JPH0448635Y2 - - Google Patents
Info
- Publication number
- JPH0448635Y2 JPH0448635Y2 JP1985104994U JP10499485U JPH0448635Y2 JP H0448635 Y2 JPH0448635 Y2 JP H0448635Y2 JP 1985104994 U JP1985104994 U JP 1985104994U JP 10499485 U JP10499485 U JP 10499485U JP H0448635 Y2 JPH0448635 Y2 JP H0448635Y2
- Authority
- JP
- Japan
- Prior art keywords
- bromine
- soc
- zinc
- complex
- 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.)
- Expired
Links
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical class [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 23
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 21
- 229910052794 bromium Inorganic materials 0.000 claims description 21
- ZRXYMHTYEQQBLN-UHFFFAOYSA-N [Br].[Zn] Chemical compound [Br].[Zn] ZRXYMHTYEQQBLN-UHFFFAOYSA-N 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 9
- 238000006073 displacement reaction Methods 0.000 claims description 7
- 239000003792 electrolyte Substances 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 238000007600 charging Methods 0.000 description 11
- 238000007599 discharging Methods 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000007726 management method Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 239000008151 electrolyte solution Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical group [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000010277 constant-current charging Methods 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
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
Landscapes
- Secondary Cells (AREA)
- Hybrid Cells (AREA)
Description
【考案の詳細な説明】
[産業上の利用分野]
本考案は亜鉛−臭素電池のSOC測定装置に関
する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an SOC measuring device for a zinc-bromine battery.
亜鉛−臭素電池は新型電池の1つとして知られ
ている(例えば電気学会雑誌第103巻8号−昭和
58年8月)。 The zinc-bromine battery is known as one of the new batteries (for example, the Journal of the Institute of Electrical Engineers of Japan Vol. 103, No. 8-Showa
(August 1958).
[従来の技術]
亜鉛−臭素電池は鉛電池に比較してその開発の
歴史が浅く、現在においても実用化のための開発
段階といつた状況である。よつて電池の充電状態
すなわち残存容量(SOC)を把握するための手
段についての検討は不十分と思われ、これについ
ての報告は皆無である。しかし、あえて充放電管
理の方法を挙げるとすれば、充電量及び放電量そ
れぞれの積算値に自己放電量の推測値を考慮する
ことによつておおよそのSOCを推定する方法が
実施されてきた。[Prior Art] Zinc-bromine batteries have a short history of development compared to lead batteries, and are still at the development stage for practical use. Therefore, it seems that there has been insufficient research into methods for determining the state of charge of batteries, that is, the remaining capacity (SOC), and there have been no reports on this. However, if we were to choose a charging/discharging management method, a method has been implemented in which a rough SOC is estimated by considering an estimated value of the self-discharge amount in the respective integrated values of the charging amount and the discharging amount.
[考案が解決しようとする問題点]
従来の問題点
しかし亜鉛−臭素電池は鉛電池に比較してその
充放電時及び休止時共にかなり自己放電量の多い
電池であり、また電池の構成、充放電条件、特に
休止時の管理(処理)によつて自己放電量の差が
大きく、正確な自己放電量の推測は極めて困難で
ある。[Problems that the invention aims to solve] Conventional problems However, compared to lead batteries, zinc-bromine batteries have a considerably higher self-discharge amount during charging and discharging and when at rest, and The amount of self-discharge varies greatly depending on the discharge conditions, especially the management (processing) during rest, and it is extremely difficult to estimate the amount of self-discharge accurately.
よつて例えば亜鉛−臭素電池によつて電気自動
車を駆動させた場合にはその残存容量からの走行
可能距離の推測が信頼性の低いものになるという
問題が生じ、同様の問題が亜鉛−臭素電池を据置
用として使用した場合にも生じることになる。 For example, when an electric vehicle is powered by a zinc-bromine battery, the problem arises that estimating the possible range based on its remaining capacity becomes unreliable.A similar problem arises when using a zinc-bromine battery. This will also occur when used as a stationary device.
また、亜鉛−臭素電池では例えば一般的な定電
流充電を行つた場合正極側の反応生成物(Br2)
がタンクに錯体として貯蔵されるため充電電圧は
ほぼ一定に保たれる。よつてSOCを充電電圧変
化から推定することは不可能であり、同時に
SOCを正確に把握できないことから電池の過充
電の可能性が高くなり、負極への亜鉛の異常電着
及び電圧の急激な上昇によるガス発生が促進され
電池性能(エネルギ密度、出力密度、寿命等)が
低下するという問題があつた。 In addition, in a zinc-bromine battery, for example, when general constant current charging is performed, the reaction product (Br 2 ) on the positive electrode side
is stored as a complex in the tank, so the charging voltage is kept almost constant. Therefore, it is impossible to estimate SOC from charging voltage changes, and at the same time
Since the SOC cannot be accurately determined, there is a high possibility of overcharging of the battery, and abnormal electrodeposition of zinc on the negative electrode and gas generation due to a sudden increase in voltage are promoted. ) was a problem.
考案の目的
本考案は前記従来の問題点に鑑みなされたもの
で、その目的は亜鉛−臭素電池の充放電それぞれ
の進行と共に変化する正極液側臭素錯体量に基づ
いて電池のSOCを正確に測定することにより、
電池の持つ潜在能力を十分に引き出すと共にその
利用性を向上させ、更にその利用面から電池性能
を大幅に改善することにある。Purpose of the invention The present invention was devised in view of the above-mentioned conventional problems, and its purpose is to accurately measure the SOC of a zinc-bromine battery based on the amount of bromine complex on the positive electrode side, which changes with the progress of charging and discharging. By doing so,
The objective is to fully draw out the potential of batteries, improve their usability, and further significantly improve battery performance in terms of usage.
[問題点を解決するための手段及び作用]
この目的を達成するために、本考案は、電池の
正極液を貯留する正極液タンク内の臭素錯体を計
測する錯体量計測手段と、この錯体量計測手段で
得られた臭素錯体量を充電状態についての物理量
に変換する変換手段と、この変換手段で得られた
物理量に基づいて充電状態であるSOCの値を表
示するSOC表示手段とを有し、正極液中の臭素
錯体量によつて電池の充電状態を測定することを
特徴とする。[Means and effects for solving the problem] In order to achieve this object, the present invention provides a complex amount measuring means for measuring the bromine complex in a catholyte tank that stores the catholyte of a battery, and a method for measuring the amount of this complex. It has a conversion means for converting the amount of bromine complex obtained by the measurement means into a physical quantity regarding the state of charge, and an SOC display means for displaying the value of SOC, which is the state of charge, based on the physical quantity obtained by the conversion means. , is characterized in that the state of charge of the battery is measured by the amount of bromine complex in the positive electrode solution.
このような構成により、亜鉛−臭素電池の真味
SOC、すなわち自己放電量も考慮したSOCに対
応して変化する臭素錯体の量に基づいてSOCを
測定することができるものである。 With this configuration, the true nature of zinc-bromine batteries can be realized.
SOC can be measured based on the amount of bromine complex that changes in response to SOC, which also takes into account the amount of self-discharge.
[実施例]
以下、図面に基づいて本考案の好適な実施例を
説明する。[Embodiments] Hereinafter, preferred embodiments of the present invention will be described based on the drawings.
第1図に示すように電解液10が満たされた正
極液タンク12内には下方を開口し上方を閉口と
する筒体14が正極液タンク12のフタを貫通し
て液密に直立状態に固定され、該筒体14の大径
部の上方には電解液流出入孔14aが形成されて
いる。 As shown in FIG. 1, in the positive electrode tank 12 filled with the electrolyte 10, a cylindrical body 14, which is open at the bottom and closed at the top, penetrates the lid of the positive electrode tank 12 and stands upright in a liquid-tight manner. An electrolytic solution inflow/outflow hole 14a is formed above the large diameter portion of the cylindrical body 14.
そして筒体14内には間隙を持たせフロート1
6が内挿されており、筒体14及びフロート16
の表面部分はすべて正極液タンク12と同様にポ
リオレフイン樹脂あるいは四フツ化樹脂等で形成
され、フロート16の比重は水性電解液10の比
重と充放電の進行と共にその量が変化する臭素錯
体18の比重の間の値、理想的には、1.8以上2.0
以下に調整され、臭素錯体18の量の変化による
臭素錯体液面18aの変位に追従して該フロート
16は上下に変位する。 A gap is provided inside the cylinder 14 so that the float 1
6 is inserted, the cylinder body 14 and the float 16
All the surface parts of the float 16 are made of polyolefin resin or tetrafluoride resin, etc., like the catholyte tank 12, and the specific gravity of the float 16 is a combination of the specific gravity of the aqueous electrolyte 10 and the amount of bromine complex 18, which changes with the progress of charging and discharging. Specific gravity value between 1.8 and 2.0, ideally
The float 16 is adjusted as follows, and the float 16 is displaced up and down following the displacement of the bromine complex liquid level 18a due to a change in the amount of the bromine complex 18.
また、正極液タンク12の上方に突出したフロ
ート16の上部には鉄心20が内蔵され、筒体1
4の上部の外周部にはフロート16の上下方向の
変位量を電気的に変換するための変換器としての
差動変圧器22が設置されている。 Further, an iron core 20 is built in the upper part of the float 16 that protrudes above the cathode liquid tank 12, and the cylindrical body 1
A differential transformer 22 as a converter for electrically converting the amount of vertical displacement of the float 16 is installed on the upper outer circumference of the float 16 .
前記差動変圧器22の一次側コイルには交流電
源24が接続され、臭素錯体18の量の変化に応
じたフロート16の変位は差動変圧器22により
電圧Vの変化として表わされ、この差動変圧器2
2の出力電圧は増幅器26を介して指示計28に
入力される。 An AC power source 24 is connected to the primary coil of the differential transformer 22, and the displacement of the float 16 in response to a change in the amount of the bromine complex 18 is expressed by the differential transformer 22 as a change in voltage V. Differential transformer 2
The output voltage of No. 2 is input to an indicator 28 via an amplifier 26.
ところで、実験結果により臭素錯体18の量と
SOCの関係は第2図のグラフに示すとおりであ
り、正極液タンク12の横断面積が一定の構造で
あればフロート16の変位は臭素錯体18の量の
変化に比例するので指示計28に第2図の関係を
SOC値として充・放電のそれぞれの過程を別々
に目盛ることにより、充電・放電のどちらの過程
においても電池のSOCを指示計28から直読す
ることができる。 By the way, the experimental results show that the amount of bromine complex 18 and
The relationship between SOC is as shown in the graph of FIG. The relationship in Figure 2
By separately calibrating each charging and discharging process as an SOC value, the SOC of the battery can be directly read from the indicator 28 in both charging and discharging processes.
尚、正極液タンク12の側面には電解液流入管
30、電解液流出管32が取り付けられ、底面に
は臭素錯体流出管34が取り付けられている。 Incidentally, an electrolyte inflow pipe 30 and an electrolyte outflow pipe 32 are attached to the side surface of the positive electrode liquid tank 12, and a bromine complex outflow pipe 34 is attached to the bottom surface.
また、他の実施例として第3図あるいは第4図
に示すように正極液タンク12の内部に臭素錯体
18を貯蔵するサブタンク36aまたは36bを
設置し、第2図の充電時曲線あるいは放電時曲線
からこのサブタンク30a,30b内に設けたフ
ロート(図示せず)の変位がSOCに比例するよ
うにサブタンク36a,36bの断面積を変化さ
せて製作することにより指示計28の目盛を充電
時あるいは放電時どちらかにおいて等間隔とする
ことも可能である。 In addition, as another embodiment, as shown in FIG. 3 or 4, a sub-tank 36a or 36b for storing the bromine complex 18 is installed inside the catholyte tank 12, and the charging time curve or discharging time curve shown in FIG. By changing the cross-sectional area of the sub-tanks 36a, 36b so that the displacement of a float (not shown) provided in the sub-tanks 30a, 30b is proportional to the SOC, the scale of the indicator 28 can be changed during charging or discharging. It is also possible to have equal intervals at either time.
更に他の実施例として差動変圧器の設定場所に
ついては、まず第5図に示すように正極液タンク
12に凹部を設け、筒体14を凹部のフタ12a
を貫通直立支持させると共にフタ12a上に突出
した筒体14の外周部に差動変圧器22を設置さ
せる方法があり、この場合、正極液タンク12の
局部的な突出部をなくすことが可能である。ま
た、第6図に示すように筒体14と差動変圧器2
2とを一体化させ、かつ正極液タンク12内に筒
体14を直立支持させる方法もあり、この場合に
は正極液タンク12の構造を複雑にすることなく
前記方法の効果を持つと共に、SOC測定装置の
設置性が向上する。 As for the setting location of the differential transformer as another embodiment, first, as shown in FIG.
There is a method in which the differential transformer 22 is installed on the outer periphery of the cylindrical body 14 that penetrates through and is supported upright and protrudes above the lid 12a. In this case, it is possible to eliminate local protrusions of the positive electrode tank 12. be. Further, as shown in FIG. 6, the cylinder body 14 and the differential transformer 2
There is also a method of integrating the cylindrical body 14 with the cathode liquid tank 12 and supporting it upright within the cathode liquid tank 12. In this case, it has the effect of the above method without complicating the structure of the cathode liquid tank 12, and the SOC The ease of installing the measuring device is improved.
なお、臭素錯体量の測定手段としては、前記フ
ロートによる液面測定のほか、錯体と電解液の境
界部を光学的に測定する手段、錯体を含む正極液
全体の重量を測定する手段なども用いることがで
きることは、当業者が容易に理解し得るところで
ある。 In addition, as a means for measuring the amount of bromine complex, in addition to the liquid level measurement using the float, a means for optically measuring the boundary between the complex and the electrolyte solution, a means for measuring the entire weight of the positive electrode solution including the complex, etc. are used. Those skilled in the art will readily understand that this can be done.
[考案の効果]
以上説明したとおり、本考案によれば、亜鉛−
臭素電池の真味のSOC、すなわち自己放電量も
考慮したSOCに対応して変化する臭素錯体の量
に基づいてSOCを測定するようにしたため、精
度の良いSOC測定が可能となり、しかも電池の
保守管理を効率的に行えるとともにエネルギ密
度、出力密度、寿命等の電池性能が改善されると
いう効果がある。[Effect of the invention] As explained above, according to the invention, zinc-
Since SOC is measured based on the amount of bromine complex that changes in response to the true SOC of a bromine battery, that is, the SOC that also takes into account self-discharge, it is possible to measure SOC with high accuracy, and it is also easy to maintain the battery. This has the effect of enabling efficient management and improving battery performance such as energy density, output density, and lifespan.
第1図は本考案の亜鉛−臭素電池のSOC測定
装置の実施例を示す説明図、第2図は臭素錯体量
との関係を示す図、第3図及び第4図はフロート
の変位とSOCを比例させるための臭素錯体用サ
ブタンクを設けた他の実施例を示す説明図、第5
図及び第6図は差動変圧器の設置場所を変更した
更に他の実施例を示す説明図である。
10……水性電解液、12……正極液タンク、
14……筒体、16……フロート、18……臭素
錯体、22……差動変圧器、28……指示計。
Figure 1 is an explanatory diagram showing an example of the SOC measuring device for a zinc-bromine battery of the present invention, Figure 2 is a diagram showing the relationship between the amount of bromine complex, and Figures 3 and 4 are diagrams showing the relationship between the displacement of the float and the SOC. Explanatory diagram showing another embodiment in which a sub-tank for bromine complex is provided for proportionalizing the
This figure and FIG. 6 are explanatory diagrams showing still another embodiment in which the installation location of the differential transformer is changed. 10...Aqueous electrolyte, 12...Positive electrolyte tank,
14... Cylindrical body, 16... Float, 18... Bromine complex, 22... Differential transformer, 28... Indicator.
Claims (1)
素錯体を計測する錯体量計測手段と、 この錯体量計測手段で得られた臭素錯体量を
充電状態についての物理量に変換する変換手段
と、 この変換手段で得られた物理量に基づいて充
電状態であるSOCの値を表示するSOC表示手
段と、 を有し、 正極液中の臭素錯体量によつて電池の充電状
態を測定することを特徴とする亜鉛−臭素電池
のSOC測定装置。 (2) 実用新案登録請求の範囲第1項記載の装置に
おいて、前記錯体量計測手段が正極液タンク内
に設けられ臭素錯体量の変化による臭素錯体液
面の変位に追従して上下方向に変位するフロー
トであることを特徴とする亜鉛−臭素電池の
SOC測定装置。 (3) 実用新案登録請求の範囲第2項記載の装置に
おいて、 前記変換手段が前記フロートの変位を電気的
変化に変換する変換器であることを特徴とする
亜鉛−臭素電池のSOC測定装置。 (4) 実用新案登録請求の範囲第3項記載の装置に
おいて、 前記変換器が差動変圧器であることを特徴と
する亜鉛−臭素電池のSOC測定装置。 (5) 実用新案登録請求の範囲第2項から第4項の
いずれかに記載の装置において、 前記フロートの比重が水性電解液の比重と臭
素錯体の比重との間であることを特徴とする亜
鉛−臭素電池のSOC測定装置。[Scope of Claim for Utility Model Registration] (1) A complex amount measuring means for measuring bromine complexes in a catholyte tank that stores the catholyte of a battery, and the amount of bromine complexes obtained by this complex amount measuring means regarding the state of charge. a conversion means for converting the physical quantity into a physical quantity; and an SOC display means for displaying the SOC value in the state of charge based on the physical quantity obtained by the conversion means, A zinc-bromine battery SOC measuring device characterized by measuring the state of charge of a zinc-bromine battery. (2) Utility Model Registration In the device according to claim 1, the complex amount measuring means is provided in the positive electrode liquid tank and is displaced in the vertical direction following the displacement of the bromine complex liquid level due to a change in the bromine complex amount. A zinc-bromine battery characterized by being a float that
SOC measuring device. (3) Utility Model Registration The device according to claim 2, wherein the converting means is a converter that converts the displacement of the float into an electrical change. (4) Utility model registration Claim 3: The SOC measuring device for a zinc-bromine battery, wherein the converter is a differential transformer. (5) The device according to any one of claims 2 to 4 for utility model registration, characterized in that the specific gravity of the float is between the specific gravity of the aqueous electrolyte and the specific gravity of the bromine complex. SOC measuring device for zinc-bromine batteries.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985104994U JPH0448635Y2 (en) | 1985-07-10 | 1985-07-10 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985104994U JPH0448635Y2 (en) | 1985-07-10 | 1985-07-10 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6214671U JPS6214671U (en) | 1987-01-28 |
| JPH0448635Y2 true JPH0448635Y2 (en) | 1992-11-16 |
Family
ID=30979004
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1985104994U Expired JPH0448635Y2 (en) | 1985-07-10 | 1985-07-10 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0448635Y2 (en) |
-
1985
- 1985-07-10 JP JP1985104994U patent/JPH0448635Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6214671U (en) | 1987-01-28 |
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