JP3295132B2 - Filter media for dust collection - Google Patents

Filter media for dust collection

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Publication number
JP3295132B2
JP3295132B2 JP18867192A JP18867192A JP3295132B2 JP 3295132 B2 JP3295132 B2 JP 3295132B2 JP 18867192 A JP18867192 A JP 18867192A JP 18867192 A JP18867192 A JP 18867192A JP 3295132 B2 JP3295132 B2 JP 3295132B2
Authority
JP
Japan
Prior art keywords
fiber
fibers
dust
filter medium
dust collection
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.)
Expired - Fee Related
Application number
JP18867192A
Other languages
Japanese (ja)
Other versions
JPH06310A (en
Inventor
豊 大垣
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.)
Japan Vilene Co Ltd
Original Assignee
Japan Vilene Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Japan Vilene Co Ltd filed Critical Japan Vilene Co Ltd
Priority to JP18867192A priority Critical patent/JP3295132B2/en
Publication of JPH06310A publication Critical patent/JPH06310A/en
Application granted granted Critical
Publication of JP3295132B2 publication Critical patent/JP3295132B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Multicomponent Fibers (AREA)
  • Nonwoven Fabrics (AREA)
  • Filtering Materials (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、塵埃(ダスト)濃度の
高い空気を清浄化するために用いる表面濾過用濾材に関
する。
The present invention relates to a front surface filtration filter medium Ru used to clean the high dust (dust) density pneumatic.

【0002】[0002]

【従来の技術】塵埃を含む空気を清浄化する濾材には、
空調装置などに使用される内部濾過用濾材と、集塵機や
掃除機などに用いられる表面濾過用濾材とがあり、両者
はそれぞれ濾過原理を異にする。内部濾過は、塵埃濃度
が比較的低い空気の清浄化に使用され、塵埃含有気流を
目の比較的粗い濾材内部にそのまま通し、その気流が濾
材内部を通過する際に塵埃を濾材内部で捕集するもので
ある。これに対し、表面濾過とは、塵埃濃度が比較的高
い空気の清浄化に使用され、目の比較的細かい濾材を用
いる。すなわち、塵埃を濾材表面で捕集して塵埃層を濾
材表面に形成させ、その塵埃層によって次々に塵埃を捕
集し、塵埃層が或る程度の厚さになったら濾材表面から
塵埃層を除去し、再び濾材表面に塵埃層を形成させる操
作を繰り返すものである。従来、不織布を利用した表面
濾過用濾材としては、ニードルパンチフェルトの表面を
毛焼して平滑にしたもの、ニードルパンチフェルトを加
圧加熱(カレンダー)処理して表面を平滑にしたもの、
更にはニードルパンチフェルトの表面にシリコーン樹脂
やテフロン樹脂を樹脂加工して高剥離性を付与したもの
が知られている。しかしながら、これらの濾材の場合
は、ポアサイズ(開孔径)が大きくなり、塵埃が濾材内
部まで侵入し易いため、濾材内部に侵入した塵埃の払い
落としがうまくいかず、濾材寿命が短くなる。また、こ
れらの表面加工でポアサイズを小さくしようとすると、
ポアサイズのコントロールが難しく、通気抵抗が大きく
なりすぎる傾向があった。また、ニードルパンチフェル
トの表面にテフロン製微孔膜をラミネートした濾材も知
られている。この濾材は微孔膜が塵埃の濾材内部への侵
入を防ぎ、効率的な表面濾過を行い、塵埃の払い落とし
性にも優れるが、払い落とし作業時に薄膜が損傷し易
く、コストも高いという欠点があった。
2. Description of the Related Art Filter media for purifying air containing dust include:
There are filter media for internal filtration used in air conditioners and the like, and filter media for surface filtration used in dust collectors and vacuum cleaners, and both have different filtration principles. Internal filtration is used to purify air with relatively low dust concentration. The dust-containing airflow passes through the relatively coarse filter media as it is, and when the airflow passes through the filter media, the dust is collected inside the filter media. Is what you do. On the other hand, surface filtration is used for cleaning air having a relatively high dust concentration, and uses a filter medium having relatively fine eyes. That is, dust is collected on the surface of the filter medium to form a dust layer on the surface of the filter medium, and the dust layer successively collects dust. When the dust layer has a certain thickness, the dust layer is removed from the surface of the filter medium. The operation of removing and again forming a dust layer on the surface of the filter medium is repeated. Conventionally, as a filter material for surface filtration using a nonwoven fabric, a needle punch felt having a smooth surface by sintering, a needle punch felt having a smooth surface by pressurizing and heating (calender) treatment,
Further, there is known a needle punched felt in which a silicone resin or a Teflon resin is resin-processed on the surface to impart high releasability. However, in the case of these filter media, the pore size (opening diameter) increases, and dust easily enters the interior of the filter media. Therefore, it is difficult to remove the dust that has entered the interior of the filter media, and the life of the filter media is shortened. Also, if you try to reduce the pore size by these surface treatments,
It was difficult to control the pore size, and the ventilation resistance tended to be too large. Also, a filter medium in which a Teflon microporous membrane is laminated on the surface of a needle punch felt is known. This filter medium has a microporous membrane that prevents dust from entering the filter medium, performs efficient surface filtration, and excels in removing dust, but has the disadvantage that the thin film is easily damaged during the removal operation and the cost is high. was there.

【0003】[0003]

【発明が解決しようとする課題】本発明者は、細い繊維
からなる繊維ウエブを水流絡合して高密度の緻密不織布
を調製し、これを、塵埃層を形成する濾材の空気流入側
に配置すると、寿命が長く、強度が大きく、コストも低
い表面濾過用濾材が得られることを見出した。本発明
は、こうした知見に基づくものである。
SUMMARY OF THE INVENTION The present inventor has prepared a high-density dense nonwoven fabric by hydroentangling a fibrous web made of fine fibers, and disposing the nonwoven fabric on the air inflow side of a filter medium forming a dust layer. Then, they found that a filter medium for surface filtration having a long life, high strength, and low cost was obtained. The present invention is based on these findings.

【0004】[0004]

【課題を解決するための手段】従って、本発明は、平均
繊度3デニール以下の繊維からなる繊維ウェブを水流絡
合して形成した、見かけ密度0.15〜0.3g/cm3
の不織布からなる緻密層を空気流入側に有することを特
徴とする、表面濾過用の集塵用濾材に関する。本発明の
好ましい態様によれば、前記繊維ウェブは、分割繊維又
は異形断面繊維を(特には25重量%以上の量で)含有
する。また、本発明の別の好ましい態様の表面濾過用の
集塵用濾材は、コロナ放電で処理することによりエレク
トレット化されている。
SUMMARY OF THE INVENTION Accordingly, the present invention provides a water-entangled fibrous web composed of fibers having an average fineness of 3 deniers or less, and has an apparent density of 0.15 to 0.3 g / cm 3.
The present invention relates to a dust-collecting filter medium for surface filtration , characterized by having a dense layer made of a nonwoven fabric on the air inflow side. According to a preferred embodiment of the present invention, the fibrous web contains split fibers or modified cross-section fibers (particularly in an amount of 25% by weight or more). Further, the filter material for dust collection for surface filtration according to another preferred embodiment of the present invention is formed into an electret by treating with a corona discharge.

【0005】本発明の集塵用濾材は、少なくとも空気流
入側に不織布からなる緻密層を有する。この不織布は、
ウエブ構成繊維として平均繊度が3デニール以下の細い
繊維を用いることによりポアサイズを小さくすると共
に、水流絡合によってウェブを高密度に絡合させ、更に
水流を施した側の表面に平滑性を付与することができ
る。これらの点は、従来の不織布濾材において利用され
ていたニードルパンチ処理では、細い繊維を高密度に絡
合させることが困難であり、ポアサイズを小さくするこ
とが容易でなかったこと、しかも表面平滑にするために
は、毛焼や加熱加圧などの平滑処理が必要であったこと
などと比較して、本発明の優れた点である。なお、平均
繊度が3デニールより太いとポアサイズが大きくなり、
捕集効果が低下すると共に塵埃の払い落とし性が悪くな
る。また、平均繊度の下限は特に制限されない。更に、
緻密層を形成する不織布の見かけ密度が0.15g/cm
3 より小さいと、濾材の捕集効果が低下する。一方、見
かけ密度0.3g/cm3 より大きいと、通気抵抗が大き
くなりすぎる。
The filter for dust collection of the present invention has a dense layer made of a nonwoven fabric at least on the air inflow side. This non-woven fabric
By using fine fibers having an average fineness of 3 denier or less as the web constituent fibers, the pore size is reduced, and the web is entangled at a high density by water entanglement, and further, the surface on the side subjected to water flow is provided with smoothness. be able to. These points indicate that it is difficult to entangle fine fibers at a high density in the needle punching process used in conventional nonwoven fabric filter media, and it was not easy to reduce the pore size. This is an excellent point of the present invention as compared with the necessity of smoothing treatment such as scabbing and heating and pressurizing. In addition, if the average fineness is larger than 3 denier, the pore size will increase,
The trapping effect is reduced, and the dust wiping property is deteriorated. The lower limit of the average fineness is not particularly limited. Furthermore,
The apparent density of the nonwoven fabric forming the dense layer is 0.15 g / cm
If it is smaller than 3 , the effect of collecting the filter medium will decrease. On the other hand, if the apparent density is larger than 0.3 g / cm 3 , the airflow resistance becomes too large.

【0006】本発明濾材の緻密層を構成する不織布の構
成繊維も特に制限されるものではなく、ポリエステル、
ポリプロピレン、ポリアミドやレーヨンなどを用いるこ
とができるが、分割繊維及び/又は異形断面繊維を少な
くとも一部含有させるのが好ましい。分割繊維として
は、例えば図1に示すような繊維断面の2成分以上の樹
脂からなる繊維を使用することができる。なお、図1の
分割繊維1は、分割前は例えばポリアミド繊維部分2と
ポリエステル繊維部分3とが結合した1本の糸としての
形状を有するが〔図1(a)〕、機械的ショックなどに
よって、ポリアミド繊維部分2〔図1(b)〕とポリエ
ステル繊維部分3〔図1(c)〕とに容易に分割され、
各繊維部分2及び3は、分割前の糸よりも更に細い糸に
なって不織布を構成することになるので、緻密性が向上
し、表面積が増加する。樹脂の組合せとしては、ポリア
ミド−ポリエステル、ポリアミド−ポリエチレンテレフ
タレート、ポリプロピレン−ポリエステル、ポリプロピ
レン−ポリエチレンなどが適している。また、断面形状
も図1に示すもの以外に多数のものが知られており、そ
れらを任意に用いることができる。分割繊維としては、
機械的衝撃や一成分を抽出することにより分割できる繊
維を使用することができる。特に、水流絡合時の機械的
衝撃により分割する繊維を使用すれば、繊維の分割と絡
合とを同時に実施することができるので好ましい。な
お、本明細書において、分割繊維の平均繊度は分割前の
数値である。
[0006] The constituent fibers of the nonwoven fabric constituting the dense layer of the filter medium of the present invention are not particularly limited.
Polypropylene, polyamide, rayon or the like can be used, but it is preferable to include at least a part of split fibers and / or fibers of irregular cross section. As the split fibers, for example, fibers made of a resin having two or more components having a fiber cross section as shown in FIG. 1 can be used. Before splitting, the split fiber 1 in FIG. 1 has, for example, a single yarn shape in which a polyamide fiber portion 2 and a polyester fiber portion 3 are combined (FIG. 1A), but is subjected to mechanical shock or the like. Easily divided into a polyamide fiber portion 2 (FIG. 1 (b)) and a polyester fiber portion 3 (FIG. 1 (c)),
Since each of the fiber portions 2 and 3 becomes a thinner yarn than the yarn before splitting and forms a nonwoven fabric, the denseness is improved and the surface area is increased. Suitable combinations of resins include polyamide-polyester, polyamide-polyethylene terephthalate, polypropylene-polyester, and polypropylene-polyethylene. Also, many cross-sectional shapes other than those shown in FIG. 1 are known, and any of them can be used. As split fibers,
Fibers that can be split by mechanical impact or by extracting one component can be used. In particular, it is preferable to use a fiber that is split by mechanical impact at the time of water entanglement, because the splitting and entanglement of the fiber can be performed simultaneously. In addition, in this specification, the average fineness of the split fiber is a numerical value before splitting.

【0007】異形断面繊維(断面が円形でない繊維)と
しても、各種断面形状を有する繊維を任意に用いること
ができ、例えば図2に示すような繊維断面形状をもつレ
ーヨン系繊維を使用することができる。これらの異形断
面繊維を用いることにより、表面積が増加する。通常繊
維でウェブを構成する場合は、細い繊維を用いるのが好
ましい。分割繊維及び/又は異形繊維を用いる場合は、
それらを25重量%以上含有させることにより、緻密性
を向上させて表面濾過効果を大きくするのが好ましい。
なお、集塵用濾材を構成する繊維に、前記緻密層も含め
て、芳香族ポリアミド系繊維、ポリフェニレンサルファ
イド(PPS)系繊維、ポリイミド系繊維などの耐熱性
繊維を使用して、本発明の集塵用濾材を耐熱性にするこ
とができる。
As the irregular cross-section fiber (fiber having a non-circular cross section), fibers having various cross-sections can be arbitrarily used. For example, rayon-based fibers having a fiber cross-section as shown in FIG. 2 can be used. it can. By using these modified cross-section fibers, the surface area is increased. When the web is usually made of fibers, it is preferable to use thin fibers. When using split fibers and / or deformed fibers,
It is preferred that by containing them in an amount of 25% by weight or more, the compactness is improved and the surface filtration effect is increased.
The fibers constituting the filter material for dust collection, including the dense layer, include heat-resistant fibers such as aromatic polyamide fibers, polyphenylene sulfide (PPS) fibers, and polyimide fibers. The dust filter medium can be made heat-resistant.

【0008】本発明の集塵用濾材は単層であっても多層
であってもよいが、空気流入側の表面層は前記の緻密層
でなければならない。緻密層の厚さは特に限定されな
い。他の層についても特に限定されないが、集塵用濾材
全体の通気抵抗などを考慮すると、緻密層よりも密度の
低いものが望ましい。また、補強のために織物、メッシ
ュ、フィラメントなどの補強材を積層してもよい。この
場合、補強材には引張強度が10kg/5cm幅以上のもの
を使用するのが望ましい。本発明の水流絡合は、水圧5
0〜200kg/cm2 の条件で行うことができる。更に、
集塵用濾材の引張強度を高めるために、繊維結合手段と
して水流絡合の他に熱接着性繊維や接着剤による結合を
用いてもよい。とくに、濾材の全面又は一部を加熱加圧
処理すると、濾材の強度を向上させるだけでなく、表面
耐性や表面平滑性を高めることができるので好ましい。
本発明の集塵用濾材は、少なくとも緻密層をエレクトレ
ット化して帯電状態にし、静電気を利用して集塵効率を
向上させるのが好ましい。エレクトレット化は、例え
ば、4kV/cm以上の電界強度のコロナ放電処理によって
実施することができる。
The filter material for dust collection of the present invention may be a single layer or a multilayer, but the surface layer on the air inflow side must be the dense layer described above. The thickness of the dense layer is not particularly limited. The other layers are not particularly limited, but those having a lower density than the dense layer are preferable in consideration of the ventilation resistance of the entire filter for dust collection. Further, a reinforcing material such as a woven fabric, a mesh, or a filament may be laminated for reinforcement. In this case, it is desirable to use a reinforcing material having a tensile strength of 10 kg / 5 cm width or more. The water entanglement of the present invention has a water pressure of 5
It can be performed under the conditions of 0 to 200 kg / cm 2 . Furthermore,
In order to increase the tensile strength of the filter material for dust collection, bonding with a thermoadhesive fiber or an adhesive may be used as the fiber bonding means in addition to the hydroentanglement. In particular, it is preferable to heat and press the entire surface or a part of the filter medium because not only the strength of the filter medium can be improved, but also the surface resistance and the surface smoothness can be increased.
In the filter for dust collection of the present invention, it is preferable that at least the dense layer is electretized to be in a charged state, and the dust collection efficiency is improved by utilizing static electricity. The electretization can be performed by, for example, corona discharge treatment with an electric field strength of 4 kV / cm or more.

【0009】[0009]

【実施例】以下、実施例によって本発明を具体的に説明
するが、これらは本発明の範囲を限定するものではな
い。なお、以下の実施例において、塵埃捕集効率及び初
期圧力損失は、平均粒度0.5μmの大気塵を含む気流
を風速5cm/秒で通過させて測定した値である。実施例1:分割繊維不織布濾材 図1(a)の繊維断面を有するポリアミド−ポリエステ
ルの樹脂成分の組合せをもつ分割繊維(繊度2デニー
ル;繊維長51mm)からなる目付150g/m2の繊維
ウェブに、水圧100kg/cm2 の条件で水流絡合を施し
て、分割繊維を分割〔図1(b)及び(c)参照〕する
と共に繊維を絡合させて、厚さ0.7mm、見かけ密度
0.21g/cm3 の集塵用濾材を得た。この濾材の塵埃
捕集効果は45%で、初期圧力損失は6mmH2 Oであっ
た。
EXAMPLES The present invention will be described below in more detail with reference to examples, but these examples do not limit the scope of the present invention. In the following examples, the dust collection efficiency and the initial pressure loss are values measured by passing an airflow containing atmospheric dust having an average particle size of 0.5 μm at a wind speed of 5 cm / sec. Example 1: Filtered fiber non-woven fabric filter material A fiber web having a basis weight of 150 g / m 2 composed of divided fibers (denier: 2 denier; fiber length: 51 mm) having a combination of a polyamide-polyester resin component having a fiber cross section shown in FIG. Under the condition of a water pressure of 100 kg / cm 2, the fibers are entangled to split the split fibers (see FIGS. 1 (b) and (c)), and the fibers are entangled to have a thickness of 0.7 mm and an apparent density of 0. A filter material for dust collection of 0.21 g / cm 3 was obtained. In the dust collecting effect is 45% of the filter medium, the initial pressure loss was 6mmH 2 O.

【0010】実施例2:異形繊維と通常繊維との不織布
濾材 図2の繊維断面を有する異形断面レーヨン繊維(繊度
1.5デニール;繊維長51mm)50%とポリエステル
繊維(繊度1.5デニール;繊維長51mm)50%とか
らなる目付180g/m2 の繊維ウェブに、水圧100
kg/cm2 の条件で水流絡合を施して、厚さ1.1mm、見
かけ密度0.16g/cm3 の集塵用濾材を得た。この濾
材の塵埃捕集効率は46%で、初期圧力損失は1.4mm
2 Oであった。
Example 2: Non-woven fabric of modified fiber and ordinary fiber
Filtering material : 180% / m 2 basis weight composed of 50% irregular rayon fiber (1.5 denier fineness; fiber length 51 mm) having a fiber cross section of FIG. 2 and 50% polyester fiber (1.5 denier fineness; 51 mm fiber length) Water pressure of 100 on fiber web
Water entanglement was performed under the condition of kg / cm 2 to obtain a filter material for dust collection having a thickness of 1.1 mm and an apparent density of 0.16 g / cm 3 . This filter medium has a dust collection efficiency of 46% and an initial pressure loss of 1.4 mm.
Was H 2 O.

【0011】比較例1:ニードルパンチ・通常繊維不織
布濾材 ポリエステル繊維(繊度1.5デニール;繊維長51m
m)からなる目付500g/m2 の繊維ウェブに、針密
度500本/cm2 の条件でニードルパンチを施して、厚
さ2.0mm、見かけ密度0.25g/cm3 の集塵用濾材
を得た。この濾材の塵埃捕集効率は30%で、初期圧力
損失は3.0mmH2 Oであった。
Comparative Example 1: Needle punch / non-woven fabric
Cloth filter media polyester fiber (denier 1.5 denier; fiber length 51m)
m), a fiber web having a basis weight of 500 g / m 2 was subjected to needle punching under the condition of a needle density of 500 needles / cm 2 to obtain a filter medium for dust collection having a thickness of 2.0 mm and an apparent density of 0.25 g / cm 3. Obtained. The dust collection efficiency of this filter medium was 30%, and the initial pressure loss was 3.0 mmH 2 O.

【0012】比較例2:太繊度通常繊維の水流絡合不織
布濾材 ポリエステル繊維(繊度4デニール;繊維長51mm)か
らなる目付150g/m2 の繊維ウェブに、水圧100
kg/cm2 の条件で水流絡合を施して、厚さ0.9mm、見
かけ密度0.17g/cm3 の集塵用濾材を得た。この濾
材の塵埃捕集効率は20%で、初期圧力損失は1.5mm
2 Oであった。
Comparative Example 2: Hydro-entangled nonwoven of large fineness ordinary fiber
Cloth filter media polyester fibers; a of basis weight 150 g / m 2 consisting of (fineness 4 deniers fiber length 51 mm) fiber web, pressure 100
Water entanglement was performed under the condition of kg / cm 2 to obtain a filter material for dust collection having a thickness of 0.9 mm and an apparent density of 0.17 g / cm 3 . This filter medium has a dust collection efficiency of 20% and an initial pressure loss of 1.5 mm.
Was H 2 O.

【0013】実施例3:分割繊維と通常繊維との不織布
濾材 前記実施例1で用いたポリアミド−ポリエステルの樹脂
成分の組合せをもつ分割繊維(繊度2デニール;繊維長
51mm)30%と、ポリエステル繊維(繊度1.5デニ
ール;繊維長51mm)70%とからなる目付150g/
2 の繊維ウェブに、水圧100kg/cm2 の条件で水流
絡合を施して、分割繊維を分割すると共に繊維を絡合さ
せて、厚さ0.8mm、見かけ密度0.19g/cm3 の集
塵用濾材を得た。この濾材の塵埃捕集効率は38%で、
初期圧力損失は4.5mmH2 Oであった。
Example 3: Nonwoven fabric of split fiber and ordinary fiber
Filter media : 30% of split fibers (fineness: 2 denier; fiber length: 51 mm) having a combination of the polyamide-polyester resin components used in Example 1 and 70% of polyester fibers (fineness: 1.5 denier; fiber length: 51 mm) Net weight 150g /
A water entanglement is applied to the fiber web of m 2 under the condition of a water pressure of 100 kg / cm 2 to split the split fibers and entangle the fibers to obtain a 0.8 mm thick, 0.19 g / cm 3 apparent density. A filter material for dust collection was obtained. The dust collection efficiency of this filter medium is 38%,
Initial pressure loss was 4.5mmH 2 O.

【0014】実施例4:異形繊維と通常繊維との不織布
濾材 前記実施例2で用いた異形断面レーヨン繊維(繊度1.
5デニール;繊維長51mm)30%と、ポリエステル繊
維(繊度1.5デニール;繊維長51mm)70%とから
なる目付180g/m2 の繊維ウェブに、水圧100kg
/cm2 の条件で水流絡合を施して、厚さ0.12mm、見
かけ密度0.15g/cm3 の集塵用濾材を得た。この濾
材の塵埃捕集効率は40%で、初期圧力損失は0.8mm
2 Oであった。
Example 4: Non-woven fabric of modified fiber and ordinary fiber
Filter media Rayon fiber with irregular cross section used in Example 2 (fineness 1.
100 kg of water pressure is applied to a fiber web having a basis weight of 180 g / m 2 , which is composed of 30% of 5 denier; fiber length 51 mm) and 70% of polyester fiber (fineness 1.5 denier; fiber length 51 mm).
/ Cm 2 to obtain a filter medium for dust collection having a thickness of 0.12 mm and an apparent density of 0.15 g / cm 3 . This filter medium has a dust collection efficiency of 40% and an initial pressure loss of 0.8 mm.
Was H 2 O.

【0015】実施例5:エレクトレット化濾材 ポリプロピレン繊維(繊度2デニール;繊維長51mm)
からなる目付120g/m2 の繊維ウェブに、水圧10
0kg/cm2 の条件で水流絡合を施して、厚さ0.8mm、
見かけ密度0.15g/cm3 とし、次いで5KV/cmの
条件でコロナ放電処理をしてエレクトレット化された集
塵用濾材を得た。この濾材の塵埃捕集効率は55%で、
初期圧力損失は1.0mmH2 Oであった。
Example 5: Electretized filter medium polypropylene fiber (denier 2 denier; fiber length 51 mm)
A fibrous web with a basis weight of 120 g / m 2 consisting of
Water entanglement under the condition of 0 kg / cm 2 , thickness 0.8 mm,
An apparent density of 0.15 g / cm 3 was obtained, and then a corona discharge treatment was performed at 5 KV / cm to obtain an electretized filter material for dust collection. The dust collection efficiency of this filter medium is 55%,
Initial pressure loss was 1.0mmH 2 O.

【0016】実施例6:耐熱性濾材 空気流入側の繊維層として、芳香族ポリアミド繊維(繊
度2デニール;繊維長51mm)30%、ポリイミド繊維
(繊度1.5デニール;繊維長51mm)30%、及びポ
リフェニレンサルファイド繊維(繊度2デニール;繊維
長51mm)40%からなる目付60g/m2 の繊維ウェ
ブを、そして空気流出側の繊維層として芳香族ポリアミ
ド繊維(繊度3デニール;繊維長51mm)60%、及び
ポリフェニレンサルファイド繊維(繊度2デニール;繊
維長51mm)40%からなる目付100g/m2 の繊維
ウェブを積層して、水圧150kg/cm2 の条件で水流絡
合を施して、厚さ0.9mm、見かけ密度0.17g/cm
3 の集塵用濾材を得た。この濾材の塵埃捕集効率は45
%で、初期圧力損失は0.8mmH2 Oであった。
Example 6: 30% of aromatic polyamide fiber (fineness: 2 denier; fiber length: 51 mm), 30% of polyimide fiber (fineness: 1.5 denier, fiber length: 51 mm) as a fiber layer on the air inlet side of the heat-resistant filter medium . And a fiber web having a basis weight of 60 g / m 2 composed of 40% of polyphenylene sulfide fiber (fineness: 2 denier; fiber length: 51 mm) and aromatic polyamide fiber (fineness: 3 denier; fiber length: 51 mm) 60% as a fiber layer on the air outflow side. And a polyphenylene sulfide fiber (denier: 2 denier; fiber length: 51 mm), a fiber web having a basis weight of 100 g / m 2 and a water entanglement under a water pressure of 150 kg / cm 2 . 9mm, apparent density 0.17g / cm
The filter material for dust collection of No. 3 was obtained. The dust collection efficiency of this filter medium is 45
%, The initial pressure loss was 0.8mmH 2 O.

【0017】実施例7:湿式水流絡合通常繊維不織布濾
ポリエステル繊維(繊度0.1デニール;繊維長5mm)
からなる目付100g/m2 の繊維ウェブを湿式抄紙
後、水圧100kg/cm2 の条件で水流絡合を施して、厚
さ0.6mm、見かけ密度0.17g/cm3 の集塵用濾材
を得た。この濾材の塵埃捕集効果は55%で、初期圧力
損失は16mmH2 Oであった。
Example 7: Wet water entangled ordinary fiber non-woven fabric filter
Material polyester fiber (fineness 0.1 denier; fiber length 5 mm)
100 g / m 2 of a fiber web made by wet papermaking, and then subjected to hydroentanglement under the condition of a water pressure of 100 kg / cm 2 to obtain a filter material for dust collection having a thickness of 0.6 mm and an apparent density of 0.17 g / cm 3. Obtained. In the dust collecting effect is 55% of the filter medium, the initial pressure loss was 16mmH 2 O.

【0018】[0018]

【発明の効果】本発明による集塵用濾材は、細い繊維か
らなる高密度の緻密不織布層を空気流入側に配置してい
るので、表面濾過用濾材として、寿命が長く、強度が大
きく、製造コストも低い。本発明の濾材は、例えば、集
塵機や掃除機用の濾材として有用である。
The filter medium for dust collection according to the present invention has a long life and a large strength as a filter medium for surface filtration because a high-density dense nonwoven fabric layer made of fine fibers is arranged on the air inflow side. Cost is low. The filter medium of the present invention is useful, for example, as a filter medium for dust collectors and vacuum cleaners.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明で用いることのできる分割繊維の断面図
であり、(a)は分割前の断面図、(b)は分割後のポ
リアミド繊維部分の断面図、そして(c)は分割後のポ
リエステル繊維部分の断面図である。
FIG. 1 is a cross-sectional view of a split fiber that can be used in the present invention, where (a) is a cross-sectional view before splitting, (b) is a cross-sectional view of a polyamide fiber portion after splitting, and (c) is a cross-sectional view after splitting. FIG. 2 is a cross-sectional view of a polyester fiber portion.

【図2】本発明で用いることのできる異形繊維の断面図
である。
FIG. 2 is a cross-sectional view of a modified fiber that can be used in the present invention.

【符号の説明】[Explanation of symbols]

1・・・分割繊維 2・・・ポリアミド繊維部分 3・・・ポリエステル繊維部分 DESCRIPTION OF SYMBOLS 1 ... Split fiber 2 ... Polyamide fiber part 3 ... Polyester fiber part

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 平均繊度3デニール以下の繊維からなる
繊維ウェブを水流絡合して形成した、見かけ密度0.1
5〜0.3g/cm3 の不織布からなる緻密層を空気流入
側に有することを特徴とする、表面濾過用の集塵用濾
材。
An apparent density of 0.1 formed by hydroentanglement of a fiber web composed of fibers having an average fineness of 3 deniers or less.
A dust-collecting filter medium for surface filtration , comprising a dense layer made of a nonwoven fabric of 5 to 0.3 g / cm 3 on the air inflow side.
【請求項2】 繊維ウェブ中に分割繊維又は異形繊維を
含有する請求項1に記載の表面濾過用の集塵用濾材。
2. The filter material for dust collection for surface filtration according to claim 1, wherein the fibrous web contains split fibers or modified fibers.
【請求項3】 繊維ウェブ中に分割繊維又は異形繊維を
25重量%以上含有する請求項2に記載の表面濾過用の
集塵用濾材。
3. The filter medium for surface filtration according to claim 2, wherein the fibrous web contains at least 25% by weight of split fibers or irregular fibers.
JP18867192A 1992-06-23 1992-06-23 Filter media for dust collection Expired - Fee Related JP3295132B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18867192A JP3295132B2 (en) 1992-06-23 1992-06-23 Filter media for dust collection

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18867192A JP3295132B2 (en) 1992-06-23 1992-06-23 Filter media for dust collection

Publications (2)

Publication Number Publication Date
JPH06310A JPH06310A (en) 1994-01-11
JP3295132B2 true JP3295132B2 (en) 2002-06-24

Family

ID=16227818

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18867192A Expired - Fee Related JP3295132B2 (en) 1992-06-23 1992-06-23 Filter media for dust collection

Country Status (1)

Country Link
JP (1) JP3295132B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU4593697A (en) * 1996-09-20 1998-04-14 Johns Manville International, Inc. Resilient mat; a method of making the resilient mat and a battery including the resilient mat
JP2000117027A (en) * 1998-08-10 2000-04-25 Toray Ind Inc Filter cloth and bag filter for dust collection
DE69929797T2 (en) 1998-08-10 2006-10-12 Toray Industries, Inc. DUST FILTER AND FILTER BAG
JP2002001020A (en) * 2000-04-10 2002-01-08 Toray Ind Inc Filter media
JP4687495B2 (en) * 2005-02-18 2011-05-25 東レ株式会社 Bag filter cloth and bag filter
JP6133035B2 (en) * 2012-10-03 2017-05-24 ダイワボウホールディングス株式会社 Electrostatic filter

Also Published As

Publication number Publication date
JPH06310A (en) 1994-01-11

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