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JP7010772B2 - Ribbed separator for lead-acid battery and lead-acid battery using the separator - Google Patents
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JP7010772B2 - Ribbed separator for lead-acid battery and lead-acid battery using the separator - Google Patents

Ribbed separator for lead-acid battery and lead-acid battery using the separator Download PDF

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JP7010772B2
JP7010772B2 JP2018116831A JP2018116831A JP7010772B2 JP 7010772 B2 JP7010772 B2 JP 7010772B2 JP 2018116831 A JP2018116831 A JP 2018116831A JP 2018116831 A JP2018116831 A JP 2018116831A JP 7010772 B2 JP7010772 B2 JP 7010772B2
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久士 大内
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Furukawa Battery 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
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Description

本発明は、鉛蓄電池用リブ付きセパレータのリブの改良、及びそのセパレータを用いた鉛蓄電池に関するものである。 The present invention relates to an improvement of the rib of a ribbed separator for a lead storage battery and a lead storage battery using the separator.

流動性をもつ電解液を正負極板間に有してなる鉛蓄電池には、図4に示すように柔軟な合成樹脂製肉薄シートの極板と当接するベース面上に、長さ方向を該ベース面の垂直方向に向けて設けたリブを有す、リブ付きセパレータが用いられることが知られている。前記リブは、鉛蓄電池の使用時に正極板から発生する酸素ガスの強い酸化力により、前記ベース面が酸化して孔が開く等による短絡を防ぐために、正極板とベース面とが直接接触しないように、正極板と当接する面に設けられている。また前記リブは、充電末期に極板から顕著に発生する酸素ガスや水素ガス(以下、これらをガスという)の排出経路としても機能する(例えば、特許文献1、図4)。 For a lead-acid battery having a fluid electrolytic solution between the positive and negative electrode plates, as shown in FIG. 4, the length direction is oriented on the base surface in contact with the electrode plate of the flexible synthetic resin thin sheet. It is known that a ribbed separator having ribs provided in the vertical direction of the base surface is used. The ribs do not come into direct contact with the positive electrode plate and the base surface in order to prevent a short circuit due to oxidation of the base surface and opening of holes due to the strong oxidizing power of oxygen gas generated from the positive electrode plate when the lead storage battery is used. Is provided on the surface that comes into contact with the positive electrode plate. The rib also functions as a discharge path for oxygen gas and hydrogen gas (hereinafter referred to as gas) remarkably generated from the electrode plate at the end of charging (for example, Patent Documents 1 and 4).

近年、燃費の向上や排気ガスの削減を目的に、アイドリングストップシステムを導入した自動車(以下、ISS車という)が普及している。ISS車用の鉛蓄電池は、従来のSLI(始動・照明・点火)用の鉛蓄電池に比べ、使用時の負荷が大きくなる。例えばISS車用の鉛蓄電池は、発進の度にエンジンを始動する大電流の放電を繰り返し、さらに、エンジン停止中もエアコンやカーナビ、カーステレオ等の機器を駆動する電力を賄うため、深い放電状態となる。また停車の度にエンジンが停止するため、オルタネータによる発電の機会も少なくなる。特に継続走行距離の短い市街地での走行などでは、放電に比べ浅い充電が繰り返されるため、ISS車用の鉛蓄電池は、十分な充電がされず部分充電状態となる。鉛蓄電池を部分充電状態で使用した場合、極板から濃度の高い硫酸が生じて沈降する一方、上記充電末期に発生するガスによる電解液の攪拌が期待できず、成層化が起き短寿命となり易い。ゆえに、ISS車用の鉛蓄電池には成層化対策が求められる。 In recent years, automobiles (hereinafter referred to as ISS vehicles) that have introduced an idling stop system have become widespread for the purpose of improving fuel efficiency and reducing exhaust gas. The lead-acid battery for ISS vehicles has a larger load during use than the conventional lead-acid battery for SLI (starting / lighting / ignition). For example, lead-acid batteries for ISS vehicles are in a deep discharge state because they repeatedly discharge a large current that starts the engine each time they start, and also supply power to drive equipment such as air conditioners, car navigation systems, and car stereos even when the engine is stopped. Will be. In addition, since the engine stops each time the vehicle is stopped, the chances of power generation by the alternator are reduced. In particular, when traveling in an urban area where the continuous mileage is short, shallow charging is repeated as compared with discharging, so that the lead-acid battery for an ISS vehicle is not sufficiently charged and becomes partially charged. When a lead-acid battery is used in a partially charged state, high-concentration sulfuric acid is generated from the electrode plate and precipitates, but the electrolytic solution cannot be expected to be agitated by the gas generated at the end of charging, and stratification occurs and the life tends to be short. .. Therefore, lead-acid batteries for ISS vehicles are required to have stratification measures.

成層化とは上述の通り、充電時に極板から生じる濃度の高い硫酸が電槽セル内底部に向かって沈降し、電解液の硫酸濃度が電槽セル内の下方では高く、上方では低い状態が続く現象のことである。該成層化は、例えば電解液の上下比重差として測定される。前記成層化が起こると、極板下部では不動態化した硫酸鉛が蓄積するサルフェーションが進行し、充電効率が低下する。また濃淡電池が形成されて自己放電が急速に進行し、鉛蓄電池は短寿命となる。 As described above, stratification means that high-concentration sulfuric acid generated from the electrode plate during charging settles toward the bottom of the battery cell, and the sulfuric acid concentration of the electrolytic solution is high in the lower part of the battery cell and low in the upper part. It is a phenomenon that follows. The stratification is measured, for example, as a difference in the vertical specific gravity of the electrolytic solution. When the stratification occurs, sulfation in which passivated lead sulfate accumulates progresses in the lower part of the electrode plate, and the charging efficiency decreases. In addition, a concentration cell is formed and self-discharge progresses rapidly, so that the lead-acid battery has a short life.

係る事情から、出願人等は特許文献2に開示するように、鉛蓄電池の負極板にキャパシタ電極材料を組み合わせて充電受入性を高め、高い充電状態を維持できるように改良された鉛蓄電池を提案している。上記のように鉛蓄電池の充電受入性を高めることで、ISS車に搭載した場合でも、充電状態が充電末期に到達することでガスを十分に発生させられる。 For this reason, the applicants, etc., as disclosed in Patent Document 2, propose an improved lead-acid battery that can maintain a high charge state by combining a capacitor electrode material with the negative electrode plate of the lead-acid battery to improve charge acceptability. is doing. By increasing the charge acceptability of the lead-acid battery as described above, even when the lead-acid battery is mounted on an ISS vehicle, the state of charge reaches the end of charging, so that gas can be sufficiently generated.

特許文献1に記載のセパレータを用いた鉛蓄電池をISS車に適用する場合は、充電時に極板から生じる濃度の高い硫酸が、垂直方向に向けて設けられたリブの隙間を通って多量に沈降するため、充電末期にガスが発生しても電解液の攪拌が不十分となり、成層化が起き易い問題があった。 When a lead-acid battery using the separator described in Patent Document 1 is applied to an ISS vehicle, a large amount of highly concentrated sulfuric acid generated from the electrode plate during charging settles through the gaps between ribs provided in the vertical direction. Therefore, even if gas is generated at the end of charging, the electrolytic solution is not sufficiently agitated, and there is a problem that stratification is likely to occur.

これに対し本発明の出願人は特許文献3において、ISS車に適用する鉛蓄電池の成層化を防止する手段として、図5に示すようなリブ付きセパレータを開示している。該リブ付きセパレータの合成樹脂製肉薄シートのベース面上に設けたリブは、その長さ方向を水平方向に設けており、前記リブの両端部の上面は内側部分の上面より高い位置にあり、前記リブの下面は、前記リブの長さ方向の中央部分が最も低い位置にあり、中央部分から両端に向けて上り勾配に形成されている。 On the other hand, the applicant of the present invention discloses in Patent Document 3 a ribbed separator as shown in FIG. 5 as a means for preventing stratification of a lead storage battery applied to an ISS vehicle. The ribs provided on the base surface of the synthetic resin thin sheet of the ribbed separator are provided in the horizontal direction in the length direction, and the upper surfaces of both ends of the ribs are located higher than the upper surface of the inner portion. The lower surface of the rib has a central portion in the length direction of the rib at the lowest position, and is formed with an upward slope from the central portion toward both ends.

この形状によれば、正極板と負極板とを上記リブ付きセパレータを介して積層された極板群を備える鉛蓄電池において、充電時に極板から生じる濃度の高い硫酸は、リブの上面で捕捉され、成層化が抑制される。また、特許文献3のリブ付きセパレータであれば、特許文献2のような充電受入性の高い鉛蓄電池と組み合わせて使用した場合でも、充電時に生じるガスは前記リブの下面に沿って上昇し、前記リブの端部から極板上方に抜ける。前記ガスが極板と電解液との間に滞留すると、活物質と電解液との接触面積の減少に伴い、充放電の際、局所的に電流密度が増加する箇所が生じ、極板の劣化を招き、短寿命の一因となる。そのため、前記ガスの排出経路の確保が重要である。 According to this shape, in a lead-acid battery including a group of electrode plates in which a positive electrode plate and a negative electrode plate are laminated via the ribbed separator, high-concentration sulfuric acid generated from the electrode plate during charging is captured on the upper surface of the rib. , Stratification is suppressed. Further, in the case of the ribbed separator of Patent Document 3, even when used in combination with a lead storage battery having high charge acceptability as in Patent Document 2, the gas generated during charging rises along the lower surface of the rib, and the said. It comes out from the end of the rib above the electrode plate. When the gas stays between the electrode plate and the electrolytic solution, the contact area between the active material and the electrolytic solution decreases, and at the time of charging / discharging, a place where the current density locally increases occurs, and the electrode plate deteriorates. Invites and contributes to a short life. Therefore, it is important to secure the gas discharge route.

特開平9-97601号公報Japanese Unexamined Patent Publication No. 9-97601 特許第5576660号公報Japanese Patent No. 5576660 特開2005-197145号公報Japanese Unexamined Patent Publication No. 2005-197145

しかしながら、特許文献3に開示されるリブ付きセパレータは、濃度の高い硫酸の沈降防止とガスの滞留防止の両立において、改良の余地があった。 However, the ribbed separator disclosed in Patent Document 3 has room for improvement in both prevention of sedimentation of high-concentration sulfuric acid and prevention of gas retention.

そこで本発明は、充電時に極板から生じる濃度の高い硫酸の沈降防止と、極板間のガスの滞留防止とを両立し、成層化を抑制し得る鉛蓄電池用リブ付きセパレータ、及びそのセパレータを用いた耐久性の高い鉛蓄電池を提供することを目的とする。 Therefore, the present invention provides a ribbed separator for a lead storage battery, which can suppress stratification by both preventing sedimentation of high-concentration sulfuric acid generated from the plates during charging and preventing gas from staying between the plates, and a separator thereof. It is an object of the present invention to provide a highly durable lead-acid battery used.

本発明の請求項1に係るリブ付きセパレータは、シートのベース面上に厚さ方向に垂直なリブを設けたリブ付きセパレータにおいて、前記リブは水平リブと、V字リブと、右斜めリブと、左斜めリブとを含み、前記水平リブは前記リブ付きセパレータを平面視したとき、上下方向の下端に設けられており、前記V字リブは前記水平リブに対して右辺の角度がπ/6radからπ/3radまでの範囲、かつ左辺の角度が2π/3radから5π/6radまでの範囲であって、前記右辺と前記左辺とで成す頂点から前記右辺と前記左辺の夫々の端部までの高さの比が0.95から1.05までの範囲であって、前記ベース面上に下に凸となるように設けられており、前記右斜めリブは前記水平リブとの交点を始点とし、前記水平リブとのなす角がπ/6radからπ/3radまでの範囲であって、右斜め上方向に延伸して設けられており、該始点は前記頂点よりも右側に位置するものであり、前記左斜めリブは前記水平リブとの交点を始点とし、前記水平リブとのなす角が2π/3radから5π/6radまでの範囲であって、左斜め上方向に延伸して設けられており、該始点は前記頂点よりも左側に位置するものであり、前記V字リブ、前記右斜めリブ、及び前記左斜めリブは前記ベース面上に夫々複数条設けられ、互いに隣接する前記V字リブ、前記右斜めリブ、前記左斜めリブ、及び前記水平リブの夫々の端部間の垂直方向の間隔は、8mmから15mmまでの範囲で設けられていることを特徴とする。いずれのリブも、短手方向の断面において、ベース面と連続した上面及び下面と、前記上面及び前記下面と連続した頂面とを備える矩形状を有するものであって、かつ該リブ付きセパレータを介して正極板と負極板とを交互に積層し極板群とした際、対向する極板の表面、又は他のリブ付きセパレータと前記頂面で当接する。ここで、前記リブの断面が矩形でない多角形である場合は、極板群を形成した際に、該リブ付きセパレータと対向する極板の表面、又は他のリブ付きセパレータと当接する面を頂面と定義する。 The ribbed separator according to claim 1 of the present invention is a ribbed separator in which ribs perpendicular to the thickness direction are provided on the base surface of the sheet, and the ribs are horizontal ribs, V-shaped ribs, and right diagonal ribs. The horizontal rib is provided at the lower end in the vertical direction when the ribbed separator is viewed in a plan view, and the V-shaped rib has an angle of π / 6 rad on the right side with respect to the horizontal rib. To π / 3rad, and the angle of the left side is in the range of 2π / 3rad to 5π / 6rad, and the height from the apex formed by the right side and the left side to the respective ends of the right side and the left side. The ratio is in the range of 0.95 to 1.05, and is provided so as to be convex downward on the base surface, and the right diagonal rib starts from the intersection with the horizontal rib. The angle formed by the horizontal rib is in the range of π / 6 rad to π / 3 rad, and is provided so as to extend diagonally upward to the right, and the starting point is located on the right side of the apex. The left diagonal rib has an angle formed with the horizontal rib in the range of 2π / 3rad to 5π / 6rad, starting from the intersection with the horizontal rib, and is provided so as to extend diagonally upward to the left. The starting point is located on the left side of the apex, and the V-shaped rib, the right diagonal rib, and the left diagonal rib are each provided with a plurality of strips on the base surface, and the V-shaped ribs adjacent to each other. The vertical distance between the ends of the right diagonal rib, the left diagonal rib, and the horizontal rib is provided in the range of 8 mm to 15 mm. Each rib has a rectangular shape having an upper surface and a lower surface continuous with the base surface and a top surface continuous with the upper surface and the lower surface in a cross section in the lateral direction, and the ribbed separator is provided. When the positive electrode plate and the negative electrode plate are alternately laminated to form a group of electrode plates, they come into contact with the surface of the opposing electrode plates or another ribbed separator at the top surface. Here, when the cross section of the rib is a non-rectangular polygon, when the electrode plate group is formed, the surface of the electrode plate facing the ribbed separator or the surface in contact with another ribbed separator is topped. Defined as a face.

前記V字リブの右辺の角度は、π/3radを超えると傾斜が急であるため、V字形状が縦長の形状になり、極板上部で生じた濃度の高い硫酸が電槽セル内底部まで沈降することを抑制する効果が小さくなる。π/6rad未満だと傾斜が緩いため、生じたガスの排気がし難い。同様に、前記V字リブの左辺の角度は、2π/3rad未満だと傾斜が急であるため、V字形状が縦長の形状になり、極板上部で生じた濃度の高い硫酸が電槽セル内底部まで沈降することを抑制する効果が小さくなる。5π/6radを超えると傾斜が緩いため、生じたガスの排気がし難い。したがって、前記V字リブの右辺、及び左辺の夫々の角度はπ/6radからπ/3radまでの範囲、及び2π/3radから5π/6radまでの範囲で形成されることが好ましい。 Since the angle of the right side of the V-shaped rib is steep when it exceeds π / 3rad, the V-shaped shape becomes a vertically long shape, and the high-concentration sulfuric acid generated at the top of the electrode plate reaches the bottom of the battery case cell. The effect of suppressing sedimentation is reduced. If it is less than π / 6rad, the slope is gentle and it is difficult to exhaust the generated gas. Similarly, if the angle of the left side of the V-shaped rib is less than 2π / 3rad, the inclination is steep, so that the V-shaped shape becomes a vertically long shape, and the high-concentration sulfuric acid generated in the upper part of the electrode plate is the battery cell. The effect of suppressing sedimentation to the inner bottom is reduced. If it exceeds 5π / 6rad, the slope is gentle, so it is difficult to exhaust the generated gas. Therefore, it is preferable that the angles of the right side and the left side of the V-shaped rib are formed in the range of π / 6rad to π / 3rad and the range of 2π / 3rad to 5π / 6rad.

同様の理由から、前記右斜めリブ、及び前記左斜めリブの前記水平リブとのなす角は夫々π/6radからπ/3radまでの範囲、及び2π/3radから5π/6radまでの範囲で形成されることが好ましい。 For the same reason, the angle formed by the right diagonal rib and the left diagonal rib with the horizontal rib is formed in the range of π / 6rad to π / 3rad and the range of 2π / 3rad to 5π / 6rad, respectively. Is preferable.

また前記水平リブは前記右斜めリブ、及び前記左斜めリブを設けることで、前記V字リブより下方でポケットを形成し、充電時に極板から生じる濃度の高い硫酸を、該ポケットを成すリブの上面で捕捉でき、電解液の成層化を抑制する。 Further, the horizontal ribs are provided with the right diagonal ribs and the left diagonal ribs to form pockets below the V-shaped ribs, and high-concentration sulfuric acid generated from the electrode plate during charging is applied to the ribs forming the pockets. It can be captured on the upper surface and suppresses the stratification of the electrolytic solution.

上記構成において、前記V字リブ、前記右斜めリブ、及び前記左斜めリブが、前記ベース面上に夫々複数条設けることで、充電時に極板から生じる濃度の高い硫酸を捕捉する領域が上下方向に分散され、濃度の高い硫酸の沈降が抑制される。上下方向に分散して捕捉された濃度の高い硫酸は、比較的少量であるため周囲の電解液に拡散し易く、電槽セル内の上部と下部の電解液比重の偏りを抑制できる。 In the above configuration, the V-shaped rib, the right diagonal rib, and the left diagonal rib are each provided in a plurality of rows on the base surface, so that a region for capturing high-concentration sulfuric acid generated from the electrode plate during charging is in the vertical direction. It is dispersed in the water and the sedimentation of high-concentration sulfuric acid is suppressed. Since the high-concentration sulfuric acid dispersed and captured in the vertical direction is relatively small, it easily diffuses into the surrounding electrolytic solution, and it is possible to suppress the deviation of the specific gravity of the upper and lower electrolytic solutions in the battery cell.

上記構成において、複数条設けられた前記V字リブは、右辺と左辺とで成す頂点から前記右辺と前記左辺の夫々の端部までの高さの比が0.95から1.05までの範囲であれば、同一のリブにおいて左右の端部の高さが略同じとなるため、充電時に極板から生じる濃度の高い硫酸が高さの低い端部側から溢れて沈降することを抑制できる。また、前記高さの比が0.95から1.05までの範囲であれば、夫々の前記頂点がベース面上の同一直線上に位置していても良いし、同一直線上に位置せず左右に疎らに位置しても良い。 In the above configuration, the V-shaped rib provided with a plurality of rows has a height ratio of 0.95 to 1.05 from the apex formed by the right side and the left side to the respective ends of the right side and the left side. If this is the case, since the heights of the left and right ends of the same rib are substantially the same, it is possible to prevent the high-concentration sulfuric acid generated from the electrode plate from overflowing and settling from the low-height end side during charging. Further, as long as the height ratio is in the range of 0.95 to 1.05, the respective vertices may be located on the same straight line on the base surface, or may not be located on the same straight line. It may be located sparsely to the left and right.

また上記構成において、互いに隣接する前記V字リブ、前記右斜めリブ、前記左斜めリブ、及び前記水平リブの夫々の端部間の垂直方向の間隔は、8mm未満だと前記間隔が狭すぎて生じたガスの排気がし難い。15mmを超えると、前記間隔が広すぎて濃度の高い硫酸を捕捉する領域が広くなり、電解液の成層化を抑制する効果が小さくなる。したがって、互いに隣接する前記V字リブ、前記右斜めリブ、前記左斜めリブ、及び前記水平リブの夫々の端部間の垂直方向の間隔は、8mmから15mmまでの範囲で形成されることが好ましい。 Further, in the above configuration, if the vertical distance between the ends of the V-shaped rib, the right diagonal rib, the left diagonal rib, and the horizontal rib adjacent to each other is less than 8 mm, the distance is too narrow. It is difficult to exhaust the generated gas. If it exceeds 15 mm, the interval is too wide and the region for capturing high-concentration sulfuric acid becomes wide, and the effect of suppressing the stratification of the electrolytic solution becomes small. Therefore, the vertical spacing between the ends of the V-shaped ribs, the right diagonal ribs, the left diagonal ribs, and the horizontal ribs adjacent to each other is preferably formed in the range of 8 mm to 15 mm. ..

本発明の請求項2に係るリブ付きセパレータは、上記構成において、前記V字リブが前記水平リブと直交する中心線を対称軸とした線対称に設けられていることを特徴とする。前記V字リブを線対称とすることで、同一のリブにおいて左右の端部の高さが同じになるため、充電時に極板から生じる濃度の高い硫酸が高さの低い端部側から溢れて沈降することを防ぎ、さらにガスも左右から均等に排気できるため、極板間でのガス滞留を防止する上で有利にはたらく。 The ribbed separator according to claim 2 of the present invention is characterized in that, in the above configuration, the V-shaped rib is provided line-symmetrically with a center line orthogonal to the horizontal rib as an axis of symmetry. By making the V-shaped rib line-symmetrical, the heights of the left and right ends of the same rib are the same, so that the high-concentration sulfuric acid generated from the electrode plate during charging overflows from the low-height end side. Since it prevents the gas from settling and the gas can be exhausted evenly from the left and right, it is advantageous in preventing the gas from staying between the plates.

本発明の請求項3に係るリブ付きセパレータは、上記構成において、複数条設けられた前記V字リブの内、最下段に位置するV字リブの頂点が前記水平リブと交点を有すように設けられていることを特徴とする。前記最下段に位置するV字リブの頂点と前記水平リブとが交点で接合されることで、極板群に所定の群圧が掛かった際に、前記最下段に位置するV字リブの頂点が前記水平リブを支え、前記水平リブの折れ曲がりによるベース面の破れ等を抑制できる。 In the ribbed separator according to claim 3 of the present invention, in the above configuration, among the plurality of V-shaped ribs provided, the apex of the V-shaped rib located at the lowest stage has an intersection with the horizontal rib. It is characterized by being provided. By joining the apex of the V-shaped rib located at the lowest stage and the horizontal rib at an intersection, the apex of the V-shaped rib located at the lowest stage when a predetermined group pressure is applied to the electrode plate group. Supports the horizontal ribs and can suppress tearing of the base surface due to bending of the horizontal ribs.

本発明の請求項4に係るリブ付きセパレータは、上記構成において、前記右斜めリブと前記左斜めリブとが前記中心線を対称軸とした線対称に設けられていることを特徴とする。前記右斜めリブと前記左斜めリブとを線対称に設けることで、前記V字リブを線対称に設けた場合と同様の理由により、左右の斜めリブにおいて左右の端部の高さが同じになるため、充電時に極板から生じる濃度の高い硫酸が高さの低い端部側から溢れて沈降することを防ぎ、さらにガスも左右から均等に排気できるため、極板間でのガス滞留を防止する上で有利にはたらく。 The ribbed separator according to claim 4 of the present invention is characterized in that, in the above configuration, the right diagonal rib and the left diagonal rib are provided in line symmetry with the center line as the axis of symmetry. By providing the right diagonal rib and the left diagonal rib line-symmetrically, the heights of the left and right ends of the left and right diagonal ribs are the same for the same reason as when the V-shaped rib is provided line-symmetrically. This prevents high-concentration sulfuric acid generated from the plates during charging from overflowing from the low end side and settling, and also prevents gas from staying between the plates because gas can be evenly exhausted from the left and right. It works to your advantage.

本発明の請求項5に係る鉛蓄電池は、上記請求項1乃至4のいずれかに係るリブ付きセパレータが用いられていることを特徴とする。前記請求項1乃至4のいずれかに係るリブ付きセパレータを鉛蓄電池に用いることで、耐久性の高い鉛蓄電池を提供することができる。 The lead-acid battery according to claim 5 of the present invention is characterized in that the ribbed separator according to any one of claims 1 to 4 is used. By using the ribbed separator according to any one of claims 1 to 4 in a lead storage battery, it is possible to provide a lead storage battery with high durability.

本発明の請求項6に係る鉛蓄電池は、上記請求項5に係る鉛蓄電池であって、極板群に掛かる群圧が5kPaから30kPaまでの範囲であることを特徴とする。前記極板群に掛かる群圧が5kPa未満では圧迫力が弱すぎて、リブと極板との間に隙間が生じ、そこから濃度の高い硫酸が流出する場合がある。また30kPaを超えると、電槽セル内に極板群が収容できない場合や収容後に電槽が膨らみ破損する場合がある。前記極板群に掛かる群圧を5kPaから30kPaまでの範囲にすることで、リブと極板との間に隙間が生じ難く、濃度の高い硫酸は前記リブ上面に良好に捕捉される。また、電槽セル内に前記極板群を破損させることなく収容できる。したがって、前記極板群に掛かる群圧は5kPaから30kPaまでの範囲であることが望ましい。 The lead-acid battery according to claim 6 of the present invention is the lead-acid battery according to claim 5, wherein the group pressure applied to the electrode plate group is in the range of 5 kPa to 30 kPa. If the group pressure applied to the plate group is less than 5 kPa, the pressing force is too weak, and a gap may be formed between the rib and the plate, and high-concentration sulfuric acid may flow out from the gap. On the other hand, if it exceeds 30 kPa, the electrode plate group may not be accommodated in the battery cell, or the battery may swell and be damaged after being accommodated. By setting the group pressure applied to the electrode plate group in the range of 5 kPa to 30 kPa, a gap is unlikely to occur between the rib and the electrode plate, and high-concentration sulfuric acid is satisfactorily captured on the upper surface of the rib. Further, the electrode plates can be housed in the battery cell without damaging the electrode plates. Therefore, it is desirable that the group pressure applied to the electrode plate group is in the range of 5 kPa to 30 kPa.

本発明のリブ付きセパレータは、充電時に極板から生じる濃度の高い硫酸を前記V字リブの上面で捕捉できる。さらに前記水平リブは前記右斜めリブ、及び前記左斜めリブを設けることで、前記V字リブより下方でポケットを形成し、充電時に極板から生じる濃度の高い硫酸を、該ポケットを成すリブの上面で捕捉できる。したがって、充電時に極板から生じる濃度の高い硫酸は前記水平リブ、前記V字リブ、前記右斜めリブ、及び前記左斜めリブにより、電槽セル内底部に沈降しないよう捕捉され、電解液の成層化を抑制できる。 The ribbed separator of the present invention can capture high-concentration sulfuric acid generated from the electrode plate during charging on the upper surface of the V-shaped rib. Further, the horizontal ribs are provided with the right diagonal ribs and the left diagonal ribs to form pockets below the V-shaped ribs, and high-concentration sulfuric acid generated from the electrode plate during charging is applied to the ribs forming the pockets. Can be captured on the top surface. Therefore, the highly concentrated sulfuric acid generated from the electrode plate during charging is captured by the horizontal ribs, the V-shaped ribs, the right diagonal ribs, and the left diagonal ribs so as not to settle on the inner bottom of the battery case, and the electrolytic solution is stratified. It can suppress the change.

また、充電時に極板から生じるガスは前記V字リブ、前記右斜めリブ、及び前記左斜めリブの下面に沿って上昇し、前記V字リブ、前記右斜めリブ、及び前記左斜めリブの端部
から極板上方に抜ける。したがって、極板間でのガス滞留を防止する上で有利にはたらく。
Further, the gas generated from the electrode plate during charging rises along the lower surfaces of the V-shaped rib, the right diagonal rib, and the left diagonal rib, and the ends of the V-shaped rib, the right diagonal rib, and the left diagonal rib. It comes out from the part above the electrode plate. Therefore, it is advantageous in preventing gas retention between the plates.

また正極板と負極板とを、本発明のリブ付きセパレータを介在させて交互に積層した極板群に掛かる群圧を5kPaから30kPaまでの範囲にすることで、リブと極板との間に隙間が生じ難く、濃度の高い硫酸は前記リブ上面に良好に捕捉される。また、電槽セル内に前記極板群を破損させることなく収容できる。 Further, by setting the group pressure applied to the electrode plate group in which the positive electrode plate and the negative electrode plate are alternately laminated by interposing the ribbed separator of the present invention in the range of 5 kPa to 30 kPa, the pressure between the rib and the electrode plate is set. Gap is unlikely to occur, and high-concentration sulfuric acid is well trapped on the upper surface of the rib. Further, the electrode plates can be housed in the battery cell without damaging the electrode plates.

以上の通り本発明によれば、充電時に極板から生じる濃度の高い硫酸の沈降防止と、極板間のガスの滞留防止とを両立し、成層化を抑制し得る鉛蓄電池用リブ付きセパレータ、及びそのセパレータを用いた耐久性の高い鉛蓄電池を提供することができる。 As described above, according to the present invention, a ribbed separator for a lead storage battery capable of suppressing stratification by both preventing sedimentation of high-concentration sulfuric acid generated from the plates during charging and preventing gas from staying between the plates. And a lead storage battery having high durability using the separator thereof can be provided.

本発明のリブ付きセパレータの実施形態を示す正面図である。It is a front view which shows the embodiment of the separator with a rib of this invention. 本発明のリブ付きセパレータを袋状にして、極板を収容する工程を示す説明図である。It is explanatory drawing which shows the process which made the ribbed separator of this invention into a bag shape, and accommodates the electrode plate. 本発明のリブ付きセパレータの実施形態におけるリブ配置パターンを示す展開図である。It is a developed view which shows the rib arrangement pattern in embodiment of the separator with a rib of this invention. 本発明の比較例1のリブ付きセパレータを示す正面図である。It is a front view which shows the separator with the rib of the comparative example 1 of this invention. 本発明の比較例2のリブ付きセパレータを示す正面図である。It is a front view which shows the separator with the rib of the comparative example 2 of this invention.

以下に、本発明の実施形態を、図を参照しながら説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は本発明のリブ付きセパレータ1の実施形態を示す正面図である。リブ付きセパレータ1は、負極板7を収納するように袋状に加工されており、正極板(図示せず)と当接する外側となるシートのベース面2上に厚さ方向に垂直なリブが設けられており、内側となるシートのベース面2上にはリブを設けないフラットな面である。前記リブは水平リブ3aと、V字リブ3bと、右斜めリブ3cと、左斜めリブ3dとを含んでいる。水平リブ3aはリブ付きセパレータ1を介して正極板と負極板7とを交互に積層し、これを積層方向に平面視したとき、正極集電耳側、及び負極集電耳側を上とする上下方向の下端に設けられている。V字リブ3bは水平リブ3aに対して右辺の角度がπ/6radからπ/3radまでの範囲、かつ左辺の角度が2π/3radから5π/6radまでの範囲であって、前記右辺と前記左辺とで成す頂点4から前記右辺、及び前記左辺の夫々の端部右5R、及び端部左5Lまでの高さの比が0.95から1.05までの範囲であって、ベース面2上に下に凸となるように設けられている。右斜めリブ3cは水平リブ3aとの交点を始点右6Rとし、水平リブ3aとのなす角がπ/6radからπ/3radまでの範囲であって、右斜め上方向に延伸して設けられており、該始点右6Rは頂点4よりも右側に位置する。左斜めリブ3dは水平リブ3aとの交点を始点左6Lとし、水平リブ3aとのなす角が2π/3radから5π/6radまでの範囲であって、左斜め上方向に延伸して設けられており、該始点左6Lは頂点4よりも左側に位置する。V字リブ3b、右斜めリブ3c、及び左斜めリブ3dはベース面2上に夫々複数条設けられている。互いに隣接するV字リブ3b、右斜めリブ3c、左斜めリブ3d、及び水平リブ3aの夫々の端部間の垂直方向の間隔Dvは8mmから15mmまでの範囲で設けられている。 FIG. 1 is a front view showing an embodiment of the ribbed separator 1 of the present invention. The ribbed separator 1 is processed into a bag shape so as to house the negative electrode plate 7, and ribs perpendicular to the thickness direction are formed on the base surface 2 of the outer sheet that comes into contact with the positive electrode plate (not shown). It is a flat surface that is provided and has no ribs on the base surface 2 of the inner sheet. The rib includes a horizontal rib 3a, a V-shaped rib 3b, a right diagonal rib 3c, and a left diagonal rib 3d. In the horizontal rib 3a, the positive electrode plate and the negative electrode plate 7 are alternately laminated via the ribbed separator 1, and when this is viewed in a plan view in the stacking direction, the positive electrode current collecting ear side and the negative electrode current collecting ear side face up. It is provided at the lower end in the vertical direction. The V-shaped rib 3b has a right side angle of π / 6rad to π / 3rad and a left side angle of 2π / 3rad to 5π / 6rad with respect to the horizontal rib 3a. The ratio of the heights from the apex 4 formed by the above to the right side, the end right 5R of each of the left sides, and the end left 5L is in the range of 0.95 to 1.05, and is on the base surface 2. It is provided so as to be convex downward. The right diagonal rib 3c has an intersection with the horizontal rib 3a as the starting point right 6R, and the angle formed with the horizontal rib 3a is in the range of π / 6rad to π / 3rad, and is provided so as to extend diagonally upward to the right. The right 6R of the starting point is located on the right side of the apex 4. The left diagonal rib 3d has an intersection with the horizontal rib 3a as a starting point left 6L, an angle formed with the horizontal rib 3a is in the range of 2π / 3rad to 5π / 6rad, and is provided so as to extend diagonally upward to the left. The left 6L of the starting point is located on the left side of the apex 4. A plurality of V-shaped ribs 3b, right diagonal ribs 3c, and left diagonal ribs 3d are provided on the base surface 2 respectively. The vertical spacing Dv between the respective ends of the V-shaped ribs 3b, the right diagonal ribs 3c, the left diagonal ribs 3d, and the horizontal ribs 3a adjacent to each other is provided in the range of 8 mm to 15 mm.

上記構成をとる本発明の実施形態に係るリブ付きセパレータ1を鉛蓄電池に用いることで、充電時に正極板から生じる濃度の高い硫酸をV字リブ3bの上面3tで捕捉できる。さらに水平リブ3aは右斜めリブ3c、及び左斜めリブ3dを設けることで、V字リブ3bより下方でポケットを形成し、充電時に正極板から生じる濃度の高い硫酸を、該ポケットを成すリブの上面3tで捕捉できる。したがって、充電時に正極板から生じる濃度の高い硫酸は水平リブ3a、V字リブ3b、右斜めリブ3c、及び左斜めリブ3dにより、電槽セル内底部に沈降しないよう捕捉され、電解液の成層化を抑制できる。 By using the ribbed separator 1 according to the embodiment of the present invention having the above configuration for a lead storage battery, highly concentrated sulfuric acid generated from the positive electrode plate during charging can be captured by the upper surface 3t of the V-shaped rib 3b. Further, the horizontal rib 3a is provided with a right diagonal rib 3c and a left diagonal rib 3d to form a pocket below the V-shaped rib 3b, and high-concentration sulfuric acid generated from the positive electrode plate during charging is applied to the rib forming the pocket. It can be captured on the upper surface 3t. Therefore, the high-concentration sulfuric acid generated from the positive electrode plate during charging is captured by the horizontal ribs 3a, V-shaped ribs 3b, right diagonal ribs 3c, and left diagonal ribs 3d so as not to settle on the inner bottom of the battery case cell, and the electrolytic solution is stratified. It can suppress the change.

また上記構成をとる本発明の実施形態に係るリブ付きセパレータ1を鉛蓄電池に用いることで、充電時に正極板から生じるガスは、V字リブ3b、右斜めリブ3c、及び左斜めリブ3dの下面3uに沿って上昇し、V字リブ3b、右斜めリブ3c、及び左斜めリブ3dの端部から正極板上方に抜ける。したがって、極板間でのガス滞留を防止する上で有利にはたらく。 Further, by using the ribbed separator 1 according to the embodiment of the present invention having the above configuration in the lead storage battery, the gas generated from the positive electrode plate during charging is the lower surface of the V-shaped rib 3b, the right diagonal rib 3c, and the left diagonal rib 3d. It rises along 3u and exits above the positive electrode plate from the ends of the V-shaped rib 3b, the right diagonal rib 3c, and the left diagonal rib 3d. Therefore, it is advantageous in preventing gas retention between the plates.

図1に示す実施形態において、V字リブ3bの右辺の角度は、π/3radを超えると傾斜が急であるため、V字形状が縦長の形状になり、正極板上部で生じた濃度の高い硫酸が電槽セル内底部まで沈降することを抑制する効果が小さくなる。π/6rad未満だと傾斜が緩いため、生じたガスの排気がし難い。同様に、V字リブ3bの左辺の角度は、2π/3rad未満だと傾斜が急であるため、V字形状が縦長の形状になり、正極板上部で生じた濃度の高い硫酸が電槽セル内底部まで沈降することを抑制する効果が小さくなる。5π/6radを超えると傾斜が緩いため、生じたガスの排気がし難い。したがって、前記V字リブ3bの右辺、及び左辺の夫々の角度はπ/6radからπ/3radまでの範囲、及び2π/3radから5π/6radまでの範囲で形成されることが好ましい。 In the embodiment shown in FIG. 1, since the angle of the right side of the V-shaped rib 3b has a steep inclination when it exceeds π / 3rad, the V-shaped shape becomes a vertically long shape, and the concentration generated in the upper part of the positive electrode plate is high. The effect of suppressing the sedimentation of sulfuric acid to the inner bottom of the battery case is reduced. If it is less than π / 6rad, the slope is gentle and it is difficult to exhaust the generated gas. Similarly, if the angle of the left side of the V-shaped rib 3b is less than 2π / 3rad, the inclination is steep, so that the V-shaped shape becomes a vertically long shape, and the high-concentration sulfuric acid generated in the upper part of the positive electrode plate is the battery cell. The effect of suppressing sedimentation to the inner bottom is reduced. If it exceeds 5π / 6rad, the slope is gentle, so it is difficult to exhaust the generated gas. Therefore, it is preferable that the angles of the right side and the left side of the V-shaped rib 3b are formed in the range of π / 6rad to π / 3rad and the range of 2π / 3rad to 5π / 6rad.

同様の理由から、前記右斜めリブ3c、及び前記左斜めリブ3dの前記水平リブ3aとのなす角は夫々π/6radからπ/3radまでの範囲、及び2π/3radから5π/6radまでの範囲で形成されることが好ましい。 For the same reason, the angles formed by the right diagonal rib 3c and the left diagonal rib 3d with the horizontal rib 3a are in the range of π / 6rad to π / 3rad and the range of 2π / 3rad to 5π / 6rad, respectively. It is preferably formed by.

また水平リブ3aは右斜めリブ3c、及び左斜めリブ3dを設けることで、V字リブ3bより下方でポケットを形成し、充電時に正極板から生じる濃度の高い硫酸を、該ポケットを成すリブの上面3tで捕捉でき、電解液の成層化を抑制する。 Further, the horizontal rib 3a is provided with a right diagonal rib 3c and a left diagonal rib 3d to form a pocket below the V-shaped rib 3b, and high-concentration sulfuric acid generated from the positive electrode plate during charging is applied to the rib forming the pocket. It can be captured on the upper surface 3t and suppresses the stratification of the electrolytic solution.

また、図1に示す実施形態において、V字リブ3b、右斜めリブ3c、及び左斜めリブ3dは、ベース面2上に夫々複数条設けられている。このようにリブをそれぞれ複数条設け、充電時に正極板から生じる濃度の高い硫酸を捕捉する領域を、上下方向に分散することで、濃度の高い硫酸の沈降が抑制される。上下方向に分散して捕捉された濃度の高い硫酸は、比較的少量であるため周囲の電解液に拡散し易く、電槽セル内の上部と下部の電解液比重の偏りを抑制できる。 Further, in the embodiment shown in FIG. 1, a plurality of V-shaped ribs 3b, right diagonal ribs 3c, and left diagonal ribs 3d are provided on the base surface 2 respectively. By providing a plurality of ribs in this way and dispersing the region for capturing the high-concentration sulfuric acid generated from the positive electrode plate in the vertical direction during charging, the sedimentation of the high-concentration sulfuric acid is suppressed. Since the high-concentration sulfuric acid dispersed and captured in the vertical direction is relatively small, it easily diffuses into the surrounding electrolytic solution, and it is possible to suppress the deviation of the specific gravity of the upper and lower electrolytic solutions in the battery cell.

また、図1に示す実施形態において、複数条設けられたV字リブ3bは右辺と左辺とで成す頂点4から、夫々の端部右5R、及び端部左5Lまでの高さの比が0.95から1.05までの範囲であれば、同一のリブにおいて左右の端部の高さが略同じとなるため、充電時に正極板から生じる濃度の高い硫酸が高さの低い端部側から溢れて沈降することを抑制できる。また、前記高さの比が0.95から1.05までの範囲であれば、夫々の前記頂点4が図1に示すようにベース面2上の同一直線上に位置していても良いし、同一直線上に位置せず左右に疎らに位置しても良い。 Further, in the embodiment shown in FIG. 1, the V-shaped ribs 3b provided with a plurality of strips have a height ratio of 0 from the apex 4 formed by the right side and the left side to the respective end right 5R and end left 5L. In the range of .95 to 1.05, the heights of the left and right ends of the same rib are substantially the same, so that the high-concentration sulfuric acid generated from the positive electrode plate during charging starts from the low-height end side. It is possible to prevent it from overflowing and settling. Further, as long as the height ratio is in the range of 0.95 to 1.05, the respective vertices 4 may be located on the same straight line on the base surface 2 as shown in FIG. , It may be located sparsely to the left and right instead of being located on the same straight line.

また、図1に示す実施形態において、互いに隣接するV字リブ3b、右斜めリブ3c、左斜めリブ3d、及び水平リブ3aの夫々の端部間の垂直方向の間隔Dvは、8mm未満だと間隔Dvが狭すぎて生じたガスの排気がし難い。15mmを超えると間隔Dvが広すぎて濃度の高い硫酸を捕捉する領域が広くなり、電解液の成層化を抑制する効果が小さくなる。したがって、互いに隣接するV字リブ3b、右斜めリブ3c、左斜めリブ3d、及び水平リブ3aの夫々の端部間の垂直方向の間隔Dvは、8mmから15mmまでの範囲で形成されることが好ましい。 Further, in the embodiment shown in FIG. 1, the vertical distance Dv between the ends of the V-shaped ribs 3b, the right diagonal ribs 3c, the left diagonal ribs 3d, and the horizontal ribs 3a adjacent to each other is less than 8 mm. It is difficult to exhaust the generated gas because the interval Dv is too narrow. If it exceeds 15 mm, the interval Dv is too wide and the region for capturing high-concentration sulfuric acid becomes wide, and the effect of suppressing the stratification of the electrolytic solution becomes small. Therefore, the vertical spacing Dv between the respective ends of the V-shaped ribs 3b, the right diagonal ribs 3c, the left diagonal ribs 3d, and the horizontal ribs 3a adjacent to each other may be formed in the range of 8 mm to 15 mm. preferable.

また、図1に示す実施形態において、V字リブ3bが水平リブ3aと直交する中心線8を対称軸とした線対称に設けられている。このようにV字リブ3bを線対称とすることで、同一のリブにおいて左右の端部の高さが同じになるため、充電時に正極板から生じる濃度の高い硫酸が高さの低い端部側から溢れて沈降することを防ぎ、さらにガスも左右から均等に排気できるため、極板間でのガス滞留を防止する上で有利にはたらく。 Further, in the embodiment shown in FIG. 1, the V-shaped rib 3b is provided line-symmetrically with the center line 8 orthogonal to the horizontal rib 3a as the axis of symmetry. By making the V-shaped rib 3b line-symmetrical in this way, the heights of the left and right ends of the same rib are the same, so that the high-concentration sulfuric acid generated from the positive electrode plate during charging is on the low-height end side. Since it prevents the gas from overflowing and settling, and the gas can be exhausted evenly from the left and right, it is advantageous in preventing gas from staying between the plates.

また、図1に示す実施形態において、最下段に位置するV字リブ3bの頂点4が水平リブ3aと交点9を有すように設けられている。このように最下段に位置するV字リブ3bの頂点4と水平リブ3aとが交点9で接合されることで、極板群に所定の群圧が掛かった際に、最下段に位置するV字リブ3bの頂点4が水平リブ3aを支え、水平リブ3aの折れ曲がりによるベース面2の破れ等を抑制できる。 Further, in the embodiment shown in FIG. 1, the apex 4 of the V-shaped rib 3b located at the lowermost stage is provided so as to have an intersection point 9 with the horizontal rib 3a. By joining the apex 4 of the V-shaped rib 3b located at the lowest stage and the horizontal rib 3a at the intersection 9 in this way, the V located at the lowest stage when a predetermined group pressure is applied to the electrode plate group. The apex 4 of the character rib 3b supports the horizontal rib 3a, and it is possible to suppress tearing of the base surface 2 due to bending of the horizontal rib 3a.

また、図1に示す実施形態において、右斜めリブ3cと左斜めリブ3dとが中心線8を対称軸とした線対称に設けられている。このように右斜めリブ3cと左斜めリブ3dとを線対称に設けることで、V字リブ3bを線対称に設けた場合と同様の理由により、左右のリブにおいて左右の端部の高さが同じになるため、充電時に正極板から生じる濃度の高い硫酸が高さの低い端部側から溢れて沈降することを防ぎ、さらにガスも左右から均等に排気できるため、極板間でのガス滞留を防止する上で有利にはたらく。 Further, in the embodiment shown in FIG. 1, the right diagonal rib 3c and the left diagonal rib 3d are provided in line symmetry with the center line 8 as the axis of symmetry. By providing the right diagonal rib 3c and the left diagonal rib 3d line-symmetrically in this way, the heights of the left and right ends of the left and right ribs are increased for the same reason as when the V-shaped rib 3b is provided line-symmetrically. Since it is the same, it prevents high-concentration sulfuric acid generated from the positive electrode plate from overflowing and settling from the low end side during charging, and gas can be evenly exhausted from the left and right, so gas stays between the plates. It works in an advantageous way to prevent.

本発明の実施形態に係る鉛蓄電池は、正極板と負極板7とを、上記リブ付きセパレータ1を介在させて交互に積層した極板群が、電槽セル内に挿入された鉛蓄電池である。上記リブ付きセパレータ1を鉛蓄電池に用いることで、耐久性の高い鉛蓄電池を提供できる。 The lead-acid battery according to the embodiment of the present invention is a lead-acid battery in which a group of electrode plates in which a positive electrode plate and a negative electrode plate 7 are alternately laminated with the ribbed separator 1 interposed therebetween is inserted in an electric tank cell. .. By using the ribbed separator 1 in a lead storage battery, a highly durable lead storage battery can be provided.

また、本発明の実施形態に係る鉛蓄電池は、前記極板群に掛かる群圧を5kPaから30kPaまでの範囲としたものである。前記極板群に掛かる群圧が5kPa未満では圧迫力が弱すぎて、リブと極板との間に隙間が生じ、そこから濃度の高い硫酸が流出する場合がある。また30kPaを超えると、電槽セル内に極板群が収容できない場合や収容後に電槽が膨らみ破損する場合がある。したがって、前記極板群に掛かる群圧は5kPaから30kPaまでの範囲であることが望ましい。 Further, in the lead storage battery according to the embodiment of the present invention, the group pressure applied to the electrode plate group is in the range of 5 kPa to 30 kPa. If the group pressure applied to the plate group is less than 5 kPa, the pressing force is too weak, and a gap may be formed between the rib and the plate, and high-concentration sulfuric acid may flow out from the gap. On the other hand, if it exceeds 30 kPa, the electrode plate group may not be accommodated in the battery cell, or the battery may swell and be damaged after being accommodated. Therefore, it is desirable that the group pressure applied to the electrode plate group is in the range of 5 kPa to 30 kPa.

また、図1に示す実施形態において、水平リブ3a、V字リブ3b、右斜めリブ3c、及び左斜めリブ3dはいずれも、破断することなく長手方向に連続してベース面2上に設けられている。夫々のリブの長さは、極板群を形成した際に、前記リブが当接した正極板の端よりも、前記リブの端部が外側に位置する長さにすれば、充電時に正極板から生じる濃度の高い硫酸を前記リブの上面3tで漏らさず捕捉できるため、より好ましい。 Further, in the embodiment shown in FIG. 1, the horizontal rib 3a, the V-shaped rib 3b, the right diagonal rib 3c, and the left diagonal rib 3d are all continuously provided on the base surface 2 in the longitudinal direction without breaking. ing. If the length of each rib is set so that the end of the rib is located outside the end of the positive electrode plate to which the rib abuts when the electrode plate group is formed, the positive electrode plate is charged. It is more preferable because the high-concentration sulfuric acid generated from the ribs can be captured by the upper surface 3t of the rib without leaking.

なお図示しないが、本発明の実施形態において、水平リブ、V字リブ、右斜めリブ、及び左斜めリブはいずれも短手方向の断面において、ベース面と連続した上面及び下面と、前記上面及び前記下面と連続した頂面とを備える矩形状を有するものであって、かつ該リブ付きセパレータを介して正極板と負極板とを交互に積層し極板群とした際、対向する極板の表面、又は他のリブ付きセパレータと前記頂面で当接する。また、前記リブに軟質材を用いると極板との密着性が高まり、濃度の高い硫酸はリブ上面でより良好に捕捉される。また、前記リブを中空材料とし弾性変形させて用いても良好な密着性が得られる。水平リブ、V字リブ、右斜めリブ、及び左斜めリブの断面形状は矩形状である例を示したが、矩形に限定されず、その他の多角形、円形など極板と密着する形状であれば任意である。 Although not shown, in the embodiment of the present invention, the horizontal ribs, the V-shaped ribs, the right diagonal ribs, and the left diagonal ribs all have an upper surface and a lower surface continuous with the base surface, and the upper surface and the upper surface in the cross section in the lateral direction. It has a rectangular shape having a lower surface and a continuous top surface, and when the positive electrode plate and the negative electrode plate are alternately laminated via the ribbed separator to form an electrode plate group, the electrode plates facing each other are formed. It abuts on the surface or other ribbed separators on the top surface. Further, when a soft material is used for the rib, the adhesion to the electrode plate is enhanced, and high-concentration sulfuric acid is better captured on the upper surface of the rib. Further, even if the rib is used as a hollow material and elastically deformed, good adhesion can be obtained. An example is shown in which the cross-sectional shapes of the horizontal rib, the V-shaped rib, the right diagonal rib, and the left diagonal rib are rectangular, but the cross-sectional shape is not limited to the rectangular shape, and any other polygonal shape, circular shape, or any other shape that is in close contact with the electrode plate may be used. Is optional.

図2は、本発明のリブ付きセパレータ1を袋状にして、負極板7を収容する工程を示す説明図である。本発明のリブ付きセパレータ1は、図2(A)に示すように、一定の寸法に切断し長方形のシート状に展開したリブ付きシート状セパレータ10を、図2(B)に示す通り負極板7を包むようにその中央線10eに沿って二つ折りにし、負極板7の下端をこの中央線10eに合わせて、図2(C)に示すように一方の側面10aと他方の側面10bとを重ね合わせ、その重ね合わせた一方の側面10aと他方の側面10bとの両側部同士を自動接合機器、本発明では2つの歯車間を通過させて接合するギヤシール方法で接合して図2(D)に示すように袋状に加工している。 FIG. 2 is an explanatory diagram showing a step of forming the ribbed separator 1 of the present invention into a bag shape and accommodating the negative electrode plate 7. As shown in FIG. 2A, the ribbed separator 1 of the present invention is a ribbed sheet-shaped separator 10 cut to a certain size and developed into a rectangular sheet shape, as shown in FIG. 2B, as a negative electrode plate. Fold it in half along the center line 10e so as to wrap around 7, align the lower end of the negative electrode plate 7 with the center line 10e, and overlap one side surface 10a and the other side surface 10b as shown in FIG. 2C. In FIG. 2 (D), both side portions of one side surface 10a and the other side surface 10b that are overlapped with each other are joined by an automatic joining device, and in the present invention, a gear sealing method in which two gears are passed and joined. It is processed into a bag shape as shown.

本実施形態では、負極板7を収納するようにリブ付きセパレータ1を袋状に加工し、正極板と当接するように外側となるシートのベース面2上には厚さ方向に垂直なリブを設け、内側となるシートのベース面2上にはリブを設けないフラットな面であるリブ付きセパレータ1に負極板7を収容し、正極板と交互に積層し極板群とすることを例示したが、リブ付きセパレータ1を袋状に加工せず、リブ付きシート状セパレータ10を中央線10eで切断して得られる2枚の半リブ付きシート状セパレータを、夫々リブを設けた面で正極板を挟むように当接させ、また夫々フラットな面で負極板を挟むように当接させて交互に積層し極板群としても構わないし、前記半リブ付きシート状セパレータの表裏ベース面2上にリブを設け、正極板、及び負極板にリブが当接するようにしたリブ付きセパレータを介して正極板と負極板とを交互に積層し極板群としても構わない。 In the present embodiment, the ribbed separator 1 is processed into a bag shape so as to house the negative electrode plate 7, and ribs perpendicular to the thickness direction are formed on the base surface 2 of the outer sheet so as to abut the positive electrode plate. It is exemplified that the negative electrode plate 7 is housed in a ribbed separator 1 which is a flat surface without ribs on the base surface 2 of the inner sheet, and is alternately laminated with the positive electrode plates to form a group of electrode plates. However, the ribbed separator 1 is not processed into a bag shape, and the two semi-ribbed sheet-shaped separators obtained by cutting the ribbed sheet-shaped separator 10 along the center line 10e are formed on the positive electrode plate on the surface provided with the ribs, respectively. The negative electrode plates may be brought into contact with each other so as to sandwich them, or the negative electrode plates may be alternately laminated so as to sandwich the negative electrode plates on the front and back base surfaces 2 of the sheet-shaped separator with half ribs. The positive electrode plate and the negative electrode plate may be alternately laminated via a ribbed separator in which ribs are provided so that the ribs abut on the positive electrode plate and the negative electrode plate to form a group of electrode plates.

以下に、本発明を実施例により具体的に説明する。但し、本発明は下記の実施例のみに限定されるものではない。 Hereinafter, the present invention will be specifically described with reference to Examples. However, the present invention is not limited to the following examples.

(実施例1)
本発明のリブ付きセパレータ1を下記の方法により製造した。まず、高密度ポリエチレン樹脂粉末と無機粉末(平均粒径5μmのシリカ粉末)と鉱物オイル(パラフィン系オイル)とをミキサーで混合し、該混合物を二軸押出機にてシート状に押し出し、一方のロールに図3に示したリブ配置パターンの溝を刻設した成形ロール間を通過させて加圧成形し、前記複数条のリブを設けたベース面の厚み0.3mmの肉薄シートを得た。その後、溶剤に浸漬して鉱物オイルの一部を除去してリブ付きシート状セパレータを得た。
(Example 1)
The ribbed separator 1 of the present invention was manufactured by the following method. First, high-density polyethylene resin powder, inorganic powder (silica powder with an average particle size of 5 μm) and mineral oil (paraffin oil) are mixed with a mixer, and the mixture is extruded into a sheet by a twin-screw extruder. A thin sheet having a thickness of 0.3 mm on the base surface provided with the plurality of ribs was obtained by passing through the molding rolls in which the grooves of the rib arrangement pattern shown in FIG. 3 were engraved on the rolls and performing pressure molding. Then, it was immersed in a solvent to remove a part of the mineral oil to obtain a ribbed sheet separator.

一定の寸法に切断し長方形のシート状に展開したリブ付きシート状セパレータ10を、図2に示すようにリブが形成された面を外側に向け、負極板7を包むように中央線10eに沿って二つ折りにした後、一方の側面10aと他方の側面10bとを重ね合わせ、その重ね合わせた一方の側面10aと他方の側面10bとを両側部10c、10d同士をギヤシール方法で接合して袋状に加工し、袋状のリブ付きセパレータ1を得た。この工程において、必要に応じて前記リブ付きシート状セパレータ10の左右の端にリブのない領域を設け、ギヤシール方法を施すための綴じ代としても良い。 The ribbed sheet separator 10 cut to a certain size and developed into a rectangular sheet is oriented along the center line 10e so as to wrap the negative electrode plate 7 with the surface on which the ribs are formed facing outward as shown in FIG. After folding in half, one side surface 10a and the other side surface 10b are overlapped, and the overlapped one side surface 10a and the other side surface 10b are joined to each other by a gear seal method to form a bag. A bag-shaped ribbed separator 1 was obtained. In this step, if necessary, ribless regions may be provided at the left and right ends of the ribbed sheet-shaped separator 10 as a binding allowance for applying the gear sealing method.

図1に示すリブ配置パターンにおいて、水平リブ3a、V字リブ3b、右斜めリブ3c、及び左斜めリブ3dの断面形状は、いずれも幅0.4mm、高さ0.5mmの矩形とした。V字リブ3bは右辺の角度をπ/4rad、左辺の角度を3π/4radの範囲とし、前記右辺と前記左辺とで成す頂点4から、夫々の端部右5R、及び端部左5Lまでの高さの比を1.00とする中心線8を対称軸とした線対称とし、最下段に位置するV字リブ3bの頂点4と水平リブ3aとを交点9で接合した。互いに隣接するV字リブ3b、右斜めリブ3c、左斜めリブ3d、及び水平リブ3aの夫々の端部間の垂直方向の間隔Dvは10mmとした。また、互いに隣接するV字リブ3bの水平方向の間隔Dhは10mmとした。また、右斜めリブ3c、及び左斜めリブ3dは水平リブ3aとのなす角を夫々π/4rad、及び3π/4radの範囲とする中心線8を対称軸とした線対称とした。 In the rib arrangement pattern shown in FIG. 1, the cross-sectional shapes of the horizontal rib 3a, the V-shaped rib 3b, the right diagonal rib 3c, and the left diagonal rib 3d are all rectangular with a width of 0.4 mm and a height of 0.5 mm. The V-shaped rib 3b has an angle of the right side in the range of π / 4rad and an angle of the left side in the range of 3π / 4rad. The center line 8 having a height ratio of 1.00 was set as the axis of symmetry, and the apex 4 of the V-shaped rib 3b located at the lowest stage and the horizontal rib 3a were joined at an intersection point 9. The vertical distance Dv between the ends of the V-shaped ribs 3b, the right diagonal ribs 3c, the left diagonal ribs 3d, and the horizontal ribs 3a adjacent to each other was set to 10 mm. Further, the horizontal spacing Dh of the V-shaped ribs 3b adjacent to each other was set to 10 mm. Further, the right diagonal rib 3c and the left diagonal rib 3d have line symmetry with the center line 8 having an angle formed by the horizontal rib 3a in the range of π / 4rad and 3π / 4rad, respectively.

上記袋状のリブ付きセパレータ1を用いた鉛蓄電池を以下の手順によって製造した。公知の方法により製造した未化成の正極充填板と負極充填板とを、上記袋状のリブ付きセパレータ1に負極充填板を収納した状態で、正極充填板と交互に積層して極板群を組み立て、これを電槽セル内に極板群に掛かる群圧を20kPaで収容し、そこに比重1.280、液温20℃の電解液を注入して常法に従って電槽化成をし、5時間率容量で50AhのD23型の実施例1の液式鉛蓄電池を製造した。 A lead-acid battery using the bag-shaped ribbed separator 1 was manufactured by the following procedure. An unchemical positive electrode filling plate and a negative electrode filling plate manufactured by a known method are alternately laminated with a positive electrode filling plate in a state where the negative electrode filling plate is housed in the bag-shaped ribbed separator 1 to form a group of electrode plates. After assembling, the group pressure applied to the electrode plate group is accommodated in the battery cell at 20 kPa, and an electrolytic solution having a specific gravity of 1.280 and a liquid temperature of 20 ° C. is injected into the battery to form a battery according to a conventional method. A D23 type liquid lead-acid battery of Example 1 having an hourly rate capacity of 50 Ah was manufactured.

(比較例1)
前記混合物を図4に示すように、垂直方向に向けて設けられた縦リブ11の端部間の水平方向の間隔Dhが10mmであって、複数条の縦リブ11のみで構成されたリブ配置パターンに、刻設された成形ロール間を通過させて加圧成形したこと以外は、実施例1と同じ方法により袋状のリブ付きセパレータ1を作製し、比較例1の液式鉛蓄電池を製造した。
(Comparative Example 1)
As shown in FIG. 4, a rib arrangement in which the horizontal distance Dh between the ends of the vertical ribs 11 provided in the vertical direction is 10 mm and the mixture is composed of only a plurality of vertical ribs 11. A bag-shaped ribbed separator 1 was produced by the same method as in Example 1 except that the pattern was pressure-molded by passing between the engraved molding rolls, and the liquid lead-acid battery of Comparative Example 1 was manufactured. did.

(比較例2)
前記混合物を図5に示すように、V字リブ3bの端部間の垂直方向の間隔Dvが実施例1と同様の10mmであって、V字リブ3bの右辺の角度がπ/36radで、左辺の角度が35π/36radの範囲とする、中心線8を対称軸とした線対称である複数条のV字リブ3bのみで構成されたリブ配置パターンに、刻設された成形ロール間を通過させて加圧成形したこと以外は、実施例1と同じ方法により袋状のリブ付きセパレータ1を作製し、比較例2の液式鉛蓄電池を製造した。
(Comparative Example 2)
As shown in FIG. 5, the vertical distance Dv between the ends of the V-shaped ribs 3b is 10 mm, which is the same as in Example 1, and the angle of the right side of the V-shaped ribs 3b is π / 36rad. Passing between the forming rolls engraved in a rib arrangement pattern composed of only a plurality of V-shaped ribs 3b that are axisymmetric with the center line 8 as the axis of symmetry, with the angle of the left side in the range of 35π / 36rad. A bag-shaped ribbed separator 1 was produced by the same method as in Example 1 except that the liquid lead-acid battery of Comparative Example 2 was produced.

上記の実施例1、比較例1、及び比較例2の液式鉛蓄電池について、以下の手順に従って充放電試験を繰り返し実施して、成層化の有無を確認した。満充電状態から、0.2C相当の電流量で5時間率容量の50%を放電し、その後0.1C相当の電流量で放電電気量の105%分を充電するサイクルを3回繰り返した後、室温で16時間以上静置し、比重計によって電槽の各セル内の上部と下部の電解液比重を測定し、係る電解液の上下比重差から成層化を評価した。このとき、上下比重差が0.005以上を成層化が起きたと判断した。また、試験中に電槽セル内の極板群から電解液中に抜け出るガスの様子を観察し、ガス抜け性を評価した。このとき、セパレータのベース面上に垂直方向に向けて縦リブを設けた比較例1のガス抜け性を100%とし、実施例1、及び比較例2のガス抜け性を評価した。 The charge / discharge tests of the liquid lead-acid batteries of Example 1, Comparative Example 1 and Comparative Example 2 were repeatedly carried out according to the following procedure to confirm the presence or absence of stratification. After repeating the cycle of discharging 50% of the 5-hour rate capacity with a current amount equivalent to 0.2C from a fully charged state and then charging 105% of the discharged electricity amount with a current amount equivalent to 0.1C three times. The cells were allowed to stand at room temperature for 16 hours or more, the specific densities of the upper and lower electrolytic solutions in each cell of the electric tank were measured, and stratification was evaluated from the difference in the upper and lower specific densities of the electrolytic solutions. At this time, it was judged that stratification occurred when the difference in the vertical density was 0.005 or more. In addition, during the test, the state of the gas that escaped from the electrode plate group in the battery case cell into the electrolytic solution was observed, and the gas release property was evaluated. At this time, the gas release property of Comparative Example 1 in which the vertical ribs were provided on the base surface of the separator in the vertical direction was set to 100%, and the gas release properties of Example 1 and Comparative Example 2 were evaluated.

(実施例、比較例の結果)
実施例1、比較例1、及び比較例2について、上記試験後の電解液の上下比重の測定結果とガス抜け性の評価結果を表1に示した。なお、上部電解液比重、及び下部電解液比重については、全6セルの平均値を示した。
(Results of Examples and Comparative Examples)
For Example 1, Comparative Example 1, and Comparative Example 2, Table 1 shows the measurement results of the vertical specific gravity of the electrolytic solution after the above test and the evaluation results of the gas release property. The average values of all 6 cells are shown for the upper electrolyte specific density and the lower electrolyte specific density.

Figure 0007010772000001
Figure 0007010772000001

表1から明らかなように、実施例1の鉛蓄電池は試験後の電解液の上下比重差が0.002であり、成層化が抑制された。これは、第一の理由として、充電時に正極板から生じた濃度の高い硫酸が、セパレータのベース面上に設けられた水平リブ、V字リブ、右斜めリブ、及び左斜めリブの上面に捕捉されて電槽セル内底部への沈降が防止されたことによると考えられる。第二の理由として、前記V字リブの右辺、及び左辺の角度の範囲、前記右斜めリブと前記左斜めリブの前記水平リブとのなす角の範囲、及び互いに隣接する前記V字リブ、前記右斜めリブ、前記左斜めリブ、及び前記水平リブの夫々の端部間の垂直方向の間隔を夫々好適な範囲とすることで、充電末期に生じるガスが前記V字リブ、前記右斜めリブ、及び前記左斜めリブの下面に沿って上昇し、リブの端部から正極板上方にガス抜けが生じたことで、極板間のガスの滞留が防止されると共に電解液の攪拌も良好に行われたことによると推定される。 As is clear from Table 1, in the lead-acid battery of Example 1, the difference in the vertical specific gravity of the electrolytic solution after the test was 0.002, and stratification was suppressed. The first reason for this is that the high-concentration sulfuric acid generated from the positive electrode plate during charging is captured by the upper surfaces of the horizontal ribs, V-shaped ribs, right diagonal ribs, and left diagonal ribs provided on the base surface of the separator. It is probable that this prevented the sedimentation to the inner bottom of the battery case. The second reason is the range of angles of the right side and the left side of the V-shaped rib, the range of the angle formed by the right diagonal rib and the horizontal rib of the left diagonal rib, and the V-shaped ribs adjacent to each other. By setting the vertical spacing between the ends of the right diagonal rib, the left diagonal rib, and the horizontal rib to a suitable range, the gas generated at the end of charging is the V-shaped rib, the right diagonal rib, and the right diagonal rib. And, as it rises along the lower surface of the left diagonal rib and gas escapes from the end of the rib above the positive electrode plate, gas retention between the plates is prevented and the electrolytic solution is well agitated. It is presumed that it was done.

比較例1は、セパレータのベース面上に垂直方向に向けて縦リブが設けられているため、充電時に正極板から生じる濃度の高い硫酸が、前記縦リブの隙間を通って多量に沈降するため、充電末期に発生するガスの抜け性が良好でも、電解液の攪拌が不十分となり成層化が起き、上下比重差が生じたものと推定される。 In Comparative Example 1, since the vertical ribs are provided on the base surface of the separator in the vertical direction, a large amount of highly concentrated sulfuric acid generated from the positive electrode plate during charging settles through the gaps between the vertical ribs. It is presumed that even if the gas generated at the end of charging is well released, the electrolytic solution is not sufficiently stirred and stratification occurs, resulting in a difference in the vertical specific gravity.

一方比較例2は、緩やかに傾斜したV字リブが設けられているため、充電時に正極板から生じる濃度の高い硫酸を前記V字リブの上面で捕捉し、電槽セル内底部への沈降を抑制するが、生じたガスの排気がし難く、電解液の攪拌がままならない。また、水平リブが設けられていないため、充電時に正極板の下部から生じた濃度の高い硫酸はセパレータのベース面下部で捕捉されず電槽セル内底部に沈降するため、多少の成層化が起き、上下比重差が生じたものと推定される。 On the other hand, in Comparative Example 2, since the gently inclined V-shaped rib is provided, highly concentrated sulfuric acid generated from the positive electrode plate during charging is captured by the upper surface of the V-shaped rib and settles to the inner bottom of the battery case cell. Although it is suppressed, it is difficult to exhaust the generated gas, and the electrolytic solution cannot be agitated. In addition, since the horizontal ribs are not provided, the high-concentration sulfuric acid generated from the lower part of the positive electrode plate during charging is not captured at the lower part of the base surface of the separator and settles at the inner bottom part of the battery case, so that some stratification occurs. , It is presumed that there was a difference in the vertical specific gravity.

以上のように本発明のリブ付きセパレータは、充電時に正極板から生じる濃度の高い硫酸をV字リブ、右斜めリブ、及び左斜めリブの上面で捕捉できる。さらに水平リブは前記右斜めリブ、及び前記左斜めリブを設けることで、前記V字リブより下方でポケットを形成し、充電時に正極板から生じる濃度の高い硫酸を、該ポケットを成すリブの上面で捕捉できる。したがって、充電時に正極板から生じる濃度の高い硫酸は、前記水平リブ、前記V字リブ、前記右斜めリブ、及び前記左斜めリブにより電槽セル内底部に沈降しないよう捕捉され、電解液の成層化を抑制できる。 As described above, the ribbed separator of the present invention can capture high-concentration sulfuric acid generated from the positive electrode plate during charging on the upper surfaces of the V-shaped rib, the right diagonal rib, and the left diagonal rib. Further, the horizontal rib is provided with the right diagonal rib and the left diagonal rib to form a pocket below the V-shaped rib, and high-concentration sulfuric acid generated from the positive electrode plate during charging is applied to the upper surface of the rib forming the pocket. Can be captured with. Therefore, the high-concentration sulfuric acid generated from the positive electrode plate during charging is captured by the horizontal ribs, the V-shaped ribs, the right diagonal ribs, and the left diagonal ribs so as not to settle on the inner bottom of the battery case, and the electrolytic solution is stratified. It can suppress the change.

また、V字リブの右辺、及び左辺の夫々の角度はπ/6radからπ/3radまでの範囲、及び2π/3radから5π/6radまでの範囲、右斜めリブ、及び左斜めリブの水平リブとのなす角は夫々π/6radからπ/3radまでの範囲、及び2π/3radから5π/6radまでの範囲、互いに隣接する前記V字リブ、前記右斜めリブ、前記左斜めリブ、及び前記水平リブの夫々の端部間の垂直方向の間隔は、8mmから15mmまでの範囲で形成されるため、充放電時に生じるガスは前記V字リブ、前記右斜めリブ、及び前記左斜めリブの下面に沿って上昇し、リブの端部から正極板上方に抜け、極板間でのガス滞留を防止する上で有利にはたらく。 The angles of the right side and the left side of the V-shaped rib are in the range of π / 6rad to π / 3rad, the range of 2π / 3rad to 5π / 6rad, the right diagonal rib, and the horizontal rib of the left diagonal rib. The angles formed by each are in the range of π / 6rad to π / 3rad and 2π / 3rad to 5π / 6rad, the V-shaped ribs adjacent to each other, the right diagonal ribs, the left diagonal ribs, and the horizontal ribs. Since the vertical spacing between the respective ends is formed in the range of 8 mm to 15 mm, the gas generated during charging and discharging is along the lower surface of the V-shaped rib, the right diagonal rib, and the left diagonal rib. It rises and escapes from the end of the rib to the upper part of the positive electrode plate, which is advantageous in preventing gas retention between the electrode plates.

また正極板と負極板とを、本発明のリブ付きセパレータを介在させて交互に積層した極板群に掛かる群圧を、5kPaから30kPaまでの範囲にすることで、リブと極板との間に隙間が生じ難く、濃度の高い硫酸は前記リブ上面に良好に捕捉される。また、電槽セル内に前記極板群を破損させることなく収容できる。 Further, by setting the group pressure applied to the electrode plate group in which the positive electrode plate and the negative electrode plate are alternately laminated with the ribbed separator of the present invention interposed therebetween in the range of 5 kPa to 30 kPa, the space between the rib and the electrode plate is set. Sulfuric acid with a high concentration is well trapped on the upper surface of the rib. Further, the electrode plates can be housed in the battery cell without damaging the electrode plates.

以上の通り本発明によれば、充電時に極板から生じる濃度の高い硫酸の沈降防止と、極板間のガスの滞留防止とを両立し、成層化を抑制し得る鉛蓄電池用リブ付きセパレータ、及びそのセパレータを用いた耐久性の高い鉛蓄電池を提供することができる。 As described above, according to the present invention, a ribbed separator for a lead storage battery capable of suppressing stratification by both preventing sedimentation of high-concentration sulfuric acid generated from the plates during charging and preventing gas from staying between the plates. And a lead storage battery having high durability using the separator thereof can be provided.

1 リブ付きセパレータ
2 ベース面
3a 水平リブ
3b V字リブ
3c 右斜めリブ
3d 左斜めリブ
3t 上面
3u 下面
4 頂点
5R 端部右
5L 端部左
6R 始点右
6L 始点左
7 極板
8 中心線
9 交点
10 リブ付きシート状セパレータ
10a,10b 側面
10c,10d 両側部
10e 中央線
11 縦リブ
1 Separator with ribs 2 Base surface 3a Horizontal ribs 3b V-shaped ribs 3c Right diagonal ribs 3d Left diagonal ribs 3t Top surface 3u Bottom surface 4 Vertices 5R End part right 5L End part left 6R Start point right 6L Start point left 7 pole plate 8 Center line 9 Intersection 10 Sheet-shaped separator with ribs 10a, 10b Side surfaces 10c, 10d Both sides 10e Center line 11 Vertical ribs

Claims (6)

シートのベース面上に厚さ方向に垂直なリブを設けたリブ付きセパレータにおいて、
前記リブは水平リブと、V字リブと、右斜めリブと、左斜めリブとを含み、
前記水平リブは前記リブ付きセパレータを平面視したとき、上下方向の下端に設けられており、
前記V字リブは前記水平リブに対して右辺の角度がπ/6radからπ/3radまでの範囲、かつ左辺の角度が2π/3radから5π/6radまでの範囲であって、前記右辺と前記左辺とで成す頂点から前記右辺と前記左辺の夫々の端部までの高さの比が0.95から1.05までの範囲であって、前記ベース面上に下に凸となるように設けられており、
前記右斜めリブは前記水平リブとの交点を始点とし、前記水平リブとのなす角がπ/6radからπ/3radまでの範囲であって、右斜め上方向に延伸して設けられており、該始点は前記頂点よりも右側に位置するものであり、
前記左斜めリブは前記水平リブとの交点を始点とし、前記水平リブとのなす角が2π/3radから5π/6radまでの範囲であって、左斜め上方向に延伸して設けられており、該始点は前記頂点よりも左側に位置するものであり、
前記V字リブ、前記右斜めリブ、及び前記左斜めリブは前記ベース面上に夫々複数条設けられ、互いに隣接する前記V字リブ、前記右斜めリブ、前記左斜めリブ、及び前記水平リブの夫々の端部間の垂直方向の間隔は、8mmから15mmまでの範囲で設けられていることを特徴とする鉛蓄電池用リブ付きセパレータ。
In a ribbed separator having ribs perpendicular to the thickness direction on the base surface of the sheet.
The ribs include horizontal ribs, V-shaped ribs, diagonal right ribs, and diagonal left ribs.
The horizontal rib is provided at the lower end in the vertical direction when the ribbed separator is viewed in a plan view.
The V-shaped rib has an angle of the right side from π / 6rad to π / 3rad and an angle of the left side of 2π / 3rad to 5π / 6rad with respect to the horizontal rib, and the right side and the left side. The ratio of the heights from the apex formed by the above to the ends of the right side and the left side is in the range of 0.95 to 1.05, and is provided so as to be convex downward on the base surface. And
The right diagonal rib starts at an intersection with the horizontal rib, and the angle formed by the horizontal rib ranges from π / 6 rad to π / 3 rad, and is provided so as to extend diagonally upward to the right. The starting point is located on the right side of the apex.
The left diagonal rib starts at an intersection with the horizontal rib and has an angle formed by the horizontal rib in the range of 2π / 3rad to 5π / 6rad, and is provided so as to extend diagonally upward to the left. The starting point is located on the left side of the apex.
A plurality of the V-shaped ribs, the right diagonal ribs, and the left diagonal ribs are provided on the base surface, respectively, and of the V-shaped ribs, the right diagonal ribs, the left diagonal ribs, and the horizontal ribs adjacent to each other. A ribbed separator for a lead-acid battery, characterized in that the vertical spacing between the ends is in the range of 8 mm to 15 mm.
前記V字リブが前記水平リブと直交する中心線を対称軸とした線対称に設けられていることを特徴とする請求項1に記載の鉛蓄電池用リブ付きセパレータ。 The separator with a rib for a lead storage battery according to claim 1, wherein the V-shaped rib is provided in line symmetry with a center line orthogonal to the horizontal rib as an axis of symmetry. 複数条設けられた前記V字リブの内、最下段に位置するV字リブの頂点が前記水平リブと交点を有するように設けられていることを特徴とする請求項1又は2のいずれか一項に記載の鉛蓄電池用リブ付きセパレータ。 One of claims 1 or 2, wherein the apex of the V-shaped rib located at the bottom of the plurality of V-shaped ribs is provided so as to have an intersection with the horizontal rib. Ribbed separator for lead-acid batteries as described in section. 前記右斜めリブと前記左斜めリブとが前記中心線を対称軸とした線対称となるように設けられていることを特徴とする請求項1乃至3のいずれか一項に記載の鉛蓄電池用リブ付きセパレータ。 The lead-acid battery according to any one of claims 1 to 3, wherein the right diagonal rib and the left diagonal rib are provided so as to have line symmetry with the center line as an axis of symmetry. Ribbed separator. 請求項1乃至4のいずれか一項に記載の鉛蓄電池用リブ付きセパレータが用いられていることを特徴とする鉛蓄電池。 A lead-acid battery according to any one of claims 1 to 4, wherein the ribbed separator for the lead-acid battery is used. 請求項5に記載の鉛蓄電池であって、極板群に掛かる群圧が5kPaから30kPaまでの範囲であることを特徴とする鉛蓄電池。 The lead-acid battery according to claim 5, wherein the group pressure applied to the electrode plate group is in the range of 5 kPa to 30 kPa.
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