JP2000308805A - Filter paper for air filter and its production - Google Patents

Filter paper for air filter and its production

Info

Publication number
JP2000308805A
JP2000308805A JP11902799A JP11902799A JP2000308805A JP 2000308805 A JP2000308805 A JP 2000308805A JP 11902799 A JP11902799 A JP 11902799A JP 11902799 A JP11902799 A JP 11902799A JP 2000308805 A JP2000308805 A JP 2000308805A
Authority
JP
Japan
Prior art keywords
filter
paper
binder
filter paper
glass fibers
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.)
Pending
Application number
JP11902799A
Other languages
Japanese (ja)
Inventor
Hiroshi Matsuoka
博 松岡
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 Sheet Glass Co Ltd
Original Assignee
Nippon Sheet Glass 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 Sheet Glass Co Ltd filed Critical Nippon Sheet Glass Co Ltd
Priority to JP11902799A priority Critical patent/JP2000308805A/en
Publication of JP2000308805A publication Critical patent/JP2000308805A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To prevent the formation of the film of a binder containing a thermosensitive solidification type resin in the surface layer part of filter paper for an air filter and to improve a dust holding capacity by bonding glass fibers by using the binder. SOLUTION: The glass fibers of the filter paper for the air filter are bonded by using the thermosensitive solidification type resin binder. An aqueous slurry is first prepared by dispersing the glass fibers into water and papermaking of the aqueous slurry is executed by a wet papermaking process, by which wet paper is obtained. Next, the thermosensitive solidification type resin binder is adhered to the wet paper and is then dried. At this time, the concentration of the thermosensitive solidification type resin binder liquid in an emulsion is preferably 0.1 to 10 wt.%. Dimethyl polysiloxane may be incorporated at 0.05 to 0.5 wt.% into the binder liquid in order to impart water repellence thereto at need. Further, the content of the thermosensitive solidification type resin in the filter paper after drying is preferably 1 to 10 wt.%.

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】本発明はエアフィルター用濾
紙、特に粉塵保持容量に優れたエアフィルター用の濾紙
およびその製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter paper for an air filter, and more particularly to a filter paper for an air filter having an excellent dust retention capacity and a method for producing the same.

【0002】[0002]

【従来の技術】電子精密工業などのクリーンルーム、バ
イオロジカルクリーンルーム、クリーンベンチなどの清
浄空間における空気中の浮遊微粒子の捕集には、エアフ
ィルター用濾紙が用いられている。このようなエアフィ
ルター用濾紙は一般に微細なガラス繊維を水中に分散さ
せて湿式抄紙した後、繊維の再飛散防止および加工時の
強度維持、その他の特性を付与させるために、樹脂溶液
または樹脂エマルジョン液中に浸漬処理し、その後乾燥
させることにより製造される。
2. Description of the Related Art Filter paper for an air filter is used for collecting airborne particulates in a clean space such as a clean room such as an electronic precision industry, a biological clean room, or a clean bench. Such filter paper for air filters is generally prepared by dispersing fine glass fibers in water and wet-making the paper.Then, in order to prevent re-scattering of the fibers and maintain strength during processing, and to impart other properties, a resin solution or resin emulsion is used. It is manufactured by immersing in a liquid and then drying.

【0003】上記樹脂バインダーとしては一般にアクリ
ル系樹脂、ウレタン系樹脂、ポリビニルアルコール系樹
脂あるいはエポキシ系樹脂を主剤として、ワックス、シ
リコンを助剤として添加したものが用いられ、その付着
量はガラス繊維に対して1〜10重量%である。
As the above resin binder, an acrylic resin, a urethane resin, a polyvinyl alcohol resin or an epoxy resin is used as a main component, and wax and silicon are added as assistants. On the other hand, it is 1 to 10% by weight.

【0004】フィルターの構成としては、一般に、目の
粗い方からプレフィルター、中間フィルター、HEPA
フィルターの順番にセットして濾過効率を良くしてい
る。ここで、中間フィルターに使用される濾紙に要求さ
れる性能は、濾過効率のほかに、捕集した粉塵の保持容
量(DHC:Dust Holding Capacitty)が重要視
される。
[0004] In general, a filter is composed of a pre-filter, an intermediate filter, a HEPA,
Filters are set in order to improve the filtration efficiency. Here, as for the performance required for the filter paper used for the intermediate filter, importance is attached to the retention capacity of the collected dust (DHC: Dust Holding Capacitty) in addition to the filtration efficiency.

【0005】中間フィルターのDHCを高める手段とし
て、 フィルターの厚み方向に繊維径の太さを順次変え、厚
み方向に密度勾配をつける。 繊維径の異なるシ−トを別々に抄紙して重ねる多層抄
紙法を採用する。 繊維交点の樹脂皮膜形成防止のためにカチオン性のエ
マルジョン性バインダーを使用する。(特開平9−14
1023) 等が提案されている。
As a means for increasing the DHC of the intermediate filter, the thickness of the fiber diameter is sequentially changed in the thickness direction of the filter, and a density gradient is provided in the thickness direction. A multilayer papermaking method is adopted in which sheets having different fiber diameters are separately made and stacked. A cationic emulsion binder is used to prevent the formation of a resin film at the fiber intersection. (JP-A-9-14
1023) has been proposed.

【0006】[0006]

【発明が解決しようとする課題】上記従来技術および
のフィルターの製造においては、バインダー樹脂エマ
ルジョンを含浸させた濾紙が乾燥されるときに、濾紙の
表面の温度が内部に比して高く表面で水の蒸発が激しく
起こるため、エマルジョン粒子が水の流れにつられて表
面に移動する結果、濾紙表層部に高い濃度で存在して、
さらに乾燥が進むとエマルジョン粒子が結合を開始し、
皮膜を形成する。すなわち表層部に皮膜ができることに
なるため、粉塵が表層部でのみ捕集されることになり、
濾紙の内層部で粉塵を保持しないようになってしまい、
フィルターの粉塵保持能力を低下させる原因になる。ま
た上記従来技術では、抄紙した濾紙に樹脂の皮膜を形
成させないようにするために、カチオン性のエマルジョ
ン性バインダーを使用しているが、樹脂皮膜形成の防止
は十分ではなく、DHCはそれほど高くない。
In the above-mentioned prior art and the production of the filter, when the filter paper impregnated with the binder resin emulsion is dried, the temperature of the surface of the filter paper is higher than that of the inside and the water on the surface is high. Because of the rapid evaporation of the emulsion particles, the emulsion particles move to the surface following the flow of water, and as a result, are present at a high concentration on the surface of the filter paper.
As the drying proceeds further, the emulsion particles start binding,
Form a film. That is, since a film will be formed on the surface layer, dust will be collected only on the surface layer,
The dust will not be retained in the inner layer of the filter paper,
This may cause a reduction in the filter's ability to retain dust. Further, in the above prior art, a cationic emulsion binder is used in order to prevent a resin film from being formed on the paper filter paper, but the prevention of resin film formation is not sufficient, and DHC is not so high. .

【0007】本発明は、表層部に形成されるバインダー
の皮膜の形成を防止して、粉塵保持容量の優れたエアフ
ィルター用濾紙を提供することを目的とする。
It is an object of the present invention to provide a filter paper for an air filter having an excellent dust retention capacity by preventing the formation of a binder film formed on a surface layer portion.

【0008】[0008]

【課題を解決するための手段】本発明の上記課題は次の
構成によって達成される。すなわち、本発明は感熱凝固
型樹脂バインダーを用いてガラス繊維を結合するエアフ
ィルター用濾紙である。
The above object of the present invention is achieved by the following constitution. That is, the present invention is a filter paper for an air filter, in which glass fibers are bound using a thermosetting resin binder.

【0009】本発明において、エアフィルター用濾紙は
次のようにして製造される。ガラス繊維を水中に分散さ
せて水性スラリーを調製し、湿式抄紙法によりこの水性
スラリーを用いて抄造して、湿紙を得る。用いるガラス
繊維は、0.1ないし2μmの平均直径を有するガラス
短繊維、および/または、0.3〜10μmの平均直径
を有するガラスフィラメントを数本〜数十本集束させ
て、数mmないし数cmの長さに切断したガラスチョッ
プドストランドが用いられ、これらの繊維の組成には、
特に制限はなく、例えばホウ珪酸ガラス、高シリカガラ
ス、Eガラスなどを用いる。
In the present invention, the filter paper for an air filter is manufactured as follows. An aqueous slurry is prepared by dispersing glass fibers in water, and papermaking is performed using this aqueous slurry by a wet papermaking method to obtain a wet paper. The glass fiber used is a glass short fiber having an average diameter of 0.1 to 2 μm and / or several to several tens of glass filaments having an average diameter of 0.3 to 10 μm. cm chopped strands cut into cm lengths are used, and the composition of these fibers is:
There is no particular limitation, and for example, borosilicate glass, high silica glass, E glass, or the like is used.

【0010】湿式抄紙をするに当たりスラリー中のガラ
ス繊維の分散性を良くするために、水に少量の酸を加
え、スラリーをpH2〜5程度とするのが好ましい。
In order to improve the dispersibility of the glass fibers in the slurry during wet papermaking, it is preferable to add a small amount of acid to water to adjust the pH of the slurry to about 2 to 5.

【0011】スラリーのpH調整に用いる酸としては、
塩酸、硫酸、硝酸などの無機酸が用いられ、その他に酢
酸などの有機酸も用いることができる。
As the acid used for adjusting the pH of the slurry,
Inorganic acids such as hydrochloric acid, sulfuric acid and nitric acid are used, and in addition, organic acids such as acetic acid can also be used.

【0012】次いで、得られた湿紙に感熱凝固型樹脂バ
インダーを付着させる。このバインダーの付着方法につ
いては、特に制限はなく、例えば湿紙を感熱凝固型樹
脂のエマルジョン液に浸せきし、余分に付着した樹脂を
吸引して取り除く、湿紙にエマルジョン液をスプレ−
により吹き付ける、等の方法が用いられる。
Next, a thermosetting resin binder is adhered to the obtained wet paper. The method of attaching the binder is not particularly limited. For example, a wet paper is immersed in an emulsion of a thermosetting resin, and the excess resin is removed by suction.
And the like.

【0013】ここでバインダーに用いる感熱凝固型樹脂
とは、エマルジョンの形で分散媒の中に分散している樹
脂粒子が加熱によりゲル状になるような熱可塑性または
熱硬化性樹脂であり(この加熱温度を曇点という)、樹
脂の種類としてはウレタン樹脂、アクリル樹脂、メタク
リル樹脂、ポリビニルアルコール樹脂、エポキシ樹脂な
どを挙げることができる。これらの中で感熱凝固型ポリ
ウレタン、例えば感熱凝固型ポリエーテル型ポリウレタ
ンが最も好ましく用いられ、感熱凝固型ポリエーテル型
ポリウレタンとしては例えば大日本インキ化学工業
(株)製 「ボンディック 1510」(分散媒;水、
固形分濃度40重量%)が市販されている。
Here, the thermosetting resin used as the binder is a thermoplastic or thermosetting resin in which resin particles dispersed in a dispersion medium in the form of an emulsion become gelled by heating. The heating temperature is referred to as the cloud point). Examples of the type of resin include urethane resin, acrylic resin, methacrylic resin, polyvinyl alcohol resin, and epoxy resin. Among these, a heat-coagulable polyurethane, for example, a thermo-coagulable polyether-type polyurethane is most preferably used. ;water,
(Solids concentration 40% by weight) is commercially available.

【0014】感熱凝固型樹脂バインダーはその曇点が比
較的に低いため、分散媒中に分散している樹脂粒子が、
比較的に低温度例えば約50℃で加熱されたときに、凝
固してゲル状になって湿紙を構成する繊維表面に付着す
るため、湿紙表面方向への分散媒(水)の移動とともに
移動するすることはなく、湿紙表層部での樹脂皮膜形成
が起こり難くなる。従って、バインダーは濾紙の厚み方
向にほぼ均一に分布した状態で、濾紙を構成するガラス
繊維同士を結合させており、粉塵が濾紙の内層部でも捕
集・保持されることになり、フィルターの粉塵保持能力
が高くなる。
Since the thermosetting coagulable resin binder has a relatively low cloud point, the resin particles dispersed in the dispersion medium are:
When heated at a relatively low temperature, for example, about 50 ° C., it solidifies and becomes gel-like and adheres to the surface of the fiber constituting the wet paper, so that the dispersion medium (water) moves toward the surface of the wet paper. It does not move, and the formation of the resin film on the surface layer portion of the wet paper web hardly occurs. Therefore, the binder binds the glass fibers constituting the filter paper in a state of being substantially uniformly distributed in the thickness direction of the filter paper, and the dust is collected and retained even in the inner layer portion of the filter paper, and the dust of the filter is removed. Retention capacity is increased.

【0015】感熱凝固型樹脂バインダー液のエマルジョ
ン中の濃度としては、0.1〜10重量%であることが
望ましい。濃度が0.1重量%未満では、湿紙への付着
率が悪くてガラス繊維同士を接合するに必要な樹脂量が
付着せず、10重量%を超えると、付着樹脂量は濃度1
0重量%のものと比較して差異はないがコスト高にな
る。バインダー液は上記感熱凝固型樹脂のほかに、必要
に応じて、撥水性をもたせるために、ジメチルポリシロ
キサンを0.05〜0.5重量%含有させることができ
る。
The concentration of the thermosetting resin binder liquid in the emulsion is desirably 0.1 to 10% by weight. If the concentration is less than 0.1% by weight, the adhering rate to wet paper is poor, and the amount of resin necessary for bonding glass fibers to each other does not adhere.
There is no difference compared to the case of 0% by weight, but the cost is high. The binder liquid may contain 0.05 to 0.5% by weight of dimethylpolysiloxane in order to impart water repellency, if necessary, in addition to the thermosetting resin.

【0016】このようして、湿紙を感熱凝固型のエマル
ジョンバインダーで処理した後は、これを加熱乾燥炉等
により乾燥する。乾燥は110〜250℃の温度で3〜
20分間とするのが望ましい。
After the wet paper is treated with the heat-sensitive coagulation type emulsion binder, the wet paper is dried by a heating drying oven or the like. Drying is performed at a temperature of 110 to 250 ° C for 3 to
Desirably, it is 20 minutes.

【0017】乾燥後の濾紙中の感熱凝固型樹脂の含有量
は、1〜10重量%であることが望ましい。含有量が1
重量%未満では繊維同士の接着が十分でなく濾紙の機械
的強度が低くなり、10重量%を超えると、粉塵保持容
量が低下する傾向があり、しかもコスト高になる。濾紙
の目付(単位面積当たりの重量)は通常は20〜200
g/m2である。
The content of the thermosetting resin in the dried filter paper is desirably 1 to 10% by weight. Content is 1
If the amount is less than 10% by weight, the fiber-to-fiber bonding is not sufficient, and the mechanical strength of the filter paper is low. If the amount exceeds 10% by weight, the dust holding capacity tends to decrease, and the cost increases. The basis weight (weight per unit area) of the filter paper is usually 20 to 200.
g / m 2 .

【0018】[0018]

【発明の実施の形態】以下、本発明の実施例および比較
例について説明する。 [実施例1]平均直径1μmのガラス短繊維、平均直径
2μmのガラス短繊維、および平均直径6μm長さ13
mmのガラスチョップドストランドをそれぞれ10重量
部、30重量部、および60重量部の割合で、pH4の
硫酸酸性の水中に分散させた後、抄紙機により湿式抄紙
した。得られた湿紙をバインダー液として下記表1に示
す重量組成のエマルジョン液に浸せきした後、吸引脱液
し、その後に140℃で10分間乾燥させた。得られた
紙の目付は64g/m2でバインダーの付着量は6重量%
であった。なお、感熱凝固型ポリエーテル型ポリウレタ
ンとして、大日本インキ化学工業(株)製 「ボンディ
ック 1510」(分散媒;水)を、ジメチルポリシロ
キサンとして、大日本インキ化学工業(株)製 「ディ
ック シリコン コンク」を使用した。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention and comparative examples will be described. Example 1 Short glass fibers having an average diameter of 1 μm, short glass fibers having an average diameter of 2 μm, and an average diameter of 6 μm and a length of 13
The glass chopped strands of 10 mm, 30 parts and 60 parts by weight were dispersed in sulfuric acid acidic water at a pH of 4, respectively, and then wet-laid with a paper machine. The obtained wet paper was immersed in an emulsion liquid having a weight composition shown in Table 1 below as a binder liquid, and was then suctioned and drained, and then dried at 140 ° C. for 10 minutes. The obtained paper has a basis weight of 64 g / m 2 and a binder adhesion amount of 6% by weight.
Met. In addition, "Bondick 1510" (dispersion medium: water) manufactured by Dainippon Ink and Chemicals, Ltd. is used as a thermo-coagulation type polyether polyurethane, and "Dick Silicon" manufactured by Dainippon Ink and Chemicals, Inc. is used as dimethylpolysiloxane. Conch "was used.

【0019】[0019]

【表1】 [Table 1]

【0020】[比較例1]実施例1で使用したバインダ
ー液に代えて下記表2に示す組成のものを使用した以外
は実施例1と同じ繊維配合、抄紙・乾燥方法により目付
64g/m2でバインダーの付着量6重量%の紙を得た。
なお、上記カチオン性アクリル酸エステル共重合物とは
アクリル酸エステルとカチオン変性アクリル酸エステル
とモノマーの共重合物であり、大日本インキ化学工業
(株)製の商品名「ボンコートSFCシリーズ」を使用
し、ジメチルポリシロキサンとしては実施例1と同じも
のを用いた。
[Comparative Example 1] The same fiber composition as in Example 1, except that the binder solution used in Example 1 was replaced with a composition shown in Table 2 below, and the basis weight was 64 g / m 2 by the papermaking / drying method. As a result, paper having a binder adhesion amount of 6% by weight was obtained.
The cationic acrylate copolymer is a copolymer of an acrylate ester, a cation-modified acrylate ester, and a monomer. The product name is “Boncoat SFC Series” manufactured by Dainippon Ink and Chemicals, Inc. The same dimethylpolysiloxane as in Example 1 was used.

【0021】[0021]

【表2】 [Table 2]

【0022】[比較例2]実施例1で使用したバインダ
ー液に代えて下記表3に示す組成のものを使用した以外
は実施例1と同じ繊維配合、抄紙・乾燥方法により目付
64g/m2でバインダーの付着量6重量%の紙を得た。
なお、上記アニオン性アクリル酸エステル共重合物とは
アクリル酸エステルとモノマーの共重合物であり、大日
本インキ化学工業(株)製の商品名「ボンコートR−3
020」を使用し、ジメチルポリシロキサンとしては実
施例1と同じものを用いた。
[Comparative Example 2] The same fiber composition as in Example 1, except that the binder solution used in Example 1 was replaced with a composition shown in Table 3 below, and the basis weight was 64 g / m 2 by the papermaking and drying method. As a result, paper having a binder adhesion amount of 6% by weight was obtained.
The anionic acrylate copolymer is a copolymer of an acrylate ester and a monomer, and is commercially available under the trade name “Boncoat R-3” manufactured by Dainippon Ink and Chemicals, Inc.
020 "and the same dimethylpolysiloxane as in Example 1.

【0023】[0023]

【表3】 [Table 3]

【0024】上記実施例と比較例で得られた濾紙につい
て、下記方法により圧力損失および捕集効率を測定し、
結果を表4に示す。 濾紙圧力損失(mmAq) 濾紙に通過風速5.3cm/秒で空気を通過させたとき
の通過抵抗をマノメーターにより測定した。 濾紙捕集効率(%) 平均粒子径約0.3μm程度のジオクチルフタレート
(DOP粒子)を発生させて濾紙を通過させ、濾紙の上
流側と下流側のDOP粒子の個数をレーザ・パーティク
ルカウンターで測定し、100×(下流側のDOP粒子
の個数)/(上流側のDOP粒子の個数)の値を捕集効
率(%)として算出した。
With respect to the filter papers obtained in the above Examples and Comparative Examples, pressure loss and collection efficiency were measured by the following methods.
Table 4 shows the results. Filter paper pressure loss (mmAq) The passage resistance when air was passed through the filter paper at a passing air velocity of 5.3 cm / sec was measured with a manometer. Filter paper collection efficiency (%) Dioctyl phthalate (DOP particles) having an average particle diameter of about 0.3 μm is generated and passed through the filter paper, and the number of DOP particles on the upstream and downstream sides of the filter paper is measured with a laser particle counter. Then, the value of 100 × (the number of DOP particles on the downstream side) / (the number of DOP particles on the upstream side) was calculated as the collection efficiency (%).

【0025】次いで、この濾紙を使用して外径寸法61
0×610×290mm、定格風量56m3/分、濾紙
面積10m2の中性能フィルターを組み立てて初期の圧
力損失、初期の捕集効率、および粉塵保持容量を測定
し、結果を表4に示す。
Next, using this filter paper, the outer diameter 61
A medium-performance filter of 0 × 610 × 290 mm, rated air volume of 56 m 3 / min, filter paper area of 10 m 2 was assembled, and the initial pressure loss, the initial collection efficiency, and the dust holding capacity were measured. The results are shown in Table 4.

【0026】フィルターの初期圧力損失(mmAq) フィルター定格風量56m3/分の空気を流して、初期
段階の圧力損失をマノメーターにより測定した。
Initial pressure loss of filter (mmAq) The air pressure of the filter was 56 m 3 / min, and the pressure loss at the initial stage was measured by a manometer.

【0027】フィルターの初期捕集効率(%) フィルターに定格風量(56m3/分)の空気を流し、
フィルター上流側空気に平均粒子径0.3μmのDOP
粒子を供給し、フィルターの上流側と下流側のDOP粒
子の個数をレーザ・パーティクルカウンターで測定し、
初期段階で、100×(下流側のDOP粒子の個数)/
(上流側のDOP粒子の個数)の値を捕集効率(%)と
して算出した。
Initial collection efficiency of filter (%) Air having a rated air flow (56 m 3 / min) is passed through the filter.
DOP with an average particle diameter of 0.3 μm in the air upstream of the filter
The particles are supplied, and the number of DOP particles on the upstream side and the downstream side of the filter is measured by a laser particle counter,
In the initial stage, 100 × (the number of DOP particles on the downstream side) /
The value of (the number of DOP particles on the upstream side) was calculated as the collection efficiency (%).

【0028】粉塵保持容量(g/m2) フィルターに定格風量(56m3/分)の空気を流し、
上流側からJIS15種ダストを70mg/m3の割合
で供給し続けて、圧力損失値が徐々に増加して30mmH
2Oに達したときのダスト付着量を単位濾紙面積(m2
当たりの重量(g)に換算した。
Dust holding capacity (g / m 2 ) Air with a rated air volume (56 m 3 / min) is passed through the filter.
Continue supplying JIS 15 class dust at a rate of 70 mg / m 3 from the upstream side, and the pressure loss value gradually increases to 30 mmH
The unit of filter paper area (m 2 )
Per unit weight (g).

【0029】[0029]

【表4】 ================================ 実施例1 比較例1 比較例2 −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 濾紙特性 圧力損失(初期) 2.8mmH2O 3.0mmH2O 3.2mmH2O 捕集効率(初期) 53% 52% 52% フィルター特性 初期圧力損失 12mmH2O 13mmH2O 13mmH2O 初期捕集効率 55% 53% 52% 粉塵保持容量 61g/m2 49g/m2 41g/m2 ================================[Table 4] ================================ Example 1 Comparative Example 1 Comparative Example 2 --------------------------- filter paper properties pressure loss (initial) 2.8mmH 2 O 3.0mmH 2 O 3.2mmH 2 O catching collecting efficiency (initial) 53% 52% 52% filter characteristic initial pressure loss 12mmH 2 O 13mmH 2 O 13mmH 2 O initial trapping efficiency of 55% 53% 52% dust retention capacity 61g / m 2 49g / m 2 41g / m 2 ===============================

【0030】表4の上記実施例と比較例を比較すると、
本発明の濾紙により製造したフィルターは比較例に比し
て粉塵保持容量が著しく大きいことがわかる。
Comparing the above example of Table 4 with the comparative example,
It can be seen that the filter produced by the filter paper of the present invention has a significantly higher dust retention capacity than the comparative example.

【0031】本発明のエアフィルター用の濾紙は空調装
置、半導体のクリーンルーム、バイオロジカルルーム、
病院の手術室、薬品工場の清浄工程、研究施設の清浄空
間などに用いる。
The filter paper for the air filter of the present invention is used for an air conditioner, a semiconductor clean room, a biological room,
Used in hospital operating rooms, cleaning processes in pharmaceutical factories, and clean spaces in research facilities.

【0032】[0032]

【発明の効果】本発明のエアフィルター用濾紙により、
圧力損失が小さく、捕集効率に優れ、粉塵保持容量の優
れたエアフィルターが得られる。
According to the filter paper for an air filter of the present invention,
An air filter with small pressure loss, excellent collection efficiency, and excellent dust retention capacity can be obtained.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) D21H 19/24 D21H 19/24 Z // C08J 5/04 CFF C08J 5/04 CFF (C08L 75/08 83:04) Fターム(参考) 4D019 AA01 BA04 BB05 BC20 CB06 4F072 AA02 AA07 AB09 AB15 AB31 AD43 AD47 AG02 AH03 AH31 AJ04 AK02 AL01 4J002 CK041 CP032 DL006 FA046 GD05 4L055 AF04 AG85 AG86 AG97 AH36 AH37 BE10 EA32 FA30 GA31──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) D21H 19/24 D21H 19/24 Z // C08J 5/04 CFF C08J 5/04 CFF (C08L 75/08 83 : 04) F term (reference) 4D019 AA01 BA04 BB05 BC20 CB06 4F072 AA02 AA07 AB09 AB15 AB31 AD43 AD47 AG02 AH03 AH31 AJ04 AK02 AL01 4J002 CK041 CP032 DL006 FA046 GD05 4L055 AF04 AG85 AG86 AG97 AH36 AH37 A3737H

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 感熱凝固型樹脂を含有するバインダーを
用いてガラス繊維を結合させたエアフィルター用濾紙。
1. A filter paper for an air filter, wherein glass fibers are bound using a binder containing a thermosetting resin.
【請求項2】 前記バインダーは、前記感熱凝固型樹脂
以外に、さらにジメチルポリシロキサンを含有する請求
項1記載のエアフィルター用濾紙。
2. The filter paper for an air filter according to claim 1, wherein the binder further contains dimethylpolysiloxane in addition to the thermosetting resin.
【請求項3】 前記バインダーは、 感熱凝固型ポリエーテル型ポリウレタン 0.1〜10重量%、 ジメチルポリシロキサン 0.05〜0.5重量%、および 水 残部 を含有する請求項2記載のエアフィルター用濾紙。3. The air filter according to claim 2, wherein the binder contains 0.1 to 10% by weight of thermosetting coagulated polyether type polyurethane, 0.05 to 0.5% by weight of dimethylpolysiloxane, and the balance of water. For filter paper. 【請求項4】 前記バインダーを、固形分で1〜10重
量%含有する請求項1〜3のいずれか1項に記載のエア
フィルター用濾紙。
4. The filter paper for an air filter according to claim 1, wherein the binder contains 1 to 10% by weight in solid content.
【請求項5】 ガラス繊維を水中に分散させて水性スラ
リーを調製し、湿式抄紙法によりこの水性スラリーを用
いて湿紙を抄造し、この湿紙に感熱凝固型樹脂を含有す
るバインダーを付着させ、その後に乾燥することを特徴
とするエアフィルター用濾紙の製造方法。
5. An aqueous slurry is prepared by dispersing glass fibers in water, a wet paper is formed by using the aqueous slurry by a wet papermaking method, and a binder containing a thermosetting resin is attached to the wet paper. And drying after that.
JP11902799A 1999-04-27 1999-04-27 Filter paper for air filter and its production Pending JP2000308805A (en)

Priority Applications (1)

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WO2004094724A1 (en) * 2003-04-22 2004-11-04 Oji Paper Co. Ltd. Wet-process nonwoven fabric and process for producing the same
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Publication number Priority date Publication date Assignee Title
WO2004094724A1 (en) * 2003-04-22 2004-11-04 Oji Paper Co. Ltd. Wet-process nonwoven fabric and process for producing the same
JP2006122856A (en) * 2004-10-29 2006-05-18 Nippon Muki Co Ltd Filter medium for drying oven, and filter for drying oven using it
JP2008194584A (en) * 2007-02-09 2008-08-28 Hokuetsu Paper Mills Ltd Filtering medium for air filter and its manufacturing method
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CN102899968A (en) * 2012-09-20 2013-01-30 蚌埠凤凰滤清器有限责任公司 Flame retardant air filter paper for automobile and preparation method thereof
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CN102899968B (en) * 2012-09-20 2015-12-09 安徽凤凰滤清器股份有限公司 A kind of flame retardant air filter paper for automobile and preparation method thereof
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CN102912685A (en) * 2012-09-25 2013-02-06 蚌埠凤凰滤清器有限责任公司 Preparation method of filter paper for air filter containing nano-porcelain clay
CN102912686A (en) * 2012-09-25 2013-02-06 蚌埠凤凰滤清器有限责任公司 Filter paper for air filter containing modified nano bamboo charcoal powder
CN102899970B (en) * 2012-09-25 2016-02-03 安徽凤凰滤清器股份有限公司 A kind of preparation technology of reed pulp filter paper
CN113289413A (en) * 2021-05-25 2021-08-24 九江市磐泰复合材料有限公司 Preparation method of high-capacity fluorine glass fiber filtering material
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