JPS6344915A - Manufacture of air filter paper - Google Patents
Manufacture of air filter paperInfo
- Publication number
- JPS6344915A JPS6344915A JP18867686A JP18867686A JPS6344915A JP S6344915 A JPS6344915 A JP S6344915A JP 18867686 A JP18867686 A JP 18867686A JP 18867686 A JP18867686 A JP 18867686A JP S6344915 A JPS6344915 A JP S6344915A
- Authority
- JP
- Japan
- Prior art keywords
- fiber
- chopped strand
- glass fiber
- paper
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 10
- 239000003365 glass fiber Substances 0.000 claims abstract description 32
- 239000011230 binding agent Substances 0.000 claims abstract description 19
- 229920002972 Acrylic fiber Polymers 0.000 claims abstract description 18
- 239000000835 fiber Substances 0.000 claims abstract description 15
- 229920002978 Vinylon Polymers 0.000 claims abstract description 12
- 238000002156 mixing Methods 0.000 claims abstract description 5
- 230000007935 neutral effect Effects 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 21
- 239000002994 raw material Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 20
- 239000004094 surface-active agent Substances 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 15
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 10
- 239000000779 smoke Substances 0.000 description 6
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 238000005470 impregnation Methods 0.000 description 4
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- HMUNWXXNJPVALC-UHFFFAOYSA-N 1-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)C(CN1CC2=C(CC1)NN=N2)=O HMUNWXXNJPVALC-UHFFFAOYSA-N 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 2
- WZFUQSJFWNHZHM-UHFFFAOYSA-N 2-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)CC(=O)N1CC2=C(CC1)NN=N2 WZFUQSJFWNHZHM-UHFFFAOYSA-N 0.000 description 2
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 2
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003063 flame retardant Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000005871 repellent Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 101100313164 Caenorhabditis elegans sea-1 gene Proteins 0.000 description 1
- 101000825841 Homo sapiens Vacuolar-sorting protein SNF8 Proteins 0.000 description 1
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 102100022787 Vacuolar-sorting protein SNF8 Human genes 0.000 description 1
- 229920006221 acetate fiber Polymers 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229920005822 acrylic binder Polymers 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- QKSIFUGZHOUETI-UHFFFAOYSA-N copper;azane Chemical compound N.N.N.N.[Cu+2] QKSIFUGZHOUETI-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- FWFGVMYFCODZRD-UHFFFAOYSA-N oxidanium;hydrogen sulfate Chemical compound O.OS(O)(=O)=O FWFGVMYFCODZRD-UHFFFAOYSA-N 0.000 description 1
- 239000002964 rayon Substances 0.000 description 1
- 230000002940 repellent Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920001909 styrene-acrylic polymer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
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のHa方法に関するものであ
り、更に詳しくは、qz均織繊維径0.3〜4μmの極
細ガラス繊維とチョップドストランド・アクリル繊維と
を主原料とし、In II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
ィルタペーパーの製造方法に関するものである。Detailed Description of the Invention [Industrial Field of Application] The present invention is an air filter paper that uses ultrafine glass fibers and chopped strand long fibers as main raw materials and is wet-paper-made using water using an internal binder. This article relates to the method, and more specifically, the main raw materials are ultrafine glass fibers with a qz uniform fiber diameter of 0.3 to 4 μm and chopped strand acrylic fibers, and by using an In II type vinylon binder internally added. 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 from medium performance to ultra-high performance because the yield of glass fiber is good.
エアフィルタの炉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、引張強度に関与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2分散性の面
から第19回紙バルブシンポジウム要旨集第9〜19頁
0984年)などに見られる様しこ硫酸酸性水(pH3
,2以下)を用いて抄紙し、またガラス繊維にはバルブ
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ユアリ
ングして製造されていた。The filter paper used as the furnace 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 fibers, which are responsible for the tensile strength. Although it is wet paper-made,
Because the hydrophilicity of the glass surface is weak, due to its dispersion and dispersion properties, sulfuric acid acidic water (pH 3
.
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どの問題の他に、捕集率に関与する
極細ガラス繊維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, some of the ultrafine glass fibers that are involved in the collection rate dissolve, reducing the yield and causing air pollution. Since the performance as a filter paper deteriorates, it is desirable to make wet paper in a neutral condition.
また、湿紙の状態で含浸法にてアクリル系のエマルショ
ンバインダを添加すると、捕集率に関与する14ノ細ガ
ラス繊M1の一部が水置換時にシー1〜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ら
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。 ゛〔間:l(i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
、チョップ1くストランド・ガラス繊維に比べ、より親
水性であるチョップドストランド・アクリル繊卸を用い
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卸と、チョップ1−ス
トランド・アクリル繊維との水中での離解9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
ョップトス1−ランド長繊維として、アクリル繊維と共
にビニロン繊維、レーヨン繊維、アセテート繊維、銅ア
ンモニア繊維などを併用してもよい。In addition, if an acrylic emulsion binder is added to the wet paper by the impregnation method, a portion of the 14-fine glass fibers M1, which are involved in the collection rate, will come out from the sheets 1 to 1 during water replacement, resulting in a decrease in yield. However, since the filter performance deteriorates, it is necessary to develop an effective addition method, including the selection of a binder. As a result of intensive study to solve the following problems, we found that chopped strand acrylic is more hydrophilic than chopped strand glass fiber. We have discovered that paper making using water is possible by using a fiber cutter.Additionally, if necessary, an ultra-fine glass fiber cutter and chop 1-strand acrylic fibers can be disintegrated in water to improve the dispersion stability. A surfactant or a sticky agent may be used in combination, and vinylon fiber, rayon fiber, acetate fiber, copper ammonia fiber, etc. may be used in combination with acrylic fiber as the chopped 1-land long fiber.
また、極細ガラス繊維と共にチョップトス1〜ランド・
アクリル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]3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, along with ultra-fine glass fiber, chop toss 1 to land
Since acrylic fibers do not have self-adhesive properties, it is essential to use a binder. However, 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 3%, 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 poor, which is not preferable.
また、水による中性の湿式抄紙法と、繊維状ビニロンバ
インダを内添法で用いることを組み合わぜることにより
、捕集率に関与する極細カラス繊維の歩留りを向−1ニ
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0.3〜477In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
細ガラス繊組の配合割合が5部以下ではシートにピンホ
ールが多1校に生じて捕集率が確保出来ず、一方90部
以」二ではシー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 increase the yield of ultrafine glass fibers, which are involved in the collection rate, by -1. Therefore, by changing the fiber diameter of the ultrafine glass fiber used from 0.3 to 477 In or by changing the blending ratio from 5 to 90 parts, various grades of air filter paper from medium performance to ultra high performance can be produced. We also found that it is possible to differentiate between the two. If the blending ratio of ultra-fine glass fibers is less than 5 parts, many pinholes will occur in the sheet and the collection rate cannot be ensured, while if it is more than 90 parts, the tensile strength of the sheets will be low. 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.
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.
実施例り
極細ガラス繊維として商品名エバンス506(0,54
〜0 、6877Illφ)(エバンス社製)12gに
、チョップ1くストランド・アクリル繊維として商品名
Al0L −1,5X5(旭化成工業社製)11.5
g (固形分70%)と。As an example of ultra-fine glass fiber, the product name Evans 506 (0.54
~0, 6877Illφ) (manufactured by Evans Corporation) (manufactured by Evans Corporation) (12 g), chop 1 strand of acrylic fiber (trade name: Al0L-1,5X5 (manufactured by Asahi Kasei Industries, Ltd.) 11.5
g (70% solids).
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)1.2g(固形分50%)をTAPPI離
解機に入れ、水2Qを加えて30秒間離解させた後、水
8Qを加え、商品名SV −538A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75g/イと
なる様に採取し水を加えて全量を4aとし、反転式アジ
タにて3分間撹拌後、自製の丸型JIS式手抄装置(金
網面積0.0191rr11.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。Put 1.2 g (solid content 50%) of the trade name SMM (manufactured by Unitika Kasei Co., Ltd.) as a fibrous vinylon binder into a TAPPI disintegrator, add 2Q of water and disintegrate for 30 seconds, then add 8Q of water and make the product under the trade name SV. The mixture was stirred for 5 minutes using a reversible agitator model -538A (manufactured by Takasaki Seisakusho). The air filter paper from which this slurry liquid is obtained is sampled so that its basis weight is about 75 g/i, water is added to make the total volume 4a, and after stirring for 3 minutes in an inverted agitator, it is made into a homemade round JIS style hand paper. Air filter paper was made using a device (wire mesh area: 0.0191rr11, mesh spacing: 75 mesh), and after drying using a cylinder dryer, the formation was visually determined.
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TS
Id8251(東芝シリコン社製)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。Furthermore, this air filter paper is manufactured under the product name Avinon 101.
After flame retardant treatment (manufactured by Sanso Chemical Co.), the product name is TS.
After water-repellent treatment using Id8251 (manufactured by Toshiba Silicon Corporation), filter performance was evaluated using a self-made flat sheet filter paper evaluation device.
比較例1−1
チョップドストランド・アクリル繊維の代わりにチョツ
プドストランド・ガラス繊維(9牌1φ〜6 mm +
加ファイバーグラス社製)を8g用い、水の代わりに
l)H2、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。Comparative Example 1-1 Chopped strand glass fiber (9 tiles 1φ~6 mm +
The same procedure as in Example 1 was carried out, except that 8 g of 1) H2,5 sulfuric acid acid water was used instead of water.
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
]と同様に行なった。Comparative Example 1-2 The same procedure as in Example was carried out except that sulfuric acid water with a pH of 2.5 was used instead of water.
比較例1−1
一3Sを1.2g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 in Example 1 was carried out except that 0.3 g of -3S was used instead of 1.2 g.
比較例1−4
Sl−4S、+、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 1-4 The same procedure as in Example 1 was carried out except that 4.8 g of Sl-4S,+ was used instead of 2 g.
比較例1−1
一5Sを1.2.、用いろ代わりにスチレン・アクリル
系エマルジョンバインダである商品名5G−5]−2(
東111i合成化学工業礼′?J、)1.5%水溶液を
含浸法て用いた以外は実施例1と同様に行なった。Comparative Example 1-1 -5S 1.2. , instead of using a styrene-acrylic emulsion binder, product name 5G-5]-2(
East 111i Synthetic Chemical Industry Association'? J,) The same procedure as in Example 1 was carried out except that a 1.5% aqueous solution was used in the impregnation method.
実施例2
極、ti11ガラス繊卸として商品名マンビル+00(
0,24’1〜O、432μIIφ)(マンビル社製)
4gと、チョツプドストラン1へ・アクリル繊維Al0
I−1,5X 5 (加化成工業社製)を22.!’1
K用い、T A fl [)I離M機で1分間処理し
た以外は実施例1と同様に行なった。Example 2 Product name Manville +00 (as a glass fiber wholesaler)
0,24'1~O, 432μIIφ) (manufactured by Manville)
4g and chopped strand 1/acrylic fiber Al0
I-1,5X 5 (manufactured by Kakasei Kogyo Co., Ltd.) at 22. ! '1
The same procedure as in Example 1 was carried out, except that the sample was treated using a T A fl [) I separation machine 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
9〜0 、53 pmφ)(エバンス社製)2gと、チ
ョップドストランド・アクリル繊維AIO+ ! 、
5 X 5 (加化成工業社製)を25.8 g用いた
以外は実施例】と同様に行なった。Example 3 Ultra-fine glass fiber with trade name Evans 504 (0,3
9-0, 53 pmφ) (manufactured by Evans) 2g and chopped strand acrylic fiber AIO+! ,
The same procedure as in Example was carried out except that 25.8 g of 5×5 (manufactured by Kakasei Kogyo Co., Ltd.) was used.
比較例3−1
極細ガラス繊細としてエバンス504を0.5gと、チ
ョップトス1へランド・アクリルJA[Aio+−1,
5×5を27゜9g用いた以外は実施例1と同様に行な
った。Comparative Example 3-1 0.5 g of Evans 504 as ultra-fine glass delicate, and Land Acrylic JA [Aio+-1,
The same procedure as in Example 1 was carried out except that 27.9 g of 5×5 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〜
4tφ)(エバンス社製)18gと、チョツプドストラ
ン1く・アクリル繊維Al0I−]、sx 5 (加化
成工業社製)を2.9g用いた以外は実施例J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 Example J was carried out except that 18 g of chopped strand 1 x acrylic fiber Al0I-], sx 5 (manufactured by Kakasei Kogyo Co., Ltd.) were used.
比較例4−1
極細ガラス繊維としてエバンス510を1.9gと、チ
ョップトス1〜ランド・アクリル繊維Al0I−1,5
×5を1.5 g、用いた以外は実施例]−と同様に行
なった。Comparative Example 4-1 1.9 g of Evans 510 as ultrafine glass fiber and Chop Toss 1 to Rand acrylic fiber Al0I-1,5
The same procedure as in Example]- was carried out except that 1.5 g of ×5 was used.
以下余白
=8−
有量口UG3−44915 (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θ−を用いれば圧力損失が低く、粉塵捕集率を表わす
0.3声径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1
kg/ 15nwn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1−1に示
した様に、チョップトス1−ランド・ガラス繊維を用い
硫酸酸性水で抄紙すると、0、Jan径D01)スモー
ク捕集率が極端に低ドして規格値以下となった。また、
比較例1−2に示した様にチョップトス1−ランド・ア
クリル繊維を用いても硫酸酸性水を用いて抄紙すると矢
張り0.3声径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
に示した様にチョップドストランド・アクリル繊維を用
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囲以下になるとシー!−の引張強度
が極端に低下し、一方、比較例1−4に示した様に適量
範囲具」二になると、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1−5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
いるとバインタ量が2倍で、はぼ同様な引張強度となる
が、0.3ρ径1)OPスモーク捕集率は低下した。Margin below = 8- Quantity mouth UG3-44915 (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 newly invented method θ- is used, the pressure loss is low, and the 0.3 voice diameter DOP smoke collection rate, which represents the dust collection rate, is also the standard 9.
9.97% or more, and the tensile strength of the product is 1.
We can manufacture ultra-high-performance air filter paper with a weight of 15 kg/15 nwn or more. On the other hand, as shown in Comparative Example 1-1, when paper is made using sulfuric acid acid water using chopped 1-land glass fiber, the smoke collection rate (0, Jan diameter D01) is extremely low and falls below the standard value. became. Also,
As shown in Comparative Example 1-2, even if chopped toss 1-land acrylic fibers were used to make paper using sulfuric acid acid water, the smoke collection rate of 0.3 voice diameter DOP was the same as Comparative Example 1-1. It decreased to below the standard value. Also, Comparative Example 1-3
As shown in Figure 2, even if chopped strand acrylic fibers are used to make neutral paper using water, if the addition rate of the fibrous vinylon binder falls below the appropriate amount range, SEE! However, when the tensile strength of Sea 1- becomes extremely low, and on the other hand, as shown in Comparative Example 1-4, the tensile strength of Sea 1- becomes high, but the filter performance deteriorates due to high pressure loss and low trapping. The collection rate becomes extremely poor. Furthermore, as shown in Comparative Example 1-5, 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 amount of binder is doubled and the tensile strength is similar to that of the fibers. Although the strength increased, the OP smoke collection rate decreased with a diameter of 0.3ρ.
次ぎに0.3庫径Dot3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ず、
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部以ドになるとピンホールが多量に発生し、その結果
が0.3P径DO「〕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9
0部以+r、1こなると、チョップトス1−ランド・ア
クリル繊維の配合効果が少なくなり、シー1への引張強
度が低くなった。Next, Table 2 shows the manufacturing results of medium/high performance air filter paper, which has a 0.3 chamber diameter Dot3 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 but also for
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 ultrafine glass fibers exceeds 5 parts, a large number of pinholes occur, resulting in an extremely low smoke collection rate of 0.3P diameter DO. Furthermore, as shown in Comparative Example 4-1, ultrafine glass fibers
If it is more than 0 parts + r or 1 part, the blending effect of the chopped toss 1-land acrylic fiber becomes less and the tensile strength to Sea 1 becomes lower.
以1−の様に平均繊維径が0.3〜4pの極細ガラス繊
H(とチョップ1くストランド・アクリル繊維とを上〃
λ料とし、繊維状ビニロンバインタ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+ハ極細
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
が可能となった。As shown in 1-1 above, the ultra-fine glass fiber H with an average fiber diameter of 0.3 to 4p (and chopped 1 strand acrylic fiber) was
By using λ material and internally adding fibrous vinylon binder, it is possible to make paper with water neutrality, and the yield of ultrafine glass fiber is good, so it is possible to make various grades from medium performance to ultra high performance. It became possible to manufacture air filter paper.
特a′(出願人 山陽国策バルブ株式会社手続補正書 昭和62年6 月311Special a′ (Applicant: Sanyo Kokusaku Valve Co., Ltd. Procedural Amendment June 311, 1988
Claims (1)
ョップドストランド・アクリル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の
製造方法。 2 極細ガラス繊維とチョップドストランド・アクリル
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の製造方法
。[Claims] 1. Ultrafine glass fibers with an average fiber diameter of 0.3 to 4 μm and chopped strand acrylic fibers are the main raw materials, and a fibrous vinylon binder is added internally to the fibers in an amount of 1 to 10% to form a neutral wet process. 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 acrylic fibers is 5:95 to 90:10.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18867686A JPS6344915A (en) | 1986-08-13 | 1986-08-13 | Manufacture of air filter paper |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18867686A JPS6344915A (en) | 1986-08-13 | 1986-08-13 | Manufacture of air filter paper |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6344915A true JPS6344915A (en) | 1988-02-25 |
Family
ID=16227897
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18867686A Pending JPS6344915A (en) | 1986-08-13 | 1986-08-13 | Manufacture of air filter paper |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6344915A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04101489U (en) * | 1991-02-08 | 1992-09-02 | 小島プレス工業株式会社 | Assembly structure of opening/closing body |
JPH10180020A (en) * | 1996-12-25 | 1998-07-07 | Hokuetsu Paper Mills Ltd | Flame retardant volume reduced high performance air filter filter medium and its production |
JP2007090292A (en) * | 2005-09-30 | 2007-04-12 | Hokuetsu Paper Mills Ltd | Non-flammable filtration material for dust removal filter and production method thereof |
CN102912684A (en) * | 2012-09-25 | 2013-02-06 | 蚌埠凤凰滤清器有限责任公司 | Preparation technology of filter paper for air filter |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62110718A (en) * | 1985-10-16 | 1987-05-21 | Kuraray Co Ltd | Filter material for air filter |
-
1986
- 1986-08-13 JP JP18867686A patent/JPS6344915A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62110718A (en) * | 1985-10-16 | 1987-05-21 | Kuraray Co Ltd | Filter material for air filter |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04101489U (en) * | 1991-02-08 | 1992-09-02 | 小島プレス工業株式会社 | Assembly structure of opening/closing body |
JPH10180020A (en) * | 1996-12-25 | 1998-07-07 | Hokuetsu Paper Mills Ltd | Flame retardant volume reduced high performance air filter filter medium and its production |
JP2007090292A (en) * | 2005-09-30 | 2007-04-12 | Hokuetsu Paper Mills Ltd | Non-flammable filtration material for dust removal filter and production method thereof |
CN102912684A (en) * | 2012-09-25 | 2013-02-06 | 蚌埠凤凰滤清器有限责任公司 | Preparation technology of filter paper for air filter |
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