JPS58163182A - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPS58163182A JPS58163182A JP57047923A JP4792382A JPS58163182A JP S58163182 A JPS58163182 A JP S58163182A JP 57047923 A JP57047923 A JP 57047923A JP 4792382 A JP4792382 A JP 4792382A JP S58163182 A JPS58163182 A JP S58163182A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- chamber
- oxidizer
- differential pressure
- oxidizing agent
- 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.)
- Granted
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
-
- 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
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
-
- 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
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04225—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells during start-up
-
- 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
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04228—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells during shut-down
-
- 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
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/043—Processes for controlling fuel cells or fuel cell systems applied during specific periods
- H01M8/04302—Processes for controlling fuel cells or fuel cell systems applied during specific periods applied during start-up
-
- 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
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/043—Processes for controlling fuel cells or fuel cell systems applied during specific periods
- H01M8/04303—Processes for controlling fuel cells or fuel cell systems applied during specific periods applied during shut-down
-
- 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
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
-
- 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)
Abstract
Description
【発明の詳細な説明】
この発明は、起動時又は停止時の圧力サージを軽減する
ことを目的とする燃料電池に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fuel cell whose purpose is to reduce pressure surges during startup or shutdown.
従来この種の装置として第１図に示すものがあつた。図
において（１）は圧力容器構造の電池筐体、（２）はそ
の電池筐体に収納された燃料電池本体、（３）は燃料室
、（４）は酸化剤室、（５）は燃料室（３）に燃料を供
給・排気する系統、（６）は酸化剤室（４）に酸化剤を
供給・排気する系統、（７）は電池筐体（１）に不活性
ガスを供給・排気する系統、（８）は系統（５）と系統
（７）とを連結し燃料室（３）を不活性ガスでパージす
る系統、（９）は系統（６）と系統（７）とを連結し酸
化剤室（４）を不活性ガスでパージする系統、（１０ａ
） （１０ｂ）は燃料と不活性ガスを切換える開閉弁、
（１０ｃ） （１０ｄ）は酸化剤と不活性ガスを切換え
る開閉弁、（ｌｌａ）は燃料の流量調節弁、（１２ａ）
は燃料流量計、（ｌｌｂ）は酸化剤の流量調節弁、（１
２ｂ）は酸化剤の流量計、（ｌｌｃ）は不活性ガスの流
量調節弁、（１２Ｃ）は不活性ガス流量計、（１８ｃ）
は電池筐体（１）と燃料室（３）の間の差圧調節弁、（
１８ｂ）は電池筐体（１）と酸化剤室（４）の間の差圧
調節弁、（１８ｃ）は電池筐体（１）の圧力調節弁、（
１４＠ｌ）は電池筐体（１）と燃料室（３）の間の差圧
計、（１４ｂ）は電池筐体（１）と酸化剤室（４）の間
の差圧計、（１４ｃ）は電池筐体（１）の圧力計である
。A conventional device of this type is shown in FIG. In the figure, (1) is the battery casing with a pressure vessel structure, (2) is the fuel cell body housed in the battery casing, (3) is the fuel chamber, (4) is the oxidizer chamber, and (5) is the fuel A system that supplies and exhausts fuel to the chamber (3), (6) a system that supplies and exhausts an oxidizer to the oxidizer chamber (4), and (7) a system that supplies and exhausts inert gas to the battery case (1). (8) is a system that connects systems (5) and (7) to purge the fuel chamber (3) with inert gas; (9) is a system that connects systems (6) and (7); A connected system for purging the oxidizer chamber (4) with an inert gas, (10a
) (10b) is an on-off valve that switches between fuel and inert gas;
(10c) (10d) is an on-off valve that switches between oxidizer and inert gas, (lla) is a fuel flow rate control valve, (12a)
is a fuel flow meter, (llb) is an oxidizer flow control valve, (1
2b) is an oxidizing agent flow meter, (llc) is an inert gas flow rate control valve, (12C) is an inert gas flow meter, (18c)
is the differential pressure regulating valve between the battery housing (1) and the fuel chamber (3), (
18b) is a differential pressure regulating valve between the battery casing (1) and the oxidizer chamber (4), (18c) is a pressure regulating valve of the battery casing (1), (
14@l) is the differential pressure gauge between the battery housing (1) and the fuel chamber (3), (14b) is the differential pressure gauge between the battery housing (1) and the oxidizer chamber (4), and (14c) is the differential pressure gauge between the battery housing (1) and the oxidizer chamber (4). This is a pressure gauge for the battery case (1).
次に動作について説明する。燃料電池の起動時は開閉弁
（１０ａ） （１０ｄ）を閉とし開閉弁（１０ｂ） （
１０ｃ）を開とし電池筐体（１）、燃料室（３）、酸化
剤室（４）に窒素などの不活性ガスを供給する。このと
き不活性ガスの流量を各流量計（１２ａ） （１２ｂ）
（１２ｃ）で検出し、流量調節弁（ｌｌａ） （ｌｌ
ｂ） （Ｈｃ）で制御する。Next, the operation will be explained. When starting up the fuel cell, close the on-off valves (10a) (10d) and close the on-off valves (10b) (
10c) is opened to supply an inert gas such as nitrogen to the battery housing (1), fuel chamber (3), and oxidizer chamber (4). At this time, each flow meter (12a) (12b) measures the flow rate of inert gas.
(12c), and the flow rate adjustment valve (lla) (ll
b) Controlled by (Hc).
また電池筐体（１）の圧力を圧力計（１４ｃ）で検出し
圧力調節弁（１８ｃ）で制御し任意の動作圧力に設定す
る。さらに燃料室（３）と電池筐体（１）の間の差圧を
差圧計（１４ａ）で検出し差圧調節弁（１ａａ）で制御
すると同時に酸化剤室（４）と電池筐体（１）の間の差
圧を差圧計（Ｈｂ）で検出し差圧調節弁（１８ｂ）で制
御する。Further, the pressure in the battery case (1) is detected by a pressure gauge (14c) and controlled by a pressure regulating valve (18c) to set it to an arbitrary operating pressure. Furthermore, the differential pressure between the fuel chamber (3) and the battery housing (1) is detected by the differential pressure gauge (14a) and controlled by the differential pressure regulating valve (1aa). ) is detected by a differential pressure gauge (Hb) and controlled by a differential pressure regulating valve (18b).
燃料電池本体（２）を所要の動作温度まで昇温後、開閉
弁（１０１）） （ＩＯＣ）を閉とし、開閉弁（１０ａ
） （１０ｄ）を開とし、燃料および酸化剤をそれぞれ
燃料室（３）酸化剤室（４）に所要流量を供給して、燃
料電池（２）を発電させる。After heating the fuel cell main body (2) to the required operating temperature, close the on-off valve (101) (IOC) and close the on-off valve (10a).
) (10d) is opened and fuel and oxidizer are supplied to the fuel chamber (3) and oxidizer chamber (4) at the required flow rates, respectively, to cause the fuel cell (2) to generate electricity.
停止時は開閉弁（１０ａ） （１０ｄ）を閉とし開閉弁
（１０ｂ） （１０ｃ）を開として燃料室（３）酸化剤
室（４）を窒素などの不活性ガスで置換後電池筐体（１
）の圧力を大気圧にする。When stopping, close the on-off valves (10a) (10d) and open the on-off valves (10b) (10c) to replace the fuel chamber (3) and oxidizer chamber (4) with an inert gas such as nitrogen, and then replace the battery casing ( 1
) to atmospheric pressure.
従来の燃料電池の運転方法は以上のように構成されてい
るので、燃料および酸化剤と窒素などの不活性ガスとの
切換時に、圧力サージが発生し電池筐体（１）と燃料室
（３）、又は酸化剤室（４）との間のシール、さらに燃
料室（３）と酸化剤室（４）とを隔離する電解液を含浸
させた多孔質部材（マトリックス）および電極を破壊す
る危険性があつｔコ。また電池筐体（１）と燃料室（３
）、又は酸化剤室（４）との間の差圧を一定値以内に保
持しながら上記のガス切換を行なうと、起動、停止に長
時間を必要とするなどの欠点があった。Since the conventional fuel cell operating method is configured as described above, when switching between the fuel and oxidizer and an inert gas such as nitrogen, a pressure surge occurs and the battery housing (1) and fuel chamber (3) are switched. ) or the risk of destroying the seal between the oxidizer chamber (4) and the electrolyte-impregnated porous material (matrix) and electrodes separating the fuel chamber (3) and the oxidizer chamber (4). Sexy T-ko. In addition, the battery housing (1) and the fuel chamber (3)
) or the oxidizer chamber (4) while maintaining the differential pressure within a certain value, there were drawbacks such as a long time required for starting and stopping.
この発明は上記のような従来のものの欠点を除去するた
めになされたもので、電池筐体内の燃料系統、及び酸化
剤系統にそれぞれ開閉弁を設け、起動時又は停止時に電
池筐体内の不活性ガスを燃料電池本体の燃料室、酸化剤
室に供給することにより、ガス切換時に発生する圧力サ
ージを軽減しさらに起動、又は停止に要する時間を短縮
できる燃料電池を提供することを目的としている。This invention was made in order to eliminate the drawbacks of the conventional ones as described above.The fuel system and the oxidizer system inside the battery case are provided with on-off valves, respectively, and the inert valve inside the battery case is closed when starting or stopping. The object of the present invention is to provide a fuel cell that can reduce pressure surges that occur when switching gases and further shorten the time required for starting or stopping by supplying gas to the fuel chamber and oxidizer chamber of the fuel cell main body.
以下、この発明の一実施例を図について説明する。第２
図において（１） 〜（７）および（１１ａ）（１１ｂ
）（ｌｌｃ） 〜（１４ａ） （１４ｂ） （１４ｃ）
は上記従来装置と同一のものである。（１５ａ）は電池
筐体（１）の内部の燃料系統（５）に取付けられた電磁
開閉弁、（１５ｂ）は電池筐体（１）の内部の酸化剤系
統（６）に取付けられた電磁開閉弁である。上記開閉弁
（１５ａ） （１５ｂ）の弁口径は、燃料室（３）およ
び酸化剤室（４）の容積と、不活性ガスで燃料室（３）
、酸化剤室（４）を置換するのに要求される時間から最
大流量を求め、さらに燃料電池が定常負荷運転時に設定
される電池筐体（１）と燃料室（３）との間の差圧およ
び電池筐体（１）と酸化剤室（４）との間の差圧から流
量係数を計算して決定する、これにより、上記開閉弁（
１５ａ） （１５ｂ）を使用して燃料室（３）酸化剤室
（４）に不活性ガスを供給している状態では、電池筐体
（１）と燃料室（３）との間の差圧および電池筐体（１
）と酸化剤室（４）との間の差圧は開閉弁（１５ａ）
（１５ｂ）で発生する圧力損失により所要の値に設定さ
れる。An embodiment of the present invention will be described below with reference to the drawings. Second
In the figure (1) to (7) and (11a) (11b
) (llc) ~(14a) (14b) (14c)
is the same as the conventional device described above. (15a) is an electromagnetic on-off valve installed in the fuel system (5) inside the battery case (1), and (15b) is an electromagnetic valve installed in the oxidizer system (6) inside the battery case (1). It is an on-off valve. The valve diameter of the on-off valves (15a) (15b) is the volume of the fuel chamber (3) and the oxidizer chamber (4), and the volume of the fuel chamber (3) with inert gas.
, determine the maximum flow rate from the time required to replace the oxidizer chamber (4), and also determine the difference between the cell housing (1) and the fuel chamber (3) when the fuel cell is set during steady load operation. The flow coefficient is calculated and determined from the pressure and the differential pressure between the battery housing (1) and the oxidizer chamber (4).
15a) When inert gas is supplied to the fuel chamber (3) and oxidizer chamber (4) using (15b), the differential pressure between the battery housing (1) and the fuel chamber (3) and battery housing (1
) and the oxidizer chamber (4) is controlled by the on-off valve (15a).
It is set to a required value by the pressure loss generated in (15b).
次に動作について説明する。燃料電池の起動時は、まず
燃料流量調節弁（ｌｌａ）酸化剤流量調節弁（ｌｌｂ）
、電池筐体（１）と燃料室（３）との差圧調節弁（１
８ａ） 、電池筐体（１）と酸化剤室（４）との差圧調
節弁（１８ｂ）を閉とし、開閉弁（１５ａ） （１５ｂ
）を開とする。Next, the operation will be explained. When starting up a fuel cell, first the fuel flow control valve (lla) and the oxidizer flow control valve (llb) are
, differential pressure control valve (1) between the battery housing (1) and the fuel chamber (3)
8a) Close the differential pressure control valve (18b) between the battery housing (1) and the oxidizer chamber (4), and close the on-off valve (15a) (15b).
) is opened.
系統（７）を使用して電池筐体（１）、燃料室（３）、
酸化剤室（４）に窒素などの不活性ガスを供給して、電
池筐体（１）内部の圧力を所要の動作圧力に設定する。Using system (7), battery housing (1), fuel chamber (3),
An inert gas such as nitrogen is supplied to the oxidizer chamber (4) to set the pressure inside the battery housing (1) to a required operating pressure.
このとき、不活性ガスの流量計（１２ｃ）で検出し流量
調節弁（ｌｉｅ）で制御すると同時に電池筐体（１）内
部の圧力を圧力計（１４ｃ）で検出し圧力調節弁（１８
ｃ）で制御する。この状態では電池筐体（１）、燃料室
（３）。At this time, the pressure inside the battery housing (1) is detected by the pressure gauge (14c) and the pressure inside the battery casing (1) is detected by the pressure regulating valve (18).
c). In this state, the battery housing (1) and the fuel chamber (3).
酸化剤室（４）は等圧となり差圧計（１４ａ） （１４
ｂ）は零点を示す。次に差圧調節弁（ｘａａ） （１ａ
ｂ）を開としてから流量調節弁（ｌｌａ） （ｌｌｂ）
を開とし、その後上記開閉弁（１５ａ） （１５ｂ）を
閉とし、燃料室（３）酸化剤室（４）にそれぞれ燃料酸
化剤を所要流量だけ供給して燃料電池を発電させる。The oxidizer chamber (4) becomes equal pressure and the differential pressure gauge (14a) (14
b) indicates the zero point. Next, the differential pressure control valve (xaa) (1a
After opening b), open the flow control valve (lla) (llb)
is opened, and then the on-off valves (15a) and (15b) are closed, and the fuel oxidizer is supplied to the fuel chamber (3) and oxidizer chamber (4) at the required flow rates, respectively, to cause the fuel cell to generate electricity.
このとき、電池筐体（１）と燃料室（３）の間の差圧を
差圧計（１４ａ）で検出し差圧調節弁（１８ａ）で制御
すると同時に、電池筐体（１）と酸化剤室（４）の間の
差圧を差圧計（１４１））で検出し差圧調節弁（１８ｂ
）で制御する。また電池筐体く】）内部の圧力を燃料室
（３）酸化剤室（４）の圧力よりやや高く（例えば１０
０ ｍｍ水柱）設定する。また燃料電池の停止時は、ま
ず上記開閉弁（１５ａ） （１５ｂ）を閉とし、次に流
量調節弁（１］、ａ ）（ｌｌｂ）を閉として燃料室（
３）酸化剤室（４）を完全に窒素などの不活性ガスで置
換した後、差圧調節弁（１８ａ） （１８ｂ）を閉とす
る。At this time, the differential pressure between the battery casing (1) and the fuel chamber (3) is detected by the differential pressure gauge (14a) and controlled by the differential pressure regulating valve (18a), and at the same time the battery casing (1) and the oxidizer are detected. The differential pressure between the chambers (4) is detected by the differential pressure gauge (141)) and the differential pressure control valve (18b) is activated.
) to control. In addition, the pressure inside the battery casing is set to be slightly higher than the pressure in the fuel chamber (3) and oxidizer chamber (4) (for example, 10
0 mm water column). When stopping the fuel cell, first close the on-off valves (15a) and (15b), then close the flow rate control valves (1), a) and (llb) to close the fuel chamber (
3) After completely replacing the oxidizer chamber (4) with an inert gas such as nitrogen, close the differential pressure control valves (18a) and (18b).
この後、」１記流量調節弁（ｌｌｃ）と圧力調節弁（１
３ｃ）を制御して、電池筐体（１）内部の圧力を大気圧
にする。After this, the flow rate control valve (llc) and the pressure control valve (1) are installed.
3c) to bring the pressure inside the battery housing (1) to atmospheric pressure.
なお、」１記実施例では、開閉弁（１５ａ） （１５ｂ
）を、電池筐体（１）の内部で燃料電池本体（２）の上
流側配管部に設けたものを示したが、開閉弁（１５ａ）
（１５ｂ）を燃料室（３）酸化剤室（４）に直接設け
ても同様の動作を期待できる。また開閉弁の一種である
調節弁を設けてもよい３、
以上のように、この発明によれば、電池筐体内部の燃料
系統、酸化剤系統にそれぞれ開閉弁を設は燃料電池の起
動時又は停止時に電池筐体内の不ｔり１
活性ガスを燃料電池本体の燃料室、酸化剤室に供給する
ように構成したので、ガス切換時に発生する圧力サージ
を軽減し、簡単な構成にて短時間の起動、停止が可能と
なる効果がある。In addition, in the embodiment 1, the on-off valves (15a) (15b
) is provided in the upstream piping section of the fuel cell main body (2) inside the battery case (1), but the on-off valve (15a)
Similar operation can be expected even if (15b) is provided directly in the fuel chamber (3) or oxidizer chamber (4). Further, a control valve, which is a type of on-off valve, may be provided.3 As described above, according to the present invention, on-off valves are provided in the fuel system and oxidizer system inside the battery case, respectively, when the fuel cell is started. The structure is configured to supply active gas to the fuel chamber and oxidizer chamber of the fuel cell main body, which reduces pressure surges that occur when switching gases and saves time with a simple configuration. It has the effect of making it possible to start and stop time.
第１図は従来の燃料電池用ガス供給装置の系統図、第２
図はこの発明の一実施例による燃料電池用ガス供給装置
の系統図である。
（１）・・・・・・・・・電池筐体、（２）・・・曲・
燃料電池本体、（３）・・・・・・・・燃料室、（４）
・・・・・・・・・酸化剤室、（５）・・・・・・・・
・燃料系統、（６）・・・・・・・・・酸化剤系統、（
７）・・・曲・不活性ガス系統、（８）・・・・・・・
・・燃料室パージ系統、（９）・曲・用酸化剤室パージ
系統、（１０ａ） （１０ｂ） （１０ｃ） （１０ｄ
） −−・・開閉弁、（ｎａ） ０１ｂ） （ｎｃ）−
流量調節弁、（ｘ２ａ） （１２ｂ）（１２ｃ）・・・
・・・・・流量計、（１８ａ） ｃ１８ｂ）・・・曲・
・差圧調節弁、（ｔａＣ）・・・・・・・・・圧力調節
弁、（１４ａ） （１４ｂ）・・・・・・・差圧計、（
１４ｃ）・・・・・・・・・圧力計、（１５ａ）（１５
ｂ）・・凹・・・開閉弁。
なお、図中、同一符号は同一、又は相当部分を示す。
代理人 葛野信−
手続補正書（自発）
昭和 ５η １Ｏ１−１２８日
２、発明の名称
燃料電池
３、補正をする者
事件との関係 特許出願人
住 所 東京都千代田区丸の山王丁目２番３号
名 称（６０１） 三菱電機株式会社代表者片山仁
八部
４、代理人
５、補正の対象
明細書の発明の詳細な説明の欄
６、 補正の内容
明細書の第７頁第５行の「弁（１５ａ）（１５ｂ）を閉
とし」を「弁（１５ａ）（１５ｂ）を開とし」と訂正す
る。
以 ｔFigure 1 is a system diagram of a conventional gas supply device for fuel cells;
The figure is a system diagram of a gas supply device for a fuel cell according to an embodiment of the present invention. (1)...Battery housing, (2)...Song...
Fuel cell body, (3)...Fuel chamber, (4)
・・・・・・・・・Oxidizer chamber, (5)・・・・・・・・・
・Fuel system, (6)... Oxidizer system, (
7)...Tune/Inert gas system, (8)...
・・Fuel chamber purge system, (9)・Oxidizer chamber purge system, (10a) (10b) (10c) (10d
) --...Opening/closing valve, (na) 01b) (nc)-
Flow control valve, (x2a) (12b) (12c)...
...flow meter, (18a) c18b) ...song...
・Differential pressure control valve, (taC)......Pressure control valve, (14a) (14b)...Differential pressure gauge, (
14c)......Pressure gauge, (15a) (15
b)...Concave...Opening/closing valve. In addition, in the figures, the same reference numerals indicate the same or equivalent parts. Agent Makoto Kuzuno - Procedural amendment (voluntary) Showa 5η 1O1-128 Day 2, Name of invention Fuel cell 3, Relationship to the case of the person making the amendment Patent applicant address 2-3 Sanno-chome, Maruno, Chiyoda-ku, Tokyo Name (601) Mitsubishi Electric Co., Ltd. Representative Hitoshi Katayama 4, Agent 5, Column 6 for detailed explanation of the invention in the specification subject to amendment, Line 5 on page 7 of the statement of contents of the amendment "The valves (15a) (15b) are closed" is corrected to "the valves (15a) (15b) are opened." From then on
Claims (2)
ガスを供給して運転する燃料電池において、上記電池筐
体内の燃料系統及び酸化剤系統にそれぞれ開閉弁を設け
、燃料電池の起動時又は停止時に電池筐体内の不活性ガ
スを燃料電池本体の燃料室及び酸化剤室に供給し得るよ
うにしたことを特徴とする燃料電池。(1) In a fuel cell that is housed in a battery housing with a container structure and operated by supplying inert gas into the battery housing, on-off valves are provided in the fuel system and oxidizer system in the battery housing, respectively, and the fuel cell 1. A fuel cell characterized in that an inert gas inside a battery housing can be supplied to a fuel chamber and an oxidizer chamber of a fuel cell main body when starting or stopping.
量値をそれぞれ燃料及び酸化剤の最大流量値以下として
開閉弁の各弁口径を決定したことを特徴とする特許請求
の範囲第１項記載の燃料電池。(2) The diameter of each valve of the on-off valve is determined so that the flow rate value of the inert gas to be supplied to the fuel chamber and the oxidizer chamber is equal to or less than the maximum flow rate of the fuel and the oxidizer, respectively. Fuel cell as described in Section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57047923A JPS58163182A (en) | 1982-03-23 | 1982-03-23 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57047923A JPS58163182A (en) | 1982-03-23 | 1982-03-23 | Fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58163182A true JPS58163182A (en) | 1983-09-27 |
| JPS6318305B2 JPS6318305B2 (en) | 1988-04-18 |
Family
ID=12788885
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57047923A Granted JPS58163182A (en) | 1982-03-23 | 1982-03-23 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58163182A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60208059A (en) * | 1984-04-02 | 1985-10-19 | Hitachi Ltd | Protection device of fuel cell |
| JPS60212966A (en) * | 1984-04-06 | 1985-10-25 | Hitachi Ltd | Fuel cell operating system |
| JPS60241660A (en) * | 1984-05-15 | 1985-11-30 | Mitsubishi Electric Corp | Fuel cell |
| JPS6132363A (en) * | 1984-07-23 | 1986-02-15 | Hitachi Ltd | Fuel cell power generation system |
| JPS61176077A (en) * | 1985-01-29 | 1986-08-07 | Mitsubishi Electric Corp | Fuel battery equipment |
| JPS63184266A (en) * | 1987-01-27 | 1988-07-29 | Toshiba Corp | Starting method for molten carbonate fuel cell |
| US4904547A (en) * | 1985-03-01 | 1990-02-27 | Mitsubishi Denki Kabushiki Kaisha | Fuel-cell device |
| JPH0398267A (en) * | 1989-09-12 | 1991-04-23 | Hitachi Ltd | Operating method and device for molten carbonate fuel cell |
| WO2003096460A1 (en) * | 2002-05-14 | 2003-11-20 | Nissan Motor Co., Ltd. | Fuel cell system and related startup method |
-
1982
- 1982-03-23 JP JP57047923A patent/JPS58163182A/en active Granted
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60208059A (en) * | 1984-04-02 | 1985-10-19 | Hitachi Ltd | Protection device of fuel cell |
| JPS60212966A (en) * | 1984-04-06 | 1985-10-25 | Hitachi Ltd | Fuel cell operating system |
| JPH0370347B2 (en) * | 1984-04-06 | 1991-11-07 | Hitachi Ltd | |
| JPS60241660A (en) * | 1984-05-15 | 1985-11-30 | Mitsubishi Electric Corp | Fuel cell |
| JPS6132363A (en) * | 1984-07-23 | 1986-02-15 | Hitachi Ltd | Fuel cell power generation system |
| JPS61176077A (en) * | 1985-01-29 | 1986-08-07 | Mitsubishi Electric Corp | Fuel battery equipment |
| US4904547A (en) * | 1985-03-01 | 1990-02-27 | Mitsubishi Denki Kabushiki Kaisha | Fuel-cell device |
| JPS63184266A (en) * | 1987-01-27 | 1988-07-29 | Toshiba Corp | Starting method for molten carbonate fuel cell |
| JPH0398267A (en) * | 1989-09-12 | 1991-04-23 | Hitachi Ltd | Operating method and device for molten carbonate fuel cell |
| WO2003096460A1 (en) * | 2002-05-14 | 2003-11-20 | Nissan Motor Co., Ltd. | Fuel cell system and related startup method |
| CN1322621C (en) * | 2002-05-14 | 2007-06-20 | 日产自动车株式会社 | Fuel cell system and related startup method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6318305B2 (en) | 1988-04-18 |
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