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JP6964033B2 - Filter material for air filter - Google Patents
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JP6964033B2 - Filter material for air filter - Google Patents

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JP6964033B2
JP6964033B2 JP2018067456A JP2018067456A JP6964033B2 JP 6964033 B2 JP6964033 B2 JP 6964033B2 JP 2018067456 A JP2018067456 A JP 2018067456A JP 2018067456 A JP2018067456 A JP 2018067456A JP 6964033 B2 JP6964033 B2 JP 6964033B2
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filter medium
air filter
filter
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fiber diameter
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栄子 目黒
正 佐藤
智彦 楚山
希 田代
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Hokuetsu Corp
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Description

本発明は空気中の不純物を濾過するために使用される除塵エアフィルタ用濾材に関し、より詳細には、塵埃などの捕集性能に優れており、かつ、低圧力損失であるエアフィルタ用濾材に関する。 The present invention relates to a filter medium for a dust-removing air filter used for filtering impurities in the air, and more specifically, to a filter medium for an air filter which is excellent in collecting dust and the like and has a low pressure loss. ..

近年、生活環境の変化や個人レベルでの室内環境に対する関心の高まりと共に、オフィスや居住空間の空気の清浄化が求められている。空気中の浮遊塵を除去する方法として、除塵フィルタを用いる方法が一般的であり、種々の除塵エアフィルタ用濾材が存在している。それらは大きいものではビルや工場などのシステム空調に使用され、小さいものでは空気清浄機やエアコンなどで広く使用されており、それに伴いよりエネルギー消費の少ない高効率かつ低圧力損失である高フィルタ性能を有するエアフィルタ用濾材が求められている。 In recent years, with changes in the living environment and growing interest in the indoor environment at the individual level, there is a demand for cleaning the air in offices and living spaces. As a method of removing airborne dust in the air, a method using a dust removal filter is common, and various filter media for a dust removal air filter exist. Larger ones are used for system air conditioning in buildings and factories, and smaller ones are widely used in air purifiers and air conditioners. There is a demand for a filter medium for an air filter having the above.

エアフィルタ用濾材としてはその対象とする粒子径や除塵効率の違いにより粗塵用フィルタ、中性能フィルタ、HEPAフィルタ、ULPAフィルタなどに大別される。これらエアフィルタの多くは不織布状、織布状、マット状などの繊維層エアフィルタ用濾材が使用され、特に、中性能フィルタ、HEPAフィルタ、ULPAフィルタには不織布状のガラス繊維製エアフィルタ用濾材が広く用いられている。 The filter medium for an air filter is roughly classified into a coarse dust filter, a medium performance filter, a HEPA filter, a ULPA filter, and the like according to the difference in the target particle size and dust removal efficiency. Most of these air filters use filter media for fiber layer air filters such as non-woven fabric, woven fabric, and matte, and in particular, non-woven glass fiber air filter filters for medium-performance filters, HEPA filters, and ULPA filters. Is widely used.

エアフィルタ用濾材の製造方法としては、短繊維であるガラス繊維や有機繊維を湿式抄紙方法においてシート化した後、バインダー及び撥水剤を付与することによってエアフィルタ用濾材を得る方法や、溶融繊維を用いたメルトブローン法に代表される乾式方法などがある。一般的にガラス繊維は湿式抄紙法によりシート化され、濾材として形成される。 As a method for producing a filter medium for an air filter, a method of obtaining a filter medium for an air filter by sheeting short glass fibers or organic fibers into a sheet by a wet papermaking method and then applying a binder and a water repellent agent, or a molten fiber. There is a dry method represented by the melt blown method using. Generally, glass fibers are sheeted by a wet papermaking method and formed as a filter medium.

ガラス繊維を用いたエアフィルタ用濾材は、ガラス繊維特有の剛性の高さと1μm以下の細い繊維径を有する特徴から他の繊維を使用したエアフィルタと比べて、低圧力損失、高捕集効率とフィルタ性能が高い。しかし、環境負荷への低減とよりクリーンな環境空間への要求が高くなっており、さらなるエネルギー消費の少ない高効率低圧力損失である高フィルタ性能を有するエアフィルタ用濾材が求められている。 Filter media for air filters using glass fibers have lower pressure loss and higher collection efficiency than air filters using other fibers due to the characteristics of high rigidity peculiar to glass fibers and a fine fiber diameter of 1 μm or less. High filter performance. However, there is an increasing demand for a cleaner environmental space and a reduction in the environmental load, and there is a demand for a filter medium for an air filter having high filter performance with low energy consumption and high efficiency and low pressure loss.

このようなエアフィルタ用濾材として、チョップドストランドガラス繊維を55質量%未満、平均繊維径1μm未満のガラス繊維が25質量%未満、平均繊維径1μm以上のガラス繊維を40〜90質量%を配合してなるエアフィルタ用濾材が提案されている(特許文献1)。 As such a filter medium for an air filter, less than 55% by mass of chopped strand glass fiber, less than 25% by mass of glass fiber having an average fiber diameter of less than 1 μm, and 40 to 90% by mass of glass fiber having an average fiber diameter of 1 μm or more are blended. A filter medium for an air filter has been proposed (Patent Document 1).

また、1.0μm未満の小繊維径の繊維の平均繊維径が0.1μm以上0.8μm未満であり、1.0μm以上の大繊維径の繊維の平均繊維径が1.2μm以上3.0μm未満であり、前記小繊維径の繊維と大繊維径の繊維の体積比が30:70〜80:20である主捕集層を有するエアフィルタ用濾材が提案されている(特許文献2参照)。しかしながら、これらのエアフィルタ用濾材はエネルギー効率が十分でなく、捕集効率も十分ではなく、よりエネルギー消費が少なく、より高効率で低圧力損失であるエアフィルタ用濾材への需要は依然として存在する。 Further, the average fiber diameter of fibers having a small fiber diameter of less than 1.0 μm is 0.1 μm or more and less than 0.8 μm, and the average fiber diameter of fibers having a large fiber diameter of 1.0 μm or more is 1.2 μm or more and 3.0 μm. A filter medium for an air filter having a main collection layer having a volume ratio of less than 30:70 to 80:20 between the fibers having a small fiber diameter and the fibers having a large fiber diameter has been proposed (see Patent Document 2). .. However, these air filter filter media are not sufficiently energy efficient, have insufficient collection efficiency, consume less energy, are more efficient and have low pressure loss, and there is still a demand for air filter filter media. ..

特表2012−518527号公報Special Table 2012-518527 Gazette 特開2017−35684号公報Japanese Unexamined Patent Publication No. 2017-35684

本発明は、よりエネルギー消費が少なく、高効率で低圧力損失であるエアフィルタ用濾材を提供する。 The present invention provides a filter medium for an air filter that consumes less energy, is highly efficient, and has a low pressure loss.

上記課題を解決するため鋭意検討した結果、チョップドストランドガラス繊維と、極細ガラス繊維からなるエアフィルタ濾材であり、前記ガラス繊維の繊維径分布を規定されたエアフィルタ濾材により上記課題を解決できることが判明した。 As a result of diligent studies to solve the above problem, it was found that the air filter filter medium is composed of chopped strand glass fiber and ultrafine glass fiber, and the above problem can be solved by the air filter filter medium in which the fiber diameter distribution of the glass fiber is defined. bottom.

すなわち、本発明のエアフィルタ用濾材は、ガラス繊維を主体とするエアフィルタ用濾材であり、前記ガラス繊維が、チョップドストランドガラス繊維および極細ガラス繊維を含有しており、前記エアフィルタ用濾材の繊維径分布において、1.5μmより大きく2.9μm以下の範囲の累積頻度が2〜15%であることを特徴とする。 That is, the filter medium for an air filter of the present invention is a filter medium for an air filter mainly composed of glass fibers, and the glass fibers contain chopped strand glass fibers and ultrafine glass fibers, and the fibers of the filter medium for the air filter. In the diameter distribution, the cumulative frequency in the range larger than 1.5 μm and 2.9 μm or less is 2 to 15%.

また、本発明のエアフィルタ用濾材は、対象粒子径0.3μm、面風速5.3cm/sec(秒)における、数1の式により示されるPF値が13.5以上であってもよい。本発明におけるPF値は、0.3μm単分散のPAO(ポリアルファオレフィン)透過率を測定し、下記の式に基づいて算出する。 Further, the filter medium for an air filter of the present invention may have a PF value of 13.5 or more represented by the formula of Equation 1 at a target particle size of 0.3 μm and a surface wind speed of 5.3 cm / sec (sec). The PF value in the present invention is calculated based on the following formula by measuring the PAO (polyalphaolefin) transmittance of a 0.3 μm monodisperse.

Figure 0006964033
Figure 0006964033

本発明によれば、エネルギー消費が少なく、高効率で低圧力損失であるエアフィルタ用濾材を提供することが可能となる。 According to the present invention, it is possible to provide a filter medium for an air filter having low energy consumption, high efficiency and low pressure loss.

本発明のエアフィルタ用濾材には、ガラス繊維として、チョップドストランドガラス繊維と、極細ガラス繊維とを含有させる。チョップドストランドガラス繊維とは、紡糸ノズルから引き出された平均繊維径数μmから数十μmのガラス短繊維を束にした繊維束を、1.5mmから25mm程度の長さに揃えたガラス繊維をいう。また、極細ガラス繊維とは、火焔延伸法やロータリー法で製造される平均繊維径6.0μm以下のウール状のガラス繊維をいう。チョップドストランドガラス繊維と、極細ガラス繊維とを併用することによって粒子捕集に必要な細い繊維と空隙を維持し、また、ユニット加工時に必要な濾材の剛性を有することができる。チョップドストランドガラス繊維と、極細ガラス繊維との配合比率は特に限定するものではないが、質量(重量)比率で、チョップドストランドガラス繊維:極細ガラス繊維=10:90〜50:50とすることが好ましい。チョプドストランドガラス繊維の質量比が50より多くなると繊維どうしの絡みが少なくなるため強度の低下を起こしやすくなる。例えば、全ガラス繊維に対して、極細ガラス繊維を50〜90質量%、好ましくは、50〜80質量%含み、チョップドストランドガラス繊維を10〜50質量%、好ましくは20〜50質量%含むガラス繊維を原材料のガラス繊維として使用することが好ましい。 The filter medium for an air filter of the present invention contains chopped strand glass fibers and ultrafine glass fibers as glass fibers. The chopped strand glass fiber refers to a glass fiber obtained by aligning a bundle of short glass fibers with an average fiber diameter of several μm to several tens of μm drawn from a spinning nozzle to a length of about 1.5 mm to 25 mm. .. The ultrafine glass fiber refers to a wool-like glass fiber having an average fiber diameter of 6.0 μm or less produced by a flame stretching method or a rotary method. By using the chopped strand glass fiber and the ultrafine glass fiber in combination, it is possible to maintain the fine fibers and voids required for particle collection, and to have the rigidity of the filter medium required for unit processing. The blending ratio of the chopped strand glass fiber and the ultrafine glass fiber is not particularly limited, but the mass (weight) ratio is preferably chopped strand glass fiber: ultrafine glass fiber = 10: 90 to 50:50. .. When the mass ratio of the chopped strand glass fibers is more than 50, the entanglement between the fibers is reduced, so that the strength is likely to decrease. For example, glass fibers containing 50 to 90% by mass, preferably 50 to 80% by mass, and chopped strand glass fibers in an amount of 10 to 50% by mass, preferably 20 to 50% by mass, based on the total glass fibers. Is preferably used as the raw material glass fiber.

ガラス繊維の種類としては、特に限定はしないがボロンを嫌う半導体工場用途などではボロン含有量の少ないローボロンガラス繊維使用しても差し支えない。 The type of glass fiber is not particularly limited, but low boron glass fiber having a low boron content may be used in semiconductor factory applications where boron is disliked.

本発明のエアフィルタ用濾材には、ガラス繊維以外の副資材を含有させることができる。このような副資材としては、天然繊維や合成樹脂からなるバインダー繊維がある。また、合成樹脂を含有させてもよい。特に、濾材への強度付与のために、バインダー繊維や非繊維状の合成樹脂バインダーを含有させることが好ましい。バインダー繊維とは、例えば、ポリエチレン繊維、変性ポリエステル繊維、芯鞘合成繊維、ポリビニルアルコール繊維などであり、これらを単独又は2種以上併用できる。バインダー繊維の含有量は、特に限定するものではないが、ガラス繊維100質量部に対して0〜20部とすることが好ましい。また、非繊維状の合成樹脂バインダーとしては、例えば、アクリル系ラテックス、NBR系ラテックス、酢ビ系ラテックス、オレフィン系ラテックス、ポリビニルアルコール系ラテックスであり、単独又は2種類以上を併用できる。合成樹脂バインダーの含有量は、特に限定するものではないが、ガラス繊維100質量部に対して2〜10部とすることが好ましい。本発明で使用される非繊維状のバインダー樹脂は、ガラス繊維同士を接着し、強度を付与することのできるポリマーから選択されればよく、水又は有機溶媒に溶解又は分散された状態で、ガラス繊維に付与されても良い。また、製造工程において、ガラス繊維を離解させる際に混合してもよい。または、合成樹脂バインダーは、濾材(湿紙シート)に対して塗布や噴霧することで付与することができる。また、必要に応じて、十分な強度が得られる範囲内で、耐水化剤、界面活性剤、消泡剤、pH調整剤等の薬剤を添加することができる。 The filter medium for an air filter of the present invention may contain an auxiliary material other than glass fiber. Such auxiliary materials include binder fibers made of natural fibers and synthetic resins. Moreover, you may contain synthetic resin. In particular, it is preferable to contain a binder fiber or a non-fibrous synthetic resin binder in order to impart strength to the filter medium. The binder fiber is, for example, polyethylene fiber, modified polyester fiber, core-sheath synthetic fiber, polyvinyl alcohol fiber, or the like, and these can be used alone or in combination of two or more. The content of the binder fiber is not particularly limited, but is preferably 0 to 20 parts with respect to 100 parts by mass of the glass fiber. The non-fibrous synthetic resin binder is, for example, acrylic latex, NBR latex, vinyl acetate latex, olefin latex, or polyvinyl alcohol latex, and can be used alone or in combination of two or more. The content of the synthetic resin binder is not particularly limited, but is preferably 2 to 10 parts with respect to 100 parts by mass of the glass fiber. The non-fibrous binder resin used in the present invention may be selected from a polymer capable of adhering glass fibers to each other and imparting strength, and the glass is dissolved or dispersed in water or an organic solvent. It may be given to the fiber. Further, in the manufacturing process, the glass fibers may be mixed when they are dissociated. Alternatively, the synthetic resin binder can be applied by applying or spraying the filter medium (wet paper sheet). Further, if necessary, chemicals such as a water resistant agent, a surfactant, an antifoaming agent, and a pH adjuster can be added within a range in which sufficient strength can be obtained.

本発明のエアフィルタ用濾材には、更に、撥水剤を含有させてもよい。撥水剤としては、特に限定するものではないが、例えば、シリコン系、フッ素系、パラフィンワックス系などの撥水剤が挙げられる。 The filter medium for an air filter of the present invention may further contain a water repellent. The water repellent is not particularly limited, and examples thereof include water repellents such as silicon-based, fluorine-based, and paraffin wax-based.

本発明のエアフィルタ用濾材の製造方法は、特に限定するものではないが、ガラス繊維を水中に分散したスラリーを用いて湿式抄紙法によりシート化し、乾燥させることで得ることができる。湿式抄紙法に用いる抄紙機は、特に限定するものではなく、長網式抄紙機、短網式抄紙機、円網式抄紙機、傾斜ワイヤ式抄紙機、ギャップフォーマ、デルタフォーマを用いることができる。乾燥方法についても特に限定するものではなく、熱風方式、赤外線方式、ヤンキードライヤーや多筒式ドライヤーなど様々な方法が利用できる。 The method for producing the filter medium for an air filter of the present invention is not particularly limited, but it can be obtained by forming a sheet by a wet papermaking method using a slurry in which glass fibers are dispersed in water and drying it. The paper machine used in the wet paper making method is not particularly limited, and a long net type paper machine, a short net type paper machine, a circular net type paper machine, an inclined wire type paper machine, a gap former, and a delta former can be used. .. The drying method is not particularly limited, and various methods such as a hot air method, an infrared method, a Yankee dryer, and a multi-cylinder dryer can be used.

本発明のエアフィルタ用濾材は、ガラス繊維の繊維径分布において、1.5μmより大きく2.9μm以下の範囲内での累積頻度が2〜15%である。より好ましくは3〜12%である。ここでエアフィルタ用濾材の繊維径分布とは、エアフィルタ用濾材において、抄紙流れ方向(以降MD方向と表記する)に対して垂直方向(以下CD方向と表記する)に切断した際の濾材断面から算出した繊維径についての個数基準での頻度分布いう。 The filter medium for an air filter of the present invention has a cumulative frequency of 2 to 15% within a range of more than 1.5 μm and 2.9 μm or less in the fiber diameter distribution of glass fibers. More preferably, it is 3 to 12%. Here, the fiber diameter distribution of the air filter filter medium is the cross section of the filter medium when the air filter filter medium is cut in the direction perpendicular to the papermaking flow direction (hereinafter referred to as the MD direction) (hereinafter referred to as the CD direction). It is the frequency distribution based on the number of fibers calculated from.

エアフィルタ用濾材の繊維径分布の測定方法としては、CD方向に切断した濾材断面の電子顕微鏡写真等を用いて計測を行う。その時の倍率については特に限定はしないが、3000倍以上が望ましく、また、エアフィルタ用濾材に使用されている全繊維の繊維径が同じ倍率で計測できることが望ましい。 As a method for measuring the fiber diameter distribution of the filter medium for an air filter, measurement is performed using an electron micrograph or the like of a cross section of the filter medium cut in the CD direction. The magnification at that time is not particularly limited, but it is desirable that it is 3000 times or more, and it is desirable that the fiber diameters of all the fibers used in the filter medium for the air filter can be measured at the same magnification.

上記濾材断面から確認できるガラス繊維の断面が楕円の場合はその短径を繊維径とする。上記濾材断面の厚さ方向は濾材表面から濾材裏面までの全濾材厚さの電子顕微鏡写真を撮影し、そのときの繊維径(Di)を測定する。また、全測定繊維径数は400以上とする。全測定繊維径が400未満の場合は、さらに一列全濾材厚さの電子顕微鏡写真を撮影し繊維径を測定する。上記方法により計測した繊維径を0.1μmから階級を0.2μm刻みとして各繊維径の本数(Ni)を算出し以下の計算方法により繊維径分布率を算出する。
繊維径:Di(μm)
繊維本数:Ni(本)
When the cross section of the glass fiber that can be confirmed from the cross section of the filter medium is elliptical, its minor axis is defined as the fiber diameter. In the thickness direction of the cross section of the filter medium, an electron micrograph of the total thickness of the filter medium from the surface of the filter medium to the back surface of the filter medium is taken, and the fiber diameter (Di) at that time is measured. The total number of measured fibers is 400 or more. If the total measured fiber diameter is less than 400, an electron micrograph of the total filter medium thickness in a row is further taken to measure the fiber diameter. The number of fibers (Ni) of each fiber diameter is calculated from the fiber diameter measured by the above method in increments of 0.2 μm from 0.1 μm, and the fiber diameter distribution ratio is calculated by the following calculation method.
Fiber diameter: Di (μm)
Number of fibers: Ni (pieces)

Figure 0006964033
Figure 0006964033

上記計算方法による繊維径分布において1.5μmより大きく2.9μm以下の範囲の累積頻度が2〜15%の範囲であるとフィルタ性能の指標であるPF値が向上することが判明した。理由については定かではないが、繊維径分布における1.5μmより大きく2.9μm以下の範囲の累積頻度が15%より大きくなると捕集効率に有効とはならないアスペクト比が小さい超微細な繊維が濾材中に留まり易くなり、濾材中の空隙を塞ぎ、圧力損失をだけを高くしてしまうと推定している。また、1.5μmより大きく2.9μm以下の範囲の累積頻度が2%未満であると捕集効率に有効となる極細ガラス繊維が濾材中への留まり難くなり、捕集効率を下げてしまうと推定する。さらに、好ましくは本発明のエアフィルタ用濾材は、対象粒子径0.3μm、面風速5.3cm/sec(秒)における、数1の式により示されるPF値が13.5以上、好ましくは14.0以上であってもよい。PF値が高いほど、同一圧力損失で高捕集効率を示す。 In the fiber diameter distribution by the above calculation method, it was found that the PF value, which is an index of filter performance, is improved when the cumulative frequency in the range larger than 1.5 μm and 2.9 μm or less is in the range of 2 to 15%. Although the reason is not clear, if the cumulative frequency in the fiber diameter distribution larger than 1.5 μm and 2.9 μm or less is greater than 15%, it will not be effective for collection efficiency. Ultra-fine fibers with a small aspect ratio are used as filter media. It is estimated that it becomes easier to stay inside, closes the voids in the filter medium, and increases only the pressure loss. Further, if the cumulative frequency in the range larger than 1.5 μm and 2.9 μm or less is less than 2%, the ultrafine glass fibers effective for the collection efficiency become difficult to stay in the filter medium, and the collection efficiency is lowered. presume. Further, preferably, the filter medium for an air filter of the present invention has a PF value of 13.5 or more, preferably 14 at a target particle size of 0.3 μm and a surface wind speed of 5.3 cm / sec (sec). It may be 0.0 or more. The higher the PF value, the higher the collection efficiency with the same pressure loss.

Figure 0006964033
Figure 0006964033

エアフィルタ用濾材の繊維径分布における1.5μmより大きく2.9μm以下の範囲の累積頻度を2〜15%の範囲とするためには、原材料として、平均繊維径が1.5〜2.9μmのガラス繊維の配合率を小さくすることが好ましい。具体的には、原料に使用するガラス繊維として、平均繊維径が1.5〜2.9μmの極細ガラス繊維の添加量を、全ガラス繊維のうち10質量%未満、好ましくは5質量%未満とすることが好ましい。ただし、本発明のエアフィルタ用濾材は、太径のチョップドストランドガラス繊維と、細径の極細ガラス繊維との両方を用いるため、特に湿式抄紙では太径のチョップドストランドガラス繊維に比べて細径の極細ガラス繊維の歩留まりが悪い。そして、配合する極細ガラス繊維の歩留りは配合する繊維径と配合率により変化するため、原材料段階での混合比率と、エアフィルタ用濾材段階での繊維径分布率とは一致しない。また、極細ガラス繊維は製造方法由来によりブロードな繊維径分布を持つため、平均繊維径が1.5〜2.9μmのガラス繊維を混合しなくとも1.5より大きく2.9μm以下の範囲に含まれる階級の累積頻度が15%以上となることもある。また、平均繊維径が1.0μ未満の極細ガラス繊維と平均繊維径が6.0μmより大きいチョップドストランドガラス繊維のように極端な繊維径を組み合わせた場合は1.5μmより大きく2.9μm以下の範囲の累積頻度が2.0%未満となることもある。エアフィルタ用濾材のPF値を高くするためにはエアフィルタ用濾材中の繊維径分布が重要となる。このような特定の繊維径分布を有するエアフィルタ用濾材を得るためには、上記に加えて、原材料として使用するガラス繊維の平均繊維径を特定のものとすれば良い。例えば、1.5μm〜2.9μmの平均繊維径を有する極細ガラス繊維の使用を一定の範囲に抑えればよい。例えば、1.5μm〜2.9μmの平均繊維径を有する極細ガラス繊維を濾材の原材料中において、5〜15質量%、5〜12質量%、さらに、0〜15質量%未満、0〜12質量%、さらに0〜5質量%、0質量%とすることが好ましい。さらに、例えば、2.9μmより大きく6.0μm以下の平均繊維径を有する極細ガラス繊維を一定量使用すればよい。例えば2.9μより大きく6.0μm以下の平均繊維径を有する極細ガラス繊維を濾材の原材料中において、20〜70質量%、さらに、50〜70質量%とすることが好ましい。さらに、6.0μmより大きい平均繊維径を有するチョップドストランドガラス繊維を一定量使用すればよい。例えば、6.0μmより大きい平均繊維径を有するチョップドストランドガラス繊維を濾材の原材料中において、20〜50質量%とすることが好ましい。さらに、例えば、6.0μmより大きい平均繊維径を有するチョップドストランドガラス繊維を濾材の原材料中において、20〜40質量%とすることが好ましい。また、1.5μm未満の平均繊維径を有する極細ガラス繊維を一定量使用すればよい。例えば1.5μm未満の平均繊維径を有する極細ガラス繊維を濾材の原材料中において、3〜50質量%、さらに、4〜30質量%とすることが好ましい。したがって、本発明のエアフィルタ用濾材の製造方法においては、上記組成を有するガラス繊維を原材料として使用することが好ましい。例えば、本発明のエアフィルタ用濾材の製造方法においては、特定の平均繊維径を有する少なくとも一種以上のチョップドストランドガラス繊維と特定の平均繊維径を有する少なくとも一種以上の極細ガラス繊維とを上記に示す割合で配合し、パルパーにてpH2〜4の硫酸などを含む酸性の水を用いて、離解後、抄紙し、手抄装置にて抄紙し湿紙を得る。その後、次に、例えば、アクリル系ラテックスなどの非繊維状の合成樹脂バインダー、とフッ素系撥水剤などの撥水剤、アセチレン系界面活性剤などの界面活性剤を含むバインダー液を用いて湿紙をバインダー液に含浸してエアフィルタ用濾材を作製すればよい。 In order to set the cumulative frequency in the range of 2.9 μm or more, which is larger than 1.5 μm in the fiber diameter distribution of the filter medium for air filters, to the range of 2 to 15%, the average fiber diameter is 1.5 to 2.9 μm as a raw material. It is preferable to reduce the blending ratio of the glass fiber of. Specifically, as the glass fiber used as a raw material, the amount of ultrafine glass fiber having an average fiber diameter of 1.5 to 2.9 μm is set to less than 10% by mass, preferably less than 5% by mass, of all the glass fibers. It is preferable to do so. However, since the filter medium for an air filter of the present invention uses both a large-diameter chopped strand glass fiber and a small-diameter ultrafine glass fiber, the diameter is smaller than that of the large-diameter chopped strand glass fiber especially in wet papermaking. The yield of ultrafine glass fiber is poor. Since the yield of the ultrafine glass fibers to be blended changes depending on the fiber diameter and the blending ratio to be blended, the mixing ratio at the raw material stage and the fiber diameter distribution ratio at the filter medium stage for the air filter do not match. In addition, since ultrafine glass fibers have a broad fiber diameter distribution due to the origin of the manufacturing method, the average fiber diameter is in the range of 2.9 μm or more, which is larger than 1.5 even if glass fibers having an average fiber diameter of 1.5 to 2.9 μm are not mixed. The cumulative frequency of the included classes may be 15% or more. The average fiber diameter of from greater 2.9μm than 1.5μm when the average fiber diameter and ultrafine glass fiber of less than 1.0 micron m is a combination of extreme fiber diameter as 6.0μm greater than chopped strand glass fibers The cumulative frequency of the range may be less than 2.0%. In order to increase the PF value of the air filter filter medium, the fiber diameter distribution in the air filter filter medium is important. In order to obtain a filter medium for an air filter having such a specific fiber diameter distribution, in addition to the above, the average fiber diameter of the glass fiber used as a raw material may be specified. For example, the use of ultrafine glass fibers having an average fiber diameter of 1.5 μm to 2.9 μm may be suppressed within a certain range. For example, ultrafine glass fibers having an average fiber diameter of 1.5 μm to 2.9 μm are used in the raw material of the filter medium in an amount of 5 to 15% by mass, 5 to 12% by mass, and further, less than 0 to 15% by mass, 0 to 12% by mass. %, Further preferably 0 to 5% by mass and 0% by mass. Further, for example, a certain amount of ultrafine glass fibers having an average fiber diameter larger than 2.9 μm and 6.0 μm or less may be used. For example, it is preferable that the ultrafine glass fiber having an average fiber diameter of more than 2.9 μm and 6.0 μm or less is 20 to 70% by mass, more preferably 50 to 70% by mass in the raw material of the filter medium. Further, a certain amount of chopped strand glass fiber having an average fiber diameter larger than 6.0 μm may be used. For example, it is preferable that the chopped strand glass fiber having an average fiber diameter larger than 6.0 μm is 20 to 50% by mass in the raw material of the filter medium. Further, for example, it is preferable that the chopped strand glass fiber having an average fiber diameter larger than 6.0 μm is 20 to 40% by mass in the raw material of the filter medium. Further, a certain amount of ultrafine glass fibers having an average fiber diameter of less than 1.5 μm may be used. For example, it is preferable that the ultrafine glass fiber having an average fiber diameter of less than 1.5 μm is 3 to 50% by mass and further 4 to 30% by mass in the raw material of the filter medium. Therefore, in the method for producing a filter medium for an air filter of the present invention, it is preferable to use glass fiber having the above composition as a raw material. For example, in the method for producing a filter medium for an air filter of the present invention, at least one or more chopped strand glass fibers having a specific average fiber diameter and at least one or more ultrafine glass fibers having a specific average fiber diameter are shown above. It is blended in a ratio, and after decoupling with acidic water containing sulfuric acid or the like having a pH of 2 to 4 with a pulper, paper is made and paper is made with a hand paper making device to obtain wet paper. Then, for example, a binder liquid containing a non-fibrous synthetic resin binder such as acrylic latex, a water repellent such as a fluorine-based water repellent, and a surfactant such as an acetylene-based surfactant is used for moistening. Paper may be impregnated with a binder solution to prepare a filter medium for an air filter.

以下に、実施例、比較例によって本発明をさらに詳しく説明する。ただし、本発明はこれら実施例により何ら限定されるものではない。 Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples. However, the present invention is not limited to these examples.

チョップドストランドガラス繊維と極細ガラス繊維とを表1に示す割合で配合し、パルパーにてpH3.0の硫酸酸性の水を用いて、濃度0.5質量%で離解後、抄紙し、手抄装置にて抄紙し湿紙を得た。次に、バインダー液組成がアクリル系ラテックス(商品名:ボンコートAN−155、製造元:大日本インキ化学工業(株))とフッ素系撥水剤(商品名:NK−ガードN−07、製造元:日華化学(株))とアセチレン系界面活性剤(商品名:ダイノール604 製造会社:日信化学工業(株))を固形分比100/20/2となる様に混合したバインダー液を用いて湿紙をバインダー液に含浸し、130℃のロータリードライヤーにて乾燥して各実施例及び比較例のエアフィルタ用濾材を作製した。全バインダー分の濾材中の含有量が実施例3、9及び12を除き5.0質量%であり、実施例3、9及び12においては6.0質量%であった。なお、チョップドストランドガラス繊維と極細ガラス繊維との配合割合は、例えば、実施例1であれば、極細ガラス繊維として、平均繊維径が0.59μmのものを11部、平均繊維径が2.3μmのものを10部、平均繊維径が4.0μmのものを54部と、チョップドストランドガラス繊維として平均繊維径が6.3μmのものを25部配合したことを示している。また、実施例3、9及び12については、チョップドストランドガラス繊維と極細ガラス繊維とをパルパーで離解する際に、PVAバインダー(粒子状)1部を配合した。尚、PVAバインダーは、エアフィルタ用濾材を作製する経過で溶ける(水分を含んだ後、加熱により溶融する)ため、繊維径分布の算出において、エアフィルタ用濾材を構成する繊維としてはカウントされない。 Chopped strand glass fiber and ultrafine glass fiber are mixed in the ratio shown in Table 1, and after disintegration at a concentration of 0.5% by mass using sulfuric acid-acidic water with a pH of 3.0 in a pulper, papermaking is performed and a hand-paper machine is used. Paper was made at the site to obtain wet paper. Next, the binder liquid composition is acrylic latex (trade name: Boncoat AN-155, manufacturer: Dainippon Ink and Chemicals Co., Ltd.) and fluorine-based water repellent (trade name: NK-Guard N-07, manufacturer: Japan). Hua Chemical Co., Ltd.) and acetylene-based surfactant (trade name: Dynol 604, manufacturing company: Nissin Chemical Industry Co., Ltd.) mixed with a binder solution so as to have a solid content ratio of 100/20/2. Paper was impregnated with a binder solution and dried with a rotary dryer at 130 ° C. to prepare filter media for air filters of each Example and Comparative Example. The content of all the binders in the filter medium was 5.0% by mass except for Examples 3, 9 and 12, and was 6.0% by mass in Examples 3, 9 and 12. The blending ratio of the chopped strand glass fiber and the ultrafine glass fiber is, for example, in Example 1, 11 parts of the ultrafine glass fiber having an average fiber diameter of 0.59 μm and an average fiber diameter of 2.3 μm. It shows that 10 parts of the fiberglass, 54 parts of the fiberglass having an average fiber diameter of 4.0 μm, and 25 parts of the chopped strand glass fiber having an average fiber diameter of 6.3 μm were blended. Further, in Examples 3, 9 and 12, when the chopped strand glass fiber and the ultrafine glass fiber were dissociated with a pulper, one part of a PVA binder (particulate) was blended. Since the PVA binder melts in the process of producing the filter medium for the air filter (it is melted by heating after containing water), it is not counted as a fiber constituting the filter medium for the air filter in the calculation of the fiber diameter distribution.

(試験方法)
(1)圧力損失
有効面積100cmのエアフィルタ用濾材、空気を面風速5.3cm/secで通風した時の差圧を微差圧計で測定した。
(Test method)
(1) Pressure loss A filter medium for an air filter having an effective area of 100 cm 2 and a differential pressure when air was ventilated at a surface wind speed of 5.3 cm / sec were measured with a micro differential pressure gauge.

(2)PAO透過率
ラスキンノズルで発生させた多分散PAO(ポリアルファオレフィン)粒子を含む空気を、有効面積100cmのエアフィルタ用濾材に、面風速5.3cm/secで通風した時のPAOの捕集効率を、リオン社製レーザーパーティクルカウンターを使用し測定した。なお、測定対象粒子径0.3μm単分散は粒子径0.2〜0.3μmと0.3〜0.4μmのPAO透過率の幾何平均を0.3μm単分散の透過率とした。PAO捕集効率は、100−(PAO透過率)の式から求めた。また、上流側のPAO発生濃度は、0.1μm以下で約1×10個/ftとした。
(2) PAO transmittance PAO when air containing polydisperse PAO (polyalphaolefin) particles generated by a Ruskin nozzle is ventilated through a filter medium for an air filter having an effective area of 100 cm 2 at a surface wind speed of 5.3 cm / sec. The collection efficiency of the particles was measured using a laser particle counter manufactured by Rion. For the particle size of 0.3 μm monodisperse to be measured, the geometric mean of the PAO transmittances of 0.2 to 0.3 μm and 0.3 to 0.4 μm was taken as the transmittance of 0.3 μm monodisperse. The PAO collection efficiency was determined from the formula of 100- (PAO transmittance). The PAO generation concentration on the upstream side was about 1 × 10 9 / ft 3 at 0.1 μm or less.

(3)PF値
濾紙のフィルタ性能の指標となるPF値は、(1)と(2)の測定に基づき、次式より求めた。PF値が高いほど、同一圧力損失で高捕集効率を示す。
(3) PF value The PF value, which is an index of the filter performance of the filter paper, was obtained from the following equation based on the measurements of (1) and (2). The higher the PF value, the higher the collection efficiency with the same pressure loss.

Figure 0006964033
Figure 0006964033

(濾材における繊維径分布)
電界放出型走査電子顕微鏡写真よりエアフィルタ用濾材をCD方向に切断した濾材断面写真から像解析ソフト(A像くん;旭化成エンジニアリング(株))「粒子解析」の手法を用いて繊維径を測定した。繊維断面の径は短径を繊維径(Di)とした。上記方法により計測した繊維径を0.1μmから階級を0.2μm刻みとして各繊維径の本数(Ni)を算出し以下の計算方法により繊維径頻度分布率を算出し、表2に示した。(表2中左端欄、例えば「0.1」の記載は「0.1μmより大きく0.3μm以下」を意味する。「0.3」以降も同様である。)また、1.5μmより大きく2.9μm以下の範囲の累積頻度(表2中1.5−2.9累積と示す)を算出し、表1および表2に示した。
繊維径:Di(μm)
繊維本数:Ni(本)
(Fiber diameter distribution in filter media)
From the field emission scanning electron micrograph, the fiber diameter was measured from the cross-sectional photograph of the filter medium for the air filter cut in the CD direction using the method of image analysis software (A image-kun; Asahi Kasei Engineering Co., Ltd.) "Particle analysis". .. As for the diameter of the fiber cross section, the minor diameter was defined as the fiber diameter (Di). The number of fibers (Ni) of each fiber diameter was calculated from the fiber diameter measured by the above method in increments of 0.2 μm from 0.1 μm, and the fiber diameter frequency distribution rate was calculated by the following calculation method, and is shown in Table 2. (In the leftmost column in Table 2 , for example, the description of "0.1" means "greater than 0.1 μm and 0.3 μm or less". The same applies to "0.3" and later.) Also, larger than 1.5 μm. The cumulative frequency in the range of 2.9 μm or less (indicated as 1.5-2.9 cumulative in Table 2) was calculated and shown in Tables 1 and 2.
Fiber diameter: Di (μm)
Number of fibers: Ni (pieces)

Figure 0006964033
Figure 0006964033

(ガラス繊維の平均繊維径)
電界放出型走査電子顕微鏡写真よりガラス繊維をCD方向に切断した断面写真から像解析ソフト(A像くん;旭化成エンジニアリング(株))「粒子解析」の手法を用いて原材料のガラス繊維の平均繊維径を測定した。繊維断面の径は短径を繊維径(Dgi)とした。上記方法により計測した繊維径を以下の計算方法によりガラス繊維の平均繊維径を算出した。計測する繊維本数(Ng)は200本以上とした。
繊維径:Dgi(μm)
繊維本数:Ng(本)
(Average fiber diameter of glass fiber)
Image analysis software (A image-kun; Asahi Kasei Engineering Co., Ltd.) Using the method of "particle analysis" from a cross-sectional photograph of glass fibers cut in the CD direction from a field emission scanning electron micrograph, the average fiber diameter of the glass fiber as a raw material Was measured. As for the diameter of the fiber cross section, the minor diameter was defined as the fiber diameter (Dgi). The average fiber diameter of the glass fiber was calculated by the following calculation method for the fiber diameter measured by the above method. The number of fibers (Ng) to be measured was 200 or more.
Fiber diameter: Dgi (μm)
Number of fibers: Ng (pieces)

Figure 0006964033
Figure 0006964033

Figure 0006964033
Figure 0006964033

Figure 0006964033
Figure 0006964033

実施例1〜13と比較例1〜4のPF値を比較すると繊維径分布において1.5μmより大きく2.9μm以下の範囲の累積頻度が2〜15%である実施例1〜13ではPF値が13.5以上と高い結果であった。それに対し同範囲の累積頻度が15%より多い比較例1〜3と、同範囲の累積頻度が2%未満である比較例4ではPF値が12.2〜13.0と低い結果であった。 Comparing the PF values of Examples 1 to 13 and Comparative Examples 1 to 4, the PF values of Examples 1 to 13 have a cumulative frequency of 2 to 15% in the range of 2.9 μm or less, which is larger than 1.5 μm in the fiber diameter distribution. Was a high result of 13.5 or more. On the other hand, in Comparative Examples 1 to 3 in which the cumulative frequency in the same range was more than 15%, and in Comparative Example 4 in which the cumulative frequency in the same range was less than 2%, the PF value was as low as 12.2 to 13.0. ..

Claims (7)

ガラス繊維を主体とするエアフィルタ用濾材であり、前記ガラス繊維がチョップドストランドガラス繊維及び6.0μm以下の平均繊維径を有する極細ガラス繊維を含有しており、かつ、前記エアフィルタ用濾材の繊維径分布において、1.5μmより大きく2.9μm以下の範囲の累積頻度が2〜15%であり、圧力損失が15〜100Paであり、ガラス繊維100質量部に対して合成樹脂バインダーを2〜10部含有することを特徴とする前記エアフィルタ用濾材。 It is a filter medium for an air filter mainly composed of glass fibers, and the glass fibers contain chopped strand glass fibers and ultrafine glass fibers having an average fiber diameter of 6.0 μm or less, and the fibers of the filter medium for the air filter. In the diameter distribution, the cumulative frequency in the range larger than 1.5 μm and 2.9 μm or less is 2 to 15%, the pressure loss is 15 to 100 Pa , and 2 to 2 to 100 parts by mass of the glass fiber. The filter medium for an air filter, which comprises 10 parts. 対象粒子径0.3μm、面風速5.3cm/secにおける、数1の式により示されるPF値が13.5以上であることを特徴とする、請求項1に記載のエアフィルタ用濾材。
Figure 0006964033
The filter medium for an air filter according to claim 1, wherein the PF value represented by the formula of Equation 1 is 13.5 or more at a target particle size of 0.3 μm and a surface wind speed of 5.3 cm / sec.
Figure 0006964033
合成樹脂バインダーがアクリル系ラテックス、NBR系ラテックス、酢ビ系ラテックス、オレフィン系ラテックス、および/または、ポリビニルアルコール系ラテックスである、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 synthetic resin binder is an acrylic latex, an NBR latex, a vinyl acetate latex, an olefin latex, and / or a polyvinyl alcohol latex. 請求項1〜のいずれか一つに記載のエアフィルタ用濾材を製造するための方法であって、
2.9μより大きく6.0μm以下の平均繊維径を有する極細ガラス繊維を原材料中において20〜70質量%含み、
6.0μmより大きい平均繊維径を有するチョップドストランドガラス繊維を原材料中において20〜50質量%含む原材料を配合し、抄紙し、湿紙を得たのち、合成樹脂バインダーを含むバインダー液に前記湿紙を含浸することを特徴とする、前記製造方法。
The method for manufacturing the filter medium for an air filter according to any one of claims 1 to 3.
The raw material contains 20 to 70% by mass of ultrafine glass fibers having an average fiber diameter of more than 2.9 μm and 6.0 μm or less.
A raw material containing 20 to 50% by mass of chopped strand glass fiber having an average fiber diameter larger than 6.0 μm is blended in the raw material, papermaking is performed to obtain a wet paper, and then the wet paper is added to a binder solution containing a synthetic resin binder. The production method, which comprises impregnating the above-mentioned production method.
前記原材料中に、1.5μm〜2.9μmの平均繊維径を有する極細ガラス繊維を原材料中において0〜12質量%含むことを特徴とする請求項に記載のエアフィルタ用濾材の製造方法。 The method for producing an air filter filter medium according to claim 4 , wherein the raw material contains 0 to 12% by mass of ultrafine glass fibers having an average fiber diameter of 1.5 μm to 2.9 μm in the raw material. 前記原材料中に、1.5μm未満の平均繊維径を有する極細ガラス繊維を原材料中において3〜50質量%含むことを特徴とする請求項4または5に記載のエアフィルタ用濾材の製造方法。 The method for producing an air filter filter medium according to claim 4 or 5 , wherein the raw material contains 3 to 50% by mass of ultrafine glass fibers having an average fiber diameter of less than 1.5 μm in the raw material. 全ガラス繊維に対して50〜80質量%の極細ガラス繊維および20〜50質量%のチョップドストランドガラス繊維を含むガラス繊維を原材料として使用することを特徴とする、請求項4〜6のいずれか一つに記載のエアフィルタ用濾材の製造方法。 Any one of claims 4 to 6 , wherein a glass fiber containing 50 to 80% by mass of ultrafine glass fiber and 20 to 50% by mass of chopped strand glass fiber with respect to the total glass fiber is used as a raw material. The method for manufacturing a filter medium for an air filter according to the above.
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