JP2005095803A - Filter medium for air filter, and air filter unit using it - Google Patents

Filter medium for air filter, and air filter unit using it Download PDF

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JP2005095803A
JP2005095803A JP2003333983A JP2003333983A JP2005095803A JP 2005095803 A JP2005095803 A JP 2005095803A JP 2003333983 A JP2003333983 A JP 2003333983A JP 2003333983 A JP2003333983 A JP 2003333983A JP 2005095803 A JP2005095803 A JP 2005095803A
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filter medium
air filter
porous membrane
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Eizo Kawano
栄三 川野
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Nitto Denko Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a filter medium for an air filter capable of forming more pleats, having large effective filtering area and small pressure loss. <P>SOLUTION: This air filter medium 1 comprises at least one layer of PTFE porous membrane 2 and multiple layers of air permeable support layers 3, the medium 1 has a thickness of 0.3mm or less. It is preferable that the pressure loss is 20-200 Pa when passing air at a velocity of 5.3 cm/sec, and a collection efficiency is 99.999% or more when measured using dioctyl phthalate of a particle size of 0.1-0.2 μm. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明はエアフィルタ用濾材およびそれを用いたエアフィルタユニットに関する。   The present invention relates to an air filter medium and an air filter unit using the same.

従来、クリーンルームで使用されるエアフィルタ用濾材には、ガラス繊維にバインダーを加えて抄紙したものが多く用いられてきた。しかし、このような濾材には、濾材中に付着した小繊維が存在したり、折り曲げ加工時に発塵するといった問題があった。さらにこの濾材には、フッ酸等、ある種の化学薬品と接触すると発塵するという問題もあった。   Conventionally, as a filter medium for an air filter used in a clean room, paper made by adding a binder to glass fiber has been used in many cases. However, such filter media have problems such as the presence of small fibers attached to the filter media and generation of dust during bending. Further, this filter medium has a problem that it generates dust when it comes into contact with certain chemicals such as hydrofluoric acid.

ポリテトラフルオロエチレン(以下「PTFE」という)は、クリーンな材料であり、近年、PTFE多孔質膜を含む濾材が、半導体工業等のクリーンルームに用いられる高性能エアフィルタの濾材として使用され始めている(例えば、特許文献1〜4参照)。一般に、PTFE多孔質膜は、補強のための通気性支持層とラミネートされてエアフィルタ用濾材とされる。実際には、強度を確保するために複数層の通気性支持層を含む構造のエアフィルタ用濾材が用いられることが多い。これらのエアフィルタ用濾材は、連続したW字状のひだ折り加工(以下「プリーツ加工」ともいう)がなされ、さらに枠付けされてエアフィルタユニットとして用いられる。
特開平5−202217号公報(第5頁、第25図) 特開平10−30031号公報(第8頁、第1−2図) 特開2000−33244号公報(第5頁) 特開2000−61280号公報(第4−5頁、第2−5図)
Polytetrafluoroethylene (hereinafter referred to as “PTFE”) is a clean material. In recent years, a filter medium including a PTFE porous membrane has begun to be used as a filter medium for a high-performance air filter used in a clean room such as the semiconductor industry ( For example, see Patent Documents 1 to 4). Generally, a porous PTFE membrane is laminated with a breathable support layer for reinforcement to form a filter material for an air filter. In practice, a filter medium for an air filter having a structure including a plurality of breathable support layers is often used to ensure strength. These air filter media are subjected to continuous W-shaped fold folding (hereinafter also referred to as “pleating”), and are further framed and used as an air filter unit.
JP-A-5-202217 (5th page, FIG. 25) Japanese Patent Laid-Open No. 10-30031 (page 8, FIG. 1-2) JP 2000-33244 A (page 5) Japanese Unexamined Patent Publication No. 2000-61280 (pages 4-5 and 2-5)

しかしながら、複数層の通気性支持層を含むエアフィルタ用濾材では、その厚みはいずれも例えば0.3mmよりも厚いため、エアフィルタを透過する気体が直交する面の単位面積当たりのひだ数(折り山数)が所望の数よりも少なくならざるをえなかった。折り山数が減少すると、エアフィルタユニットの濾過有効面積が減少し、圧力損失が増大することが問題であった。   However, in the air filter medium including a plurality of air-permeable support layers, the thickness of each is greater than, for example, 0.3 mm. Therefore, the number of pleats per unit area of the plane perpendicular to the gas passing through the air filter (folded) The number of peaks) must be less than the desired number. When the number of folds is reduced, the effective filtration area of the air filter unit is reduced, and the pressure loss is increased.

本発明のエアフィルタ用濾材は、少なくとも1層のPTFE多孔質膜と複数層の通気性支持層とを含むエアフィルタ用濾材であって、前記エアフィルタ用濾材の厚さが0.3mm以下であることを特徴とする。   The air filter medium of the present invention is an air filter medium including at least one PTFE porous membrane and a plurality of air-permeable support layers, and the thickness of the air filter medium is 0.3 mm or less. It is characterized by being.

本発明のエアフィルタユニットは、本発明のエアフィルタ用濾材を用いたことを特徴とする。   The air filter unit of the present invention is characterized by using the air filter medium of the present invention.

本発明によれば、より多くのプリーツを形成可能なエアフィルタ用濾材、濾過有効面積が大きく、圧力損失が小さいエアフィルタユニットを提供できる。   ADVANTAGE OF THE INVENTION According to this invention, the filter medium for air filters which can form more pleats, the air filter unit with a large effective filtration area and a small pressure loss can be provided.

以下に、本発明のエアフィルタ用濾材およびそれを用いたエアフィルタユニットの一例を、図面を用いて説明する。   Hereinafter, an example of a filter medium for an air filter of the present invention and an air filter unit using the same will be described with reference to the drawings.

図1に示すように、本実施の形態のエアフィルタ用濾材1は、少なくとも1層のPTFE多孔質膜2と複数層の通気性支持層3とを含み、エアフィルタ用濾材1の厚さが0.3mm以下であるので、下記の実施例において示すように、より多くのプリーツを形成可能である。したがって、本実施の形態のエアフィルタ用濾材1を用いれば、濾過有効面積が大きく、圧力損失が小さいエアフィルタユニットを提供きる。尚、エアフィルタ用濾材1の厚さの下限について特に制限はなく、通常、100μm以上である。   As shown in FIG. 1, the air filter medium 1 of the present embodiment includes at least one PTFE porous membrane 2 and a plurality of air-permeable support layers 3, and the thickness of the air filter medium 1 is as follows. Since it is 0.3 mm or less, more pleats can be formed as shown in the following examples. Therefore, if the filter material 1 for air filters of this Embodiment is used, the air filter unit with a large effective filtration area and a small pressure loss can be provided. In addition, there is no restriction | limiting in particular about the minimum of the thickness of the filter medium 1 for air filters, Usually, it is 100 micrometers or more.

尚、本発明において、エアフィルタ用濾材の厚みは下記の方法に従って測定した値である。   In the present invention, the thickness of the air filter medium is a value measured according to the following method.

[エアフィルタ用濾材の厚み]
ダイヤルシックネスゲージ(測定子直径10mm、最小目盛0.01mm)により、エアフィルタ用濾材1の任意の箇所の厚みを5点測定し、その平均値を求める。
[Thickness of air filter media]
Using a dial thickness gauge (measuring element diameter 10 mm, minimum graduation 0.01 mm), the thickness of an arbitrary portion of the filter medium 1 for air filter is measured at five points, and the average value is obtained.

PTFE多孔質膜2は、使用用途に応じた捕集機能が発揮されるものであれば、孔径等について特に限定されないが、通常、平均孔径が0.01〜5μm、厚みが2μm〜30μmであることが好ましい。   The PTFE porous membrane 2 is not particularly limited with respect to the pore diameter and the like as long as the collection function according to the intended use is exhibited, but usually the average pore diameter is 0.01 to 5 μm and the thickness is 2 to 30 μm. It is preferable.

PTFE多孔質膜2の圧力損失は、5.3cm/sの流速で空気を透過させたときのエアフィルタ用濾材1の圧力損失が20Pa〜200Paとなるように決定すればよいが、通常30Pa〜150Pa程度が適当である。   The pressure loss of the PTFE porous membrane 2 may be determined so that the pressure loss of the air filter medium 1 when air is permeated at a flow rate of 5.3 cm / s is 20 Pa to 200 Pa. About 150 Pa is appropriate.

PTFE多孔質膜2の捕集効率は、粒径が0.1μm〜0.2μmのジオクチルフタレートを用いて測定した場合に99.9999%以上であることが好ましい。PTFE多孔質膜2の捕集効率が99.9999%以上であると、PTFE多孔質膜2に通気性支持層3を積層することにより、上記方法により測定した捕集効率が99.999%以上であるエアフィルタ用濾材の作製が容易だからである。   The collection efficiency of the PTFE porous membrane 2 is preferably 99.9999% or more when measured using dioctyl phthalate having a particle size of 0.1 μm to 0.2 μm. When the collection efficiency of the PTFE porous membrane 2 is 99.9999% or more, the collection efficiency measured by the above method is 99.999% or more by laminating the air-permeable support layer 3 on the PTFE porous membrane 2. This is because it is easy to produce a filter medium for air filter.

尚、PTFE多孔質膜2およびエアフィルタ用濾材1の圧力損失、捕集効率は下記のようにして測定した値である。   In addition, the pressure loss and the collection efficiency of the PTFE porous membrane 2 and the filter medium 1 for air filter are values measured as follows.

(1)圧力損失
サンプルを有効面積が100cm2となるように円形ホルダーにセットし、入口側から空気を供給しつつ、入口側と出口側に圧力差を与え、このサンプルを通過する空気の流速を5.3cm/sに調整したときの圧力損失(初期値)を圧力計(マノメーター)で測定した。
(1) Pressure loss Set the sample in a circular holder so that the effective area is 100 cm 2 , supply air from the inlet side, give a pressure difference between the inlet side and the outlet side, and the flow velocity of air passing through this sample Was adjusted to 5.3 cm / s, and the pressure loss (initial value) was measured with a pressure gauge (manometer).

(2)捕集効率
サンプルを有効面積が100cm2となるように円形ホルダーにセットし、サンプルを通過する空気の流速を5.3cm/sに調整しながら、サンプルの上流側に粒径が0.1μm〜0.2μmのジオクチルフタレート(DOP)を濃度が約107個/リットルとなるように供給する。上流側の粒子濃度(個/リットル)とサンプルを透過してきた下流側の粒子濃度(個/リットル)とをパーティクルカウンターで測定し、その測定値を下記式(数1)に代入して捕集効率を求める。
(数1)
捕集効率(%)=(1−(下流側濃度/上流側濃度))×100
(2) Collection efficiency The sample is set in a circular holder so that the effective area is 100 cm 2, and the particle size is 0 on the upstream side of the sample while adjusting the flow rate of air passing through the sample to 5.3 cm / s. .1 μm to 0.2 μm of dioctyl phthalate (DOP) is supplied so that the concentration is about 10 7 pieces / liter. The upstream particle concentration (pieces / liter) and the downstream particle concentration (pieces / liter) that have permeated through the sample are measured with a particle counter, and the measured values are substituted into the following equation (Equation 1) for collection. Seeking efficiency.
(Equation 1)
Collection efficiency (%) = (1− (downstream concentration / upstream concentration)) × 100

捕集効率と圧力損失のバランスを示す尺度として、PF(Performance of filter)値がよく用いられる。PF値が大きな濾材ほど粒子の捕集効率が高く、かつ圧力損失が低いことになる。PTFE多孔質膜2のPF値は22以上であることが好ましく、エアフィルタ用濾材1のPF値も22以上であることが好ましい。PF値は下記式(数2)で与えられる。尚、(数2)中の透過率は、透過率=(100−捕集効率)の関係から得られる。
(数2)
PF値=[−Log(透過率/100)/圧力損失(mmH2O)]×100
A PF (Performance of filter) value is often used as a measure of the balance between collection efficiency and pressure loss. A filter medium with a larger PF value has higher particle collection efficiency and lower pressure loss. The PF value of the PTFE porous membrane 2 is preferably 22 or more, and the PF value of the air filter medium 1 is also preferably 22 or more. The PF value is given by the following equation (Equation 2). In addition, the transmittance | permeability in (Equation 2) is obtained from the relationship of the transmittance | permeability = (100-collection efficiency).
(Equation 2)
PF value = [− Log (transmittance / 100) / pressure loss (mmH 2 O)] × 100

次にPTFE多孔質膜2の作製方法の一例を説明する。まず、PTFEファインパウダーに液状潤滑剤を加えたペースト状の混和物を予備成形する。PTFEファインパウダーには特に制限はなく、市販のものを使用できる。液状潤滑剤としては、PTFEファインパウダーの表面を濡らすことができ、抽出や加熱により除去できるものであれば特に制限されず、例えば、ナフサ、ホワイトオイル等の炭化水素を使用できる。液状潤滑剤の添加量は、PTFEファインパウダー100重量部に対して5〜50重量部程度が適当である。予備成形は、液状潤滑剤が絞り出されない程度の圧力で行うとよい。   Next, an example of a method for producing the PTFE porous membrane 2 will be described. First, a paste-like mixture obtained by adding a liquid lubricant to PTFE fine powder is preformed. There is no restriction | limiting in particular in PTFE fine powder, A commercially available thing can be used. The liquid lubricant is not particularly limited as long as it can wet the surface of the PTFE fine powder and can be removed by extraction or heating. For example, hydrocarbons such as naphtha and white oil can be used. The addition amount of the liquid lubricant is suitably about 5 to 50 parts by weight with respect to 100 parts by weight of PTFE fine powder. The preforming may be performed at a pressure that does not squeeze out the liquid lubricant.

次に、予備成形体を押出し、圧延することによってシート状に成形し、このようにして得られたシート状の成形体を少なくとも一軸方向に延伸してPTFE多孔質膜を得る。尚、延伸は、液状潤滑剤を除去してから行うとよい。延伸条件は、適宜設定できるが、通常、温度は30〜320℃であり、延伸倍率は、縦方向、横方向ともに2〜30倍である。   Next, the preform is extruded and rolled to form a sheet, and the sheet-like formed body thus obtained is stretched at least in a uniaxial direction to obtain a PTFE porous membrane. The stretching may be performed after removing the liquid lubricant. Stretching conditions can be set as appropriate, but usually the temperature is 30 to 320 ° C., and the stretching ratio is 2 to 30 times in both the longitudinal and transverse directions.

以上のようにして作製されたPTFE多孔質膜は、未焼成の状態では強度が弱いため、熱処理を行うことが望ましい。熱処理はPTFE多孔質膜の融点以上で行うが、350〜450℃で行うことが好ましい。加熱方法について特に制限はないが、熱風を吹き付ける方法や、高温の炉内を通過させる方法等がある。   Since the PTFE porous membrane produced as described above has low strength in an unfired state, it is desirable to perform heat treatment. The heat treatment is performed at a temperature equal to or higher than the melting point of the PTFE porous membrane, but is preferably performed at 350 to 450 ° C. Although there is no restriction | limiting in particular about a heating method, There exist the method of blowing a hot air, the method of allowing the inside of a high temperature furnace to pass, etc.

通気性支持層3は、PTFE多孔質膜2との接合により厚さが0.3mm以下のエアフィルタ用濾材を作製できれば、材質、構造、形態等について特に制限はないが、PTFE多孔質膜よりも通気性に優れた材料、例えば、フェルト、不織布、織布、メッシュ(網目状シート)、その他の多孔質材料を用いることができる。特には、強度、捕集性、柔軟性および作業性の点からは不織布が好ましい。さらに、不織布を構成する一部または全部の繊維が芯鞘構造の複合繊維であり、芯成分が鞘成分より相対的に融点が高い繊維、例えば合成繊維であることが好ましい。通気性支持層3を鞘成分の融点より高い温度に加熱すれば、通気性支持層3とPTFE多孔質膜2とを容易に熱ラミネートできる。   The air-permeable support layer 3 is not particularly limited in terms of material, structure, form, and the like as long as a filter medium for an air filter having a thickness of 0.3 mm or less can be produced by joining with the PTFE porous membrane 2, but from the PTFE porous membrane Also, a material excellent in air permeability, for example, felt, non-woven fabric, woven fabric, mesh (mesh sheet), and other porous materials can be used. In particular, a nonwoven fabric is preferable from the viewpoints of strength, collection property, flexibility, and workability. Furthermore, it is preferable that a part or all of the fibers constituting the nonwoven fabric are composite fibers having a core-sheath structure, and the core component is a fiber having a relatively higher melting point than the sheath component, for example, a synthetic fiber. If the breathable support layer 3 is heated to a temperature higher than the melting point of the sheath component, the breathable support layer 3 and the PTFE porous membrane 2 can be easily heat-laminated.

通気性支持層3の材料としては、特に制限はないが、ポリオレフィン(ポリエチレン(PE)、ポリプロピレン(PP)等)、ポリアミド、ポリエステル(ポリエチレンテレフタレート(PET)等)、芳香族ポリアミドまたはこれらの複合材等を用いることができる。   The material of the breathable support layer 3 is not particularly limited, but polyolefin (polyethylene (PE), polypropylene (PP), etc.), polyamide, polyester (polyethylene terephthalate (PET), etc.), aromatic polyamide, or a composite material thereof. Etc. can be used.

通気性支持層3が不織布である場合、その目付け量は100g/m2以下であることが好ましい。目付け量が100g/m2以下であれば、通気性支持層3とPTFE多孔質膜2とを、エアフィルタ用濾材1の厚みが0.3mm以下となるように、例えば熱ラミネート法等により圧着すれば、圧力損失が20Pa〜200Paのエアフィルタ用濾材を容易に作製できるからである。目付け量の下限について特に制限はないが、通常10g/m2以上であることが好ましい。 When the air-permeable support layer 3 is a nonwoven fabric, the basis weight is preferably 100 g / m 2 or less. If the basis weight is 100 g / m 2 or less, the breathable support layer 3 and the PTFE porous membrane 2 are pressure-bonded by, for example, a heat laminating method so that the thickness of the air filter medium 1 is 0.3 mm or less. This is because an air filter medium having a pressure loss of 20 Pa to 200 Pa can be easily produced. Although there is no restriction | limiting in particular about the minimum of the fabric weight, Usually, it is preferable that it is 10 g / m < 2 > or more.

通気性支持層3の厚みについては、PTFE多孔質膜2との接合により厚さが0.3mm以下のエアフィルタ用濾材1を作製できれば、特に制限はないが、エアフィルタ用濾材1が、例えば、図2に示すように、2層のPTFE多孔質膜2と3層の通気性支持層3を含み、通気性支持層3の目付け量が10〜20g/m2である場合、PTFE多孔質膜2と接合される前における通気性支持層3の厚みは、通常50〜120μmが適当である。 The thickness of the air-permeable support layer 3 is not particularly limited as long as the air filter medium 1 having a thickness of 0.3 mm or less can be produced by bonding with the PTFE porous membrane 2, but the air filter medium 1 is, for example, 2, when two layers of the PTFE porous membrane 2 and three layers of the air-permeable support layer 3 are included, and the basis weight of the air-permeable support layer 3 is 10 to 20 g / m 2 , the PTFE porous material The thickness of the breathable support layer 3 before being bonded to the membrane 2 is usually 50 to 120 μm.

すなわち、図2に示した本実施の形態のエアフィルタ用濾材1の製造方法においては、例えば、PTFE多孔質膜2と通気性支持層3とを重ね合わせた後、加熱しながら加圧して、PTFE多孔質膜2と通気性支持層3とを接合する工程を含み、上記工程において、厚みが50〜120μm、目付け量が10〜20g/m2の通気性支持層3を用いることが好ましい。 That is, in the method for manufacturing the air filter medium 1 of the present embodiment shown in FIG. 2, for example, after the PTFE porous membrane 2 and the air-permeable support layer 3 are superposed, pressurizing while heating, Including the step of bonding the PTFE porous membrane 2 and the air-permeable support layer 3, it is preferable to use the air-permeable support layer 3 having a thickness of 50 to 120 μm and a weight per unit area of 10 to 20 g / m 2 .

通気性支持層3とPTFE多孔質膜2との接合は、上記熱ラミネートの他に、例えば、接着剤ラミネート、加熱溶着、超音波溶着、振動溶着、接着剤による接着等の方法により行える。例えば、熱ラミネートにより通気性支持層3とPTFE多孔質膜2とを接合する場合は、加熱により通気性支持層3の一部を溶融し、通気性支持層3とPTFE多孔質膜2とを接着すればよい。また、ホットメルトパウダーのような融着剤を介在させてPTFE多孔質膜2と通気性支持層3とを接着してもよい。   The breathable support layer 3 and the PTFE porous membrane 2 can be joined by, for example, a method such as adhesive lamination, heat welding, ultrasonic welding, vibration welding, and adhesion using an adhesive, in addition to the above thermal laminate. For example, when the breathable support layer 3 and the PTFE porous membrane 2 are joined by heat lamination, a part of the breathable support layer 3 is melted by heating, and the breathable support layer 3 and the PTFE porous membrane 2 are bonded. What is necessary is just to adhere. Further, the PTFE porous membrane 2 and the air-permeable support layer 3 may be bonded with a fusing agent such as hot melt powder interposed.

エアフィルタ用濾材1は、図1または図2に示した例に制限されないが、図1および図2に示した例のように、エアフィルタ用濾材1が、複数層の通気性支持層3から選ばれる少なくとも1対の通気性支持層3の間に少なくとも1層のPTFE多孔質膜2が配置された構造を含むと、少なくとも1層のPTFE多孔質膜2について外力等による損傷を抑制できるので好ましい。   The air filter medium 1 is not limited to the example shown in FIG. 1 or FIG. 2, but the air filter medium 1 is formed from a plurality of air-permeable support layers 3 as in the examples shown in FIGS. Including at least one layer of the PTFE porous membrane 2 between at least one pair of the breathable support layers 3 selected can damage the at least one layer of the PTFE porous membrane 2 due to an external force or the like. preferable.

さらに図2に示すように、エアフィルタ用濾材1が、2層以上のPTFE多孔質膜2を含み、1対のPTFE多孔質膜2の間に通気性支持層3が配置された構造を含んでいると、例えば、外力等によって一方のPTFE多孔質膜2にピンホールが発生しても、他方のPTFE多孔質膜2については損傷しづらく、濾材としての機能が直ちに損われることないので好ましい。   Further, as shown in FIG. 2, the air filter medium 1 includes a structure in which two or more layers of the PTFE porous membrane 2 are included, and the air-permeable support layer 3 is disposed between the pair of PTFE porous membranes 2. In this case, for example, even if a pinhole is generated in one PTFE porous membrane 2 due to an external force or the like, the other PTFE porous membrane 2 is not easily damaged, and the function as a filter medium is not immediately impaired. .

エアフィルタ用濾材1は、全体の厚みが0.3mm以下であれば、図1および図2に示した例のようにPTFE多孔質膜2と通気性支持層3とが交互に積層されていてもよいし、PTFE多孔質膜2および通気性支持層3のいずれか一方もしくは両方が連続して積層されている部分があってもよい。特性が互いに異なる複数層のPTFE多孔質膜2、特性が互いに異なる複数層の通気性支持層3を含んでいてもよい。   If the entire thickness of the air filter medium 1 is 0.3 mm or less, the PTFE porous membrane 2 and the air-permeable support layer 3 are alternately laminated as in the example shown in FIGS. 1 and 2. Alternatively, there may be a portion in which either one or both of the PTFE porous membrane 2 and the air-permeable support layer 3 are continuously laminated. A plurality of porous PTFE membranes 2 having different characteristics and a plurality of breathable support layers 3 having different characteristics may be included.

複数層のPTFE多孔質膜2が連続して積層された形態では、複数層のPTFE多孔質膜2は単に重ね合わせるだけでもよいし、成膜時に圧着、熱融着等により互いに接合してもよい。   In a form in which a plurality of layers of PTFE porous membranes 2 are continuously laminated, the plurality of layers of PTFE porous membranes 2 may be simply overlapped, or may be joined together by pressure bonding, heat fusion, or the like during film formation. Good.

図3は、プリーツ加工されたエアフィルタ用濾材1の一例の断面図である。長尺の濾材を長さ方向に所定の間隔をおいて交互に山折り/谷折りしていくと(プリーツ加工を施すと)、断面方向から見て連続したW字状のエアフィルタ用濾材1を得ることができる。   FIG. 3 is a cross-sectional view of an example of the air filter medium 1 that has been pleated. When a long filter medium is alternately fold-folded / valley-folded at a predetermined interval in the length direction (when pleating is applied), a continuous W-shaped filter medium for air filter 1 as viewed from the cross-sectional direction Can be obtained.

プリーツ加工は、例えば、外周にブレードを配置した一対の回転ドラムを回転させながら濾材をひだ折りしていくロータリー方式、濾材の移送方向に所定の間隔をおいて配置した一対のブレードを移動させながら濾材を両面から交互に折り畳んでいくレシプロ方式等が採用できる。   The pleating process is, for example, a rotary method in which a pair of rotating drums having blades arranged on the outer periphery is rotated while the filter medium is folded, while a pair of blades arranged at a predetermined interval in the transfer direction of the filter medium is moved. A reciprocating method in which the filter medium is alternately folded from both sides can be adopted.

W字状に折り畳まれたエアフィルタ用濾材1は、例えば図4に示すように、アルミニウムからなる支持枠22等で枠付けされてエアフィルタユニットとなる。   For example, as shown in FIG. 4, the air filter medium 1 folded in a W shape is framed with a support frame 22 made of aluminum to form an air filter unit.

次に、実施例を挙げて本発明をより具体的に説明するが、本発明は下記の実施例に限定されるものではない。   Next, the present invention will be described more specifically with reference to examples, but the present invention is not limited to the following examples.

(実施例1)
PTFEファインパウダー(旭硝子社製、「フルオンCD−123」)100重量部に対して液状潤滑剤(ドデカン)20重量部を均一に混合してペースト状の混和物を予備成形し、ペースト押出により丸棒状に成型した。成形物を厚み0.2mmに圧延し液状潤滑剤をノルマルデカンにより抽出除去した後、二軸方向に延伸してPTFE多孔質膜(厚さ10μm、気孔率93%、平均孔径1.0μm、圧力損失80Pa、捕集効率99.95%、PF値41)を得た。次に、このPTFE多孔質膜とPET/PE芯鞘不織布(厚さ110μm、目付け量20g/m2)とを熱ラミネート(ロール温度180℃)して、5層構造(不織布/PTFE多孔質膜/不織布/PTFE多孔質膜/不織布)のエアフィルタ用濾材を得た。
(Example 1)
20 parts by weight of a liquid lubricant (Dodecane) is uniformly mixed with 100 parts by weight of PTFE fine powder (manufactured by Asahi Glass Co., Ltd., “Fluon CD-123”) to pre-form a paste-like mixture, and round by paste extrusion Molded into a rod shape. The molded product was rolled to a thickness of 0.2 mm, and the liquid lubricant was extracted and removed with normal decane, and then stretched in the biaxial direction to form a PTFE porous membrane (thickness 10 μm, porosity 93%, average pore diameter 1.0 μm, pressure A loss of 80 Pa, a collection efficiency of 99.95%, and a PF value of 41) were obtained. Next, this PTFE porous membrane and a PET / PE core-sheath nonwoven fabric (thickness 110 μm, basis weight 20 g / m 2 ) are thermally laminated (roll temperature 180 ° C.) to form a five-layer structure (nonwoven fabric / PTFE porous membrane). / Filter / nonwoven fabric / PTFE porous membrane / nonwoven fabric).

(実施例2)
実施例1で作製したPTFE多孔質膜とPET/PE芯鞘不織布(厚さ90μm、目付け量15g/m2)とを熱ラミネート(ロール温度180℃)して、5層構造(不織布/PTFE多孔質膜/不織布/PTFE多孔質膜/不織布)のエアフィルタ用濾材を得た。
(Example 2)
The PTFE porous membrane prepared in Example 1 and a PET / PE core-sheath nonwoven fabric (thickness 90 μm, basis weight 15 g / m 2 ) are thermally laminated (roll temperature 180 ° C.) to form a five-layer structure (nonwoven fabric / PTFE porous The filter material for air filters of a membrane / nonwoven fabric / PTFE porous membrane / nonwoven fabric) was obtained.

(比較例1)
実施例1で作製したPTFE多孔質膜とPET/PE芯鞘不織布(厚さ150μm、目付け量30g/m2)とを熱ラミネート(ロール温度180℃)して、5層構造(不織布/PTFE多孔質膜/不織布/PTFE多孔質膜/不織布)のエアフィルタ用濾材を得た。
(Comparative Example 1)
The PTFE porous membrane prepared in Example 1 and a PET / PE core-sheath nonwoven fabric (thickness 150 μm, basis weight 30 g / m 2 ) are thermally laminated (roll temperature 180 ° C.) to form a five-layer structure (nonwoven fabric / PTFE porous The filter material for air filters of a membrane / nonwoven fabric / PTFE porous membrane / nonwoven fabric) was obtained.

実施例1、2および比較例1のエアフィルタ用濾材の厚さ、圧力損失、捕集効率、PF値を求め、表1に示した。また、実施例1、2および比較例1のエアフィルタ用濾材について、プリーツ加工機を用いて、エアフィルタ用濾材の折り畳み方向の厚さが610mmになるまでプリーツ加工(折り幅30mm)を施し、折り山数を求め、表1に示した。折り山数は、610mmをエアフィルタ用濾材の厚みの2倍で除して算出した。   The thickness, pressure loss, collection efficiency, and PF value of the air filter media of Examples 1 and 2 and Comparative Example 1 were determined and shown in Table 1. Moreover, about the filter medium for air filters of Examples 1, 2 and Comparative Example 1, using a pleating machine, pleating (folding width 30 mm) is performed until the thickness in the folding direction of the filter medium for air filter is 610 mm, The number of folds was determined and shown in Table 1. The number of folds was calculated by dividing 610 mm by twice the thickness of the air filter medium.

Figure 2005095803
表1に示すとおり、エアフィルタ用濾材の厚さが0.3mm以下であると、より多くのプリーツを形成可能であることが確認できた。
Figure 2005095803
As shown in Table 1, it was confirmed that more pleats could be formed when the thickness of the air filter medium was 0.3 mm or less.

以上のように、本発明のエアフィルタ用濾材は、より多くのプリーツを形成可能であり、エアフィルタ用濾材等として有用である。また、本発明のエアフィルタ用濾材を用いた本発明のエアフィルタユニットは、濾過有効面積が大きく、圧力損失が小さいのでエアフィルタユニット等として有用である。   As described above, the air filter medium of the present invention can form more pleats and is useful as an air filter medium. The air filter unit of the present invention using the air filter medium of the present invention is useful as an air filter unit or the like because it has a large effective filtration area and a small pressure loss.

本発明のエアフィルタ用濾材の一例を示す断面図Sectional drawing which shows an example of the filter medium for air filters of this invention 本発明のエアフィルタ用濾材の他の例を示す断面図Sectional drawing which shows the other example of the filter medium for air filters of this invention 本発明のエアフィルタ用濾材の他の例を示す断面図Sectional drawing which shows the other example of the filter medium for air filters of this invention 本発明のエアフィルタユニットの一例を示す斜視図The perspective view which shows an example of the air filter unit of this invention

符号の説明Explanation of symbols

1 エアフィルタ用濾材
2 PTFE多孔質膜
3 通気性支持層
DESCRIPTION OF SYMBOLS 1 Filter medium for air filters 2 PTFE porous membrane 3 Breathable support layer

Claims (9)

少なくとも1層のポリテトラフルオロエチレン多孔質膜と複数層の通気性支持層とを含むエアフィルタ用濾材であって、前記エアフィルタ用濾材の厚さが0.3mm以下であることを特徴とするエアフィルタ用濾材。   An air filter medium comprising at least one polytetrafluoroethylene porous membrane and a plurality of breathable support layers, wherein the thickness of the air filter medium is 0.3 mm or less. Air filter media. 5.3cm/sの流速で空気を透過させたときの圧力損失が20Pa〜200Paである請求項1に記載のエアフィルタ用濾材。   The filter medium for an air filter according to claim 1, wherein a pressure loss when air is permeated at a flow rate of 5.3 cm / s is 20 Pa to 200 Pa. 粒径が0.1μm〜0.2μmのジオクチルフタレートを用いて測定される捕集効率が99.999%以上である請求項1または2に記載のエアフィルタ用濾材。   The filter medium for an air filter according to claim 1 or 2, wherein the collection efficiency measured using dioctyl phthalate having a particle size of 0.1 µm to 0.2 µm is 99.999% or more. 前記複数層の通気性支持層から選ばれる少なくとも1対の通気性支持層の間に、少なくとも1層の前記ポリテトラフルオロエチレン多孔質膜が配置されている請求項1〜3のいずれかの項に記載のエアフィルタ用濾材。   The at least 1 layer of the said polytetrafluoroethylene porous membrane is arrange | positioned between the at least 1 pair of air permeable support layers chosen from the said several air permeable support layers. The filter medium for air filters described in 1. 複数層の前記ポリテトラフルオロエチレン多孔質膜を含み、前記複数層のポリテトラフルオロエチレン多孔質膜から選ばれる少なくとも1対のポリテトラフルオロエチレン多孔質膜の間に、少なくとも1層の通気性支持層が配置されている請求項1〜4のいずれかの項に記載のエアフィルタ用濾材。   A plurality of layers of the polytetrafluoroethylene porous membrane, and at least one layer of air-permeable support between at least one pair of polytetrafluoroethylene porous membranes selected from the plurality of layers of polytetrafluoroethylene porous membrane The filter medium for an air filter according to any one of claims 1 to 4, wherein a layer is disposed. 前記通気性支持層が不織布からなる請求項1〜5のいずれかの項に記載のエアフィルタ用濾材。   The air filter medium according to any one of claims 1 to 5, wherein the air-permeable support layer is made of a nonwoven fabric. 前記不織布を構成する一部または全部の繊維が芯鞘構造の複合繊維であり、芯成分が鞘成分より融点が高い繊維である請求項6に記載のエアフィルタ用濾材。   The filter medium for an air filter according to claim 6, wherein a part or all of the fibers constituting the nonwoven fabric are composite fibers having a core-sheath structure, and the core component is a fiber having a melting point higher than that of the sheath component. 連続したW字状に折り畳まれた請求項1〜7のいずれかの項に記載のエアフィルタ用濾材。   The filter medium for an air filter according to any one of claims 1 to 7, which is folded into a continuous W shape. 請求項8に記載のエアフィルタ用濾材を用いたことを特徴とするエアフィルタユニット。   An air filter unit using the air filter medium according to claim 8.
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JP2009136863A (en) * 2007-11-14 2009-06-25 Nitto Denko Corp Filter member, its manufacturing method and filter unit
CN102100987A (en) * 2009-12-21 2011-06-22 东丽纤维研究所(中国)有限公司 Wound filter element and application thereof
JP2013032514A (en) * 2011-07-05 2013-02-14 Nitto Denko Corp Porous polytetrafluoroethylene film and air filter filtration material
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JP2009136863A (en) * 2007-11-14 2009-06-25 Nitto Denko Corp Filter member, its manufacturing method and filter unit
CN102100987A (en) * 2009-12-21 2011-06-22 东丽纤维研究所(中国)有限公司 Wound filter element and application thereof
JP2013032514A (en) * 2011-07-05 2013-02-14 Nitto Denko Corp Porous polytetrafluoroethylene film and air filter filtration material
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JP2015160198A (en) * 2014-02-28 2015-09-07 アポロトレイディング株式会社 filter
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US10537836B2 (en) 2016-03-11 2020-01-21 Daikin Industries, Ltd. Filter medium for air filter, filter pack, air filter unit and method for producing the filter medium for air filter
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WO2021117361A1 (en) * 2019-12-13 2021-06-17 住友化学株式会社 Separation membrane sheet, separation membrane element, separation membrane module, and separation device
CN113384962A (en) * 2020-03-11 2021-09-14 中国人民解放军69007部队 Novel nuclear biochemical protective smoke filter layer and preparation method and application thereof
WO2023286974A1 (en) * 2021-07-13 2023-01-19 삼성전자 주식회사 Multifunctional air purification filter, and purification device comprising same

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