JP4069057B2 - High performance air filter - Google Patents

High performance air filter Download PDF

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JP4069057B2
JP4069057B2 JP2003368692A JP2003368692A JP4069057B2 JP 4069057 B2 JP4069057 B2 JP 4069057B2 JP 2003368692 A JP2003368692 A JP 2003368692A JP 2003368692 A JP2003368692 A JP 2003368692A JP 4069057 B2 JP4069057 B2 JP 4069057B2
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nonwoven fabric
acid amide
sheet
water
air filter
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JP2005131485A (en
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順 児玉
豊 高堂
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Tapyrus Co Ltd
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Description

本発明は、熱可塑性樹脂の不織布からなる高性能エアフィルタに関し、特に、帯電量を多くした熱可塑性樹脂極細繊維不織布からなる低圧力損失、高効率濾材の高性能エアフィルタに関する。   The present invention relates to a high-performance air filter made of a nonwoven fabric of thermoplastic resin, and more particularly to a high-performance air filter of a low pressure loss, high-efficiency filter medium made of a thermoplastic resin ultrafine fiber nonwoven fabric having an increased charge amount.

従来より、気体中の微粒子の捕集はもとより比較的大きいダストを効率良く捕集できるフィルタ材として、極細繊維からなる不織布が用いられ、特に低圧力損失下で微粒子の捕集効率を高めるフィルタの材料として、不織布に電荷を付与したエレクトレット化不織布が主に用いられてきている。
これらのフィルタにおけるエレクトレット化は、主として不織布をコロナ帯電させる方法、水流を衝突させる方法などが用いられている。しかしながら、コロナ帯電させる方法では、帯電量を十分に高めるようにするためには電圧を上げる必要があり、電圧を上げすぎるとスパークが起こり不織布にピンホールが生じやすいという問題を有している。また、水流の衝突にによる方法では、高圧水流の衝突によって不織布構成繊維が絡まりやすく、その結果、繊維配向が変わり、開口が形成されやすく、エレクトレット化による濾過効率と圧力損失を両立する不織布濾過材の設計が難しくなる等の問題を有していた。
Conventionally, non-woven fabric made of ultrafine fibers has been used as a filter material that can efficiently collect relatively large dust as well as fine particles in gas. Especially, it is a filter that improves the collection efficiency of fine particles under low pressure loss. As a material, electret nonwoven fabric obtained by imparting electric charge to a nonwoven fabric has been mainly used.
For electretization in these filters, a method of corona charging a non-woven fabric, a method of colliding a water flow, and the like are mainly used. However, in the corona charging method, it is necessary to increase the voltage in order to sufficiently increase the charge amount, and there is a problem that if the voltage is increased too much, sparks occur and pinholes are likely to occur in the nonwoven fabric. Moreover, in the method based on the collision of the water flow, the nonwoven fabric constituting fibers are easily entangled by the collision of the high pressure water flow. However, it was difficult to design.

このような問題を解決する方法として、熱可塑性樹脂からなる構造体に対して、極性液体を介して超音波振動を作用させてエレクトレット化をさせる方法(例えば、特許文献1参照。)が開示され、また、メルトブロー不織布に高圧流体噴霧処理を施し、その後コロナ帯電する方法(例えば、特許文献2参照。)が開示されている。しかしながら、これらの方法は、いずれも複雑な工程を必要とし、より簡便な方法の開発が求められている。
特開2003−205210号公報 特開2003−220310号公報
As a method for solving such a problem, there is disclosed a method (for example, refer to Patent Document 1) in which ultrasonic vibration is applied to a structure made of a thermoplastic resin via a polar liquid to make it electretized. In addition, a method is disclosed in which a melt blown nonwoven fabric is subjected to a high-pressure fluid spray treatment and then corona charged (for example, see Patent Document 2). However, these methods all require complicated steps, and the development of simpler methods is required.
JP 2003-205210 A JP 2003-220310 A

本発明の目的は、前述の問題点を解決し、帯電量を多くした熱可塑性極細繊維不織布からなる低圧力損失、高効率濾材の高性能エアフィルタを提供することにある。 An object of the present invention is to solve the above-mentioned problems and to provide a high-performance air filter having a low pressure loss and a high-efficiency filter medium made of a thermoplastic ultra-fine fiber nonwoven fabric having an increased charge amount.

本発明者らは、上記の目的を達成すべく鋭意研究を重ねた結果、不織布の原料樹脂に特定量の脂肪酸アマイド化合物を配合した樹脂組成物から得られる不織布を水流処理した後、乾燥することにより、粒子捕集効率に優れ、低圧力損失の高性能エアフィルタ用不織布が得られることを見出し本発明を完成させた。 As a result of intensive studies to achieve the above-mentioned object, the present inventors water-treated a nonwoven fabric obtained from a resin composition in which a specific amount of a fatty acid amide compound is blended with a raw material resin of the nonwoven fabric, and then dry the nonwoven fabric. As a result, it was found that a nonwoven fabric for high-performance air filters having excellent particle collection efficiency and low pressure loss can be obtained, thereby completing the present invention.

すなわち、本発明の第1の発明によれば、熱可塑性樹脂に脂肪酸アマイド化合物を0.05〜3重量%配合した樹脂組成物から得られる極細繊維不織布を水流帯電法によりエレクトレット化した不織布からなることを特徴とする高性能エアフィルタが提供される。   That is, according to the first invention of the present invention, it comprises a nonwoven fabric obtained by electretizing an ultrafine fiber nonwoven fabric obtained from a resin composition in which a fatty acid amide compound is blended in a thermoplastic resin in an amount of 0.05 to 3% by weight. A high-performance air filter characterized by the above is provided.

また、本発明の第2の発明によれば、第1の発明において、熱可塑性樹脂がポリオレフィン、ポリエチレンテレフタレート、ポリブチレンテレフタレートからなる群から選ばれる少なくとも一種類の樹脂であることを特徴とする高性能エアフィルタが提供される。   According to the second invention of the present invention, in the first invention, the thermoplastic resin is at least one resin selected from the group consisting of polyolefin, polyethylene terephthalate, and polybutylene terephthalate. A performance air filter is provided.

また、本発明の第3の発明によれば、第1又は2の発明において、不織布が、目付け5〜100g/m、平均繊維径2〜30μm、厚み0.1〜0.6mm、通気度20〜200cc/sec/cmのポリプロピレンメルトブロー不織布であることを特徴とする高性能エアフィルタが提供される。 According to the third invention of the present invention, in the first or second invention, the nonwoven fabric has a basis weight of 5 to 100 g / m 2 , an average fiber diameter of 2 to 30 μm, a thickness of 0.1 to 0.6 mm, and an air permeability. A high-performance air filter characterized by being a polypropylene melt blown nonwoven fabric of 20 to 200 cc / sec / cm 2 is provided.

本発明のフィルタは、脂肪酸アマイド化合物を含有する熱可塑性樹脂の不織布を水流処理法によりエレクトレット化したもので、粒子捕集効率に優れ、低圧力損失の高性能エアフィルタとして用いることができる。   The filter of the present invention is obtained by electretizing a thermoplastic resin nonwoven fabric containing a fatty acid amide compound by a water flow treatment method, and can be used as a high-performance air filter having excellent particle collection efficiency and low pressure loss.

本発明を以下に詳しく説明する。
本発明の不織布に用いる熱可塑性樹脂は、ポリエチレン、ポリプロピレン等のポリオレフィン、ポリエチレンテレフタレート、ポリブチレンテレフタレート等のポリエステル、ナイロン6、ナイロン66、ナイロン46等のポリアミド、ポリ塩化ビニル、ポリ塩化ビニリデン、ポリスチレン、ポリカーボネート、ポリフッ化ビニリデン、ポリアリーレンスルフィド等を挙げることができる。これらの中では、ポリオレフィン、ポリエステルが好ましく、特に、プロピレンからなる単独重合体、共重合体が細い均一な繊維構成を得やすく、かつまた、不織布強度の面から好ましい。また、これらの熱可塑性樹脂は、必要に応じて適宜ブレンドして用いることができる。
The present invention is described in detail below.
The thermoplastic resin used in the nonwoven fabric of the present invention includes polyolefins such as polyethylene and polypropylene, polyesters such as polyethylene terephthalate and polybutylene terephthalate, polyamides such as nylon 6, nylon 66 and nylon 46, polyvinyl chloride, polyvinylidene chloride, polystyrene, Polycarbonate, polyvinylidene fluoride, polyarylene sulfide and the like can be mentioned. Among these, polyolefins and polyesters are preferable, and in particular, homopolymers and copolymers made of propylene are easy to obtain a thin and uniform fiber structure, and are also preferable from the viewpoint of nonwoven fabric strength. Further, these thermoplastic resins can be appropriately blended and used as necessary.

また、上記熱可塑性樹脂の2種類以上の組合せからなる複合繊維を用いてもよい。例えば、外層がポリエチレンからなり、内芯層が外層ポリエチレンより20℃以上、好ましくは30℃以上高い融点を有する樹脂よりなる複合繊維が挙げられる。この複合繊維においては、例えば、外層のポリエチレンとしては、超高分子量ポリエチレン、高密度ポリエチレン、中密度ポリエチレン、低密度ポリエチレン、エチレン−酢酸ビニル共重合体等のいずれも使用できるが、特に低密度ポリエチレン、エチレン−酢酸ビニル共重合体等の低融点のポリエチレンが好ましい。   Moreover, you may use the composite fiber which consists of 2 or more types of combinations of the said thermoplastic resin. For example, a composite fiber made of a resin having an outer layer made of polyethylene and an inner core layer having a melting point higher than that of the outer layer polyethylene by 20 ° C. or more, preferably 30 ° C. or more. In this composite fiber, for example, as the outer layer polyethylene, any of ultrahigh molecular weight polyethylene, high density polyethylene, medium density polyethylene, low density polyethylene, ethylene-vinyl acetate copolymer, etc. can be used. Polyethylene having a low melting point such as an ethylene-vinyl acetate copolymer is preferable.

内芯層を構成する樹脂としては、ポリエチレンの融点より20℃以上高い融点を有する樹脂で、ポリプロピレン、ポリ−4−メチルペンテン−1、ポリ−3−メチルブテン−1、ポリエチレンテレフタレート、ポリブチレンテレフタレート、ポリカーボネート、ポリアミド、ポリアリーレンスルフィド、ポリアリーレンオキシド等の樹脂が挙げられ、特に、好ましくはポリプロピレンである。   As a resin constituting the inner core layer, a resin having a melting point higher than that of polyethylene by 20 ° C. or more, polypropylene, poly-4-methylpentene-1, poly-3-methylbutene-1, polyethylene terephthalate, polybutylene terephthalate, Examples of the resin include polycarbonate, polyamide, polyarylene sulfide, and polyarylene oxide. Particularly preferred is polypropylene.

内芯層の太さは、繊維径の1/5〜4/5程度であることが、外層の接着性と内芯層による形状保持効果を保つ上で望ましく、内芯層の位置は繊維の中心であっても偏芯していてもよい。
鞘の材質がポリエチレンであると、不織布製造時の熱エンボス処理や熱カレンダー処理の加工工程をより低温で行うことができるために好ましい。また、メルトブロー法ポリプロピレン不織布のポリプロピレンの結晶化温度においてポリエチレン部分を融解させてポリプロピレン繊維との結合度を増すことになり好都合である。さらに、鞘のポリエチレンが溶融しても、芯の部分は溶融せず、繊維としての形状が保持され、かつ強度も保持される。
The thickness of the inner core layer is preferably about 1/5 to 4/5 of the fiber diameter in order to maintain the adhesiveness of the outer layer and the shape retention effect of the inner core layer. The position of the inner core layer is the position of the fiber. It may be centered or eccentric.
It is preferable that the material of the sheath is polyethylene because the processing step of the heat embossing process and the heat calendar process when manufacturing the nonwoven fabric can be performed at a lower temperature. In addition, the polyethylene part is melted at the crystallization temperature of the polypropylene of the melt blown polypropylene nonwoven fabric, which advantageously increases the degree of bonding with polypropylene fibers. Further, even when the sheath polyethylene is melted, the core portion is not melted, the shape as a fiber is maintained, and the strength is also maintained.

本発明において、上記熱可塑性樹脂に配合して用いる脂肪酸アマイド化合物は、熱可塑性樹脂のメルトブロー不織布繊維の水流によるエレクトレット化帯電率を向上させる機能を有する化合物である。本発明で用いることのできる脂肪酸アマイド化合物としては、脂肪酸、不飽和脂肪酸のモノアマイド類、ビスアマイド類が挙げられ、例えば、ステアリン酸アマイド、バルミチン酸アマイド、ベヘニン酸アマイド、ミリスチン酸アマイド、エルカ酸アマイド、オレイン酸アマイド、カプリル酸アマイド、カプリン酸アマイド、リノール酸アマイド、リノレン酸アマイド、リジノールサンアマイド、パルミトレイン酸アマイド、ラウリン酸アマイド、アラキド酸アマイド、アラキジン酸アマイド、エイコセン酸アマイド、ブライジン酸アマイド、エライジン酸アマイド、N−ステアリルエルカ酸アマイド、N−(2−ハイドロキシメチル)・ステアリン酸アマイド、N−(2−ハイドロキシエチル)ラウリン酸アマイド、エチレンビスオレイン酸アマイド、エチレンビスステアリン酸アマイド、メチレンビスステアリン酸アマイド、ヘキサメチレンビスオレイン酸アマイド、ヘキサメチレンビスエルカ酸アマイド、オクタメチレンビスエルカ酸アマイド等を挙げることができる。   In the present invention, the fatty acid amide compound used by blending with the thermoplastic resin is a compound having a function of improving electret electrification rate by water flow of the melt blown nonwoven fabric fiber of the thermoplastic resin. Examples of fatty acid amide compounds that can be used in the present invention include fatty acids, monoamides of unsaturated fatty acids, and bisamides. Examples include stearic acid amide, valmitic acid amide, behenic acid amide, myristic acid amide, erucic acid amide, Oleic acid amide, caprylic acid amide, capric acid amide, linoleic acid amide, linolenic acid amide, ridinol sun amide, palmitoleic acid amide, lauric acid amide, arachidic acid amide, arachidic acid amide, eicosenoic acid amide, bridic acid amide, elaidin Acid amide, N-stearyl erucic acid amide, N- (2-hydroxymethyl) stearic acid amide, N- (2-hydroxyethyl) lauric acid amide, ethylenebisolein Amide, ethylene bis-stearic acid amide, methylene bis-stearic acid amide, may be mentioned hexamethylene bis oleic acid amide, hexamethylene bis erucic acid amide, an octamethylene bis erucic acid amide and the like.

本発明において、熱可塑性樹脂に配合する脂肪酸アマイド化合物の配合量は、熱可塑性樹脂に対して0.05〜3重量%、好ましくは0.5〜2重量%である。配合量が0.05重量%未満では繊維の電荷の維持効果が小さく、3重量%を超えると効果の飽和とともに、配合物が不織布化工程で分解し製品の着発色、臭気、揮発成分の生成などの副作用が起きやすくなり好ましくない。   In this invention, the compounding quantity of the fatty acid amide compound mix | blended with a thermoplastic resin is 0.05 to 3 weight% with respect to a thermoplastic resin, Preferably it is 0.5 to 2 weight%. If the blending amount is less than 0.05% by weight, the effect of maintaining the electric charge of the fiber is small. It is not preferable because side effects such as

本発明の不織布は、上記の熱可塑性樹脂に脂肪酸アマイド化合物を配合した樹脂組成物を用い、メルトブロー法、スパンボンド法、乾式法、湿式法等で製造して得られる。
特にポリオレフィンを用いたメルトブロー法不織布としては、目付けは、好ましくは5〜100g/mであり、より好ましくは10〜40g/mである。平均繊維径は、好ましくは2〜30μmであり、より好ましくは4〜25μmである。厚みは、好ましくは0.1〜0.6mmであり、より好ましくは0.2〜0.4mmである。通気度は、好ましくは20〜200cc/sec/cmであり、より好ましくは30〜150cc/sec/cmである。このような物性を有するポリプロピレンメルトブロー不織布がエアーフィルタとして用いるのに好ましい。
また、ポリオレフィンを用いたスパンボンド法不織布としては、目付重量は、好ましくは5〜100g/mであり、より好ましくは10〜40g/mである。平均繊維径は、好ましくは10〜30μmであり、より好ましくは10〜20μmである。厚みは、好ましくは0.1〜0.6mmであり、より好ましくは0.2〜0.4mmである。通気度は、好ましくは100〜400cc/sec/cmであり、より好ましくは150〜300cc/sec/cmである。このような物性を有すポリプロピレンスパンボンド不織布がエアーフィルタとして用いるのに好ましい。
The nonwoven fabric of the present invention is obtained by using a resin composition in which a fatty acid amide compound is blended with the above thermoplastic resin, and manufactured by a melt blow method, a spun bond method, a dry method, a wet method, or the like.
In particular, as a melt blown nonwoven fabric using polyolefin, the basis weight is preferably 5 to 100 g / m 2 , more preferably 10 to 40 g / m 2 . An average fiber diameter becomes like this. Preferably it is 2-30 micrometers, More preferably, it is 4-25 micrometers. The thickness is preferably 0.1 to 0.6 mm, more preferably 0.2 to 0.4 mm. The air permeability is preferably 20 to 200 cc / sec / cm 2 , more preferably 30 to 150 cc / sec / cm 2 . A polypropylene melt blown nonwoven fabric having such physical properties is preferable for use as an air filter.
The weight per unit area of the spunbond nonwoven fabric using polyolefin is preferably 5 to 100 g / m 2 , more preferably 10 to 40 g / m 2 . An average fiber diameter becomes like this. Preferably it is 10-30 micrometers, More preferably, it is 10-20 micrometers. The thickness is preferably 0.1 to 0.6 mm, more preferably 0.2 to 0.4 mm. The air permeability is preferably 100 to 400 cc / sec / cm 2 , more preferably 150 to 300 cc / sec / cm 2 . A polypropylene spunbond nonwoven fabric having such physical properties is preferable for use as an air filter.

本発明における不織布のエレクトレット化は、水の噴流または水滴流を衝突させる方法による。水の噴流または水滴流を衝突させる方法としては、特に限定されず、不織布に水が満遍なく浸透状態にすることができる下記の方法が好ましい。
例えば、熱可塑性樹脂を多数の紡糸孔を設けた口金から溶融紡出し、その紡出糸を下方のネットに捕集して不織布にする際、口金からネットまでの紡出糸に水を噴射又は噴霧し、紡出糸を捕集して得た不織布を乾燥してエレクトレット化シートにする方法が挙げられる。このように溶融紡糸と同時に直接不織布を製布する際、口金から捕集ネットまでの紡出糸に水を噴射又は噴霧したのちネット上に不織布を形成するので、その不織布に水が満遍なく浸透状態になり、この不織布を乾燥することで高品質、高性能のエレクトレット化シートにすることができる。しかも、紡糸から一工程でエレクトレット化シートを得ることができ、また製造設備は、紡糸設備、水の噴射又は噴霧設備、乾燥設備などであるので、従来の高電圧発生設備に比べて低廉になり、かつ安全維持管理を低コストで行うことができる。
The electretization of the nonwoven fabric in the present invention is based on a method in which a jet of water or a droplet of water collides. The method of causing the water jet or water droplet flow to collide is not particularly limited, and the following method is preferable because water can be uniformly infiltrated into the nonwoven fabric.
For example, when a thermoplastic resin is melt-spun from a die having a large number of spinning holes and the spun yarn is collected in a lower net to form a nonwoven fabric, water is sprayed onto the spun yarn from the die to the net or There is a method in which the nonwoven fabric obtained by spraying and collecting the spun yarn is dried to form an electret sheet. When fabricating a nonwoven fabric directly at the same time as melt spinning, water is sprayed or sprayed onto the spun yarn from the base to the collection net, and then a nonwoven fabric is formed on the net. Thus, by drying the nonwoven fabric, a high-quality, high-performance electret sheet can be obtained. In addition, electret sheets can be obtained in one step from spinning, and the production facilities are spinning facilities, water injection or spraying facilities, drying facilities, etc., so that they are less expensive than conventional high voltage generating facilities. In addition, safety maintenance management can be performed at a low cost.

また、予め製造した熱可塑性樹脂の不織布シートを走行させながら該シートにスリット状の吸引ノズルをシート幅方向に横切るように接触させると共に、該接触部の反対側のシート面を水面に接触又は浸漬させ、該吸引ノズルから水をシート厚さ方向に貫通するように吸引して該不織布シート内に水を浸透させ、次いで該不織布シートを乾燥する方法が挙げられる。このように不織布シートを走行させながら、そのシートにスリット状の吸引ノズルを接触させ、その接触部の反対側のシート面を水面に接触又は浸漬させて、吸引ノズルから水を吸引することにより、水をシート厚さ方向に貫通するように移動させるため、シート内部の厚さ方向全体に水を浸透させることができる。しかも、吸引ノズルをシート幅方向を横切るように配置し、かつシートを走行させながら吸引を行うから、上記シート厚さ方向全体の水の浸透作用をシート全面に満遍なく行き渡らせる。したがって、このシートを乾燥すると、シート全面に電荷が均一かつ高密度に帯電したエレクトレット化シートを得ることができる。
また、上記浸透作用は、スリット状の吸引ノズルを非導電性繊維シートに接触させた箇所だけで局部的な水の吸引操作だけでよいため、小さな水槽で達成することができ、大型水槽は不要になる。したがって、製造装置を可及的にコンパクトにすることができ、また従来の高電圧発生設備が不要であるため安全且つ低コストにすることができる。
In addition, while running a nonwoven fabric sheet of a thermoplastic resin produced in advance, the sheet is brought into contact with the sheet so as to cross the slit-shaped suction nozzle in the sheet width direction, and the sheet surface opposite to the contact portion is in contact with or immersed in the water surface. And a method of sucking water through the suction nozzle so as to penetrate in the sheet thickness direction so that the water penetrates into the nonwoven fabric sheet, and then drying the nonwoven fabric sheet. While running the nonwoven sheet in this way, the slit-like suction nozzle is brought into contact with the sheet, the sheet surface on the opposite side of the contact portion is brought into contact with or immersed in the water surface, and water is sucked from the suction nozzle, Since the water is moved so as to penetrate in the sheet thickness direction, the water can be permeated throughout the thickness direction inside the sheet. In addition, since the suction nozzle is disposed so as to cross the sheet width direction and suction is performed while the sheet is running, the permeation action of the water in the entire sheet thickness direction is evenly distributed over the entire sheet surface. Therefore, when this sheet is dried, an electret sheet having a uniform and high charge on the entire surface of the sheet can be obtained.
In addition, the above-mentioned osmotic action can be achieved with a small water tank only because the slit-like suction nozzle is in contact with the non-conductive fiber sheet, so it can be achieved with a small water tank, and no large water tank is required. become. Therefore, the manufacturing apparatus can be made as compact as possible, and the conventional high voltage generating facility is unnecessary, so that it can be made safe and low in cost.

さらに、予め製造した熱可塑性樹脂の不織布シートに5GPa以上の水圧でウォータージェットを吹付け、次いで該不織布シートを乾燥する方法が挙げられる。この方法では、高圧の水圧により、水をシート厚さ方向に貫通させ、シート内部の厚さ方向全体に水を浸透させることができる。したがって、このシートを乾燥すると、シート全面に電荷が均一かつ高密度に帯電したエレクトレット化シートを得ることができる。   Furthermore, the method of spraying a water jet with the water pressure of 5 GPa or more to the nonwoven fabric sheet of the thermoplastic resin manufactured previously, and drying this nonwoven fabric sheet is mentioned. In this method, the water can be penetrated in the thickness direction inside the sheet by the high water pressure, and the water can penetrate into the entire thickness direction inside the sheet. Therefore, when this sheet is dried, an electret sheet having a uniform and high charge on the entire surface of the sheet can be obtained.

また、本発明のフィルタは、上記熱可塑性樹脂に脂肪酸アマイド化合物を配合した樹脂組成物から得られるエレクトレット化不織布にプリーツ加工等の機能を付与するために他の不織布を積層して用いても良い。積層できる不織布としては、ケミカルボンド不織布、乾式不織布、サーマルボンド乾式不織布、湿式不織布等を挙げることができる。   In addition, the filter of the present invention may be used by laminating other non-woven fabrics in order to impart functions such as pleating to the electret non-woven fabric obtained from the resin composition in which the fatty acid amide compound is blended with the thermoplastic resin. . As a nonwoven fabric which can be laminated | stacked, a chemical bond nonwoven fabric, a dry-type nonwoven fabric, a thermal bond dry-type nonwoven fabric, a wet nonwoven fabric etc. can be mentioned.

本発明のフィルタは、脂肪酸アマイド化合物が配合された熱可塑性樹脂から得られている不織布を水流によるエレクトレット化しているので、帯電量は高くなり、空気清浄用フィルタ、マスク、自動車用キャビンフィルタ、ワイパー等に有効に用いることができる。   In the filter of the present invention, since the nonwoven fabric obtained from the thermoplastic resin blended with the fatty acid amide compound is electretized by a water stream, the charge amount is increased, and the air cleaning filter, mask, automobile cabin filter, wiper Can be used effectively.

本発明を以下の実施例、比較例によって具体的に説明する。なお、物性の測定は以下の方法を用いて行った。
(1)平均繊維径:試験片の任意な5箇所を電子顕微鏡で5枚の写真撮影を行い、1枚の写真につき20本の繊維の直径を測定し、これら5枚の写真について行い、合計100本の繊維径を平均して求めた。
(2)目付け:試料長さ方向より、100×100mmの試験片を採取し、水分平衡状態の重さを測定し、1m当たりに換算して求めた。
(3)厚み:試料長さ方向より、100×100mmの試験片を採取し、ダイヤルシックネスゲージで測定した。
(4)捕集効率:0.3μmのNaCl粒子の試験用粉塵含有空気を95L/minの流量で通過させ、JIS Z 8813に準じた光散乱光量積算方式により、通過前通過後の粉塵濃度を同時に連続的に測定し、次式により、捕集効率を求めた。
捕集効率(%)=(通過後の粉塵濃度(mg/m)−通過前の粉塵濃度(mg/m))/(通過前の粉塵濃度(mg/m)×100
(5)圧力損失:捕集効率の試験と並行してアネロイド式圧力計を用い、0.3μmのNaCl粒子の試験用粉塵含有空気の通過前後の圧力を測定し、その差圧を求めた。
The present invention will be specifically described by the following examples and comparative examples. The physical properties were measured using the following methods.
(1) Average fiber diameter: Take five photographs with an electron microscope at any five points of the test piece, measure the diameter of 20 fibers per photograph, and perform these five photographs. 100 fiber diameters were averaged.
(2) Weight per unit: A test piece of 100 × 100 mm was taken from the sample length direction, the weight in a moisture equilibrium state was measured, and calculated per 1 m 2 .
(3) Thickness: A test piece of 100 × 100 mm was taken from the sample length direction and measured with a dial thickness gauge.
(4) Collection efficiency: 0.3 μm NaCl particle test air containing dust is passed at a flow rate of 95 L / min, and the dust concentration after passing before passing is measured by the light scattering light quantity integrating method according to JIS Z 8813. Simultaneously measured continuously, the collection efficiency was determined by the following equation.
Collection efficiency (%) = (Dust concentration after passage (mg / m 2 ) −Dust concentration before passage (mg / m 2 )) / (Dust concentration before passage (mg / m 2 ) × 100
(5) Pressure loss: Using an aneroid pressure gauge in parallel with the collection efficiency test, the pressure before and after the passage of the test dust-containing air of 0.3 μm NaCl particles was measured, and the differential pressure was determined.

(実施例1)
メルトフローレート50g/10分のホモポリプロピレン(PP)に対し、2重量%のエチレンビスステアリン酸アマイド(日本化成(株)製スリパックス−E)を配合した樹脂組成物を押出機によって溶融可塑化し、ポリマーラインを経て、ダイ幅20インチ、ノズル孔が10インチ当たり300孔、エアギャップ1.0mm、セットバック1.0mmのノズルピースにより樹脂全吐出量7kg/hr、ダイ温度300℃、空気温度300℃、空気流量15Nm/hr、ダイ−コンベア距離200mmで、加熱された圧縮空気とともに大気中に吐出し、これを回転スクリーン上に連続的に捕集させ、スクリーンの移動速度を適当に調節して、平均繊維径4μm、目付け40g/m、厚み0.19mmのメルトブロー不織布を得た。
次に、得られたメルトブロー不織布の片面に水を噴霧し、水の通過量が約1L/mになるように反対側から吸引を行い、その後80℃の温度で乾燥してエレクトレット化フィルタを得た。得られたフィルタの捕集効率及び圧力損失を測定した。その結果を表1に示す。
Example 1
A resin composition containing 2% by weight of ethylenebisstearic acid amide (Sripax-E manufactured by Nippon Kasei Co., Ltd.) with respect to homopolypropylene (PP) having a melt flow rate of 50 g / 10 min is melt-plasticized by an extruder. Through the polymer line, a nozzle piece with a die width of 20 inches, nozzle holes of 300 holes per 10 inches, an air gap of 1.0 mm, and a setback of 1.0 mm, a total resin discharge rate of 7 kg / hr, a die temperature of 300 ° C., and an air temperature of 300 ° C., air flow rate 15 Nm 3 / hr, the die - in conveyor length 200 mm, discharged into the atmosphere together with the heated compressed air, which is continuously collected on a rotary screen, appropriately adjusting the moving speed of the screen Thus, a melt blown nonwoven fabric having an average fiber diameter of 4 μm, a basis weight of 40 g / m 2 , and a thickness of 0.19 mm was obtained.
Next, water is sprayed on one side of the obtained melt blown nonwoven fabric, suction is performed from the opposite side so that the amount of water passing is about 1 L / m 2 , and then drying is performed at a temperature of 80 ° C. Obtained. The collection efficiency and pressure loss of the obtained filter were measured. The results are shown in Table 1.

(比較例1)
エチレンビスステアリン酸アマイドを配合しないポリプロピレンを用い、コロナ放電法によりエレクトレット化する以外は、実施例1と同様にしてフィルタを得た。得られたフィルタの捕集効率及び圧力損失を測定した。その結果を表1に示す。
(Comparative Example 1)
A filter was obtained in the same manner as in Example 1 except that polypropylene containing no ethylenebisstearic acid amide was used and electretized by a corona discharge method. The collection efficiency and pressure loss of the obtained filter were measured. The results are shown in Table 1.

(比較例2)
エチレンビスステアリン酸アマイドを配合しないポリプロピレンを用いる以外は、実施例1と同様にしてフィルタを得た。得られたフィルタの捕集効率及び圧力損失を測定した。その結果を表1に示す。
(Comparative Example 2)
A filter was obtained in the same manner as in Example 1 except that polypropylene not containing ethylenebisstearic acid amide was used. The collection efficiency and pressure loss of the obtained filter were measured. The results are shown in Table 1.

(比較例3)
エレクトレット化をコロナ放電処理による以外は、実施例1と同様にしてフィルタを得た。得られたフィルタの捕集効率及び圧力損失を測定した。その結果を表1に示す。
(Comparative Example 3)
A filter was obtained in the same manner as in Example 1 except that the electretization was performed by corona discharge treatment. The collection efficiency and pressure loss of the obtained filter were measured. The results are shown in Table 1.

Figure 0004069057
Figure 0004069057

本発明のフィルタは、脂肪酸アマイド化合物を含有する熱可塑性樹脂の不織布を水流処理法によりエレクトレット化したもので、粒子捕集効率に優れ、低圧力損失の高性能エアフィルタとして、ビル空調用フィルタ、キャビンフィルタ、マスク用として有用である。   The filter of the present invention is obtained by electretizing a thermoplastic resin nonwoven fabric containing a fatty acid amide compound by a water flow treatment method, as a high-performance air filter with excellent particle collection efficiency and low pressure loss, Useful for cabin filters and masks.

Claims (3)

熱可塑性樹脂に脂肪酸アマイド化合物を0.05〜3重量%配合した樹脂組成物から得られる極細繊維不織布を水流帯電法によりエレクトレット化した不織布からなることを特徴とする高性能エアフィルタ。   A high-performance air filter comprising a nonwoven fabric obtained by electretizing an ultrafine fiber nonwoven fabric obtained from a resin composition containing 0.05 to 3% by weight of a fatty acid amide compound in a thermoplastic resin. 熱可塑性樹脂がポリオレフィン、ポリエチレンテレフタレート、ポリブチレンテレフタレートからなる群から選ばれる少なくとも一種類の樹脂であることを特徴とする請求項1に記載の高性能エアフィルタ。   The high-performance air filter according to claim 1, wherein the thermoplastic resin is at least one resin selected from the group consisting of polyolefin, polyethylene terephthalate, and polybutylene terephthalate. 不織布が、目付け5〜100g/m、平均繊維径2〜30μm、厚み0.1〜0.6mm、通気度20〜200cc/sec/cmのポリプロピレンメルトブロー不織布であることを特徴とする請求項1又は2に記載の高性能エアフィルタ。 The nonwoven fabric is a polypropylene melt blown nonwoven fabric having a basis weight of 5 to 100 g / m 2 , an average fiber diameter of 2 to 30 μm, a thickness of 0.1 to 0.6 mm, and an air permeability of 20 to 200 cc / sec / cm 2. The high performance air filter according to 1 or 2.
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