JPS6344916A - Manufacture of air filter paper - Google Patents

Manufacture of air filter paper

Info

Publication number
JPS6344916A
JPS6344916A JP18867786A JP18867786A JPS6344916A JP S6344916 A JPS6344916 A JP S6344916A JP 18867786 A JP18867786 A JP 18867786A JP 18867786 A JP18867786 A JP 18867786A JP S6344916 A JPS6344916 A JP S6344916A
Authority
JP
Japan
Prior art keywords
fiber
glass fiber
chopped strand
paper
binder
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
JP18867786A
Other languages
Japanese (ja)
Inventor
Osamu Inada
稲田 治
Ryoji Ito
伊藤 良二
Masanori Nishimoto
政典 西本
Noboru Takeshita
竹下 登
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.)
Sanyo Kokusaku Pulp Co Ltd
Original Assignee
Sanyo Kokusaku Pulp 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 Sanyo Kokusaku Pulp Co Ltd filed Critical Sanyo Kokusaku Pulp Co Ltd
Priority to JP18867786A priority Critical patent/JPS6344916A/en
Publication of JPS6344916A publication Critical patent/JPS6344916A/en
Pending legal-status Critical Current

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  • Paper (AREA)
  • Filtering Materials (AREA)

Abstract

PURPOSE:To carry out a neutral paper manufacturing and increase yield of superfine glass fiber by adding fiber-shaped vinylon binder to superfine glass fiber and chopped strand rayon fiber. CONSTITUTION:By using copped strand rayon fiber more hydrophilic than chopped strand glass fiber, paper can be manufactured by water. To enhance dispersing stability of superfine glass fiber and chopped strand rayon fiber in water, surface active agent or binder can be used. As both of fibers have no self-binding properties, fiber-shaped vinylon binder is added. The adding percentage is preferably 1-10%. By modifying the diameter of superfine glass fiber within a range of 0.3-4mum or changing blending ratio to 5-90 part, filtered paper of medium and high performance is manufactured.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は極細ガラス繊維とチョツプドストランド長繊維
とを主原料とし、内添バインダを用いて水にて湿式抄紙
するエアフィルタペーパーを製造する方法に関するもの
であり、更に詳しくは、’=Ji均繊維経繊維径3〜4
声の極細ガラス#a維とチョップトス1〜ランド・レー
ヨン繊維とを主原料とし、繊維状ビニロンバインダを内
添して用いることにより極細ガラス繊維の歩留りが良好
となるため、中性能用から超高性能用まで各種グレード
のエアフィルタに使用される炉材の製造を可能とするエ
アフィルタペーパーを製造する方法に関するものである
[Detailed Description of the Invention] [Industrial Application Field] The present invention manufactures air filter paper using ultrafine glass fibers and chopped strand long fibers as main raw materials and wet-paper-making with water using an internal binder. In more detail, '=Ji average fiber warp diameter 3 to 4.
By using Koe's ultra-fine glass #a fiber and Chop Toss 1~Rand Rayon fiber as the main raw materials, and using a fibrous vinylon binder internally, the yield of ultra-fine glass fiber is good, so it can be used for medium to ultra-high performance applications. The present invention relates to a method for producing air filter paper that enables the production of furnace materials used in air filters of various grades up to high performance.

〔従来の技術〕[Conventional technology]

エアフィルタのが材として使用されるフィルタペーパー
は、粉塵捕集率(以下捕集率と略す)に関与する極細ガ
ラス繊維と、引張強度に関す、するチョツプドストラン
ド・ガラス繊維とを主原料として湿式抄紙されているが
、ガラス表面の親水性が弱いため、その離解9分散性の
面から第19回紙パルプシンポジウム要旨集第9〜19
頁(1984年)などに見られる様に硫酸酸性水(pt
13.2以下)を用いて抄紙し、またガラス繊維Fこは
バルブの様な自己接着性が無いため、アクリル系のエマ
ルジョンバインダを湿紙に含浸し、ドライヤにて乾燥キ
ュアリングして製造されていた。
Filter paper, which is used as a material for air filters, is mainly made of ultra-fine glass fibers, which are responsible for the dust collection rate (hereinafter referred to as collection rate), and chopped strand glass fiber, which is responsible for the tensile strength. However, due to the weak hydrophilicity of the glass surface, the 19th Paper and Pulp Symposium Abstracts No. 9-19 due to its disintegration and dispersibility.
(1984), sulfuric acid acid water (pt.
13.2 or less), and since glass fiber F does not have self-adhesive properties like bulbs, it is manufactured by impregnating wet paper with an acrylic emulsion binder and drying and curing it in a dryer. was.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

湿紙抄紙に於いて硫酸酸性水を使用すると、作業の安全
性や装置の腐食性なとの問題の他に、捕集率に閏Ijす
る極細ガラス繊組゛の一部が溶解して歩留りが低下しエ
アフィルタペーパーとしての性能が悪くなるため、中性
にて湿式抄紙することが望ましい。
When sulfuric acid acid water is used in wet paper making, in addition to problems such as work safety and corrosiveness of equipment, part of the ultra-fine glass fibers, which affect the collection rate, dissolves and the yield rate decreases. It is desirable to perform wet paper making at neutrality, since the performance as an air filter paper decreases.

また、湿紙の状態で含浸法にてアクリル系のエマルジョ
ンバインダを添加すると、捕集率に関与する極細ガラス
繊維の一部が水置換時にシート中から抜けるために歩留
りが低下し、フィルタ性能が悪くなることかr)バイン
ダの選択を含め、効果的な添加方法の開発が必要となる
Additionally, if an acrylic emulsion binder is added to a wet paper using the impregnation method, some of the ultrafine glass fibers that are involved in the collection rate will come out of the sheet during water replacement, resulting in a decrease in yield and a decrease in filter performance. r) It is necessary to develop an effective addition method, including the selection of a binder.

〔問題点を解決するための手段及び作用〕之等の問題点
を解決すべく鋭意検討した結果、チョツプドストランド
・ガラス繊維に比べ、より親水性であるチョツプドスト
ランド・レーヨン繊維を用いることにより水による抄紙
が可能となることを見出した。なお必要に応じて極細ガ
ラス繊維と、チョツプドストランド・レーヨン繊維との
水中での離解2分散安定性を高めるために界面活性剤や
粘剤を併用してもよく、チョツプドストランド長繊維と
して、レーヨン繊維と共にビニロン繊維、アクリル繊維
、アセテ−1−繊維、銅アンモニア繊維などを併用して
もよい。
[Means and effects for solving the problems] As a result of intensive study to solve the problems, we decided to use chopped strand rayon fiber, which is more hydrophilic than chopped strand glass fiber. It was discovered that paper making using water becomes possible. If necessary, a surfactant or a sticky agent may be used in combination with the ultrafine glass fibers and chopped strand rayon fibers to enhance the dispersion stability in water. As such, vinylon fiber, acrylic fiber, acetate-1 fiber, copper ammonia fiber, etc. may be used in combination with rayon fiber.

また、極細ガラス繊維と共にチョップトス1−ランド・
レーヨン繊維にも自己接着性が無いため、バインダの使
用が必須となるが、繊維状ビニロンバインダを内添にて
用いると、従来行なっている含浸法に比べ、より少ない
バインダ量で同一引張強度が得られ、また極細ガラス繊
維の歩留りが向上することからフィルタ性能も良好とな
ることを見出した。なお、用いる繊維状ビニロンバイン
ダの添加率は1〜10%(対繊維)で、好ましくは3〜
6%である。添加率が1%未満では得られるシートの引
張強度が低く、一方、10%を超えると引張強度は高く
なるがフィルタ性能は極端に低下するために好ましくな
い。
In addition, chop toss 1-land with ultra-fine glass fiber.
Since rayon fibers do not have self-adhesive properties, it is essential to use a binder, but if a fibrous vinylon binder is added internally, the same tensile strength can be achieved with a smaller amount of binder than the conventional impregnation method. It has also been found that the filter performance is improved because the yield of ultrafine glass fibers is improved. The addition rate of the fibrous vinylon binder used is 1 to 10% (based on fibers), preferably 3 to 10% (based on fibers).
It is 6%. If the addition rate is less than 1%, the resulting sheet will have a low tensile strength, while if it exceeds 10%, the tensile strength will be high but the filter performance will be extremely deteriorated, which is not preferable.

また、水による中性の湿式抄紙法と、繊維状ビ二ロンバ
インダを内添法で用いることを組み合わせることにより
、捕集率に関与する極細ガラス繊維の歩留りを向」−さ
せることが可能となるため、用いる極細ガラス繊維の繊
維径を0.3〜4pに変えたり、或いはその配合割合を
5〜90部と変えることにより、中性能用から超高性能
用まで各種グレードのエアフィルタペーパーを造り分け
ることが可能となることも見出した。ここで極細ガラス
繊維の配合割合が5部以下ではシートにピンホールが多
■に生じて捕集率が確保出来ず、一方90部以1−では
シー1〜の引張強度が低くなるため好ましくない。
In addition, by combining the water-neutral wet papermaking method with the internal addition of a fibrous vinylon binder, it is possible to improve the yield of ultrafine glass fibers, which are involved in the collection rate. Therefore, by changing the fiber diameter of the ultra-fine glass fiber used to 0.3 to 4p, or by changing the blending ratio to 5 to 90 parts, various grades of air filter paper from medium performance to ultra high performance can be manufactured. We also found that it is possible to separate them. If the blending ratio of ultra-fine glass fiber is less than 5 parts, many pinholes will occur in the sheet, making it impossible to ensure the collection rate, while if it is more than 90 parts, the tensile strength of the sheet will decrease, which is undesirable. .

なお、本発明において撥水性を確保するための撥水剤や
、難燃性を確保するための難燃剤を使用しても何等支障
はない。
In the present invention, there is no problem in using a water repellent to ensure water repellency or a flame retardant to ensure flame retardancy.

〔実施例〕〔Example〕

本発明を更に詳述するために、次に具体例により説明す
る。
In order to further explain the present invention in detail, specific examples will now be described.

実施例】 44j $111ガラス繊維として商品名エバンス50
6 (0,54〜0.68Pφ)(エバンス社製)12
gに、チョツプドストランド・レーヨン繊維として商品
名コロナSB2×5(大和紡績社製)17.8 g (
固形分45%)と、繊維状ビニロンバインダとして商品
名SMM (ユニチカ化成社製0.2 g (固形分5
0%)をTAPPI離解機に入れ、水2Qを加えて30
秒間離解させた後、水8flを加え、商品名SV −5
38A型(高崎製作所製)の反転式アジタにて5分間撹
拌した。このスラリ液を得られるエアフィルタペーパー
の坪量が約75 g / rr?どなる様に採取し水を
加えて全量を4Qとし、反転式アジタにて3分間撹拌後
、自製の文型JIS式手抄装置(金網面積0.0191
f、目間75mesh)にてエアフィルタペーパーを抄
紙し、シリンダドライヤにて乾燥した後、目視により地
合を判定した。更にこのエアフィルタペーパーを商品名
アビノン101(三相ケミカル社製)にて難燃処理して
がら商品名TSW8251 (東芝シリコン社11)に
て撥水処理後、自製したフラットシート用フィルタペー
パー評価装置にてフィルタ性能を評価した。
Example] 44j $111 Glass fiber with trade name Evans 50
6 (0.54~0.68Pφ) (manufactured by Evans) 12
g, 17.8 g of chopped strand rayon fiber (trade name Corona SB2×5 (manufactured by Daiwabo Co., Ltd.)
solid content 45%) and a fibrous vinylon binder with the trade name SMM (manufactured by Unitika Kasei Co., Ltd., 0.2 g (solid content 5
0%) in the TAPPI disintegrator, add 2Q of water and boil for 30 minutes.
After disintegrating for seconds, 8 fl of water was added and the product name was SV-5.
The mixture was stirred for 5 minutes using a 38A type (manufactured by Takasaki Seisakusho) reversible agitator. Is the basis weight of the air filter paper from which this slurry liquid can be obtained approximately 75 g/rr? Collect the samples in a manner similar to that, add water to make a total volume of 4Q, stir for 3 minutes in an inverted agitator, and then use a self-made Bunkata JIS style hand paper machine (wire mesh area: 0.0191
After drying with a cylinder dryer, the texture was visually determined. This air filter paper was then flame-retardant treated with Avinon 101 (trade name, manufactured by Sansho Chemical Co., Ltd.) and water-repellent treated with TSW8251 (trade name, manufactured by Toshiba Silicon Co., Ltd.). The filter performance was evaluated.

比1鮫例1− ] ヂョツブ1〜ストラン1−・レーヨン繊維の代わりにチ
月ツブトストラン1く・ガラス繊維(9声φ〜に胴、力
11ファイバークラス社製)を8g用い、水の代オ)り
にpH2,5の硫酸酸性水を用いる以外は実施例1と同
様に行なった。
Ratio 1 Shark Example 1-] Instead of Jotsubu 1~Stran 1-/Rayon fiber, use 8g of Jiyotsubu Stran 1/Glass fiber (made by Fiber Class Co., Ltd. with a body of 9 φ~ and a force of 11), and use water instead of O. Example 1 was carried out in the same manner as in Example 1, except that sulfuric acid acidic water with a pH of 2.5 was used.

比較例1−2 水の代わりにpH2,5の硫酸水を用いた以外は実施例
1と同様に行なった。
Comparative Example 1-2 The same procedure as in Example 1 was carried out except that sulfuric acid water with a pH of 2.5 was used instead of water.

比較例1−1− 23Sを1.2に用いる代わりに0.3g用いた以外は
実施例1と同様に行なった。
Comparative Example 1-1- The same procedure as Example 1 was carried out except that 0.3 g of 23S was used instead of 1.2.

比較例】−4 5MMを1.2g用いる代わりに4.8g用いた以外は
実施例1と同様に行なった。
Comparative Example]-4 The same procedure as in Example 1 was carried out except that 4.8 g of 5MM was used instead of 1.2 g.

比、IR例1−1 一5Sを1.2g用いる代わりにスチレン・アクリル系
エマルジョンバインダである商品名5G−51−2(東
すli合成化学工業社製)1.5%水溶液を含浸法で用
いた以外は実施例1と同様に行なった。
Ratio, IR Example 1-1 Instead of using 1.2 g of 5S, a 1.5% aqueous solution of 5G-51-2 (trade name, manufactured by Tosuli Gosei Kagaku Kogyo Co., Ltd.), which is a styrene-acrylic emulsion binder, was used by an impregnation method. The same procedure as in Example 1 was carried out except that the following was used.

実施例2 極細ガラス繊維として商品名マンビル100(0,29
〜0 、327a++φ)(マンビル社製)4gと、チ
ョツプドストラン1−・レーヨン繊維コロナ5R2X5
(大和紡績社製)を35.6g用い、T A P P 
I離解機で1分間処理した以外は実施例】と同様に行な
った。
Example 2 Ultra-fine glass fiber with trade name Manville 100 (0.29
~0, 327a++φ) (manufactured by Manville) 4g and chopped strand 1-rayon fiber Corona 5R2X5
(manufactured by Daiwabo Co., Ltd.) using 35.6g, T A P
The same procedure as in Example 1 was carried out except that the mixture was treated with I disintegrator for 1 minute.

実施例3 極細ガラス繊維として商品名エバンス504 (0,3
!1〜0.531Jnφ)(エバンス社製)2gと、チ
ョップトスj−ランド・レーヨン繊維コロナ5B2x5
(大和紡績社製)を10g用いた以外は実施例1と同様
に行なった。
Example 3 Ultra-fine glass fiber with trade name Evans 504 (0,3
! 1~0.531Jnφ) (manufactured by Evans) 2g and Choptos J-Land Rayon Fiber Corona 5B2x5
The same procedure as in Example 1 was carried out except that 10 g of (manufactured by Daiwabo Co., Ltd.) was used.

比較例3−1 極細ガラス繊維としてエバンス504をO,Sgと、チ
ョップトスj−ランド・レーヨン繊維コロナ5112×
5を43.4 g用いた以外は実施例]と同様に行なっ
た。
Comparative Example 3-1 Evans 504 as ultra-fine glass fiber with O, Sg and Choptos J-Land Rayon Fiber Corona 5112×
The same procedure as in Example] was carried out except that 43.4 g of 5 was used.

実施例4 極細ガラス繊維として商品名エバンス510(2,5〜
4 /Jlφ)(エバンス社製)18gと、チョツプド
スフ− hランド・レーヨン繊維コロナ5R2X5(大和紡績礼
jJQ )を4.5g用いた以外は実施例1と同様に行
なった。
Example 4 As an ultrafine glass fiber, the trade name Evans 510 (2,5~
The same procedure as in Example 1 was conducted except that 18 g of Chopped Soft-H Land Rayon Fiber Corona 5R2X5 (Daiwa Boseki JJQ) was used.

比較例4−1 (41細ガラス[1としてエバンス510を19gと、
ヂョツプドス1〜ランド・レーヨン繊維コロナSR2×
5を2.3g用いた以外は実施例]と同様に行なった。
Comparative Example 4-1 (19 g of Evans 510 as 41 fine glass [1,
Jotupdos 1~Rand Rayon Fiber Corona SR2×
The same procedure as in Example] was carried out except that 2.3 g of No. 5 was used.

以下余白 −8= 有量BaG3−44916(4) 〔発明の効果〕 超高性能用エアフィルタペーパーの製造結果を表1に示
した。実施例1.実施例2に示した様に今回発明した方
法を用いれば圧力損失が低く、粉塵捕集率を表わす0.
37zm径DOPスモーク捕集率も、その規格である9
9.97%以上を充分に満足し、製品の引張強度もik
g/15mn以」−を確保した超高性能用エアフィルタ
ペーパーが製造出来る。一方、比較例]、−1に示した
様に、チョップトス1−ラン1〜・ガラス繊維を用い硫
酸酸性水で抄紙すると、0.3岬径DO11スモーク捕
集率が極端に低下して規格値以下となった。また、比較
例]−2に示した様しこチョツプドストラン1−・レー
ヨン繊維を用いても硫酸酸性水を用いて抄紙すると矢張
り0.37a径DOPスモーク捕集率が比較例1−1と
同様に低下して規格値以下となった。また比較例1−3
に示した様にチョツプドストランド・レーヨン繊維を用
いて水による中性抄紙をしても、繊維状ビニロンバイン
ダの添加率が適量範1f@以下になるとシートの引張強
度が極端に低下し、一方、比較例】−一4に示した様に
適量範囲以上になると、シー1−の引張強度は高くなる
ものの、フィルタ性能は高圧力損失、低捕集率となり、
極端に悪化する。また比較例]−−5に示した様に繊維
状ビニロンバインダを内添法にて用いる代わりにエマル
ジョンタイプのスチレン・アクリル系バインダを含浸法
で用いるとバインダ量が2倍で、はぼ同様な引張強度と
なるが、0.31An径DOPスモーク捕集率は低下し
た。
Below margin -8 = Abundant BaG3-44916 (4) [Effects of the invention] Table 1 shows the manufacturing results of the ultra-high performance air filter paper. Example 1. As shown in Example 2, if the method invented this time is used, the pressure loss is low and the dust collection rate is 0.
37zm diameter DOP smoke collection rate is also the standard 9
9.97% or more is fully satisfied, and the tensile strength of the product is also ik.
It is possible to manufacture ultra-high performance air filter paper that ensures g/15 mn or more. On the other hand, as shown in Comparative Example], -1, when paper was made using sulfuric acid acid water using chop toss 1-run 1~, the smoke collection rate of 0.3 cape diameter DO11 was extremely reduced to the standard value. It became the following. In addition, even if the similar chopped strand 1-rayon fiber shown in Comparative Example]-2 is used, when paper is made using sulfuric acid acid water, the DOP smoke collection rate of 0.37a diameter is lower than that of Comparative Example 1- As in 1, it decreased to below the standard value. Also, Comparative Example 1-3
As shown in Figure 2, even if chopped strand rayon fibers are used to make paper with water neutralization, when the addition rate of fibrous vinylon binder falls below the appropriate range of 1f@, the tensile strength of the sheet decreases extremely. On the other hand, as shown in Comparative Example]-1-4, when the amount exceeds the appropriate range, the tensile strength of Sea 1- becomes high, but the filter performance becomes high pressure loss and low collection rate.
becomes extremely worse. In addition, as shown in [Comparative Example]--5, if an emulsion type styrene/acrylic binder is used by the impregnation method instead of using the fibrous vinylon binder by the internal addition method, the binder amount is doubled and the same result is obtained. Although the tensile strength decreased, the 0.31 An diameter DOP smoke collection rate decreased.

次ぎに0.3戸径1〕OPスモーク捕集率が超高性能用
に比べて低い、中・高性能用エアフィルタペーパーの製
造結果を表2に示した。実施例3.実施例4に示した様
に今回発明した方法を用いれば超高性能用のみならす、
中・高性能用エアフィルタペーパーも製造出来た。但し
、比較例3−1に示した様に、極細ガラス繊維の配合が
5爪具ドになるとピンホールが多量に発生し、その結果
が0 、37nn径DOPスモーク捕集率が極端に悪化
する。また比較例4−1に示した様に、極細ガラス繊維
が90部爪具−1こなると、チョツプドストランド・レ
ーヨン繊維の配合効果が少なくなり、シー1〜の引張強
度が低くなった。
Next, Table 2 shows the manufacturing results of medium- to high-performance air filter paper, which has a 0.3 door diameter 1] OP smoke collection rate lower than that of ultra-high-performance paper. Example 3. As shown in Example 4, if the method invented this time is used, it can be used not only for ultra-high performance.
We were also able to produce air filter paper for medium and high performance. However, as shown in Comparative Example 3-1, when the blend of ultra-fine glass fibers becomes 5-jaw, a large number of pinholes occur, resulting in an extremely poor collection rate of 0 and 37 nn diameter DOP smoke. . Furthermore, as shown in Comparative Example 4-1, when 90 parts of ultrafine glass fiber were used in Claw-1, the blending effect of the chopped strand rayon fiber was reduced, and the tensile strength of C-1 was lowered.

以」−の様に平均繊維径が0.3〜4声の極細ガラス繊
細とチョツプドストランド・レーヨン繊維とを主原料と
し、繊維状ビニロンバインダを内添にて用いることによ
り水による中性抄紙が可能となり、しかも、極細ガラス
繊維の歩留りが良好となるため中性能用から超高性能用
まで各種グレードのエアフィルタペーパーの製造か可能
となった。
As shown in the figure below, the main raw materials are ultra-fine glass fibers with an average fiber diameter of 0.3 to 4 tones and chopped strand rayon fibers, and by internally adding a fibrous vinylon binder, it is neutralized by water. Paper making has become possible, and the yield of ultra-fine glass fibers has been improved, making it possible to manufacture various grades of air filter paper from medium to ultra-high performance.

特許出願人 山陽閤策パルプ株式会社 −】2− 手続補正書 昭和62年6ノ13 日 特許庁長官 黒1)明alt  殿 1、事件の表示 特願昭61−188677壮 2、発明の名称 エアフィルタペーパーを製造する方法 3、補正をする者 事件との関係  特許出願人 住所 東京都千代田区丸の内1−4−5名称 (23/
l)山陽国策バルブ株式会社取締役社長 那 須  忠
 己 4、代理人〒1. OO 住所 東京都千代田区丸の内1−4.−5永楽ビJl/
234号室電話214−286]番■氏名 (701,
0)弁理士 野 間  忠 之、−m−\、 6、補正の対象 明細書の発明の詳細な説明の欄 7、補IT:、の内容 明細11)中の下記の諸点を補正致します。
Patent applicant: Sanyo Konsaku Pulp Co., Ltd. -] 2 - Procedural amendment June 13, 1988 Commissioner of the Japan Patent Office Black 1) Akira Alt 1, Indication of the case Patent application 188677 So 2, Name of the invention Air Method for manufacturing filter paper 3, relationship with the amended case Patent applicant address 1-4-5 Marunouchi, Chiyoda-ku, Tokyo Name (23/
l) Sanyo Kokusaku Valve Co., Ltd. President and CEO Tadami Nasu 4, Agent 〒1. OO Address 1-4 Marunouchi, Chiyoda-ku, Tokyo. -5 Eiraku Bi Jl/
Room 234 Telephone 214-286] Number ■ Name (701,
0) Patent Attorney Tadayuki Noma, -m-\, 6. We will amend the following points in Column 7 of the detailed explanation of the invention of the specification subject to amendment, Supplementary IT: 11).

(1)第2頁第16行目 [要旨年第9〜19頁」とあるを [要旨集9〜19頁jと補正致します。(1) Page 2, line 16 [Summary page 9-19] [Corrected as abstract page 9-19 j.

(2)第3頁第73行口 「湿紙抄紙」とあるを 「湿式抄紙」と補正致します。(2) Page 3, line 73 It says "wet paper making" We will correct it to "wet paper making".

(:3)第4頁第1行目 「レーヨン繊維との」とあるを 「レーヨン繊維の」と補iE致します。(:3) Page 4, 1st line It says "with rayon fiber" I would like to add "rayon fiber".

(4)第12頁第16行[I [その結果が0.3prnJとあるを [その結果0.37sJ と補iTE致します。(4) Page 12, line 16 [I [The result is 0.3 prnJ] [The result will be 0.37sJ.

−よ−-Yo-

Claims (1)

【特許請求の範囲】 1 平均繊維径が0.3〜4μmの極細ガラス繊維とチ
ョップドストランド・レーヨン繊維とを主原料とし、繊
維状ビニロンバインダを対繊維1〜10%内添し中性で
湿式抄紙することを特徴とするエアフィルタペーパーを
製造する方法。 2 極細ガラス繊維とチョップドストランド・レーヨン
繊維との配合割合が5:95〜90:10である特許請
求の範囲第1項記載のエアフィルタペーパーを製造する
方法。
[Claims] 1. Ultrafine glass fibers with an average fiber diameter of 0.3 to 4 μm and chopped strand rayon fibers are the main raw materials, and a fibrous vinylon binder is added internally to the fibers in an amount of 1 to 10%, and a neutral wet process is performed. A method for producing air filter paper, which comprises paper-making. 2. The method for producing air filter paper according to claim 1, wherein the blending ratio of ultrafine glass fibers and chopped strand rayon fibers is 5:95 to 90:10.
JP18867786A 1986-08-13 1986-08-13 Manufacture of air filter paper Pending JPS6344916A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18867786A JPS6344916A (en) 1986-08-13 1986-08-13 Manufacture of air filter paper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18867786A JPS6344916A (en) 1986-08-13 1986-08-13 Manufacture of air filter paper

Publications (1)

Publication Number Publication Date
JPS6344916A true JPS6344916A (en) 1988-02-25

Family

ID=16227913

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18867786A Pending JPS6344916A (en) 1986-08-13 1986-08-13 Manufacture of air filter paper

Country Status (1)

Country Link
JP (1) JPS6344916A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09103624A (en) * 1995-10-12 1997-04-22 Nippon Glass Fiber Co Ltd Filter medium for air filter and its manufacture
JP2007090292A (en) * 2005-09-30 2007-04-12 Hokuetsu Paper Mills Ltd Non-flammable filtration material for dust removal filter and production method thereof
JP2008246321A (en) * 2007-03-29 2008-10-16 Hokuetsu Paper Mills Ltd Filter medium for dust removing air filter and its manufacturing method
CN102877368A (en) * 2012-09-20 2013-01-16 蚌埠凤凰滤清器有限责任公司 High temperature resistant flame retardant filter paper used for diesel filter and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54153383A (en) * 1978-05-24 1979-12-03 Koken Kk Preparation of air filter with highhperformance
JPS5562215A (en) * 1978-10-26 1980-05-10 Kuraray Co Ltd Polyvinyl alcohol binder fiber and its production
JPS60231816A (en) * 1984-04-27 1985-11-18 Kuraray Co Ltd Polyvinyl alcohol-based binder fiber and its manufacture

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54153383A (en) * 1978-05-24 1979-12-03 Koken Kk Preparation of air filter with highhperformance
JPS5562215A (en) * 1978-10-26 1980-05-10 Kuraray Co Ltd Polyvinyl alcohol binder fiber and its production
JPS60231816A (en) * 1984-04-27 1985-11-18 Kuraray Co Ltd Polyvinyl alcohol-based binder fiber and its manufacture

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09103624A (en) * 1995-10-12 1997-04-22 Nippon Glass Fiber Co Ltd Filter medium for air filter and its manufacture
JP2007090292A (en) * 2005-09-30 2007-04-12 Hokuetsu Paper Mills Ltd Non-flammable filtration material for dust removal filter and production method thereof
JP2008246321A (en) * 2007-03-29 2008-10-16 Hokuetsu Paper Mills Ltd Filter medium for dust removing air filter and its manufacturing method
CN102877368A (en) * 2012-09-20 2013-01-16 蚌埠凤凰滤清器有限责任公司 High temperature resistant flame retardant filter paper used for diesel filter and preparation method thereof

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