JPH04249075A - Zn-br battery - Google Patents

Zn-br battery

Info

Publication number
JPH04249075A
JPH04249075A JP3013602A JP1360291A JPH04249075A JP H04249075 A JPH04249075 A JP H04249075A JP 3013602 A JP3013602 A JP 3013602A JP 1360291 A JP1360291 A JP 1360291A JP H04249075 A JPH04249075 A JP H04249075A
Authority
JP
Japan
Prior art keywords
electrolyte
concentration
zinc
temperature
battery
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
JP3013602A
Other languages
Japanese (ja)
Inventor
Nobuo Watanabe
修夫 渡辺
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor 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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP3013602A priority Critical patent/JPH04249075A/en
Publication of JPH04249075A publication Critical patent/JPH04249075A/en
Pending legal-status Critical Current

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Classifications

    • 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
    • Y02E60/10—Energy storage using batteries

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  • Secondary Cells (AREA)
  • Hybrid Cells (AREA)

Abstract

PURPOSE:To provide a Zn-Br battery, whose charged condition can be sensed accurately at any arbitrary temperature. CONSTITUTION:Arrangement according to the present invention is equipped with concentration sensing means 32a,32b and ones 33a, 33b to sense the Zn ion concentration in electrolyte and also with temp. sensing means 31a, 31b. On the basis of temps. sensed by these temp. sensing means 31a, 31b, a calculating device 30 corrects the Zn ion concentration sensed by the concentration sensing means 32a, 32b and the ones 33a, 33b, and the battery charged condition calculated on the basis of the corrected value is displayed.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は亜鉛臭素電池、特に電解
液を循環して充放電反応を行う亜鉛臭素電池に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a zinc bromine battery, and more particularly to a zinc bromine battery in which charging and discharging reactions are carried out by circulating an electrolyte.

【0002】0002

【従来の技術】電解液貯蔵層と反応槽との間で電解液を
循環させ所定の充放電反応を行う形式の金属−臭素電池
、例えば亜鉛−臭素電池は新型電池の1つとして知られ
、正極および負極が設けられた反応槽内において式1に
示す基本的な電気化学反応が行われている。
BACKGROUND OF THE INVENTION A metal-bromine battery, such as a zinc-bromine battery, in which an electrolyte is circulated between an electrolyte storage layer and a reaction tank to carry out predetermined charging and discharging reactions, is known as a new type of battery. A basic electrochemical reaction shown in Formula 1 is carried out in a reaction tank provided with a positive electrode and a negative electrode.

【0003】0003

【式1】[Formula 1]

【0004】0004

【0005】この反応式からも明らかなように、充電時
には負極上に亜鉛Znが析出し、正極では臭素Br2 
が生成されこのBr2 は電解液中に溶解する。また、
放電時には、負極板上に析出された亜鉛Znが酸化され
てZn2+となって電解液中に溶解し、また電解液中の
臭素Br2 は還元されて臭素イオン2Br− となっ
て電解液中に同様に溶解する。
As is clear from this reaction equation, zinc Zn is deposited on the negative electrode during charging, and bromine Br2 is deposited on the positive electrode.
is generated and this Br2 is dissolved in the electrolyte. Also,
During discharge, zinc Zn deposited on the negative electrode plate is oxidized to become Zn2+ and dissolved in the electrolyte, and bromine Br2 in the electrolyte is reduced to become bromine ions 2Br- and similarly dissolved in the electrolyte. dissolve in

【0006】図4には、この様な原理を用いて形成され
た従来の亜鉛−臭素電池が示されており、この電池は、
反応槽10内の両側に正極13aおよび負極13bを設
け、これら両電極13a,13b間で電解液12を介し
て式1の電気化学反応を行っている。
FIG. 4 shows a conventional zinc-bromine battery formed using such a principle.
A positive electrode 13a and a negative electrode 13b are provided on both sides in the reaction tank 10, and the electrochemical reaction of formula 1 is performed between these electrodes 13a and 13b via an electrolytic solution 12.

【0007】この様な亜鉛−臭素電池では、電解液12
として臭化亜鉛(ZnBr2 )水溶液を用いており、
これに加えて必要に応じて電導度向上剤、臭素錯化剤、
デンドライト抑制剤等が添加されている。
In such a zinc-bromine battery, the electrolyte 12
Zinc bromide (ZnBr2) aqueous solution is used as
In addition to this, conductivity improvers, bromine complexing agents,
Contains dendrite inhibitors, etc.

【0008】そして、充電時には、反応槽10内におい
て、式1に示す充電反応が行われ、正極13a側では臭
素Br2 が生成され電解液12内に溶解し、また負極
13bでは亜鉛Znが析出し負極13b上に亜鉛の析出
層22が形成されていく。
[0008] During charging, the charging reaction shown in equation 1 is carried out in the reaction tank 10, and bromine Br2 is generated and dissolved in the electrolyte 12 at the positive electrode 13a, and zinc Zn is precipitated at the negative electrode 13b. A zinc precipitation layer 22 is gradually formed on the negative electrode 13b.

【0009】また、放電時には、前記充電時とは逆の反
応が行われ、正極13a側では臭素Br2 が還元され
て臭素イオン2Br− となって電解液12中に溶解し
、負極13b側では亜鉛の析出層22が酸化されて亜鉛
イオンZn2+となって電解液12中に溶解する。
Furthermore, during discharging, a reaction opposite to that during charging takes place; bromine Br2 is reduced on the positive electrode 13a side and becomes bromine ions 2Br-, which are dissolved in the electrolytic solution 12, and on the negative electrode 13b side, zinc The deposited layer 22 is oxidized to become zinc ions Zn2+ and dissolved in the electrolytic solution 12.

【0010】この様な電気化学反応が行われる反応槽1
0内は、充電時に発生する臭素Br2 により自己放電
が発生することがないよう、その内部がセパレータ膜1
1により正極側反応槽10aと負極側反応槽10bとに
分離されている。
[0010] Reaction tank 1 in which such an electrochemical reaction is carried out
0 indicates that the inside is covered with a separator film 1 to prevent self-discharge from occurring due to bromine Br2 generated during charging.
1 into a positive electrode side reaction tank 10a and a negative electrode side reaction tank 10b.

【0011】このセパレータ膜11は、自己放電を防止
するために電解液12は透過するがこれに溶解している
臭素Br2 の透過は阻止するものである。この様なセ
パレータ膜11としては、一般にイオン交換膜あるいは
多孔質膜が用いられるが、電池の内部抵抗を少なくする
という観点から多孔質膜が使用されている。
This separator film 11 allows the electrolytic solution 12 to pass therethrough in order to prevent self-discharge, but it blocks the penetration of bromine Br2 dissolved therein. As such a separator membrane 11, an ion exchange membrane or a porous membrane is generally used, and a porous membrane is used from the viewpoint of reducing the internal resistance of the battery.

【0012】そして、電解液循環型の電池では、充電時
における電解反応によって得たエネルギを貯蔵するため
、正極側電解液貯蔵槽14aと負極側電解液貯蔵槽14
bとが設けられている。
In the electrolyte circulation type battery, in order to store the energy obtained by the electrolytic reaction during charging, the positive electrode side electrolyte storage tank 14a and the negative electrode side electrolyte storage tank 14 are used.
b is provided.

【0013】前記正極側電解液貯蔵槽14aは正極側反
応槽10aとの間で配ダクト21a,17aを介して電
解液循環経路を構成しており、循環経路に設けたポンプ
15aにより正極側反応槽10a内において反応した正
極側電解液12aを貯蔵槽14aへ向け送り出し、貯蔵
槽14a内に貯蔵された新たな電解液12aを反応槽1
0aに供給している。
The positive electrode side electrolyte storage tank 14a and the positive electrode side reaction tank 10a constitute an electrolyte circulation path via distribution ducts 21a and 17a, and the positive electrode side reaction is carried out by a pump 15a provided in the circulation path. The positive electrode electrolyte 12a that has reacted in the tank 10a is sent to the storage tank 14a, and the new electrolyte 12a stored in the storage tank 14a is transferred to the reaction tank 1.
It is supplied to 0a.

【0014】ここにおいて、電解液12内に臭素錯化剤
が添加されている場合には、充電時に発生した臭素Br
2 は錯体化され、電解液12に不溶な錯化合物となっ
て析出し、第4図に示す電池において該錯化合物は貯蔵
槽14aの底部を錯体貯蔵部19としてここに順次沈澱
して貯蔵されていく。
Here, if a bromine complexing agent is added to the electrolytic solution 12, the bromine Br generated during charging
2 is complexed and precipitated as a complex compound insoluble in the electrolytic solution 12, and in the battery shown in FIG. To go.

【0015】また、この錯体貯蔵部19と配ダクト17
aとの間は、バルブ20を有する錯体供給ダクト23に
より連絡されている。そして、このバルブ20は、通常
解放されており、錯体貯蔵部19に沈澱した錯化合物を
配ダクト17aを介して反応槽10aに向けて放電用に
送り出す。
[0015] Furthermore, this complex storage section 19 and the distribution duct 17
a is connected by a complex supply duct 23 having a valve 20. This valve 20 is normally open, and the complex compound precipitated in the complex storage section 19 is sent out for discharge toward the reaction tank 10a via the distribution duct 17a.

【0016】また、前記負極側電解液貯蔵槽14bは、
同様にして負極側反応槽10bとの間で、配ダクト21
b,17bを介して電解液循環経路を形成しており、循
環経路に設けたポンプ15bを用い負極反応槽10b内
にて反応した負極側電解液12bを貯蔵槽14bへ向け
送り出し、貯蔵槽14bから新たな電解液12bを反応
槽10bに向け供給している。
[0016] Furthermore, the negative electrode side electrolyte storage tank 14b is
Similarly, the distribution duct 21 is connected to the negative electrode side reaction tank 10b.
An electrolytic solution circulation path is formed through the electrodes b and 17b, and a pump 15b provided in the circulation path is used to send out the negative electrode side electrolyte 12b reacted in the negative electrode reaction tank 10b toward the storage tank 14b. A new electrolytic solution 12b is supplied from the reactor to the reaction tank 10b.

【0017】この様に、この亜鉛−臭素電池は、貯蔵槽
14a,14b内に電解液12を十分に貯蔵し、該貯蔵
電解液12を用いて充電時には、式1に示す充電反応を
行い、錯体貯蔵部19に臭素の錯化合物を貯蔵し、負極
13b上に亜鉛の析出層22を形成して電力を貯蔵する
ことができる。また、放電時には、錯体貯蔵部19に貯
蔵されている臭素の錯化合物を正極側反応槽10aに向
け送り出し、該錯化合物と負極13b上に形成されてい
る亜鉛の析出層22とを用い、式1に示す放電反応を行
い、その充電電力を放出することができる。
As described above, this zinc-bromine battery sufficiently stores the electrolyte 12 in the storage tanks 14a and 14b, and when charging using the stored electrolyte 12, the charging reaction shown in equation 1 is performed, A bromine complex compound is stored in the complex storage section 19, and a zinc deposit layer 22 is formed on the negative electrode 13b, so that electric power can be stored. Further, during discharge, the bromine complex compound stored in the complex storage section 19 is sent out toward the positive electrode side reaction tank 10a, and using the complex compound and the zinc precipitation layer 22 formed on the negative electrode 13b, the formula The discharge reaction shown in 1 can be performed and the charging power can be released.

【0018】[0018]

【発明が解決しようとする課題】ここで、式1に示され
るように、電池の充放電に伴い電解液中の亜鉛イオンの
濃度が変動することがわかる。すなわち、電池が充電さ
れる際には電解液中の亜鉛イオンの濃度が減少すること
がわかり、放電に伴い電解液中の亜鉛イオンの濃度が増
大することがわかる。したがって、電解液中の亜鉛イオ
ンの濃度は電池の充電状態の指標となるものであり、実
際に、この電解液の亜鉛イオンの濃度検出を行うことに
より電池の充電状態(SOC)が検出されている。
[Problems to be Solved by the Invention] Here, as shown in Equation 1, it can be seen that the concentration of zinc ions in the electrolytic solution changes as the battery is charged and discharged. That is, it can be seen that the concentration of zinc ions in the electrolyte decreases when the battery is charged, and that the concentration of zinc ions in the electrolyte increases as the battery is discharged. Therefore, the concentration of zinc ions in the electrolyte is an indicator of the state of charge of the battery, and in fact, the state of charge (SOC) of the battery can be detected by detecting the concentration of zinc ions in the electrolyte. There is.

【0019】ところで、電解液中の亜鉛イオンの濃度を
検出するにあたっては、屈折率や伝導度や密度などを基
にした検出方法が使用されるが、これらは温度依存性が
あるので電池の電解液の温度変化によって、その検出値
に変動が生じる。
By the way, in order to detect the concentration of zinc ions in the electrolyte, detection methods based on refractive index, conductivity, density, etc. are used, but since these are temperature dependent, Changes in the temperature of the liquid cause fluctuations in the detected value.

【0020】しかし、従来装置においては、この検出値
の温度による変動を考慮していなかったため正確な充電
状態を検出できないという欠点があった。
However, the conventional device has the disadvantage that it cannot accurately detect the state of charge because it does not take into account the variation of the detected value due to temperature.

【0021】本発明は以上のような課題を鑑みてなされ
たものであり、その目的は任意の温度で正確に電池の充
電状態を検出することのできる検出機構を備えた亜鉛臭
素電池を提供することにある。
The present invention has been made in view of the above-mentioned problems, and its purpose is to provide a zinc bromine battery equipped with a detection mechanism that can accurately detect the state of charge of the battery at any temperature. There is a particular thing.

【0022】[0022]

【課題を解決するための手段】以上のような目的を達成
するために、本発明における亜鉛臭素電池においては、
電解液の亜鉛イオン濃度を検出する濃度検出手段と、電
解液の温度を検出する温度検出手段と、前記温度検出手
段のデータに基づき前記濃度検出手段により検出された
亜鉛イオン濃度を補正する濃度補正手段とを有し、電解
液の亜鉛イオン濃度を検出することを特徴とする。
[Means for Solving the Problems] In order to achieve the above objects, in the zinc bromine battery of the present invention,
concentration detection means for detecting the zinc ion concentration of the electrolytic solution; temperature detection means for detecting the temperature of the electrolytic solution; and concentration correction for correcting the zinc ion concentration detected by the concentration detection means based on the data of the temperature detection means. and means for detecting the zinc ion concentration of the electrolyte.

【0023】[0023]

【作用】以上のような構成を有する本発明に係る亜鉛臭
素電池においては、濃度検出手段により検出された電池
の電解液の亜鉛イオン濃度が温度検出手段により検出さ
れた電解液の温度に基づいて電解液の亜鉛イオン濃度が
補正され、これにより任意の温度において正確な電解液
の亜鉛イオン濃度を検出することが可能となる。
[Operation] In the zinc bromine battery according to the present invention having the above configuration, the zinc ion concentration of the battery electrolyte detected by the concentration detection means is determined based on the temperature of the electrolyte detected by the temperature detection means. The zinc ion concentration of the electrolyte is corrected, thereby making it possible to accurately detect the zinc ion concentration of the electrolyte at any temperature.

【0024】[0024]

【実施例】図1は、本発明に係る亜鉛臭素電池の一実施
例の構成を示した図である。なお、従来例と同一部材同
一構成要素には同一符号を付し、その説明を省略する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a diagram showing the structure of an embodiment of a zinc bromine battery according to the present invention. Note that the same members and constituent elements as in the conventional example are given the same reference numerals, and their explanations will be omitted.

【0025】本発明において特徴的なことは、濃度検出
手段32a及び32bならびに33a及び33bと、温
度検出手段31a及び31bが設置され、これらは演算
手段30に接続されていることである。ここで、電池が
セパレータ11により正極側と負極側に分離されており
、正極側電解液と負極側電解液の間では亜鉛イオン濃度
に差を生じている場合が多いため、実施例において、濃
度検出手段は正極側と負極側にそれぞれ分配されて設置
されている。すなわち、正極側には、正極側電解液12
aの電解液の亜鉛イオン濃度を検出するための濃度検出
手段32aならびに33aが設置されており、同時に温
度検出手段31aが設置されている。一方、負極側には
、負極側電解液の亜鉛イオン濃度を測定するために濃度
測定手段32bと33bが設置されており、同時に温度
検出手段31bが設置されている。
A characteristic feature of the present invention is that concentration detection means 32a and 32b, 33a and 33b, and temperature detection means 31a and 31b are provided, and these are connected to calculation means 30. Here, the battery is separated into a positive electrode side and a negative electrode side by a separator 11, and there is often a difference in zinc ion concentration between the positive electrode side electrolyte and the negative electrode side electrolyte. The detection means are distributed and installed on the positive electrode side and the negative electrode side, respectively. That is, on the positive electrode side, the positive electrode side electrolyte 12
Concentration detection means 32a and 33a for detecting the zinc ion concentration of the electrolytic solution a are installed, and at the same time, a temperature detection means 31a is installed. On the other hand, on the negative electrode side, concentration measuring means 32b and 33b are installed to measure the zinc ion concentration of the negative electrode side electrolyte, and at the same time, a temperature detecting means 31b is installed.

【0026】実施例において、濃度検出手段32a及び
32bには屈折率により電解液の亜鉛イオン濃度を検出
する屈折率センサを用いており、濃度検出手段33a及
び33bには密度により電解液の亜鉛イオン濃度を検出
する密度センサを用いている。これらによりそれぞれ検
出された電解液の亜鉛イオン濃度は、それぞれ演算手段
30に入力され、温度検出手段である温度センサ31a
及び31bにより検出された電解液の温度に基づいて温
度補正されることとなる。
In the embodiment, the concentration detecting means 32a and 32b use refractive index sensors that detect the zinc ion concentration in the electrolytic solution based on the refractive index, and the concentration detecting means 33a and 33b use refractive index sensors that detect the zinc ion concentration in the electrolytic solution based on the density. A density sensor is used to detect concentration. The zinc ion concentrations of the electrolyte solution detected by these methods are respectively input to the calculating means 30, and the temperature sensor 31a serving as the temperature detecting means
The temperature is corrected based on the temperature of the electrolytic solution detected by and 31b.

【0027】図2は、演算手段30の構成を示したブロ
ック図である。まず、濃度検出手段及び温度検出手段か
らの信号はアナログ/デジタル変換器(A/D変換器)
に入力され、ここでデジタル信号に変換される。そして
、このデジタル信号はマイクロコンピュータ40に入力
されてメモリ47内のデータと比較される。ここで、実
施例において、メモリ47には検量線法によって求めら
れたデータが備えられている。すなわち、温度に対する
亜鉛イオン濃度検出値の変化を実験的に求めたデータが
収納されているので、これを用いて任意の温度における
電解液の亜鉛イオン濃度が標準状態(25℃)での濃度
に補正される。そしてさらに、補正された亜鉛イオン濃
度検出値に基づいて算出された電池の充電状態が表示部
45において表示される。
FIG. 2 is a block diagram showing the configuration of the calculation means 30. First, the signals from the concentration detection means and temperature detection means are sent to an analog/digital converter (A/D converter).
and is converted into a digital signal here. This digital signal is then input to the microcomputer 40 and compared with the data in the memory 47. Here, in the embodiment, the memory 47 is provided with data determined by the calibration curve method. In other words, since it contains experimental data on changes in the detected zinc ion concentration with respect to temperature, this data can be used to calculate the zinc ion concentration of the electrolyte at any temperature to the concentration in the standard state (25°C). Corrected. Further, the state of charge of the battery calculated based on the corrected zinc ion concentration detection value is displayed on the display section 45.

【0028】図3は、本発明に係る亜鉛臭素電池の濃度
補正機構の流れを示した図である。まず、実施例におい
て、屈折率センサ32a及び32b並びに密度センサ3
3a及び33bにより検出された電解液の亜鉛イオン濃
度がS201において取り込まれ、更に、S202にお
いて温度センサ31a及び31bによって検出された温
度が取り込まれる。次に、温度比較工程S203におい
て、検出された電解液の温度が25℃か否か比較される
。ここで、電解液の温度が25℃であった場合には濃度
検出工程S201で取り込まれた電解液の亜鉛イオン濃
度は、そのままこの電池の電解液の亜鉛イオン濃度とし
てS205においてデータが決定されると共に、表示部
45で、この値に基づいて算出された電池の充電状態が
表示される。しかし、電解液の温度が25℃でなかった
場合には、S204において、メモリ47に備えられて
いる検量線データに基づいた補正がされる。このように
して、S201で取り込まれた任意の温度に於ける電解
液の亜鉛イオン濃度は、標準状態25℃での亜鉛イオン
濃度に補正されてから、この補正値が電池の電解液の正
確な亜鉛イオン濃度としてS205にて決定される。 そしてさらに、その補正値に基づいて算出された電池の
充電状態が表示部45において表示される。なお、本実
施例においては濃度検出手段として密度センサと屈折率
センサを用いたが、これを電解液の電気伝導度により電
解液の亜鉛イオン濃度を検出する手段にするなど、他の
濃度検出手段を用いたとしても、それが電解液の亜鉛イ
オン濃度を適確に検出できるものであれば、もちろん同
様の効果を得ることができる。  更に、亜鉛イオン濃
度を補正する手段として、本実施例においては検量線法
を用いた補正を行ったが、これを亜鉛イオン濃度検出値
の温度依存性を示した式に代入して亜鉛イオン濃度の温
度補正を行う手段を用いてもよく、亜鉛イオン濃度検出
値の温度依存性を検知できるものであれば、これらに限
られるものではない。  また、本実施例では、濃度検
出手段を2種類2組とし、温度検出手段を1対用いたが
、これらの組み合わせはこれに限られるものではない。 したがって、温度検出手段1個に対する濃度検出手段の
比は本実施例のように2に限られるものではなく、2以
外でも一向に差し支えない。
FIG. 3 is a diagram showing the flow of the concentration correction mechanism of the zinc bromine battery according to the present invention. First, in the embodiment, the refractive index sensors 32a and 32b and the density sensor 3
The zinc ion concentration of the electrolytic solution detected by sensors 3a and 33b is captured in S201, and further, the temperature detected by temperature sensors 31a and 31b is captured in S202. Next, in a temperature comparison step S203, it is compared whether the detected temperature of the electrolytic solution is 25°C. Here, if the temperature of the electrolyte is 25°C, the zinc ion concentration of the electrolyte taken in the concentration detection step S201 is determined as the zinc ion concentration of the electrolyte of this battery in S205. At the same time, the display unit 45 displays the charging state of the battery calculated based on this value. However, if the temperature of the electrolytic solution is not 25° C., correction is performed in S204 based on the calibration curve data stored in the memory 47. In this way, the zinc ion concentration of the electrolyte at any temperature taken in S201 is corrected to the zinc ion concentration at the standard state of 25°C, and then this correction value is used to accurately determine the electrolyte of the battery. The zinc ion concentration is determined in S205. Further, the state of charge of the battery calculated based on the correction value is displayed on the display section 45. In this example, a density sensor and a refractive index sensor were used as the concentration detection means, but other concentration detection means could be used, such as using this as a means of detecting the zinc ion concentration of the electrolyte based on the electrical conductivity of the electrolyte. Of course, the same effect can be obtained even if the method is used, as long as it can accurately detect the zinc ion concentration of the electrolyte. Furthermore, as a means of correcting the zinc ion concentration, a calibration curve method was used in this example to correct the zinc ion concentration. Any means for temperature correction may be used, and the present invention is not limited to these as long as the temperature dependence of the detected zinc ion concentration value can be detected. Further, in this embodiment, two types of concentration detection means and two sets of concentration detection means and one pair of temperature detection means are used, but these combinations are not limited to these. Therefore, the ratio of concentration detecting means to one temperature detecting means is not limited to 2 as in this embodiment, and may be other than 2 without any problem.

【0029】[0029]

【発明の効果】以上のような構成を有する本発明に係る
亜鉛臭素電池においては、電池の正確な充電状態を知る
ことができるため、この電池を使用する機械の制御を的
確に行うことができるようになる。
[Effects of the Invention] In the zinc bromine battery according to the present invention having the above-described configuration, since the accurate state of charge of the battery can be known, it is possible to accurately control the machine that uses this battery. It becomes like this.

【0030】これと同時に、密度測定手段における定期
的なキャリブレーションをとる際においても、電解液の
温度が考慮されるので、より正確なキャリブレーション
を行うことができる。
At the same time, since the temperature of the electrolyte is taken into consideration when periodically calibrating the density measuring means, more accurate calibration can be performed.

【0031】更に、電池の温度管理をより精密に行うこ
とができるため電池寿命が向上するという利点もある。
Furthermore, since the temperature of the battery can be controlled more precisely, there is also the advantage that the battery life can be improved.

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

【図1】本発明に係る亜鉛臭素電池の一実施例を示した
図である。
FIG. 1 is a diagram showing an example of a zinc bromine battery according to the present invention.

【図2】本実施例に用いた演算装置の具体的な構成を示
したブロック図である。
FIG. 2 is a block diagram showing a specific configuration of an arithmetic device used in this embodiment.

【図3】本実施例における亜鉛臭素電池の濃度補正機構
の流れを示すフローチャートである。
FIG. 3 is a flowchart showing the flow of the concentration correction mechanism of the zinc bromine battery in this embodiment.

【図4】従来の亜鉛臭素電池の構造を示した図である。FIG. 4 is a diagram showing the structure of a conventional zinc bromine battery.

【符号の説明】[Explanation of symbols]

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】電解液を循環して充放電反応を行う亜鉛臭
素電池において、電解液の亜鉛イオン濃度を検出する濃
度検出手段と、電解液の温度を検出する温度検出手段と
、前記温度検出手段のデータに基づき前記濃度検出手段
により検出された電解液の亜鉛イオン濃度を補正する濃
度補正手段と、を有し、任意の温度に於いて補正された
電解液の亜鉛イオン濃度を検出することを特徴とする亜
鉛臭素電池。
1. A zinc bromine battery that performs charging and discharging reactions by circulating an electrolytic solution, comprising a concentration detecting means for detecting the concentration of zinc ions in the electrolytic solution, a temperature detecting means for detecting the temperature of the electrolytic solution, and a temperature detecting means for detecting the temperature of the electrolytic solution. and a concentration correction means for correcting the zinc ion concentration of the electrolyte detected by the concentration detection means based on the data of the means, and detecting the corrected zinc ion concentration of the electrolyte at an arbitrary temperature. A zinc bromine battery featuring:
JP3013602A 1991-02-04 1991-02-04 Zn-br battery Pending JPH04249075A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3013602A JPH04249075A (en) 1991-02-04 1991-02-04 Zn-br battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3013602A JPH04249075A (en) 1991-02-04 1991-02-04 Zn-br battery

Publications (1)

Publication Number Publication Date
JPH04249075A true JPH04249075A (en) 1992-09-04

Family

ID=11837768

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3013602A Pending JPH04249075A (en) 1991-02-04 1991-02-04 Zn-br battery

Country Status (1)

Country Link
JP (1) JPH04249075A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016058255A (en) * 2014-09-10 2016-04-21 トヨタ自動車株式会社 Battery system
JP2017506811A (en) * 2014-02-27 2017-03-09 ヴィズン エナジー システムズ インコーポレーテッドVizn Energy Systems, Inc. Flow cell with shunt current counter electrode

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017506811A (en) * 2014-02-27 2017-03-09 ヴィズン エナジー システムズ インコーポレーテッドVizn Energy Systems, Inc. Flow cell with shunt current counter electrode
JP2016058255A (en) * 2014-09-10 2016-04-21 トヨタ自動車株式会社 Battery system

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