JPS63236512A - Air filter filtering medium - Google Patents
Air filter filtering mediumInfo
- 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
Links
- 238000001914 filtration Methods 0.000 title claims abstract description 8
- 239000000835 fiber Substances 0.000 claims abstract description 66
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims description 18
- 229920001059 synthetic polymer Polymers 0.000 claims description 7
- 239000000428 dust Substances 0.000 abstract description 7
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 abstract description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 2
- 239000001023 inorganic pigment Substances 0.000 abstract description 2
- 229920002994 synthetic fiber Polymers 0.000 abstract description 2
- 239000012209 synthetic fiber Substances 0.000 abstract description 2
- 239000012784 inorganic fiber Substances 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000000839 emulsion Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 229920000728 polyester Polymers 0.000 description 5
- 229920000271 Kevlar® Polymers 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 239000004761 kevlar Substances 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- 229920001410 Microfiber Polymers 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- 239000004952 Polyamide Substances 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000003658 microfiber Substances 0.000 description 2
- 239000011859 microparticle Substances 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- HSAOVLDFJCYOPX-UHFFFAOYSA-N 2-[4-(1,3-benzothiazol-2-yl)phenyl]-1,3-benzothiazole Chemical compound C1=CC=C2SC(C3=CC=C(C=C3)C=3SC4=CC=CC=C4N=3)=NC2=C1 HSAOVLDFJCYOPX-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- 229910001369 Brass Inorganic materials 0.000 description 1
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- IVJISJACKSSFGE-UHFFFAOYSA-N formaldehyde;1,3,5-triazine-2,4,6-triamine Chemical compound O=C.NC1=NC(N)=NC(N)=N1 IVJISJACKSSFGE-UHFFFAOYSA-N 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000002688 persistence Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920003190 poly( p-benzamide) Polymers 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920003366 poly(p-phenylene terephthalamide) Polymers 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 239000000941 radioactive substance Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- MHSKRLJMQQNJNC-UHFFFAOYSA-N terephthalamide Chemical compound NC(=O)C1=CC=C(C(N)=O)C=C1 MHSKRLJMQQNJNC-UHFFFAOYSA-N 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/08—Filter cloth, i.e. woven, knitted or interlaced material
- B01D39/083—Filter cloth, i.e. woven, knitted or interlaced material of organic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/12—Special parameters characterising the filtering material
- B01D2239/1233—Fibre diameter
Abstract
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、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.
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.
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.
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.
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)
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.
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)
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)
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 |
-
1987
- 1987-03-23 JP JP62068634A patent/JPH0798130B2/en not_active Expired - Fee Related
Patent Citations (2)
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)
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 |
US8956437B2 (en) | 2009-12-22 | 2015-02-17 | Hollingsworth & Vose Company | Filter media and articles including dendrimers and/or other components |
CN102711948B (en) * | 2009-12-22 | 2015-04-08 | 霍林斯沃思和沃斯有限公司 | Filter media and articles including dendrimers and/or other components |
CN106861290A (en) * | 2009-12-22 | 2017-06-20 | 霍林斯沃思和沃斯有限公司 | Product and filter medium comprising waterproofing agent |
CN106861290B (en) * | 2009-12-22 | 2019-08-09 | 霍林斯沃思和沃斯有限公司 | Product and filter medium comprising waterproofing agent |
Also Published As
Publication number | Publication date |
---|---|
JPH0798130B2 (en) | 1995-10-25 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |