JPS63236512A - Air filter filtering medium - Google Patents

Air filter filtering medium

Info

Publication number
JPS63236512A
JPS63236512A JP6863487A JP6863487A JPS63236512A JP S63236512 A JPS63236512 A JP S63236512A JP 6863487 A JP6863487 A JP 6863487A JP 6863487 A JP6863487 A JP 6863487A JP S63236512 A JPS63236512 A JP S63236512A
Authority
JP
Japan
Prior art keywords
fibers
fiber diameter
less
organic fibers
fiber
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
JP6863487A
Other languages
Japanese (ja)
Other versions
JPH0798130B2 (en
Inventor
Yoshimi Oshitari
忍足 義見
Katsutada Fukui
克任 福井
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.)
OSHIDARI KENKYUSHO KK
Daicel Corp
Oshitari Laboratory Inc
Original Assignee
OSHIDARI KENKYUSHO KK
Daicel Chemical Industries Ltd
Oshitari Laboratory Inc
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 OSHIDARI KENKYUSHO KK, Daicel Chemical Industries Ltd, Oshitari Laboratory Inc filed Critical OSHIDARI KENKYUSHO KK
Priority to JP62068634A priority Critical patent/JPH0798130B2/en
Publication of JPS63236512A publication Critical patent/JPS63236512A/en
Publication of JPH0798130B2 publication Critical patent/JPH0798130B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/08Filter cloth, i.e. woven, knitted or interlaced material
    • B01D39/083Filter cloth, i.e. woven, knitted or interlaced material of organic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12Special parameters characterising the filtering material
    • B01D2239/1233Fibre diameter

Abstract

PURPOSE:To prepare a filtering medium of high dust collecting rate and volume- reducible in combustion by forming a mixture consisting of 2-50wt.% organic fibers of 1mum fiber diameter or less and inorganic fibers of 5mum or more fiber diameter for the remaining part into a sheet. CONSTITUTION:An air filter medium is prepared by forming a fiber mixture consisting of 2-50wt.% organic fibers of 1mum fiber diameter or less and 50-98wt.% organic fibers of fiber diameter 5mum or more into a sheet. For the preparation of organic fibers of 1mum fiber diameter or less, extremely superfine fibers of organic synthetic high molecules, micro-fibrillated substances, whiskers and the like are used. As for organic fibers of 5mum fiber diameter or more, synthetic fibers, pulps and the like, preferably of 20mum fiber diameter or less, are used. In case of fibers originated from synthetic high molecules, fibers not containing inorganic pigments or the like should be used for the sake of volume reduction at the time of incineration.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、気体中に含有される微粒子を効率よく除去し
、クリーンな気体を得るための高性能濾過材に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a high-performance filter material for efficiently removing particulates contained in gas and obtaining clean gas.

〔従来の技術とその問題点〕[Conventional technology and its problems]

従来、空気中の微細粉塵を除去する方法として紙状のフ
ィルターが使用されて来た。この場合使用!lIi維が
細ければ細いほど粉度の捕捉率は大きくなるが、一方通
気抵抗も増大する。
Traditionally, paper filters have been used to remove fine dust from the air. Use in this case! The finer the IIi fibers, the greater the particle capture rate, but also the greater the ventilation resistance.

微細粉廖除去のための濾過材としては、径の小さいもの
が製造でき、且つ比較的剛直なため捕捉性能を上げるこ
とができる割には通気抵抗が上がりに(いので、ガラス
、繊維がこの分野で主として使用されて来た。しかしな
がら、ガラス微小繊維は製造中に微量ではあるが微小粒
子を副生じて含有しており、濾過材の製造及び使用中に
このような微小粒子が透過側へ脱落するという欠点があ
る。また、空気濾過の一つの用途である放射性物質含有
粉塵の除去に使用した場合、これら松原を吸着した濾過
材は燃焼させて容量を小さくして廃棄処分をするのであ
るが、ガラス繊維ではこの減容ができないという問題が
ある。
As a filter material for removing fine particles, it is possible to manufacture a material with a small diameter, and it is relatively rigid, so although it can improve the trapping performance, it has a high airflow resistance (because it is difficult to use glass or fiber). However, glass microfibers contain a small amount of microparticles as a by-product during production, and during the production and use of filter media, these microparticles are transferred to the permeate side. It has the disadvantage of falling off.Also, when used to remove dust containing radioactive substances, which is one of the applications of air filtration, the filter material that adsorbs these matsubara is burned to reduce its capacity and disposed of. However, there is a problem in that this volume reduction cannot be achieved with glass fiber.

〔問題点を解決するための手段〕[Means for solving problems]

近年、有機質繊維においても径の極めて小さい繊維が得
られるようになったが、発明者らは、比較的剛直な微小
径有機繊維を限定された条件で使用することにより、粉
塵捕捉率が高く且つ通気抵抗が小であり、燃焼減容の可
能な濾過材を得ることに成功し、本発明に到達した。
In recent years, it has become possible to obtain organic fibers with extremely small diameters, but the inventors were able to achieve a high dust capture rate and The present invention was achieved by successfully obtaining a filter material that has low ventilation resistance and whose volume can be reduced by combustion.

〔発明の構成〕[Structure of the invention]

即ち本発明は、繊維径1μm以下の有機質繊維2〜50
重量%と繊維径5μm以上の有機質繊維50〜98重量
%からなる繊維混合物をシート状化してなるエアフィル
ター濾過材に関するものである。
That is, the present invention uses 2 to 50 organic fibers with a fiber diameter of 1 μm or less.
The present invention relates to an air filter filtration material formed by sheeting a fiber mixture consisting of 50 to 98% by weight of organic fibers having a fiber diameter of 5 μm or more.

本発明に使用する繊維径1μm以下の有機質繊維は、有
機合成高分子の超極細繊維、ミクロフィブリル化物、及
びウィスカーなどから該当するものを選択使用すればよ
い。
The organic fibers having a fiber diameter of 1 μm or less used in the present invention may be selected from among ultrafine fibers of organic synthetic polymers, microfibrillated products, whiskers, and the like.

その製法としては、 (イ) スプリットしうる複合繊維を製造しスプリット
する (口) 溶液から剪断力下に紡出する (ハ) 溶液を高圧側から低圧側にフラッシュし、のち
叩解する (二) 繊維を高圧側から低圧側に通過させる際、器壁
に衝突させ、これをくりかえしてフィブリル化する (ホ) 高分子モノマーを溶液中重合させながら結晶生
成させてウィスカーとする などの方法をとることができる。
The manufacturing method is as follows: (a) Manufacture and split splittable composite fibers (1) Spun from solution under shearing force (c) Flush the solution from the high pressure side to the low pressure side and then beat it (2) When the fibers are passed from the high-pressure side to the low-pressure side, they collide with the wall of the vessel and are repeatedly fibrillated. Can be done.

上記径1μm以下の有機質繊維としてはできるだけ剛直
なものが好ましく、特に剛直鎖合成高分子と総称される
材料からなる繊維が好適である。剛直鎖合成高分子とは
、溶液中直線状を維持する鎖長く持続長)が50Å以上
ある高分子のことであり、例えば、ポリ (P−フェニ
レンテレフタルアミド)、ポリ (P−ベンズアミド)
、ホ!J=(P−フェニレンベンゾビスチアゾール)、
ポリ (P−)ユニしンベンゾビスオキサゾール)、ポ
リ (アミドヒドラジド)、ポリヒドラジド、ポリ (
P−フェニレンテレフタルアミド−3,4−ジフェニル
エーテルテレフタルアミド)などがある。特に、これら
剛直鎖合成高分子は、一旦紡糸して繊維形状としたもの
を上記(ニ)の方法で、ミクロフィブリル化して実質的
に径1μm以下のフィブリルとすることができる。この
ように、通常の方法で紡糸した繊維を使用できるので、
上記の内、(ニ)の方法が経済的に有利である。
The organic fibers having a diameter of 1 μm or less are preferably as rigid as possible, and fibers made of materials collectively referred to as rigid and straight chain synthetic polymers are particularly suitable. Rigid and linear synthetic polymers are polymers with a long chain length (long persistence length) that maintains a linear shape in solution of 50 Å or more, such as poly (P-phenylene terephthalamide), poly (P-benzamide), etc.
, Ho! J=(P-phenylenebenzobisthiazole),
poly (P-)unisine benzobisoxazole), poly (amide hydrazide), polyhydrazide, poly (
P-phenylene terephthalamide-3,4-diphenyl ether terephthalamide). In particular, these rigid and linear synthetic polymers can be spun into fibers and then microfibrillated into fibrils having a diameter of substantially 1 μm or less using the method (d) above. In this way, fibers spun using normal methods can be used.
Among the above methods, method (d) is economically advantageous.

又本発明に使用する繊維径5μm以上の有機質繊維とは
、ポリオレフィン、ポリアミド、ポリエステルなどの合
成繊維のほか、パルプ、リンク−、リントおよびその誘
導体などを適宜使用することができる。エアフィルター
においては、繊維径が小さいほど粉塵捕捉率がよいので
径5μm以上の繊維においても径20μm以下程度であ
ることが好ましい。繊維径5μm以上の繊維と径1μm
以下の繊維は、水に混合分散させてスラリーとし、金網
上で水を分離する抄紙方法によってシート化し、濾過材
とすることができる。
The organic fibers having a fiber diameter of 5 μm or more used in the present invention include synthetic fibers such as polyolefin, polyamide, and polyester, as well as pulp, lint, lint, and derivatives thereof. In air filters, the smaller the fiber diameter, the better the dust capture rate, so even for fibers with a diameter of 5 μm or more, the diameter is preferably about 20 μm or less. Fibers with a diameter of 5 μm or more and fibers with a diameter of 1 μm
The following fibers can be mixed and dispersed in water to form a slurry, and formed into a sheet by a papermaking method in which water is separated on a wire mesh to form a filter medium.

繊維径5μm以上の繊維がパルプ、リンター、リントで
ある場合を除いて、生成する紙の強度は強くないので、
抄紙後水エマルジヨン接着剤、例えば、ポリ酢酸ビニル
エマルジョン、ポリブタジェンエマルジョン等を付加し
て補強するのがよい。或いは、径5μm以上の繊維の一
部を熱融着性の繊維例えば、エチレン酢酸ビニル共重合
体、熱融着性ポリアミド繊維とし、抄紙後、熱融着に充
分な温度の熱を加える方法もとることができる。エアフ
ィルター濾過材となる紙状シート材の製造において、繊
維径1μm以下の繊維量が多いほど捕捉率は向上するが
、原価が高くなり、また紙力強度も低下する。従って全
繊維分の2〜50重量%が好ましい。
Unless the fibers with a fiber diameter of 5 μm or more are pulp, linter, or lint, the strength of the paper produced is not strong.
After papermaking, it is preferable to add a water emulsion adhesive such as polyvinyl acetate emulsion, polybutadiene emulsion, etc. for reinforcement. Alternatively, there is also a method in which some of the fibers with a diameter of 5 μm or more are made into heat-fusible fibers, such as ethylene-vinyl acetate copolymer or heat-fusible polyamide fibers, and heat is applied to a temperature sufficient for heat-fusion after paper making. You can take it. In the production of a paper-like sheet material used as an air filter filtration material, the larger the amount of fibers with a fiber diameter of 1 μm or less, the higher the capture rate, but the higher the cost and the lower the paper strength. Therefore, it is preferably 2 to 50% by weight of the total fiber content.

また、繊維が合成高分子から作られたものを使用する場
合、無機顔料などを含有しない繊維を使用することが焼
却時の減容のために必要である。好ましい減容の程度は
、大気中800℃で焼却したときの灰分が4.0重量%
以下であること、即ち、焼却後の重量が原材料重量の4
%以下となるような場合である。
Furthermore, when using fibers made from synthetic polymers, it is necessary to use fibers that do not contain inorganic pigments in order to reduce the volume during incineration. The preferred degree of volume reduction is that the ash content when incinerated at 800°C in the atmosphere is 4.0% by weight.
The weight after incineration must be less than 4% of the weight of the raw material.
% or less.

〔発明の効果〕〔Effect of the invention〕

本発明のエアフィルターは、微小粉席の捕捉性能が大で
あるとともに通気抵抗が高くなく、折曲げ加工性及びセ
ツティング形状保持性が良いので、プリーツ、コルゲー
トなどの形でエアフィルターに組立てるのに適している
。さらに、灰分量が少ないので使用後の焼却処分が容易
である。
The air filter of the present invention has a high ability to capture fine particles, does not have high ventilation resistance, and has good bending workability and shape retention properties, so it can be assembled into an air filter in the form of pleats, corrugates, etc. suitable for Furthermore, since the ash content is small, it is easy to incinerate after use.

〔実施例〕〔Example〕

以下実施例により本発明を更に詳細に説明するが、本発
明はこれらに限定されるものではない。
The present invention will be explained in more detail below with reference to Examples, but the present invention is not limited thereto.

実施例1 ケブラー繊維(Du pant社製品パルプグレード、
3〜4デニール、繊維長約2n++++にカッティング
したもの) 10gを水11に分散させて均質化装置(
Gaulin社製15M−87A)に約25℃で仕込み
、420kg/cm2の圧力をかけて30回循環通過さ
せ、ケブラーのミクロフィブリル化繊維が安定に水に懸
濁している懸濁液を得たく固型分濃度1%)。
Example 1 Kevlar fiber (Du pant product pulp grade,
3-4 denier, fiber length approximately 2n++++) Disperse 10g in water 11 and use a homogenizer (
Gaulin 15M-87A) was charged at approximately 25°C and circulated 30 times under a pressure of 420 kg/cm2 to obtain a suspension of Kevlar microfibrillated fibers stably suspended in water. mold concentration 1%).

懸濁液中のミクロフィブリル化繊維の径は約0.4μm
であった。0.5デニール(繊維径約7μm)、5.1
cm長のポリエステル繊維70重畳部、上記ミクロフィ
ブリル化ケブラー懸濁液3000重量部、及び水200
0重量部を混合撹拌してスラリーとし、標準角形手抄き
抄紙機(真鋳ワイヤー80メッンユ)を用いて抄造し、
坪量75g/m2の紙状シート材を得た。得られたシー
ト材の圧力損失と集■効率を下記の方法で測定した。又
、シート材を大気中800℃で焼却した際の焼却残分(
灰分)を測定した。
The diameter of microfibrillated fibers in the suspension is approximately 0.4 μm
Met. 0.5 denier (fiber diameter approximately 7 μm), 5.1
70 overlapping parts of cm-long polyester fibers, 3000 parts by weight of the above microfibrillated Kevlar suspension, and 200 parts by weight of water.
0 parts by weight were mixed and stirred to form a slurry, and the slurry was made into paper using a standard square hand paper machine (brass wire 80 mm).
A paper-like sheet material having a basis weight of 75 g/m2 was obtained. The pressure loss and collection efficiency of the obtained sheet material were measured by the following methods. In addition, the incineration residue (
Ash content) was measured.

圧力損失;濾過材に空気を流速4.75Cm/秒で通気
させたときの通気抵抗を水柱マノ メーターにより求めた。
Pressure loss: The ventilation resistance when air was passed through the filter medium at a flow rate of 4.75 Cm/sec was determined using a water column manometer.

集塵効率;平均粒径0.3μmのジオクチルフタレート
粒子を発生させ、この粒子を 含有する空気を流速5.3Cm/秒で濾過材を通過させ
、濾過材の前後で空 気をサンプリングし、それぞれの粒 子濃度をマルチダストカウンターで 測定し算出した。
Dust collection efficiency: Dioctyl phthalate particles with an average particle size of 0.3 μm are generated, the air containing these particles is passed through a filter medium at a flow rate of 5.3 Cm/sec, the air is sampled before and after the filter medium, and each Particle concentration was measured and calculated using a multi-dust counter.

実施例2 実施例1で得たミクロフィブリル化ケブラー懸濁液15
00重量部にポリエステル繊維85重量部、水3500
重量部を加え、同様に抄紙し、一旦乾燥させた後、4.
0%固型分濃度のアクリルニトリル/ブタジェン水性エ
マルジョンを28重量部添加し、その1/2量が添着す
る程度にメツシュの下から吸引し、乾燥してシート材を
得た。
Example 2 Microfibrillated Kevlar suspension 15 obtained in Example 1
00 parts by weight, 85 parts by weight of polyester fiber, and 3500 parts by weight of water.
After adding parts by weight, making paper in the same manner, and once drying, 4.
28 parts by weight of an acrylonitrile/butadiene aqueous emulsion having a solid content concentration of 0% was added and suctioned from below the mesh until 1/2 of the emulsion was adhered, and dried to obtain a sheet material.

比較例1 径約0,6 μm1長さ0.4mmのガラスマイクロウ
ール30重量部、0.5デニール(繊維径約7μm)、
長さ5.1cmのポリエステル繊維70重量部を水40
00重量部と混合撹拌してスラリーとし、抄紙後メラミ
ンホルマリン樹脂1%水溶液700重壷部を加え、自由
落下により添着する分のみを添着させて乾燥シート材を
得た。
Comparative Example 1 30 parts by weight of glass micro wool with a diameter of approximately 0.6 μm and a length of 0.4 mm, 0.5 denier (fiber diameter approximately 7 μm),
70 parts by weight of polyester fiber with a length of 5.1 cm and 40 parts by weight of water
After paper making, 700 parts by weight of a 1% aqueous solution of melamine-formalin resin was added to the slurry, and only the amount to be adhered by free fall was adhered to obtain a dry sheet material.

比較例2 比較例1のガラスマイクロウールに代えて、ポリエステ
ル繊維マイクロファイバー(径約1.0μm1長さ0.
5mm)を用いたほかは同様にしてシート材を得た。
Comparative Example 2 In place of the glass microwool in Comparative Example 1, polyester fiber microfiber (diameter: approximately 1.0 μm, length: 0.0 μm) was used.
A sheet material was obtained in the same manner except that 5 mm) was used.

シート材の物性測定値を第1表にまとめて示す。Measured physical properties of the sheet material are summarized in Table 1.

第1表 ■Table 1 ■

Claims (1)

【特許請求の範囲】 1 繊維径1μm以下の有機質繊維2〜50重量%と、
繊維径5μm以上の有機質繊維50〜98重量%からな
る繊維混合物をシート状化してなるエアフィルター濾過
材。 2 繊維径1μm以下の有機質繊維が剛直鎖合成高分子
のミクロフィブリル化物又は剛直鎖合成高分子のウィス
カーである特許請求の範囲第1項記載のエアフィルター
濾過材。 3 大気中800℃で焼却したときの灰分が4.0重量
%以下である特許請求の範囲第1項又は第2項記載のエ
アフィルター濾過材。
[Scope of Claims] 1. 2 to 50% by weight of organic fibers with a fiber diameter of 1 μm or less;
An air filter filtration material formed by sheeting a fiber mixture consisting of 50 to 98% by weight of organic fibers with a fiber diameter of 5 μm or more. 2. The air filter filtration material according to claim 1, wherein the organic fibers having a fiber diameter of 1 μm or less are microfibrillated products of rigid linear synthetic polymers or whiskers of rigid linear synthetic polymers. 3. The air filter filtration material according to claim 1 or 2, which has an ash content of 4.0% by weight or less when incinerated at 800°C in the atmosphere.
JP62068634A 1987-03-23 1987-03-23 Air filter-filter material Expired - Fee Related JPH0798130B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62068634A JPH0798130B2 (en) 1987-03-23 1987-03-23 Air filter-filter material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62068634A JPH0798130B2 (en) 1987-03-23 1987-03-23 Air filter-filter material

Publications (2)

Publication Number Publication Date
JPS63236512A true JPS63236512A (en) 1988-10-03
JPH0798130B2 JPH0798130B2 (en) 1995-10-25

Family

ID=13379366

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62068634A Expired - Fee Related JPH0798130B2 (en) 1987-03-23 1987-03-23 Air filter-filter material

Country Status (1)

Country Link
JP (1) JPH0798130B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5171339A (en) * 1991-11-07 1992-12-15 E. I. Du Pont De Nemours And Company Filter bag for hot gases
US5480466A (en) * 1994-05-04 1996-01-02 Schuller International, Inc. Air filtration media
US5607491A (en) * 1994-05-04 1997-03-04 Jackson; Fred L. Air filtration media
JP2003129393A (en) * 2001-10-25 2003-05-08 Oji Paper Co Ltd Organic extra-superfine fiber sheet
WO2006035174A1 (en) * 2004-09-29 2006-04-06 Valeo Materiaux De Friction Filter medium for filtration of gases filtration device and method for production of filter medium
CN102711948A (en) * 2009-12-22 2012-10-03 霍林斯沃思和沃斯有限公司 Filter media and articles inc.luding dendrimers and/or other components

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5765311A (en) * 1980-10-08 1982-04-20 Asahi Chem Ind Co Ltd Filter material
JPS58208498A (en) * 1982-05-27 1983-12-05 帝人株式会社 Sheet-like article

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5765311A (en) * 1980-10-08 1982-04-20 Asahi Chem Ind Co Ltd Filter material
JPS58208498A (en) * 1982-05-27 1983-12-05 帝人株式会社 Sheet-like article

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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