JPS63279576A - Cathode recycle device for fused carbonate fuel cell - Google Patents

Cathode recycle device for fused carbonate fuel cell

Info

Publication number
JPS63279576A
JPS63279576A JP62112544A JP11254487A JPS63279576A JP S63279576 A JPS63279576 A JP S63279576A JP 62112544 A JP62112544 A JP 62112544A JP 11254487 A JP11254487 A JP 11254487A JP S63279576 A JPS63279576 A JP S63279576A
Authority
JP
Japan
Prior art keywords
cathode
exhaust gas
compressor
air
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
Application number
JP62112544A
Other languages
Japanese (ja)
Inventor
Toru Shimizu
徹 清水
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IHI Corp
Original Assignee
IHI Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by IHI Corp filed Critical IHI Corp
Priority to JP62112544A priority Critical patent/JPS63279576A/en
Publication of JPS63279576A publication Critical patent/JPS63279576A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04097Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04014Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
    • H01M8/04022Heating by combustion
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Abstract

PURPOSE:To dispense with a hot blower by having all oxidic gases exhausted out of the cathode, while mixing the partial gas turned to low temperature and atmospheric pressure with air, compressing it for pressure up, and supplying it to the cathode, thereby recycling it. CONSTITUTION:At a supply line 9 for feeding the cathode 2 with oxidic gas, the air A compressed by a compressor 6 is led thereinto through a heat exchanger 7, but at this heat exchanger 7, heat exchange takes place between the compressed air and the exhaust gas discharged out of an exhaust gas turbine 5. And, the compressed air is preheated and fed to the cathode 2, while the exhaust gas turns to low temperature and atmospheric pressure and is discharged out and, after the partial gas is mixed with air at the suction side of the compressor 6, it is compressed for pressure up at the compressor 6, then it is referred to the cathode 2. With this constitution, it gets off without using the conventional hot blower in consequence.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は燃料の有する化学エネルギーを直接電気エネル
ギーに変換させるエネルギ一部門で用いる燃料電池のう
ち、溶融炭酸塩型燃料電池のカソードに供給する酸化ガ
スのリサイクル装置に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is applicable to fuel cells used in the energy sector that directly convert the chemical energy of fuel into electrical energy, and which is supplied to the cathode of a molten carbonate fuel cell. This invention relates to an oxidizing gas recycling device.

[従来の技術] 現在までに提案されている溶融炭酸塩型燃料電池は、溶
融炭酸塩を多孔質物質にしみ込ませてなる電解質板(タ
イル)を、カソード(酸素極)とアノード(燃料極)で
両面から挾み、カソード側に酸化ガスを供給すると共に
アノード側に燃料ガスを供給することによりカソードと
アノードとの間で発生する電位差により発電が行われる
ようにしたものを1セルとし、各セルをセパレータを介
して多層に積層し、燃料電池スタックとして使用するよ
うにしてある。
[Prior Art] Molten carbonate fuel cells that have been proposed to date include an electrolyte plate (tile) made of porous material impregnated with molten carbonate, and a cathode (oxygen electrode) and an anode (fuel electrode). One cell is a cell in which power is generated by the potential difference generated between the cathode and the anode by sandwiching them from both sides, supplying oxidizing gas to the cathode side and supplying fuel gas to the anode side. Cells are stacked in multiple layers with separators interposed in between, and used as a fuel cell stack.

上記溶融炭酸塩型燃料電池のカソードへ酸化ガスを導く
カソードリサイクル装置は、燃料電池発電システムとし
ての効率向上や電池の温度コントロールのために有効な
手段であり、従来は、第2図に示す如く、タイルaの両
面をカソ−ドbとアノードCて挾み、カソードb側に酸
化ガスを、又、7ノートC側へ燃料ガスをそれぞれ流す
ようにした構成において、カソードbへ酸化ガスを供給
するため、コンプレッサからの圧縮空気を供給する供給
ラインdと、カソードbから排出された酸化ガスを流す
排出ラインeとを、熱交換器f、高温ブロワgを途中に
有するバイ/<スラインhで接続し、カソードbから排
出された酸化ガスの一部を高温ブロワgで酸化ガス供給
側に導き、コンプレッサからの圧縮空気に合流させてカ
ソードbに供給される空気の温度をコントロールするよ
うにしてある。
The cathode recycling device that guides oxidizing gas to the cathode of the molten carbonate fuel cell is an effective means for improving the efficiency of the fuel cell power generation system and controlling the temperature of the cell. , in a configuration in which both sides of tile a are sandwiched between cathode b and anode C, oxidizing gas is flowed to the cathode b side, and fuel gas is flowing to the 7 note C side, oxidizing gas is supplied to cathode b. In order to A part of the oxidizing gas discharged from cathode b is guided to the oxidizing gas supply side by high temperature blower g, and is merged with compressed air from the compressor to control the temperature of the air supplied to cathode b. be.

通常、燃料電池内は650℃〜700’Cに達するため
、第2図に示した従来の方式では、熱交換器fで酸化ガ
スの温度を下げた後、高温ブロワ9を経て供給ラインd
の空気に合流させ、カソードbに入る酸化ガスとしての
温度を約550℃位にコントロールさせている。
Normally, the temperature inside the fuel cell reaches 650°C to 700'C, so in the conventional method shown in Fig. 2, the temperature of the oxidizing gas is lowered in the heat exchanger f, and then passed through the high-temperature blower 9 to the supply line d.
The temperature of the oxidizing gas entering cathode b is controlled at approximately 550°C.

[発明が解決しようとする問題点] 上記従来の方式では、高温ブロワQを用いていて、燃料
電池内での酸化ガスの圧損弁を高温ブロワQで補ってい
るので、効率がよいものとなるが、高温ブロワとしては
、通常、350℃位のガスを扱うものがほとんどで、前
記の如き700℃近くの高温ガスを入れて出すような高
温ブロワは現存せず、第2図に示す従来方式は坦在実用
化できないものである。実用化するためには、700°
C近くの高温ガスを扱える高温ブロワQを特別に作らな
ければならず、高価なものになるおそれがある。
[Problems to be Solved by the Invention] The above conventional system uses a high temperature blower Q, and the high temperature blower Q compensates for the pressure loss valve of the oxidizing gas within the fuel cell, so it is efficient. However, most high-temperature blowers usually handle gas at around 350°C, and there is no existing high-temperature blower that can input and discharge high-temperature gas at around 700°C, as shown in Figure 2. cannot be put into practical use. For practical use, 700°
A high-temperature blower Q that can handle high-temperature gas near C must be specially manufactured, which may result in an expensive product.

そこで、本発明は、高価なものとなる高温ブロワを用い
ないでカソードリサイクルを可能にさせるようにしよう
とするものである。
Therefore, the present invention attempts to enable cathode recycling without using an expensive high-temperature blower.

[問題点を解決するための手段] 本発明は、上記目的を達成するために、カソードから排
出された高温の排ガスの排出ラインに、排ガスタービン
過給機の排ガスタービンを組み込み、且つ上記排出ライ
ンより分岐した排ガス分岐ラインを上記排ガスタービン
過給機のコンプレッサの入口側に接続し、該コンプレッ
サの吐出側をカソードの供給側に接続し、排ガスがカソ
ードにリサイクルさせるようにした構成とする。
[Means for Solving the Problems] In order to achieve the above object, the present invention incorporates an exhaust gas turbine of an exhaust gas turbine supercharger into an exhaust line for high temperature exhaust gas discharged from the cathode, and A more branched exhaust gas branch line is connected to the inlet side of the compressor of the exhaust gas turbine supercharger, and the discharge side of the compressor is connected to the supply side of the cathode, so that the exhaust gas is recycled to the cathode.

[作  用] 排ガスタービン過給機のコンプレッサで圧縮された空気
はカソードに供給される。カソードから排出された高温
排ガスは、排ガスタービンで膨張させられて圧力が下げ
られると共に温度が下げられる。温度の下がった排ガス
の一部が排ガス分岐ラインよりコンプレッサに吸入され
る空気と混合し、該コンプレッサで圧縮昇圧されてカソ
ードに供給される。これにより従来の高温ブロワを使用
しないですむ。
[Operation] Air compressed by the compressor of the exhaust gas turbine supercharger is supplied to the cathode. The high-temperature exhaust gas discharged from the cathode is expanded in an exhaust gas turbine to lower its pressure and temperature. A part of the exhaust gas whose temperature has decreased is mixed with air taken into the compressor from the exhaust gas branch line, compressed and pressurized by the compressor, and then supplied to the cathode. This eliminates the need for conventional high temperature blowers.

[実 施 例] 以下、本発明の実施例を図面を参照して説明づる。[Example] Embodiments of the present invention will be described below with reference to the drawings.

第1図に示す如く、タイル1を挾むようにカソード2と
アノード3を両面に配し、カソード2側に酸化ガスを供
給し、又、アノード3側に燃料ガスを供給するようにし
てある燃料電池の1セルをセパレータを介して積層しで
ある構成において、カソード2に酸化ガスを供給するた
め、空気Aをコンプレッサ6で圧縮した後、熱交換器7
で予熱してカソード2に供給するよう供給ライン9を設
け、一方、上記コンプレッサ6の扇車と排ガスタービン
5のタービン翼車とを軸8にて一体に連結してなる排ガ
スタービン過給機4における上記排ガスタービン5を、
カソード2から排出される酸化ガスの排出ライン10に
組み込むと共に、上記供給ライン9の途中に設けた熱交
換器7で空気を予熱するように上記排出ライン10に熱
交換器7を組み込み、且つ上記排出ライン10の熱交換
器7下流位置に、本発明の最も特徴をなす排ガス分岐ラ
イン11を設け、該排ガス分岐ライン11を排ガスター
ビン過給機のコンプレッサ6の吸気側に接続して、カソ
ード2から排出された酸化ガスの一部を空気に混合して
コンプレッサ6で圧縮しリサイクルさせるようにする。
As shown in FIG. 1, a fuel cell has a cathode 2 and an anode 3 arranged on both sides so as to sandwich a tile 1, and supplies oxidizing gas to the cathode 2 side and supplies fuel gas to the anode 3 side. In a configuration in which one cell of 1 is stacked with a separator in between, in order to supply oxidizing gas to the cathode 2, air A is compressed by a compressor 6, and then is compressed by a heat exchanger 7.
A supply line 9 is provided so that the preheated gas is supplied to the cathode 2, and an exhaust gas turbine supercharger 4 is provided in which the fan wheel of the compressor 6 and the turbine impeller of the exhaust gas turbine 5 are integrally connected by a shaft 8. The exhaust gas turbine 5 in
A heat exchanger 7 is installed in the exhaust line 10 for the oxidizing gas discharged from the cathode 2, and a heat exchanger 7 is installed in the supply line 9 so as to preheat the air. An exhaust gas branch line 11, which is the most characteristic feature of the present invention, is provided in the exhaust line 10 at a position downstream of the heat exchanger 7, and the exhaust gas branch line 11 is connected to the intake side of the compressor 6 of the exhaust gas turbine supercharger. A part of the oxidizing gas discharged from the tank is mixed with air, compressed by a compressor 6, and recycled.

燃料電池のカソード2から排出された酸化ガスのすべて
が排出ライン10途中の排ガスタービン5に導かれるた
め、排ガスのもつエネルギーが、排ガスタービン5を駆
動してコンプレッサ6を回転させる動力として回収され
る。上記カソード2から出た高温、高圧の酸化ガスは、
排ガスタービン5で膨張させられることにより圧力が下
がると共に温度も下げられて該排ガスタービン5から排
出され、熱交換器7に導かれる。
Since all of the oxidizing gas discharged from the cathode 2 of the fuel cell is guided to the exhaust gas turbine 5 in the middle of the exhaust line 10, the energy of the exhaust gas is recovered as power to drive the exhaust gas turbine 5 and rotate the compressor 6. . The high temperature and high pressure oxidizing gas emitted from the cathode 2 is
By being expanded by the exhaust gas turbine 5, the pressure and temperature are lowered, and the exhaust gas is discharged from the exhaust gas turbine 5 and guided to the heat exchanger 7.

カソード2に酸化ガスを供給するための供給ライン9で
は、コンプレッサ6により圧縮された空気へが熱交換器
7を通して導かれるが、熱交換器7では、圧縮された空
気と排ガスタービン5から出た排ガスとの間で熱交換が
行われ、圧縮空気は予熱されてカソード2へ供給され、
排ガスは低温、大気圧となって排出され、その一部がコ
ンプレッサ6の吸気側で空気と混合された後、コンプレ
ッサ6で圧縮昇圧されて再びカソード2に供給されるこ
とになる。この際、コンプレッサ6に入る空気の温度は
低いほどコンプレッサ6の効率が上がるが、本発明では
、排カスは低温にして空気と混合させているので、コン
プレッサ6の効率を下げることはない。
In the supply line 9 for supplying the oxidizing gas to the cathode 2, the air compressed by the compressor 6 is led through a heat exchanger 7, in which the compressed air and the exhaust gas exiting from the turbine 5 are connected. Heat exchange is performed with the exhaust gas, and the compressed air is preheated and supplied to the cathode 2.
The exhaust gas is discharged at low temperature and atmospheric pressure, and a part of it is mixed with air on the intake side of the compressor 6, and then compressed and pressurized by the compressor 6 and supplied to the cathode 2 again. At this time, the lower the temperature of the air entering the compressor 6, the higher the efficiency of the compressor 6, but in the present invention, the exhaust waste is kept at a lower temperature and mixed with the air, so the efficiency of the compressor 6 is not lowered.

[発明の効果] 以上述べた如く、本発明の溶融炭酸塩型燃料電池のカソ
ードリサイクル装置によれば、カソードから排出された
酸化ガスのすべてを排ガスタービン過給機のタービンに
導いて動力回収させ、低温、大気圧となったガスの一部
をコンプレツリの吸気側に導いて空気と混合し、該コン
プレッサで圧縮昇圧してカソードに供給してリサイクル
させるようにしであるので、従来方式の如き高価となる
高温ブロワを使用せずに、安価な既存の排ガスタービン
過給機によりカソードリサイクルをざぜることができる
、という優れた効果を奏し得る。
[Effects of the Invention] As described above, according to the cathode recycling device for a molten carbonate fuel cell of the present invention, all of the oxidizing gas discharged from the cathode is guided to the turbine of the exhaust gas turbine supercharger for power recovery. A part of the low-temperature, atmospheric-pressure gas is introduced into the intake side of the compressor, mixed with air, compressed and pressurized by the compressor, and then supplied to the cathode for recycling, making it less expensive than conventional methods. An excellent effect can be achieved in that cathode recycling can be accelerated using an inexpensive existing exhaust gas turbine supercharger without using a high-temperature blower.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の溶融炭酸塩型燃料電池のカソードリサ
イクル装置の実施例を示す概略図、第2図は従来方式の
概略図である。 1・・・タイル、2・・・カソード、3・・・アノード
、4・・・排ガスタービン過給機、5・・・排ガスター
ビン、6・・・コンプレッサ、7・・・熱交換器、9・
・・供給ライン、10・・・排出ライン、11・・・排
ガス分岐ライン。
FIG. 1 is a schematic diagram showing an embodiment of a cathode recycling device for a molten carbonate fuel cell according to the present invention, and FIG. 2 is a schematic diagram of a conventional system. DESCRIPTION OF SYMBOLS 1... Tile, 2... Cathode, 3... Anode, 4... Exhaust gas turbine supercharger, 5... Exhaust gas turbine, 6... Compressor, 7... Heat exchanger, 9・
... Supply line, 10... Discharge line, 11... Exhaust gas branch line.

Claims (1)

【特許請求の範囲】[Claims] 1)溶融炭酸塩をしみ込ませたタイルをカソードとアノ
ードとで挾み、カソード側に酸化ガスを、アノード側に
燃料ガスをそれぞれ供給するようにしてある溶融炭酸塩
型燃料電池における上記カソードから排出される酸化ガ
スの排出ラインに、排ガスタービン過給機の排ガスター
ビンを組み込み、且つ該排ガスタービンの下流側の排出
ライン位置より分岐した排ガス分岐ラインを、上記排ガ
スタービン過給機のコンプレッサの吸気側に接続したこ
とを特徴とする溶融炭酸塩型燃料電池のカソードリサイ
クル装置。
1) Discharge from the cathode in a molten carbonate fuel cell in which a tile impregnated with molten carbonate is sandwiched between a cathode and an anode, and oxidizing gas is supplied to the cathode side and fuel gas is supplied to the anode side. The exhaust gas turbine of the exhaust gas turbine supercharger is installed in the exhaust line of the oxidizing gas, and the exhaust gas branch line branched from the exhaust line position on the downstream side of the exhaust gas turbine is connected to the intake side of the compressor of the exhaust gas turbine supercharger. A cathode recycling device for a molten carbonate fuel cell, characterized in that the device is connected to a molten carbonate fuel cell.
JP62112544A 1987-05-11 1987-05-11 Cathode recycle device for fused carbonate fuel cell Pending JPS63279576A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62112544A JPS63279576A (en) 1987-05-11 1987-05-11 Cathode recycle device for fused carbonate fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62112544A JPS63279576A (en) 1987-05-11 1987-05-11 Cathode recycle device for fused carbonate fuel cell

Publications (1)

Publication Number Publication Date
JPS63279576A true JPS63279576A (en) 1988-11-16

Family

ID=14589306

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62112544A Pending JPS63279576A (en) 1987-05-11 1987-05-11 Cathode recycle device for fused carbonate fuel cell

Country Status (1)

Country Link
JP (1) JPS63279576A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996013871A2 (en) * 1994-10-19 1996-05-09 Siemens Aktiengesellschaft Fuel cell plant with utilization of the cathode heat, and process for operating it
WO2000039874A1 (en) * 1998-12-28 2000-07-06 International Fuel Cells, Llc Pressurized water recovery system for a fuel cell power plant
JP2000348749A (en) * 1999-06-01 2000-12-15 Ishikawajima Harima Heavy Ind Co Ltd Starting method of fuel cell power generation plant
JP2001015134A (en) * 1999-06-29 2001-01-19 Ishikawajima Harima Heavy Ind Co Ltd Combined power generating device of fuel cell with gas turbine

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996013871A2 (en) * 1994-10-19 1996-05-09 Siemens Aktiengesellschaft Fuel cell plant with utilization of the cathode heat, and process for operating it
WO1996013871A3 (en) * 1994-10-19 1996-06-13 Siemens Ag Fuel cell plant with utilization of the cathode heat, and process for operating it
WO2000039874A1 (en) * 1998-12-28 2000-07-06 International Fuel Cells, Llc Pressurized water recovery system for a fuel cell power plant
US6171718B1 (en) * 1998-12-28 2001-01-09 International Fuel Cells, Llc Pressurized water recovery system for a fuel cell power plant
JP2000348749A (en) * 1999-06-01 2000-12-15 Ishikawajima Harima Heavy Ind Co Ltd Starting method of fuel cell power generation plant
JP2001015134A (en) * 1999-06-29 2001-01-19 Ishikawajima Harima Heavy Ind Co Ltd Combined power generating device of fuel cell with gas turbine

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