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JPH0622152B2 - Electrolyte replenishment method for molten carbonate fuel cell power generator - Google Patents
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JPH0622152B2 - Electrolyte replenishment method for molten carbonate fuel cell power generator - Google Patents

Electrolyte replenishment method for molten carbonate fuel cell power generator

Info

Publication number
JPH0622152B2
JPH0622152B2 JP61006422A JP642286A JPH0622152B2 JP H0622152 B2 JPH0622152 B2 JP H0622152B2 JP 61006422 A JP61006422 A JP 61006422A JP 642286 A JP642286 A JP 642286A JP H0622152 B2 JPH0622152 B2 JP H0622152B2
Authority
JP
Japan
Prior art keywords
electrolyte
fuel cell
storage tank
molten carbonate
lioh
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 - Fee Related
Application number
JP61006422A
Other languages
Japanese (ja)
Other versions
JPS62165871A (en
Inventor
嘉男 岩瀬
俊樹 加原
浩一 三次
秀夫 岡田
将人 竹内
弘毅 田村
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP61006422A priority Critical patent/JPH0622152B2/en
Publication of JPS62165871A publication Critical patent/JPS62165871A/en
Publication of JPH0622152B2 publication Critical patent/JPH0622152B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • H01M8/04276Arrangements for managing the electrolyte stream, e.g. heat exchange
    • H01M8/04283Supply means of electrolyte to or in matrix-fuel cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/14Fuel cells with fused electrolytes
    • H01M2008/147Fuel cells with molten carbonates
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0048Molten electrolytes used at high temperature
    • H01M2300/0051Carbonates
    • 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

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】 〔発明の利用分野〕 本発明は運転中減少する電解質量を自動的に検知し、補
給する機構を有する燃料電池発電装置に関する。
Description: FIELD OF THE INVENTION The present invention relates to a fuel cell power generator having a mechanism for automatically detecting and replenishing an electrolytic mass that decreases during operation.

〔発明の背景〕[Background of the Invention]

溶融炭酸塩型燃料電池はリン酸型に続く第2世代の電力
用の燃料電池であり、発電効率が高く、LNGから石炭
まで幅広い燃料が使用出来る上に、電極材料として白金
を使用しない等の利点を持つために、国内外での研究開
発は強力に推進されている。溶融炭酸塩型燃料電池はそ
の名称が示すように、高温(498℃)で溶融する強ア
ルカリの炭酸塩を電解質として使用し、650℃程度の
温度で作動させるものである。
The molten carbonate fuel cell is a second-generation fuel cell for electric power following the phosphoric acid fuel cell, has high power generation efficiency, can use a wide range of fuels from LNG to coal, and does not use platinum as an electrode material. In order to have the advantage, domestic and foreign R & D is strongly promoted. As its name implies, the molten carbonate fuel cell uses a strong alkaline carbonate that melts at high temperature (498 ° C.) as an electrolyte and operates at a temperature of about 650 ° C.

この型の燃料電池発電装置における最大の問題は、電解
質板からの電解質の逃散,消失である。この為に電池本
体内の内部抵抗が増大すると共に電解質板マトリツクス
を通して、燃料ガスと酸化ガスが貫通して流れてしまう
“クロスオーバー”現象が起き、電池特性は急速に低下
し、発電が不可能となる。
The biggest problem in this type of fuel cell power generator is the escape and disappearance of the electrolyte from the electrolyte plate. As a result, the internal resistance of the battery increases and a “crossover” phenomenon occurs in which the fuel gas and the oxidizing gas flow through the electrolyte plate matrix, causing rapid deterioration of the battery characteristics and making power generation impossible. Becomes

この“クロスオーバー”を引き起こす原因である電解質
の電池外部への流出及び電極による吸収は電解質板の保
持力の不足によるものであり、電解質板マトリツクスの
改善が望まれるが、機械的強度が強い上に、空孔率も高
く、保持力も大きくなければならないといつた、言うな
れば相反する条件が電解質板には要求されており、さら
に生産性を考慮すると電解質板の保持力を飛躍的に改善
することは難しい。さらに、電解質が反応ガス(排気ガ
ス)中及び電池外部雰囲気中へ蒸発することは電解質板
保持力に関係なく起こる現象であり、これを防止する方
法は今のところ見つかつていない。このように、電解質
の損失を解決することは難しく、これがこの発電装置の
実用化を大きく阻害していると言うことができる。
The electrolyte outflow to the outside of the battery and the absorption by the electrodes that cause this "crossover" are due to the lack of holding power of the electrolyte plate, and improvement of the electrolyte plate matrix is desired, but the mechanical strength is high. In addition, the porosity must be high and the holding power must be large. In other words, the electrolyte plate is required to have contradictory conditions. Considering productivity, the holding power of the electrolyte plate is dramatically improved. Difficult to do. Further, the evaporation of the electrolyte into the reaction gas (exhaust gas) and the atmosphere outside the battery is a phenomenon that occurs regardless of the holding power of the electrolyte plate, and a method for preventing this has not yet been found. As described above, it is difficult to solve the loss of the electrolyte, and it can be said that this greatly hinders the practical use of this power generation device.

この問題を解決する方法として考えられるのが電解質を
補給する方法である。電池を解体して補給することがで
きれば好都合であるが、この型の燃料電池は650℃と
いう高温の作動温度では解体という作業は不可能であ
り、作業可能な温度では電解質は固体となりセパレータ
ごと密着してしまうため、再作動可能な解体は出来な
い。そこで考えられるのは作業中に電解質を補給する方
法である。即ち、文献ユーエス デパートメント オブ
エナージ(U.S.DEPARTMENT OF ENEGY),No.AC03
−77 ET11319 April1980,p.p3−77〜3−79に記されて
いるように、貯蔵槽及び供給管中に電解質板と同じ細孔
分布を持つマトリツクスを充てんさせ、液体の状態で貯
蔵する方法である。貯蔵槽,供給管内にもマトリツクス
を充てんさせるのは電解質の量を電池本体内部と外部で
平衡に保つためである。そして電池作動中に電解質板の
電解質が一部消失すると平衡を保つために貯蔵槽の溶融
電解質が電解質板側に補給される。
A method for resolving this problem is to replenish the electrolyte. It would be convenient if the battery could be disassembled and replenished, but this type of fuel cell cannot be disassembled at an operating temperature as high as 650 ° C. At the workable temperature, the electrolyte becomes a solid and adheres together with the separator. Therefore, it cannot be dismantled so that it can be re-operated. A possible solution is to replenish the electrolyte during the work. That is, the document US Department of Energy (No.AC03), US DEPARTMENT OF ENEGY
-77 ET11319 April 1980, p.p3-77 to 3-79, a method of storing a liquid state by filling a storage tank and a supply pipe with a matrix having the same pore size distribution as that of the electrolyte plate. Is. The matrix is also filled in the storage tank and the supply pipe in order to keep the amount of electrolyte in equilibrium inside and outside the battery body. When the electrolyte in the electrolyte plate partially disappears during the operation of the battery, the molten electrolyte in the storage tank is replenished to the electrolyte plate side to maintain equilibrium.

しかし、この装置では、本体内部の細孔が小さすぎる場
合には、電極を濡らし過ぎる結果となり、電極のガス拡
散が悪くなり、三相界面が減少するため、性能が低下し
てしまう。本体外部の細孔が小さすぎる場合には、貯蔵
電解質を本体内部の電解質板中に補供しないばかりか逆
にすいとつてしまい、本来の目的と反対の結果となる。
However, in this device, when the pores inside the main body are too small, the electrode becomes too wet, gas diffusion of the electrode deteriorates, and the three-phase interface decreases, so that the performance deteriorates. If the pores outside the body are too small, the storage electrolyte will not be supplemented in the electrolyte plate inside the body, but will also be contaminated, resulting in the opposite of the intended purpose.

このように電解質を液体として貯蔵することは難しい点
が多い。更に、本燃料電池の電解質は強アルカリである
ため、貯蔵槽及び供給管の材料の面においても耐食性の
優れたものを選択せねばならない。
As described above, it is difficult to store the electrolyte as a liquid. Furthermore, since the electrolyte of the present fuel cell is a strong alkali, it is necessary to select a material having excellent corrosion resistance in terms of materials for the storage tank and the supply pipe.

〔発明の目的〕[Object of the Invention]

本発明の目的は、燃料電池本体に適切に電解質を供給す
ることにより、電解質の不足による電池性能の低下を防
止して電池本体の寿命をのばし、溶融炭酸塩型燃料電池
発電装置の長期安定運転を可能にするためにある。
An object of the present invention is to appropriately supply an electrolyte to a fuel cell main body, thereby preventing deterioration of cell performance due to lack of electrolyte to prolong the life of the cell main body, and to ensure stable long-term operation of a molten carbonate fuel cell power generator. Is to enable.

〔発明の概要〕[Outline of Invention]

本発明は、燃料極、空気極及びLi2CO3とK2CO3
混合溶融炭酸塩電解質を保持する電解質板からなる電池
本体の、前記電解質板の電解質量を検知し、該検知信号
により電解質貯蔵槽の電解質を前記電解質板へ補給する
溶融炭酸塩型燃料電池発電装置の電解質補給方法におい
て、前記電解質貯蔵槽にLiOHとKOHを固体状態で
貯蔵し、前記検知信号によって、前記電解質貯蔵槽内の
LiOHとKOHを融点以上に加熱し、前記融点以上に
加熱されたLiOHとKOHを反応槽に供給してCO2
と接触させてLi2CO3とK2CO3にした後、前記電解
質板に補給することを特徴とする。
The present invention detects the electrolytic mass of the electrolyte plate of a battery body composed of a fuel electrode, an air electrode, and an electrolyte plate holding a mixed molten carbonate electrolyte of Li 2 CO 3 and K 2 CO 3 , and detects the electrolytic mass by the detection signal. In an electrolyte replenishing method of a molten carbonate fuel cell power generator for replenishing an electrolyte of an electrolyte storage tank to the electrolyte plate, LiOH and KOH are stored in a solid state in the electrolyte storage tank, and the electrolyte storage tank is stored according to the detection signal. LiOH and KOH in the interior are heated to a melting point or higher, and LiOH and KOH heated to a temperature higher than the melting point are supplied to a reaction tank to produce CO 2
It is characterized in that it is contacted with Li 2 CO 3 and K 2 CO 3 and then replenished to the electrolyte plate.

電解質貯蔵槽にLiOHとKOHとを固体状態で貯蔵し
電解質補給時にCO2と接触させて炭酸塩に変換するこ
とにより、Li2CO3とK2CO3の形態で貯蔵するより
も、貯蔵槽の腐食を少なく抑えることができる。
LiOH and KOH are stored in a solid state in an electrolyte storage tank, and are contacted with CO 2 at the time of replenishing the electrolyte to convert it into a carbonate, so that the storage tank is stored in the form of Li 2 CO 3 and K 2 CO 3. Corrosion can be suppressed to a minimum.

また、本発明によれば前記電解質貯蔵槽のLiOHとK
OHを加熱して液体状にし、補給に必要な量だけLi2
CO3とK2CO3に変換し、電解質を電池に補給するこ
とができる。これにより、下記(イ)(ロ)の効果が得られ
る。
Also, according to the present invention, LiOH and K in the electrolyte storage tank
OH is heated to a liquid state, and Li 2
It can be converted to CO 3 and K 2 CO 3 to replenish the battery with electrolyte. As a result, the following effects (a) and (b) can be obtained.

(イ)電解質貯蔵槽にLi2CO3及びK2CO3の形態で貯
蔵しておいて補給するよりも、電解質補給の応答性を高
めることができ、迅速な電解質の補給が可能になる。
(A) The responsiveness of electrolyte replenishment can be enhanced and the electrolyte can be replenished quickly compared to the case of replenishing after storing Li 2 CO 3 and K 2 CO 3 in the electrolyte storage tank.

LiOH及びKOHの融点は、それぞれ、LiOHが4
77℃、KOHが404℃であり、その混合物(LiOH:K
OH=62:38)の融点は259℃である。
The melting points of LiOH and KOH are respectively 4 for LiOH.
77 ℃, KOH is 404 ℃, the mixture (LiOH: K
The melting point of OH = 62: 38) is 259 ° C.

また、他の組成の混合物(LiOH:KOH=40:60或は82:1
8)の融点は310℃である。
In addition, mixtures of other compositions (LiOH: KOH = 40: 60 or 82: 1)
The melting point of 8) is 310 ° C.

一方、Li2CO3の融点は618℃、K2CO3の融点は
891℃であり、その混合物(Li2CO3:K2CO3=6
2:38)の融点は498℃である。
On the other hand, the melting point of Li 2 CO 3 is 618 ° C., the melting point of K 2 CO 3 is 891 ° C., and its mixture (Li 2 CO 3 : K 2 CO 3 = 6).
The melting point of 2:38) is 498 ° C.

このように、LiOH及びKOHの融点はLi2CO3
びK2CO3のそれに比べて著しく低いので、溶解させる
ために必要な熱エネルギーが少なくて済み、溶解に要す
る時間も短くできるので、迅速に補給できるようにな
る。
Thus, since the melting points of LiOH and KOH are remarkably lower than those of Li 2 CO 3 and K 2 CO 3 , less heat energy is required for melting and the time required for melting can be shortened. Will be able to replenish.

(ロ)Li2CO3とK2CO3の形態よりもLiOHとKO
Hの形態の方が、固−液間の体積変化が小さく、固−液
変態に伴い電解質貯蔵槽容器に加わる応力の影響も少な
いので、容器の劣化や破壊を防ぎ、容器寿命の長期化が
可能である。
(B) LiOH and KO rather than Li 2 CO 3 and K 2 CO 3 forms
The H form has a smaller volume change between the solid and the liquid and is less affected by the stress applied to the electrolyte storage container due to the solid and liquid transformation. Therefore, deterioration and destruction of the container are prevented, and the life of the container is prolonged. It is possible.

つまり、電解質貯蔵槽内の電解質原料は、電解質補給の
度に加熱及び冷却され、体積変化が繰り返されるが、本
発明によれば、Li2CO3及びK2CO3の形態で貯蔵す
るものに較べて、前記体積変化の繰り返しに起因する電
解質貯蔵槽の疲労、劣化及び破壊を抑制することができ
る。
That is, the electrolyte raw material in the electrolyte storage tank is heated and cooled every time the electrolyte is replenished, and the volume change is repeated. According to the present invention, the electrolyte raw material is stored in the form of Li 2 CO 3 and K 2 CO 3. In comparison, fatigue, deterioration and destruction of the electrolyte storage tank due to the repeated volume change can be suppressed.

電解質の不足を検知する代表的な方法としては、まず、
電池本体の内部抵抗(液抵抗)を測定する方法がある。電
池本体の内部抵抗(液抵抗)は、電解質板内の電解質保持
量によって異なる。電解質が十分に保持されていれば、
炭酸イオン(CO3 2-)の移動は容易であるため液抵抗も
低い値であるが、その保持量が減少するに従って抵抗値
は増大する。このことから、電池本体の内部抵抗(液抵
抗)を連続的に測定し、その値の増大により電解質不足
を検知することができる。
As a typical method to detect the lack of electrolyte, first,
There is a method to measure the internal resistance (liquid resistance) of the battery body. The internal resistance (liquid resistance) of the battery body varies depending on the amount of electrolyte retained in the electrolyte plate. If the electrolyte is well retained,
Since the carbonate ions (CO 3 2 −) move easily, the liquid resistance also has a low value, but the resistance value increases as the retained amount decreases. From this, it is possible to continuously measure the internal resistance (liquid resistance) of the battery main body and detect the electrolyte shortage by the increase of the value.

他の方法は酸素センサー、水素センサー(ガスクロマト
グラフィー装置を含む。)により、クロスオーバーによ
り生じたクロスガスを検出する方法である。クロスオー
バー現象の起きる原因としては、電解質板の中の電解質
の消失により生じた細孔を通してガスクロスが起こる場
合と、電解質板の割れによって生じたヒビを通して起こ
る場合がる。
The other method is a method of detecting a cross gas generated by crossover with an oxygen sensor and a hydrogen sensor (including a gas chromatography device). The cause of the crossover phenomenon is that gas crossing occurs through the pores generated by the disappearance of the electrolyte in the electrolyte plate, or through cracks caused by the cracking of the electrolyte plate.

後者が原因である場合は余分は電解質を供給する危険性
もあるが、電解質板の割れは電池寿命の上ではむしろ致
命的であり、この場合は運転を止めなければならない。
割れは電解質製造法の改善により、電解質板の強度を増
せば無くすことができる。将来的にはクロスオーバー現
象の原因としては電解質の消失による不足のみが残り、
クロスしたガスの検知により、電解質補給の信号源とす
ることができる。
If the latter is the cause, there is a risk of supplying extra electrolyte, but cracking of the electrolyte plate is rather fatal in terms of battery life, and in this case the operation must be stopped.
The cracks can be eliminated by improving the strength of the electrolyte plate by improving the electrolyte manufacturing method. In the future, the only cause of the crossover phenomenon will be the lack of electrolytes,
By detecting the crossed gas, it can be used as a signal source for electrolyte replenishment.

〔実施例〕〔Example〕

第1図は比較例であり、電解質を電解質貯蔵槽から電池
に直接供給する電解質補給システムの概略図である。L
2CO3とK2CO3との混合塩を固体状態で、電解質貯
蔵槽2に貯蔵し、必要に応じて液化させ、電池本体に供
給する燃料電池発電装置である。図中6は電解質として
Li2CO3とK2CO3との混合溶融塩を用い、燃料極に
は水素、空気極には空気と炭酸ガスの混合ガスを供給す
ることにより発電する燃料電池本体である。
FIG. 1 is a comparative example and is a schematic view of an electrolyte replenishing system for supplying an electrolyte directly from an electrolyte storage tank to a battery. L
This is a fuel cell power generator in which a mixed salt of i 2 CO 3 and K 2 CO 3 is stored in a solid state in the electrolyte storage tank 2, liquefied if necessary, and supplied to the cell body. Reference numeral 6 in the figure is a fuel cell main body for generating electricity by using a mixed molten salt of Li 2 CO 3 and K 2 CO 3 as an electrolyte, supplying hydrogen to the fuel electrode and supplying a mixed gas of air and carbon dioxide to the air electrode. Is.

前記燃料電池での長期運転による電解質不足を検知する
検知器4を備え、該検知器の信号によりリレースイッチ
3が働き、電解質貯蔵槽2内の前記Li2CO3とK2
3とを加熱し液化して、電解質供給管5を通して燃料
電池本体1に供給する。
A detector 4 for detecting electrolyte shortage due to long-term operation in the fuel cell is provided, and a relay switch 3 is activated by a signal of the detector to cause the Li 2 CO 3 and K 2 C in the electrolyte storage tank 2 to operate.
O 3 and liquefied are heated and supplied to the fuel cell main body 1 through the electrolyte supply pipe 5.

電解質が十分に補給されると、検知器4により、リレー
スイッチ3が再び働き、電解質原料の加熱は停止され
る。
When the electrolyte is sufficiently replenished, the detector 4 causes the relay switch 3 to operate again, and the heating of the electrolyte raw material is stopped.

第2図は本発明の実施例である。FIG. 2 shows an embodiment of the present invention.

図中6は電解質としてLi2CO3とK2CO3との混合溶
融塩を用い、燃料極には水素、空気極には空気と炭酸ガ
スの混合ガスを供給することにより発電する燃料電池本
体である。
Reference numeral 6 in the figure is a fuel cell main body for generating electricity by using a mixed molten salt of Li 2 CO 3 and K 2 CO 3 as an electrolyte, supplying hydrogen to the fuel electrode and supplying a mixed gas of air and carbon dioxide to the air electrode. Is.

電解質貯蔵槽7ではLiOHとKOHとが固体状態で貯
蔵されている。
In the electrolyte storage tank 7, LiOH and KOH are stored in a solid state.

前記燃料電池本体の電解質不足を検知する検知器9を備
え、該検知器の信号によりリレースイッチ8が働き、電
解質液化の熱源となる高温流体が、前記電解質貯蔵槽7
などの外部を矢印にそって巡環し、電解質を加熱して液
化する。
A detector 9 for detecting the electrolyte shortage of the fuel cell main body is provided, and the relay switch 8 is actuated by the signal of the detector, and the high temperature fluid serving as a heat source for electrolyte liquefaction is stored in the electrolyte storage tank 7
The outside is circulated along the arrow, and the electrolyte is heated and liquefied.

前記電解質貯蔵槽7内の液化した前記水酸化物を、フィ
ーダ12により反応槽13へ取出し、加熱しつつCO2
と接触させて前記炭酸塩に変換し、電解質供給管10を
通して燃料電池本体6に供給する。
The liquefied hydroxide in the electrolyte storage tank 7 is taken out to the reaction tank 13 by the feeder 12 and heated to CO 2
It is converted into the above-mentioned carbonate by contacting with and is supplied to the fuel cell main body 6 through the electrolyte supply pipe 10.

電解質が十分に補給されると、検知器9により、リレー
スイッチ8が再び働き、電解質原料の液化及びCO2
の接触は停止される。
When the electrolyte is sufficiently replenished, the detector 9 causes the relay switch 8 to operate again, and the liquefaction of the electrolyte raw material and the contact with CO 2 are stopped.

本発明によれば前記電解質貯蔵槽のLiOHとKOHを
加熱して液体状にし、電解質供給に必要な量だけLi2
CO3とK2CO3とに変換し、電池に供給することがで
きる。
According to the present invention, LiOH and KOH in the electrolyte storage tank are heated into a liquid state, and Li 2 and KOH are added in an amount necessary for supplying the electrolyte.
It can be converted into CO 3 and K 2 CO 3 and supplied to the battery.

なお、前記貯蔵層の空間部は炭酸ガス、純窒素ガス、ま
たはアルゴン等の酸化防止ガスが供給されていることが
望ましい。
In addition, it is desirable that an antioxidant gas such as carbon dioxide gas, pure nitrogen gas, or argon is supplied to the space portion of the storage layer.

電池本体の電解質不足を検知する前記検知器は液抵抗測
定装置を用いることが望ましい。該検知器は液抵抗値が
一定値より大きくなると、リレースイッチ8が作動する
ようにすることが好ましい。
It is desirable to use a liquid resistance measuring device as the detector for detecting the electrolyte shortage in the battery body. The detector preferably activates the relay switch 8 when the liquid resistance value exceeds a certain value.

なお、前記高温流体は排熱有効利用の上から、電池本体
又は外部リフォーマの排ガスを使用することが望まし
い。
In addition, it is desirable to use the exhaust gas of the battery main body or the external reformer as the high temperature fluid from the viewpoint of effective utilization of exhaust heat.

また、前記電解質を加熱する際は、前記の手段の他に、
発電電力の一部を使用して前記貯蔵槽等にヒーターを設
けて、それを作動させてもよい。
Further, when heating the electrolyte, in addition to the above means,
A heater may be provided in the storage tank or the like and a part of the generated power may be used to operate the heater.

前記電解質供給管はSUS管を使用することもできる
が、α−Al23管であることが望ましい。
The electrolyte supply pipe may be a SUS pipe, but is preferably an α-Al 2 O 3 pipe.

反応槽13の内部では以下の反応が進行する。The following reactions proceed inside the reaction tank 13.

2LiOH+CO2→Li2CO3+H23…(1) 2KOH+CO2→K2CO3+H2O …(2) (1)式、(2)式の水酸化物は加熱及び炭酸ガスの供給に
より炭酸塩となる。炭酸塩の混合比は、原料として供給
する水酸化物のモル比により決定される。例えば、希望
する炭酸塩の混合比がLi2CO3:K2CO3=62:38
であるなら、水酸化物をLiOH:KOH=62:38で
供給すればよい。
2LiOH + CO 2 → Li 2 CO 3 + H 2 O 3 (1) 2KOH + CO 2 → K 2 CO 3 + H 2 O (2) The hydroxides of the formulas (1) and (2) are heated and supplied with carbon dioxide gas. It becomes a carbonate. The mixing ratio of the carbonate is determined by the molar ratio of the hydroxide supplied as the raw material. For example, the desired mixing ratio of carbonate is Li 2 CO 3 : K 2 CO 3 = 62: 38.
If so, the hydroxide may be supplied as LiOH: KOH = 62: 38.

また、反応槽13で前記水酸化物をCO2と接触させて
炭酸塩としたときに生じた水蒸気はアノードのシフト反
応によるカーボン析出を防止するために、アノードの反
応ガス中に混合させることも可能である。
Further, the steam generated when the hydroxide is brought into contact with CO 2 in the reaction tank 13 to form a carbonate may be mixed with the reaction gas of the anode in order to prevent carbon deposition due to the shift reaction of the anode. It is possible.

第3図に、実施例に示された燃料電池発電装置の性能の
経時変化を示した。電解質補充がなされない発電装置の
場合は、2000時間を超えると破線のように性能(電
池電圧E)が低下するが、電解質が補充される本発明の
実施例の発電装置では、6000時間以上の寿命が記録
された。
FIG. 3 shows the change over time in the performance of the fuel cell power generator shown in the examples. In the case of a power generator that is not replenished with electrolyte, the performance (battery voltage E) decreases as indicated by the broken line after more than 2000 hours, but in the power generator of the embodiment of the present invention in which electrolyte is replenished, the performance of 6000 hours or more Lifespan was recorded.

〔発明の効果〕〔The invention's effect〕

本発明によれば、燃料電池本体中の電解質板に必要時に
適当量の電解質を迅速に補給することができるため、電
池本体の寿命を延ばし、溶融炭酸塩型燃料電池の長期安
定運転が可能となる。
According to the present invention, the electrolyte plate in the fuel cell body can be quickly replenished with an appropriate amount of electrolyte when necessary, so that the life of the cell body can be extended and the molten carbonate fuel cell can be stably operated for a long period of time. Become.

【図面の簡単な説明】[Brief description of drawings]

第1図は比較例であり、炭酸塩電解質を電解質貯蔵槽か
ら電池に直接供給する電解質補給システムの概略図、第
2図は本発明の一実施例の電解質補給システムの概略
図、第3図は本発明の経時変化を示す図である。 1,6……燃料電池本体、2,7……電解質貯蔵槽、
3,8……リレースイツチ、4,9……検知器、5,1
0……電解質補給管、11……炭酸ガスライン、12…
…フイーダ、13……反応槽。
FIG. 1 is a comparative example, and is a schematic diagram of an electrolyte replenishing system for supplying a carbonate electrolyte directly from an electrolyte storage tank to a battery, and FIG. 2 is a schematic diagram of an electrolyte replenishing system of one embodiment of the present invention, and FIG. FIG. 3 is a diagram showing a change with time of the present invention. 1,6 ... Fuel cell body, 2,7 ... electrolyte storage tank,
3, 8 ... Relay switch, 4, 9 ... Detector, 5, 1
0 ... Electrolyte supply pipe, 11 ... Carbon dioxide line, 12 ...
... Feeder, 13 ... Reaction tank.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 岡田 秀夫 茨城県日立市久滋町4026番地 株式会社日 立製作所日立研究所内 (72)発明者 竹内 将人 茨城県日立市久滋町4026番地 株式会社日 立製作所日立研究所内 (72)発明者 田村 弘毅 茨城県日立市久滋町4026番地 株式会社日 立製作所日立研究所内 (56)参考文献 特開 昭60−264055(JP,A) 特開 昭60−264054(JP,A) 特開 昭61−214367(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Hideo Okada, 4026 Kushimachi, Hitachi City, Hitachi, Ibaraki Prefecture, Hitachi Research Institute, Ltd. (72) Masato Takeuchi, 4026, Kushimachi, Hitachi City, Ibaraki, Hitachi, Ltd. Hitachi Research Laboratory (72) Inventor Hiroki Tamura 4026 Kushimachi, Hitachi City, Ibaraki Prefecture Hitachi Research Laboratory, Hitachi, Ltd. (56) Reference JP 60-264055 (JP, A) JP 60-264054 (JP) JP, A) JP-A-61-214367 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】燃料極、空気極及びLi2CO3とK2CO3
の混合溶融炭酸塩電解質を保持する電解質板からなる電
池本体の、前記電解質板の電解質量を検知し、該検知信
号により電解質貯蔵槽の電解質を前記電解質板へ補給す
る溶融炭酸塩型燃料電池発電装置の電解質補給方法にお
いて、前記電解質貯蔵槽にLiOHとKOHを固体状態
で貯蔵し、前記検知信号によって、前記電解質貯蔵槽内
のLiOHとKOHを融点以上に加熱し、前記融点以上
に加熱されたLiOHとKOHを反応槽に供給してCO
2と接触させてLi2CO3とK2CO3にした後、前記電
解質板に補給することを特徴とする溶融炭酸塩型燃料電
池発電装置の電解質補給方法。
1. A fuel electrode, an air electrode, and Li 2 CO 3 and K 2 CO 3
A molten carbonate fuel cell power generation for detecting the electrolytic mass of the electrolyte plate of a battery main body composed of an electrolyte plate holding a mixed molten carbonate electrolyte, and supplying the electrolyte in the electrolyte storage tank to the electrolyte plate by the detection signal. In the electrolyte replenishing method of the apparatus, LiOH and KOH are stored in the electrolyte storage tank in a solid state, and LiOH and KOH in the electrolyte storage tank are heated to a melting point or higher by the detection signal and heated to the melting point or higher. Supplying LiOH and KOH to the reaction tank, CO
A method for replenishing electrolyte in a molten carbonate fuel cell power generator, comprising replenishing the electrolyte plate after contacting with 2 to form Li 2 CO 3 and K 2 CO 3 .
JP61006422A 1986-01-17 1986-01-17 Electrolyte replenishment method for molten carbonate fuel cell power generator Expired - Fee Related JPH0622152B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61006422A JPH0622152B2 (en) 1986-01-17 1986-01-17 Electrolyte replenishment method for molten carbonate fuel cell power generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61006422A JPH0622152B2 (en) 1986-01-17 1986-01-17 Electrolyte replenishment method for molten carbonate fuel cell power generator

Publications (2)

Publication Number Publication Date
JPS62165871A JPS62165871A (en) 1987-07-22
JPH0622152B2 true JPH0622152B2 (en) 1994-03-23

Family

ID=11637935

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61006422A Expired - Fee Related JPH0622152B2 (en) 1986-01-17 1986-01-17 Electrolyte replenishment method for molten carbonate fuel cell power generator

Country Status (1)

Country Link
JP (1) JPH0622152B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7939219B2 (en) 2005-05-27 2011-05-10 Fuelcell Energy, Inc. Carbonate fuel cell and components thereof for in-situ delayed addition of carbonate electrolyte
CN111883733A (en) * 2020-04-15 2020-11-03 浙江安力能源有限公司 Electrolyte injection device and method

Also Published As

Publication number Publication date
JPS62165871A (en) 1987-07-22

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