JP3233988B2 - Filter cloth and method for producing the same - Google Patents

Filter cloth and method for producing the same

Info

Publication number
JP3233988B2
JP3233988B2 JP17496492A JP17496492A JP3233988B2 JP 3233988 B2 JP3233988 B2 JP 3233988B2 JP 17496492 A JP17496492 A JP 17496492A JP 17496492 A JP17496492 A JP 17496492A JP 3233988 B2 JP3233988 B2 JP 3233988B2
Authority
JP
Japan
Prior art keywords
filter cloth
web
sheet
fiber
ultrafine
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
JP17496492A
Other languages
Japanese (ja)
Other versions
JPH0671122A (en
Inventor
邦夫 俣木
修二 堀
渉 京塚
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 JP17496492A priority Critical patent/JP3233988B2/en
Publication of JPH0671122A publication Critical patent/JPH0671122A/en
Application granted granted Critical
Publication of JP3233988B2 publication Critical patent/JP3233988B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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、気体の濾過に適用され
るバグフィルターに好適な濾過布およびその製造方法に
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 suitable for a bag filter applied to gas filtration and a method for producing the same.

【0002】[0002]

【従来の技術】従来のバグフィルター用の濾過布として
は、主として織物やフェルトが使用されているが、単な
る織物やフェルトでは微粒子の集塵が難しい。このこと
から微粒子集塵用として特開平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 Fabrics and felts are mainly used as conventional filter cloths for bag filters, but it is difficult to collect fine particles with a mere fabric or felt. For this reason, as disclosed in JP-A-3-60712, a filter cloth has been proposed 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 as disclosed in JP-A-3-60712. .

【0003】[0003]

【発明が解決すべき課題】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た濾過布は、微粒子の
集塵効率は良いものの、ダストの払い落し性が悪いため
目詰まりが生じ、早期に圧力損失が上昇することから比
較的短期間に濾過布を交換しなければならない。そのう
えシート基材であるニードルフェルトと極細繊維不織布
シートとはホットメルト型の接着剤によりあるいはニー
ドルフェルトの表層を溶融してラミネートされているた
め、例えばバグフィルターとして使用した場合、濾過布
の温度上昇等の要因によって接着が軟化し、ダストの
払い落とし振動を受けて部分的に層間剥離が発生し、早
期に使用不能となる事態がしばしば生じる。
However, a filter cloth obtained by laminating a nonwoven sheet made of ultrafine fibers having an average fineness of 0.2 denier or less on the surface of a needle felt has good dust collection efficiency of fine particles, but has a low dust removal property. Since the filter cloth is bad, clogging occurs and the pressure loss increases early, so that the filter cloth must be replaced in a relatively short time. In addition, the needle felt and the microfiber nonwoven sheet, which are the sheet base materials, are laminated with a hot-melt type adhesive or by melting the surface layer of the needle felt. For example, when used as a bag filter, the temperature of the filter cloth increases. Due to such factors, the bonding surface is softened, and delamination occurs partially due to dust sweeping vibration, which often causes a situation in which the device cannot be used early.

【0004】本発明の目的は、濾過面を改善することに
よって微粒子の集塵効率、ダスト払い落し性を良くし、
圧力損失の上昇を遅延させて濾過布の交換周期を延長さ
せ、さらに濾過面を構成している極細繊維層を接着剤を
用いることなくシート基材に交絡して一体化し、層間剥
離のない濾過布およびその製造方法をを提供するにあ
る。
[0004] It is an object of the present invention to improve the collection efficiency of fine particles and the dust removing property by improving the filtration surface,
It delays the rise of pressure loss and extends the exchange cycle of the filter cloth.Furthermore, the ultrafine fiber layer constituting the filter surface is entangled and integrated with the sheet substrate without using an adhesive, and filtration without delamination is performed. It is an object of the present invention to provide a fabric and a method for producing the same.

【0005】[0005]

【課題を解決するための手段】本発明は、濾過布のダス
ト供給側面(以下濾過面と称することもある)を構成す
る層を分割型複合繊維が分割された繊維群によって形成
するとともにこの分割型複合繊維をシート基材に交絡す
ることにより一体化し、極細繊維で形成された濾過面を
平滑化することによつて上記課題を解決した。
SUMMARY OF THE INVENTION According to the present invention, a layer constituting a dust supply side (hereinafter sometimes referred to as a filtration side) of a filter cloth is formed by a group of fibers obtained by dividing a splittable conjugate fiber. The object has been solved by entanglement of the conjugate fiber with the sheet base material and by smoothing the filtration surface formed of the ultrafine fibers.

【0006】即ち本発明の濾過布は、シート基材の一方
の面に、このシート基材と繊維交絡により一体化された
平均繊度が0.5デニール以下の極細繊維による不織布
層が配されて濾過面が形成され、その極細繊維の不織布
層の表面が平滑化されていることを特徴とし、またその
濾過布の製造方法にあっては、シート基材の一方の面に
分割後の平均繊度が0.5デニール以下となる分割型複
合繊維ウェブを重ね合わせてそのウェブ側からニードル
パンチングを施して分割型複合繊維ウェブを上記シート
基材に交絡させ、次いでウェブ側から高圧液体流処理を
行って分割型複合繊維を分割してシート基材の面に極細
繊維による不織布層を形成し、乾燥後、濾過面を形成し
ている極細繊維が溶融しない程度に加熱した加熱ロール
により上記ウェブ面を平滑化することを特徴としている
ものである。
Namely filter cloth of the present invention, on one surface of the sheet over preparative substrate, average fineness, which is integrated by the sheet substrate and the fiber entangled nonwoven layer according to the following ultrafine fibers 0.5 denier distribution is filtered surface is formed, characterized in that the surface of the nonwoven fabric layer of the ultrafine fibers is smoothed, also in the manufacturing method of the filter cloth, divided into one surface of the sheet over preparative substrate A split type composite fiber web having an average fineness of 0.5 denier or less is superimposed, needle-punched from the web side to entangle the split type composite fiber web with the sheet substrate, and then a high pressure liquid is applied from the web side. Flow treatment is performed to divide the splittable conjugate fiber, form a nonwoven fabric layer of ultrafine fibers on the surface of the sheet substrate, and form a filtration surface after drying.
The web surface is smoothed by a heating roll heated to such an extent that the ultrafine fibers do not melt .

【0007】本発明の濾過布の濾過面を形成する0.5
デニール以下の極細繊維としては、異質の2成分が交互
に存在してなる分割型複合繊維のステープルが好まし
い。そして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12
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成分で構成することが特に好ましい。また分割型複
合繊維の繊維断面形状は特に限定するものではないが高
圧水流で分割容易な放射線状型が好ましい。
[0007] 0.5 to form the filtration surface of the filter cloth of the present invention
As the ultrafine fiber having a denier or less, a staple of a splittable conjugate fiber in which two different components are alternately present is preferable. As the 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 12
Although it can be appropriately selected from polyamide-based polymers or copolymers such as those described above, it is particularly preferable that the composition be composed of two components having a melting point difference of 20 ° C. or more. The fiber cross-sectional shape of the splittable conjugate fiber is not particularly limited, but a radial type which is easily split by a high-pressure water flow is preferable.

【0008】濾過面の層は、シート基材の上に分割型複
合繊維のウェブを重ね合わせてニードルパンチングを施
して両者を交絡一体化したのち、分割型複合繊維のウェ
ブ側から高圧水流処理して分割型複合繊維を分割して極
細化し、しかるのちローラ加工をしてその表面を平滑化
するとよい。
[0008] layer of the filtration surface, after entangling integrated both subjected to needle punching by superposing a web of splittable conjugate fibers onto the sheet over preparative substrate, high-pressure water from the web side of the splittable conjugate fiber It is preferable to divide the splittable conjugate fiber to make it ultrafine, and then to perform roller processing to smooth the surface.

【0009】また他の方法として、分割型複合繊維を分
割して0.5デニール以下の極細繊維を少なくとも50
重量%含有してなるウェブをシート基材の上に重ね合わ
せ、ニードルパンチングを施して両者を交絡一体化した
のち、ローラ加工をしてその表面を平滑化してもよい。
[0009] As another method, the splittable conjugate fiber is divided into ultrafine fibers of 0.5 denier or less and at least 50 deniers.
A web comprising wt% superimposed on the sheet over preparative substrate, after both were entangled integrally subjected to needle punching, the surface may be smoothed by a roller machining.

【0010】分割型複合繊維を分割するための高圧水流
処理の条件としては、吐出水圧が30〜200kg/cm2
好ましくは80〜150kg/cm2であって、被処理物の移
動速度1〜5m/min 程度がよい。吐出水圧が30kg/c
m2未満、速度が5m/min より速いと分割不十分となり、
吐出水圧200kg/cm2より大きいと過剰処理となり不経
済である。
The conditions of the high-pressure water flow treatment for splitting the splittable conjugate fiber include a discharge water pressure of 30 to 200 kg / cm 2 ,
It is preferably 80 to 150 kg / cm 2 , and the moving speed of the object is preferably about 1 to 5 m / min. Discharge water pressure is 30kg / c
less than m 2, the speed is insufficient dividing faster than 5 m / min,
If the discharge water pressure is higher than 200 kg / cm 2, it is excessively processed, which is uneconomical.

【0011】極細繊維の太さが0.5デニールを超えた
り、濾過面を形成する不織布層の極細繊維の構成割合が
50重量%未満であると所望精度の濾過面が得られず、
またこの不織布層の目付が100g/m2未満であると微粒
子集塵が期待できない。そして目付を150g/m2以上と
してもさほど微粒子集塵効率が上がらないことから、極
細繊維層の目付けは100〜150g/m2程度が経済的で
ある。
If the thickness of the ultrafine fibers exceeds 0.5 denier, or if the composition ratio of the ultrafine fibers in the nonwoven fabric layer forming the filtration surface is less than 50% by weight, a filtration surface with a desired accuracy cannot be obtained.
If the basis weight of the nonwoven fabric layer is less than 100 g / m 2 , dust collection cannot be expected. The basis weight since no sufficiently enhanced fine particle dust efficiently even a 150 g / m 2 or more, the basis weight of the microfiber layer is about 100 to 150 g / m 2 is economically.

【0012】シート基材としては、基布を介装してなる
目付けが300〜500g/m2 の市販のニードルパンチン
グ不織布や、低番手のパーロック糸またはマルチフィラ
メント糸で織成された織布が好ましく適用できる。
[0012] As the sheet substrate, woven fabric weight obtained by interposing a base fabric of the city sales of needle punching the nonwoven fabric and 300 to 500 g / m 2, interwoven with Parokku yarns or multifilament yarns of low yarn count fabric Is preferably applicable.

【0013】濾過布の通気度は、例えばバグフィルター
用としては、2〜10ml/cm2/sec、好ましくは2〜6ml
/cm2/secの範囲がよい。通気度が2ml/cm2/sec未満であ
ると圧力損失が高くなり、10ml/cm2/secより大きくな
るとダスト払い落し性、集塵効率低下する。
The air permeability of the filter cloth is, for example, 2 to 10 ml / cm 2 / sec, preferably 2 to 6 ml for a bag filter.
The range of / cm 2 / sec is good. Air permeability pressure loss is increased is less than 2ml / cm 2 / sec, dust brushing resistance becomes greater than 10ml / cm 2 / sec, the dust collection efficiency is lowered.

【0014】濾過面を平滑化するためのロール加工の条
件としては、濾過面を形成している極細繊維が溶融しな
い程度に加熱された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、極細繊維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
するとよく、平滑度や通気度はこのロールの線圧の調整
によって行うことができる。
As the conditions for the roll processing for smoothing the filtration surface, two calender rolls, a hot roll and a normal temperature roll, which are heated to such an extent that the ultrafine fibers forming the filtration surface are not melted, are used. The ultrafine fiber layer side may be treated as a heat roll with a linear pressure of 50 to 100 kg / cm and a speed of 3 to 7 m / min, and the smoothness and air permeability can be adjusted by adjusting the linear pressure of the roll.

【0015】[0015]

【作用】本発明の濾過布は、ダスト供給側面即ち濾過面
側を構成している太さが0.5デニール以下の極細繊維
を含む不織布層が、接着剤を使用することなくシート基
材との繊維交絡によってシート基材と一体化されている
ため、使用中濾過布の温度が上昇し、その昇温下におい
て頻繁にダストの払い落とし振動を受けても層間剥離が
生じない。そして極細繊維の集合層の平滑化された濾過
面は、微粒子集塵効率を向上させ、ダスト払い落し性が
よくし、濾過布の交換周期の延長に寄与する。
According to the filter cloth of the present invention, the non-woven fabric layer containing the ultrafine fibers having a thickness of 0.5 denier or less constituting the dust supply side surface, that is, the filter surface side, is formed on the sheet base without using an adhesive. Since the fiber entanglement is integrated with the sheet substrate, the temperature of the filter cloth rises during use, and delamination does not occur even if the filter cloth is frequently shaken off by dust at the temperature rise. The smoothed filtration surface of the aggregate layer of the microfibers improves the particulate collection efficiency, improves the dust removal property, and contributes to the extension of the filter cloth replacement cycle.

【0016】[0016]

【実施例】[実施例1] 図1は本発明の濾過布の縦方
向の断面拡大図を示し、(1) は濾過布、(2) は濾過面を
形成している極細繊維の不織布層、そして(3) はシート
基材である。不織布層(2) は、図4に示すような繊維断
面(但し、16分割)を有し、A成分(8) としてポリエ
ステル、B成分(9) としてナイロン−6を配してなる
均繊度3デニールの剥離分割型の複合繊維(10)が分割さ
れたところの平均繊度が0.19デニールの極細繊維で
構成され、シート基材(3) には補強基布(4)を有するポ
リエチレンテレフタレート繊維(太さ2デニール)から
なる目付400g/m2のニードルパンチング不織布[商品
名:FT0408.日本フェルト工業(株)製]が使用
されていて、両者はニードルパンチング手段による繊維
交絡によって接合され一体化されている。そして極細繊
維の不織布層(2) の表面は、極細繊維の低融点成分側
(B成分)の軟化溶融温度程度に加熱された熱ロールで
もって加工されて毛羽のない平滑な濾過面(5) となって
いる。
EXAMPLES Example 1 FIG. 1 is an enlarged cross-sectional view of a filter cloth of the present invention in the longitudinal direction, wherein (1) is a filter cloth, and (2) is a nonwoven fabric layer of ultrafine fibers forming a filter surface. And (3) are sheet substrates. The non-woven fabric layer (2) has a fiber cross section as shown in FIG. 4 (however, divided into 16), and is made of a flat material comprising polyester as the component (8) and nylon-6 as the component (9).
The split-fiber composite fiber (10) having an average fineness of 3 deniers is composed of microfibers having an average fineness of 0.19 denier when divided, and the sheet substrate (3) has a reinforcing base cloth (4). Needle-punched nonwoven fabric with a basis weight of 400 g / m 2 made of polyethylene terephthalate fiber (thickness: 2 denier) [trade name: FT0408. Manufactured by Nippon Felt Industry Co., Ltd.], which are joined and integrated by fiber entanglement by needle punching means. The surface of the non-woven fabric layer of microfibers (2) is processed with a hot roll heated to about the softening and melting temperature of the low melting point component side (B component) of the microfibers, so that the smooth filtration surface without fluff (5) It has become.

【0017】上記[実施例1]の濾過布(1) は次のよう
にして製造した。図4に例示しているような剥離分割型
複合繊維、即ちA成分(8) としてポリエステル、B成分
(9)としてナイロン−6を配してなる分割型複合繊維を
溶融複合押出紡糸し、3倍延伸後、切断を行って得た
均繊度3デニール、長さ45mmの分割型複合繊維(10)を
準備したのちこの分割型複合繊維(10)を100重量%用
いてカード機によりカードウェブとなす。次いでこのウ
ェブを目付けが約125g/m2に調整したウェブシートと
なし、図3に略示しているように、まず上記シート基材
(3) の上にウェブシート(11)を重ね合わせてそのウェブ
側からニードルパンチングを施して分割型複合繊維ウェ
ブを上記シート基材(3) に交絡させ、次いでこの積層交
絡不織布(12)を速度4m/min で移動させながら分割型複
合繊維ウェブ側から、幅方向に多数の微細なノズルが列
設された高圧液体流処理装置(13)により水圧150kg/c
m2でもって分割型複合繊維の分割処理を行って、シート
基材(3) の面に平均繊度が0.19デニールの極細繊維
による不織布層(2) が形成された複合不織布(14)とな
し、乾燥した。かくして得られた複合不織布(14)は不織
布層(2) の表面の分割型複合繊維は大部分極細化され、
かつ前工程のニードルパンチングの針の刺通孔が消去さ
れていた。しかるのち不織布層(2) 側を温度185℃の
熱ローラ(15)、シート基材(3) 側を常温ローラ(16)と
した一対のローラ(15)(16)でもって線圧100kg/cm 、
速度4m/min でカレンダー加工を行い、熱ロール(15)に
より上記不織布層(2) のナイロン−6成分を軟化して平
滑化し、平滑濾過面(5) を有した濾過布(1) となした。
得られた濾過布(1) の通気度は4.2ml/cm2/secであっ
た。
The filter cloth (1) of the above [Example 1] was produced as follows. The split-split conjugate fiber as exemplified in FIG. 4, that is, polyester as component A (8) and component B
As (9), a splittable composite fiber obtained by disposing nylon-6 is melt-composite-extruded, spun three times, and cut to obtain a flat composite fiber.
After preparing a splittable conjugate fiber (10) having a uniformity of 3 denier and a length of 45 mm, a card web is formed by a carding machine using 100% by weight of the splittable conjugate fiber (10). The web was then made into a web sheet with a basis weight of about 125 g / m 2 , and as shown schematically in FIG.
A web sheet (11) is overlaid on (3) and needle-punched from the web side to entangle the splittable conjugate fiber web with the sheet substrate (3). While moving at a speed of 4 m / min, a water pressure of 150 kg / c is applied from a split type composite fiber web side by a high pressure liquid flow treatment device (13) in which a number of fine nozzles are arranged in the width direction.
performing division processing of splittable conjugate fibers with m 2, and the sheet substrate and the nonwoven fabric layer by an average fineness 0.19 denier microfine fibers on the surface of (3) (2) composite nonwoven fabric which is formed (14) None, dried. In the composite non-woven fabric (14) thus obtained, the splittable composite fibers on the surface of the non-woven fabric layer (2) are mostly ultrafine,
In addition, the puncture hole of the needle in the needle punching in the previous process was deleted. Thereafter, a pair of rollers (15) and (16) having a non-woven fabric layer (2) side having a heat roller (15) at a temperature of 185 ° C. and a sheet substrate (3) side having a room temperature roller (16) has a linear pressure of 100 kg / cm. ,
Calendering is performed at a speed of 4 m / min, and the nylon-6 component of the non-woven fabric layer (2) is softened and smoothed by a hot roll (15) to obtain a filter cloth (1) having a smooth filtration surface (5). did.
The air permeability of the obtained filter cloth (1) was 4.2 ml / cm 2 / sec.

【0018】[実施例2]ート基材(3) として、綿
番手5S のポリプロピレン繊維のパーロック紡績糸の3
本撚糸を経糸および緯糸に使用し、経糸密度16本/イ
ンチ、緯糸密度15本/インチの重厚な平織物を用い
た。そして上記実施例1と同様にこのシート基材(3) の
上に目付け約125g/m2の分割型複合繊維ウェブシート
を重ね合わせてニードルパンチングを行い、次いで高圧
水流処理をし、乾燥後、カレンダーローラ加工を行っ
て、図2のようにシート基材(3) に不織布層(2) の繊維
が交絡して一体化されて不織布層(2) の繊維が極細化さ
れ、かつ濾過面(5)が平滑な濾過布(1) となした。
[0018] [Example 2] over preparative substrate as a (3), 3 Parokku spun yarn polypropylene fibers of cotton count 5 S
This twisted yarn was used for the warp and the weft, and a heavy plain fabric having a warp density of 16 yarns / inch and a weft density of 15 yarns / inch was used. Then, in the same manner as in Example 1 above, a split-type composite fiber web sheet having a basis weight of about 125 g / m 2 was superposed on the sheet base material (3), needle-punched, followed by high-pressure water-flow treatment, and after drying, By performing calendering, the fibers of the nonwoven fabric layer (2) are entangled and integrated with the sheet substrate (3) as shown in FIG. 5) became a smooth filter cloth (1).

【0019】得られたこの濾過布(1) は、濾過面の不織
布層(2) は極細繊維で構成され、その表面は極めて平滑
であって実施例1のものよりも柔軟性に富み、通気度は
2.1ml/cm2/secであった。
In the obtained filter cloth (1), the nonwoven fabric layer (2) on the filter surface is composed of ultrafine fibers, the surface of which is extremely smooth, is more flexible than that of Example 1, and has a ventilation The degree was 2.1 ml / cm 2 / sec.

【0020】[比較例] 実施例の分割型複合繊維でも
って目付け125g/m2のウェブシートを作り、このウエ
ブシートに高圧水流処理を施して分割型複合繊維を極細
化するとともに繊維間を交絡させて極細繊維不織布とな
し、この不織布を実施例1のシート基材の一方の面にホ
ットメルト剤でもって接合したのち実施例と同様にカレ
ンダー加工をして濾過面が極細繊維不織布層の濾過布と
なした。なおホツトメルト剤として、[ポリアミド系.
ダイアミド1000#(ダイセル化学(株)]を使用した。
Comparative Example A web sheet having a basis weight of 125 g / m 2 was prepared using the splittable conjugate fiber of the example, and the web sheet was subjected to a high-pressure water flow treatment to make the splittable conjugate fiber extremely fine and to entangle the fibers. Then, the non-woven fabric was formed into an ultra-fine fiber non-woven fabric. The non-woven fabric was bonded to one surface of the sheet substrate of Example 1 with a hot melt agent, and then calendered in the same manner as in Example to filter the ultra-fine fiber non-woven fabric layer. Made with cloth. In addition, as a hot melt agent, [polyamide.
Daiamide 1000 # (Daicel Chemical Co., Ltd.) was used.

【0021】上記実施例1と比較例の濾過布の濾過性能
は「表1」の通りであった。
The filtering performance of the filter cloths of Example 1 and Comparative Example was as shown in Table 1.

【0022】[0022]

【表1】 [Table 1]

【0023】なお濾過性能については次のようにして評
価した。JIS試験用ダスト11種を使用し、平面型集
塵試験機(自社製)でテストした。該試験機の条件を、
濾過面積44.156cm2 、濾過速度3/mimに
設定し、濾過布面圧力ΔP=200mmH2 Oに達する
まで行った。
The filtration performance was evaluated as follows. Using 11 kinds of JIS test dusts, a test was conducted with a flat type dust tester (manufactured by the company). The conditions of the testing machine were
The filtration area was set at 44.156 cm 2 , the filtration speed was 3 m / mim, and the filtration was performed until the pressure on the cloth surface reached 200 mmH 2 O.

【0024】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。 ダスト付着量(g):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。 集塵効率(%)=上記試験によるダスト洩れ量A、濾過
面へのダスト付着量Bから、集塵効率=[B/(A+
B)]×100の式により算出した。 初期圧力損失(mmH2 O):ダストを供給しない場合
の濾過面圧力。 D.H.C(g/m2 ):m2 当たりのダストの捕集能
力。 ダスト払い落とし率(%):上記試験後の濾過布に、今
までとは逆方向に5kg/cm2 の圧力空気を0.25
秒流し、濾過布上のダストを払い落としを行ったのちの
濾過布上の残留ダスト重量Cを測定し、ダスト払い落と
し率(%)=[1−(C/B)]×100の式より算出
した。
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 adhesion amount (g): Dust weight obtained by measuring the weight of the filter cloth after the test and subtracting the weight of the filter cloth before the test. Dust collection efficiency (%) = Dust collection efficiency = [B / (A +)
B)] × 100. Initial pressure loss (mmH 2 O): filtration surface pressure when dust is not supplied. D. H. C (g / m 2 ): Capability of collecting dust per m 2 . Dust brushing rate (%): the filter cloth after the above test, the pressure air of 5kg / cm 2 in a direction opposite to the until now 0.25
After a second flow, the dust on the filter cloth was wiped off and the residual dust weight C on the filter cloth was measured, and the dust removal rate (%) = [1- (C / B)] × 100 Calculated.

【0025】また上記実施例1と比較例の濾過布の層間
剥離強力は「表2」の通りであった。なお剥離強力はJ
IS−L−1089 5.10に基づいて測定した。
The delamination strength of the filter cloths of Example 1 and Comparative Example was as shown in Table 2. The peel strength is J
It measured based on IS-L-1089 5.10.

【0026】[0026]

【表2】 [Table 2]

【0027】実施例1と比較例の濾過布でもって内径1
20mm、長さ200cmのバグフィルターとなし、パルス
間隔2min,0.1sec/1ハ゜ルスの払い落とし装置を備えた陶土
の濾過室にて実用テストをしたところ、濾過性能および
ダスト払い落とし性は共に良好であったが、使用時間が
延べ1300時間に達した時点において点検したとこ
ろ、比較例のバグフィルターにはシート基材と不織布層
との層間剥離が認められ、以後の使用は不能となった。
しかし実施例1の濾過布によるバグフィルターには層間
剥離が全くみらなかった。
With the filter cloths of Example 1 and Comparative Example,
Practical tests were conducted in a porcelain clay filtration room equipped with a 20 mm, 200 cm long bag filter and a pulse interval of 2 min, 0.1 sec / 1 pulse. The filtration performance and dust removal were both good. However, inspection was conducted at a point in time when the total use time reached 1300 hours. As a result, delamination between the sheet base material and the nonwoven fabric layer was observed in the bag filter of the comparative example, and subsequent use was impossible.
However, no delamination was observed in the bag filter using the filter cloth of Example 1.

【0028】[0028]

【発明の効果】このように本発明の濾過布(1) は、シ
ト基材(3) の一方の面に、このシート基材(3) と繊維交
絡により一体化された平均繊度が0.5デニール以下の
極細繊維による不織布層(2) が配されて濾過面(5) が形
成され、その極細繊維の不織布層(2) の表面が平滑化さ
れてなるものであるから、濾過面側の極細繊維不織布層
(2) によって濾過精度および微粒子の集塵効率が著しく
向上し、しかもその表層の濾過面(5) が平滑化されてい
るためダスト払い落とし性もよい。そのうえシート基材
(3) と極細繊維の不織布層(2) とは接着剤を使用するこ
となく繊維の交絡によって接合一体化されているから、
濾過布が温度上昇している使用環境下において払い落と
し振動を受けても、層間剥離の憂いはなく、濾過布の耐
用寿命を大幅に延長することができる。したがつて本発
明の濾過布(1) はバグフィルター用として好適となる。
[Effect of the Invention] filter cloth according to the present invention in this way (1), on one surface of the sheet over <br/> preparative substrate (3), the sheet substrate and (3) are integrated by fiber entanglement A nonwoven fabric layer (2) made of ultrafine fibers having an average fineness of 0.5 denier or less is arranged to form a filtration surface (5), and the surface of the nonwoven fabric layer (2) of the ultrafine fibers is smoothed. There is an extra fine fiber non-woven fabric layer on the filtration side
By (2), the filtration accuracy and the dust collection efficiency of fine particles are remarkably improved, and the filtering surface (5) of the surface layer is smoothed, so that dust can be easily removed. In addition, sheet base
Since (3) and the nonwoven fabric layer (2) of microfibers are joined and integrated by entanglement of the fibers without using an adhesive,
Even if the filter cloth is subjected to a sweeping vibration in a use environment where the temperature is rising, there is no fear of delamination and the useful life of the filter cloth can be greatly extended. Therefore, the filter cloth (1) of the present invention is suitable for bag filters.

【0029】また極細繊維の不織布層(2) は、分割型複
合繊維ウェブをシート基材にニードルパンチングしたの
ち高圧液体流処理を行って形成するものであるから、こ
の高圧液体流処理によってニードルパンチング時の針刺
通孔が消去され、面に亘り均整な微細孔径をもった濾
過布がられる。
Since the nonwoven fabric layer (2) of microfibers is formed by needle-punching a splittable composite fiber web on a sheet substrate and then performing a high-pressure liquid flow treatment, the needle-punching is performed by the high-pressure liquid flow treatment. is erased needle piercing hole of time, the filter cloth is obtained with a proportioned fine pore diameter over the entire surface.

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

【図1】本発明の濾過布の断面拡大図である。FIG. 1 is an enlarged cross-sectional view of a filter cloth of the present invention.

【図2】本発明の他の実施例を示した断面拡大図であ
る。
FIG. 2 is an enlarged sectional view showing another embodiment of the present invention.

【図3】図1の濾過布の製造方法の概略説明図である。FIG. 3 is a schematic explanatory view of a method for producing the filter cloth of FIG.

【図4】分割型複合繊維の一例を示した繊維断面図であ
る。
FIG. 4 is a fiber sectional view showing an example of a splittable conjugate fiber.

【符号の説明】[Explanation of symbols]

1 濾過布 2 極細繊維の不織布層 3 シート基材 4 補強基布 5 濾過面 DESCRIPTION OF SYMBOLS 1 Filtration cloth 2 Microfiber nonwoven fabric layer 3 Sheet base material 4 Reinforcement base cloth 5

───────────────────────────────────────────────────── フロントページの続き 審査官 新居田 知生 (56)参考文献 実開 平5−18615(JP,U) (58)調査した分野(Int.Cl.7,DB名) B01D 39/00 - 39/20 ────────────────────────────────────────────────── ─── Continuing from the front page Examiner Tomoo Niida (56) References Japanese Utility Model No. 5-18615 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) B01D 39/00-39 / 20

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ート基材の一方の面に、このシート基
材と繊維交絡により一体化された平均繊度が0.5デニ
ール以下の極細繊維による不織布層が配されて濾過面が
形成され、その極細繊維の不織布層の表面が該極細繊維
は溶融せずに平滑化されていることを特徴とする濾過
布。
On one surface of 1. A sheet over preparative substrate, average fineness, which is integrated by the sheet substrate and the fibers entangled filtration surface nonwoven layer is arranged for the following ultrafine fibers 0.5 denier formed is, surface ultrafine fibers of the nonwoven fabric layer of the ultrafine fibers
Is a filter cloth characterized by being smoothed without melting .
【請求項2】 上記極細繊維層の目付けが100〜15
0g/m2である請求項1記載の濾過布。
2. The fabric weight of the ultrafine fiber layer is 100 to 15
2. The filter cloth according to claim 1, wherein the amount is 0 g / m 2 .
【請求項3】ート基材の一方の面に分割後の太さが
0.5デニール以下となる分割型複合繊維ウェブを重ね
合わせてそのウェブ側からニードルパンチングを施して
分割型複合繊維ウェブを上記シート基材に交絡させ、次
いでウェブ側から高圧液体流処理を行って分割型複合繊
維を分割してシート基材の面に極細繊維による不織布層
を形成し、乾燥後、濾過面を形成している極細繊維が溶
融しない程度に加熱した加熱ロールにより上記ウェブ面
を平滑化することを特徴とする濾過布の製造方法。
3. A sheet over preparative group one surface in the thickness after the division is less than 0.5 deniers splittable conjugate fiber by overlapping web splittable conjugate fiber is subjected to needle punching from the web side of the material the web is entangled to the sheet substrate, then dividing the splittable conjugate fiber by performing a high-pressure liquid jet process to form a nonwoven layer by ultrafine fiber on the surface of the sheet base material from the web side, after drying, the filtering surface The ultrafine fibers that are forming
A method for producing a filter cloth, wherein the web surface is smoothed by a heating roll heated so as not to melt .
JP17496492A 1992-06-08 1992-06-08 Filter cloth and method for producing the same Expired - Fee Related JP3233988B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17496492A JP3233988B2 (en) 1992-06-08 1992-06-08 Filter cloth and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17496492A JP3233988B2 (en) 1992-06-08 1992-06-08 Filter cloth and method for producing the same

Publications (2)

Publication Number Publication Date
JPH0671122A JPH0671122A (en) 1994-03-15
JP3233988B2 true JP3233988B2 (en) 2001-12-04

Family

ID=15987821

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17496492A Expired - Fee Related JP3233988B2 (en) 1992-06-08 1992-06-08 Filter cloth and method for producing the same

Country Status (1)

Country Link
JP (1) JP3233988B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100364868B1 (en) * 2000-10-25 2002-12-16 주식회사 나노테크닉스 A carbin air filter for car, and a process of preparing the same
JP3864123B2 (en) * 2002-08-19 2006-12-27 株式会社クラレ Roller brush structure for painting
KR20100102601A (en) * 2007-12-07 2010-09-24 데이진 화이바 가부시키가이샤 Process for production of fabrics, fabrics and textile goods
JP6453152B2 (en) * 2015-04-27 2019-01-16 日本フエルト株式会社 Filter material for bag filter and method for producing the same
CN105148610B (en) * 2015-06-25 2017-04-12 杭州金百合非织造布有限公司 Bubble-point type air filtering gauze for doors and windows
CN106283393B (en) * 2015-06-25 2018-05-08 杭州金百合非织造布有限公司 A kind of coloured plane formula framework material for door and window air filtration
CN106310789B (en) * 2015-06-30 2018-05-11 厦门三维丝环保股份有限公司 A kind of super fine fibre ultra-clean filtering high temperature filtrate of low grammes per square metre and preparation method thereof
CN110508055A (en) * 2019-09-28 2019-11-29 辽东学院 A kind of high-precision composite filtering cloth
CN112473245A (en) * 2020-09-14 2021-03-12 福州大学 Filter material substrate, ultra-clean high-flux filter material and preparation method thereof

Also Published As

Publication number Publication date
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