JP2554259Y2 - Filter cloth - Google Patents

Filter cloth

Info

Publication number
JP2554259Y2
JP2554259Y2 JP1991083793U JP8379391U JP2554259Y2 JP 2554259 Y2 JP2554259 Y2 JP 2554259Y2 JP 1991083793 U JP1991083793 U JP 1991083793U JP 8379391 U JP8379391 U JP 8379391U JP 2554259 Y2 JP2554259 Y2 JP 2554259Y2
Authority
JP
Japan
Prior art keywords
fibers
nonwoven fabric
filter cloth
melting point
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.)
Expired - Fee Related
Application number
JP1991083793U
Other languages
Japanese (ja)
Other versions
JPH0526122U (en
Inventor
邦夫 俣木
一成 福嶋
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.)
Daiwabo Co Ltd
Daiwabo Holdings Co Ltd
Original Assignee
Daiwabo Co Ltd
Daiwabo Holdings 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 Daiwabo Co Ltd, Daiwabo Holdings Co Ltd filed Critical Daiwabo Co Ltd
Priority to JP1991083793U priority Critical patent/JP2554259Y2/en
Publication of JPH0526122U publication Critical patent/JPH0526122U/en
Application granted granted Critical
Publication of JP2554259Y2 publication Critical patent/JP2554259Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Filtering Materials (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Laminated Bodies (AREA)
  • Nonwoven Fabrics (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案は、流体中の微細なダスト
を捕捉集塵するに好適なバグフィルター用の濾過布に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter cloth for a bag filter suitable for capturing and collecting fine dust in a fluid.

【0002】[0002]

【従来の技術】バグフィルターのように気体中の微細な
ダストの捕集に使用されている濾過布は、高強度と形態
安定性のほかに緻密性が要求されるため、濾過布には従
来から重厚な織物や不織布が用いられている。ところが
近年においては種々な分野においてより高精度な集塵性
が要求されるに至り、従来の濾過布ではこれらの要求に
対応することが困難であることから濾過精度の高い濾過
布が要望されている。そしてかかる要望に対応して例え
ば特開平3−60712号公報にみられるようにニード
ルフェルトの表面に平均繊度0.2デニール以下の極細
繊維からなる不織布シートをラミネートした濾過布が提
案されている。
2. Description of the Related Art Filter cloth used for collecting fine dust in a gas, such as a bag filter, is required to be dense in addition to high strength and form stability. And heavy woven and non-woven fabrics are used. However, in recent years, more accurate dust collection has been required in various fields, and it is difficult to meet these requirements with conventional filter cloths. I have. In response to this demand, for example, as disclosed in Japanese Patent Application Laid-Open No. 3-60712, there has been proposed a filter cloth in which a nonwoven fabric sheet made of ultrafine fibers having an average fineness of 0.2 denier or less is laminated on the surface of a needle felt.

【0003】[0003]

【考案が解決しようとする課題】しかしながらニードル
フェルトの表面に平均繊度0.2デニール以下の極細繊
維からなる不織布シートをラミネートしてなる濾過布
は、強力、形態安定性に優れ、また微粒子の集塵効率も
良いという多くの長所を具備しているが、濾過面(ダス
ト供給側)はラミネート時における加圧により平滑化さ
れているに留まり、濾過面に付着したダストの払い落と
し性において必ずしも満足すべきものではない。そして
この払い落とし性の良し悪しは、圧力損失や濾過布の交
換周期に影響を及ぼすことになる。本考案は上記課題を
改善することを目的としてなされたものである。
However, a filter cloth obtained by laminating a nonwoven fabric sheet made of ultrafine fibers having an average fineness of 0.2 denier or less on the surface of a needle felt is excellent in strength, form stability and fine particle collection. Although it has many advantages of good dust efficiency, the filtration surface (dust supply side) is only smoothed by pressing during lamination, and it is not always satisfactory in removing dust attached to the filtration surface Not something to do. And the pay-off of the good or bad will be及boss an effect on the exchange period of pressure loss and filtration cloth. The present invention has been made to improve the above problems.

【0004】[0004]

【課題を解決するための手段】本考案は、織物基布の上
に接合する不織布の少なくとも一部に低融点極細繊維と
高融点極細繊維を使用し、熱ロールによる濾過面側の平
滑化処理時に低融点極細繊維を軟化させることによって
通気度を抑制とともに濾過面の平滑性をより高め、ダス
トの払い落とし性を向上させた。即ち本考案は、目付が
200〜800g/m2の織物基布の上に、分割型複合繊維
が分割して形成された太さ0.5デニール以下の低融点
極細繊維と高融点極細繊維とが1:1の割合で混在した
極細繊維材料少なくとも50重量%以上含有し、かつ
不織布を構成する繊維同士がニードルパンチもしくは高
圧液体流により交絡してなる目付60〜250g/m2の不
織布をバインダーを介して接合し、その不織布表面に熱
カレンダー処理を施して濾過面の上記低融点極細繊維
軟化し隣接繊維間を接着することによって濾過面を平滑
化し、通気度を3〜15ml/cm2/secに抑制して濾過布と
なしたものである。
SUMMARY OF THE INVENTION The present invention uses a low-melting ultrafine fiber and a high-melting ultrafine fiber for at least a part of a non-woven fabric to be bonded onto a woven fabric base, and smoothes the filtration surface with a hot roll. In some cases, the low-melting ultrafine fibers were softened to suppress the air permeability, further increase the smoothness of the filtration surface, and improve the dust removal property. That is, the present invention has, on basis weight of the fabric the base fabric of 200 to 800 g / m 2, the splittable conjugate fibers
There the low melting point microfine fiber thickness 0.5 denier or less that are formed by dividing a high melting point microfine fibers is 1: The mixed ultrafine fiber material in a ratio of 1 contains at least 50% by weight or more, and
Needle punch or high
A nonwoven fabric having a basis weight of 60 to 250 g / m 2 entangled by a pressurized liquid flow is joined via a binder, and the surface of the nonwoven fabric is subjected to a heat calendering treatment to soften the low-melting point ultrafine fibers on the filtration surface and to reduce the distance between adjacent fibers. The filter surface is smoothed by bonding, and the air permeability is suppressed to 3 to 15 ml / cm 2 / sec to form a filter cloth.

【0005】低融点極細繊維と高融点極細繊維とが1:
1の割合で混在した0.5デニール以下の極細繊維材料
は、分割型複合繊維を分割することによって得ることが
できる。この分割型複合繊維の構成成分としては、例え
ばポリエチレン、ポリプロピレン、ポリ4−メチルペン
テン−1、エチレン−ビニルアルコール共重合体、エチ
レン−酢酸ビニル共重合体等のポリオレフィン系重合体
もしくは共重合体、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系重合体もし
くは共重合体、ナイロン6、ナイロン66、ナイロン1
2等のポリアミド系重合体もしくは共重合体等の中から
適宜選択することができるが、20℃以上の融点差を有
する2成分以上で構成するとよい。分割型複合繊維の繊
維断面形状も種々考えられ、特に限定するものではない
が、放射線状型が好ましい。
[0005] The low melting point ultrafine fiber and the high melting point ultrafine fiber are:
The ultrafine fiber material of 0.5 denier or less mixed at a ratio of 1 can be obtained by dividing the splittable conjugate fiber. As constituent components of the splittable conjugate fiber, for example, polyethylene, polypropylene, poly-4-methylpentene-1, ethylene-vinyl alcohol copolymer, polyolefin-based polymer or copolymer such as ethylene-vinyl acetate copolymer, Polyester polymers or copolymers such as polyethylene terephthalate and polybutylene terephthalate, nylon 6, nylon 66, nylon 1
Although it can be appropriately selected from polyamide-based polymers or copolymers such as No. 2 and the like, it may be composed of two or more components having a melting point difference of 20 ° C. or more. Various fiber cross-sectional shapes of the splittable conjugate fiber can be considered and are not particularly limited, but a radial type is preferable.

【0006】濾過面となる不織布層は、上記分割型複合
繊維を分割した0.5デニール以下の極細繊維を50重
量%以上、好ましくは85重量%以上含有した目付60
〜250g/m2の不織布が好ましい。不織布は、上記繊維
をカード法、クロスレイヤー法、ランダムウェバー法、
湿式抄造法、乾式または湿熱接着法、ニードルパンチ
法、高圧液流法等により不織布となすが、この時点で分
割が不十分のものは更にニードルパンチ処理、高圧液流
処理、超音波処理等の処理を施すが特に高圧液体流処理
が好ましく、条件としては、吐出水圧が30〜200kg
/cm2、 好ましくは80〜150kg/cm2、速度が1〜5m/
min で少なくとも表裏各2回処理することが好ましい。
吐出水圧が30kg/cm2未満、速度が5m/min より速いと
分割不十分となり、微粒子集塵効率があがらず、吐出水
圧200kg/cm2より大きく、速度が1m/min 未満である
と過剰処理となり、不経済である。また、不織布には5
0重量%未満の他繊維を混綿することができるが、他繊
維としては綿、麻等の天然繊維、レーヨン等の半合成繊
維、ポリオレフィン、ポリエステル、ポリアミド等の合
成繊維の中から使用用途に応じて適宜選択すればよい。
極細繊維が0.5デニールを超えたり、上記極細繊維の
含有量が50重量%未満であり、また目付が60g/m2
満であると微粒子捕捉が期待できない。また逆に上記不
織布の目付を250g/m2以上となしてもさほど微粒子捕
捉効率が上がらず価格が高くつくのみとなる。
[0006] The nonwoven fabric layer serving as a filtration surface contains at least 50% by weight, preferably at least 85% by weight, of ultrafine fibers of 0.5 denier or less obtained by dividing the splittable conjugate fiber.
Nonwoven to 250 g / m 2 is preferred. For the non-woven fabric, the above fibers are formed by a card method, a cross-layer method, a random webber method,
Nonwoven fabrics are formed by wet papermaking, dry or wet heat bonding, needle punching, high-pressure liquid flow, etc. High pressure liquid flow treatment is particularly preferable, and the discharge water pressure is 30 to 200 kg.
/ cm 2 , preferably 80-150 kg / cm 2 , speed 1-5 m /
It is preferable to perform the treatment at least twice on each of the front and back sides with min.
If the discharge water pressure is less than 30 kg / cm 2 and the speed is higher than 5 m / min, the division will be insufficient, the efficiency of collecting fine particles will not be improved, and if the discharge water pressure is higher than 200 kg / cm 2 and the speed is less than 1 m / min, excessive processing will be performed. It is uneconomical. In addition, 5
Other fibers of less than 0% by weight can be mixed, but other fibers may be selected from natural fibers such as cotton and hemp, semi-synthetic fibers such as rayon, and synthetic fibers such as polyolefin, polyester and polyamide according to the intended use. May be selected as appropriate.
If the ultrafine fibers exceed 0.5 denier, if the content of the ultrafine fibers is less than 50% by weight, and if the basis weight is less than 60 g / m 2 , fine particle capture cannot be expected. Conversely, even if the basis weight of the nonwoven fabric is 250 g / m 2 or more, the efficiency of capturing fine particles does not increase so much and only the cost increases.

【0007】織物基布としては、上記不織布層の低融点
成分より融点の高い繊維からなる基布であればよく、例
えば1.5デニール以上の合成繊維スパン糸、マルチフ
ィラメントで構成され、濾過布として強度と形態を保て
る織物が好ましい。織物基布に使用する合成繊維として
は、単一成分繊維あるいは並列型、芯鞘型、分割型、海
島型等の複合繊維等いずれをも用いることができるが、
経済的にみて単一成分繊維が好ましく、例えば上記記載
のポリオレフィン、ポリエステル、ポリアミド等繊維を
用いるとよい。織物基布の目付としては、200〜80
0g/m2、好ましくは400〜600g/m2であり、目付が
200g/m2未満であると濾過布としての形態保持が難し
く、800g/m2より大きくなると濾過布として嵩張った
ものとなる。
The woven fabric base fabric may be any fabric that is made of fibers having a melting point higher than that of the low melting point component of the nonwoven fabric layer. For example, it is composed of synthetic fiber spun yarn of 1.5 denier or more, multifilament, and filter cloth. A woven fabric that can maintain strength and form is preferred. As the synthetic fibers used in the woven fabric, any of single component fibers or side-by-side, core-sheath, split, and sea-island composite fibers can be used.
From the viewpoint of economy, a monocomponent fiber is preferable. For example, the above-mentioned fibers such as polyolefin, polyester, and polyamide may be used. The basis weight of the woven fabric is 200 to 80
0 g / m 2 , preferably 400 to 600 g / m 2 , if the basis weight is less than 200 g / m 2, it is difficult to maintain the form as a filter cloth, and if it is more than 800 g / m 2 , the filter cloth becomes bulky. Become.

【0008】本考案の濾過布は、上記で得られた不織布
と織物基布との間にホットメルト剤を介在させて熱カレ
ンダー加工を施し一体化して形成する。この熱カレンダ
ー加工時に不織布層表面の低融点極細繊維を軟化あるい
は部分溶融させて隣接繊維と接合させ、この軟化あるい
は溶融度合いを加減することによって通気度3〜15ml
/cm2/sec、好ましくは5〜10ml/cm2/secに抑制された
濾過布とする。低融点極細繊維の軟化溶融が過度となる
と表面の樹脂化が顕著となり通気度が3ml/cm2/sec未満
となってダストの払い落とし性はよくなるが使用時にお
ける圧力損失が大きくなり、モーターに負荷がかかり短
期間で濾過布交換が必要となる。また不織布層表面の低
融点極細繊維を軟化が不足であると繊維間接着ができ
ず、通気度が15ml/cm2/secを超えて使用時における圧
力損失は小さくなるが、表面の平滑性が不十分となって
不織布面に付着したダストの払い落し性が悪くなって集
塵効率が低下する。
[0008] The filter cloth of the present invention is integrally formed by hot calendering with a hot melt agent interposed between the nonwoven fabric obtained above and the woven fabric base cloth. At the time of this heat calendering, the low-melting ultrafine fibers on the surface of the nonwoven fabric layer are softened or partially melted and joined to the adjacent fibers, and the degree of softening or melting is adjusted so that the air permeability is 3 to 15 ml.
/ cm 2 / sec, preferably 5 to 10 ml / cm 2 / sec. If the softening and melting of the low-melting ultrafine fibers become excessive, the resinification of the surface becomes remarkable, the air permeability becomes less than 3 ml / cm 2 / sec, and the dust wiping property is improved. A load is applied and the filter cloth needs to be replaced in a short period of time. In addition, if the softening of the low melting point ultrafine fibers on the surface of the non-woven fabric layer is insufficient, the fibers cannot be bonded to each other, the air permeability exceeds 15 ml / cm 2 / sec, and the pressure loss during use is small, but the surface smoothness is low. Insufficiently, the ability to remove dust adhering to the surface of the nonwoven fabric is deteriorated, and the dust collection efficiency is reduced.

【0009】不織布層と織物基布とを接合するためのホ
ットメルト剤としては、ポリアミド系、ポリエステル
系、ポリオレフィン系など汎用されている低融点のもの
を用いるとよく、特に濾過布に使用する素材と同族系の
ホットメルト剤が好ましい。
As a hot-melt agent for joining the nonwoven fabric layer and the woven fabric, generally used low melting point materials such as polyamide, polyester, and polyolefin may be used. And the like are preferred.

【0010】不織布層と織物基布とを接合する熱カレン
ダー加工の条件としては、不織布層の低融点極細繊維の
軟化点以上高融点成分の融点以下の範囲にある熱ロール
と常温ロールとの2本のカレンダーロールを用い、不織
布層側を熱ロールとして線圧50〜100kg/cm、速度3
〜7m/min でもって処理するとよい。線圧が100kg/c
m 以上、速度3m/min 未満であると低融点極細繊維の軟
化溶融樹脂化が過度となり、通気性が低下する。また線
圧が50kg/cm より低く、処理速度が7m/minより大き
いと不織布層表面の低融点極細繊維の軟化が不十分とな
って繊維間接着ができず、ダスト払い落し性のよい平滑
な表面となすことができない
[0010] The conditions of the heat calendering process for joining the nonwoven fabric layer and the woven fabric base are as follows: a hot roll and a normal temperature roll having a range from the softening point of the low melting point ultrafine fiber of the nonwoven fabric layer to the melting point of the high melting point component. Using a calender roll with a non-woven fabric layer side as a heat roll, a linear pressure of 50 to 100 kg / cm, and a speed of 3
処理 7m / min. Linear pressure 100kg / c
If the speed is not less than 3 m / min and less than 3 m / min, the low-melting ultrafine fibers are excessively softened and melted, and the air permeability is reduced. On the other hand, if the linear pressure is lower than 50 kg / cm and the processing speed is higher than 7 m / min, the softening of the low melting point ultrafine fibers on the surface of the non-woven fabric layer becomes insufficient, so that the fibers cannot be bonded to each other, and the dust can be easily removed. Cannot make surface .

【0011】[0011]

【作用】本考案の濾過布は、織物基布でもって強度と寸
法安定性とを保持し、濾過面(ダスト供給側面)を形成
しているところの0.5デニール以下の極細繊維を含む
不織布層は微細なダストを捕集する。そして低融点極細
繊維の軟化による繊維接着により形成された平滑な表面
は、毛羽を抑制し、微粒子の集塵効率をより向上させる
とともにダスト払い落し性を良くする。
The filter cloth of the present invention is a non-woven fabric containing ultra-fine fibers of 0.5 denier or less, which maintains the strength and dimensional stability with a woven fabric base and forms a filtration surface (dust supply side surface). The layer collects fine dust. The smooth surface formed by the fiber bonding due to the softening of the low-melting ultrafine fibers suppresses fluff, improves the dust collection efficiency of the fine particles, and improves the dust removing property.

【0012】[0012]

【実施例】以下本考案の実施例を示している図にもとづ
いて説明すると、図1において、(1) は濾過布、(2) は
不織布層、そして(3) は織物基布を示している。不織布
層(2) には、図2に示しているように、低融点極細繊維
となるA成分(4)としてナイロン6(融点214℃)、
高融点極細繊維となるのB成分(5) としてポリエチレン
テレフタレート(融点256℃)とを放射状に交互に配
してなる分割型複合繊維(16分割型)を紡糸温度29
0℃で溶融複合押出紡糸し、75℃の温水中で3倍延伸
後、切断を行い、3デニール、45mmの分割型複合繊維
(6) のステープルとなし、この分割型複合繊維(6) を1
00重量%用いてカード機によりカードウェブとしたの
ち、水圧150kg/cm2、速度3m/min で表裏各3回高圧
液体流処理して分割型複合繊維(6) をA成分(4) の低融
点極細繊維(太さ0.19デニール)とB成分(5) の高
融点極細繊維(太さ0.19デニール)に分割するとと
もに繊維間交絡させた目付120g/m2の不織布を使用し
た。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to the drawings showing an embodiment of the present invention, FIG. 1 shows (1) a filter cloth, (2) a nonwoven fabric layer, and (3) a fabric base cloth. I have. As shown in FIG. 2, the nonwoven fabric layer (2) has nylon 6 (melting point 214 ° C.)
A splittable conjugate fiber (16-split type) obtained by alternately arranging polyethylene terephthalate (melting point: 256 ° C.) as a component B (5) to be a high melting point ultrafine fiber at a spinning temperature of 29
Spun at 0 ° C for melt composite extrusion, stretched 3 times in hot water at 75 ° C, cut and cut to 3 denier, 45 mm splittable composite fiber
The staple of (6) is used, and this splittable conjugate fiber (6) is
After making a card web with a card machine by using a 100% by weight, a high-pressure liquid flow treatment was performed three times on each of the front and back sides at a water pressure of 150 kg / cm 2 and a speed of 3 m / min to reduce the splittable conjugate fiber (6) to a low A component (4) A non-woven fabric having a basis weight of 120 g / m 2 , which was divided into ultra-melting point ultrafine fibers (0.19 denier in thickness) and high-melting point ultra-fine fibers of component B (5) (0.19 denier in thickness) and entangled between the fibers, was used.

【0013】織物基布(3) には、綿番手5S のポリエス
テル紡績糸を三本撚り合わしてなる撚糸を経糸および緯
糸に使用して織成している目付400g/m2の平織物を使
用した。
As the woven fabric fabric (3), a plain woven fabric having a basis weight of 400 g / m 2 woven by using twisted yarns obtained by twisting three polyester spun yarns having a cotton count of 5 S as warps and wefts was used. .

【0014】そして上記不織布層(2) と織物基布(3) の
間に目付25g/m2の低融点ポリエステル系のホットメル
ト剤(7) を介在させ、不織布層(2) 側を温度195℃の
熱ローラ、織物基布(3) 側を常温ローラとしたカレンダ
ーローラを使用し、線圧100kg/cm、速度4m/min でカ
レンダー加工を行い、不織布層(2) の表面側の低融点極
細繊維を軟化させて隣接する繊維間を接着(8) すると共
にホットメルト剤(7)を溶融して不織布層(2) と織物基
布(3) とを一体化して濾過布(1) となした。この濾過布
(1) の通気度は6.2ml/cm2/secであった。
A low-melting polyester-based hot melt agent (7) having a basis weight of 25 g / m 2 is interposed between the nonwoven fabric layer (2) and the woven fabric base fabric (3). Using a heat roller at ℃ and a calender roller with the fabric base fabric (3) side as a normal temperature roller, calendering is performed at a linear pressure of 100 kg / cm and a speed of 4 m / min to obtain a low melting point on the surface side of the nonwoven fabric layer (2). The ultrafine fibers are softened to bond the adjacent fibers (8), and the hot melt agent (7) is melted to integrate the nonwoven fabric layer (2) and the fabric base fabric (3) to form a filter cloth (1). Done This filter cloth
The air permeability of (1) was 6.2 ml / cm 2 / sec.

【0015】[比較例1] 実施例の不織布層の目付を
50g/m2とし、実施例と同じ織物基布を使用して実施例
と同じ要領により濾過布となした。この濾過布の通気度
は9.6ml/cm2/secであった。
[Comparative Example 1] A filter cloth was formed in the same manner as in the example using the same woven fabric as the example and the basis weight of the nonwoven fabric layer in the example was 50 g / m 2 . The air permeability of this filter cloth was 9.6 ml / cm 2 / sec.

【0016】[比較例2] 不織布層として実施例と同
じ目付120g/m2の不織布を使用し、実施例と同じ織物
基布の上に低融点のホットメルト剤を介在させ、熱カレ
ンダーローラでもって接着して表面の極細繊維に軟化や
溶融のない濾過布となした。この濾過布の通気度は18
ml/cm2/secであった。
Comparative Example 2 A nonwoven fabric having a basis weight of 120 g / m 2 was used as a nonwoven fabric layer, and a low-melting hot-melt agent was interposed on the same woven fabric as in the example. The filter cloth was adhered to form a filter cloth without softening or melting of the ultrafine fibers on the surface. The air permeability of this filter cloth is 18
ml / cm 2 / sec.

【0017】「表1」は実施例および比較例1,2の濾
過布の濾過性能評価結果をしめしている。
Table 1 shows the results of evaluating the filtration performance of the filter cloths of the examples and comparative examples 1 and 2.

【0018】尚、濾過性能については、次のように評価
した。JIS試験用ダスト10種を使用し、パルス型集
塵試験機でテストした。該試験機の条件は、次の通り設
定した。風量2.5m3/min、濾過面積0.66m2、パル
ス間隔2min,0.1sec/1ハ゜ルス 、パルス圧3kg/cm2、試験
時間7hr、温度(室温)とし、加速のためと一次付着層
を形成するため濾過布面圧力ΔP=150mmH2O に達す
るまでダストを払い落とさずに行った。
The filtration performance was evaluated as follows. Using 10 kinds of JIS test dusts, a test was conducted with a pulse type dust tester. The conditions of the tester were set as follows. Air volume 2.5m 3 / min, filtration area 0.66m 2 , pulse interval 2min, 0.1sec / 1 pulse, pulse pressure 3kg / cm 2 , test time 7hr, temperature (room temperature), primary adhesion layer for acceleration The formation was performed without dusting off until the pressure on the filter cloth reached ΔP = 150 mmH 2 O.

【0019】ダスト洩れ量(g):濾過布を通過したダ
スト0.1μmまで捕集可能な濾紙で捕集した重量。 集塵効率(%):ダスト供給機より入口ダスト濃度A
(g/m3)を測定し、濾過布を通過した風量と上記ダスト
洩れ量により出口ダスト濃度B(g/m3)を測定し、集塵
効率(%)=[1−(B/A)]×100の式より算出
した。 通気低下度(%):上記試験前の通気度C(ml/cm2/se
c)と試験後の通気度D(ml/cm2/sec)とを測定し、通
気低下度(%)=[1−(D/C)]×100の式より
算出した。 圧力損失(mmH2O ):上記試験ΔP=150mmH2O 後の
最大値。 ダスト払い落し性[ダスト付着量(g/m2)]:上記試験
後の濾過布の重量を測定し試験前の濾過布の重量を差し
引いたダスト重量。(ダスト重量が少ない程、剥離性が
よい。)
Dust leakage amount (g): Weight collected by filter paper capable of collecting up to 0.1 μm of dust that has passed through the filter cloth. Dust collection efficiency (%): Inlet dust concentration A from dust feeder
(G / m 3 ), and the outlet dust concentration B (g / m 3 ) was measured based on the amount of air passing through the filter cloth and the amount of dust leakage, and the dust collection efficiency (%) = [1- (B / A) )] × 100. Permeability decrease (%): Permeability C (ml / cm 2 / se) before the above test
c) and the air permeability D (ml / cm 2 / sec) after the test were measured, and calculated from the equation of air permeability reduction (%) = [1- (D / C)] × 100. Pressure loss (mmH 2 O): the test ΔP = 150mmH 2 maximum value after O. Dust removing property [Dust adhesion amount (g / m 2 )]: Dust weight obtained by measuring the weight of the filter cloth after the above test and subtracting the weight of the filter cloth before the test. (The smaller the dust weight, the better the peelability.)

【0020】[0020]

【表1】 [Table 1]

【0021】[0021]

【考案の効果】本考案の濾過布(1) は、目付が200〜
800g/m2の織物基布(3)の上に、分割型複合繊維が分
割して形成された太さ0.5デニール以下の低融点極細
繊維と高融点極細繊維とが1:1の割合で混在した極細
繊維材料を少なくとも50重量%以上含有し、かつ不織
布を構成する繊維同士がニードルパンチもしくは高圧液
体流により交絡してなる不織布がバインダーを介して接
合され、その不織布層(2) 表面に熱カレンダー処理が施
されて表面の上記低融点極細繊維が軟化され隣接繊維間
が接着(4) されて平滑化され、通気度が3〜15ml/cm2
/secに抑制されてなるものであるから、不織布層(2) の
極細繊維の交絡緻密性と通気度規制により濾過精度を著
しく向上させることができ、しかも濾過面の低融点極細
繊維の軟化による繊維間接着(4) により毛羽が抑えら
れ、ダスト払い落し性が良好となり、圧力損失が減少す
る。そして織物基布(3) が濾過布(1) の寸法安定性と強
度を保持しているから苛酷な使用に耐える。したがって
特にバグフィルター用として好適なものとなる。
[Effect of the Invention] The filter cloth (1) of the present invention has a basis weight of 200 to
On the 800 g / m 2 woven fabric base (3), the splittable conjugate fibers are separated.
Split by a low melting point microfine fiber thickness below 0.5 denier formed by the high melting point microfine fibers is 1: The mixed ultrafine fiber material in a ratio of 1 contains at least 50 wt% or more, and non-woven
Needle punch or high pressure liquid
The nonwoven fabric entangled by the body flow is bonded via a binder, and the surface of the nonwoven fabric layer (2) is subjected to a heat calendering treatment to soften the low-melting-point ultrafine fibers on the surface and adhere (4) between adjacent fibers. Smoothed and air permeability 3-15ml / cm 2
/ sec, the filtration accuracy can be remarkably improved by the entangled denseness of the fine fibers of the nonwoven fabric layer (2) and the regulation of the air permeability, and the softening of the low melting point fine fibers of the filtration surface The fiber-to-fiber bonding (4) reduces fluff, improves dust removal and reduces pressure loss. The woven fabric base (3) maintains the dimensional stability and strength of the filter cloth (1) and can withstand severe use. Therefore, it is particularly suitable for a bag filter.

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

【図1】本考案の濾過布の断面図である。FIG. 1 is a sectional view of the filter cloth of the present invention.

【図2】複合繊維の一例を示した繊維断面図である。FIG. 2 is a fiber sectional view showing an example of a conjugate fiber.

【符号の説明】[Explanation of symbols]

1 濾過布 2 不織布層 3 織物基布 4 A成分 5 B成分 6 分割型複合繊維 7 ホットメルト剤 8 繊維間接着 DESCRIPTION OF SYMBOLS 1 Filtration cloth 2 Nonwoven fabric layer 3 Fabric base cloth 4 A component 5 B component 6 Splittable composite fiber 7 Hot melt agent 8 Adhesion between fibers

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 目付が200〜800g/m2の織物基布の
上に、分割型複合繊維が分割して形成された太さ0.5
デニール以下の低融点極細繊維と高融点極細繊維とが
1:1の割合で混在した極細繊維材料を少なくとも50
重量%以上含有し、かつ不織布を構成する繊維同士がニ
ードルパンチもしくは高圧液体流により交絡してなる目
付60〜250g/m2の不織布がバインダーを介して接合
され、その不織布表面に熱カレンダー処理が施されて表
面の上記低融点極細繊維が軟化され隣接繊維間が接着さ
れて平滑化され、通気度が3〜15ml/cm2/secに抑制さ
れていることを特徴とする濾過布。
[Claim 1] A splittable conjugate fiber is formed on a woven fabric base fabric having a basis weight of 200 to 800 g / m 2 by a thickness of 0.5.
An ultrafine fiber material in which a low melting point ultrafine fiber having a denier or less and a high melting point ultrafine fiber are mixed at a ratio of 1: 1 is used in at least 50 parts.
% By weight and the fibers constituting the nonwoven fabric
A nonwoven fabric having a basis weight of 60 to 250 g / m 2 entangled by a needle punch or a high-pressure liquid flow is joined via a binder, and the surface of the nonwoven fabric is subjected to a heat calendering treatment to soften the low-melting-point ultrafine fibers on the surface and to form adjacent fibers A filter cloth characterized in that the gap is adhered and smoothed, and the air permeability is suppressed to 3 to 15 ml / cm 2 / sec.
JP1991083793U 1991-09-18 1991-09-18 Filter cloth Expired - Fee Related JP2554259Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991083793U JP2554259Y2 (en) 1991-09-18 1991-09-18 Filter cloth

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991083793U JP2554259Y2 (en) 1991-09-18 1991-09-18 Filter cloth

Publications (2)

Publication Number Publication Date
JPH0526122U JPH0526122U (en) 1993-04-06
JP2554259Y2 true JP2554259Y2 (en) 1997-11-17

Family

ID=13812531

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991083793U Expired - Fee Related JP2554259Y2 (en) 1991-09-18 1991-09-18 Filter cloth

Country Status (1)

Country Link
JP (1) JP2554259Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100361431B1 (en) * 2000-07-14 2002-11-22 주식회사 프리챌홀딩스 Gas filter manufactured with fine yarn
KR100361430B1 (en) * 2000-07-14 2002-11-22 주식회사 프리챌홀딩스 Gas filter manufactured with ultra-fine yarn

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0233559B2 (en) * 1982-08-19 1990-07-27 Fujita Corp GASUKIKYU
JPS5944500A (en) * 1982-09-02 1984-03-12 株式会社ハツコ− Dehumidifying system in large diameter pipe
JPH0796089B2 (en) * 1989-07-28 1995-10-18 市川毛織株式会社 For bag filter

Also Published As

Publication number Publication date
JPH0526122U (en) 1993-04-06

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