JP2003159507A - Filter medium for air filter - Google Patents

Filter medium for air filter

Info

Publication number
JP2003159507A
JP2003159507A JP2001361016A JP2001361016A JP2003159507A JP 2003159507 A JP2003159507 A JP 2003159507A JP 2001361016 A JP2001361016 A JP 2001361016A JP 2001361016 A JP2001361016 A JP 2001361016A JP 2003159507 A JP2003159507 A JP 2003159507A
Authority
JP
Japan
Prior art keywords
polyvinyl alcohol
filter
filter medium
air filter
weight
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.)
Granted
Application number
JP2001361016A
Other languages
Japanese (ja)
Other versions
JP2003159507A5 (en
JP3848139B2 (en
Inventor
Nobuyuki Sakazume
信之 坂爪
Eiko Meguro
栄子 目黒
Tomohiko Soyama
智彦 楚山
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.)
Hokuetsu Paper Mills Ltd
Original Assignee
Hokuetsu Paper Mills 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 Hokuetsu Paper Mills Ltd filed Critical Hokuetsu Paper Mills Ltd
Priority to JP2001361016A priority Critical patent/JP3848139B2/en
Publication of JP2003159507A publication Critical patent/JP2003159507A/en
Publication of JP2003159507A5 publication Critical patent/JP2003159507A5/ja
Application granted granted Critical
Publication of JP3848139B2 publication Critical patent/JP3848139B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

<P>PROBLEM TO BE SOLVED: To provide a filter medium for an air filter with high stiffness and high strength against delamination, low increase of pressure loss and excellent in pleating processability. <P>SOLUTION: In a filter medium for an air filter consisting of a nonwoven fabric of a basis weight 25-150 g/m<SP>2</SP>, the filter medium for an air filter wherein a polyvinyl alcohol fiber-like binder adhering component fibers is not completely dissolved and swells while holding a fiber form and uniformly exists in the thickness direction of the filter medium. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、半導体製造などの各種
クリーンルーム、ビル空調用、空気清浄の用途などに使
用されるガラス繊維を主体としたエアフィルタ用濾材に
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter material for an air filter, which is mainly made of glass fiber and is used in various clean rooms such as semiconductor manufacturing, air conditioning for buildings, and air cleaning applications.

【0002】[0002]

【従来の技術】従来、極細ガラス繊維、又はチョップド
ガラス繊維主体のエアフィルタ用濾材は、ガラス繊維自
体に接着力が無く、濾材強度が出ないため、従来より水
系の合成樹脂系バインダーやポリビニルアルコール繊維
状バインダーなどを単独使用、あるいは併用して強度付
与させている。このうち、ポリビニルアルコール繊維状
バインダーは、濾材製造時では、原料ガラス繊維に混合
して水に分散し、湿式抄紙でシート化する「内添法」で
使用され、繊維状であるため、抄紙時のシートへの歩留
まりが良く、合成樹脂系バインダーのようにバインダー
を含浸させるための後工程を必要としないなどの利点が
ある。ところが、ポリビニルアルコール繊維状バインダ
ーにおいては、製造時の乾燥工程で、シート中の熱水に
いったん溶解するため、同工程の中でシートの厚みの外
側方向に、次第にバインダーが移動するいわゆる「マイ
グレーション」を起こしやすい。
2. Description of the Related Art Conventionally, a filter material for an air filter, which is mainly composed of ultrafine glass fiber or chopped glass fiber, has no adhesive strength to the glass fiber itself and does not exhibit the strength of the filter material. A fibrous binder or the like is used alone or in combination to impart strength. Among them, the polyvinyl alcohol fibrous binder is used in the “internal addition method” in which it is mixed with the raw glass fibers and dispersed in water at the time of manufacturing the filter medium, and is made into a sheet by wet papermaking. The sheet has a good yield and does not require a post-process for impregnating the binder like a synthetic resin binder. However, in the polyvinyl alcohol fibrous binder, since it once dissolves in the hot water in the sheet in the drying step during manufacturing, the binder gradually moves in the outward direction of the sheet thickness in the same step, so-called "migration". Easy to cause.

【0003】この結果、シート表面に樹脂だまりができ
て、濾材の目をふさぎ、圧力損失を増大させたり、シー
ト内部のバインダー不足が原因で、シートの剛性が低下
する。また、これをひだ折りプリーツ加工を行い、濾材
をユニットとして組み立てる際、割れ、層剥離、折り山
姿不良等のトラブルを起こすことが知られている。
As a result, a resin puddle is formed on the surface of the sheet, which blocks the eyes of the filter medium to increase the pressure loss and the rigidity of the sheet is lowered due to the lack of binder in the sheet. It is also known that when this is subjected to pleat folding pleating and the filter medium is assembled as a unit, troubles such as cracking, layer peeling, and defective folded mountain shape are caused.

【0004】[0004]

【発明が解決しようとする課題】本発明の課題は、上記
欠点や問題点を解決し、ガーレー剛度が高く、圧力損失
が低く、ひだ折りプリーツ加工特性、特に剥離強度の良
好なエアフィルタ用濾材を提供することである。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned drawbacks and problems, to obtain a filter material for an air filter which has a high Gurley rigidity, a low pressure loss, and good pleat folding pleating properties, particularly peel strength. Is to provide.

【0005】[0005]

【課題を解決するための手段】本発明者は、従来の様
に、繊維状バインダーを完全溶融させると、前述のごと
く問題が生ずるが、これを半溶融状態、即ち繊維の形態
を保持させた状態に制御して、バインダーとして用いる
ことにより、これらの問題点を解決できる事を見出し
た。
SUMMARY OF THE INVENTION The inventor of the present invention maintains the semi-molten state, that is, the morphology of the fiber, although the problem occurs as described above when the fibrous binder is completely melted as in the conventional case. It was found that these problems can be solved by controlling the state and using it as a binder.

【0006】即ち、本発明は、坪量25〜150g/m
2 の不織布からなるエアフィルタ用濾材において、構成
繊維を接着させるポリビニルアルコール繊維状バインダ
ーが完全溶解することなく繊維形態を保持しながら膨潤
し、濾材の厚さ方向に均一に存在していることを特徴と
する、エアフィルタ用濾材に関する。
That is, the present invention has a basis weight of 25 to 150 g / m.
In the filter material for an air filter composed of the non-woven fabric of 2, the polyvinyl alcohol fibrous binder for adhering the constituent fibers swells while maintaining the fiber morphology without being completely dissolved, and is present evenly in the thickness direction of the filter material. The present invention relates to a filter material for an air filter, which is characterized.

【0007】本発明の好ましい実施態様においては、膨
潤後のポリビニルアルコール繊維状バインダーの繊維径
が7.5〜110μmである。本発明の別の好ましい実
施態様においては、ポリビニルアルコール繊維状バイン
ダーの繊維径が膨潤前の繊維径の1.1〜7.0倍であ
る。濾材中のポリビニルアルコール繊維状バインダーが
濾材重量を基準として0.1〜10重量%であるのが有
利である。
In a preferred embodiment of the present invention, the fiber diameter of the polyvinyl alcohol fibrous binder after swelling is 7.5 to 110 μm. In another preferred embodiment of the present invention, the fiber diameter of the polyvinyl alcohol fibrous binder is 1.1 to 7.0 times the fiber diameter before swelling. Advantageously, the polyvinyl alcohol fibrous binder in the filter medium is from 0.1 to 10% by weight, based on the weight of the filter medium.

【0008】本発明のエアフィルタ用濾材はガラス繊維
を主体とした不織布であるのが有利である。エアフィル
タ用濾材は、例えば平均繊維径6μm以下の極細ガラス
繊維またはチョップドガラス繊維を主体とするが、必要
に応じてポリエチレン、ポリプロピレン、ポリエステ
ル、ポリアラミド、アクリル、ビニロン、レーヨンなど
の有機繊維が配合されていてもよい。
The air filter material of the present invention is advantageously a non-woven fabric composed mainly of glass fibers. The filter material for an air filter is mainly composed of ultrafine glass fibers or chopped glass fibers having an average fiber diameter of 6 μm or less, but if necessary, organic fibers such as polyethylene, polypropylene, polyester, polyaramid, acrylic, vinylon and rayon are blended. May be.

【0009】エアフィルタ用濾材の製造工程におけるバ
インダーの付与方法には、繊維シート形成後に付与する
外添法と、原料繊維の分散工程で添加する内添法がある
が、本発明においては、ポリビニルアルコール繊維状バ
インダーを均一に分散させるために、内添法で行なう必
要がある。また、本発明の濾材を製造する際には、ポリ
ビニルアルコール繊維状バインダーを含んだ湿紙の乾燥
前の含水率が後述の理由から50〜80重量%である必
要がある。
The method of applying the binder in the process of manufacturing the filter material for the air filter includes an external addition method which is applied after forming the fiber sheet and an internal addition method which is added in the step of dispersing the raw material fibers. In the present invention, polyvinyl is used. In order to uniformly disperse the alcohol fibrous binder, it is necessary to carry out the internal addition method. Further, when the filter medium of the present invention is manufactured, the moisture content of the wet paper containing the polyvinyl alcohol fibrous binder before drying needs to be 50 to 80% by weight for the reason described below.

【0010】即ち、本発明のエアフィルタ用濾材は、原
料繊維を水中でスラリー化し、このスラリー化工程の際
にポリビニルアルコール繊維状バインダーを添加し、得
られるスラリーを抄紙機で抄紙し、50〜80重量%の
含水率の湿紙を形成しそして乾燥することを特徴とする
方法によって製造される。この方法も本発明の対象であ
る。
That is, in the filter medium for an air filter of the present invention, raw material fibers are slurried in water, a polyvinyl alcohol fibrous binder is added during this slurrying step, and the resulting slurry is paper-made by a paper machine. Produced by a process characterized in that a wet paper web with a water content of 80% by weight is formed and dried. This method is also the subject of the present invention.

【0011】本発明を以下に更に詳細に説明する。ポリ
ビニルアルコール繊維状バインダーを内添法で使用する
際に、シートが乾燥工程に入り、シートが保持する水の
温度が溶解温度に達すると、繊維状バインダーはその表
面から溶融し、混合した他の繊維との交点に付着し、シ
ートの水分が蒸発するとともに固化し、強度を発揮す
る。その際、繊維状バインダーの直径は、溶融前後で太
くなる現象、つまり「膨潤」が見られ、この現象と本発
明の効果とで高い相関があることを本発明者等は発見し
た。
The present invention will be described in more detail below. When the polyvinyl alcohol fibrous binder is used in the internal addition method, when the sheet enters the drying step and the temperature of the water held by the sheet reaches the melting temperature, the fibrous binder is melted from its surface and mixed with other materials. It adheres to the intersections with the fibers and solidifies as the water content of the sheet evaporates, providing strength. At that time, the diameter of the fibrous binder was thickened before and after melting, that is, "swelling" was observed, and the present inventors found that there is a high correlation between this phenomenon and the effect of the present invention.

【0012】即ち、半溶融状態であるポリビニルアルコ
ール繊維状バインダーの直径は、溶融前に比べ1.1倍
〜7倍に膨潤しており、この膨潤状態に制御できれば繊
維状バインダーが乾燥工程でマイグレーションを起こさ
ないことが分かった。繊維状バインダーは7倍より多く
膨潤すると完全溶解してマイグレーションを起し、膨潤
度が1.1倍より小さいと、ほとんど溶解部分がなく、
バインダー効果が発揮されない。この膨潤状態は、電子
顕微鏡下、あるいは後述の如く、繊維状バインダーを着
色して実態顕微鏡下で観察することができ、膨潤前の繊
維直径との関係から膨潤度を算出することができる。ま
た、膨潤度1.1倍以下の繊維状バインダーは、電子顕
微鏡や実態顕微鏡での観察で、繊維状バインダーとガラ
ス繊維、あるいは繊維状バインダー同志との交点での融
着が見られない。
That is, the diameter of the polyvinyl alcohol fibrous binder in a semi-molten state is 1.1 to 7 times as large as that before the melting, and if the swelling state can be controlled, the fibrous binder migrates in the drying step. I found that it does not cause. When the fibrous binder swells more than 7 times, it completely dissolves and causes migration, and when the degree of swelling is less than 1.1 times, there is almost no dissolved portion,
The binder effect is not exhibited. This swelling state can be observed under an electron microscope, or as described later, by coloring the fibrous binder and observing under a real microscope, and the degree of swelling can be calculated from the relationship with the fiber diameter before swelling. Further, the fibrous binder having a swelling degree of 1.1 times or less does not show fusion at the intersection of the fibrous binder and the glass fiber, or the fibrous binders, when observed with an electron microscope or an actual microscope.

【0013】本発明で用いられるポリビニルアルコール
繊維状バインダー直径は、通常7μmから15μmのも
のが用いられるが、これらは繊維状バインダーとして一
般的なものである。ちなみに、15μm以上のものは単
位重量当たりの本数が少なくなるため、接着交点が少な
くバインダー効果が低く、一方、7μm以下のものは、
ポリビニルアルコール繊維状バインダーの製造コストが
高くなってしまう。これらを前述の膨潤度1.1〜7.
0倍に制御することにより、本発明の効果を発揮させる
ことができる。ポリビニルアルコール繊維状バインダー
の膨潤後の直径は、7.5〜110μmの範囲内となり
得る。
The polyvinyl alcohol fibrous binder used in the present invention usually has a diameter of 7 μm to 15 μm. These are common fibrous binders. By the way, since the number of particles of 15 μm or more is small per unit weight, the number of adhesive intersections is small and the binder effect is low, while those of 7 μm or less are
The production cost of the polyvinyl alcohol fibrous binder increases. These have swelling degrees of 1.1 to 7.
By controlling to 0 times, the effect of the present invention can be exhibited. The swelled diameter of the polyvinyl alcohol fibrous binder can be in the range of 7.5 to 110 μm.

【0014】また、本発明で用いられるポリビニルアル
コール繊維状バインダーには、構造式、溶解温度の異な
るさまざまなタイプのものがあり、本発明の効果を発揮
させるためこれら選定に注意しなければならない。ポリ
ビニルアルコール繊維状バインダーについて各種溶解温
度のものが知られているが、自身の溶解温度が低過ぎる
と、湿熱効果により乾燥工程で完全溶解してしまい、マ
イグレーションを起こし、剛度が低下し、圧力損失が増
加してしまう。また、溶解温度が高過ぎると、繊維間の
接着力が低くなり、濾材強度が低くなる。
There are various types of polyvinyl alcohol fibrous binders used in the present invention having different structural formulas and melting temperatures, and it is necessary to pay attention to their selection in order to exert the effects of the present invention. Polyvinyl alcohol fibrous binders with various melting temperatures are known, but if the melting temperature of itself is too low, it will completely dissolve in the drying process due to the wet heat effect, causing migration, lowering the rigidity and pressure loss. Will increase. On the other hand, if the melting temperature is too high, the adhesive force between the fibers becomes low and the strength of the filter medium becomes low.

【0015】繊維の形態保持をさせる方法としては、特
に1つに限定するものではないが、例えば、湿紙の水分
にも充分に注意する必要がある。好ましい溶解温度は、
抄紙機の乾燥能力、条件等の関係で選定されるが、通常
50℃〜80℃である。水分が少な過ぎると、溶解せず
繊維間の接着力が少なくなり、濾材強度が低くなる。ま
た、水分が高過ぎると、完全溶解してしまい、マイグレ
ーションを起こし、剛度が低下し、圧力損失が増加して
しまう。本発明では、乾燥工程に入る直前の湿紙の水分
を50%〜80%、好ましくは55%〜70%にするこ
とが望ましい。
The method for maintaining the shape of the fiber is not particularly limited to one, but for example, it is necessary to pay sufficient attention to the water content of the wet paper. The preferred melting temperature is
The temperature is usually 50 ° C to 80 ° C, although it is selected depending on the drying ability of the paper machine, the conditions, and the like. If the water content is too low, it will not dissolve and the adhesive force between the fibers will decrease, resulting in a low strength of the filter medium. Further, if the water content is too high, it will be completely dissolved, causing migration, lowering the rigidity and increasing the pressure loss. In the present invention, it is desirable that the moisture content of the wet paper sheet immediately before entering the drying step be 50% to 80%, preferably 55% to 70%.

【0016】また、熱水溶解温度の高いポリビニルアル
コール繊維状バインダーを選定するのも一つの方法であ
る。その他、ポリビニルアルコール繊維状バインダー
が、熱水に溶解するのにある程度の時間がかかるのを利
用し、湿紙を高温で急加熱し、一気に水分をとばす方
法、あるいは、前述の通り乾燥工程に入る前に、湿紙の
水分をプレス脱水や真空吸引で十分に減らしておいて、
乾燥させる方法などが挙げられる。ただし、いずれの方
法も条件が厳しすぎると、繊維が全く溶解、膨張しない
で、バインダー効果を発揮しなくなるので、条件設定に
は十分注意しなければならない。
Further, one method is to select a polyvinyl alcohol fibrous binder having a high hot water dissolution temperature. In addition, the polyvinyl alcohol fibrous binder takes a certain amount of time to dissolve in hot water, so that the wet paper web is rapidly heated at a high temperature to quickly remove the moisture, or the drying process is started as described above. Before doing so, sufficiently reduce the water content of the wet paper by press dehydration or vacuum suction,
Examples include a method of drying. However, in any of the methods, if the conditions are too strict, the fibers will not dissolve or expand at all, and the binder effect will not be exhibited.

【0017】ポリビニルアルコール繊維状バインダーの
含有量は、望ましくは0.1重量%〜10重量%である
が、0.5重量%〜7重量%がより望ましい。ポリビニ
ルアルコール繊維状バインダーの含有量が対濾材重量
0.1重量%未満では効果が少なく、10重量%を超え
ると、エアフィルタ用濾材の圧力損失を著しく増加させ
てしまう。
The content of the polyvinyl alcohol fibrous binder is preferably 0.1% by weight to 10% by weight, more preferably 0.5% by weight to 7% by weight. If the content of the polyvinyl alcohol fibrous binder is less than 0.1% by weight based on the weight of the filter medium, the effect is small, and if it exceeds 10% by weight, the pressure loss of the filter medium for an air filter is significantly increased.

【0018】ポリビニルアルコール繊維状バインダー
は、単独で内添法により用いて本発明の目的を達成させ
ることができるが、濾材に通常要求される耐水性、撥水
性、耐薬品性を付与させたい場合は、更に合成樹脂系バ
インダーラテックスあるいは撥水剤を併用することが望
ましい。これらの濾材中におけるポリビニルアルコール
繊維状バインダーとの合計含有量は10重量%以下、好
ましくは7重量%以下である。多くの合成樹脂系バイン
ダーラテックスは、繊維間で膜状物を形成し、圧力損失
の上昇を起こしやすいため、その量は少ない程よい。
The polyvinyl alcohol fibrous binder can be used alone by the internal addition method to achieve the object of the present invention, but when it is desired to impart water resistance, water repellency and chemical resistance which are usually required for a filter medium. It is desirable to use a synthetic resin binder latex or a water repellent together. The total content of the polyvinyl alcohol fibrous binder in these filter media is 10% by weight or less, preferably 7% by weight or less. Since many synthetic resin binder latexes form a film-like substance between fibers and easily cause an increase in pressure loss, the smaller the amount, the better.

【0019】合成樹脂系バインダーラテックスとして
は、特に限定されるものではないが、例えば、アクリル
系ラテックス、酢ビ系ラテックス、ウレタン系ラテック
ス、エポキシ系ラテックス、SBR系ラテックス、NB
R系ラテックス、オレフィン系ラテックス等を単独、又
は2種類以上併用できるが、基材との接着性が良く、膜
状物を形成し難いものを選定するべきである。
The synthetic resin binder latex is not particularly limited, but examples thereof include acrylic latex, vinyl acetate latex, urethane latex, epoxy latex, SBR latex and NB.
R-based latex, olefin-based latex and the like can be used alone or in combination of two or more kinds, but one having good adhesiveness to the substrate and difficult to form a film-like substance should be selected.

【0020】本発明の濾材は、一般紙や湿式不織布を製
造するための抄紙機、例えば、長網抄紙機、円網抄紙
機、傾斜ワイヤー式抄紙機などの湿式抄紙機で製造でき
る。乾燥にはシリンダードライヤー、ヤンキードライヤ
ー、スルードライヤー、赤外線ドライヤーなどの乾燥機
を用いることができる。また、2種類以上の乾燥機を使
用し、本発明の濾材を乾燥することは何ら差し支えな
い。
The filter medium of the present invention can be produced by a paper machine for producing general paper or wet non-woven fabric, for example, a wet paper machine such as a Fourdrinier paper machine, a cylinder paper machine or a tilted wire paper machine. A dryer such as a cylinder dryer, a Yankee dryer, a through dryer or an infrared dryer can be used for drying. Further, there is no problem in drying the filter medium of the present invention by using two or more kinds of dryers.

【0021】[0021]

【実施例】以下に実施例を挙げて本発明を具体的に説明
するが、本発明はこれらの実施例に限定されるものでは
ない。なお、実施例及び比較例における坪量、シートの
厚さ、ガーレー剛度、剥離強度及び圧力損失は以下の方
法で測定した。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples. The basis weight, sheet thickness, Gurley rigidity, peel strength and pressure loss in the examples and comparative examples were measured by the following methods.

【0022】本発明で測定を行った坪量、シートの厚さ
は、JIS L−1096に準拠して行った。ガーレー
剛度については、TAPPI STANDARD T5
43pm−84に準拠して行ったが、サンプルの長さ
2.5インチ、幅1インチにて測定を行った。剥離強度
は、TAPPI UM569に準拠して測定を行った。
圧力損失は(Pa)、JIS B9908に準じて測定
され、濾材に空気を風速5.3cm/秒で通気させた時
の通気抵抗を測定した。シート乾燥前後のポリビニルア
ルコール繊維状バインダーの直径は、紙パルプの種類と
その試験法(紙パルプ技術協会編、“紙パルプの種類と
その試験法”のPVAのヨウ素硼酸試験、昭和41年、
p301)を用いて着色を行い、その着色された繊維の
直径を実体顕微鏡にて任意に10本測定し、それらの繊
維径の平均値を算出した。プリーツ加工適性について
は、加工機に通した時の割れ、剥離、折姿の状況を目視
にて判定した。
The basis weight and sheet thickness measured in the present invention were measured in accordance with JIS L-1096. For Gurley stiffness, TAPPI STANDARD T5
The measurement was carried out in accordance with 43 pm-84, but the length of the sample was 2.5 inches and the width was 1 inch. The peel strength was measured according to TAPPI UM569.
The pressure loss (Pa) was measured according to JIS B9908, and the ventilation resistance when air was passed through the filter medium at a wind speed of 5.3 cm / sec was measured. The diameter of the polyvinyl alcohol fibrous binder before and after the sheet is dried is determined by the type of paper pulp and its test method (edited by the Japan Paper Pulp Technology Association, “Type of Paper Pulp and Its Test Method”, PVA iodine boric acid test, 1966,
Coloring was performed using p301), and the diameters of the colored fibers were arbitrarily measured with a stereomicroscope, and the average value of the fiber diameters was calculated. Regarding the suitability for pleating, the state of cracking, peeling, and folding when passing through a processing machine was visually determined.

【0023】実施例1:平均繊維径6μm以下の極細ガ
ラス繊維90重量%とチョップドガラス繊維10重量%
及び対濾材重量0.5重量%のポリビニルアルコール繊
維状バインダー(SPG 056、クラレ(株)製、
7.3μm×3mm)をパルパーにて、pH3.5の酸
性水を用いて離解し、水性スラリーを作成して、これら
のスラリーから標準角型手抄き抄紙機を用いて、シート
を形成した。これにアクリル系ラテックス(SFA−3
3、大日本インキ(株)製)を湿紙に付与し、湿紙の水
分を55%にし、その後130℃のロータリードライヤ
ーにて一気に乾燥し、坪量70g/m2 、バインダー樹
脂分6.2重量%で、シート乾燥後の膨潤したポリビニ
ルアルコール繊維状バインダーの繊維径が8.1mmの
シートを得た。
Example 1 90% by weight of ultrafine glass fibers having an average fiber diameter of 6 μm or less and 10% by weight of chopped glass fibers
And polyvinyl alcohol fibrous binder (SPG 056, manufactured by Kuraray Co., Ltd.
(7.3 μm × 3 mm) was disaggregated with a pulper using acidic water having a pH of 3.5 to prepare an aqueous slurry, and a sheet was formed from these slurries using a standard square handmade paper machine. . Acrylic latex (SFA-3
3. Dainippon Ink and Co., Ltd. was applied to the wet paper to make the wet paper have a water content of 55%, and then dried at once with a rotary dryer at 130 ° C., a basis weight of 70 g / m 2 , a binder resin content of 6. A sheet having a fiber diameter of the swollen polyvinyl alcohol fibrous binder after sheet drying of 8.1 mm was obtained at 2% by weight.

【0024】実施例2:湿紙の水分を70%にした以外
は実施例1を繰り返した。シート乾燥後のポリビニルア
ルコール繊維状バインダーの繊維径は40μmであり、
坪量70g/m 2 、バインダー樹脂分5.8重量%のシ
ートを得た。
Example 2: Except that the wet paper has a water content of 70%
Example 1 was repeated. Polyvinyl acetate after sheet drying
The fiber diameter of the lucol fibrous binder is 40 μm,
Basis weight 70g / m 2, Binder resin content of 5.8% by weight
I got a card.

【0025】実施例3:ポリビニルアルコール繊維状バ
インダー(VPB101 クラレ(株)製:12.9μ
m×3mm)を6.0重量%とし、湿紙の水分を55%
にした以外は、実施例1を繰り返した。坪量70g/m
2 、バインダー樹脂分6.5重量%で、シート乾燥後の
ポリビニルアルコール繊維状バインダーの繊維径が1
4.2μmのシートを得た。
Example 3: Polyvinyl alcohol fibrous binder (VPB101 manufactured by Kuraray Co., Ltd .: 12.9 μm)
m x 3 mm) is 6.0% by weight, and the moisture content of the wet paper is 55%
Example 1 was repeated except that Basis weight 70g / m
2 , the binder resin content is 6.5% by weight, and the fiber diameter of the polyvinyl alcohol fibrous binder after sheet drying is 1
A 4.2 μm sheet was obtained.

【0026】実施例4:ポリビニルアルコール繊維状バ
インダー(VPB101、クラレ(株)製、12.9μ
m×3mm)を6.0重量%とし、湿紙の水分を70%
とした以外は実施例2を繰り返した。坪量70g/
2 、バインダー樹脂分6.8重量%のシートを得た。
シート乾燥後のポリビニルアルコール繊維状バインダー
の繊維径が88.7μmのシートを得た。
Example 4: Polyvinyl alcohol fibrous binder (VPB101, manufactured by Kuraray Co., Ltd., 12.9 μm)
m × 3 mm) is 6.0% by weight, and the moisture content of the wet paper is 70%
Example 2 was repeated except that Basis weight 70g /
A sheet having m 2 and a binder resin content of 6.8% by weight was obtained.
A sheet having a fiber diameter of the polyvinyl alcohol fibrous binder after drying the sheet was 88.7 μm was obtained.

【0027】比較例1:平均繊維径6μm以下の極細ガ
ラス繊維90重量%とチョップドガラス繊維10重量%
及び対濾材重量0.5重量%のポリビニルアルコール繊
維状バインダー(SPG 056、クラレ(株)製、
7.3μm×3mm)をパルパーにて、pH3.5の酸
性水を用いて離解し、水性スラリーを作成して、これら
のスラリーから標準角型手抄き抄紙機を用いて、シート
を形成した。これにアクリル系ラテックス(SFA−3
3、大日本インキ(株)製)を湿紙に付与し、湿紙の水
分を35%とし、その後130℃のロータリードライヤ
ーで一気に乾燥し、坪量70g/m2 、バインダー樹脂
分6.1重量%で、シート乾燥後のポリビニルアルコー
ル繊維状バインダーの繊維径が7.3μmのシートを得
た。
Comparative Example 1: 90% by weight of ultrafine glass fibers having an average fiber diameter of 6 μm or less and 10% by weight of chopped glass fibers
And polyvinyl alcohol fibrous binder (SPG 056, manufactured by Kuraray Co., Ltd.
(7.3 μm × 3 mm) was disaggregated with a pulper using acidic water having a pH of 3.5 to prepare an aqueous slurry, and a sheet was formed from these slurries using a standard square handmade paper machine. . Acrylic latex (SFA-3
3, Dainippon Ink and Co., Ltd.) was applied to the wet paper, the moisture content of the wet paper was set to 35%, and then it was dried at once with a rotary dryer at 130 ° C., the basis weight was 70 g / m 2 , and the binder resin content was 6.1. By weight%, a sheet having a fiber diameter of the polyvinyl alcohol fibrous binder after sheet drying of 7.3 μm was obtained.

【0028】比較例2:平均繊維径6μm以下の極細ガ
ラス繊維90重量%とチョップドガラス繊維10重量%
及び対濾材重量6.0重量%のポリビニルアルコール繊
維状バインダー(SPG 056、クラレ(株)製、
7.3μm×3mm)をパルパーにて、pH3.5の酸
性水を用いて離解し、水性スラリーを作成して、これら
のスラリーから標準角型手抄き抄紙機を用いて、シート
を形成した。これにアクリル系ラテックス(SFA−3
3、大日本インキ(株)製)を湿紙に付与し、湿紙の水
分を95%とし、その後130℃のロータリードライヤ
ーで一気に乾燥し、坪量70g/m2 、バインダー樹脂
分6.8重量%で、シート乾燥後のポリビニルアルコー
ル繊維状バインダーが、繊維形態をなしていないシート
を得た。
Comparative Example 2: 90% by weight of ultrafine glass fibers having an average fiber diameter of 6 μm or less and 10% by weight of chopped glass fibers
And a polyvinyl alcohol fibrous binder (SPG 056 manufactured by Kuraray Co., Ltd.
(7.3 μm × 3 mm) was disaggregated with a pulper using acidic water having a pH of 3.5 to prepare an aqueous slurry, and a sheet was formed from these slurries using a standard square handmade paper machine. . Acrylic latex (SFA-3
3, Dainippon Ink and Chemicals, Inc.) was applied to the wet paper, the wet paper had a water content of 95%, and then dried at once with a rotary dryer at 130 ° C., the basis weight was 70 g / m 2 , and the binder resin content was 6.8. By weight%, a sheet was obtained in which the polyvinyl alcohol fibrous binder after sheet drying was not in fibrous form.

【0029】比較例3:湿紙の水分を35%とした以外
は実施例3を繰り返した。シート乾燥後のポリビニルア
ルコール繊維状バインダーの繊維径は13μmであり、
得られるシートは坪量70g/m2 で、バインダー樹脂
分6.7重量%であった。
Comparative Example 3: Example 3 was repeated except that the moisture content of the wet paper was 35%. The fiber diameter of the polyvinyl alcohol fibrous binder after sheet drying is 13 μm,
The resulting sheet had a basis weight of 70 g / m 2 and a binder resin content of 6.7% by weight.

【0030】比較例4:湿紙の水分を90%とした以外
は実施例3を繰り返した。シート乾燥後のポリビニルア
ルコール繊維状バインダーは繊維形態をなしていない。
得られたシートは坪量70g/m2 で、バインダー樹脂
分6.9重量%であった。
Comparative Example 4: Example 3 was repeated except that the wet paper had a water content of 90%. The polyvinyl alcohol fibrous binder after sheet drying is not in fiber form.
The obtained sheet had a basis weight of 70 g / m 2 and a binder resin content of 6.9% by weight.

【0031】比較例5:平均繊維径6μm以下の極細ガ
ラス繊維90重量%とチョップドガラス繊維10重量%
及び対濾材重量11.0重量%のポリビニルアルコール
繊維状バインダー(SPG 056、クラレ(株)製、
7.3μm×3mm)をパルパーにて、pH3.5の酸
性水を用いて離解し、水性スラリーを作成して、これら
のスラリーから標準角型手抄き抄紙機を用いて、シート
を形成した。これにアクリル系ラテックス(SFA−3
3、大日本インキ(株)製)を湿紙に付与し、湿紙の水
分を55%とし、その後130℃のロータリードライヤ
ーで一気に乾燥し、坪量70g/m2 、バインダー樹脂
分13.0重量%で、シート乾燥後のポリビニルアルコ
ール繊維状バインダーの繊維径が8.1μmのシートを
得た。
Comparative Example 5: 90% by weight of ultrafine glass fibers having an average fiber diameter of 6 μm or less and 10% by weight of chopped glass fibers
And a polyvinyl alcohol fibrous binder (SPG 056 manufactured by Kuraray Co., Ltd.
(7.3 μm × 3 mm) was disaggregated with a pulper using acidic water having a pH of 3.5 to prepare an aqueous slurry, and a sheet was formed from these slurries using a standard square handmade paper machine. . Acrylic latex (SFA-3
3, Dainippon Ink and Co., Ltd.) was applied to the wet paper to make the wet paper have a water content of 55%, and then dried at once with a rotary dryer at 130 ° C., a basis weight of 70 g / m 2 , and a binder resin content of 13.0. By weight%, a sheet having a fiber diameter of the polyvinyl alcohol fibrous binder after drying the sheet of 8.1 μm was obtained.

【0032】シート物性を表1にまとめて示す。The physical properties of the sheet are summarized in Table 1.

【0033】[0033]

【表1】 [Table 1]

【0034】上記実施例1〜4で示した濾材は、ガーレ
ー剛度ならびに剥離強度が高く、圧力損失の上がりも少
なく、プリーツ加工特性が良好なエアーフィルター用濾
材であった。
The filter media shown in Examples 1 to 4 were air filter media having high Gurley rigidity and peel strength, little increase in pressure loss, and good pleating characteristics.

【0035】比較例1では、圧力損失は上昇していない
が、ガーレー剛度、剥離強度が低く、ひだ折プリーツ加
工適性が悪い。
In Comparative Example 1, the pressure loss did not increase, but the Gurley rigidity and peel strength were low, and the pleat pleating processability was poor.

【0036】比較例2では、圧力損失の上昇が著しく、
ガーレー剛度、剥離強度は低い。また、ひだ折プリーツ
加工適性が悪い。
In Comparative Example 2, the pressure loss increased remarkably,
Gurley stiffness and peel strength are low. Also, the pleat processing suitability for pleat folding is poor.

【0037】比較例3では、圧力損失は上昇していない
が、ガーレー剛度、剥離強度は低い。また、ひだ折プリ
ーツ加工適性が悪い。
In Comparative Example 3, the pressure loss did not increase, but the Gurley rigidity and peel strength were low. Also, the pleat processing suitability for pleat folding is poor.

【0038】比較例4では、圧力損失の上昇が著しく、
ガーレー剛度、剥離強度が低い。また、ひだ折プリーツ
加工適性が悪い。
In Comparative Example 4, the pressure loss increased remarkably,
Gurley stiffness and peel strength are low. Also, the pleat processing suitability for pleat folding is poor.

【0039】比較例5では、圧力損失の上昇が激しく、
ガーレー剛度、剥離強度は高い。また、ひだ折プリーツ
加工適性が悪い。
In Comparative Example 5, the pressure loss increased sharply,
Gurley rigidity and peel strength are high. Also, the pleat processing suitability for pleat folding is poor.

【0040】[0040]

【発明の効果】本発明は、エアフィルタ用濾材につい
て、内添法におけるポリビニルアルコール繊維状バイン
ダーの溶融の度合いを制御することにより、エアフィル
タ用濾材としての適性を損なうことのない、新規な濾材
を提供するものである。
INDUSTRIAL APPLICABILITY The present invention relates to a filter medium for air filters, which is a novel filter medium which does not impair its suitability as a filter medium for air filters by controlling the degree of melting of the polyvinyl alcohol fibrous binder in the internal addition method. Is provided.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 楚山 智彦 新潟県長岡市西蔵王三丁目五番一号 北越 製紙株式会社研究所内 Fターム(参考) 4D019 AA01 BA04 BB03 CB06 DA10 4L047 AA05 BA09 BA21 BB03    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Tomohiko Soyama             3-5-1, Nishi-Zao, Nagaoka-shi, Niigata Hokuetsu             Research Institute of Paper Manufacturing Co., Ltd. F-term (reference) 4D019 AA01 BA04 BB03 CB06 DA10                 4L047 AA05 BA09 BA21 BB03

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 坪量25〜150g/m2 の不織布から
なるエアフィルタ用濾材において、構成繊維を接着させ
るポリビニルアルコール繊維状バインダーが完全溶解す
ることなく繊維形態を保持しながら膨潤し、濾材の厚さ
方向に均一に存在していることを特徴とする、エアフィ
ルタ用濾材。
1. A filter medium for an air filter comprising a nonwoven fabric having a basis weight of 25 to 150 g / m 2 , wherein the polyvinyl alcohol fibrous binder for adhering the constituent fibers swells while maintaining the fiber morphology without being completely dissolved. A filter medium for an air filter, characterized by being uniformly present in the thickness direction.
【請求項2】 請求項1の膨潤後のポリビニルアルコー
ル繊維状バインダーの繊維径が7.5〜110μmであ
る、請求項1に記載のエアフィルタ用濾材。
2. The filter medium for an air filter according to claim 1, wherein the swollen polyvinyl alcohol fibrous binder according to claim 1 has a fiber diameter of 7.5 to 110 μm.
【請求項3】 請求項1の膨潤後のポリビニルアルコー
ル繊維状バインダーの繊維径が、膨潤前の繊維径の1.
1〜7倍である、請求項1記載のエアフィルタ用濾材。
3. The fiber diameter of the polyvinyl alcohol fibrous binder after swelling according to claim 1 is 1.
The filter material for an air filter according to claim 1, which is 1 to 7 times.
【請求項4】 濾材中のポリビニルアルコール繊維状バ
インダーが、濾材重量を基準として0.1〜10重量%
である、請求項1〜3のいずれか一つに記載のエアフィ
ルタ用濾材。
4. The polyvinyl alcohol fibrous binder in the filter medium is 0.1 to 10% by weight based on the weight of the filter medium.
The filter material for an air filter according to any one of claims 1 to 3, which is
【請求項5】 エアフィルタ用濾材がガラス繊維を主体
とした不織布である請求項1〜4のいずれか一つに記載
のエアフィルタ用濾材。
5. The filter medium for an air filter according to claim 1, wherein the filter medium for an air filter is a non-woven fabric mainly composed of glass fibers.
【請求項6】 請求項1〜5のいずれか一つに記載のエ
アフィルター用濾材を製造する方法において、原料繊維
を水中でスラリー化し、このスラリー化工程の際にポリ
ビニルアルコール繊維状バインダーを添加し、得られる
スラリーを抄紙機で抄紙し、50〜80重量%の含水率
の湿紙を形成しそして乾燥することを特徴とする、上記
方法。
6. The method for producing a filter medium for an air filter according to claim 1, wherein raw material fibers are slurried in water, and a polyvinyl alcohol fibrous binder is added during the slurrying step. Then, the resulting slurry is subjected to papermaking with a paper machine to form a wet paper having a water content of 50 to 80% by weight and drying.
JP2001361016A 2001-11-27 2001-11-27 Air filter media Expired - Fee Related JP3848139B2 (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62110718A (en) * 1985-10-16 1987-05-21 Kuraray Co Ltd Filter material for air filter
JPH05261224A (en) * 1992-03-23 1993-10-12 Hokuetsu Paper Mills Ltd Filter material for air filter
JPH06285315A (en) * 1993-04-06 1994-10-11 Nippon Sheet Glass Co Ltd Deodorizing antibacterial filter paper
JPH10212683A (en) * 1997-01-29 1998-08-11 Tennex:Kk Production of filter medium

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62110718A (en) * 1985-10-16 1987-05-21 Kuraray Co Ltd Filter material for air filter
JPH05261224A (en) * 1992-03-23 1993-10-12 Hokuetsu Paper Mills Ltd Filter material for air filter
JPH06285315A (en) * 1993-04-06 1994-10-11 Nippon Sheet Glass Co Ltd Deodorizing antibacterial filter paper
JPH10212683A (en) * 1997-01-29 1998-08-11 Tennex:Kk Production of filter medium

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Publication number Publication date
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