JP2002117824A - Manufacturing method of separator for lead-acid battery - Google Patents

Manufacturing method of separator for lead-acid battery

Info

Publication number
JP2002117824A
JP2002117824A JP2000310717A JP2000310717A JP2002117824A JP 2002117824 A JP2002117824 A JP 2002117824A JP 2000310717 A JP2000310717 A JP 2000310717A JP 2000310717 A JP2000310717 A JP 2000310717A JP 2002117824 A JP2002117824 A JP 2002117824A
Authority
JP
Japan
Prior art keywords
mineral oil
separator
raw material
kneading
material mixture
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
JP2000310717A
Other languages
Japanese (ja)
Inventor
Takashi Hirashima
敬 平島
Tadamasa Wada
忠正 和田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Muki Co Ltd
Original Assignee
Nippon Muki Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Muki Co Ltd filed Critical Nippon Muki Co Ltd
Priority to JP2000310717A priority Critical patent/JP2002117824A/en
Publication of JP2002117824A publication Critical patent/JP2002117824A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

PROBLEM TO BE SOLVED: To provide a manufacturing method of a separator for a lead-acid battery fully satisfying a separator characteristic and a battery characteristic without reducing productivity and product quality even if inorganic powder to absorb a small amount of oil is used. SOLUTION: In the manufacturing method of the separator for the lead-acid battery wherein after a raw material mixture having three kinds of polyolefinic resin, inorganic powders and mineral oil has been molded as the main raw materials mixture in a sheet-form while kneading in a heating fusion, subsequently a part or all of the mineral oil is removed from the sheet, and the mineral oil is blended at divided times of a preparing time of the raw material mixture before the kneading in the heating fusion and of a kneading time in the heating fusion.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ポリオレフィン系
樹脂を構成主体とする鉛蓄電池用セパレータであって、
ポリオレフィン系樹脂を主原料として加熱溶融混練によ
ってシート化する方法で製造される鉛蓄電池用セパレー
タの製造方法に関するものである。
TECHNICAL FIELD The present invention relates to a separator for a lead-acid battery mainly comprising a polyolefin resin,
The present invention relates to a method for manufacturing a separator for a lead-acid battery manufactured by a method of forming a sheet by heat-melt kneading using a polyolefin-based resin as a main raw material.

【0002】[0002]

【従来の技術】従来、ポリオレフィン系樹脂を構成主体
とした鉛蓄電池用セパレータを製造する一般的な方法と
しては、まず、主原料であるポリオレフィン系樹脂、無
機粉体及び鉱物オイルの3者をミキサを使用して混合
し、原料混合物を作製する。この場合、先にポリオレフ
ィン系樹脂と無機粉体を混合しておき、後から鉱物オイ
ルを投入し、各原料が均一に分散され、原料混合物の外
観状態が顆粒状となるまで混合を行うのが一般的であ
る。次に、得られた原料混合物を温度制御された押出成
形機へ連続投入し、加熱溶融混練により溶融樹脂の状態
にして、Tダイからシート状に押し出す。続いて、2本
の成形ロールにより加圧して、所定の厚さのシートに成
形する。この場合、成形ロールには、通常、その一方又
は双方に所定の形状を有した溝が彫刻してあり、シート
に様々な形状のリブを連続および/または不連続に形成
することができる。また、押出成形機としては、通常、
生産性の観点から、二軸同方向回転のスクリュウを備え
たシリンダ部を有するものが使用される。次に、得られ
た押出成形シートを適当な有機溶剤中に一定時間浸漬し
て、含有する鉱物オイルの一部を抽出除去した後、加熱
乾燥することによって、鉛蓄電池用セパレータが得られ
る。
2. Description of the Related Art Conventionally, as a general method for producing a lead storage battery separator mainly composed of a polyolefin resin, first, a polyolefin resin, which is a main raw material, an inorganic powder and a mineral oil are mixed with a mixer. To make a raw material mixture. In this case, the polyolefin resin and the inorganic powder are mixed in advance, and mineral oil is added later, and the raw materials are uniformly dispersed and mixed until the appearance of the raw material mixture becomes granular. General. Next, the obtained raw material mixture is continuously charged into a temperature-controlled extruder, brought into a molten resin state by heat-melt kneading, and extruded from a T-die into a sheet. Subsequently, pressure is applied by two forming rolls to form a sheet having a predetermined thickness. In this case, usually, a groove having a predetermined shape is engraved on one or both of the forming rolls, and ribs having various shapes can be continuously and / or discontinuously formed on the sheet. Also, as an extruder, usually
From the viewpoint of productivity, one having a cylinder portion provided with a screw that rotates biaxially in the same direction is used. Next, the obtained extruded sheet is immersed in an appropriate organic solvent for a certain period of time to extract and remove a part of the contained mineral oil, and then dried by heating to obtain a lead-acid battery separator.

【0003】[0003]

【発明が解決しようとする課題】上記従来の鉛蓄電池用
セパレータの製造方法において、原料混合物を構成する
3つの主原料は、それぞれ次のような機能を有してい
る。ポリオレフィン系樹脂は、セパレータとしての形状
を形作る役割を有しているほか、セパレータの機械的強
度や電池寿命に大きく関わる耐酸化特性を確保するため
の役割を担っている。無機粉体は、原料混合物の段階に
おいては鉱物オイルが遊離しないよう原料混合物内に保
持する役割を有しているほか、押出成形シートから鉱物
オイルを除去して微孔を形成させる際には、鉱物オイル
が抽出されることによって起こるシートの収縮を抑制
し、微孔の確保を手助けする役割を担っている。鉱物オ
イルは、原料混合物の押出成形時の可塑剤として、また
有機溶剤により抽出されることによる微孔形成剤とし
て、更にはセパレータ中に5〜30質量%残留せしめて
耐酸化性付与剤として機能する。したがって、これら3
つの主原料の原料混合物中における配合割合は、お互い
の様々な条件が複雑に重なり合った結果として導き出さ
れているものであり、微妙なバランスの上に成り立って
いるものであると言える。したがって、一旦確立された
この配合割合を変動させることは、鉛蓄電池用セパレー
タとしての品質やセパレータの生産性に影響を与えてし
まうことになりかねないため、困難である上リスクが伴
う。特に、無機粉体と鉱物オイルとの配合割合は重要
で、両者の割合において、鉱物オイルの割合が少ない
と、セパレータの空間率が低下し、セパレータの電気抵
抗が高くなり、その結果、電池特性を低下させてしま
う。また、鉱物オイルの割合が少ないと、可塑剤として
の効果が低くなり、押出成形機への負荷が増大し、生産
性を著しく低下させてしまう。一方、鉱物オイルの割合
が多いと、無機粉体が鉱物オイルを吸収、保持する能力
(吸油量)の限界を越えるため、原料混合物とした時に
無機粉体は鉱物オイルの全量を吸収、保持し切れず、鉱
物オイルの一部が遊離して原料混合物が良好な顆粒状で
はなく塊状(団子状)になってしまう。このような場合
には、次工程において押出成形機へ原料混合物を投入す
る際、定量ずつ安定して投入することができなくなるた
め、製品品質にも影響を与えかねない。この現象には、
無機粉体の吸油量と鉱物オイルの配合割合(配合量)と
の関係(バランス)が影響しているため、上記の例のよ
うに、無機粉体の吸油量が同じ場合には、鉱物オイルの
配合割合が多くなり過ぎた場合に起こり得るほか、鉱物
オイルの配合割合が同じ場合であっても、無機粉体の吸
油量が小さくなれば同様の現象が起こり得る。上記した
ように、鉱物オイルの割合が少ないと種々の問題が生じ
るので、鉱物オイルはある所定の配合割合にて配合する
必要がある。一般に、吸油量の大きい無機粉体ほど高価
であるため、吸油量のより小さい無機粉体を使用する方
がコスト面では有利である。しかしながら、上記したよ
うに、吸油量の小さい無機粉体を使用すると、原料混合
物が塊状となる不都合があることから、従来では、吸油
量の小さい無機粉体を使用することは避けられ、高価な
吸油量の大きい無機粉体が使用されてきた。本発明は、
以上のような問題点に鑑み、吸油量の小さい無機粉体を
使用した場合であっても、生産性や製品品質を低下させ
ることがなく、セパレータ特性や電池特性を十分に満足
する鉛蓄電池用セパレータの製造方法を提供することを
目的とする。
In the above-mentioned conventional method for manufacturing a lead-acid battery separator, the three main raw materials constituting the raw material mixture have the following functions. The polyolefin-based resin has a role of shaping the shape as a separator, and also has a role of securing the mechanical strength of the separator and the oxidation resistance which is greatly related to the battery life. Inorganic powder has the role of retaining the mineral oil in the raw material mixture at the stage of the raw material mixture so as not to be released, and when removing the mineral oil from the extruded sheet to form micropores, It suppresses the shrinkage of the sheet caused by the extraction of the mineral oil, and plays a role in helping to secure micropores. Mineral oil functions as a plasticizer at the time of extrusion molding of the raw material mixture, as a pore forming agent by being extracted with an organic solvent, and as an oxidation resistance imparting agent by remaining in a separator in an amount of 5 to 30% by mass. I do. Therefore, these three
The mixing ratio of the two main raw materials in the raw material mixture is derived as a result of complicatedly overlapping various conditions, and can be said to be based on a delicate balance. Therefore, changing the once-established mixing ratio may affect the quality as a lead storage battery separator and the productivity of the separator, which is difficult and involves risks. In particular, the mixing ratio of the inorganic powder and the mineral oil is important. In both the ratios, if the ratio of the mineral oil is small, the porosity of the separator decreases, and the electrical resistance of the separator increases. Is reduced. On the other hand, when the proportion of the mineral oil is small, the effect as a plasticizer is reduced, the load on the extruder is increased, and the productivity is significantly reduced. On the other hand, if the ratio of mineral oil is large, the inorganic powder exceeds the limit of the ability to absorb and retain mineral oil (oil absorption), so when it is used as a raw material mixture, the inorganic powder absorbs and retains the entire amount of mineral oil. It does not break, and a part of the mineral oil is liberated, and the raw material mixture becomes a lump (dumpling) instead of a good granule. In such a case, when the raw material mixture is injected into the extruder in the next step, it is impossible to stably input the raw material mixture by a fixed amount, which may affect the product quality. This phenomenon includes
Since the relationship (balance) between the oil absorption of the inorganic powder and the mixing ratio (compounding amount) of the mineral oil is affected, when the oil absorption of the inorganic powder is the same as in the above example, the mineral oil May occur when the mixing ratio of the inorganic powder becomes too large, and even when the mixing ratio of the mineral oil is the same, the same phenomenon may occur if the oil absorption of the inorganic powder becomes small. As described above, if the ratio of the mineral oil is small, various problems occur. Therefore, it is necessary to mix the mineral oil at a certain mixing ratio. Generally, an inorganic powder having a larger oil absorption is more expensive, and therefore, it is more advantageous in terms of cost to use an inorganic powder having a smaller oil absorption. However, as described above, the use of an inorganic powder having a small oil absorption has a disadvantage that the raw material mixture has a problem of agglomeration. Inorganic powders with high oil absorption have been used. The present invention
In view of the above problems, even when using an inorganic powder having a small oil absorption, without reducing the productivity and product quality, a lead-acid battery that sufficiently satisfies separator characteristics and battery characteristics. An object of the present invention is to provide a method for manufacturing a separator.

【0004】[0004]

【課題を解決するための手段】本発明者らは、上記の点
に鑑み、種々の検討を行った結果、次のような考え方を
導き出すに至った。つまり、吸油量の小さい無機粉体を
使用する場合には、配合すべき鉱物オイルの規定量に対
して、無機粉体の吸油量が十分でなくなるため、このま
までは原料混合物が塊状となってしまう。そこで、これ
を避けるため、鉱物オイルの配合を、原料混合物の作製
時には、無機粉体の吸油量に見合った量を配合するにと
どめ、残りの量は、加熱溶融混練時に押出成形機内に投
入して配合することで、従来の吸油量の大きい無機粉体
を使用した場合と同じ配合組成を持つ押出成形シートが
得られることを見出した。
Means for Solving the Problems In view of the above points, the present inventors have conducted various studies, and as a result, have derived the following concept. That is, when using an inorganic powder having a small oil absorption, the amount of the inorganic powder absorbed becomes insufficient with respect to the specified amount of the mineral oil to be blended, so that the raw material mixture becomes a lump as it is. . Therefore, in order to avoid this, only mix the mineral oil in the amount appropriate for the oil absorption of the inorganic powder when preparing the raw material mixture, and put the remaining amount into the extruder at the time of heat melting and kneading. It has been found that, by blending, an extruded sheet having the same blending composition as in the case of using a conventional inorganic powder having a large oil absorption is obtained.

【0005】すなわち、本発明の鉛蓄電池用セパレータ
の製造方法は、請求項1記載の通り、ポリオレフィン系
樹脂、無機粉体及び鉱物オイルの3者を主原料とした原
料混合物を加熱溶融混練しながらシート状に成形後、次
いで該シートから前記鉱物オイルの一部又は全部を除去
する鉛蓄電池用セパレータの製造方法において、前記鉱
物オイルを、加熱溶融混練前の原料混合物作製時と、加
熱溶融混練時とに分割して配合することを特徴とする。
また、請求項2記載の鉛蓄電池用セパレータの製造方法
は、請求項1記載の製造方法において、前記無機粉体
は、吸油量が220ml/100g以下であることを特
徴とする。また、請求項3記載の鉛蓄電池用セパレータ
の製造方法は、請求項1または2記載の製造方法におい
て、前記加熱溶融混練及びシート成形は、押出成形機を
用いて行うものであるとともに、前記鉱物オイルの加熱
溶融混練時における配合を、押出成形機の加熱溶融混練
を行う部位であるシリンダ部の末端に設けられた原料投
入口から対向末端にかけてのいずれかの位置から行うこ
とを特徴とする。また、請求項4記載の鉛蓄電池用セパ
レータの製造方法は、請求項3記載の製造方法におい
て、前記鉱物オイルの加熱溶融混練時における配合を、
原料投入口が設けられた一方のシリンダ部末端を起点と
してシリンダ部の全長の3/5までのいずれかの位置か
ら行うことを特徴とする。
That is, according to the method of manufacturing a separator for a lead storage battery of the present invention, as described in claim 1, a raw material mixture mainly composed of a polyolefin resin, an inorganic powder and a mineral oil is melted and kneaded. In a method for producing a separator for a lead-acid battery, after forming into a sheet and then removing a part or all of the mineral oil from the sheet, the mineral oil may be mixed with a raw material mixture before heating and melting and kneading. And being compounded separately.
According to a second aspect of the present invention, there is provided a method of manufacturing a lead storage battery separator according to the first aspect, wherein the inorganic powder has an oil absorption of 220 ml / 100 g or less. The method for producing a separator for a lead storage battery according to claim 3 is the method for producing a lead storage battery according to claim 1 or 2, wherein the heat-melt kneading and sheet forming are performed using an extruder. The compounding of the oil during the heat melting and kneading is performed from any position from the raw material input port provided at the end of the cylinder portion, which is the portion where the heat melting and kneading of the extruder is performed, to the opposite end. In addition, the method for producing a lead storage battery separator according to claim 4 is the production method according to claim 3, wherein the mineral oil is mixed at the time of heat melting and kneading.
Starting from the end of one of the cylinder portions provided with the raw material inlet, the process is performed from any position up to 3/5 of the entire length of the cylinder portion.

【0006】[0006]

【発明の実施の形態】本発明の鉛蓄電池用セパレータに
用いる主原料は、ポリオレフィン系樹脂と無機粉体と鉱
物オイルの3者である。ポリオレフィン系樹脂として
は、ポリエチレン、ポリプロピレン、ポリブテンおよび
これらの共重合物、あるいはこれらの混合物等が使用で
きるが、セパレータの機械的強度の面からは、平均分子
量が200万以上の超高分子量ポリエチレンを用いるこ
とが望ましい。
BEST MODE FOR CARRYING OUT THE INVENTION The main raw materials used for the lead-acid battery separator of the present invention are a polyolefin resin, an inorganic powder and a mineral oil. As the polyolefin-based resin, polyethylene, polypropylene, polybutene and copolymers thereof, or a mixture thereof can be used, but from the viewpoint of mechanical strength of the separator, ultra-high molecular weight polyethylene having an average molecular weight of 2,000,000 or more is used. It is desirable to use.

【0007】無機粉体としては、珪酸、珪酸カルシウ
ム、アルミナ、炭酸カルシウム、カオリンクレー、タル
ク、珪藻土、ガラス繊維粉等の1種または2種以上が使
用できる。
As the inorganic powder, one or more of silicic acid, calcium silicate, alumina, calcium carbonate, kaolin clay, talc, diatomaceous earth, glass fiber powder and the like can be used.

【0008】鉱物オイルとしては、主としてパラフィン
系オイルが使用されるが、これに限定されるものではな
い。
As the mineral oil, paraffin oil is mainly used, but it is not limited to this.

【0009】尚、本発明の鉛蓄電池用セパレータには、
少量の抗酸化剤や濡れ性向上のための浸透剤を配合して
も構わない。
The lead storage battery separator of the present invention includes:
A small amount of an antioxidant or a penetrant for improving wettability may be blended.

【0010】本発明の鉛蓄電池用セパレータの製造方法
においては、鉱物オイルを、加熱溶融混練前の原料混合
物作製時と、加熱溶融混練時とに分割して配合する。つ
まり、原料混合物の作製時には、無機粉体の吸油量に見
合った量を配合するにとどめ、残りの量は、加熱溶融混
練時に押出成形機内に投入して配合する。原料混合物の
作製時に配合する鉱物オイルの量は、使用する無機粉体
の種類、すなわち粉体の持つ吸油量特性によって適宜決
定される。
In the method for producing a separator for a lead storage battery according to the present invention, the mineral oil is separately compounded into a raw material mixture before heat melting and kneading and a heat melting and kneading. That is, when preparing the raw material mixture, only an amount corresponding to the amount of oil absorption of the inorganic powder is added, and the remaining amount is put into an extruder at the time of heating and melting and kneading to mix. The amount of the mineral oil to be blended when preparing the raw material mixture is appropriately determined according to the type of the inorganic powder to be used, that is, the oil absorption characteristics of the powder.

【0011】加熱溶融混練時の押出成形機への鉱物オイ
ルの投入は、押出成形機の加熱溶融混練を行う部位であ
るシリンダ部の末端に設けられた原料投入口から対向末
端にかけてのいずれかの位置から行えばよいが、より好
ましくは、原料投入口が設けられた一方のシリンダ部末
端を起点としてシリンダ部の全長の3/5までのいずれ
かの位置から行うのが好ましい。これは、鉱物オイルを
原料投入口から投入すると、投入した鉱物オイルが原料
混合物の顆粒表面に付着することにより、顆粒同士が結
合性を持ち易くなるため、塊状物を形成して投入口で詰
まりを生じてしまい、逆に、シリンダ部の全長の3/5
を越えた位置から投入すると、原料混合物はシリンダ内
部で完全に溶融されているため、鉱物オイルを投入して
もこれらとうまく混ざり合わず、投入した鉱物オイルが
遊離した状態でシリンダ内に滞留するため、スクリュウ
と押出材料との間に滑りが生じ、押出成形の妨げとなっ
てしまうからである。
The mineral oil is charged into the extruder at the time of the heat-melt kneading, and the mineral oil is charged at any point from the raw material input port provided at the end of the cylinder portion, which is the portion where the heat-melt kneading of the extruder is performed, to the opposite end. It may be carried out from the position, but more preferably from any position up to 3/5 of the total length of the cylinder part from the end of one cylinder part provided with the raw material inlet. This is because when the mineral oil is injected from the raw material inlet, the injected mineral oil adheres to the surface of the granules of the raw material mixture, so that the granules easily have a binding property. And conversely, 3/5 of the total length of the cylinder part
When the raw material mixture is charged from a position beyond the above, the raw material mixture is completely melted inside the cylinder, so even if the mineral oil is charged, it does not mix well with them, and the charged mineral oil stays in the cylinder in a released state Therefore, slippage occurs between the screw and the extruded material, which hinders extrusion molding.

【0012】図1に、本発明の製造方法に好適に使用さ
れる押出成形機の概略図を示す。加熱溶融混練時の押出
成形機10への鉱物オイルの投入は、例えば、図1に示
したように、シリンダ部1の末端に設けられた原料投入
口2から対向末端にかけてのいずれかの位置に、より好
ましくは、原料投入口が設けられた一方のシリンダ部末
端を起点としてシリンダ部の全長Lの3/5までのいず
れかの位置にシリンダ部内に連通する鉱物オイル投入口
3を設け、該部分へパイプを通して鉱物オイルを定量供
給するようにすればよい。
FIG. 1 shows a schematic diagram of an extrusion molding machine suitably used in the production method of the present invention. The injection of the mineral oil into the extruder 10 during the heat-melt kneading is performed, for example, at any position from the raw material input port 2 provided at the end of the cylinder unit 1 to the opposite end, as shown in FIG. More preferably, a mineral oil input port 3 communicating with the inside of the cylinder portion is provided at any position up to 3/5 of the total length L of the cylinder portion starting from the end of one cylinder portion provided with the raw material input port, Mineral oil may be supplied to the section through a pipe.

【0013】[0013]

【実施例】次に、本発明を実施例に基づき詳細に説明
が、本発明は以下の記載に何ら限定されるものではな
い。尚、以下で用いる無機粉体の吸油量とは、JIS
K5101の吸油量測定方法に基づいて測定された数値
である。
Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to the following description. In addition, the oil absorption of the inorganic powder used below is defined by JIS
It is a numerical value measured based on the oil absorption amount measurement method of K5101.

【0014】(実施例1)重量平均分子量200万の高
密度ポリエチレン樹脂粉体20質量部と、吸油量が16
9ml/100gであるシリカ微粉体30質量部をヘン
シェルミキサを用いて2分間混合した。得られた混合物
に、パラフィン系オイルの本来配合すべき規定量の3/
5に当たる30質量部を加えて再び混合した。840秒
後、3者の混合物が顆粒状となった時点で混合を終了し
た。次に、所定温度に制御されたTダイ付き二軸同方向
回転型押出成形機を用意し、該押出成形機のシリンダ部
の末端に設けられた原料投入口からは、得られた原料混
合物を440kg/hのペースで連続投入するととも
に、原料投入口が設けられた一方のシリンダ部末端を起
点としてシリンダ部の全長の約2/5の距離にある位置
に設けられたシリンダ部内に連通する鉱物オイル投入口
からは、パラフィン系オイルを110kg/hのペース
で連続投入して、シート状に押し出すとともに、2本の
成形ロール間を通して加圧成形し、厚さ0.25mmの
押出成形シートを得た。次に、得られた押出成形シート
を、トリクロロエチレン液中に3分間浸漬して、該シー
ト中の鉱物オイルの一部を抽出除去した後、加熱乾燥し
て、鉛蓄電池用セパレータを得た。尚、本実施例におい
て、原料混合物の押出性および製品品質は良好であっ
た。
Example 1 20 parts by mass of a high-density polyethylene resin powder having a weight average molecular weight of 2,000,000 and an oil absorption of 16
30 parts by mass of fine silica powder of 9 ml / 100 g was mixed for 2 minutes using a Henschel mixer. In the obtained mixture, the specified amount of paraffin oil is 3 /
30 parts by mass corresponding to 5 were added and mixed again. After 840 seconds, the mixing was terminated when the mixture of the three became granular. Next, a twin-screw co-rotating extruder equipped with a T-die controlled at a predetermined temperature is prepared, and the obtained raw material mixture is supplied through a raw material inlet provided at an end of a cylinder portion of the extruder. Mineral that is continuously charged at a rate of 440 kg / h and communicates with a cylinder provided at a position about 2/5 of the entire length of the cylinder starting from the end of one cylinder provided with the raw material inlet. From the oil inlet, a paraffin-based oil is continuously fed at a rate of 110 kg / h, extruded into a sheet shape, and pressed and formed between two forming rolls to obtain an extruded sheet having a thickness of 0.25 mm. Was. Next, the obtained extruded sheet was immersed in a trichloroethylene solution for 3 minutes to extract and remove a part of the mineral oil in the sheet, and then heated and dried to obtain a lead storage battery separator. In this example, the extrudability and the product quality of the raw material mixture were good.

【0015】(比較例1)重量平均分子量200万の高
密度ポリエチレン樹脂粉体20質量部と、吸油量が16
9ml/100gであるシリカ微粉体30質量部をヘン
シェルミキサを用いて2分間混合した。得られた混合物
に、パラフィン系オイルの本来配合すべき規定量の全量
に当たる50質量部を加えて再び混合した。5秒後、3
者の混合物は、塊状(団子状)となり、ミキサに著しい
負荷がかかったので、混合を終了した。鉱物オイルを投
入してからわずか5秒しか混合していないことで3者の
原料が均一に混ざり合っていないことと、塊状となって
しまったことで押出成形機への定量投入ができないこと
から、押出成形は不可能と判断した。
Comparative Example 1 20 parts by mass of a high-density polyethylene resin powder having a weight average molecular weight of 2,000,000 and an oil absorption of 16
30 parts by mass of fine silica powder of 9 ml / 100 g was mixed for 2 minutes using a Henschel mixer. To the obtained mixture, 50 parts by mass corresponding to the total amount of the specified amount of the paraffin-based oil to be originally blended was added and mixed again. After 5 seconds, 3
The mixture of the sampler became a lump (dumpling) and a significant load was applied to the mixer, so that the mixing was terminated. Because the raw materials of the three parties are not evenly mixed because they are mixed only for 5 seconds after the mineral oil is injected, and because they have become lump, they cannot be quantitatively injected into the extruder. Extrusion molding was judged impossible.

【0016】(従来例1)重量平均分子量200万の高
密度ポリエチレン樹脂粉体20質量部と、吸油量が24
1ml/100gであるシリカ微粉体30質量部をヘン
シェルミキサを用いて2分間混合した。得られた混合物
に、パラフィン系オイルの本来配合すべき規定量の全量
に当たる50質量部を加えて再び混合した。720秒
後、3者の混合物が顆粒状となった時点で混合を終了し
た。次に、所定温度に制御されたTダイ付き二軸同方向
回転型押出成形機を用意し、該押出成形機のシリンダ部
の末端に設けられた原料投入口から、得られた原料混合
物を550kg/hのペースで連続投入して、シート状
に押し出すとともに、2本の成形ロール間を通して加圧
成形し、厚さ0.25mmの押出成形シートを得た。次
に、得られた押出成形シートを、トリクロロエチレン液
中に3分間浸漬して、該シート中の鉱物オイルの一部を
抽出除去した後、加熱乾燥して、鉛蓄電池用セパレータ
を得た。尚、本従来例において、原料混合物の押出性お
よび製品品質は良好であった。
(Conventional Example 1) 20 parts by mass of a high-density polyethylene resin powder having a weight average molecular weight of 2,000,000 and an oil absorption of 24
30 parts by mass of 1 ml / 100 g of silica fine powder was mixed for 2 minutes using a Henschel mixer. To the obtained mixture, 50 parts by mass corresponding to the total amount of the specified amount of the paraffin-based oil to be originally blended was added and mixed again. After 720 seconds, the mixing was terminated when the mixture of the three became granular. Next, a twin-screw co-rotating extruder equipped with a T-die controlled at a predetermined temperature is prepared, and 550 kg of the obtained raw material mixture is fed from a raw material inlet provided at an end of a cylinder portion of the extruder. / H, continuously extruded at a rate of / h, extruded into a sheet shape, and formed under pressure through two forming rolls to obtain an extruded sheet having a thickness of 0.25 mm. Next, the obtained extruded sheet was immersed in a trichloroethylene solution for 3 minutes to extract and remove a part of the mineral oil in the sheet, and then heated and dried to obtain a lead storage battery separator. In this conventional example, the extrudability and product quality of the raw material mixture were good.

【0017】[0017]

【発明の効果】本発明の鉛蓄電池用セパレータの製造方
法によれば、ポリオレフィン系樹脂、無機粉体及び鉱物
オイルの3者を主原料とした原料混合物を加熱溶融混練
しながらシート状に成形後、次いで該シートから前記鉱
物オイルの一部又は全部を除去する鉛蓄電池用セパレー
タの製造方法において、前記鉱物オイルを、加熱溶融混
練前の原料混合物作製時と、加熱溶融混練時とに分割し
て配合することにより、吸油量の小さい無機粉体を使用
した場合であっても、生産性や品質を低下させることが
なく、セパレータ特性や電池特性を十分に満足する鉛蓄
電池用セパレータが得られるため、セパレータのコスト
ダウンが図れる。
According to the method for producing a separator for a lead storage battery of the present invention, a raw material mixture mainly composed of a polyolefin resin, an inorganic powder and a mineral oil is formed into a sheet while being melted and kneaded. Then, in the method for producing a lead storage battery separator for removing part or all of the mineral oil from the sheet, the mineral oil is divided into a raw material mixture before heat melting and kneading and a heat melting and kneading. By blending, even when using an inorganic powder having a small oil absorption, a separator for a lead-acid battery that sufficiently satisfies separator characteristics and battery characteristics can be obtained without lowering productivity or quality. In addition, the cost of the separator can be reduced.

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

【図1】 本発明の製造方法に好適に使用される押出成
形機の概略図である。
FIG. 1 is a schematic view of an extrusion molding machine suitably used in the production method of the present invention.

【符号の説明】[Explanation of symbols]

1 シリンダ部(スクリュウによる加熱溶融部分) 2 原料投入口 3 鉱物オイル投入口 4 Tダイ 5 成形ロール 6 溶融樹脂から製造された押出成形シート 10 押出成形機 L シリンダ部の全長 DESCRIPTION OF SYMBOLS 1 Cylinder part (the part heated and melted with a screw) 2 Raw material input port 3 Mineral oil input port 4 T die 5 Forming roll 6 Extruded sheet manufactured from molten resin 10 Extruder L Length of cylinder section

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 ポリオレフィン系樹脂、無機粉体及び鉱
物オイルの3者を主原料とした原料混合物を加熱溶融混
練しながらシート状に成形後、次いで該シートから前記
鉱物オイルの一部又は全部を除去する鉛蓄電池用セパレ
ータの製造方法において、前記鉱物オイルを、加熱溶融
混練前の原料混合物作製時と、加熱溶融混練時とに分割
して配合することを特徴とする鉛蓄電池用セパレータの
製造方法。
1. A material mixture mainly composed of a polyolefin resin, an inorganic powder and a mineral oil is formed into a sheet while being heated, melt-kneaded, and then a part or all of the mineral oil is removed from the sheet. A method for manufacturing a separator for a lead-acid battery, wherein the mineral oil is divided and mixed at the time of preparing a raw material mixture before heat-melting and kneading and at the time of heating-melting and kneading. .
【請求項2】 前記無機粉体は、吸油量が220ml/
100g以下であることを特徴とする請求項1記載の鉛
蓄電池用セパレータの製造方法。
2. The inorganic powder has an oil absorption of 220 ml /
The method for producing a lead storage battery separator according to claim 1, wherein the weight is 100 g or less.
【請求項3】 前記加熱溶融混練及びシート成形は、押
出成形機を用いて行うものであるとともに、前記鉱物オ
イルの加熱溶融混練時における配合を、押出成形機の加
熱溶融混練を行う部位であるシリンダ部の末端に設けら
れた原料投入口から対向末端にかけてのいずれかの位置
から行うことを特徴とする請求項1または2記載の鉛蓄
電池用セパレータの製造方法。
3. The heat-melt kneading and sheet forming are performed by using an extruder, and the blending of the mineral oil at the time of heat-melt kneading is a portion where the heat-melt kneading of the extruder is performed. The method for producing a separator for a lead storage battery according to claim 1, wherein the method is performed from any position from a raw material inlet provided at an end of the cylinder portion to an opposite end.
【請求項4】 前記鉱物オイルの加熱溶融混練時におけ
る配合を、原料投入口が設けられた一方のシリンダ部末
端を起点としてシリンダ部の全長の3/5までのいずれ
かの位置から行うことを特徴とする請求項3記載の鉛蓄
電池用セパレータの製造方法。
4. Mixing of said mineral oil during heat melting and kneading is carried out from any position up to 3/5 of the total length of the cylinder part, starting from the end of one cylinder part provided with a raw material inlet. A method for producing a separator for a lead storage battery according to claim 3, characterized in that:
JP2000310717A 2000-10-11 2000-10-11 Manufacturing method of separator for lead-acid battery Withdrawn JP2002117824A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000310717A JP2002117824A (en) 2000-10-11 2000-10-11 Manufacturing method of separator for lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000310717A JP2002117824A (en) 2000-10-11 2000-10-11 Manufacturing method of separator for lead-acid battery

Publications (1)

Publication Number Publication Date
JP2002117824A true JP2002117824A (en) 2002-04-19

Family

ID=18790624

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000310717A Withdrawn JP2002117824A (en) 2000-10-11 2000-10-11 Manufacturing method of separator for lead-acid battery

Country Status (1)

Country Link
JP (1) JP2002117824A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004281208A (en) * 2003-03-14 2004-10-07 Tomoegawa Paper Co Ltd Separator for electronic part
JP2006338918A (en) * 2005-05-31 2006-12-14 Tomoegawa Paper Co Ltd Electronic component and separator therefor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004281208A (en) * 2003-03-14 2004-10-07 Tomoegawa Paper Co Ltd Separator for electronic part
JP4691314B2 (en) * 2003-03-14 2011-06-01 株式会社巴川製紙所 Manufacturing method of separator for electronic parts
JP2006338918A (en) * 2005-05-31 2006-12-14 Tomoegawa Paper Co Ltd Electronic component and separator therefor

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