JPS6124169A - Fused carbonate type fuel cell - Google Patents
Fused carbonate type fuel cellInfo
- Publication number
- JPS6124169A JPS6124169A JP59146320A JP14632084A JPS6124169A JP S6124169 A JPS6124169 A JP S6124169A JP 59146320 A JP59146320 A JP 59146320A JP 14632084 A JP14632084 A JP 14632084A JP S6124169 A JPS6124169 A JP S6124169A
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- gas
- anode
- cathode
- fuel cell
- 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.)
- Pending
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
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
- H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
- H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
- H01M8/0625—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
-
- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2457—Grouping of fuel cells, e.g. stacking of fuel cells with both reactants being gaseous or vaporised
-
- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/244—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes with matrix-supported molten electrolyte
-
- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/2484—Details of groupings of fuel cells characterised by external manifolds
- H01M8/2485—Arrangements for sealing external manifolds; Arrangements for mounting external manifolds around a stack
-
- 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
- H01M8/14—Fuel cells with fused electrolytes
- H01M2008/147—Fuel cells with molten carbonates
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0048—Molten electrolytes used at high temperature
- H01M2300/0051—Carbonates
-
- 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
Abstract
Description
【発明の詳細な説明】
(発明の技術分野〕
この発明は、溶融炭酸塩燃料電池、特に反応ガス供給機
構に関するものである。DETAILED DESCRIPTION OF THE INVENTION TECHNICAL FIELD OF THE INVENTION This invention relates to molten carbonate fuel cells, and in particular to reactant gas supply mechanisms.
第1図は従来の溶融炭酸塩形燃料電池を示している。図
において、(υは端板、12)はカソード用集電板兼ガ
ス流路すなわち流路骨のガス分離板、(3)はカソード
、(4)は電解質保持体、(5jはアノード・(61は
アノード用集電板兼ガス流路すなわち流路付ノカス分離
板、(7)はマニホールド、(8)はマニホールドシー
ル用のガスケットである。対向するアノード電極(5)
とカソード電極(31および両電極<s+ 、(51間
に介在する電解質保持体(4)により単電池が構成され
、この単電池とガス分離板(21、+61を交互に積層
して積層体が構成されている。第2図は@1図に示す燃
料電池のマニホールド配置とガスノ流しを示している。FIG. 1 shows a conventional molten carbonate fuel cell. In the figure, (υ is the end plate, 12) is the cathode current collector plate and gas flow path, that is, the gas separation plate of the flow path bone, (3) is the cathode, (4) is the electrolyte holder, (5j is the anode/( 61 is a current collector plate for the anode and a gas flow path, that is, a nocas separation plate with a flow path, (7) is a manifold, and (8) is a gasket for manifold sealing.Anode electrode (5) facing
A single cell is constituted by the electrolyte holder (4) interposed between the cathode electrode (31 and both electrodes <s+, (51), and the cell and the gas separation plate (21, +61) are alternately laminated to form a laminate. Figure 2 shows the manifold arrangement and gas flow of the fuel cell shown in Figure 1.
第8図は第1図の変形例としてアノード(6)に凹凸を
設けその凹部に改質触媒(9)を充填した場合を示して
いる。FIG. 8 shows a modification of FIG. 1 in which the anode (6) is provided with irregularities and the recesses are filled with a reforming catalyst (9).
次に動作について説明する。第1図に示す燃料電池の場
合、マニホールド(7)から導入されるアノードガスは
矢印の方向に流れてアノード(5月こ達し。Next, the operation will be explained. In the case of the fuel cell shown in Fig. 1, the anode gas introduced from the manifold (7) flows in the direction of the arrow and reaches the anode.
アノード反応を起こす。−万、カソード(3)は第1図
の紙面に直交する方向に同様なマニホールドからカソー
ドガスが導入され、カソード反応が生じ。Causes an anode reaction. - 10,000, cathode gas was introduced into the cathode (3) from a similar manifold in a direction perpendicular to the plane of the paper of FIG. 1, and a cathode reaction occurred.
上記アノード反応と合せて電池反応が成り立ち。Together with the above anode reaction, a battery reaction is established.
燃料電池として電力が発生する。マニホールド(7)は
ガスケット(8)を介して積層体側面に押しつけられる
ことによりガスシール性を確保している。第8図に示す
燃料電池の場合には、改質触媒(9]によりメタン(C
H4)を主成分とする天然ガスや石炭ガスを改質し、水
素を主成分とするガスに転換して直ちにアノード反応に
使用することになり、効率良い燃料電池が期待されてい
た。Electricity is generated as a fuel cell. The manifold (7) is pressed against the side surface of the laminate through the gasket (8) to ensure gas sealing. In the case of the fuel cell shown in FIG. 8, methane (C
Natural gas or coal gas whose main component is H4) is reformed and converted into a gas whose main component is hydrogen, which is immediately used in the anode reaction, and an efficient fuel cell was expected.
従来の溶融炭酸塩形燃料電池は以上のように構成されて
いるので、先ず、マニホールド(7)のシールにガスケ
ット(8)を用いた場合、電解質、温度。Since the conventional molten carbonate fuel cell is constructed as described above, first, when the gasket (8) is used to seal the manifold (7), the electrolyte and the temperature are controlled.
および圧縮に耐える材質的な問題があること、さらには
、内部改質触媒(9)の場合には、電解質保持体(4)
からの電解質が浸透して改質触媒(9]を濡らすことに
より触媒活性が低下するという欠点を有していた。Furthermore, in the case of an internal reforming catalyst (9), the electrolyte holder (4)
This had the disadvantage that the electrolyte from the reforming catalyst (9) permeated and wetted the reforming catalyst (9), resulting in a decrease in catalytic activity.
(発明の概要〕
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、積層体内部に積層方向と並行に設
けられ、アノードガス流路と連通する反応ガス供給孔、
およびこの反応ガス供給孔内部に配設され、改質触媒を
充填した反応管を備え、上記改質触媒で改質されたガス
を上記反応ガス供給孔に導くようにすることにより、ガ
スシール性に優れ、かつ上記改質触媒の電解質による濡
れを防止して内部改質反応を効率良く行なわせることが
できる溶融炭酸塩形燃料電池を提供することを目的とし
ている。(Summary of the Invention) This invention was made to eliminate the drawbacks of the conventional ones as described above, and includes a reaction gas supply hole provided inside the stack in parallel with the stacking direction and communicating with the anode gas flow path.
and a reaction tube disposed inside the reaction gas supply hole and filled with a reforming catalyst, and by guiding the gas reformed by the reforming catalyst to the reaction gas supply hole, the gas sealing property is improved. It is an object of the present invention to provide a molten carbonate fuel cell which has excellent properties and is capable of efficiently carrying out an internal reforming reaction by preventing wetting of the reforming catalyst by the electrolyte.
以下、この発明の一実施例を図をもとに説明する。第4
図はこの発明の一実施例による溶融炭酸塩形燃料電池を
示す断面図である。図において。An embodiment of the present invention will be described below with reference to the drawings. Fourth
The figure is a sectional view showing a molten carbonate fuel cell according to an embodiment of the present invention. In fig.
Q(Iは反応ガス供給孔であり、積層体内部に積層方向
と並行に設けられ、アノードガス流路(6)と連通ずる
。東は反応管であり、この例では一部の反応ガス供給孔
−内部に配設され、改質触媒(9)が充填されている。Q (I is a reaction gas supply hole, which is provided inside the stack in parallel with the stacking direction and communicates with the anode gas flow path (6). The east side is a reaction tube, and in this example, a part of the reaction gas supply hole The pores are disposed inside and filled with a reforming catalyst (9).
なお、矢印はアノードガスの流れを示す。Note that arrows indicate the flow of anode gas.
次に動作について説明する。天然ガスや石炭ガスなどの
アノードガスは先ず反応管(ロ)に供給される。反応管
αυを通過するうちに改質触媒(9)の作用で改質され
たアノードガスは1反応管回の頂部より一転して反応管
(ロ)の外周部すなわち反応ガス供給孔OQの内部を下
方向に流れ2反応ガス供給孔QOと連°通ずるアノード
ガス流路(6)より各アノード15)1ζ供給される。Next, the operation will be explained. An anode gas such as natural gas or coal gas is first supplied to the reaction tube (b). The anode gas reformed by the action of the reforming catalyst (9) while passing through the reaction tube αυ turns from the top of one reaction tube turn to the outer periphery of the reaction tube (b), that is, the inside of the reaction gas supply hole OQ. 1ζ is supplied to each anode 15) from an anode gas flow path (6) that flows downward and communicates with the two reaction gas supply holes QO.
その後、大部分は反応に寄与し一部は未反応のまま、第
4図左方の反応ガス供給孔QGに達し、外部へ排田され
る。すなわち、溶融炭酸塩形燃料電池用の7ノードガス
である天然ガスや石炭ガスは反応管αηに導かれ、積層
体が650 ℃で運転されるので同温度になっている反
応管ゆで改質反応が生じ、改質されたガスは反応管aυ
の頂上から周囲の反応ガス供給孔明に入る一反応ガス供
給孔Q(Iはアノードガス流路(6)と連通しているの
で、改質ガスは速やかにアノード(5)に浸透して行き
、アノード反応に寄与する。−万、カソード(3)には
1図面の手前と向う側に反応管(ロ)を持たない反応ガ
ス供給孔(図示せず)をアノード(6)の場合と同様に
積層方向と並行に設け、この反応ガス供給孔を通じて各
カソードガス流路(2目ζカソードガスを供給すること
によりカソード反応が生じ、上述のアノード反応と合せ
て全体として電池反応が進行する。Thereafter, most of the gas contributes to the reaction, while some remains unreacted, reaches the reaction gas supply hole QG on the left side of FIG. 4, and is discharged to the outside. In other words, natural gas and coal gas, which are the 7-node gases for the molten carbonate fuel cell, are led to the reaction tube αη, and the stack is operated at 650°C, so the reforming reaction is carried out by boiling the reaction tube at the same temperature. The generated and reformed gas is transferred to the reaction tube aυ
Since the reactant gas supply hole Q (I is in communication with the anode gas flow path (6)), the reformed gas quickly permeates into the anode (5). Contributes to the anode reaction. - In the cathode (3), reactant gas supply holes (not shown) without reaction tubes (b) are stacked on the front and opposite sides of the drawing in the same way as the anode (6). A cathode reaction occurs by supplying cathode gas to each cathode gas flow path (second ζ) through this reaction gas supply hole, and the battery reaction as a whole proceeds together with the above-mentioned anode reaction.
このような反応ガス供給機構とすれば、反応ガス供給の
ためのマニホールドすなわち反応ガス供給孔QOのシー
ルが容易にでき、しかもアノードガスの改質反応をこの
反応ガス供給孔QQの内部で行なわせる仁とにより、改
質触媒(9)の電解質による濡れを防止することができ
るので、信頼性が高くしかも高効率な電池反応が得られ
る。With such a reaction gas supply mechanism, the manifold for supplying the reaction gas, that is, the reaction gas supply hole QO, can be easily sealed, and the reforming reaction of the anode gas can be carried out inside the reaction gas supply hole QQ. Since the reforming catalyst (9) can be prevented from being wetted by the electrolyte, a highly reliable and highly efficient cell reaction can be obtained.
なお・上記実施例ではアノードガスを積層体の下方から
反応管(ロ)に導入する場合を示したが、上方から導入
してもよい。Although the above embodiment shows the case where the anode gas is introduced into the reaction tube (b) from below the stacked body, it may also be introduced from above.
また、上記実施例ではカソード(31側にもアノード(
5)側と同様な反応ガス供給孔QOを設けた場合につい
て説明したが、カソード(IJ側には第1図の従来例で
示すような箱型のいわゆる外部マニホールド(7)を設
けても上記実施例と同様の効果が得られる。In addition, in the above embodiment, the anode (
Although we have explained the case in which a reaction gas supply hole QO similar to that on the 5) side is provided, even if a box-shaped so-called external manifold (7) as shown in the conventional example in Fig. 1 is provided on the cathode (IJ side), Effects similar to those of the embodiment can be obtained.
し発明の効果〕
以上のように、この発明によれば、積層体内部に積層方
向と並行に設けられ、アノードガス流路と連通ずる反応
ガス供給孔、およびこの反応ガス供給孔内部に配設され
、改質触媒を充填した反応管を備え、上記改質触媒で改
質されたガスを上記反応ガス供給孔に導くようにしたの
で、ガスシール性に優れ、かつ上記改質触媒の電解質に
よる濡れを防出して内部改質反応を効率良く行なわせる
ことができる効果がある。[Effects of the Invention] As described above, according to the present invention, there is a reaction gas supply hole provided inside the laminate in parallel with the stacking direction and communicating with the anode gas flow path, and a reaction gas supply hole provided inside the reaction gas supply hole. The structure is equipped with a reaction tube filled with a reforming catalyst, and the gas reformed by the reforming catalyst is guided to the reaction gas supply hole, so that it has excellent gas sealing properties, and the electrolyte of the reforming catalyst It has the effect of preventing wetting and allowing internal reforming reactions to occur efficiently.
第1図は従来の溶融炭酸塩形燃料電池の一例を示す断面
図、第2図は第1図に示す燃料電池のマニホールドの配
置と反応ガスの流れを模式的に示す説明図、第8図は第
1図に示す従来の溶融炭酸塩形燃料電池の変形例の主要
部を示す断面図、第4図はこの発明の一実施例による溶
融炭酸塩形燃料電池を示す断面図である。
図において、 (21、(61はガス流路骨のガス分離
板、(3]はカソード、(4]は電解質保持体、(5)
はアノード、(9)は改質触媒、 Q(Iは反応ガス供
給孔、C1υは反応管である。
なお、各図中同一符号は同一または相当部分を示すもの
とする。Figure 1 is a sectional view showing an example of a conventional molten carbonate fuel cell, Figure 2 is an explanatory diagram schematically showing the arrangement of the manifold and the flow of reactant gas in the fuel cell shown in Figure 1, and Figure 8. FIG. 4 is a sectional view showing a main part of a modification of the conventional molten carbonate fuel cell shown in FIG. 1, and FIG. 4 is a sectional view showing a molten carbonate fuel cell according to an embodiment of the present invention. In the figure, (21, (61 is the gas separation plate of the gas flow path bone, (3) is the cathode, (4) is the electrolyte holder, (5)
is an anode, (9) is a reforming catalyst, Q (I is a reaction gas supply hole, and C1υ is a reaction tube. In each figure, the same reference numerals indicate the same or corresponding parts.
Claims (1)
ドを有する単電池、並びに上記アノードに対設するアノ
ードガス流路と上記カソードに対設するカソードガス流
路とを分離するガス分離板を交互に積層して積層体を構
成する溶融炭酸塩形燃料電池において、上記積層体内部
に積層方向と並行に設けられ、上記アノードガス流路と
連通する反応ガス供給孔、およびこの反応ガス供給孔内
部に配設され、改質触媒を充填した反応管を備え、改質
触媒で改良されたガスを上記反応ガス供給孔に導くよう
にしたことを特徴とする溶融炭酸塩形燃料電池。Single cells having an anode and a cathode facing each other with an electrolyte holder interposed therebetween, and gas separation plates that separate an anode gas flow path facing the anode from a cathode gas flow path facing the cathode are alternately laminated. In the molten carbonate fuel cell which constitutes a stacked body, a reactive gas supply hole is provided in the stacked body in parallel with the stacking direction and communicates with the anode gas flow path, and a reactive gas supply hole is arranged inside the reactive gas supply hole. 1. A molten carbonate fuel cell comprising a reaction tube filled with a reforming catalyst, the gas being improved by the reforming catalyst being guided to the reaction gas supply hole.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59146320A JPS6124169A (en) | 1984-07-13 | 1984-07-13 | Fused carbonate type fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59146320A JPS6124169A (en) | 1984-07-13 | 1984-07-13 | Fused carbonate type fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6124169A true JPS6124169A (en) | 1986-02-01 |
Family
ID=15404999
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59146320A Pending JPS6124169A (en) | 1984-07-13 | 1984-07-13 | Fused carbonate type fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6124169A (en) |
Cited By (4)
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---|---|---|---|---|
WO1996005625A2 (en) * | 1994-08-08 | 1996-02-22 | Ztek Corporation | Ultra-high efficiency turbine and fuel cell combination |
WO1996025773A1 (en) * | 1995-02-16 | 1996-08-22 | Siemens Aktiengesellschaft | Solid electrolyte high-temperature fuel cell module and method of operating the latter |
US6099983A (en) * | 1996-10-18 | 2000-08-08 | Kabushiki Kaisha Toshiba | Fuel cell containing a fuel supply means, gas generating means and temperature control means operated to prevent the deposition of carbon |
KR100952604B1 (en) | 2008-07-28 | 2010-04-15 | 한국과학기술원 | Solid oxide fuel cell system integrated with reformer |
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JPS58129780A (en) * | 1982-01-29 | 1983-08-02 | Toshiba Corp | Fused carbonate fuel cell layer body |
JPS58164171A (en) * | 1982-03-25 | 1983-09-29 | Kansai Electric Power Co Inc:The | Cell stack of fuel cell |
-
1984
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Publication number | Priority date | Publication date | Assignee | Title |
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JPS58119167A (en) * | 1982-01-11 | 1983-07-15 | Toshiba Corp | Fuel cell device |
JPS58129780A (en) * | 1982-01-29 | 1983-08-02 | Toshiba Corp | Fused carbonate fuel cell layer body |
JPS58164171A (en) * | 1982-03-25 | 1983-09-29 | Kansai Electric Power Co Inc:The | Cell stack of fuel cell |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5976332A (en) * | 1994-03-21 | 1999-11-02 | Ztek Corporation | Ultra-high efficiency turbine and cell combination |
WO1996005625A2 (en) * | 1994-08-08 | 1996-02-22 | Ztek Corporation | Ultra-high efficiency turbine and fuel cell combination |
WO1996005625A3 (en) * | 1994-08-08 | 1996-07-18 | Ztek Corp | Ultra-high efficiency turbine and fuel cell combination |
US5693201A (en) * | 1994-08-08 | 1997-12-02 | Ztek Corporation | Ultra-high efficiency turbine and fuel cell combination |
KR100271096B1 (en) * | 1994-08-08 | 2000-11-01 | 데니스 엠. 오길비 | Gas and steam turbin power system |
WO1996025773A1 (en) * | 1995-02-16 | 1996-08-22 | Siemens Aktiengesellschaft | Solid electrolyte high-temperature fuel cell module and method of operating the latter |
US6099983A (en) * | 1996-10-18 | 2000-08-08 | Kabushiki Kaisha Toshiba | Fuel cell containing a fuel supply means, gas generating means and temperature control means operated to prevent the deposition of carbon |
KR100952604B1 (en) | 2008-07-28 | 2010-04-15 | 한국과학기술원 | Solid oxide fuel cell system integrated with reformer |
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