JPH0227789B2 - - Google Patents
Info
- Publication number
- JPH0227789B2 JPH0227789B2 JP57048380A JP4838082A JPH0227789B2 JP H0227789 B2 JPH0227789 B2 JP H0227789B2 JP 57048380 A JP57048380 A JP 57048380A JP 4838082 A JP4838082 A JP 4838082A JP H0227789 B2 JPH0227789 B2 JP H0227789B2
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- line
- air
- fuel
- fuel gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04104—Regulation of differential pressures
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Description
【発明の詳細な説明】
この発明は電解液を保持したマトリツクス層を
挾んでその両側に燃料電極および空気電極を対向
配置してなる燃料電池本体に対し、各電極へそれ
ぞれ燃料ガスラインおよび空気ラインを通じて燃
料ガス、空気を送り込むように構成された燃料電
池の供給ガス圧力制御方式の改良に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a fuel cell body comprising a matrix layer holding an electrolyte and a fuel electrode and an air electrode arranged oppositely on both sides thereof, and a fuel gas line and an air line connected to each electrode. The present invention relates to an improvement in a supply gas pressure control method for a fuel cell configured to feed fuel gas and air through the fuel cell.
よく知られているようにこの種の燃料電池の本
体は、互に隔置されたアノードとカソードの2枚
の電極間に電解液を保持させた多孔性のマトリツ
クス層が置かれて構成されている。このマトリツ
クス層は、多孔質材料で作られており、かつ微細
孔中に電解液を保持させる構造となつている。こ
のようなマトリツクス型燃料電池の運転に関して
は、電池に供給する燃料ガス(例えば水素)及び
酸化剤(例えば空気)の圧力制御が極めて重要な
問題となる。例えば燃料ガスが電解液保持層であ
るマトリツクス層を透過して隔置された対極に到
達すれば、燃料電池の電気的特性を低下させるば
かりでなく、燃料ガスと空気が混合して爆鳴気を
つくり、爆発事故を引きおこす可能性を含んでい
る。また、逆に空気がマトリツクス層を透過して
対極に到達した場合にも、同様な危険性を含んで
いる。これに対し電解液を保持するマトリツクス
層は、それ自身で一方の電極側から他方への電極
側に反応ガスが移行するのを抑制するある程度の
泡圧力を有しているとは言え、これには限界があ
るし、加えてマトリツクス層は機械的強度が弱
く、かつもろいものであることから、マトリツク
ス層を挾む両側の燃料ガス圧と空気圧との間の圧
力差が許容限界を超えると、一方から他方へマト
リツクス層を透過して前述した燃料ガスと空気の
混合による危険、およびマトリツクス層の破損、
寿命低下を引き起す。しかも電池本体におけるこ
の圧力差の許容範囲は水柱数十ミリメートル程度
と極めて小さく、このことから燃料電池における
ガス供給系統では、燃料ガスラインおよび空気ラ
インを通じて燃料電池へ送り込む燃料ガス圧と空
気圧との間に過大な圧力差が生じないように電池
入口側のガス圧に対して1/1000オーダーの極めて
高い精度による供給ガスの圧力制御が要求され
る。またこの場合にガス供給系に不測な事態が生
じて圧力変動が生じた際にも、燃料ガスと空気と
が互に直接混合し合わない保証が望まれる。 As is well known, the main body of this type of fuel cell consists of a porous matrix layer holding an electrolyte between two electrodes, an anode and a cathode, which are spaced apart from each other. There is. This matrix layer is made of a porous material and has a structure in which the electrolyte is held in the micropores. Regarding the operation of such a matrix fuel cell, pressure control of the fuel gas (for example, hydrogen) and the oxidant (for example, air) supplied to the cell is an extremely important issue. For example, if fuel gas passes through the matrix layer that holds the electrolyte and reaches the spaced-apart counter electrode, it not only deteriorates the electrical characteristics of the fuel cell, but also causes the fuel gas and air to mix, resulting in an explosion. This includes the possibility of causing an explosion. Conversely, when air passes through the matrix layer and reaches the opposite electrode, there is a similar risk. On the other hand, although the matrix layer that holds the electrolyte has its own certain bubble pressure that suppresses the migration of the reactant gas from one electrode side to the other, In addition, the matrix layer has a weak mechanical strength and is brittle, so if the pressure difference between the fuel gas pressure and the air pressure on both sides of the matrix layer exceeds the allowable limit, The risk of the above-mentioned mixing of fuel gas and air passing through the matrix layer from one side to the other, and damage to the matrix layer.
This causes a decrease in lifespan. Moreover, the allowable range of this pressure difference in the cell body is extremely small, about several tens of millimeters of water column. Therefore, in the gas supply system of the fuel cell, the pressure difference between the fuel gas pressure and the air pressure that is sent to the fuel cell through the fuel gas line and air line is extremely small. The pressure of the supplied gas must be controlled with extremely high accuracy on the order of 1/1000 of the gas pressure at the cell inlet to prevent excessive pressure differences from occurring. In this case, it is also desirable to ensure that the fuel gas and air do not mix directly with each other even when pressure fluctuations occur due to an unexpected situation in the gas supply system.
ところで従来における燃料電池のガス供給系統
のガス圧力制御システムは第1図のように構成さ
れている。すなわち第1図において、10は電池
本体であり、燃料電極11、空気電極12、マト
リツクス層13、および燃料室14、空気室15
から構成されている。そして燃料室14、空気室
15にはそれぞれ燃料ガスライン20および空気
ライン30を通じて燃料ガスおよび空気が送り込
まれる。また各ライン20,30にはそれぞれ流
量および圧力調整器21,31、各種コントロー
ル弁22,23、および32,33等の圧力調節
手段が介挿接続されている。なお図中のベント2
4,34は凝縮器に通じ、ベント25,35は例
えば燃料ガスのリフオーマに通じるものである。
そして燃料ガスは図示されてないリフオーマを経
由し、空気は大気中からそれぞれブロア等により
加圧された状態で送風されてくる。上記のガス供
給系統に対するガス圧制御システムは、燃料ガス
ライン20と空気ライン30との間に差圧検出手
段としての差圧発信器40が接続されており、こ
の差圧発信器40の出力信号を基にフイードバツ
ク制御あるいは演算処理によつて、前記の圧力調
整器21,31および各ライン20,30からの
分岐ラインに介挿されたコントロール弁23,3
3等を作動して圧力制御を行うように構成されて
いる。そして燃料ガスライン20と空気ライン3
0との間で圧力のアンバランスが生じた場合に
は、電池本体10の入口側での燃料ガス圧と空気
圧との圧力差が許容値範囲に収まるように圧力制
御を行う。なお図中の41,42,43は差圧発
信器40の保守、点検、および零点調整を行うた
めにそれぞれ燃料ガスライン20、空気ライン3
0および両方のラインの間にまたがつて介挿され
た手動止弁であり、差圧発信器40の零点調整は
止弁41,42を閉じ、43を開いてライン2
0,30の電池本体側の圧力バランスを行つた状
態で行われる。また常時は止弁41と42が開、
43が閉の状態に保持されている。 By the way, a conventional gas pressure control system for a gas supply system of a fuel cell is configured as shown in FIG. That is, in FIG. 1, 10 is a battery main body, which includes a fuel electrode 11, an air electrode 12, a matrix layer 13, a fuel chamber 14, and an air chamber 15.
It consists of Fuel gas and air are fed into the fuel chamber 14 and the air chamber 15 through a fuel gas line 20 and an air line 30, respectively. Further, pressure regulating means such as flow rate and pressure regulators 21, 31, various control valves 22, 23, and 32, 33 are inserted and connected to each line 20, 30, respectively. In addition, vent 2 in the diagram
4 and 34 communicate with a condenser, and vents 25 and 35 communicate with, for example, a fuel gas reformer.
The fuel gas passes through a reformer (not shown), and the air is blown from the atmosphere in a pressurized state by a blower or the like. In the gas pressure control system for the gas supply system described above, a differential pressure transmitter 40 as differential pressure detection means is connected between the fuel gas line 20 and the air line 30, and the output signal of the differential pressure transmitter 40 is connected to the fuel gas line 20 and the air line 30. The control valves 23 and 3 inserted into the pressure regulators 21 and 31 and the branch lines from the respective lines 20 and 30 are controlled by feedback control or arithmetic processing based on the above.
3, etc., to perform pressure control. and fuel gas line 20 and air line 3
0, the pressure is controlled so that the pressure difference between the fuel gas pressure and the air pressure on the inlet side of the battery main body 10 falls within an allowable value range. Note that 41, 42, and 43 in the figure are a fuel gas line 20 and an air line 3, respectively, for maintenance, inspection, and zero point adjustment of the differential pressure transmitter 40.
This is a manual stop valve inserted between the line 2 and both lines, and the zero point adjustment of the differential pressure transmitter 40 is performed by closing the stop valves 41 and 42 and opening line 2.
This is done with the pressure balanced on the battery main body side at 0.0 and 30. Also, stop valves 41 and 42 are always open.
43 is held in the closed state.
しかして上従従来の圧力制御システムでは、電
池の運転中に差圧発信器40の点検、零点調整を
行うことは極めて危険であり、これを行うことが
できなかつた。その理由は、止弁43を開くと、
燃料ガスと空気とが直接混合し合つて爆発事故を
招く可能性があるためである。また上記システム
では、保守要員が運転中に誤まつて止弁43を開
いても同様な危険があり、このことが圧力制御シ
ステムにおける安全面での重大な欠点となつてい
る。更に上記システムでは、燃料ガス圧と空気圧
との間の相対的な差圧のみを検出して制御を行つ
ているので、燃料電池の運転に要求される供給ガ
ス圧の制御に対しては各ラインごとに別な制御系
を設けて行わなければならない。このために二つ
の制御系統の制御動作が互に干渉し合つてハンチ
ング現象を引き起したりして、要求される高精度
な圧力制御を行うことが極めて困難となる。 However, in the conventional pressure control systems, it is extremely dangerous to inspect the differential pressure transmitter 40 and adjust the zero point while the battery is in operation, and it has not been possible to do so. The reason is that when the stop valve 43 is opened,
This is because there is a possibility that the fuel gas and air will directly mix with each other, leading to an explosion accident. Further, in the above system, there is a similar danger if maintenance personnel accidentally open the stop valve 43 during operation, and this is a serious drawback in terms of safety in the pressure control system. Furthermore, in the above system, control is performed by detecting only the relative pressure difference between fuel gas pressure and air pressure, so each line is required to control the supply gas pressure required for fuel cell operation. A separate control system must be installed for each. For this reason, the control operations of the two control systems interfere with each other, causing a hunting phenomenon, making it extremely difficult to perform the required high-precision pressure control.
この発明は上記の点にかんがみなされたもので
あり、その目的は従来方式の欠点を除去し、燃料
ガスと空気との直接混合の恐れがなく、しかも同
時に燃料ガスと空気の差圧制御および供給圧力制
御を行うことができる等、安全性並びに制御精度
の面で高い信頼性の得られる供給ガス圧力制御方
式を提供することにある。 This invention was made in consideration of the above points, and its purpose is to eliminate the drawbacks of the conventional method, eliminate the fear of direct mixing of fuel gas and air, and simultaneously control and supply the differential pressure between fuel gas and air. It is an object of the present invention to provide a supply gas pressure control method that is highly reliable in terms of safety and control accuracy, such as being able to perform pressure control.
かかる目的は、電解液を保持したマトリツクス
層を挟んで燃料電極および空気電極を対極させて
なる電池本体の各電極へそれぞれ圧力調整器を備
えた燃料ガスラインおよび空気ラインを通じて燃
料、空気を供給し、前記燃料ガスラインおよび空
気ラインとは別に、圧力調整器を備えた不活性ガ
スラインを設けて、該不活性ガスラインを通じて
前記燃料電池本体を収容した容器内へ不活性ガス
を供給するようにした燃料電池の供給ガス圧力制
御装置であつて、前記燃料ガスラインおよび空気
ラインがそれぞれ有する分岐ラインに設けられた
コントロール弁と、前記不活性ガスラインと前記
燃料ガスラインおよび空気ラインとの間にそれぞ
れ設けられたコントロール弁と、前記不活性ガス
ラインと前記燃料ガスラインおよび空気ラインと
の間にそれぞれ設けられた差圧検出手段とを備
え、該差圧検出手段で得た差圧信号を基に、電池
本体の燃料ガス圧と空気圧、および燃料ガス圧と
空気圧との間の差圧がそれぞれ設定値および許容
範囲に収まるように前記コントロール弁および圧
力調整器を制御するようにしたことにより達成さ
れる。 This purpose is to supply fuel and air to each electrode of the battery body, which consists of a fuel electrode and an air electrode as opposite electrodes with a matrix layer holding an electrolyte in between, through a fuel gas line and an air line each equipped with a pressure regulator. , an inert gas line equipped with a pressure regulator is provided separately from the fuel gas line and the air line, and inert gas is supplied into the container housing the fuel cell main body through the inert gas line. A supply gas pressure control device for a fuel cell comprising: a control valve provided in a branch line of the fuel gas line and the air line, and between the inert gas line and the fuel gas line and the air line; control valves provided respectively, and differential pressure detection means provided respectively between the inert gas line and the fuel gas line and air line, and based on the differential pressure signal obtained by the differential pressure detection means. This is achieved by controlling the control valve and pressure regulator so that the fuel gas pressure and air pressure in the battery body, and the differential pressure between the fuel gas pressure and air pressure, respectively, fall within set values and allowable ranges. be done.
以下この発明を図示実施例に基づき詳述する。 The present invention will be described in detail below based on illustrated embodiments.
第2図において、この発明により燃料ガスライ
ン20、空気ライン30とは別個に、新たに例え
ば窒素ガスを用いた不活性ガスライン50が設け
られている。この不活性ガスライン50は一方に
おいて窒素ガス圧力源に接続され、かつ電池本体
10を収容した圧力容器16にも接続して圧力容
器内を不活性ガス雰囲気に保つ。また圧力源側に
は圧力調整器51が介挿され、更に燃料ガスライ
ン20および空気ライン30との相互間を結んで
それぞれコントロール弁52,53を介挿したバ
イパス管路54,55が配管されている。56は
排ガス系に通じるベントである。かかるガス供給
系統に対し、まず不活性ガスライン50のガス圧
は圧力設定器57に与えられた設定値にしたが
い、圧力調整器51を介して所定の圧力に保持さ
れる。この圧力は燃料電池の運転に要求される反
応ガスの供給ガス圧を基に定められている。また
不活性ガスライン50と燃料ガスライン20との
間、および不活性ガスライン50と空気ライン3
0との間に架け渡して、それぞれ圧力センサおよ
びび演算装置を具備した差圧発信器60および7
0が接続され、その出力信号が差圧発信器60に
ついては圧力調整器21とコントロール弁23,
52に、また差圧発信器70については圧力調整
器31とコントロール弁33,53に与えられる
ように制御回路が構成されている。また図示のよ
うに介挿された手動止弁61,62,71,72
および58は差圧発信器60,70の保守、点検
および零点調整を行う際に操作されるものであ
り、通常は止弁61,71,58が開、止弁6
2,72が閉に保持されている。 In FIG. 2, according to the present invention, an inert gas line 50 using nitrogen gas, for example, is newly provided separately from the fuel gas line 20 and the air line 30. This inert gas line 50 is connected on one side to a nitrogen gas pressure source and also connected to the pressure vessel 16 housing the battery body 10 to maintain an inert gas atmosphere inside the pressure vessel. Further, a pressure regulator 51 is inserted on the pressure source side, and bypass pipes 54 and 55 are connected to the fuel gas line 20 and the air line 30 and have control valves 52 and 53 inserted therein, respectively. ing. 56 is a vent leading to the exhaust gas system. In such a gas supply system, the gas pressure in the inert gas line 50 is first maintained at a predetermined pressure via the pressure regulator 51 in accordance with the setting value given to the pressure setting device 57. This pressure is determined based on the reactant gas supply gas pressure required for operation of the fuel cell. Also, between the inert gas line 50 and the fuel gas line 20, and between the inert gas line 50 and the air line 3
differential pressure transmitters 60 and 7 each equipped with a pressure sensor and an arithmetic device;
0 is connected, and its output signal is transmitted to the pressure regulator 21 and control valve 23 for the differential pressure transmitter 60.
52, and a control circuit is configured to be applied to the pressure regulator 31 and control valves 33, 53 for the differential pressure transmitter 70. In addition, manual stop valves 61, 62, 71, 72 are inserted as shown in the figure.
and 58 are operated when performing maintenance, inspection, and zero point adjustment of the differential pressure transmitters 60, 70, and normally the stop valves 61, 71, 58 are open, and the stop valve 6 is closed.
2,72 are held closed.
上記構成において、今燃料ガスラインの電池入
口圧力が不活性ガスライン50の入口圧力より高
圧になつたとすると、差圧発信器60は圧力調整
器に制御信号を与えるとともに、コントロール弁
23を開くように指令を出してガスの排出量を増
し、燃料ガスラインと不活性ガスラインの電池入
口での圧力差はあらかじめ設定されてある所定の
範囲内におさまるように圧力制御される。また逆
に燃料ガスラインのガス圧力が不活性ガスライン
のガス圧力より低圧になつた場合には、差圧発信
器60は圧力調整器21に圧力を高める指令を与
えるとともに、一方ではコントロール弁52を開
くように指令を出し、この結果窒素ガスが、燃料
ガスライン20に供給されて燃料ガスラインの圧
力を高め、燃料ガスと窒素ガスとの相対的な圧力
差はあらかじめ設定されてある所定の範囲内にお
さまる。一方空気ライン30と不活性ガスライン
50との間でも同様な圧力制御が行なわれ、かく
して燃料ガス圧と空気圧との間の相対的な圧力差
は許容の範囲内におさまるようになる。差圧発信
器60の零点調整については、止弁61と58を
閉じて62を開くことにより、下流側域で燃料ガ
スライン20と不活性ガスライン50との間の圧
力をバランスさせて行う。これに対し差圧発信器
70での零点調整は、止弁58,71を閉じ、止
弁72を開いて行う。しかしていずれの場合にも
必ず不活性ガスライン50との間で行うので、燃
料ガスと空気とが直接混合し合う恐れはない。ま
た電池へ供給する燃料ガスおよび空気の供給圧力
の圧力制御は、不活性ガスライン50における圧
力設定器57に与える設定値を、電池の運転に必
要な所定のガス圧に合わせて定めることにより、
この設定値を基準にして前述した差圧制御と併せ
て同時に行われることになる。すなわち従来では
燃料ガスと空気の間の差圧制御系と、供給ガス圧
制御系とが別々であつたのを、同じ制御系で同時
に制御することができ、それだけ高精度での圧力
制御が可能となる。 In the above configuration, if the cell inlet pressure of the fuel gas line is now higher than the inlet pressure of the inert gas line 50, the differential pressure transmitter 60 gives a control signal to the pressure regulator and causes the control valve 23 to open. The pressure is controlled so that the pressure difference between the fuel gas line and the inert gas line at the cell inlet is within a predetermined range. Conversely, when the gas pressure in the fuel gas line becomes lower than the gas pressure in the inert gas line, the differential pressure transmitter 60 gives a command to the pressure regulator 21 to increase the pressure, and on the other hand, the control valve 52 As a result, nitrogen gas is supplied to the fuel gas line 20 to increase the pressure in the fuel gas line, and the relative pressure difference between the fuel gas and nitrogen gas is increased to a predetermined preset value. Stay within range. On the other hand, similar pressure control is performed between the air line 30 and the inert gas line 50, so that the relative pressure difference between the fuel gas pressure and the air pressure is within an acceptable range. The zero point adjustment of the differential pressure transmitter 60 is performed by closing the stop valves 61 and 58 and opening the stop valve 62 to balance the pressure between the fuel gas line 20 and the inert gas line 50 in the downstream region. On the other hand, zero point adjustment by the differential pressure transmitter 70 is performed by closing the stop valves 58 and 71 and opening the stop valve 72. In either case, the fuel gas and air are always mixed together with the inert gas line 50, so there is no fear that the fuel gas and air will mix directly with each other. In addition, the supply pressure of fuel gas and air supplied to the battery can be controlled by setting the setting value given to the pressure setting device 57 in the inert gas line 50 in accordance with a predetermined gas pressure necessary for battery operation.
Based on this set value, the differential pressure control described above is performed at the same time. In other words, the differential pressure control system between fuel gas and air and the supply gas pressure control system, which were previously separate, can be controlled simultaneously by the same control system, making it possible to control the pressure with higher precision. becomes.
以上述べたようにこの発明の圧力制御方式によ
れば、不活性ガスラインを介して燃料ガスライン
と空気ラインとの間の差圧制御を行なつているた
めに、従来の方式の欠点であつた燃料と空気の直
接混合を、確実に防ぐことが出来るようになる。
また燃料ガスラインと空気ラインとの間に不活性
ガスラインを介在しているために、弁の操作のミ
スなどによる燃料ガスと空気との直接混合がなく
なり、それだけ信頼性の高い圧力制御が可能とな
る。 As described above, according to the pressure control method of the present invention, the differential pressure between the fuel gas line and the air line is controlled via the inert gas line, which eliminates the drawbacks of conventional methods. This makes it possible to reliably prevent direct mixing of fuel and air.
In addition, since an inert gas line is interposed between the fuel gas line and the air line, there is no direct mixing of fuel gas and air due to valve operation errors, etc., and highly reliable pressure control is possible. becomes.
またこの発明は、今までに説明した燃料ガスと
空気との直接混合がなく、信頼性の高い圧力制御
が出来るという効果の他に、不活性ガスラインの
ガス圧を基準にして燃料ガスラインと空気ライン
との間でそれぞれの差圧制御を行うようにし、か
つ燃料ガスラインまたは空気ラインの圧力が低い
場合に、不活性ガスラインと燃料ガスラインまた
は空気ラインとの間にそれぞれ設けられたコント
ロール弁により制御された不活性ガスが、前記燃
料ガスラインまたは空気ラインに供給されて、圧
力を適正にコントロールするようにしているの
で、燃料ガスラインまたは空気ラインに設けられ
た圧力調節器の応答が遅い場合においても、極め
て精度の高い燃料電池の供給ガス圧力制御が可能
となり、燃料電池の高圧での運転にも充分な信頼
性が得られる。つまり予め不活性ガスラインの圧
力を所定の圧力に設定しておけば、電池本体に供
給される燃料ガス圧力と空気の圧力との差圧が、
マトリツクス層の機械的な保護、およびマトリツ
クス層の泡圧力保持の見地から定められた許容範
囲に収まるようにした差圧制御と同時に、前記の
不活性ガスラインで設定されたガス圧力を基準に
して燃料ガスおよび空気の電池入口側の供給圧力
を設定値に合わせるように圧力制御が行える。か
くしてより信頼性の高い燃料電池の運転が達成で
きる。 In addition to the effect that there is no direct mixing of fuel gas and air as described above and highly reliable pressure control, this invention also has the advantage that the fuel gas line is adjusted based on the gas pressure of the inert gas line. Controls are provided between the inert gas line and the fuel gas line or air line when the pressure of the fuel gas line or air line is low. An inert gas controlled by a valve is supplied to the fuel gas line or air line to properly control the pressure, so that the response of the pressure regulator installed in the fuel gas line or air line is Even when the speed is slow, it is possible to control the supply gas pressure of the fuel cell with extremely high accuracy, and sufficient reliability can be obtained even when the fuel cell is operated at high pressure. In other words, if the pressure of the inert gas line is set to a predetermined pressure in advance, the differential pressure between the fuel gas pressure supplied to the battery body and the air pressure will be
At the same time, the differential pressure is controlled to be within the permissible range determined from the viewpoint of mechanical protection of the matrix layer and bubble pressure maintenance of the matrix layer, and at the same time, the pressure is controlled based on the gas pressure set in the inert gas line. Pressure control can be performed to match the supply pressure of fuel gas and air at the cell inlet side to a set value. In this way, more reliable fuel cell operation can be achieved.
第1図および第2図はそれぞれ従来およびこの
発明の実施例による燃料電池の供給ガス圧力制御
システムの系統図である。
10:燃料電池本体、20:燃料ガスライン、
30:空気ライン、50:不活性ガスライン、2
1,31,51:圧力調整器、57:圧力設定
器、60,70:差圧検出手段としての差圧発信
器、23,33,52,53:コントロール弁、
58,61,62,71,72:手動止弁。
FIGS. 1 and 2 are system diagrams of a conventional fuel cell supply gas pressure control system and an embodiment of the present invention, respectively. 10: fuel cell main body, 20: fuel gas line,
30: Air line, 50: Inert gas line, 2
1, 31, 51: pressure regulator, 57: pressure setting device, 60, 70: differential pressure transmitter as differential pressure detection means, 23, 33, 52, 53: control valve,
58, 61, 62, 71, 72: Manual stop valve.
Claims (1)
料電極および空気電極を対極させてなる電池本体
の各電極へそれぞれ圧力調整器を備えた燃料ガス
ラインおよび空気ラインを通じて燃料、空気を供
給し、前記燃料ガスラインおよび空気ラインとは
別に、圧力調整器を備えた不活性ガスラインを設
けて、該不活性ガスラインを通じて前記燃料電池
本体を収容した容器内へ不活性ガスを供給するよ
うにした燃料電池の供給ガス圧力制御装置であつ
て、前記燃料ガスラインおよび空気ラインがそれ
ぞれ有する分岐ラインに設けられたコントロール
弁と、前記不活性ガスラインと前記燃料ガスライ
ンおよび空気ラインとの間にそれぞれ設けられた
コントロール弁と、前記不活性ガスラインと前記
燃料ガスラインおよび空気ラインとの間にそれぞ
れ設けられた差圧検出手段とを備え、該差圧検出
手段で得た差圧信号を基に、電池本体の燃料ガス
圧と空気圧、および燃料ガス圧と空気圧との間の
差圧がそれぞれ設定値および許容範囲に収まるよ
うに前記コントロール弁および圧力調整器を制御
するようにしたことを特徴とする燃料電池の供給
ガス圧力制御装置。1. Fuel and air are supplied to each electrode of the battery body, which is made up of a fuel electrode and an air electrode as opposite electrodes with a matrix layer holding an electrolyte in between, through a fuel gas line and an air line each equipped with a pressure regulator, and the fuel A fuel cell including an inert gas line equipped with a pressure regulator, separate from the gas line and the air line, and supplying inert gas into a container housing the fuel cell main body through the inert gas line. The supply gas pressure control device includes a control valve provided in a branch line of the fuel gas line and the air line, and a control valve provided between the inert gas line and the fuel gas line and the air line. a control valve, and differential pressure detection means provided between the inert gas line and the fuel gas line and the air line, respectively. The fuel is characterized in that the control valve and the pressure regulator are controlled so that the fuel gas pressure and air pressure of the main body and the differential pressure between the fuel gas pressure and air pressure are respectively within set values and allowable ranges. Battery supply gas pressure control device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57048380A JPS58165270A (en) | 1982-03-26 | 1982-03-26 | Pressure control system of supply gas to fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57048380A JPS58165270A (en) | 1982-03-26 | 1982-03-26 | Pressure control system of supply gas to fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58165270A JPS58165270A (en) | 1983-09-30 |
| JPH0227789B2 true JPH0227789B2 (en) | 1990-06-19 |
Family
ID=12801704
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57048380A Granted JPS58165270A (en) | 1982-03-26 | 1982-03-26 | Pressure control system of supply gas to fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58165270A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60198064A (en) * | 1984-03-19 | 1985-10-07 | Toshiba Corp | Fuel cell system |
| US7465156B2 (en) | 2004-12-17 | 2008-12-16 | Lg Electronics Inc. | Apparatus for mounting compressor |
| JP5463251B2 (en) * | 2010-09-17 | 2014-04-09 | 日立アプライアンス株式会社 | Compressor and compressor built-in products |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5853164A (en) * | 1981-09-24 | 1983-03-29 | Toshiba Corp | Fuel cell device |
-
1982
- 1982-03-26 JP JP57048380A patent/JPS58165270A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58165270A (en) | 1983-09-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5151166A (en) | Oxygen monitoring method and apparatus | |
| US5397656A (en) | Differential pressure controlling method and apparatus for plate reformer of fuel cell power generation system | |
| US4904547A (en) | Fuel-cell device | |
| US5146105A (en) | Internal pressure explosion-proof system | |
| JPS6151772A (en) | Flow control device for fuel cell power generation equipment | |
| JPH0227789B2 (en) | ||
| US20030094378A1 (en) | Electrochemical cell pressure regulating system and methods of using the same | |
| JPS58163182A (en) | Fuel cell | |
| JPH0227788B2 (en) | ||
| JPS57210573A (en) | Fuel-cell generating system | |
| JPH079812B2 (en) | Fuel cell | |
| JPH0562372B2 (en) | ||
| JPS5853164A (en) | Fuel cell device | |
| US3525642A (en) | Fuel reactor with control system | |
| JPS5750774A (en) | Fuel cell protecting apparatus | |
| JPH0389466A (en) | Feed gas flow control device for fuel cell | |
| RU2845019C1 (en) | Method for oxygen enrichment of gases supplied through a pipeline, a system for implementing such a method and an oxygen control line for such a system | |
| JPS591626A (en) | Moistening method for atmosphere gas | |
| JPS60213729A (en) | Gas combustion safety device | |
| JPH0571643B2 (en) | ||
| JPH046755A (en) | Phosphoric acid type fuel cell power generating device | |
| JPH088521Y2 (en) | Fuel cell differential pressure control device | |
| JPH0135410Y2 (en) | ||
| JPS62160665A (en) | Fuel cell power generation system | |
| JPS62160667A (en) | Fuel cell power generation system |