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JP2005183040A - Method for measuring current distribution of stacked fuel cell, stacked fuel cell, and operation method of stacked fuel cell - Google Patents

Method for measuring current distribution of stacked fuel cell, stacked fuel cell, and operation method of stacked fuel cell Download PDF

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JP2005183040A
JP2005183040A JP2003418230A JP2003418230A JP2005183040A JP 2005183040 A JP2005183040 A JP 2005183040A JP 2003418230 A JP2003418230 A JP 2003418230A JP 2003418230 A JP2003418230 A JP 2003418230A JP 2005183040 A JP2005183040 A JP 2005183040A
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fuel cell
stacked
current
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JP4926372B2 (en
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Tetsuo Kikuchi
哲郎 菊地
Kazuo Horibe
和夫 堀部
Hiroyuki Takashima
博之 高嶋
Taketoshi Kato
豪俊 加藤
Naohiro Takeshita
直宏 竹下
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Denso Corp
Toyota Motor Corp
Soken Inc
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Nippon Soken Inc
Toyota Motor Corp
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    • 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
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Abstract

<P>PROBLEM TO BE SOLVED: To observe a power generating state in a fuel cell in order to operate the fuel cell in the optimum state. <P>SOLUTION: The current distribution measuring method of a stacked fuel cell is that a cell stack 1 of the fuel cell is formed by joining an air electrode to one side of an electrolyte and a fuel electrode to the other side, interposing them between separators each having a gas passage to form a cell, stacking the cells, and installing current collecting members 2 taking out electric power in the vertical direction to the stacking thickness direction at the end part, a magnetic sensor 3 is arranged at the end part in the thickness direction the fuel cell cell stack, a magnetic field generating when current flows in the current collecting member 2 is measured with the magnetic sensor 3, and the current distribution of the fuel cell cell stack 1 is measured based on the measured magnetic field. The cause of a drop in power generation capacity is determined from a part where power generation capacity is dropped in the fuel cell cell, and operation restoring the drop in power generation capacity can be conducted. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、水素と酸素との電気化学反応により電気エネルギを発生させる燃料電池セルが積層した積層型燃料電池に関する。   The present invention relates to a stacked fuel cell in which fuel cells that generate electrical energy by an electrochemical reaction between hydrogen and oxygen are stacked.

燃料電池、特に固体高分子型燃料電池は、車両用あるいは固定用の発電システムとして開発が進められている。   Development of fuel cells, particularly polymer electrolyte fuel cells, is being promoted as a power generation system for vehicles or stationary.

燃料電池では、以下に示した水素と酸素の電気化学反応が起こり、電気エネルギが発生する。   In a fuel cell, the following electrochemical reaction between hydrogen and oxygen occurs, and electric energy is generated.

(燃料極側)H2→2H++2e-
(空気極側)2H++1/2O2+2e-→H2
(全体) H2+1/2O2→H2
燃料電池は、通常は、電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを形成し、空気極に酸素を有する空気を燃料極に水素を供給して発電を行っている。そして、一つの燃料電池セルでは実用に供するだけの電力がえられないため、多数の燃料電池セルを積層させた積層型燃料電池とすることで高い発電量を得ている。なお、積層型燃料電池において、多数の燃料電池セルは、電気的に直列に接続されている。
(Fuel electrode side) H 2 → 2H + + 2e
(Air electrode side) 2H + + 1 / 2O 2 + 2e → H 2 O
(Overall) H 2 + 1 / 2O 2 → H 2 O
In a fuel cell, normally, an air electrode is joined to one surface of an electrolyte, and a fuel electrode is joined to the other surface. A fuel cell is formed by sandwiching the electrode with a separator having a gas flow path. Electric power is generated by supplying hydrogen to the fuel electrode. Since a single fuel battery cell cannot provide enough power for practical use, a stacked fuel cell in which a large number of fuel battery cells are stacked provides a high power generation amount. In the stacked fuel cell, many fuel cells are electrically connected in series.

燃料電池においては、燃料電池セルへの燃料ガス(水素)および空気(酸素)の供給量をできるだけ少なくして最大の発電量を得ることが運転の目的の一つとされている。また、固体高分子型燃料電池においては水をプロトンの媒体として使用するため、燃料電池セルに供給される燃料ガス(水素)は加湿されている。   In the fuel cell, one of the purposes of operation is to obtain the maximum power generation amount by reducing the supply amount of the fuel gas (hydrogen) and air (oxygen) to the fuel cell as much as possible. Further, in the polymer electrolyte fuel cell, since water is used as a proton medium, the fuel gas (hydrogen) supplied to the fuel cell is humidified.

しかしながら、燃料電池はその反応が示すように発電によって水が発生する。燃料電池内において水分が過剰となると、余分な量の水分が発電を阻害して発電力が低下するようになるという問題があった。このため、燃料電池の中では適正な範囲の水分を保つことが要求されている。   However, the fuel cell generates water as a result of its reaction. When the moisture is excessive in the fuel cell, there is a problem that an excessive amount of moisture inhibits power generation and power generation is reduced. For this reason, it is required to maintain a proper range of moisture in the fuel cell.

そして、この燃料電池の中を適正な範囲の水分で保つという要求は、積層型燃料電池のそれぞれの燃料電池セルにおいても要求されている。詳しくは、燃料電池に供給されるガスの温度、圧力あるいは湿度を調節して燃料電池を適正な状態に保ったとしても、燃料電池を構成するそれぞれの燃料電池セルにおいては、部分的に適正な条件から外れるようになることがある。適正な条件から外れると、その部分は十分な発電を行うことができなくなり、燃料電池セルにおいて発電を行う部分が偏るようになる。発電を行う部分が偏ると、その部分の劣化の進行がはやくなり、燃料電池全体の寿命が短くなっていた。また、取り出せる電圧が低くなってしまう。このため、燃料電池セルにおいても、適正な範囲の水分で保つことが要求されている。   And the request | requirement of keeping the inside of this fuel cell with the water | moisture content of an appropriate range is also requested | required also in each fuel cell of a laminated | stacked fuel cell. Specifically, even if the temperature, pressure, or humidity of the gas supplied to the fuel cell is adjusted to keep the fuel cell in an appropriate state, each fuel cell constituting the fuel cell is partially appropriate. It may become out of condition. If it deviates from an appropriate condition, the portion cannot perform sufficient power generation, and the portion of the fuel cell that performs power generation is biased. If the portion where power generation is performed is biased, the deterioration of the portion is accelerated, and the life of the entire fuel cell is shortened. Moreover, the voltage which can be taken out will become low. For this reason, it is requested | required also to hold | maintain with the water | moisture content of an appropriate range also in a fuel cell.

一方、積層型燃料電池においては、端部のセルの温度は中央部よりも低くなりがちであるので、一般に水分がたまりやすく、その結果として、発電電力が低くなるという傾向があった。   On the other hand, in the stacked fuel cell, the temperature of the cell at the end tends to be lower than that at the central portion, so that moisture generally tends to accumulate, and as a result, the generated power tends to decrease.

燃料電池の状態を監視する手段としては、それぞれの燃料電池セルの発電電圧を測定する方法が用いられている。詳しくは、燃料電池セルのセル電圧の低下から異常状態を診断する方法である。また、燃料電池内の電流分布から反応ガスの過不足を診断し、反応ガス流量もしくは負荷電流を制御して燃料電池の破壊を防止するようにしたものも提案されている(例えば、特許文献1参照)。しかしながら、この方法では、それぞれの燃料電池セルの発電能力は監視できるが、燃料電池セルに部分的に発電できない部分が生じることまで判別は不能であった。
特開平9−259913号公報
As a means for monitoring the state of the fuel cell, a method of measuring the generated voltage of each fuel cell is used. Specifically, this is a method of diagnosing an abnormal state from a decrease in the cell voltage of the fuel cell. In addition, there has been proposed one that diagnoses the excess or deficiency of the reaction gas from the current distribution in the fuel cell and controls the reaction gas flow rate or load current to prevent the destruction of the fuel cell (for example, Patent Document 1). reference). However, with this method, the power generation capability of each fuel cell can be monitored, but it has not been possible to discriminate until a portion where the fuel cell cannot partially generate power is generated.
JP-A-9-259913

本発明は上記実状に鑑みてなされたものであり、最適な状態で燃料電池を運転するために電池内の発電状況を観測する方法を提供することを課題とする。   This invention is made | formed in view of the said actual condition, and makes it a subject to provide the method of observing the electric power generation condition in a battery in order to drive | operate a fuel cell in the optimal state.

上記課題を解決するために本発明者らは検討を重ねた結果、本発明の積層型燃料電池の電流分布の測定方法、電流分布の測定方法を有する積層型燃料電池ならびに積層型燃料電池の運転方法を見出した。   As a result of repeated studies by the present inventors to solve the above-mentioned problems, the method for measuring the current distribution of the stacked fuel cell of the present invention, the stacked fuel cell having the current distribution measuring method, and the operation of the stacked fuel cell I found a way.

本発明の積層型燃料電池の電流分布の測定方法は、電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設した燃料電池セル積層体を有する積層型燃料電池の電流分布の測定方法であって、燃料電池セル積層体の厚さ方向の端部に磁気センサを配設し、集電部材に電気が流れるときに発生する磁界を磁気センサにより測定し、測定された磁界から燃料電池セル積層体の電流分布を測定することを特徴とする。   The method of measuring the current distribution of the stacked fuel cell according to the present invention comprises a fuel cell comprising an air electrode joined to one surface of an electrolyte and a fuel electrode joined to the other surface and sandwiched by a separator having a gas flow path. A method for measuring the current distribution of a stacked fuel cell having a fuel cell stack in which a current collecting member for stacking and collecting power in a direction perpendicular to the thickness direction stacked at an end thereof is provided, A magnetic sensor is arranged at the end of the cell stack in the thickness direction, the magnetic field generated when electricity flows through the current collector is measured by the magnetic sensor, and the current distribution of the fuel cell stack is measured from the measured magnetic field. Is measured.

本発明の電流分布の測定方法は、燃料電池セルの端部に流れる電流により生じる磁界を磁気センサで測定することで燃料電池セル積層体の電流分布を測定する。   The current distribution measuring method of the present invention measures the current distribution of the fuel cell stack by measuring the magnetic field generated by the current flowing through the end of the fuel cell with a magnetic sensor.

本発明の積層型燃料電池は、電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設した燃料電池セル積層体と、燃料電池セル積層体の端部に配設された磁気センサと、を有することを特徴とする。   The laminated fuel cell according to the present invention comprises a fuel cell unit in which an air electrode is joined to one surface of an electrolyte and a fuel electrode is joined to the other surface, and sandwiched by a separator having a gas flow path. A fuel cell stack having a current collecting member for extracting power in a direction perpendicular to the thickness direction stacked on the fuel cell, and a magnetic sensor disposed at an end of the fuel cell stack. And

本発明の積層型燃料電池は、燃料電池セル積層体の端部に配設された磁気センサが燃料電池セル積層体において発電により生じた電流の電流分布を測定できる。そして、測定された電流分布から、最適な発電状態となるように運転条件を調節することが可能となる。   In the stacked fuel cell of the present invention, the magnetic sensor disposed at the end of the fuel cell stack can measure the current distribution of the current generated by the power generation in the fuel cell stack. And it becomes possible to adjust an operating condition so that it may become an optimal electric power generation state from the measured electric current distribution.

本発明の積層型燃料電池の電流分布の運転方法は、電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設した燃料電池セル積層体と、燃料電池セル積層体の端部に配設された磁気センサと、を有する積層型燃料電池を運転する積層型燃料電池の運転方法であって、磁気センサにより測定される集電部材に流れる電流により発生する磁界から燃料電池セルにおける電流分布を算出し、燃料電池セル積層体へ供給されるガスの制御を行うことを特徴とする。   The operation method of the current distribution of the stacked fuel cell according to the present invention includes a fuel cell in which an air electrode is joined to one surface of an electrolyte and a fuel electrode is joined to the other surface and sandwiched by a separator having a gas flow path. A fuel cell stack in which a current collecting member for stacking and collecting power in a direction perpendicular to the thickness direction stacked on the end of the stack is disposed; and a magnetic sensor disposed on an end of the fuel cell stack; A method for operating a stacked fuel cell, wherein a current distribution in a fuel cell is calculated from a magnetic field generated by a current flowing through a current collecting member measured by a magnetic sensor. Control of the gas supplied to the cell stack is performed.

本発明の運転方法は、燃料電池セル積層体の端部に配設された磁気センサが燃料電池セル積層体において発電により生じた電流の電流分布を測定し、測定された電流分布から、最適な発電状態となるように燃料電池セル積層体へ供給されるガスの制御を行うことで最適な運転状況で積層型燃料電池を運転できる。   In the operation method of the present invention, the magnetic sensor disposed at the end of the fuel cell stack measures the current distribution of the current generated by the power generation in the fuel cell stack, and the optimum current is measured from the measured current distribution. By controlling the gas supplied to the fuel cell stack so as to be in a power generation state, the stacked fuel cell can be operated in an optimal operating condition.

本発明の積層型燃料電池の電流分布の測定方法は、燃料電池セル積層体の端部に配設された集電部材に流れる電流が発生させる磁界を測定し、測定された磁界から燃料電池セル積層体の電流分布を得る。そして、燃料電池セル積層体の電流分布から、燃料電池セルにおいて発電能力の低下した部分が判断でき、発電能力の低下の原因を判断できるようになる。   The method for measuring the current distribution of a stacked fuel cell according to the present invention measures a magnetic field generated by a current flowing through a current collecting member disposed at an end of a fuel cell stack, and the fuel cell from the measured magnetic field. Obtain the current distribution of the laminate. Then, from the current distribution of the fuel cell stack, it is possible to determine a portion where the power generation capability is reduced in the fuel cell, and to determine the cause of the decrease in the power generation capability.

本発明の積層型燃料電池は、上記電流分布の測定方法を実施できる燃料電池であり、発電能力の低下の原因を判断できることで、発電能力の低下の原因に対処することができ、全体としての発電能力の低下を抑えることが可能な燃料電池である。   The stacked fuel cell of the present invention is a fuel cell that can carry out the above current distribution measurement method, and can determine the cause of the decrease in the power generation capability, thereby addressing the cause of the decrease in the power generation capability. This is a fuel cell capable of suppressing a decrease in power generation capacity.

本発明の積層型燃料電池の運転方法は、上記燃料電池の運転方法であり、磁気センサにより燃料電池セル積層体に流れる電流分布を求め、電流分布にかたよりを生じたときに燃料電池セル積層体に供給されるガスを調節することで燃料電池セル内を最適な条件に保ち、発電能力の低下を抑える運転方法である。   The operation method of the stacked fuel cell according to the present invention is the above-described operation method of the fuel cell, wherein a current distribution flowing through the fuel cell stack is obtained by a magnetic sensor, and the fuel cell stack is generated when the current distribution is affected. It is an operation method that keeps the inside of the fuel cell cell under optimum conditions by adjusting the gas supplied to the body and suppresses the decrease in power generation capacity.

(積層型燃料電池の電流分布の測定方法)
本発明の電流分布の測定方法は、電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設した燃料電池セル積層体を有する積層型燃料電池の電流分布の測定方法である。
(Measurement method of current distribution of stacked fuel cell)
The current distribution measuring method according to the present invention comprises stacking fuel cells in which an air electrode is joined to one surface of an electrolyte and a fuel electrode is joined to the other surface and sandwiched by a separator having a gas flow path. This is a method for measuring the current distribution of a stacked fuel cell having a fuel cell stack in which a current collecting member for taking out electric power in a direction perpendicular to the thickness direction stacked on the part is disposed.

本発明の電流分布の測定方法は、燃料電池セル積層体の厚さ方向の端部に磁気センサを配設し、集電部材に電気が流れるときに発生する磁界を磁気センサにより測定し、測定された磁界から燃料電池セル積層体の電流分布を測定する。   In the current distribution measuring method of the present invention, a magnetic sensor is disposed at the end of the fuel cell stack in the thickness direction, and the magnetic field generated when electricity flows through the current collector is measured by the magnetic sensor. The current distribution of the fuel cell stack is measured from the applied magnetic field.

一般に、無限長の長さの導線に電流i(A)が流れると、導線からの距離がr(m)の地点においては、数1式で示された大きさの磁束密度B(Wb/m2)が発生することが知られている(右ねじの法則)。 In general, when a current i (A) flows through a lead wire having an infinite length, a magnetic flux density B (Wb / m) having a magnitude expressed by the formula 1 is obtained at a point where the distance from the lead wire is r (m). 2 ) is known to occur (right-hand rule).

Figure 2005183040
Figure 2005183040

本発明の電流分布の測定方法は、燃料電池セル積層体の端部に配設した集電部材をこの導線に見立てて、燃料電池セル積層体の磁界を測定するものである。燃料電池セル積層体は、それぞれの燃料電池セルにおいて発電された電力を集電部材を介して電池の外部に取り出す。燃料電池セルの発電領域において発電された電力は、燃料電池セル積層体においては厚さ方向に流れる。そして、集電部材により電気が集められ、集電部材の延びる方向(燃料電池セル積層体の厚さ方向に垂直な方向)に電流が流れる。燃料電池セルの発電領域に対応した位置にある集電部材に流れる電流は、電流の流れる方向の下流部に進むにつれて大きくなる。集電部材において集められた電流が流れる方向を導線の長さ方向として考えたときには、集電部材の延びる方向に垂直な断面における周方向に磁界が発生している。このとき、本発明の電流分布の測定方法は、この磁界の変化から、燃料電池セル積層体の電流分布を求めるものである。   The current distribution measuring method of the present invention measures the magnetic field of the fuel cell stack, with the current collecting member disposed at the end of the fuel cell stack being regarded as this conducting wire. The fuel cell stack takes out the electric power generated in each fuel cell through the current collecting member to the outside of the battery. The electric power generated in the power generation region of the fuel cell flows in the thickness direction in the fuel cell stack. Then, electricity is collected by the current collecting member, and a current flows in the direction in which the current collecting member extends (direction perpendicular to the thickness direction of the fuel cell stack). The current flowing through the current collecting member at a position corresponding to the power generation region of the fuel battery cell increases as it proceeds to the downstream portion in the current flowing direction. When the direction in which the current collected in the current collecting member flows is considered as the length direction of the conducting wire, a magnetic field is generated in the circumferential direction in the cross section perpendicular to the direction in which the current collecting member extends. At this time, the current distribution measuring method of the present invention obtains the current distribution of the fuel cell stack from the change of the magnetic field.

積層型燃料電池(および燃料電池セル)ならびに積層型燃料電池の周囲の物体の透磁率が空気と同じであるとし、本発明の電流分布の測定方法を図1〜5を用いて具体的に説明する。   The magnetic permeability of the stacked fuel cell (and fuel cell) and the objects around the stacked fuel cell is the same as that of air, and the current distribution measuring method of the present invention will be specifically described with reference to FIGS. To do.

燃料電池セルおよびその発電可能領域が長方形に形成されているものとする。ここで、発電可能領域とは、燃料電池セルにおいて電気化学反応が進行する領域を示すものであり、実際の燃料電池セルにおいては空気極、電解質、燃料極が積層した状態でガスが供給される領域である。   It is assumed that the fuel cell and its power generation possible region are formed in a rectangular shape. Here, the power generation possible region indicates a region where an electrochemical reaction proceeds in a fuel cell, and in an actual fuel cell, gas is supplied in a state where an air electrode, an electrolyte, and a fuel electrode are stacked. It is an area.

このような燃料電池セルを積層させた燃料電池セル積層体1の集電板2は、燃料電池セルの外周形状と略一致する集電本体部20と、集電本体部20に一体にもうけられ燃料電池セル積層体1の短辺の外周から突出する端子部21と、を有している。   The current collector plate 2 of the fuel cell stack 1 in which such fuel cells are stacked is integrally provided on the current collector main body 20 and the current collector main body 20 that substantially match the outer peripheral shape of the fuel cell. And a terminal portion 21 protruding from the outer periphery of the short side of the fuel cell stack 1.

燃料電池セル積層体1において発電が行われると、燃料電池セル積層体1の厚さ方向に電流が流れる(図1)。厚さ方向に流れた電流は、集電板2の集電本体部20に到達する。そして、集電板2の集電本体部20においては、端子部21に向かって電流が流れる。集電本体部20に流れる電流は、端子部21に近づくにつれて大きくなる(図2)。なお、図2(〜5)においては、集電板2に流れる電流の大きさを矢印の太さで示している。集電本体部20の端子部21から最も離れた領域においては、燃料電池セルのその位置に対応した部分において発電された電流が流れ込み、この電流が流れる(図2中の右端に並んだ矢印で示された電流)。   When power generation is performed in the fuel cell stack 1, a current flows in the thickness direction of the fuel cell stack 1 (FIG. 1). The current flowing in the thickness direction reaches the current collector body 20 of the current collector plate 2. In the current collector body 20 of the current collector plate 2, a current flows toward the terminal portion 21. The current flowing through the current collector main body 20 increases as it approaches the terminal portion 21 (FIG. 2). 2 (~ 5), the magnitude of the current flowing through the current collector plate 2 is indicated by the thickness of the arrow. In the region farthest from the terminal portion 21 of the current collecting main body portion 20, a current generated in a portion corresponding to the position of the fuel cell flows, and this current flows (indicated by an arrow aligned at the right end in FIG. 2). Indicated current).

そして、集電本体部20の端子部21から最も離れた位置から端子部21にわずかに近づいた領域においては、集電本体部20の端子部21から最も離れた位置に対応した燃料電池セルにおいて発電され集電本体部20を端子部21に向かって流れる電流(図2中の右端の矢印で示された電流)と、この領域に対応した燃料電池セルの部分において発電された(燃料電池セル積層体1から流れ込む電流)電流と、の和の電流が流れることになる(図2中の右から2列目に並んだ矢印で示された電流)。このように、端子部21に近づくほど集電本体部20において流れる電流が大きくなる。   And in the area | region which approached the terminal part 21 slightly from the position most distant from the terminal part 21 of the current collection main body part 20, in the fuel cell corresponding to the position furthest from the terminal part 21 of the current collection main body part 20 A current (current indicated by an arrow at the right end in FIG. 2) that is generated and flows through the current collector main body 20 toward the terminal portion 21 and generated in the portion of the fuel cell corresponding to this region (fuel cell) A current that is the sum of the current flowing from the laminate 1 and the current (current indicated by an arrow in the second column from the right in FIG. 2) flows. As described above, the closer to the terminal portion 21, the larger the current flowing in the current collector body portion 20.

ここで、燃料電池セル積層体1のそれぞれの燃料電池セルが、発電可能領域で均一な発電を行ったとすると、集電板2の集電本体部20に流れる電流の大きさは、図2で示したように、端子部21からの距離が同じ位置であればほぼ同じとなる。なお、図2で示したように、端子部21は集電本体部20よりも幅(図2においての上下方向の幅)が狭いので、集電本体部20の端子部21近傍に流れる電流は、端子部21に向かう方向となっている。   Here, assuming that each fuel cell of the fuel cell stack 1 performs uniform power generation in the power generation possible region, the magnitude of the current flowing through the current collector body 20 of the current collector plate 2 is as shown in FIG. As shown, if the distance from the terminal portion 21 is the same position, the distance is almost the same. As shown in FIG. 2, since the terminal portion 21 is narrower than the current collecting main body portion 20 (the vertical width in FIG. 2), the current flowing in the vicinity of the terminal portion 21 of the current collecting main body portion 20 is The direction is toward the terminal portion 21.

このとき、図2に示された電流が集電板2に流れると、集電板2には図3で示したように、そのまわりに磁界が発生する。具体的には、集電板2の端子部21の突出した方向に対して垂直な断面において周方向の磁力線を有する磁界が発生する。燃料電池セル1のそれぞれの燃料電池セルが発電可能領域で均一な発電を行ったときには、集電板2のまわりに発生する磁界の磁束密度は端子部21からの距離に比例して小さくなる。本発明の電流密度の測定方法は、この磁界を磁気センサで測定するものである。   At this time, when the current shown in FIG. 2 flows through the current collector plate 2, a magnetic field is generated around the current collector plate 2 as shown in FIG. Specifically, a magnetic field having a circumferential magnetic field line is generated in a cross section perpendicular to the protruding direction of the terminal portion 21 of the current collector plate 2. When each fuel cell of the fuel cell 1 performs uniform power generation in the power generation possible region, the magnetic flux density of the magnetic field generated around the current collector plate 2 decreases in proportion to the distance from the terminal portion 21. The current density measuring method of the present invention measures this magnetic field with a magnetic sensor.

この燃料電池セル積層体1において、燃料電池セルの発電可能領域の一部(図4のAの領域に対応した位置)で発電が停止したとする。発電が停止すると、集電本体部のAの領域には電流が流れ込まなくなる。Aの領域に電流が流れ込まなくなると、Aの領域に隣接しかつAの領域より端子部21に近い領域(図4のBの領域)においては、Bの領域で集電本体部20に燃料電池セル積層体1から流れ込む電流のみが流れることとなる。燃料電池セルの一部に発電が停止しなかった場合には、Aの領域で集電本体部に集められる電流とBの領域で燃料電池セルから集電板本体部に集められる電流との和の電流がBの領域で流れている。   In the fuel cell stack 1, it is assumed that power generation is stopped in a part of the power generation possible region of the fuel cell (a position corresponding to the region A in FIG. 4). When the power generation is stopped, no current flows into the area A of the current collecting main body. When the current stops flowing into the region A, in the region adjacent to the region A and closer to the terminal portion 21 than the region A (region B in FIG. 4), the fuel cell is connected to the current collector main body 20 in the region B. Only the current flowing from the cell stack 1 will flow. When power generation does not stop in a part of the fuel cell, the sum of the current collected in the current collector body in the region A and the current collected in the current collector plate body from the fuel cell in the region B Current flows in the region B.

すなわち、燃料電池セルの一部に発電が停止した領域が生じると、この領域に対応した集電本体部20に流れる電流が変化する。さらに、発電が停止した領域に対応した集電本体部20の端子部21側の領域に流れる電流が変化する。集電本体部20を流れる電流に変化が生じると、集電板2に生じる磁界も変化する。具体的には、図4に示した集電板2においては、図5に示したようにAの領域をのぞいた領域に流れる電流により磁界が発生する。また、図5のBの領域を含む断面における磁界の磁束密度は、図3の同じ断面における磁界の磁束密度より小さくなっている。これは、図5のBの領域の電流が図3の同じ領域と比べて低いことに起因する。   That is, when a region where power generation is stopped occurs in a part of the fuel battery cell, the current flowing through the current collector body 20 corresponding to this region changes. Furthermore, the current flowing through the region on the terminal part 21 side of the current collector main body 20 corresponding to the region where power generation is stopped changes. When the current flowing through the current collector body 20 changes, the magnetic field generated in the current collector plate 2 also changes. Specifically, in the current collector plate 2 shown in FIG. 4, a magnetic field is generated by a current flowing in a region except the region A as shown in FIG. Further, the magnetic flux density of the magnetic field in the cross section including the region B in FIG. 5 is smaller than the magnetic flux density of the magnetic field in the same cross section in FIG. This is because the current in the region B in FIG. 5 is lower than that in the same region in FIG.

そして、図3と図5のそれぞれの集電板2に発生した磁界を磁気センサにより測定することで、燃料電池セル積層体1の発電状況を判断できる。また、磁界の測定位置によっては、燃料電池セル積層体1において発電能力の停止した領域が判断できる。すなわち、燃料電池セル積層体1の集電部材に発生した磁界を測定することで、燃料電池セル積層体の電流密度の低下した領域を判断できる。   And the electric power generation condition of the fuel cell laminated body 1 can be judged by measuring the magnetic field which generate | occur | produced in each current collecting plate 2 of FIG. 3 and FIG. 5 with a magnetic sensor. Moreover, the area | region where the power generation capability stopped in the fuel cell laminated body 1 can be determined depending on the measurement position of the magnetic field. That is, by measuring the magnetic field generated in the current collecting member of the fuel cell stack 1, it is possible to determine the region where the current density of the fuel cell stack is reduced.

本発明の電流分布の測定方法は、集電部材に発生した磁界を磁気センサで測定するものであり、この測定により発電が停止したあるいは発電能力が低下した領域を判断することが可能となる。これにより、燃料電池セル積層体の電流分布を得ることができる。   The current distribution measuring method of the present invention measures a magnetic field generated in a current collecting member with a magnetic sensor, and by this measurement, it is possible to determine a region where power generation is stopped or power generation capacity is reduced. Thereby, the current distribution of the fuel cell stack can be obtained.

本発明の電流分布の測定方法は、集電部材において電流が流れる方向に垂直な断面の周方向に発生する磁界を測定するものであるため、磁気センサが燃料電池セル積層体の厚さ方向の端部に配設される。   The current distribution measuring method of the present invention measures the magnetic field generated in the circumferential direction of the cross section perpendicular to the direction in which the current flows in the current collecting member, so that the magnetic sensor is in the thickness direction of the fuel cell stack. Arranged at the end.

集電部材が集電板により形成され、磁気センサは、集電板の磁界を測定することが好ましい。集電部材が板状の集電板よりなることで、燃料電池セルと同様に積層させることができ、燃料電池セル積層体の形成が容易となる。また、集電板は、(燃料電池セル積層体の厚さ方向の)厚さが均一であり、電流の流れる方向に垂直な断面において集電板に流れる電流が均一となる。   The current collecting member is preferably formed of a current collecting plate, and the magnetic sensor preferably measures the magnetic field of the current collecting plate. When the current collecting member is made of a plate-shaped current collecting plate, the current collecting member can be laminated in the same manner as the fuel battery cell, and the formation of the fuel battery cell laminate is facilitated. The current collector plate has a uniform thickness (in the thickness direction of the fuel cell stack), and the current flowing through the current collector plate is uniform in a cross section perpendicular to the current flow direction.

複数個の磁気センサが配設されることが好ましい。通常、地磁気により±0.3G程度の誤差が生じるが、複数個の磁気センサが配設されることで地磁気の補正を行うことができ、より精度の高い測定を行うことができる。すなわち、複数の磁気センサが配設されることで、それぞれの磁気センサにより得られたデータからより正確な電流分布を得ることができる。   A plurality of magnetic sensors are preferably provided. Normally, an error of about ± 0.3 G occurs due to geomagnetism, but by providing a plurality of magnetic sensors, the geomagnetism can be corrected, and more accurate measurement can be performed. That is, by providing a plurality of magnetic sensors, a more accurate current distribution can be obtained from data obtained by each magnetic sensor.

(積層型燃料電池)
本発明の積層型燃料電池は、燃料電池セル積層体と、磁気センサと、を有する。
(Stacked fuel cell)
The stacked fuel cell of the present invention includes a fuel cell stack and a magnetic sensor.

燃料電池セル積層体は、電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設してなる。また、磁気センサは、燃料電池セル積層体の端部に配設される。本発明の積層型燃料電池は、上記電流分布の測定方法を適用できる燃料電池である。   A fuel cell stack is formed by stacking fuel cells in which an air electrode is joined to one surface of an electrolyte and a fuel electrode is joined to the other surface, and sandwiched by a separator having a gas flow path. A current collecting member for taking out electric power in a direction perpendicular to the thickness direction is provided. The magnetic sensor is disposed at the end of the fuel cell stack. The stacked fuel cell of the present invention is a fuel cell to which the current distribution measuring method can be applied.

集電部材が集電板により形成され、磁気センサは、集電板の磁界を測定することが好ましい。集電部材が板状の集電板よりなることで、燃料電池セルと同様に積層させることができ、燃料電池セル積層体の形成が容易となる。また、集電板は、(燃料電池セル積層体の厚さ方向の)厚さが均一であり、電流の流れる方向に垂直な断面において集電板に流れる電流が均一となる。   The current collecting member is preferably formed of a current collecting plate, and the magnetic sensor preferably measures the magnetic field of the current collecting plate. When the current collecting member is made of a plate-shaped current collecting plate, the current collecting member can be laminated in the same manner as the fuel battery cell, and the formation of the fuel battery cell laminate is facilitated. The current collector plate has a uniform thickness (in the thickness direction of the fuel cell stack), and the current flowing through the current collector plate is uniform in a cross section perpendicular to the current flow direction.

磁気センサの配設される場所は、集電部材に発生した磁界を測定できる位置であれば特に限定されるものではない。たとえば、集電部材の燃料電池セルに背向した表面に当接した状態や、集電部材に一体に配設してもよい。磁気センサは、集電部材に当接して配設されることがより好ましい。   The place where the magnetic sensor is disposed is not particularly limited as long as it is a position where the magnetic field generated in the current collecting member can be measured. For example, you may arrange | position in the state contact | abutted to the surface facing the fuel cell of the current collection member, or the current collection member. More preferably, the magnetic sensor is disposed in contact with the current collecting member.

複数個の磁気センサが配設されることが好ましい。通常、地磁気により±0.3×10-4T(0.3G)程度の誤差が生じるが、複数個の磁気センサが配設されることで地磁気の補正を行うことができ、より精度の高い測定を行うことができる。すなわち、複数の磁気センサが配設されることで、それぞれの磁気センサにより得られたデータからより正確な電流分布を得ることができる。 A plurality of magnetic sensors are preferably provided. Normally, an error of about ± 0.3 × 10 −4 T (0.3 G) occurs due to geomagnetism, but the geomagnetism can be corrected by providing a plurality of magnetic sensors, and the accuracy is higher. Measurements can be made. That is, by providing a plurality of magnetic sensors, a more accurate current distribution can be obtained from data obtained by each magnetic sensor.

磁気センサの数は、多くなるほど発電能力の低下した領域の特定に効果を発揮するため、多いほど好ましい。   The larger the number of magnetic sensors, the more effective the identification of the region where the power generation capacity is reduced.

磁気センサは、配設された場所における磁界を測定できるセンサであれば特に限定されるものではない。ここで、一般的な固体高分子型の燃料電池であり、発電領域の面積が400cm2、1A/cm2の電流密度の燃料電池においては、磁束密度の最大値は±6×10-4T(6G)程度であることから、ホール素子、磁気抵抗素子、フラックスゲートセンサ等の磁気センサを用いることができる。また、これらの素子のうち、厚さ方向に垂直な面における磁束密度を測定できる素子が磁気センサとしてより好ましい。 A magnetic sensor will not be specifically limited if it is a sensor which can measure the magnetic field in the place arrange | positioned. Here, a fuel cell of a general polymer electrolyte, in the fuel cell of the current density of the area of the power generation area is 400cm 2, 1A / cm 2, the maximum value of the magnetic flux density is ± 6 × 10 -4 T Since it is about (6G), a magnetic sensor such as a Hall element, a magnetoresistive element, or a fluxgate sensor can be used. Of these elements, an element capable of measuring the magnetic flux density in a plane perpendicular to the thickness direction is more preferable as a magnetic sensor.

本発明の積層型燃料電池は、磁気センサの測定値から電流分布を算出する演算手段を有することが好ましい。演算手段を有することで、磁気センサの測定値から電流分布を算出することが可能となる。また、この演算手段は、燃料電池セル積層体の電流分布から積層型燃料電池の最適な運転条件を決定することが好ましい。   The stacked fuel cell of the present invention preferably has a calculation means for calculating the current distribution from the measured value of the magnetic sensor. By having the computing means, it is possible to calculate the current distribution from the measured value of the magnetic sensor. Moreover, it is preferable that this calculating means determines the optimal operating condition of a laminated | stacked fuel cell from the electric current distribution of a fuel cell laminated body.

本発明の積層型燃料電池は、空気極および/または燃料極に供給されるガスのガス流量および/または湿度を制御するガス制御手段を有することが好ましい。ガス制御手段を有することで、空気極および/または燃料極に供給されるガスが調節され、燃料電池セル内における発電性能の低下を抑えることができる。   The stacked fuel cell of the present invention preferably has gas control means for controlling the gas flow rate and / or humidity of the gas supplied to the air electrode and / or the fuel electrode. By having the gas control means, the gas supplied to the air electrode and / or the fuel electrode is adjusted, and a decrease in power generation performance in the fuel cell can be suppressed.

さらに、ガス制御手段は、演算手段と接続されたことが好ましい。ガス制御手段と演算手段とが接続されることで、電流分布から積層型燃料電池の運転条件を決定することができ、この運転条件にそった発電を行うことができる。   Furthermore, the gas control means is preferably connected to the calculation means. By connecting the gas control means and the calculation means, it is possible to determine the operating conditions of the stacked fuel cell from the current distribution, and it is possible to perform power generation according to the operating conditions.

本発明の積層型燃料電池は、燃料電池セル積層体の端部に磁気センサを配設した以外は、従来公知の積層型燃料電池と同様の構成とすることができる。また、本発明の積層型燃料電池は、燃料電池セルが積層したものであればその種類が限定されるものではないが、固体高分子型の燃料電池であることが好ましい。   The stacked fuel cell of the present invention can have the same configuration as a conventionally known stacked fuel cell except that a magnetic sensor is disposed at the end of the fuel cell stack. The type of the stacked fuel cell of the present invention is not limited as long as the fuel cells are stacked, but is preferably a solid polymer fuel cell.

本発明の積層型燃料電池の実施のひとつの形態を図1および図6〜10に示した。なお、以下に示す積層型燃料電池は、本発明の燃料電池のひとつの形態を示すものであり、本発明を限定するものではない。   One embodiment of the stacked fuel cell of the present invention is shown in FIG. 1 and FIGS. The laminated fuel cell shown below shows one form of the fuel cell of the present invention, and does not limit the present invention.

図6は燃料電池セル6の断面図である。燃料電池セル6は、電解質膜60の両側面に電極61,62が配置されたMEA(Membrane Electrode Assembly)と、このMEAを挟持する空気側セパレータ63および燃料側セパレータ64とで構成されている。ここで、空気側セパレータ63および燃料側セパレータ64は、導電性の材質よりなり、それぞれの極の集電板を兼ねている。この燃料電池セルにおいては、燃料側セパレータ64が−極の集電板を、空気側セパレータ63は+極の集電板を兼ねている。なお、図6は、燃料電池セル6の構成を模式的に示した図であり、実際には空気側セパレータ63および燃料側セパレータ64は電解質膜60よりはるかに厚くなっている。具体的には、セパレータ63,64はおおむね1〜2mmの厚さであり、MEAは電解質膜と拡散層と触媒の合計がおよそ0.5mmである。なお、電極61,62は、拡散層をも示している。この拡散層は、通常、0.2mm程度の厚さを有している。   FIG. 6 is a cross-sectional view of the fuel cell 6. The fuel cell 6 includes an MEA (Membrane Electrode Assembly) in which electrodes 61 and 62 are disposed on both side surfaces of the electrolyte membrane 60, and an air-side separator 63 and a fuel-side separator 64 that sandwich the MEA. Here, the air-side separator 63 and the fuel-side separator 64 are made of a conductive material and also serve as current collector plates for the respective electrodes. In this fuel cell, the fuel side separator 64 also serves as a negative electrode current collector plate, and the air side separator 63 also serves as a positive electrode current collector plate. FIG. 6 is a diagram schematically showing the configuration of the fuel battery cell 6, and the air-side separator 63 and the fuel-side separator 64 are actually much thicker than the electrolyte membrane 60. Specifically, the separators 63 and 64 have a thickness of about 1 to 2 mm, and the MEA has a total of about 0.5 mm of the electrolyte membrane, the diffusion layer, and the catalyst. The electrodes 61 and 62 also indicate diffusion layers. This diffusion layer usually has a thickness of about 0.2 mm.

図7は空気側セパレータ63を示した図であり、空気側セパレータ63は、積層したときに発電領域に空気を導入する空気導入流路を形成する空気流通孔630と、空気流通孔630に接続される空気入口部631と、積層したときに発電領域から空気を排出する空気排出流路を形成する空気排出孔634と、空気排出孔634と接続される空気出口部633と、空気出口部633に接続され空気入口部631から空気出口部633に向かって空気を流すための空気流路溝632とを備えている。また、空気側セパレータ63は、積層したときに水素導入流路を形成する水素流通孔635と、水素排出流路を形成する水素排出孔636とが形成されている。   FIG. 7 is a view showing the air-side separator 63, and the air-side separator 63 is connected to the air circulation hole 630 that forms an air introduction passage for introducing air into the power generation region when stacked. An air inlet portion 631, an air outlet hole 634 that forms an air outlet passage for discharging air from the power generation region when stacked, an air outlet portion 633 connected to the air outlet hole 634, and an air outlet portion 633. And an air flow path groove 632 for flowing air from the air inlet portion 631 toward the air outlet portion 633. Further, the air-side separator 63 is formed with a hydrogen circulation hole 635 that forms a hydrogen introduction channel when stacked and a hydrogen discharge hole 636 that forms a hydrogen discharge channel.

図8は燃料側セパレータ64を示した図であり、燃料側セパレータ64は、積層したときに発電領域に水素を導入する水素導入流路を形成する水素流通孔640と、水素流通孔640に接続される水素入口部641と、積層したときに発電領域から水素を排出する水素排出流路を形成する水素排出孔644と、水素排出孔644と接続される水素出口部643と、水素出口部643に接続され水素入口部641から水素出口部643に向かって水素を流すための水素流路溝642とを備えている。また、燃料側セパレータ64は、積層したときに空気導入流路を形成する空気流通孔645と、空気排出流路を形成する空気排出孔646とが形成されている。   FIG. 8 is a view showing the fuel-side separator 64, and the fuel-side separator 64 is connected to the hydrogen circulation hole 640 that forms a hydrogen introduction channel for introducing hydrogen into the power generation region when stacked, and the hydrogen circulation hole 640. A hydrogen inlet port 641, a hydrogen outlet hole 644 forming a hydrogen outlet channel for discharging hydrogen from the power generation region when stacked, a hydrogen outlet portion 643 connected to the hydrogen outlet hole 644, and a hydrogen outlet portion 643 And a hydrogen channel groove 642 for flowing hydrogen from the hydrogen inlet portion 641 toward the hydrogen outlet portion 643. In addition, the fuel separator 64 is formed with an air circulation hole 645 that forms an air introduction passage when stacked, and an air discharge hole 646 that forms an air discharge passage.

また、空気側セパレータ63および燃料側セパレータ64には、積層したときに冷却剤が流通する冷却剤流路を区画する冷却流路孔637,647がもうけられている。   The air-side separator 63 and the fuel-side separator 64 are provided with cooling flow path holes 637 and 647 that define a coolant flow path through which the coolant flows when stacked.

そして、この燃料電池セル6を空気側セパレータ63と燃料側セパレータ64とが背向した状態で50層程度を積層させて燃料電池セル積層体1が形成される。このとき、燃料電池セル積層体1の厚さ方向には、空気導入流路、空気排出流路、水素導入流路、水素排出流路、ならびに冷却剤流路がもうけられている。なお、空気側セパレータ63と燃料側セパレータ64とが一体をなすことが好ましい。   Then, the fuel cell stack 1 is formed by laminating about 50 layers of the fuel cell 6 with the air-side separator 63 and the fuel-side separator 64 facing away from each other. At this time, an air introduction channel, an air discharge channel, a hydrogen introduction channel, a hydrogen discharge channel, and a coolant channel are provided in the thickness direction of the fuel cell stack 1. Note that the air-side separator 63 and the fuel-side separator 64 are preferably integrated.

燃料電池セル積層体1の両端部には、金属板を所定形状に切り出してなる集電板2が配設されている。この集電板2は、燃料電池セル6の外周形状と略一致する外周形状の集電本体部20と、集電本体部20に一体にもうけられ燃料電池セル積層体1の外周から突出する端子部21と、を有している。   At both ends of the fuel cell stack 1, current collector plates 2 are formed by cutting a metal plate into a predetermined shape. The current collector plate 2 includes a current collector body 20 having an outer peripheral shape that substantially matches the outer peripheral shape of the fuel cell 6, and a terminal that is provided integrally with the current collector body 20 and protrudes from the outer periphery of the fuel cell stack 1. Part 21.

また、燃料電池セル積層体1は、気密性を確保するとともに燃料電池セル3の密着性を高めるために厚さ方向に加圧されている。この加圧は、絶縁板4を介した状態で加圧板5により燃料電池セル積層体1の厚さ方向に押圧することでなされた。   In addition, the fuel cell stack 1 is pressurized in the thickness direction in order to ensure airtightness and improve the adhesion of the fuel cells 3. This pressurization was performed by pressing in the thickness direction of the fuel cell stack 1 with the pressurizing plate 5 through the insulating plate 4.

絶縁板4は、集電本体部20と同じ形状を有するガラスエポキシ樹脂よりなり、複数の磁気センサ3が埋め込まれている。また、絶縁板4が配設されたときに、磁気センサ3は、集電板2と当接した。   The insulating plate 4 is made of a glass epoxy resin having the same shape as that of the current collector body 20, and a plurality of magnetic sensors 3 are embedded therein. Further, the magnetic sensor 3 was in contact with the current collector plate 2 when the insulating plate 4 was disposed.

そして、この磁気センサ3が配設された燃料電池セル積層体1の空気導入流路、空気排出流路、水素導入流路、水素排出流路、ならびに冷却剤流路のそれぞれを空気導入手段7A、空気排出手段7B、水素導入手段8A、水素排出手段8B、冷却剤導入手段(図示せず)、冷却剤排出手段(図示せず)のそれぞれに接続した。なお、これらの手段は、いずれも流量を調節する流量調節手段と、ガス中の水分量を調節する水分量調節手段と、を有するものである。   Then, each of the air introduction flow path, the air discharge flow path, the hydrogen introduction flow path, the hydrogen discharge flow path, and the coolant flow path of the fuel cell stack 1 in which the magnetic sensor 3 is disposed is connected to the air introduction means 7A. , Air discharge means 7B, hydrogen introduction means 8A, hydrogen discharge means 8B, coolant introduction means (not shown) and coolant discharge means (not shown). Each of these means has a flow rate adjusting means for adjusting the flow rate and a moisture content adjusting means for adjusting the moisture content in the gas.

そして、磁気センサ3を演算手段9に接続した。また、演算手段9は、各手段7A,7B,8A,8Bのそれぞれの流量調節手段および水分量調節手段に接続され、流量調節手段における流量および水分量調節手段におけるガスの水分量の調節を指示する。すなわち、演算手段9は、磁気センサ2において測定された磁界から燃料電池セル積層体1の電流分布を求め、発電能力の低下等により電流分布にかたよりが生じたときにその原因を判断し、電流分布のかたよりを解消できるように、燃料電池セル積層体へのガスの調節を行う。   Then, the magnetic sensor 3 was connected to the calculation means 9. The arithmetic means 9 is connected to the flow rate adjusting means and the moisture amount adjusting means of each means 7A, 7B, 8A, 8B, and instructs to adjust the flow rate in the flow rate adjusting means and the moisture content of the gas in the moisture amount adjusting means. To do. That is, the calculation means 9 obtains the current distribution of the fuel cell stack 1 from the magnetic field measured by the magnetic sensor 2, and determines the cause when the current distribution is caused by a decrease in power generation capacity or the like, The gas to the fuel cell stack is adjusted so as to eliminate the current distribution.

この積層型燃料電池の構成を図9に示した。   The structure of this stacked fuel cell is shown in FIG.

なお、本発明の積層型燃料電池は、磁気センサにより燃料電池セル積層体の磁界を測定することから、燃料電池全体を構成するための構造材料には、磁界(磁束密度分布)を乱さない低透磁率の材料を用いることが好ましい。このような材料として、オーステナイト系ステンレスを用いることが好ましい。オーステナイト系ステンレスを用いるときに、冷間加工による透磁率の上昇を磁気焼鈍等の処理により抑えることが好ましい。   Since the stacked fuel cell of the present invention measures the magnetic field of the fuel cell stack with a magnetic sensor, the structural material for constituting the entire fuel cell has a low magnetic field (magnetic flux density distribution). It is preferable to use a material having magnetic permeability. As such a material, it is preferable to use austenitic stainless steel. When using austenitic stainless steel, it is preferable to suppress an increase in magnetic permeability due to cold working by a process such as magnetic annealing.

(積層型燃料電池の運転方法)
本発明の積層型燃料電池の電流分布の運転方法は、電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設した燃料電池セル積層体と、燃料電池セル積層体の端部に配設された磁気センサと、を有する積層型燃料電池を運転する積層型燃料電池の運転方法であって、磁気センサにより測定される集電部材に流れる電流により発生する磁界から燃料電池セルにおける電流分布を算出し、燃料電池セル積層体へ供給されるガスの制御を行う。
(Operation method of stacked fuel cell)
The operation method of the current distribution of the stacked fuel cell according to the present invention includes a fuel cell in which an air electrode is joined to one surface of an electrolyte and a fuel electrode is joined to the other surface and sandwiched by a separator having a gas flow path. A fuel cell stack in which a current collecting member for stacking and collecting power in a direction perpendicular to the thickness direction stacked on the end of the stack is disposed; and a magnetic sensor disposed on an end of the fuel cell stack; A method for operating a stacked fuel cell, wherein a current distribution in a fuel cell is calculated from a magnetic field generated by a current flowing through a current collecting member measured by a magnetic sensor. The gas supplied to the cell stack is controlled.

本発明の運転方法は、上記積層型燃料電池において、燃料電池セルに部分的な発電能力の低下を生じさせることなく発電を行うことができる運転方法である。   The operation method of the present invention is an operation method capable of generating power without causing a partial decrease in power generation capacity of the fuel cell in the stacked fuel cell.

燃料電池は、電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルの空気極に酸素を含有する空気を、燃料極に水素を供給し、水素と酸素の電気化学反応により電気エネルギを発生させる。このため、燃料電池セルに供給される空気と水素の供給状況を調節することで、その発電能力を調節できる。   In a fuel cell, an air electrode is joined to one surface of an electrolyte, and a fuel electrode is joined to the other surface, and this is sandwiched by a separator having a gas flow path. Hydrogen is supplied to the electrode, and electric energy is generated by an electrochemical reaction between hydrogen and oxygen. For this reason, the power generation capacity can be adjusted by adjusting the supply status of air and hydrogen supplied to the fuel cells.

本発明の運転方法は、燃料電池セル積層体の集電部材の電流分布から燃料電池セルの発電能力が低下した部分を求め、その発電能力の低下の原因を判断し、燃料電池セル積層体に供給されるガスを制御するものである。このガスの制御を行うことで、発電能力の低下を解消できる。   The operation method of the present invention obtains a portion where the power generation capacity of the fuel cell is reduced from the current distribution of the current collecting member of the fuel cell stack, determines the cause of the decrease in the power generation capacity, The gas to be supplied is controlled. By controlling this gas, it is possible to eliminate a decrease in power generation capacity.

燃料電池は、空気極に空気を、燃料極に水素を供給し、酸素と水素の電気化学的な反応から電力を取り出すものであり、固体高分子型燃料電池においては水をプロトンの媒体として使用するため、燃料電池セルに供給されるガス(水素)は加湿されている。しかしながら、燃料電池において水分が過剰となると、余分な量の水分が発電を阻害して発電力が低下するようになる。   A fuel cell supplies air to the air electrode and hydrogen to the fuel electrode to extract electric power from the electrochemical reaction between oxygen and hydrogen. In solid polymer fuel cells, water is used as the proton medium. Therefore, the gas (hydrogen) supplied to the fuel cell is humidified. However, when the moisture is excessive in the fuel cell, an excessive amount of moisture inhibits power generation and the generated power is reduced.

すなわち、燃料電池セルにおいて部分的な発電能力の低下は、水分により生じると考えられる。さらに、この部分的な発電能力の低下は、燃料極側においては加湿された水素が導入される水素入り口部と、空気極側においては発電反応により発生した水が集まる空気出口部と、において起こりやすくなっている。   That is, it is considered that a partial decrease in power generation capacity in the fuel cell is caused by moisture. Further, this partial decrease in power generation capacity occurs at the hydrogen inlet where humidified hydrogen is introduced on the fuel electrode side, and at the air outlet where water generated by the power generation reaction collects on the air electrode side. It has become easier.

このため、燃料電池セル積層体の電流分布から、一部の発電能力が低下したときにその低下した位置がわかることとなる。すなわち、その発電能力の低下の原因を判断できる。そして、この発電能力の低下を解消するように燃料電池セル積層体に供給されるガスを調節することで、発電能力の低下を解消できる。   For this reason, from the current distribution of the fuel cell stack, when a part of the power generation capacity is reduced, the lowered position is known. That is, the cause of the decrease in power generation capacity can be determined. And the fall of a power generation capability can be eliminated by adjusting the gas supplied to a fuel cell laminated body so that this fall of a power generation capability may be eliminated.

本発明の積層型燃料電池の運転方法において、磁気センサは、燃料電池セル積層体の厚さ方向の略中央部に配設されることが好ましい。   In the operation method of the stacked fuel cell of the present invention, it is preferable that the magnetic sensor is disposed at a substantially central portion in the thickness direction of the fuel cell stack.

本発明の積層型燃料電池の運転方法において、複数個の磁気センサが配設されることが好ましい。   In the operation method of the stacked fuel cell of the present invention, it is preferable that a plurality of magnetic sensors are provided.

本発明の積層型燃料電池の運転方法のひとつの形態を以下に説明する。なお、本説明は、上記図1および図6〜9において示された積層型燃料電池を用いて説明する。   One embodiment of the operation method of the stacked fuel cell of the present invention will be described below. In addition, this description is demonstrated using the laminated | stacked fuel cell shown in the said FIG. 1 and FIGS.

まず、積層型燃料電池においては、燃料電池セル6の空気極61に空気が、燃料極62に加湿された水素が導入され、発電が行われている。発電領域の全面で適切な発電が行われているときには、燃料電池セル積層体1の厚さ方向に流れる電流の電流分布にはかたよりが生じていない。   First, in the stacked fuel cell, power is generated by introducing air into the air electrode 61 of the fuel battery cell 6 and humidified hydrogen into the fuel electrode 62. When appropriate power generation is performed on the entire surface of the power generation region, the current distribution of the current flowing in the thickness direction of the fuel cell stack 1 is not affected.

燃料極62には、加湿された水素(水分を含む水素ガス)が水素導入流路を介して導入される。水素に含まれる水分はプロトンの媒体としてはたらくため、水素が燃料側セパレータ64に区画された水素流路溝642を進むにつれて水分はプロトンの媒体として消費される。このため、水素入り口部641近傍から水素出口部643に向かってすすむにつれて水素流路溝642を流れる水素中の水分濃度は低下する。   Humidified hydrogen (water-containing hydrogen gas) is introduced into the fuel electrode 62 through a hydrogen introduction channel. Since the moisture contained in the hydrogen acts as a proton medium, the moisture is consumed as the proton medium as the hydrogen travels through the hydrogen flow channel 642 partitioned by the fuel-side separator 64. For this reason, the moisture concentration in the hydrogen flowing through the hydrogen flow channel groove 642 decreases as the process proceeds from the vicinity of the hydrogen inlet 641 toward the hydrogen outlet 643.

ここで、燃料極62に導入される水素中の水分量が多くなったとする。水素流路溝642の水素入り口部641の近傍における水素中の水分量が多くなる。そして、水素中の水分量が過剰となると、水素流路溝642の水素入り口部641の近傍における発電のための電気化学反応の進行を水分が阻害し、この部分における発電能力が低下する。この発電能力の低下は、燃料電池セル6の発電領域において発電される電力量にかたよりを生じさせる。そして、集電板2の集電本体部20のこの発電量が低下した部分に対応した領域には燃料電池セル積層体1から流れ込む電流が小さくなる。集電本体部20のこの領域およびこの領域と端子部21との間の領域に流れる電流量も小さくなる。すなわち、集電板2に流れる電流分布にかたよりが生じる。この電流分布のかたよりにより発生した磁界は、磁気センサ3により測定される。そして、磁気センサ2から演算手段9に測定データが送られ、演算手段9において電流分布のかたよりの発生およびその位置が算出される。そして、演算手段9においては、電流分布のかたよりの発生位置から、水素中の水分量が過剰となったことにより発電能力が低下したものと判断し、水素導入手段8Aおよび水素排出手段8Bに燃料電池セル6に導入される水素中の水分量を低下させる(適切な水分量とする)ように指示する。演算手段9からの指示により、それぞれの流量調節手段および水分量調節手段が調節されて、水素中の水分量が(減少された)適切な量とする。これにより、水素流路溝642の水素入り口部641の近傍における水素中の水分量が減少し、水分が発電のための電気化学反応の進行を阻害しなくなり、燃料電池セル6の発電領域において均一な発電が行われるようになる。   Here, it is assumed that the amount of water in the hydrogen introduced into the fuel electrode 62 has increased. The amount of water in the hydrogen in the vicinity of the hydrogen inlet 641 of the hydrogen flow channel 642 increases. If the amount of water in hydrogen becomes excessive, the water hinders the progress of the electrochemical reaction for power generation in the vicinity of the hydrogen inlet 641 of the hydrogen flow channel 642, and the power generation capacity in this portion decreases. This reduction in the power generation capacity is caused by the amount of power generated in the power generation region of the fuel cell 6. Then, the current flowing from the fuel cell stack 1 is reduced in the region corresponding to the portion where the power generation amount of the current collector main body 20 of the current collector plate 2 is reduced. The amount of current flowing in this region of the current collector main body 20 and the region between this region and the terminal portion 21 is also reduced. That is, there is a difference in the distribution of current flowing through the current collector plate 2. The magnetic field generated by this current distribution is measured by the magnetic sensor 3. Then, measurement data is sent from the magnetic sensor 2 to the calculation means 9, and the calculation means 9 calculates the generation and position of the current distribution. Then, the calculation means 9 determines that the power generation capacity has decreased due to the excessive amount of water in the hydrogen from the generation position based on the current distribution, and supplies the fuel to the hydrogen introduction means 8A and the hydrogen discharge means 8B. An instruction is given to reduce the amount of water in the hydrogen introduced into the battery cell 6 (set to an appropriate amount of water). In accordance with an instruction from the calculation means 9, the flow rate adjustment means and the water content adjustment means are adjusted so that the water content in hydrogen becomes an appropriate amount (reduced). As a result, the amount of water in the hydrogen in the vicinity of the hydrogen inlet 641 of the hydrogen channel groove 642 is reduced, and the water does not hinder the progress of the electrochemical reaction for power generation, and is uniform in the power generation region of the fuel cell 6. Power generation will be performed.

なお、水素中の水分量の不足は、積層型燃料電池の発電力と、水素排出手段8Bに排出された水素中の水分量から判断することができる。   Insufficient water content in hydrogen can be determined from the power generated by the stacked fuel cell and the water content in the hydrogen discharged to the hydrogen discharging means 8B.

また、空気極61で発電のための電気化学反応により生じた水分は、電解質60内を逆拡散し、燃料極63側に到達し、H+イオンをプロトンの状態で空気極61に引き連れていく。すなわち、空気出口部633近傍は、逆拡散した水分による発電能力の低下が発生しやすくなっている。 Further, the water generated by the electrochemical reaction for power generation at the air electrode 61 is reversely diffused in the electrolyte 60 and reaches the fuel electrode 63 side, and H + ions are drawn to the air electrode 61 in a proton state. . That is, in the vicinity of the air outlet 633, a decrease in power generation capacity due to the back-diffused moisture is likely to occur.

電解質60を透過した水分が多くなると、空気流路溝632中の水分量が多くなる。そして、空気流路溝632中の水分量が過剰となると、逆浸透により燃料極64側に水分が移動し、空気流路溝632の空気出口部633の近傍における発電のための電気化学反応の進行を水分が阻害し、この部分における発電能力が低下する。この発電能力の低下は、燃料電池セル積層体1の電流分布にかたよりを生じさせ、さらには集電板2に流れる電流分布にかたよりを生じさせる。この電流分布のかたよりにより発生した磁界は、磁気センサ3により測定される。そして、磁気センサ2から演算手段9に測定データが送られ、演算手段9において電流分布のかたよりおよびその発生位置を算出する。そして、電流分布のかたよりの発生位置から、空気流路溝632中の水分量が過剰となったことにより発電能力が低下したものと判断し、空気導入手段7Aおよび空気排出手段7Bに燃料電池セル6に導入される空気中の水分量を低下させて適切な水分量とするように指示し、それぞれの流量調節手段および水分量調節手段が適切な水分量とする。このとき、同時に水素挿入手段8Aおよび水素排出手段8Bに水素中の水分量の調節を指示させてもよい。これにより、空気中の水分量が過剰となることによる発電能力の低下が抑えられ、積層型燃料電池の最適な発電状態が維持できる。   When the moisture permeated through the electrolyte 60 increases, the amount of moisture in the air flow channel groove 632 increases. When the amount of water in the air flow channel groove 632 becomes excessive, the water moves to the fuel electrode 64 side by reverse osmosis, and an electrochemical reaction for power generation near the air outlet 633 of the air flow channel groove 632 occurs. Moisture inhibits the progress, and the power generation capacity in this part decreases. This decrease in the power generation capacity causes the current distribution of the fuel cell stack 1 and further causes the current distribution flowing through the current collector plate 2. The magnetic field generated by this current distribution is measured by the magnetic sensor 3. Then, measurement data is sent from the magnetic sensor 2 to the calculation means 9, and the calculation means 9 calculates the current distribution and its generation position. Then, it is determined from the generation position based on the current distribution that the power generation capacity has decreased due to an excessive amount of water in the air flow channel groove 632, and the fuel cell is connected to the air introduction means 7 A and the air discharge means 7 B. 6 is instructed to reduce the amount of moisture in the air introduced to an appropriate amount of water, and the respective flow rate adjusting means and moisture amount adjusting means set the appropriate amount of water. At this time, the hydrogen insertion means 8A and the hydrogen discharge means 8B may be simultaneously instructed to adjust the amount of water in the hydrogen. As a result, a decrease in power generation capacity due to an excessive amount of moisture in the air can be suppressed, and an optimal power generation state of the stacked fuel cell can be maintained.

上記したように、燃料電池セル積層体1の端部に配設された磁気センサ2により集電板2の電流分布を測定し、その電流分布から燃料電池セル積層体1に供給されるガス(空気あるいは水素)を調節することで、積層型燃料電池は最適な運転状況が維持された。積層型燃料電池が最適な運転状況で運転されることで、高い発電力を保った発電を行うことができた。   As described above, the current distribution of the current collector plate 2 is measured by the magnetic sensor 2 disposed at the end portion of the fuel cell stack 1, and the gas supplied to the fuel cell stack 1 from the current distribution ( By adjusting the air or hydrogen), the stacked fuel cell was maintained in an optimal operating condition. When the stacked fuel cell is operated in an optimal operating condition, it was possible to generate power while maintaining high power generation.

燃料電池セル積層体の電流の流れを示した図である。It is the figure which showed the flow of the electric current of a fuel cell laminated body. 集電坂内を流れる電流を示した図である。It is the figure which showed the electric current which flows through the current collection slope. 集電板に磁界が発生した状態を示した図である。It is the figure which showed the state which the magnetic field generate | occur | produced on the current collecting plate. 一部に発電停止領域を有する燃料電池セル積層体の集電板に流れる電流を示した図である。It is the figure which showed the electric current which flows into the collector plate of the fuel cell laminated body which has a power generation stop area | region in part. 一部に発電停止領域を有する燃料電池セル積層体の集電板に磁界が発生した状態を示した図である。It is the figure which showed the state which the magnetic field generate | occur | produced in the current collection board of the fuel cell laminated body which has a power generation stop area | region in part. 燃料電池セルの断面図である。It is sectional drawing of a fuel battery cell. 空気側セパレータを示した図である。It is the figure which showed the air side separator. 燃料側セパレータを示した図である。It is the figure which showed the fuel side separator. 積層型燃料電池の構成を示した図である。It is the figure which showed the structure of the laminated fuel cell.

符号の説明Explanation of symbols

1…燃料電池セル積層体
2…集電板
3…磁気センサ
4…絶縁板
5…加圧板
6…燃料電池セル 60…電解質
61…空気極 62…燃料極
63…空気側セパレータ 64…燃料側セパレータ
630…空気流通孔 631…空気入口部
632…空気流路溝 633…空気出口部
634…空気排出孔 635…水素流通孔
636…水素排出孔 637…冷却流路孔
640…水素流通孔 641…水素入口部
642…水素流路溝 643…水素出口部
644…水素排出孔 645…空気流通孔
646…空気排出孔 647…冷却流路孔
7A…空気導入手段 7B…空気排出手段
8A…水素導入手段 8B…水素排出手段
9…演算手段
DESCRIPTION OF SYMBOLS 1 ... Fuel cell laminated body 2 ... Current collecting plate 3 ... Magnetic sensor 4 ... Insulating plate 5 ... Pressure plate 6 ... Fuel cell 60 ... Electrolyte 61 ... Air electrode 62 ... Fuel electrode 63 ... Air side separator 64 ... Fuel side separator 630 ... Air circulation hole 631 ... Air inlet part 632 ... Air channel groove 633 ... Air outlet part 634 ... Air outlet hole 635 ... Hydrogen outlet hole 636 ... Hydrogen outlet hole 637 ... Cooling channel hole 640 ... Hydrogen passage hole 641 ... Hydrogen Inlet part 642 ... Hydrogen flow path groove 643 ... Hydrogen outlet part 644 ... Hydrogen discharge hole 645 ... Air flow hole 646 ... Air discharge hole 647 ... Cooling flow path hole 7A ... Air introduction means 7B ... Air discharge means 8A ... Hydrogen introduction means 8B ... Hydrogen discharge means 9 ... Calculation means

Claims (11)

電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設した燃料電池セル積層体を有する積層型燃料電池の電流分布の測定方法であって、
該燃料電池セル積層体の該厚さ方向の端部に磁気センサを配設し、該集電部材に電気が流れるときに発生する磁界を該磁気センサにより測定し、測定された磁界から該燃料電池セル積層体の電流分布を測定することを特徴とする積層型燃料電池の電流分布の測定方法。
An air electrode is joined to one surface of the electrolyte, and a fuel electrode is joined to the other surface, and fuel cells sandwiched between them by a separator having a gas flow path are stacked, and perpendicular to the thickness direction stacked at the end. A method for measuring the current distribution of a stacked fuel cell having a fuel cell stack in which a current collecting member for extracting electric power in a direction is provided,
A magnetic sensor is disposed at the end of the fuel cell stack in the thickness direction, and a magnetic field generated when electricity flows through the current collecting member is measured by the magnetic sensor, and the fuel is measured from the measured magnetic field. A method for measuring a current distribution of a stacked fuel cell, comprising measuring a current distribution of a battery cell stack.
前記集電部材が集電板により形成され、
前記磁気センサは、該集電板の磁界を測定する請求項1記載の積層型燃料電池の電流分布の測定方法。
The current collecting member is formed by a current collecting plate;
The method of measuring a current distribution of a stacked fuel cell according to claim 1, wherein the magnetic sensor measures a magnetic field of the current collector plate.
複数個の前記磁気センサが配設される請求項1記載の積層型燃料電池の電流分布の測定方法。   The method of measuring a current distribution of a stacked fuel cell according to claim 1, wherein a plurality of the magnetic sensors are provided. 電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設した燃料電池セル積層体と、
該燃料電池セル積層体の端部に配設された磁気センサと、
を有することを特徴とする積層型燃料電池。
An air electrode is joined to one surface of the electrolyte, and a fuel electrode is joined to the other surface, and fuel cells sandwiched between them by a separator having a gas flow path are stacked, and perpendicular to the thickness direction stacked at the end. A fuel cell stack having a current collecting member for extracting electric power in the direction;
A magnetic sensor disposed at an end of the fuel cell stack;
A stacked fuel cell comprising:
前記集電部材が集電板により形成され、
前記磁気センサは、該集電板の磁界を測定する請求項4記載の積層型燃料電池。
The current collecting member is formed by a current collecting plate;
The stacked fuel cell according to claim 4, wherein the magnetic sensor measures a magnetic field of the current collector plate.
複数個の前記磁気センサが配設される請求項4記載の積層型燃料電池。   The stacked fuel cell according to claim 4, wherein a plurality of the magnetic sensors are disposed. 前記磁気センサの測定値から電流分布を算出する演算手段を有する請求項4記載の積層型燃料電池。   The stacked fuel cell according to claim 4, further comprising calculation means for calculating a current distribution from a measurement value of the magnetic sensor. 電解質の一方の面に空気極を他方の面に燃料極を接合し、これをガス流路を備えたセパレータで挟持した燃料電池セルを積層し、その端部に積層した厚さ方向と垂直な方向に電力を取り出す集電部材を配設した燃料電池セル積層体と、該燃料電池セル積層体の端部に配設された磁気センサと、を有する積層型燃料電池を運転する積層型燃料電池の運転方法であって、
該磁気センサにより測定される該集電部材に流れる電流により発生する磁界から該燃料電池セルにおける電流分布を算出し、該燃料電池セル積層体へ供給されるガスの制御を行うことを特徴とする積層型燃料電池の運転方法。
An air electrode is joined to one surface of the electrolyte, and a fuel electrode is joined to the other surface, and fuel cells sandwiched between them by a separator having a gas flow path are stacked, and perpendicular to the thickness direction stacked at the end. A stacked fuel cell for operating a stacked fuel cell having a fuel cell stack having a current collecting member for extracting electric power in a direction and a magnetic sensor disposed at an end of the fuel cell stack Driving method,
A current distribution in the fuel cell is calculated from a magnetic field generated by a current flowing through the current collecting member measured by the magnetic sensor, and a gas supplied to the fuel cell stack is controlled. Operation method of stacked fuel cell.
前記集電部材が集電板により形成され、
前記磁気センサは、該集電板の磁界を測定する請求項8記載の積層型燃料電池の運転方法。
The current collecting member is formed by a current collecting plate;
The method of operating a stacked fuel cell according to claim 8, wherein the magnetic sensor measures a magnetic field of the current collector plate.
複数個の前記磁気センサが配設される請求項8記載の積層型燃料電池の運転方法。   The operation method of the stacked fuel cell according to claim 8, wherein a plurality of the magnetic sensors are provided. 前記ガスの制御は、前記空気極および/または前記燃料極に供給される前記ガスのガス流量および/または湿度を制御することでなされる請求項8記載の積層型燃料電池の運転方法。   The operation method of the stacked fuel cell according to claim 8, wherein the gas is controlled by controlling a gas flow rate and / or humidity of the gas supplied to the air electrode and / or the fuel electrode.
JP2003418230A 2003-12-16 2003-12-16 Method for measuring current distribution of stacked fuel cell, stacked fuel cell, and operation method of stacked fuel cell Expired - Fee Related JP4926372B2 (en)

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JP2007200674A (en) * 2006-01-26 2007-08-09 Toyota Motor Corp Fuel cell stack
JP2007200675A (en) * 2006-01-26 2007-08-09 Toyota Motor Corp Method and apparatus for operating fuel cell stack
JP2008066120A (en) * 2006-09-07 2008-03-21 Nissan Motor Co Ltd Fuel cell system
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JP2012053000A (en) * 2010-09-03 2012-03-15 Pulstec Industrial Co Ltd Current distribution measurement device
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007179901A (en) * 2005-12-28 2007-07-12 Nippon Soken Inc Fuel cell current measurement system and current measurement method
JP2007200674A (en) * 2006-01-26 2007-08-09 Toyota Motor Corp Fuel cell stack
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