉄の残量)を検知していないため、鉄の残量が少なくなっているにも拘わらず負荷に電気を供給し続ければ過放電が起こる場合がある。また、酸化鉄が還元され鉄残量が増えているにも拘わらず充電を続ければ過充電が起こる場合がある。過放電や過充電が起こると、固体酸化物型燃料電池が劣化したり、破損したりすることがある。 However, since the secondary battery type fuel cell system disclosed in Patent Document 1 does not detect the ratio (remaining amount of iron) in which the hydrogen generating member is not oxidized, the remaining amount of iron is reduced. However, over-discharge may occur if electricity is continuously supplied to the load. In addition, overcharging may occur if charging continues even though iron oxide is reduced and the amount of remaining iron is increasing. If overdischarge or overcharge occurs, the solid oxide fuel cell may be deteriorated or damaged.
 また、特許文献2で開示されている2次電池型燃料電池システムは、測定対象物の重量を測定する重量測定部と、重量測定部の出力信号において最も強調されている周波数成分を演算する振動周波数演算部とによって、測定対象物の重量を測定している。そして、測定対象物の重量から水素発生部材の酸化状態が同定され、その同定された酸化状態から水素発生部材の酸化反応をしていない割合(鉄の残量)が求まる。 In addition, the secondary battery type fuel cell system disclosed in Patent Document 2 includes a weight measuring unit that measures the weight of an object to be measured, and a vibration that calculates the frequency component most emphasized in the output signal of the weight measuring unit. The frequency calculation unit measures the weight of the measurement object. Then, the oxidation state of the hydrogen generating member is identified from the weight of the object to be measured, and the ratio (remaining amount of iron) in which the hydrogen generating member is not oxidized is determined from the identified oxidation state.
 しかしながら、特許文献2で開示されている2次電池型燃料電池システムは、固体酸化物型燃料電池と水素発生部材とが一体的に配置される構成であるため、重量測定部は測定対象物の重量として、固体酸化物型燃料電池や水素発生部材等を含む容器全体の重量を測定している。したがって、例えば容器全体の重量に対する水素発生部材の重量の比率が小さい場合、水素発生部材の重量変化は容器全体の重量に対して僅かとなり、鉄の残量の検出精度が低くなるという課題がある。ここで、水素発生部材および2次電池型燃料電池システムの重量は、燃料電池システムの用途(ポータブル燃料電池、家庭用燃料電池コージェネレーション、発電施設など)によって大きく変わるが、仮に、水素発生部材を10kg、固体酸化物型燃料電池の重量を10kgとした場合、全体として20kgとなる。一方、水素発生部材の酸化還元反応による重量変化は、徐々に化学反応が進んだ場合、数グラム単位の僅かな変化となり、20kgの重量を測定する計量器において数グラム単位の変化を精度よく測定することは困難である。また、発電・充電時における重量変化は、水素発生部材だけでなく、固体酸化物型燃料電池側においても電極が化学反応をすることによって発生する。そのため、固体酸化物型燃料電池や水素発生部材等を含む容器全体の重量を測定すると、水素発生部材以外に重量変化する要因が含まれることになり、水素発生部材単体の重量変化を精度よく測定することが困難になる。 However, since the secondary battery type fuel cell system disclosed in Patent Document 2 has a configuration in which the solid oxide fuel cell and the hydrogen generating member are integrally disposed, the weight measuring unit is the object to be measured. As the weight, the weight of the entire container including the solid oxide fuel cell and the hydrogen generating member is measured. Therefore, for example, when the ratio of the weight of the hydrogen generating member to the weight of the entire container is small, the change in the weight of the hydrogen generating member is small relative to the weight of the entire container, and there is a problem that the detection accuracy of the remaining amount of iron is lowered. . Here, the weight of the hydrogen generating member and the secondary battery type fuel cell system varies greatly depending on the use of the fuel cell system (portable fuel cell, household fuel cell cogeneration, power generation facility, etc.). If the weight of the solid oxide fuel cell is 10 kg, the total is 20 kg. On the other hand, the weight change due to the oxidation-reduction reaction of the hydrogen generating member becomes a slight change of several grams when the chemical reaction gradually progresses, and the change of several grams is accurately measured with a measuring instrument measuring 20 kg. It is difficult to do. In addition, the change in weight during power generation / charging is generated not only by the hydrogen generating member but also by the chemical reaction of the electrode on the solid oxide fuel cell side. Therefore, when the weight of the entire container including the solid oxide fuel cell and the hydrogen generating member is measured, factors other than the hydrogen generating member are included in the weight change, and the weight change of the hydrogen generating member alone is accurately measured. It becomes difficult to do.
 さらに、特許文献3では鉄材の酸化・還元を利用して水素発生と貯蔵とが可能である水素発生方法が開示されている。鉄材の酸化・還元の状態は、還元工程では、鉄材の還元によって発生した水蒸気を冷却して水にし、水の総重量を読み取って算出している。また、酸化工程では、発生した水素ガスの総流量を流量計で読み取って算出している。しかしながら、還元工程では、配管の保温が不十分であると水蒸気が目的の場所(水タンク)以外で結露するため、発生した水の総重量が正確に測定できないという課題がある。また、酸化工程では、流量計は通常、あるガス種、あるガス組成で正しい値を示すように校正されており、通過するガスの組成が変わると正確な値を示さない。したがって、例えば鉄材の残量によって水蒸気との反応量が変わり、流量計を通過するガスの組成が変わると、発生した水素ガスの総流量を正確に測定できないという課題がある。 Furthermore, Patent Document 3 discloses a hydrogen generation method capable of generating and storing hydrogen using oxidation / reduction of an iron material. In the reduction process, the state of oxidation / reduction of the iron material is calculated by cooling the water vapor generated by the reduction of the iron material into water and reading the total weight of the water. In the oxidation step, the total flow rate of the generated hydrogen gas is calculated by reading with a flow meter. However, in the reduction process, if the temperature of the piping is insufficient, water vapor is condensed outside the target place (water tank), and thus there is a problem that the total weight of the generated water cannot be measured accurately. In the oxidation process, the flow meter is usually calibrated to show a correct value for a certain gas type and a certain gas composition, and does not show an accurate value when the composition of the passing gas changes. Therefore, for example, when the amount of reaction with water vapor changes depending on the remaining amount of iron material and the composition of the gas passing through the flow meter changes, there is a problem that the total flow rate of the generated hydrogen gas cannot be measured accurately.
 本発明は、上記の状況に鑑み、燃料発生部材の酸化状態を精度良く検出することができる燃料電池システムを提供することを目的とする。 In view of the above situation, an object of the present invention is to provide a fuel cell system capable of accurately detecting the oxidation state of a fuel generating member.
 上記目的を達成するために本発明に係る燃料電池システムは、酸化反応により燃料ガスを発生する燃料発生部材と、酸素を含む酸化剤ガスと前記燃料発生部材から供給される燃料ガスとの反応により発電を行う燃料電池部と、前記燃料発生部材を収容する第1容器と、前記燃料電池部を収容する第2容器と、前記燃料発生部材と前記燃料電池部の燃料極との間でガスが流通するように前記第1容器と前記第2容器の間に設けられる配管と、前記燃料発生部材を含む前記第1容器全体の重量変化に応じた前記第1容器の位置の変化に基づき、前記燃料発生部材を含む前記第1容器全体の重量を測定する重量測定部と、前記重量測定部の測定結果に基づいて前記燃料発生部材の酸化状態を検出する検出部と、を備え、前記配管が、前記第1容器の位置の変化方向に可動する可動部を有する構成とする。 In order to achieve the above object, a fuel cell system according to the present invention comprises a fuel generating member that generates fuel gas by an oxidation reaction, an oxidant gas containing oxygen, and a fuel gas supplied from the fuel generating member. Gas is generated between a fuel cell unit that generates power, a first container that houses the fuel generation member, a second container that houses the fuel cell unit, and a fuel electrode of the fuel generation member and the fuel cell unit. Based on a change in the position of the first container in accordance with a weight change of the entire first container including the fuel generation member, a pipe provided between the first container and the second container so as to circulate, A weight measuring unit for measuring the weight of the entire first container including the fuel generating member; and a detecting unit for detecting an oxidation state of the fuel generating member based on a measurement result of the weight measuring unit, wherein the pipe is The first container A structure having a movable portion that moves in the direction of change of position.
 本発明に係る燃料電池システムによると、配管が第1容器の位置の変化方向に可動する可動部を有しているので、燃料発生部材を含む第1容器全体の重量変化に応じた第1容器の位置の変化が配管によって妨げられない。また、重量測定部が、燃料電池部や第2容器の重量の影響を受けずに第1容器全体の重量を測定しているので、重量測定部の測定結果に対する燃料発生部材の重量の比率が大きくなる。これらにより、燃料発生部材の重量を正確に把握することが可能となる。したがって、重量測定部の測定結果に基づいて燃料発生部材の酸化状態を精度良く検出することができる。 According to the fuel cell system of the present invention, since the pipe has the movable part that moves in the direction of change of the position of the first container, the first container corresponding to the weight change of the entire first container including the fuel generating member. The change in position is not hindered by the piping. Further, since the weight measuring unit measures the weight of the entire first container without being affected by the weight of the fuel cell unit or the second container, the ratio of the weight of the fuel generating member to the measurement result of the weight measuring unit is growing. Thus, the weight of the fuel generating member can be accurately grasped. Therefore, it is possible to accurately detect the oxidation state of the fuel generating member based on the measurement result of the weight measuring unit.
本発明の第1実施形態に係る燃料電池システムの概略構成を示す図である。1 is a diagram showing a schematic configuration of a fuel cell system according to a first embodiment of the present invention. 燃料発生部材の重量が増加した場合の本発明の第1実施形態に係る燃料電池システムを示す図である。It is a figure which shows the fuel cell system which concerns on 1st Embodiment of this invention when the weight of a fuel generation member increases. 本発明の第1実施形態に係る燃料電池システムの変形例を示す図である。It is a figure which shows the modification of the fuel cell system which concerns on 1st Embodiment of this invention. 本発明の第1実施形態に係る燃料電池システムの他の変形例を示す図である。It is a figure which shows the other modification of the fuel cell system which concerns on 1st Embodiment of this invention. 本発明の第2実施形態に係る燃料電池システムの概略構成を示す図である。It is a figure which shows schematic structure of the fuel cell system which concerns on 2nd Embodiment of this invention. 燃料発生部材の重量が増加した場合の本発明の第2実施形態に係る燃料電池システムを示す図である。It is a figure which shows the fuel cell system which concerns on 2nd Embodiment of this invention when the weight of a fuel generation member increases. 本発明の第3実施形態に係る燃料電池システムの概略構成を示す図である。It is a figure which shows schematic structure of the fuel cell system which concerns on 3rd Embodiment of this invention. 燃料発生部材の重量が増加した場合の本発明の第3実施形態に係る燃料電池システムを示す図である。It is a figure which shows the fuel cell system which concerns on 3rd Embodiment of this invention when the weight of a fuel generation member increases.
 本発明の実施形態について図面を参照して以下に説明する。なお、本発明は、後述する実施形態に限られない。 Embodiments of the present invention will be described below with reference to the drawings. In addition, this invention is not restricted to embodiment mentioned later.
<第1実施形態>
 本発明の第1実施形態に係る燃料電池システムの概略構成を図1に示す。本実施形態に係る燃料電池システムは、酸化反応により燃料ガスを発生する燃料発生部材1と、酸素を含む酸化剤ガスと燃料発生部材1から供給される燃料ガスとの反応により発電を行う燃料電池部2と、燃料発生部材1を収容する容器3と、燃料電池部2を収容する容器4と、燃料発生部材1と燃料電池部2の燃料極2Bとの間でガスが流通するように容器3と容器4の間に設けられる配管5とを備えている。
<First Embodiment>
FIG. 1 shows a schematic configuration of the fuel cell system according to the first embodiment of the present invention. The fuel cell system according to the present embodiment includes a fuel generating member 1 that generates a fuel gas by an oxidation reaction, and a fuel cell that generates power by a reaction between an oxidant gas containing oxygen and a fuel gas supplied from the fuel generating member 1. A container 2 for housing the fuel generating member 1, a container 4 for housing the fuel cell unit 2, and a container so that gas flows between the fuel generating member 1 and the fuel electrode 2 B of the fuel cell unit 2. 3 and a pipe 5 provided between the containers 4.
 また、配管5は、可動部である蛇腹状の配管6を有している。本実施形態では、配管5は、蛇腹状の配管6を含めてステンレス製である。 Also, the pipe 5 has a bellows-like pipe 6 which is a movable part. In the present embodiment, the pipe 5 is made of stainless steel including the bellows-like pipe 6.
 また、本実施形態に係る燃料電池システムは、燃料発生部材1を含む容器3全体の重量を測定するバネ秤7と、バネ秤7の測定結果に基づいて燃料発生部材1の酸化状態を検出する検出部8と、残量表示器9とを備えている。 In addition, the fuel cell system according to the present embodiment detects the oxidation state of the fuel generating member 1 based on the spring balance 7 that measures the weight of the entire container 3 including the fuel generating member 1 and the measurement result of the spring balance 7. A detection unit 8 and a remaining amount indicator 9 are provided.
 なお、必要に応じて、燃料発生部材1や燃料電池部2の周辺に温度を調節するヒーターや温度を検出する温度センサ等を設けてもよい。また、ガスを強制的に流動させるためのポンプやブロア等を、配管5、燃料電池部2の酸化剤極2Cに酸化剤ガスである空気を供給するための配管、燃料電池部2の酸化剤極2Cからガスを排出するための配管に配置してもよい。配管5に配置する場合には、バネ秤7の測定対象物にポンプやブロア等が含まれることを回避するために、ポンプやブロア等を蛇腹状の配管6と容器4との間に設けることが望ましい。 If necessary, a heater for adjusting the temperature, a temperature sensor for detecting the temperature, or the like may be provided around the fuel generating member 1 or the fuel cell unit 2. Further, a pump, a blower or the like for forcibly flowing the gas is connected to the pipe 5, a pipe for supplying air as an oxidant gas to the oxidant electrode 2 </ b> C of the fuel cell unit 2, and an oxidant of the fuel cell unit 2 You may arrange | position to piping for discharging | emitting gas from the pole 2C. When arranged in the pipe 5, a pump, a blower or the like is provided between the bellows-like pipe 6 and the container 4 in order to avoid a pump or a blower being included in the measurement object of the spring balance 7. Is desirable.
 燃料発生部材1としては、例えば、基材料(主成分)が鉄である微粒子圧縮体からなる燃料発生部材を用いることができる。また、燃料電池部2としては、例えば、O2-を透過する固体電解質を挟み、両側にそれぞれ燃料極と酸化剤極が形成されているMEA(Membrane Electrode  Assembly;膜・電極接合体)構造をなす固体酸化物燃料電池部を用いることができる。なお、図1では、MEAを1つだけ設けた構造を図示しているが、MEAを複数設けたり、さらに複数のMEAを積層構造にしたりしてもよい。 As the fuel generating member 1, for example, a fuel generating member made of a fine particle compressed body whose base material (main component) is iron can be used. The fuel cell unit 2 has, for example, a MEA (Membrane Electrode Assembly) structure in which a solid electrolyte that transmits O 2− is sandwiched and a fuel electrode and an oxidant electrode are formed on both sides. A solid oxide fuel cell unit can be used. Although FIG. 1 illustrates a structure in which only one MEA is provided, a plurality of MEAs may be provided, or a plurality of MEAs may be stacked.
 以下の説明では、燃料発生部材1として基材料(主成分)が鉄である微粒子圧縮体からなる燃料発生部材を用い、燃料電池部2として固体酸化物燃料電池部を用い、燃料ガスとして水素を用いた場合について説明する。 In the following description, a fuel generating member made of a fine particle compact whose base material (main component) is iron is used as the fuel generating member 1, a solid oxide fuel cell unit is used as the fuel cell unit 2, and hydrogen is used as the fuel gas. The case where it is used will be described.
 本実施形態に係る燃料電池システムの発電時に燃料電池部2は外部負荷(不図示)に電気的に接続される。燃料電池部2では、本実施形態に係る燃料電池システムの発電時に、燃料極2Bにおいて下記の(1)式の反応が起こる。
 H2+O2-→H2O+2e- …(1)
The fuel cell unit 2 is electrically connected to an external load (not shown) during power generation of the fuel cell system according to the present embodiment. In the fuel cell unit 2, the following reaction (1) occurs at the fuel electrode 2B during power generation of the fuel cell system according to the present embodiment.
H 2 + O 2− → H 2 O + 2e (1)
 上記の(1)式の反応によって生成された電子は、外部負荷(不図示)を通って、酸化剤極2Cに到達し、酸化剤極2Cにおいて下記の(2)式の反応が起こる。
 1/2O2+2e-→O2- …(2)
The electrons generated by the reaction of the above formula (1) pass through an external load (not shown) and reach the oxidant electrode 2C, and the reaction of the following formula (2) occurs at the oxidant electrode 2C.
1 / 2O 2 + 2e → O 2− (2)
 そして、上記の(2)式の反応によって生成された酸素イオンは、固体電解質2Aを通って、燃料極2Bに到達する。上記の一連の反応を繰り返すことにより、燃料電池部2が発電動作を行うことになる。また、上記の(1)式から分かるように、本実施形態に係る燃料電池システムの発電動作時には、燃料極2B側においてH2が消費されH2Oが生成されることになる。 And the oxygen ion produced | generated by reaction of said (2) Formula passes through the solid electrolyte 2A, and arrives at the fuel electrode 2B. By repeating the above series of reactions, the fuel cell unit 2 performs a power generation operation. Further, as can be seen from the above equation (1), during the power generation operation of the fuel cell system according to the present embodiment, H 2 is consumed and H 2 O is generated on the fuel electrode 2B side.
 上記の(1)式及び(2)式より、本実施形態に係る燃料電池システムの発電動作時における燃料電池部2での反応は下記の(3)式の通りになる。
 H2+1/2O2→H2O …(3)
From the above formulas (1) and (2), the reaction in the fuel cell unit 2 during the power generation operation of the fuel cell system according to the present embodiment is as shown in the following formula (3).
H 2 + 1 / 2O 2 → H 2 O (3)
 一方、燃料発生部材1は、下記の(4)式に示す酸化反応により、本実施形態に係る燃料電池システムの発電時に燃料電池部2の燃料極2B側で生成されたH2Oを消費してH2を生成する。
 3Fe+4H2O→Fe34+4H2 …(4)
On the other hand, the fuel generating member 1 consumes H 2 O generated on the fuel electrode 2B side of the fuel cell unit 2 during power generation of the fuel cell system according to the present embodiment by an oxidation reaction expressed by the following equation (4). To produce H 2 .
3Fe + 4H 2 O → Fe 3 O 4 + 4H 2 (4)
 上記の(4)式に示す鉄の酸化反応が進むと、鉄から酸化鉄への変化が進んで鉄の残量が減っていくが、上記の(4)式の逆反応(還元反応)により、燃料発生部材1を再生することができ、本実施形態に係る燃料電池システムを充電することができる。 When the oxidation reaction of iron shown in the above equation (4) proceeds, the change from iron to iron oxide proceeds and the remaining amount of iron decreases, but by the reverse reaction (reduction reaction) of the above equation (4) The fuel generating member 1 can be regenerated, and the fuel cell system according to this embodiment can be charged.
 本実施形態に係る燃料電池システムの充電時に燃料電池部2は外部電源(不図示)に接続される。燃料電池部2では、本実施形態に係る燃料電池システムの充電時に、上記の(3)式の逆反応である下記の(5)式に示す電気分解反応が起こり、燃料極2B側においてH2Oが消費されH2が生成され、燃料発生部材1では、上記の(4)式に示す酸化反応の逆反応である下記(6)式に示す還元反応が起こり、燃料電池部2の燃料極2B側で生成されたH2が消費されH2Oが生成される。
 H2O→H2+1/2O2 …(5)
 Fe34+4H2→3Fe+4H2O …(6)
When the fuel cell system according to this embodiment is charged, the fuel cell unit 2 is connected to an external power source (not shown). In the fuel cell unit 2, when the fuel cell system according to the present embodiment is charged, an electrolysis reaction shown in the following equation (5), which is the reverse reaction of the above equation (3), occurs, and H 2 on the fuel electrode 2B side. O is consumed and H 2 is generated, and the fuel generating member 1 undergoes a reduction reaction represented by the following equation (6), which is the reverse reaction of the oxidation reaction represented by the above equation (4). H 2 produced on the 2B side is consumed and H 2 O is produced.
H 2 O → H 2 + 1 / 2O 2 (5)
Fe 3 O 4 + 4H 2 → 3Fe + 4H 2 O (6)
 燃料発生部材1は、本実施形態に係る燃料電池システムの発電時に上記の(4)式に示す酸化反応によって酸化され、重量が増加する。例えば3molのFeが酸化されて1molのFe34になると、重量は約168gから約232gに変化し、約64g重量が増加する。一方、燃料発生部材1は、本実施形態に係る燃料電池システムの充電時に上記の(6)式に示す還元反応によって還元(再生)され、重量が減少する。 The fuel generating member 1 is oxidized by the oxidation reaction shown in the above formula (4) during power generation of the fuel cell system according to this embodiment, and the weight increases. For example, when 3 mol of Fe is oxidized to 1 mol of Fe 3 O 4 , the weight changes from about 168 g to about 232 g, and the weight increases by about 64 g. On the other hand, the fuel generating member 1 is reduced (regenerated) by the reduction reaction shown in the above equation (6) when the fuel cell system according to this embodiment is charged, and the weight is reduced.
 したがって、燃料発生部材1の重量変化から燃料発生部材1の酸化状態を検出することができる。本実施形態に係る燃料電池システムの電池残量は燃料発生部材1から発生可能な燃料ガスの量によって決まるため、燃料発生部材1の酸化状態は本実施形態に係る燃料電池システムの電池残量を示す指標となる。尚、燃料発生部材1の酸化状態を検出する方法としては、燃料電池部2の総発電量に基づき検出する方法があるが、間接的な測定方法であり、本実施形態のように燃料発生部材1の重量変化を測定する方が、より精度が高い結果が得られる。 Therefore, the oxidation state of the fuel generating member 1 can be detected from the weight change of the fuel generating member 1. Since the battery remaining amount of the fuel cell system according to the present embodiment is determined by the amount of fuel gas that can be generated from the fuel generating member 1, the oxidation state of the fuel generating member 1 is the battery remaining amount of the fuel cell system according to the present embodiment. It becomes an indicator to show. In addition, as a method for detecting the oxidation state of the fuel generating member 1, there is a method for detecting based on the total power generation amount of the fuel cell unit 2, but this is an indirect measurement method, and the fuel generating member as in this embodiment. Measuring the weight change of 1 gives a more accurate result.
 本実施形態に係る燃料電池システムでは、バネ秤7が、燃料発生部材1を含む容器3全体の重量を測定し、検出部8が、バネ秤7の測定結果と燃料発生部材1の酸化状態との関係を示すデータテーブルまたはバネ秤7の測定結果と燃料発生部材1の酸化状態との関係を示す計算式を用いて、バネ秤7の測定結果に基づいて燃料発生部材1の酸化状態を検出する。検出部8は、燃料発生部材1の酸化している割合が閾値以上であると判断した場合、燃料発生部材1の鉄残量が少ないことを示す残量表示器9をONにし、燃料発生部材1の酸化している割合が閾値未満であると判断した場合、残量表示器9をOFFにする。残量表示器9としては例えばLEDなどを用いることができる。 In the fuel cell system according to the present embodiment, the spring balance 7 measures the weight of the entire container 3 including the fuel generation member 1, and the detection unit 8 determines the measurement result of the spring balance 7 and the oxidation state of the fuel generation member 1. The oxidation state of the fuel generating member 1 is detected on the basis of the measurement result of the spring balance 7 using a data table indicating the relationship between the spring balance 7 and a calculation formula indicating the relationship between the measurement result of the spring balance 7 and the oxidation state of the fuel generating member 1 To do. When the detection unit 8 determines that the ratio of oxidation of the fuel generating member 1 is equal to or greater than the threshold value, the detecting unit 8 turns on the remaining amount indicator 9 indicating that the remaining amount of iron in the fuel generating member 1 is small, and the fuel generating member 1 When it is determined that the oxidation ratio of 1 is less than the threshold, the remaining amount indicator 9 is turned off. For example, an LED or the like can be used as the remaining amount indicator 9.
 本実施形態に係る燃料電池システムでは、蛇腹状の配管6が容器3の位置の変化方向に可動する。例えば、燃料発生部材1の重量が増加すると、図2に示すように、容器3の位置は下方に変化し、それに伴い蛇腹状の配管6も下方に可動する。このため、燃料発生部材1を含む容器3全体の重量変化に応じた容器3の位置の変化が配管5によって妨げられない。また、バネ秤7が、燃料電池部2や容器4の重量の影響を受けずに容器3全体の重量を測定しているので、バネ秤7の測定結果に対する燃料発生部材1の重量の比率が大きくなり、僅かな重量変化でも精度よく測定することができ、燃料発生部材の重量変化を正確に把握することが可能となる。したがって、バネ秤7の測定結果に基づいて燃料発生部材1の酸化状態を精度良く検出することができる。 In the fuel cell system according to the present embodiment, the bellows-like pipe 6 moves in the direction of change of the position of the container 3. For example, when the weight of the fuel generating member 1 increases, as shown in FIG. 2, the position of the container 3 changes downward, and accordingly, the bellows-like pipe 6 also moves downward. For this reason, the change of the position of the container 3 according to the weight change of the whole container 3 including the fuel generating member 1 is not hindered by the pipe 5. Further, since the spring balance 7 measures the weight of the entire container 3 without being affected by the weight of the fuel cell unit 2 or the container 4, the ratio of the weight of the fuel generating member 1 to the measurement result of the spring balance 7 is It becomes large, and even a slight change in weight can be accurately measured, and the change in weight of the fuel generating member can be accurately grasped. Therefore, the oxidation state of the fuel generating member 1 can be accurately detected based on the measurement result of the spring balance 7.
 なお、図1および図2に示した構成ではバネ秤7を容器3の下側に設置したが、図3に示すようにバネ秤7を容器3の上側に設置しバネ秤7で容器3を吊るような形態にしてもよい。 1 and 2, the spring balance 7 is installed on the lower side of the container 3. However, the spring balance 7 is installed on the upper side of the container 3 as shown in FIG. You may make it the form which hangs.
 また、バネ秤7を、例えば特開平8-86686号公報に開示されているような、てことバネを用いた一般的な体重計と同様の構造にすると、例えばバネ秤7の測定物設置面に対して測定物である容器3が傾いて設置された場合でも燃料発生部材1を含む容器3全体の重量を正確に測定することができる。 Further, when the spring balance 7 has the same structure as a general weight scale using a lever spring as disclosed in, for example, Japanese Patent Application Laid-Open No. 8-86686, for example, a measurement object installation surface of the spring balance 7 is used. However, even when the container 3 as the measurement object is installed at an inclination, the weight of the entire container 3 including the fuel generating member 1 can be accurately measured.
 また、図1~図3に示した構成では燃料発生部材1と燃料電池部2とを水平方向に並べて配置しているが、燃料発生部材1と燃料電池部2とを垂直方向に並べて配置してもよい。垂直方向に並べて配置する場合は、例えば図4に示すように容器4を支柱10で支える等の構成にして、バネ秤7が、燃料電池部2や容器4の重量の影響を受けずに燃料発生部材1を含む容器3全体の重量を測定できるようにすればよい。ここで、蛇腹状の配管6(可動部)は容器3と容器4との間のどの位置にあってもよいが、容器3に近い位置にある方が、配管5の重量の影響を受けにくく、燃料発生材1の重量をより正確に測定することができる。また可動部が容器3の近くにある方が、燃料発生部材1が劣化した場合の交換がしやすい。 1 to 3, the fuel generating member 1 and the fuel cell unit 2 are arranged side by side in the horizontal direction, but the fuel generating member 1 and the fuel cell unit 2 are arranged in the vertical direction. May be. In the case where they are arranged side by side in the vertical direction, for example, as shown in FIG. 4, the container 4 is supported by a column 10, and the spring balance 7 is not affected by the weight of the fuel cell unit 2 or the container 4. What is necessary is just to enable it to measure the weight of the whole container 3 containing the generating member 1. FIG. Here, the bellows-like pipe 6 (movable part) may be located at any position between the container 3 and the container 4, but the position closer to the container 3 is less affected by the weight of the pipe 5. The weight of the fuel generating material 1 can be measured more accurately. Further, when the movable part is near the container 3, it is easier to replace when the fuel generating member 1 is deteriorated.
 また、図1~図4に示した構成では、可動部は配管の一部のみに構成されているが、配管のより広範囲にわたって構成されていてもよく、あるいは配管の殆ど全てに構成されていてもよい。 In addition, in the configurations shown in FIGS. 1 to 4, the movable part is configured only in a part of the piping, but may be configured over a wider range of the piping, or may be configured in almost all of the piping. Also good.
 以上のように、本実施形態において、容器3と容器4との間にガス流路を形成する配管5上に可動部を形成することにより、燃料発生部材1の重量変化を精度よく検出し、その結果に基づき、燃料発生部材1の酸化状態を精度よく検出することができる。尚、容器3のみの重量変化をその位置変化によって測定する構成としては、本実施形態のように配管5上に可動部を設けるのではなく、配管5と容器3との接続部において、容器3の重量変化に伴う位置変化を可能とするスライド部を設けることも考えられる。しかしながら、この構成であると、スライド部からガスが外部へ流出する可能性が高くなる。ガスが流出した場合、その分、外部から気体が混入することになり、発電・充電効率の低下につながる。一方、本実施形態の構成によると、配管5上の可動部が変形するだけであるので、容器3と容器4との間の密閉性を保つことが容易になり、発電・充電効率を維持することができる。 As described above, in this embodiment, by forming the movable part on the pipe 5 that forms the gas flow path between the container 3 and the container 4, the weight change of the fuel generating member 1 is accurately detected, Based on the result, the oxidation state of the fuel generating member 1 can be accurately detected. In addition, as a structure which measures the weight change of only the container 3 by the position change, a container 3 is not provided in the connection part of the pipe 5 and the container 3 instead of providing a movable part on the pipe 5 like this embodiment. It is also conceivable to provide a slide portion that can change the position according to the weight change. However, with this configuration, there is a high possibility that gas will flow out from the slide portion. When the gas flows out, the gas is mixed in from the outside, which leads to a decrease in power generation / charging efficiency. On the other hand, according to the configuration of the present embodiment, since the movable part on the pipe 5 is only deformed, it becomes easy to maintain the sealing property between the container 3 and the container 4, and the power generation / charging efficiency is maintained. be able to.
<第2実施形態>
 本発明の第2実施形態に係る燃料電池システムの概略構成を図5に示す。本実施形態に係る燃料電池システムは、蛇腹状の配管6の代わりにフレキシブルな樹脂配管11を可動部として用いている以外は第1実施形態に係る燃料電池システムと同様の構成である。
Second Embodiment
FIG. 5 shows a schematic configuration of a fuel cell system according to the second embodiment of the present invention. The fuel cell system according to the present embodiment has the same configuration as that of the fuel cell system according to the first embodiment, except that a flexible resin pipe 11 is used as a movable part instead of the bellows-like pipe 6.
 本実施形態に係る燃料電池システムでは、樹脂配管11が容器3の位置の変化方向に可動する。例えば、燃料発生部材1の重量が増加すると、図6に示すように、容器3の位置は下方に変化し、それに伴い蛇腹状の配管6も下方に可動する。 In the fuel cell system according to the present embodiment, the resin pipe 11 moves in the direction of change of the position of the container 3. For example, when the weight of the fuel generating member 1 increases, as shown in FIG. 6, the position of the container 3 changes downward, and accordingly, the bellows-like pipe 6 also moves downward.
 したがって、本実施形態に係る燃料電池システムは、第1実施形態に係る燃料電池システムと同様に、バネ秤7の測定結果に基づいて燃料発生部材1の酸化状態を精度良く検出することができる。 Therefore, the fuel cell system according to the present embodiment can accurately detect the oxidation state of the fuel generating member 1 based on the measurement result of the spring balance 7 as in the fuel cell system according to the first embodiment.
 なお、本実施形態では、樹脂配管11が金属製配管に比べて耐熱性が低いことを考慮して、燃料電池システムの充放電時に樹脂配管11の温度を調節する。耐熱性の観点からは200℃程度以下が好ましく、また低温になりすぎると、樹脂配管11内で水蒸気が結露する可能性があるため、120℃程度以上が好ましい。例えば、ヒーターで加熱するのは燃料発生部材1と燃料電池部2のみとし樹脂配管11の部分は熱の影響の少ない外部に露出しておくことによって樹脂配管11の温度上昇を抑えたり、または樹脂配管11の部分に冷却器を配置するなどが考えられる。また、配管の素材としては、フレキシブルな素材であれば、樹脂に限らない。 In this embodiment, the temperature of the resin pipe 11 is adjusted at the time of charging / discharging of the fuel cell system, considering that the resin pipe 11 has lower heat resistance than the metal pipe. From the viewpoint of heat resistance, about 200 ° C. or lower is preferable, and if the temperature becomes too low, water vapor may be condensed in the resin pipe 11, and therefore, about 120 ° C. or higher is preferable. For example, only the fuel generating member 1 and the fuel cell unit 2 are heated by the heater, and the resin pipe 11 is exposed to the outside with little influence of heat, thereby suppressing the temperature rise of the resin pipe 11 or resin. For example, a cooler may be disposed in the pipe 11. Moreover, as a material of piping, if it is a flexible material, it will not be restricted to resin.
<第3実施形態>
 本発明の第3実施形態に係る燃料電池システムの概略構成を図7に示す。本実施形態に係る燃料電池システムは、蛇腹状の配管6の代わりに滑り継手12を可動部として用いている以外は第1実施形態に係る燃料電池システムと同様の構成である。
<Third Embodiment>
FIG. 7 shows a schematic configuration of the fuel cell system according to the third embodiment of the present invention. The fuel cell system according to the present embodiment has the same configuration as that of the fuel cell system according to the first embodiment, except that the sliding joint 12 is used as a movable part instead of the bellows-like pipe 6.
 滑り継手12は、ステンレス製の小径管部12Aと、小径管部12Aよりも径が大きいステンレス製の大径管部12Bと、パッキン12Cとを備え、小径管部12Aおよび大径管部12Bが同軸上に配置され、パッキン12Cが大径管部12Bに固着されて小径管部12Aと大径管部12Bとの隙間に設けられる構成である。このような構成により、滑り継手12は、ガスのシール性を確保しながら小径管部12Aおよび大径管部12Bの軸方向に伸縮可能である。 The sliding joint 12 includes a stainless-made small-diameter pipe portion 12A, a stainless-steel large-diameter pipe portion 12B having a diameter larger than that of the small-diameter pipe portion 12A, and a packing 12C. The small-diameter pipe portion 12A and the large-diameter pipe portion 12B include It is arranged on the same axis, and the packing 12C is fixed to the large-diameter pipe portion 12B and is provided in the gap between the small-diameter pipe portion 12A and the large-diameter pipe portion 12B. With such a configuration, the slip joint 12 can be expanded and contracted in the axial direction of the small-diameter pipe portion 12A and the large-diameter pipe portion 12B while ensuring gas sealing performance.
 滑り継手12の滑り方向は一次元であるが、本実施形態に係る燃料電池システムでは、滑り継手12の滑り方向と容器の位置の変化方向とを揃えているので、滑り継手12が容器3の位置の変化方向に可動する。例えば、燃料発生部材1の重量が増加すると、図8に示すように、容器3の位置は下方に変化し、それに伴い滑り継手12が伸長して下方に可動する。 Although the sliding direction of the sliding joint 12 is one-dimensional, in the fuel cell system according to the present embodiment, the sliding direction of the sliding joint 12 is aligned with the direction of change of the container position. It moves in the direction of change of position. For example, when the weight of the fuel generating member 1 increases, as shown in FIG. 8, the position of the container 3 changes downward, and the slip joint 12 expands and moves downward accordingly.
 したがって、本実施形態に係る燃料電池システムは、第1実施形態に係る燃料電池システムと同様に、バネ秤7の測定結果に基づいて燃料発生部材1の酸化状態を精度良く検出することができる。 Therefore, the fuel cell system according to the present embodiment can accurately detect the oxidation state of the fuel generating member 1 based on the measurement result of the spring balance 7 as in the fuel cell system according to the first embodiment.
 なお、パッキン12Cに耐熱性が低い樹脂パッキンを用いる場合は、燃料電池システムの充放電時に滑り継手12の温度を調節する。耐熱性の観点からは200℃程度以下が好ましく、また低温になりすぎると、滑り継手12内で水蒸気が結露する可能性があるため、120℃程度以上が好ましい。温度調節においては、第2実施形態と同様の構成が考えられる。 In addition, when using resin packing with low heat resistance for the packing 12C, the temperature of the sliding joint 12 is adjusted during charging / discharging of the fuel cell system. From the viewpoint of heat resistance, about 200 ° C. or lower is preferable, and if the temperature is too low, water vapor may be condensed in the slip joint 12, and therefore, about 120 ° C. or higher is preferable. In temperature control, the same configuration as in the second embodiment can be considered.
<その他>
 上述した実施形態では、重量測定部としてバネ秤7を用いたが、例えばバネ秤7の代わりに歪ゲージを用いた重さセンサを用いても良い。
<Others>
In the above-described embodiment, the spring balance 7 is used as the weight measuring unit. However, for example, a weight sensor using a strain gauge may be used instead of the spring balance 7.
 上述した実施形態においては、燃料電池部2の電解質膜2Aとして固体酸化物電解質を用いて、発電の際に燃料極2B側で水を発生させるようにする。この構成によれば、燃料発生部材1が設けられた側で水を発生するため、装置の簡素化や小型化に有利である。一方、特開2009-99491号公報に開示された燃料電池のように、燃料電池部2の電解質膜2Aとして水素イオンを通す固体高分子電解質を用いることも可能である。但し、この場合には、発電の際に燃料電池部2の酸化剤極2C側で水が発生されることになるため、この水を燃料発生部1に伝搬する流路を設ければよい。そして、燃料電池部2の酸化剤極2C側で発生した水を燃料発生部1に伝搬する流路にも、配管5の可動部と同様の可動部を設ければよい。 In the embodiment described above, a solid oxide electrolyte is used as the electrolyte membrane 2A of the fuel cell unit 2, and water is generated on the fuel electrode 2B side during power generation. According to this configuration, water is generated on the side where the fuel generating member 1 is provided, which is advantageous for simplification and miniaturization of the apparatus. On the other hand, as a fuel cell disclosed in Japanese Patent Application Laid-Open No. 2009-99491, a solid polymer electrolyte that allows hydrogen ions to pass through can be used as the electrolyte membrane 2A of the fuel cell unit 2. However, in this case, since water is generated on the oxidant electrode 2C side of the fuel cell unit 2 during power generation, a flow path for propagating this water to the fuel generation unit 1 may be provided. A movable part similar to the movable part of the pipe 5 may be provided in the flow path for propagating water generated on the oxidant electrode 2 </ b> C side of the fuel cell part 2 to the fuel generation part 1.
 また、上述した実施形態では、1つの燃料電池部2が発電も水の電気分解も行っているが、燃料電池(例えば発電専用の固体酸化物燃料電池)と水の電気分解器(例えば水の電気分解専用の固体酸化物燃料電池)が燃料発生部材1に対してガス流路上並列に接続される構成にしてもよい。そして、水の電気分解器を収容する容器と燃料発生部材1を収容する容器3との間に設けられる配管にも、配管5の可動部と同様の可動部を設ければよい。 In the above-described embodiment, one fuel cell unit 2 performs both power generation and water electrolysis. However, a fuel cell (for example, a solid oxide fuel cell dedicated to power generation) and a water electrolyzer (for example, water) A solid oxide fuel cell dedicated for electrolysis may be connected to the fuel generating member 1 in parallel on the gas flow path. A movable part similar to the movable part of the pipe 5 may be provided also in the pipe provided between the container containing the water electrolyzer and the container 3 containing the fuel generating member 1.
 また、上述した実施形態では、燃料電池部2の燃料ガスを水素にしているが、一酸化炭素や炭化水素など水素以外の還元性ガスを燃料電池部2の燃料ガスとして用いても構わない。 In the above-described embodiment, the fuel gas of the fuel cell unit 2 is hydrogen, but a reducing gas other than hydrogen such as carbon monoxide or hydrocarbon may be used as the fuel gas of the fuel cell unit 2.
 また、上述した各実施形態同士は、矛盾のない限り適宜組み合わせて実施しても構わない。例えば、配管5が、蛇腹状の配管6と樹脂配管11の両方を有するようにしても良い。また、上述した各実施形態において説明した変形例は矛盾のない限り他の実施形態において適用しても構わない。 Further, the above-described embodiments may be appropriately combined as long as there is no contradiction. For example, the pipe 5 may include both the bellows-like pipe 6 and the resin pipe 11. The modifications described in the above embodiments may be applied to other embodiments as long as there is no contradiction.
   1 燃料発生部材
   2 燃料電池部
   2A 電解質膜
   2B 燃料極
   2C 酸化剤極
   3、4 容器
   5 配管
   6 蛇腹状の配管
   7 バネ秤
   8 検出部
   9 残量表示器
   10 支柱
   11 樹脂配管
   12 滑り継手
   12A 小径管部
   12B 大径管部
   12C パッキン
DESCRIPTION OF SYMBOLS 1 Fuel generating member 2 Fuel cell part 2A Electrolyte membrane 2B Fuel electrode 2C Oxidant electrode 3, 4 Container 5 Piping 6 Bellows-like piping 7 Spring balance 8 Detection part 9 Remaining capacity indicator 10 Post 11 Resin piping 12 Sliding joint 12A Small diameter Pipe part 12B Large diameter pipe part 12C Packing

Claims (9)

  1.  酸化反応により燃料ガスを発生する燃料発生部材と、
     酸素を含む酸化剤ガスと前記燃料発生部材から供給される燃料ガスとの反応により発電を行う燃料電池部と、
     前記燃料発生部材を収容する第1容器と、
     前記燃料電池部を収容する第2容器と、
     前記燃料発生部材と前記燃料電池部の燃料極との間でガスが流通するように前記第1容器と前記第2容器の間に設けられる配管と、
     前記燃料発生部材を含む前記第1容器全体の重量変化に応じた前記第1容器の位置の変化に基づき、前記燃料発生部材を含む前記第1容器全体の重量を測定する重量測定部と、
     前記重量測定部の測定結果に基づいて前記燃料発生部材の酸化状態を検出する検出部と、
     を備え、
     前記配管が、前記第1容器の位置の変化方向に可動する可動部を有することを特徴とする燃料電池システム。
    A fuel generating member that generates fuel gas by an oxidation reaction;
    A fuel cell unit that generates power by a reaction between an oxidant gas containing oxygen and a fuel gas supplied from the fuel generating member;
    A first container containing the fuel generating member;
    A second container for housing the fuel cell unit;
    Piping provided between the first container and the second container so that gas flows between the fuel generating member and the fuel electrode of the fuel cell unit;
    A weight measuring unit for measuring the weight of the entire first container including the fuel generating member based on a change in the position of the first container in accordance with a change in the weight of the entire first container including the fuel generating member;
    A detecting unit for detecting an oxidation state of the fuel generating member based on a measurement result of the weight measuring unit;
    With
    The fuel cell system, wherein the pipe has a movable portion that is movable in a changing direction of the position of the first container.
  2.  前記可動部が、蛇腹状の配管を含むことを特徴とする請求項1に記載の燃料電池システム。 The fuel cell system according to claim 1, wherein the movable part includes a bellows-like pipe.
  3.  前記可動部が、フレキシブルな素材で形成された配管を含むことを特徴とする請求項1または請求項2に記載の燃料電池システム。 3. The fuel cell system according to claim 1, wherein the movable portion includes a pipe formed of a flexible material.
  4.  前記フレキシブルな素材は樹脂であることを特徴とする請求項3に記載の燃料電池システム。 4. The fuel cell system according to claim 3, wherein the flexible material is a resin.
  5.  前記可動部が、滑り継手を含み、
     前記滑り継手の滑り方向と前記第1容器の位置の変化方向とが揃っていることを特徴とする請求項1から4のいずれか一項に記載の燃料電池システム。
    The movable part includes a sliding joint;
    The fuel cell system according to any one of claims 1 to 4, wherein a sliding direction of the sliding joint and a changing direction of the position of the first container are aligned.
  6.  前記重量測定部はバネ秤であることを特徴とする請求項1から5のいずれか一項に記載の燃料電池システム。 The fuel cell system according to any one of claims 1 to 5, wherein the weight measuring unit is a spring balance.
  7.  前記検出部は、前記重量測定部の測定結果と前記燃料発生部材の酸化状態との関係を示すデータテーブルまたは前記重量測定部の測定結果と前記燃料発生部材の酸化状態との関係を示す計算式を用いて、前記重量測定部の測定結果に基づいて前記燃料発生部材の酸化状態を検出することを特徴とする請求項1から6のいずれか一項に記載の燃料電池システム。 The detection unit is a data table indicating the relationship between the measurement result of the weight measurement unit and the oxidation state of the fuel generation member, or a calculation formula indicating the relationship between the measurement result of the weight measurement unit and the oxidation state of the fuel generation member The fuel cell system according to claim 1, wherein an oxidation state of the fuel generation member is detected based on a measurement result of the weight measurement unit.
  8.  前記燃料発生部材は鉄を含み、
     前記燃料電池システムは前記検出部の検出結果に基づき前記鉄の残量が所定の値より少ないことを示す残量表示部を備えたことを特徴とする請求項1から7のいずれか一項に記載の燃料電池システム。
    The fuel generating member includes iron;
    8. The fuel cell system according to claim 1, further comprising: a remaining amount display unit that indicates that the remaining amount of iron is less than a predetermined value based on a detection result of the detecting unit. The fuel cell system described.
  9.  前記燃料電池部は水を含む酸化剤ガスを電気分解し、前記燃料発生部材は前記電気分解によって発生した水素との反応により還元することを特徴とする請求項1から8のいずれか一項に記載の燃料電池システム。 9. The fuel cell unit according to claim 1, wherein the fuel cell unit electrolyzes an oxidant gas containing water, and the fuel generating member reduces by reaction with hydrogen generated by the electrolysis. The fuel cell system described.
PCT/JP2014/051640 2013-02-08 2014-01-27 Fuel cell system WO2014123020A1 (en)

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