JP3229214U - A container that houses the catalyst material, and a lead-acid battery that contains the container. - Google Patents

A container that houses the catalyst material, and a lead-acid battery that contains the container. Download PDF

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JP3229214U
JP3229214U JP2020003623U JP2020003623U JP3229214U JP 3229214 U JP3229214 U JP 3229214U JP 2020003623 U JP2020003623 U JP 2020003623U JP 2020003623 U JP2020003623 U JP 2020003623U JP 3229214 U JP3229214 U JP 3229214U
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catalyst
container
lead
membrane
electrolytic solution
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小林 康太郎
康太郎 小林
麻生 昌之
昌之 麻生
雅司 小野
雅司 小野
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W.L.Gore&Associates G.K.
W.L.Gore&Associates,Co.,LTD.
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    • 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
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    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • 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
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Abstract

【課題】電解液量の減少を抑制することができ、また温度制御等の冗長的な対策をする必要のない、鉛蓄電池において触媒層材を収容する容器、およびこれを用いた鉛蓄電池を提供する。【解決手段】鉛蓄電池において触媒材30を収容する容器20であって、触媒材は、酸素および水素から水または水蒸気を生成する反応を促進する触媒を含み、且つ容器は膜40で覆われた開口部を持ち、膜は、酸素、水素および水蒸気を触媒層と容器の外部との間で連通し、且つ重力方向に対して0°以上80°以下の角度で配向される。【選択図】図3PROBLEM TO BE SOLVED: To provide a container for accommodating a catalyst layer material in a lead storage battery, which can suppress a decrease in the amount of electrolytic solution and which does not require redundant measures such as temperature control, and a lead storage battery using the same. To do. SOLUTION: A container 20 for accommodating a catalyst material 30 in a lead storage battery, the catalyst material contains a catalyst for promoting a reaction for producing water or water vapor from oxygen and hydrogen, and the container is covered with a film 40. With an opening, the membrane communicates oxygen, hydrogen and water vapor between the catalyst layer and the outside of the vessel and is oriented at an angle of 0 ° to 80 ° with respect to the direction of gravity. [Selection diagram] Fig. 3

Description

本考案は、鉛蓄電池において触媒材を収容する容器、およびその容器を含んでなる鉛蓄電池に関係する。特に、当該触媒材は、酸素および水素から水または水蒸気を生成する反応を促進する触媒を含む。 The present invention relates to a container for accommodating a catalyst material in a lead storage battery, and a lead storage battery including the container. In particular, the catalyst material comprises a catalyst that promotes a reaction that produces water or water vapor from oxygen and hydrogen.

鉛蓄電池、中でも自動車用鉛蓄電池では、希硫酸等の電解液が自由に流動できるいわゆる開放型の構造が広く用いられている。この構造の鉛蓄電池は充電時に酸素や水素ガスが発生するため、これらのガスを外部に放出するためのベント(排気口)を有している。さもなければ、電池内部でガス圧力が高まり、電池の変形、破損につながるからである。
また、このような、ベントからのガスの放出は電解液中の水の減少に繋がる。電解液中の水が減少すると、総電解液量が減少するとともに電解液比重が上昇し電池化学反応が十分に行われなくなり、充電能力および放電能力が低下する。
これらの問題に対して、これまでも様々な取り組みがなされてきた。
In lead-acid batteries, especially lead-acid batteries for automobiles, a so-called open type structure in which an electrolytic solution such as dilute sulfuric acid can freely flow is widely used. Since a lead storage battery having this structure generates oxygen and hydrogen gas during charging, it has a vent (exhaust port) for releasing these gases to the outside. Otherwise, the gas pressure inside the battery will increase, leading to deformation and damage of the battery.
Further, such release of gas from the vent leads to a decrease in water in the electrolytic solution. When the amount of water in the electrolytic solution decreases, the total amount of the electrolytic solution decreases, the specific gravity of the electrolytic solution increases, the battery chemical reaction does not occur sufficiently, and the charging capacity and the discharging capacity decrease.
Various efforts have been made to address these issues.

特許文献1は、鉛蓄電池のための触媒部品を開示しており、その触媒部品は、
酸素および水素から水または水蒸気を生成する反応を促進する触媒を含む触媒層、及び
前記触媒反応で生成した水または水蒸気の少なくとも一部が凝縮し前記鉛蓄電池内部へ環流される構成を有する。この触媒部品により、電解液からのガス放出、それらによる電解液量の減少を抑制でき、電解液が減少しないために長寿命を実現できる。
Patent Document 1 discloses a catalyst component for a lead storage battery, and the catalyst component is
It has a catalyst layer containing a catalyst that promotes a reaction for producing water or water vapor from oxygen and hydrogen, and a configuration in which at least a part of water or water vapor generated by the catalytic reaction is condensed and recycled into the lead-acid battery. With this catalyst component, gas release from the electrolytic solution and a decrease in the amount of the electrolytic solution due to them can be suppressed, and a long life can be realized because the electrolytic solution does not decrease.

特許文献2は、電解液の分解ガスを再結合する触媒装置を開示している。この触媒装置は、触媒毒(酸性電解液)を濾過して取り除く能力を有する。より具体的には、この触媒装置は、ガスは透過するが液体は透過しない多孔質部を有し、触媒毒(酸性電解液等)が触媒に到達しないようにされており、またいる。多孔質部を通過したガスは、触媒部に到達し再結合され、多孔質部を通って環流できると記載されている。 Patent Document 2 discloses a catalyst device that recombines the decomposition gas of the electrolytic solution. This catalyst device has the ability to filter and remove the catalyst poison (acidic electrolyte). More specifically, this catalyst device has a porous portion that allows gas to permeate but does not allow liquid to permeate, so that the catalyst poison (acidic electrolyte, etc.) does not reach the catalyst. It is described that the gas that has passed through the porous portion reaches the catalyst portion, is recombined, and can be recirculated through the porous portion.

特開2017−201594号公報JP-A-2017-201594 米国特許第7326489号明細書U.S. Pat. No. 7,326,489

上述のとおり、一般的な鉛蓄電池では、充電時に発生する酸素や水素ガスが、ベントから外部に放出され、鉛蓄電池内の電解液量が減少する。電解液量が減少すると、電池化学反応が十分に行われなくなり、充電能力および放電能力が低下する。特定の理論に拘束されることを望むものではないが、電解液中の希硫酸濃度が上昇して正極板の腐食劣化により容量低下が進行すること、電解液面の低下により極板が電解液から露出することで放電容量が急激に低下すること、さらに、負極板とストラップとの接続部が腐食するといったことが考えられる。 As described above, in a general lead-acid battery, oxygen and hydrogen gas generated during charging are released from the vent to the outside, and the amount of electrolyte in the lead-acid battery is reduced. When the amount of the electrolytic solution is reduced, the battery chemical reaction is not sufficiently performed, and the charging capacity and the discharging capacity are reduced. Although it is not desired to be bound by a specific theory, the dilute sulfuric acid concentration in the electrolytic solution increases and the capacity decreases due to corrosion deterioration of the positive electrode plate, and the electrode plate becomes the electrolytic solution due to the decrease in the electrolytic solution level. It is conceivable that the discharge capacity drops sharply due to exposure from the negative electrode plate, and that the connection portion between the negative electrode plate and the strap is corroded.

さらに、電解液量の減少は、サルフェーションおよび浸透短絡にも繋がると考えられる。サルフェーションとは、放電によって生成された硫酸鉛を、充電によって二酸化鉛と鉛とに十分に回復することができず、硫酸鉛の粗大結晶が発生することである。この粗大結晶は、金属鉛への還元が困難であり、電池性能を低下させ、電池寿命を短くする。さらに、この粗大結晶は浸透短絡にも関係する。粗大結晶は電極上で成長して、「デンドライト」と呼称される針状結晶となる。このデンドライトが成長し続けると、他方の電極に到達して、短絡を生じる。これが浸透短絡であり、以後の充電放電はできなくなる。逆に言えば、電解液量の減少を防ぐことにより、サルフェーションおよび浸透短絡を防ぐことができる。 Furthermore, the decrease in the amount of electrolyte is considered to lead to sulfation and osmotic short circuit. Sulfation means that lead sulfate produced by electric discharge cannot be sufficiently restored to lead dioxide and lead by charging, and coarse crystals of lead sulfate are generated. This coarse crystal is difficult to reduce to metallic lead, lowers battery performance and shortens battery life. In addition, this coarse crystal is also involved in osmotic short circuits. The coarse crystals grow on the electrodes into acicular crystals called "dendrites". As this dendrite continues to grow, it reaches the other electrode, causing a short circuit. This is a permeation short circuit, and subsequent charging and discharging cannot be performed. Conversely, by preventing a decrease in the amount of electrolyte, sulfation and osmotic short circuit can be prevented.

特許文献1、2では、電解液からのガス放出、それらによる電解液量の減少を抑制するための、触媒部品または触媒装置を開示している。つまり、鉛蓄電池内部から発生する酸素や水素ガスを、触媒により、水または水蒸気に再結合して、電池内部へ環流させている。 Patent Documents 1 and 2 disclose a catalyst component or a catalyst device for suppressing outgassing from an electrolytic solution and a decrease in the amount of the electrolytic solution due to them. That is, oxygen and hydrogen gas generated from the inside of the lead storage battery are recombined with water or water vapor by a catalyst and recirculated inside the battery.

ただし、鉛蓄電池内部に、これらの触媒部品や触媒装置を取り付けた場合でも、電解液量の減少が十分に抑制できないことがある。電解液量の減少は、上述したような充放電能力の劣化、電池内部の損傷にも繋がる。したがって、電解液量の減少を抑制することが強く望まれる。 However, even when these catalyst parts and catalyst devices are installed inside the lead-acid battery, the decrease in the amount of electrolytic solution may not be sufficiently suppressed. The decrease in the amount of electrolyte leads to the deterioration of the charge / discharge capacity and the damage inside the battery as described above. Therefore, it is strongly desired to suppress the decrease in the amount of electrolytic solution.

また、特許文献2の触媒装置は、比較的高温(およそ70〜90℃)に温度制御することが必要であり、電源設備のバックアップ用途で使われるような常時充電されるような環境では使用できるが、充電が不連続であり温度制御のできない環境では使用できない。例えば、自動車用鉛蓄電池等では、常時充電状態で使用されない場合や、寒冷地でも使用される場合があるため、特許文献2の装置は好適ではない。 Further, the catalyst device of Patent Document 2 needs to be temperature-controlled to a relatively high temperature (about 70 to 90 ° C.), and can be used in an environment where it is constantly charged as used for backup of power supply equipment. However, it cannot be used in an environment where charging is discontinuous and temperature control is not possible. For example, the device of Patent Document 2 is not suitable for a lead storage battery for an automobile or the like because it may not be used in a constantly charged state or may be used even in a cold region.

上記に鑑みて、本考案は、電解液量の減少を抑制することができ、また温度制御等の冗長的な対策をする必要のない、鉛蓄電池において触媒層材を収容する容器、およびこれを用いた鉛蓄電池を提供することを目的とする。 In view of the above, the present invention provides a container for accommodating a catalyst layer material in a lead storage battery, which can suppress a decrease in the amount of electrolytic solution and does not require redundant measures such as temperature control. An object of the present invention is to provide a lead-acid battery used.

本考案により、以下の態様が提供される。 The present invention provides the following aspects.

[1]
鉛蓄電池において触媒材を収容する容器であって、
前記触媒材は、酸素および水素から水または水蒸気を生成する反応を促進する触媒を含み、且つ前記容器は膜で覆われた開口部を持ち、
前記膜は、前記酸素、前記水素および前記水蒸気を前記触媒層と当該容器の外部との間で連通し、且つ重力方向に対して0°以上80°以下の角度で配向される、ことを特徴とする、容器。
[2]
前記膜が疎水性多孔質膜を含んでなることを特徴とする、項目[1]に記載の容器。
[3]
前記膜が多孔質PTFEを含んでなることを特徴とする、項目[1]または[2]に記載の容器。
[4]
当該容器の境界形状の少なくとも一部は、円柱、円錐、円錐台、多角形柱、多角形錐、多角形錐台、または球体のいずれか少なくとも一つの形状の少なくとも一部を含む、ことを特徴とする、項目[1]〜[3]のいずれか1項に記載の容器。
[5]
項目[1]〜[4]のいずれか1項に記載の容器を含んでなる、鉛蓄電池。
[1]
A container that houses a catalyst material in a lead-acid battery.
The catalyst material comprises a catalyst that promotes a reaction that produces water or water vapor from oxygen and hydrogen, and the container has a membrane-covered opening.
The membrane is characterized in that the oxygen, the hydrogen and the water vapor communicate with each other between the catalyst layer and the outside of the container, and are oriented at an angle of 0 ° or more and 80 ° or less with respect to the direction of gravity. And the container.
[2]
The container according to item [1], wherein the membrane comprises a hydrophobic porous membrane.
[3]
The container according to item [1] or [2], wherein the film comprises porous PTFE.
[4]
The boundary shape of the container is characterized by including at least a part of at least one shape of a cylinder, a cone, a truncated cone, a truncated cone, a polygonal cone, a polygonal cone, or a sphere. The container according to any one of items [1] to [3].
[5]
A lead-acid battery comprising the container according to any one of items [1] to [4].

本願考案により、電解液量の減少を十分に抑制することができ、また温度制御等の冗長的な対策をする必要のない、鉛蓄電池において触媒層材を収容する容器、およびこれを用いた鉛蓄電池が提供される。
この容器および鉛蓄電池では、電解液量の減少を十分に抑制することができるため、長期にわたってその充放電性能および電池内部の健全性を維持することができる。
According to the invention of the present application, a container for accommodating a catalyst layer material in a lead storage battery, which can sufficiently suppress a decrease in the amount of electrolytic solution and does not require redundant measures such as temperature control, and lead using the same. Batteries are provided.
Since the container and the lead storage battery can sufficiently suppress a decrease in the amount of electrolytic solution, the charge / discharge performance and the soundness inside the battery can be maintained for a long period of time.

鉛蓄電池内の触媒収容容器で生じる作用機序について説明する概略図である。It is the schematic explaining the mechanism of action which occurs in the catalyst containing container in a lead storage battery. 鉛蓄電池のベントキャップに触媒収容容器を取り付けたものを示す概略模式図である。It is a schematic schematic diagram which shows the thing which attached the catalyst accommodating container to the vent cap of the lead storage battery. 膜の配向角度が0°(垂直)である触媒収容容器とベントキャップを示す概略模式図である。It is a schematic schematic diagram which shows the catalyst containing container and the vent cap which the orientation angle of a membrane is 0 ° (vertical).

本考案の一態様である容器は、
鉛蓄電池において触媒材を収容する容器であって、
前記触媒材は、酸素および水素から水または水蒸気を生成する反応を促進する触媒を含み、且つ前記容器は膜で覆われた開口部を持ち、
前記膜は、前記酸素、前記水素および前記水蒸気を前記触媒材と当該容器の外部との間で連通し、且つ重力方向に対して0°以上80°以下の角度で配向される。
The container, which is one aspect of the present invention, is
A container that houses a catalyst material in a lead-acid battery.
The catalyst material comprises a catalyst that promotes a reaction that produces water or water vapor from oxygen and hydrogen, and the container has a membrane-covered opening.
The membrane communicates the oxygen, the hydrogen and the water vapor between the catalyst material and the outside of the container, and is oriented at an angle of 0 ° to 80 ° with respect to the direction of gravity.

当該容器は、鉛蓄電池において触媒材を収容する容器である。
鉛蓄電池の電解液は希硫酸水溶液であるので、電池内部空間には、電解液(希硫酸水溶液)、硫酸ミスト、水分、電池反応によって生じた水素ガスおよび酸素ガスが存在している。水素ガスおよび酸素ガスは、電池容器のベントから外部環境へ放出されることがあり、これは電池内部の電解液量の減少につながり、ひいては電池性能および電池健全性の劣化につながる。
The container is a container for accommodating a catalyst material in a lead storage battery.
Since the electrolytic solution of the lead storage battery is a dilute sulfuric acid aqueous solution, an electrolytic solution (dilute sulfuric acid aqueous solution), sulfuric acid mist, moisture, hydrogen gas and oxygen gas generated by the battery reaction are present in the battery internal space. Hydrogen gas and oxygen gas may be released from the vent of the battery container to the external environment, which leads to a decrease in the amount of electrolyte inside the battery, which in turn leads to deterioration of battery performance and battery health.

当該容器に収容される触媒材は、酸素および水素から水または水蒸気を生成する反応を促進する触媒を含む。そのため、電池反応によって生じた水素ガスおよび酸素ガスが、当該触媒材に接触することで、それらが再結合されて水または水蒸気となり、また場合により水または水蒸気は凝縮され、電池内部へ環流され、結果として電池内部の電解液中の水の減少が抑制される。なお、触媒材とは、触媒作用を有する材料であることを意味し、その形態は特に限定されるものではなく、層状であってもよく、粉末状であってもよく、焼結体や圧縮体等のように塊状であってもよく、担体に坦持された状態でもよく、または枠体等に充填された状態でもよい。触媒作用を有する材料の一例として、白金、パラジウム、ニッケル、鉄、コバルト等の金属元素を挙げることができる。 The catalyst material contained in the container contains a catalyst that promotes a reaction that produces water or water vapor from oxygen and hydrogen. Therefore, when the hydrogen gas and oxygen gas generated by the battery reaction come into contact with the catalyst material, they are recombined into water or water vapor, and in some cases, the water or water vapor is condensed and recirculated inside the battery. As a result, the decrease of water in the electrolytic solution inside the battery is suppressed. The catalytic material means a material having a catalytic action, and its form is not particularly limited, and may be in a layered form or a powdery form, and may be a sintered body or a compressed material. It may be lumpy like a body, may be carried on a carrier, or may be filled in a frame or the like. Examples of materials having a catalytic action include metal elements such as platinum, palladium, nickel, iron and cobalt.

また、当該容器は膜で覆われた開口部を持ち、当該膜は、前記酸素、前記水素および前記水蒸気を前記触媒材と当該容器の外部との間で連通する。これらの開口部および膜により、容器に収容された前記触媒材に電池反応によって生じた水素ガスおよび酸素ガスが接触することが可能である。またこの構成により、前記触媒材は、当該容器内から漏出することなく、当該容器内に収容される。 Further, the container has an opening covered with a membrane, and the membrane communicates the oxygen, the hydrogen and the water vapor between the catalyst material and the outside of the container. These openings and membranes allow the catalyst material contained in the container to come into contact with hydrogen gas and oxygen gas generated by the battery reaction. Further, with this configuration, the catalyst material is housed in the container without leaking from the container.

さらに、前記開口部を覆う膜は、重力方向に対して0°以上80°以下の角度で配向される。 Further, the film covering the opening is oriented at an angle of 0 ° or more and 80 ° or less with respect to the direction of gravity.

膜を配向させる理由および背景について説明する。
従来、例えば特許文献1、2に記載されるように、鉛蓄電池において触媒を用いて、電池反応によって生じた水素ガスおよび酸素ガスを再結合させて、電解液中の水の減少を抑制する試みは行なわれていた。しかしながら、本考案者らが実際に確認をしたところでは、開放型鉛蓄電では電解液中の水の減少を十分に抑制できないことがあり、その原因について検討した結果、以下の作用機序に想い至った。図1を参照しながら説明する。
鉛蓄電池内部の下部には電解液(希硫酸)が存在し、その液温は外気温や電池反応により約60℃になることがある。この温度の電解液からは水素ガス、酸素ガス、水蒸気、硫酸ミストが発生し、それらは鉛蓄電池の上部に存在し、その雰囲気温度は約40℃になることがある。そして、鉛蓄電池内部の上部(天井部)に、触媒を収容した容器は、取り付けられている。
このような環境下で、触媒およびその近傍では次の事象が生じる。
1.触媒収容容器の膜の表面で水が凝縮し、膜の表面に液体(水)の層が形成される。
2.膜表面の液体(水)の層が、水素ガスおよび酸素ガス(H/O)の触媒容器内部への流入を妨げる。
3.水素ガスおよび酸素ガス(H/O)の流入が低下し、触媒反応が低下するので、触媒温度も低下する。
4.(触媒温度低下により)触媒収容容器内部で水の凝縮が生じる。
5.(凝縮水により)さらに触媒温度が低下する。
6.触媒収容容器の内外で硫酸の濃度差(外部で高く、内部で低い)によって、硫酸が膜表面の液体の層を介して触媒収容容器内部へ浸入し、触媒が被毒し劣化する。
7.触媒の劣化により、水素ガスおよび酸素ガス(H/O)の反応が促進されず、電解液量の減少に繋がる。
The reason for orienting the film and the background will be described.
Conventionally, as described in Patent Documents 1 and 2, for example, an attempt to suppress a decrease in water in an electrolytic solution by recombining hydrogen gas and oxygen gas generated by a battery reaction using a catalyst in a lead storage battery. Was being done. However, according to the actual confirmation by the present inventors, the decrease in water in the electrolytic solution may not be sufficiently suppressed by the open lead storage, and as a result of investigating the cause, the following mechanism of action is considered. I arrived. This will be described with reference to FIG.
An electrolytic solution (dilute sulfuric acid) exists in the lower part inside the lead-acid battery, and the liquid temperature may reach about 60 ° C. depending on the outside air temperature and the battery reaction. Hydrogen gas, oxygen gas, water vapor, and sulfuric acid mist are generated from the electrolytic solution at this temperature, and they are present in the upper part of the lead storage battery, and the ambient temperature may be about 40 ° C. A container containing the catalyst is attached to the upper part (ceiling part) inside the lead-acid battery.
In such an environment, the following events occur in and around the catalyst.
1. 1. Water condenses on the surface of the membrane of the catalyst containment vessel, forming a layer of liquid (water) on the surface of the membrane.
2. 2. A layer of liquid (water) on the surface of the membrane prevents the inflow of hydrogen gas and oxygen gas (H 2 / O 2 ) into the catalyst vessel.
3. 3. Since the inflow of hydrogen gas and oxygen gas (H 2 / O 2 ) is reduced and the catalytic reaction is reduced, the catalyst temperature is also reduced.
4. Water condensation occurs inside the catalyst storage container (due to the decrease in catalyst temperature).
5. The catalyst temperature is further lowered (due to condensed water).
6. Due to the difference in the concentration of sulfuric acid between the inside and outside of the catalyst storage container (high outside and low inside), sulfuric acid infiltrates into the inside of the catalyst storage container through the liquid layer on the membrane surface, and the catalyst is poisoned and deteriorated.
7. Due to the deterioration of the catalyst, the reaction of hydrogen gas and oxygen gas (H 2 / O 2 ) is not promoted, leading to a decrease in the amount of electrolytic solution.

上記の作用機序を考慮して、本考案者らは、触媒収容容器の膜の表面で水が凝縮することを防ぐことにより、当該作用機序の各ステップの進行を止めることができ、電解液量の減少を抑制することができる、ことを着想した。 In view of the above mechanism of action, the present inventors can stop the progress of each step of the mechanism of action by preventing water from condensing on the surface of the membrane of the catalyst containing container, and electrolyze. I came up with the idea that the decrease in the amount of liquid can be suppressed.

本態様では、触媒材を収容する容器の開口部を覆う膜は、重力方向に対して0°以上80°以下の角度で配向される。この角度で膜を配向することにより、膜の表面で水が凝縮した場合であっても、凝縮水は重力方向へ滑落するので、膜の表面に液体(水)の層が形成されることを防ぐことができる。これにより、その後の一連の作用機序のステップも進行しない。結果として、触媒の劣化は生じず、電解液量の減少を十分に抑制することができる。また、この態様は、温度制御等の冗長的な作業およびそのための装置を必要とせず、その点で有利である。 In this aspect, the membrane covering the opening of the container containing the catalyst material is oriented at an angle of 0 ° or more and 80 ° or less with respect to the direction of gravity. By orienting the membrane at this angle, even if water is condensed on the surface of the membrane, the condensed water slides down in the direction of gravity, so that a layer of liquid (water) is formed on the surface of the membrane. Can be prevented. As a result, the subsequent steps of the series of action mechanisms do not proceed. As a result, deterioration of the catalyst does not occur, and a decrease in the amount of electrolytic solution can be sufficiently suppressed. Further, this aspect is advantageous in that it does not require redundant work such as temperature control and a device for that purpose.

なお、本考案者らは、本態様の着想を得るまでに、鉛蓄電池において触媒の性能を向上させる手法を見つけるために、電池容器の形状や構造を変更する種々の試行錯誤を重ねた。具体的には、触媒装置(触媒収容容器)を従来とは異なる位置に配置すること、触媒装置内の触媒量を従来より増加すること、触媒装置の開口部を覆う膜の素材、寸法、構成等を調整すること、および、触媒装置の配向(向き)を調整すること等を行なった。実際的には、これらの改良手法の候補は、電池容器の形状や構造によって制約を受けることがしばしばあるので、容易には実現できない。特に、触媒装置の配向を調整することは、電池の組み立ての深さへの影響が大きい点で、好ましくないこと、および触媒装置はフラットに配置をすることが好ましいことを当業者であれば容易に理解する。つまり、当業者が、触媒装置の配向を調整しようとする動機付けは、容易には得られないことに留意されたい。
それにも関わらず、本考案者らは、上記の試行錯誤を実際に行ない、そして、驚くべきことに、触媒装置の配向を調整することが、電解液量を減少させる点で、最も有効であることを見出した。
The present inventors repeated various trials and errors to change the shape and structure of the battery container in order to find a method for improving the performance of the catalyst in the lead-acid battery until the idea of this aspect was obtained. Specifically, the catalyst device (catalyst storage container) is arranged at a position different from the conventional one, the amount of catalyst in the catalyst device is increased from the conventional one, and the material, size, and configuration of the membrane covering the opening of the catalyst device are provided. Etc., and the orientation (orientation) of the catalyst device was adjusted. In practice, candidates for these improved methods are often constrained by the shape and structure of the battery container and are not easily feasible. In particular, it is easy for those skilled in the art to adjust the orientation of the catalyst device, which is not preferable because it has a large effect on the depth of battery assembly, and that the catalyst device is preferably arranged flat. Understand. That is, it should be noted that motivation for those skilled in the art to adjust the orientation of the catalyst device is not easily obtained.
Nonetheless, the present inventors have actually performed the above trial and error, and surprisingly, adjusting the orientation of the catalyst device is most effective in reducing the amount of electrolyte. I found that.

以下の簡便な方法で、本考案の効果を確認することができる。図2に、鉛蓄電池の封口栓に、触媒を収容した容器を取り付けたものを示す。図2(a)のもの(Flat design)は、触媒収容容器の膜が水平に(重力方向に対して90°の角度で)配向されて鉛蓄電池に設置される。図2(b)のもの(Vertical design)は、触媒収容容器の膜が垂直に(重力方向に対して0°の角度で)配向されて鉛蓄電池に設置される。これらの触媒収容容器を取り付けた14.4V鉛蓄電池をそれぞれ12週間に渡って温水浴(ウォーターバス)に設置して電解液の温度を60℃に維持し、電池内部の電解液の減少量を測定した。なお、温水浴の温水の高さと鉛蓄電池内部の電解液の高さがほぼ一致するように調整した。これは、電解液のみを60℃に維持しつつ、電解液より上方、言い換えると触媒収容容器の周囲の雰囲気温度を、できるだけ低温にして、触媒収容容器の膜での水の凝縮を促すためである。また、対照として、触媒収容容器を取り付けない(ベントキャップのみ取り付けた)鉛蓄電池も用意し、電解液の減少量を測定した。 The effect of the present invention can be confirmed by the following simple method. FIG. 2 shows a lead-acid battery with a container containing a catalyst attached to the sealing plug. In FIG. 2A, the membrane of the catalyst container is horizontally oriented (at an angle of 90 ° with respect to the direction of gravity) and installed in the lead-acid battery. In the one shown in FIG. 2B (Vertical design), the membrane of the catalyst containing container is vertically oriented (at an angle of 0 ° with respect to the direction of gravity) and installed in the lead-acid battery. A 14.4V lead-acid battery equipped with these catalyst containing containers was installed in a hot water bath (water bath) for 12 weeks to maintain the temperature of the electrolytic solution at 60 ° C., and the amount of decrease in the electrolytic solution inside the battery was reduced. It was measured. The height of the hot water in the hot water bath was adjusted so that the height of the electrolytic solution inside the lead-acid battery was almost the same. This is to promote the condensation of water in the membrane of the catalyst accommodating container by keeping the ambient temperature above the electrolytic solution, in other words, the ambient temperature of the catalyst accommodating container, as low as possible while maintaining only the electrolytic solution at 60 ° C. is there. As a control, a lead-acid battery without a catalyst container (with only a vent cap attached) was also prepared, and the amount of decrease in the electrolytic solution was measured.

さらに、参考のために、本考案者らが行なった試行錯誤の一部について紹介する。一つ目の試行錯誤は、「触媒量増量」であり、これは上述の水平型の触媒収容容器において、触媒材の充填密度を5倍にしたものである。大量の触媒材が反応熱を高くして、水の凝縮を抑えることを期待したものである。もう一つの試行錯誤は、「二重膜構造」であり、これは上述の水平型の触媒収容容器において、もとの膜の上にさらにもう1枚膜を設置したものである。二重膜構造により、凝縮した水が膜表面を閉塞することを抑えることを期待したものである。 Furthermore, for reference, some of the trial and error performed by the present inventors will be introduced. The first trial and error is "increasing the amount of catalyst", which is the above-mentioned horizontal catalyst container in which the packing density of the catalyst material is increased five times. It is expected that a large amount of catalyst material will increase the heat of reaction and suppress the condensation of water. Another trial and error is the "double membrane structure", which is the above-mentioned horizontal catalyst storage container in which another membrane is placed on the original membrane. It is expected that the double membrane structure will prevent the condensed water from blocking the membrane surface.

上記の簡便な試験の結果、対照の触媒なしの鉛蓄電池では、12週間後の電解液の減少量は約650gであった。触媒収容容器の膜が水平に設置された(Flat design)鉛蓄電池では、約2週間で触媒が劣化し、触媒反応が進まないため、試験を中断した。その後は対照の触媒なしと同様に電解液が減少すると考えられ、12週間後の電解液の減少量は約550gであると考えられる。一方、触媒収容容器の膜が垂直に設置された(Vertical design)鉛蓄電池では、触媒の劣化は見られず、12週間後の電解液の減少量は約250gであった。また、参考用の「触媒量増量」および「二重膜構造」では、約4週間で触媒が劣化し、触媒反応が進まないため、試験を中断した。12週間後の電解液の減少量は約500gであると考えられる。このように、本考案の一態様による、触媒収容容器では、電解液の減少量を十分に抑制できることが確認できる。 As a result of the above simple test, in the control non-catalyst lead-acid battery, the amount of decrease in the electrolytic solution after 12 weeks was about 650 g. In a lead-acid battery in which the membrane of the catalyst storage container was installed horizontally (Flat design), the test was interrupted because the catalyst deteriorated in about 2 weeks and the catalytic reaction did not proceed. After that, the amount of the electrolytic solution is considered to decrease as in the case of no control catalyst, and the amount of decrease of the electrolytic solution after 12 weeks is considered to be about 550 g. On the other hand, in the lead-acid battery in which the membrane of the catalyst container was vertically installed (Vertical design), no deterioration of the catalyst was observed, and the amount of decrease in the electrolytic solution after 12 weeks was about 250 g. In addition, in the reference "catalyst amount increase" and "double membrane structure", the test was interrupted because the catalyst deteriorated in about 4 weeks and the catalytic reaction did not proceed. The amount of decrease in the electrolytic solution after 12 weeks is considered to be about 500 g. As described above, it can be confirmed that the reduction amount of the electrolytic solution can be sufficiently suppressed in the catalyst container according to one aspect of the present invention.

触媒収容容器の膜の配向方向は、重力方向に対して0°以上80°以下である。配向方向は、重力方向、言い換えると0°またはそれに近いほど、凝縮水が膜から滑落しやすくなり有利である。膜の配向方向が重力方向に対して80°を越えると、凝縮水が膜から滑落せずに、膜の表面に液体(水)の層が形成されることがあり、その場合、電解液量の減少を十分に抑制できないことがある。したがって、膜の配向方向は、重力方向に対して0°以上80°以下である。なお、触媒収容容器を取り付けるためのスペースや周囲の構造物の形状に応じて、前記の範囲で適宜角度を調整してもよい。 The orientation direction of the membrane of the catalyst containing container is 0 ° or more and 80 ° or less with respect to the direction of gravity. The orientation direction is the direction of gravity, in other words, the closer it is to 0 ° or closer, the more easily the condensed water slides off the membrane, which is advantageous. If the orientation direction of the membrane exceeds 80 ° with respect to the direction of gravity, condensed water may not slide off the membrane and a layer of liquid (water) may be formed on the surface of the membrane. In that case, the amount of electrolyte solution It may not be possible to sufficiently suppress the decrease in. Therefore, the orientation direction of the film is 0 ° or more and 80 ° or less with respect to the direction of gravity. The angle may be appropriately adjusted within the above range according to the space for mounting the catalyst storage container and the shape of the surrounding structure.

本考案の一態様では、触媒収容容器の膜が疎水性多孔質膜を含んでいてもよい。
疎水性多孔質膜は、疎水(撥水)性であるため、硫酸ミストや電解液(希硫酸水溶液)が、触媒収容容器内の触媒材に直に接触することを防止することができ、触媒の寿命を長くすることができる。
In one aspect of the present invention, the membrane of the catalyst containing container may include a hydrophobic porous membrane.
Since the hydrophobic porous film is hydrophobic (water repellent), it is possible to prevent the sulfuric acid mist and the electrolytic solution (dilute sulfuric acid aqueous solution) from coming into direct contact with the catalyst material in the catalyst container, and the catalyst. Life can be extended.

本考案の一態様では、前記膜が多孔質PTFEを含んでもいてもよい。
前記膜の材質は、酸素、水素および水蒸気を透過できるものであれば特に限定されるものではないが、電池内部の他の材料、例えば硫酸塩等と反応を生じないものが好ましく、ポリエチレン(PE)、ポリプロピレン(PP)、ポリテトラフルオロエチレン(PTFE)等を用いることができ、それらの織布、不織布、編布または多孔質膜を用いてもよい。疎水性多孔質膜が、多孔質ポリテトラフルオロエチレン(PTFE)であってもよい。ポリテトラフルオロエチレンは、疎水性、耐薬品性、耐紫外線性、耐酸化性、耐熱性などの優れた性質を有しており、電池を構成する材料として適している。また、ポリテトラフルオロエチレンを延伸すること等により、容易に多孔質膜を得ることができる。
In one aspect of the present invention, the film may also contain porous PTFE.
The material of the film is not particularly limited as long as it can permeate oxygen, hydrogen and water vapor, but a material that does not react with other materials inside the battery, such as sulfate, is preferable, and polyethylene (PE). ), Polypropylene (PP), polytetrafluoroethylene (PTFE) and the like, and woven fabrics, non-woven fabrics, knitted fabrics or porous films thereof may be used. The hydrophobic porous membrane may be porous polytetrafluoroethylene (PTFE). Polytetrafluoroethylene has excellent properties such as hydrophobicity, chemical resistance, ultraviolet ray resistance, oxidation resistance, and heat resistance, and is suitable as a material for constituting a battery. Further, a porous membrane can be easily obtained by stretching polytetrafluoroethylene or the like.

本考案の一態様では、触媒収容容器の境界形状の少なくとも一部は、円柱、円錐、円錐台、多角形柱、多角形錐、多角形錐台、または球体のいずれか少なくとも一つの形状の少なくとも一部を含んでもよい。
当該触媒収容容器の境界形状(または外形形状)は、前記膜が所定の角度で配向されるものであれば、特に限定されるものではなく、種々の形状を含んでよい。触媒材を収容しやすい観点から、円柱、多角形柱の形状を選択してもよい。触媒材の反応効率を高める観点から、単位体積あたりの表面積が大きくなる球体を選択してもよい。また、触媒収容容器を鉛蓄電池の内部、特に天井部に設置しやすい観点から、当該容器の一部に突起状の円錐、円錐台、多角形錐、多角形錐台の形状を選択してもよい。さらに、種々の形状を、目的用途に応じて、適宜組み合わせることもできる。なお、当該容器がカートリッジタイプであってもよい。
In one aspect of the invention, at least part of the boundary shape of the catalyst containment vessel is at least one of the following shapes: a cylinder, a cone, a truncated cone, a polygonal column, a polygonal cone, a truncated cone, or a sphere. It may include a part.
The boundary shape (or outer shape) of the catalyst containing container is not particularly limited as long as the film is oriented at a predetermined angle, and may include various shapes. From the viewpoint of easily accommodating the catalyst material, the shape of a cylinder or a polygonal column may be selected. From the viewpoint of increasing the reaction efficiency of the catalyst material, a sphere having a large surface area per unit volume may be selected. In addition, from the viewpoint that the catalyst container can be easily installed inside the lead-acid battery, especially in the ceiling, the shape of a protruding cone, a truncated cone, a polygonal cone, or a polygonal cone may be selected for a part of the container. Good. Further, various shapes can be appropriately combined according to the intended use. The container may be a cartridge type.

本考案の一態様では、前述の触媒収容容器を含んだ鉛蓄電池が提供される。
上述した触媒収容容器を含む鉛蓄電池では、電解液量の減少を十分に抑制でき、また温度制御等の冗長的な対策の必要もない。そのため、長期にわたってその充放電性能および電池内部の健全性を維持することができる。
In one aspect of the present invention, a lead storage battery including the above-mentioned catalyst storage container is provided.
In the lead storage battery including the catalyst accommodating container described above, the decrease in the amount of electrolytic solution can be sufficiently suppressed, and there is no need for redundant measures such as temperature control. Therefore, the charge / discharge performance and the soundness inside the battery can be maintained for a long period of time.

以下、実施例および比較例を示して、本考案をより具体的に説明する。ただし、本考案は下記の実施例に限定して解釈されるものではない。 Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples. However, the present invention is not construed as being limited to the following examples.

次の手順で、触媒を収容した容器を用意した。樹脂製の円筒を用意し、その底部に円筒(側面)と同素材の円板を溶着して、円筒の底部を密封した。円筒内部に、酸素および水素から水または水蒸気を生成する反応を促進する触媒材を詰め、円筒の上部(開口部)を表2に示す種々の材質の膜で覆った。なお、対照として、触媒材を詰めない容器のみも用意した。
用意した触媒収容容器を、膜が表2に示す配向角度(重力方向に対する膜の角度)になるように、鉛蓄電池の上部(天井部)に取り付けた。具体的には、触媒収容容器をベントキャップに取り付けて配向角度を調整し、当該ベントキャップを鉛蓄電池の天井部に取り付けた。図3は、膜の配向角度が0°(垂直)である触媒収容容器とベントキャップの例である。なお、鉛蓄電池は、市販のLN2型EFB(GSユアサ製ENJ375LN2−IS)を用いた。
A container containing the catalyst was prepared by the following procedure. A resin cylinder was prepared, and a disk of the same material as the cylinder (side surface) was welded to the bottom of the cylinder to seal the bottom of the cylinder. The inside of the cylinder was filled with a catalyst material that promotes the reaction of producing water or water vapor from oxygen and hydrogen, and the upper part (opening) of the cylinder was covered with membranes of various materials shown in Table 2. As a control, only a container not filled with a catalyst material was prepared.
The prepared catalyst storage container was attached to the upper part (ceiling part) of the lead storage battery so that the film had an orientation angle (angle of the film with respect to the direction of gravity) shown in Table 2. Specifically, the catalyst container was attached to the vent cap to adjust the orientation angle, and the vent cap was attached to the ceiling of the lead-acid battery. FIG. 3 shows an example of a catalyst container and a vent cap in which the orientation angle of the membrane is 0 ° (vertical). As the lead storage battery, a commercially available LN2 type EFB (ENJ375LN2-IS manufactured by GS Yuasa) was used.

触媒収容容器を取り付けた鉛蓄電池をそれぞれ12週間に渡って温水浴(ウォーターバス)に設置して電解液の温度を60℃に維持し、電池総重量を測定することにより電池内部の電解液の減少量を測定した。なお、温水浴の温水の高さと鉛蓄電池内部の電解液の高さがほぼ一致するように調整した。これは、電解液のみを60℃に維持しつつ、電解液より上方、言い換えると触媒収容容器の周囲の雰囲気温度を、できるだけ低温にして、触媒収容容器の膜での水の凝縮を促すためである。また、対照として、触媒材を詰めない容器を取り付けた鉛蓄電池も用意し、電解液の減少量を測定した。結果を表2に示す。 Lead-acid batteries with catalyst storage containers are installed in hot water baths (water baths) for 12 weeks to maintain the temperature of the electrolyte at 60 ° C, and the total weight of the batteries is measured to measure the electrolyte inside the batteries. The amount of decrease was measured. The height of the hot water in the hot water bath was adjusted so that the height of the electrolytic solution inside the lead-acid battery was almost the same. This is to promote the condensation of water in the membrane of the catalyst accommodating container by keeping the ambient temperature above the electrolytic solution, in other words, the ambient temperature of the catalyst accommodating container, as low as possible while maintaining only the electrolytic solution at 60 ° C. is there. In addition, as a control, a lead storage battery equipped with a container not filled with a catalyst material was also prepared, and the amount of decrease in the electrolytic solution was measured. The results are shown in Table 2.

上記の結果から、対照の触媒なしの鉛蓄電池では、12週間後の電解液の減少量は約400gであった。
触媒収容容器の膜が本考案の範囲の角度で配向されている場合、12週間後でも電解液の減少量は約50〜200gと、対照に比べて大幅に減少しており、また、触媒収容容器およびその周囲の雰囲気は約40℃に維持されていた(特に温度制御のため加熱等の冗長的な操作は行なっていない)。これらのことから触媒反応が安定して進行していたことが示唆された。
一方、膜が90°の角度で、つまり水平に配向されている場合、電解液の減少量は約360gであり、対照に比べて十分に減少しなかった。この比較例では、膜の表面で水が凝縮し、膜が水平であるために当該凝縮水が滑落せずに、膜の表面に液体(水)の層が形成されて、触媒反応が促されず、最終的には触媒の劣化に至ったことが示唆された。
From the above results, in the control non-catalyst lead-acid battery, the amount of decrease in the electrolytic solution after 12 weeks was about 400 g.
When the membrane of the catalyst container is oriented at an angle within the range of the present invention, the amount of decrease in the electrolytic solution is about 50 to 200 g even after 12 weeks, which is significantly reduced as compared with the control, and the catalyst is contained. The atmosphere of the container and its surroundings was maintained at about 40 ° C. (particularly, redundant operations such as heating were not performed for temperature control). From these facts, it was suggested that the catalytic reaction proceeded stably.
On the other hand, when the film was oriented at an angle of 90 °, that is, horizontally, the amount of decrease in the electrolytic solution was about 360 g, which was not sufficiently reduced as compared with the control. In this comparative example, water is condensed on the surface of the membrane, and since the membrane is horizontal, the condensed water does not slide down, and a layer of liquid (water) is formed on the surface of the membrane to promote the catalytic reaction. However, it was suggested that the catalyst eventually deteriorated.

10 鉛蓄電池用ベントキャップ
20 触媒収容容器
30 触媒材
40 膜
50 ホルダー
10 Vent cap for lead-acid battery 20 Catalyst storage container 30 Catalyst material 40 Membrane 50 Holder

Claims (5)

鉛蓄電池において触媒材を収容する容器であって、
前記触媒材は、酸素および水素から水または水蒸気を生成する反応を促進する触媒を含み、且つ前記容器は膜で覆われた開口部を持ち、
前記膜は、前記酸素、前記水素および前記水蒸気を前記触媒材と当該容器の外部との間で連通し、且つ重力方向に対して0°以上80°以下の角度で配向される、ことを特徴とする、容器。
A container that houses a catalyst material in a lead-acid battery.
The catalyst material comprises a catalyst that promotes a reaction that produces water or water vapor from oxygen and hydrogen, and the container has a membrane-covered opening.
The membrane is characterized in that the oxygen, the hydrogen and the water vapor communicate with each other between the catalyst material and the outside of the container, and are oriented at an angle of 0 ° or more and 80 ° or less with respect to the direction of gravity. And the container.
前記膜が疎水性多孔質膜を含んでなることを特徴とする、請求項1に記載の容器。 The container according to claim 1, wherein the membrane comprises a hydrophobic porous membrane. 前記膜が多孔質PTFEを含んでなることを特徴とする、請求項1または2に記載の容器。 The container according to claim 1 or 2, wherein the film comprises porous PTFE. 当該容器の境界形状の少なくとも一部は、円柱、円錐、円錐台、多角形柱、多角形錐、多角形錐台、または球体のいずれか少なくとも一つの形状の少なくとも一部を含む、ことを特徴とする、請求項1〜3のいずれか1項に記載の容器。 The boundary shape of the container is characterized by including at least a part of at least one shape of a cylinder, a cone, a truncated cone, a truncated cone, a polygonal cone, a polygonal cone, or a sphere. The container according to any one of claims 1 to 3. 請求項1〜4のいずれか1項に記載の容器を含んでなる、鉛蓄電池。 A lead-acid battery comprising the container according to any one of claims 1 to 4.
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