JP2023137062A - Filter medium for measure against salt damage, and pleat type filter - Google Patents

Filter medium for measure against salt damage, and pleat type filter Download PDF

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JP2023137062A
JP2023137062A JP2022043061A JP2022043061A JP2023137062A JP 2023137062 A JP2023137062 A JP 2023137062A JP 2022043061 A JP2022043061 A JP 2022043061A JP 2022043061 A JP2022043061 A JP 2022043061A JP 2023137062 A JP2023137062 A JP 2023137062A
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filter medium
melt
fiber layer
salt damage
nonwoven fabric
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誠 井上
Makoto Inoue
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Toyobo MC Corp
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Abstract

To provide a filter medium that reduces re-entrainment of salt during deliquescence by high salt retention characteristics while securing dust removal efficiency and ventilation resistance.SOLUTION: A filter medium for measures against salt damage according to the present invention comprises a support fiber layer for being arranged on the upstream side of ventilation, and a melt-blown nonwoven fabric layer for being arranged on the downstream side. The support fiber layer has moisture absorbency and fire retardancy. The melt-blown nonwoven fabric layer is subjected to liquid-repellent treatment. The melt-blown nonwoven fabric layer and the support fiber layer are joined together with an adhesive.SELECTED DRAWING: Figure 1

Description

本発明は、空調用やエアコン用等に使用されるフィルターやフィルターユニットに用いられる濾材に関するものである。 The present invention relates to a filter medium used in filters and filter units used for air conditioning, air conditioners, and the like.

従来、一般に工場、ビル等に外気を取り入れる場合、JIS B 9908:2011のうち形式2が適用されるやや微細な粉塵用フィルターユニットを用いる。一般的に外こうした用途ではガラス繊維よりなる濾材をジグザグ状に折り畳んで枠内に挿入したフィルター形状をしている。こうしたフィルターユニットは外気が比較的乾燥した状態では外気中に含まれる塩分粒子は結晶状の固体粒子となっている為、通常外気中に含まれている粒子と同様に除去することが可能であるが、外気が高湿度である場合には一旦フィルターユニットの濾材表面に捕集された塩分粒子が潮解することにより濾材表面に膜状に広がり、圧力損失が急上昇すると共にやがて濾材を通過して工場、ビル内に侵入し、塩害をもたらすという問題点があった。また、強風により界面よりの海水粒子の飛散が激しい場合にも液状の海水粒子が飛来する為に、同様の現象を生ずる。 Conventionally, when outside air is taken into a factory, building, etc., a rather fine dust filter unit to which Type 2 of JIS B 9908:2011 is applied is used. Generally, in such applications, a filter is formed by folding a filter medium made of glass fiber into a zigzag shape and inserting it into a frame. With these filter units, when the outside air is relatively dry, the salt particles contained in the outside air become crystalline solid particles, so they can be removed in the same way as the particles normally contained in the outside air. However, when the outside air is humid, the salt particles that were once collected on the surface of the filter medium of the filter unit deliquesce and spread in the form of a film on the surface of the filter medium, causing a sudden increase in pressure loss and eventually passing through the filter medium to the factory. There was a problem with salt entering buildings and causing salt damage. Furthermore, when seawater particles are violently scattered from the interface due to strong winds, the same phenomenon occurs because liquid seawater particles are blown away.

こうした塩分捕集に伴う一時的な圧力損失や下流側への再飛散を低減した濾材が各種考案されている。例えば、ある特定の繊維直径と充填率により塩分の潮解を起こさせないももの(特許文献1)、撥水性を有する2つの濾材層間に、吸脱湿機能を有する繊維を含んでなる中間濾材層を設け中間層で塩分を含んだ水分を捕集するもの(特許文献2)といったもの、イオン交換能を有する素材に塩分を含んだ粒子を吸着させて捕集する方法(特許文献3)が存在する。しかしながら、特許文献1ではある程度の粒子捕集効率を必要とするためには相応の繊維密度を必要とするため除塵効率を上げることが難しく、特許文献2においては潮解した塩分を中間層で捕集するもの、濾材の厚みが厚くなるためひだおり後のフィルターにした状態での通気抵抗が相対的に高くなる。また、特許文献3ではイオン交換に用いる素材が粒状であるため反応に必要な幾何表面積が少なく、塩分の捕集量が思わしくないといった問題点がある。 Various types of filter media have been devised that reduce the temporary pressure loss and re-scattering downstream due to salt collection. For example, a filter that does not cause salt deliquescence due to a certain fiber diameter and packing ratio (Patent Document 1), and an intermediate filter medium layer that contains fibers that have a moisture absorption and desorption function between two water-repellent filter medium layers. There are methods in which salt-containing moisture is collected in an intermediate layer (Patent Document 2), and methods in which salt-containing particles are adsorbed and collected by a material with ion exchange ability (Patent Document 3). . However, in Patent Document 1, it is difficult to increase the dust removal efficiency because a certain level of particle collection efficiency requires a certain fiber density, and in Patent Document 2, deliquesced salt is collected in an intermediate layer. However, since the thickness of the filter medium becomes thicker, the ventilation resistance after folding becomes relatively high. Further, in Patent Document 3, since the material used for ion exchange is granular, the geometric surface area necessary for the reaction is small, and there is a problem that the amount of salt captured is unsatisfactory.

こうした課題を解決するため吸水性の高い支持層と撥水性高い微粉塵捕集層を組み合わせた濾材も考案されている(特許文献4)。しかし、特許文献1乃至4においては安全性の上で確保されるべき難燃性が考慮されていない。そのため、セルロースを主体とした繊維にリン酸塩を主体とした難燃剤が添加された熱溶融製樹脂を混ぜてシート化されたフィルター(特許文献5)や、ハロゲンを含有しないポリエステル繊維を主成分としてバインダーとしてイソシアナート系樹脂で結着したシート(特許文献6)など存在する。 In order to solve these problems, a filter medium that combines a highly water-absorbent support layer and a highly water-repellent fine dust collection layer has also been devised (Patent Document 4). However, in Patent Documents 1 to 4, flame retardance, which should be ensured in terms of safety, is not taken into consideration. Therefore, there are filters that are made into sheets by mixing cellulose-based fibers with hot-melt resin containing a phosphate-based flame retardant (Patent Document 5), and filters that are made of halogen-free polyester fibers as a main component. There are sheets bound with isocyanate resin as a binder (Patent Document 6).

特開平5-15716号公報Japanese Patent Application Publication No. 5-15716 特開平7-148406号公報Japanese Unexamined Patent Publication No. 7-148406 特開平6-182127号公報Japanese Patent Application Publication No. 6-182127 特開2020-189255号公報Japanese Patent Application Publication No. 2020-189255 特開平11-253717号公報Japanese Patent Application Publication No. 11-253717 特開2001-310106号公報Japanese Patent Application Publication No. 2001-310106

しかしながら、難燃剤や難燃機能を有するバインダーが繊維中に添加されたシートでは潮解した塩分をシートに吸収することができず、通気抵抗の上昇や捕集された塩分の再飛散が懸念される。 However, sheets in which flame retardants or binders with flame retardant properties are added to the fibers are unable to absorb deliquescent salt into the sheet, and there are concerns about increased ventilation resistance and re-scattering of the collected salt. .

そこで、本発明は上記課題に鑑みなされ、その目的は、高い粉塵除去効率を確保しつつ、塩分保持特性による潮解時の塩分再飛散を低減でき、難燃性を有する、塩害対策濾材を提供することである。 Therefore, the present invention was made in view of the above problems, and its purpose is to provide a filter medium for preventing salt damage, which can reduce salt re-scattering during deliquescence due to its salt retention properties, and has flame retardancy, while ensuring high dust removal efficiency. That's true.

本発明者の鋭意検討により本発明を得た。本発明は以下の通りである。
(1)通気の上流側に配置される支持繊維層と下流側に配置されるメルトブロー不織布層とを備えた塩害対策濾材において、前記支持繊維層は吸湿性と難燃性とを有し、前記前記メルトブロー不織布層は撥水性を有し、前記メルトブロー不織布層と前記支持繊維層とは接着剤にて接合されていること特徴とする塩害対策濾材。
(2)前記支持繊維層は、JIS L 1907:2004におけるパイレック法による吸水度が10mm以上である上記(1)に記載の塩害対策濾材。
(3)上記支持繊維層は、繊維層重量に対して15~35重量%の難燃性物質を含有する上記(1)または(2)に記載の塩害対策濾材。
(4)前記メルトブロー不織布層は、帯電化されており、かつ、表面張力が34mN/m以下である上記(1)~(3)のいずれか1に記載の塩害対策濾材。
(5)前記メルトブロー不織布層は、ポリオレフィン系メルトブロー不織布の表面にフッ素系化合物が付着されて成る上記(1)~(4)のいずれか1に記載の塩害対策濾材。
(6)上記(1)~(5)のいずれか1に記載の塩害対策濾材を用いたプリーツ型フィルター。
The present invention was achieved through intensive study by the present inventor. The invention is as follows.
(1) In a salt damage prevention filter medium comprising a support fiber layer disposed on the upstream side of ventilation and a melt-blown nonwoven fabric layer disposed on the downstream side, the support fiber layer has hygroscopicity and flame retardancy, and the support fiber layer has hygroscopicity and flame retardancy; A filter medium for preventing salt damage, characterized in that the melt-blown non-woven fabric layer has water repellency, and the melt-blown non-woven fabric layer and the supporting fiber layer are bonded together with an adhesive.
(2) The filter medium for preventing salt damage according to (1) above, wherein the supporting fiber layer has a water absorption degree of 10 mm or more according to the Pyrex method according to JIS L 1907:2004.
(3) The filter medium for preventing salt damage according to (1) or (2) above, wherein the supporting fiber layer contains a flame retardant material in an amount of 15 to 35% by weight based on the weight of the fiber layer.
(4) The filter medium for preventing salt damage according to any one of (1) to (3) above, wherein the melt-blown nonwoven fabric layer is electrically charged and has a surface tension of 34 mN/m or less.
(5) The filter medium for preventing salt damage according to any one of (1) to (4) above, wherein the melt-blown non-woven fabric layer is formed by adhering a fluorine compound to the surface of a polyolefin-based melt-blown non-woven fabric.
(6) A pleated filter using the salt damage prevention filter medium according to any one of (1) to (5) above.

本発明により、粉塵捕集効率や粉塵供給量といった一般的なフィルター特性を維持しつつ、塩害対策フィルターとして潮解した塩分の下流側への再飛散が少なく、かつ難燃性を有する濾材を提供することが可能となる。本発明の濾材は、JIS B 9908:2011のうち形式2が適用されるやや微細な粉塵用フィルターユニットに好適に使用される。 The present invention provides a filter medium that maintains general filter characteristics such as dust collection efficiency and dust supply amount, has low re-scattering of deliquesced salt to the downstream side as a salt damage prevention filter, and has flame retardant properties. becomes possible. The filter medium of the present invention is suitably used in a filter unit for slightly fine dust to which Type 2 of JIS B 9908:2011 is applied.

本発明に係る塩害対策濾材の断面図である。FIG. 2 is a cross-sectional view of a salt damage prevention filter medium according to the present invention. 本発明に用いる粒子捕集効率評価設備の概略図である。It is a schematic diagram of particle collection efficiency evaluation equipment used in the present invention. 本発明に用いる塩分再飛散率評価設備の概略図である。FIG. 2 is a schematic diagram of salt re-entrainment rate evaluation equipment used in the present invention. 本発明に用いる燃焼性試験設備の概略図である。1 is a schematic diagram of flammability test equipment used in the present invention.

以下、本発明に関して具体的に説明するが、本発明は下記に限定される訳ではなく前・後記の趣旨に適合し得る範囲で適当に変更を加えて実施することも可能であり、それらはいずれも本発明の技術的範囲に包含される。 The present invention will be explained in detail below, but the present invention is not limited to the following and can be practiced with appropriate modifications within the scope of the spirit of the above and below. All are included within the technical scope of the present invention.

図1に本発明に係る難燃性能を有る塩害対策濾材(以下、濾材)100の断面図を示す。濾材100は、塩害対策フィルターに適用される。濾材10は少なくとも気流の上流側に配置される支持繊維層1と気流の下流側に配置されるメルトブロー不織布層2とを備えている。支持繊維層1は吸湿性と難燃性とを有し、メルトブロー不織布層は撥水性を有し、支持繊維層1とメルトブロー不織布層2とは接着剤にて接合されている。 FIG. 1 shows a cross-sectional view of a filter medium 100 for preventing salt damage (hereinafter referred to as a filter medium) having flame retardant properties according to the present invention. The filter medium 100 is applied to a salt damage prevention filter. The filter medium 10 includes at least a support fiber layer 1 disposed on the upstream side of the airflow and a melt-blown nonwoven fabric layer 2 disposed on the downstream side of the airflow. The supporting fiber layer 1 has hygroscopicity and flame retardancy, the melt-blown nonwoven fabric layer has water repellency, and the supporting fiber layer 1 and the melt-blown nonwoven fabric layer 2 are bonded with an adhesive.

支持繊維層1は難燃性と吸湿性を有するシート状繊維であり、濾材としての形態保持を目的とした適度の強度と難燃性、吸湿性と併せ持つ繊維層である。この吸湿性により、下流側に一時的に捕集されている塩分を含んだ水滴を積極的に吸収する。 The support fiber layer 1 is a sheet-like fiber that has flame retardancy and hygroscopicity, and is a fibrous layer that has appropriate strength, flame retardancy, and hygroscopicity for the purpose of maintaining its shape as a filter medium. Due to this hygroscopicity, it actively absorbs water droplets containing salt that are temporarily collected on the downstream side.

メルトブロー不織布層2は、メルトブロー不織布に撥水(撥液)処理が施されていることが好ましく、メルトブロー繊維上での水滴の繊維状への広がりを抑制する。 The melt-blown non-woven fabric layer 2 preferably has a water-repellent (liquid-repellent) treatment applied to the melt-blown non-woven fabric to suppress the spread of water droplets on the melt-blown fibers into the fibrous form.

そのため、支持繊維層1とメルトブロー不織布層2との2層の相乗効果により、塩分を含んだ水粒子はより撥水性を伴ったメルトブロー不織布に捕集されることで、繊維表面への潮解を抑制されるため広がらず、大きな液滴となって繊維表面上に存在し、吸水性を持つ上流側支持繊維層1によって速やかに吸収される。こうした機構により捕集された塩分を含む水滴は下流側への再飛散が抑制される。 Therefore, due to the synergistic effect of the supporting fiber layer 1 and the melt-blown nonwoven fabric layer 2, water particles containing salt are collected by the melt-blown nonwoven fabric with more water repellency, thereby suppressing deliquescence on the fiber surface. Because of this, it does not spread out, but instead exists as large droplets on the fiber surface, and is quickly absorbed by the upstream support fiber layer 1, which has water absorption properties. This mechanism prevents the collected salt-containing water droplets from scattering downstream again.

支持繊維層1は、支持体本来の形態維持と吸水性保持が必要である。もちろん濾材であるため通気抵抗は低い方が好ましい。支持繊維層1の吸水性としては、JIS L 1907:2004におけるパイレック法による吸水度において10mm以上、好ましくは15mm以上の吸水度であることが望ましい。吸水度が10mm未満である場合、十分な吸水が期待できず捕集された液滴を保持することが出来ないため下流側への再飛散が発生し好ましくない。 The support fiber layer 1 needs to maintain the original shape of the support and maintain water absorption. Of course, since it is a filter medium, it is preferable that the ventilation resistance is low. The water absorbency of the support fiber layer 1 is desirably 10 mm or more, preferably 15 mm or more, as determined by the Pyrex method according to JIS L 1907:2004. If the water absorption is less than 10 mm, sufficient water absorption cannot be expected and the collected droplets cannot be retained, resulting in re-scattering to the downstream side, which is not preferable.

支持繊維層1は、吸水性と本来の支持繊維層1としての強度や通気抵抗といった機能とを両立するために、例えば、ポリエステル、ナイロン、レーヨン、綿といった親水性基を有した素材を単一、もしくは適宜混合してシート化し、親水性を発現するバインダーを公知の方法で添付することによって得られる。特に通気性やハンドリング、価格といった面でシートとしては不織布を使用することが好ましい。具体的には支持繊維層1は、上述の素材の短繊維をウェブ化して公知の方法、例えばニードルパンチや水流交絡によってシート化し、ディップ法やコーティング法によってアクリル系バインダーをシート中に含浸、乾燥させることによって得られる。支持繊維層1は、例えば、繊度1.1~5.5Tの繊維が用いられ、適度な強度を得るため10~30重量%のバインダーを含み、目付30~90g/m、厚み0.3~1.0mmの範囲であるのが好ましい。 The supporting fiber layer 1 is made of a single material having a hydrophilic group such as polyester, nylon, rayon, or cotton, in order to achieve both water absorption and the original functions of the supporting fiber layer 1, such as strength and ventilation resistance. Alternatively, it can be obtained by appropriately mixing them, forming them into a sheet, and adding a binder that exhibits hydrophilicity using a known method. In particular, it is preferable to use nonwoven fabric as the sheet in terms of breathability, handling, and cost. Specifically, the support fiber layer 1 is made by forming short fibers of the above-mentioned materials into a web, forming it into a sheet by a known method such as needle punching or hydroentangling, impregnating the sheet with an acrylic binder by a dipping method or coating method, and drying it. obtained by letting For example, the supporting fiber layer 1 uses fibers with a fineness of 1.1 to 5.5T, contains 10 to 30% by weight of a binder to obtain appropriate strength, has a basis weight of 30 to 90 g/m 2 , and a thickness of 0.3 It is preferably in the range of ~1.0 mm.

また、濾材100自体の難燃性を担保するために支持繊維層1には難燃剤(難燃性物質)が付加される。難燃剤については支持繊維層との馴染みよく、かつ吸水性が維持される必要がある。ここでは特にリン系の水溶性難燃剤、特にリン酸1水素アンモニウムやリン酸グアニジンおよびその類似物が好適に用いられる。難燃性物質が吸水性の支持繊維層1に付加されていることにより本来持つ吸水性を損なうことなく難燃性を有することが可能となる。撥水性の機能を有する難燃剤を用いた場合、本来の支持繊維層の持つ吸水性が損なわれ、吸水量が低下して目的とする塩分捕集性能を維持することができない。 Furthermore, a flame retardant (flame retardant substance) is added to the support fiber layer 1 to ensure the flame retardancy of the filter medium 100 itself. The flame retardant needs to be compatible with the support fiber layer and maintain water absorption. In particular, phosphorus-based water-soluble flame retardants, particularly ammonium monohydrogen phosphate, guanidine phosphate, and their analogs are preferably used. By adding a flame-retardant substance to the water-absorbent supporting fiber layer 1, it becomes possible to have flame retardancy without impairing the inherent water-absorbing property. When a flame retardant having a water-repellent function is used, the original water absorption of the support fiber layer is impaired, the amount of water absorption decreases, and the desired salt-trapping performance cannot be maintained.

支持繊維層1の繊維総重量に対して難燃性物質の添加量は、15重量%から35%、好ましくは20%から30%が、難燃性と吸湿性を得る上で好適である。15重量%未満の場合、十分な難燃性が確保されず、35%を超える場合、潮解性物質が多すぎるためかえって塩分を吸収することができず、好ましくない。支持繊維層1への難燃物質の付加は、公知の方法で実施可能であるが、支持繊維層1の持つ本来の吸水性を維持しつつ難燃性を担保するためには、水溶性の難燃剤をディップ法により均一に添着し、乾燥させる方法が好適である。水溶性の難燃剤は、完全水溶性のものの他、エマルジョンタイプも適用可能であるが、非水溶性のものの場合繊維層への均一な担持ができないため、十分な難燃性を期待できない。 The addition amount of the flame retardant substance to the total fiber weight of the support fiber layer 1 is preferably 15% to 35% by weight, preferably 20% to 30% in order to obtain flame retardancy and hygroscopicity. If it is less than 15% by weight, sufficient flame retardancy cannot be ensured, and if it exceeds 35%, the amount of deliquescent substances is too large and salt cannot be absorbed, which is not preferable. Addition of a flame retardant substance to the support fiber layer 1 can be carried out by a known method, but in order to maintain flame retardancy while maintaining the original water absorbency of the support fiber layer 1, it is necessary to add a water-soluble substance to the support fiber layer 1. A preferred method is to uniformly apply the flame retardant by a dipping method and then dry it. In addition to completely water-soluble water-soluble flame retardants, emulsion type flame retardants can also be used, but water-insoluble flame retardants cannot be uniformly supported on the fiber layer, so sufficient flame retardancy cannot be expected.

メルトブロー不織布層層2は、ポリオレフィン樹脂からなる繊維から構成され、ポリオレフィン樹脂としては、特にポリプロピレン樹脂が好適に用いられる。また、規格に応じた通気抵抗と捕集効率を得るために適度な繊維径と目付のものが選定される。しかし撥水性を得るために必要な撥水処理を施されることが必要である。特に繊維表面にフッ素系化合物が付着したものは繊維表面にナノレベル微細な凹凸が形成され、表面張力を下げることによって撥水性を上げることが可能となる。フッ素系化合物の繊維表面の付着によって表面張力を34mN/m以下にすることで適度な撥水性が得られる。フッ素系化合物を繊維表面に付着させる方法はフッ素系化合物を含有した薬液を水や有機溶剤中に分散させてdip法やスプレー法といった公知の方法によって得られるが、再公表特許2016年088692号公法に記載された蒸着による方法も用いられ、特に方法には限定されない。また、除塵効率を向上させて通気抵抗を低減させる場合、公知の方法において荷電処理を施し、エレクトレット化することで可能となる。 The melt-blown nonwoven fabric layer 2 is composed of fibers made of polyolefin resin, and polypropylene resin is particularly preferably used as the polyolefin resin. In addition, appropriate fiber diameter and fabric weight are selected in order to obtain ventilation resistance and collection efficiency according to the standards. However, in order to obtain water repellency, it is necessary to perform necessary water repellent treatment. In particular, when a fluorine-based compound is attached to the fiber surface, nano-level fine irregularities are formed on the fiber surface, which lowers the surface tension, making it possible to increase water repellency. Appropriate water repellency can be obtained by reducing the surface tension to 34 mN/m or less by adhering the fluorine-based compound to the fiber surface. A method for attaching a fluorine-based compound to the fiber surface is by dispersing a chemical solution containing a fluorine-based compound in water or an organic solvent and using a known method such as a dip method or a spray method. The vapor deposition method described in 2007 can also be used, and the method is not particularly limited. Further, in order to improve the dust removal efficiency and reduce the ventilation resistance, it is possible to perform charging treatment using a known method to make it an electret.

支持繊維層1とメルトブロー不織布層2とは層間に接着剤を介して積層、接合され濾材となる。積層、接着方法は、接着剤となるパウダーを、少なくとも一方の層上に散布して加熱・圧縮する方法や、溶融した接着剤を細いノズルから噴き出して少なくとも一方の層の表面上に細かく散布して圧縮する方法(スプレー法)、接着性繊維のシートを層間に積層して加熱圧縮する方法などあるが、特に限定されない。より強力な難燃性を求める場合は接着剤に難燃剤を混入して使用したり、接着性繊維を用いる場合はROI値の高い素材を選択したりすることで、対応できる。 The supporting fiber layer 1 and the melt-blown nonwoven fabric layer 2 are laminated and bonded with an adhesive between the layers to form a filter medium. Lamination and bonding methods include spraying adhesive powder onto at least one layer and heating and compressing it, or spraying molten adhesive from a thin nozzle and finely scattering it over the surface of at least one layer. There are methods such as a method of compressing the material by heating (spray method), a method of laminating sheets of adhesive fibers between layers and compressing with heat, but there are no particular limitations. If stronger flame retardancy is desired, this can be achieved by mixing a flame retardant into the adhesive, or by selecting a material with a high ROI value when using adhesive fibers.

塩害対策濾材は、他のシートと積層されたり、加工されたりして用いられてもよい。また、塩害対策濾材を用いたプリーツ型フィルターも本発明の範疇に含まれる。 The salt damage prevention filter medium may be used by being laminated with other sheets or processed. Further, pleated filters using filter media for preventing salt damage are also included in the scope of the present invention.

以下では、実施例及び比較例を用いて本発明を具体的に説明するが、本発明は実施例の
みに限定されるものではない。
The present invention will be specifically explained below using Examples and Comparative Examples, but the present invention is not limited only to the Examples.

始めに、実施例及び比較例の物性値の測定方法について説明する。
<難燃剤含有率>
難燃剤含有率(%):難燃剤添着前後のシート乾燥重量を測定し、下記の式(1)を用いて算出した。
難燃剤含有率=(1-添着前重量/難燃剤添着後の全重量)×100・・・(1)
<目付>
目付(g/m)は、200mm角の寸法で切り出し、秤量して寸法で除した。
First, methods for measuring physical property values of Examples and Comparative Examples will be explained.
<Flame retardant content>
Flame retardant content (%): The sheet dry weight before and after flame retardant impregnation was measured, and calculated using the following formula (1).
Flame retardant content = (1-weight before impregnation/total weight after flame retardant impregnation) x 100...(1)
<Weight>
The basis weight (g/m 2 ) was determined by cutting out a 200 mm square, weighing it, and dividing it by the size.

<厚み>
厚み(mm)は、荷重0.7kPaの厚みを読み取った。
<圧力損失・粒子捕集効率>
図2に示す粒子捕集効率評価設備200を用いて、ダクト4にサンプル12をセットし、線速10cm/秒に設定した空気を流して濾材の上下流における差圧を差圧計7で測定、圧力損失とした。さらに上流側と下流側の空気をサンプリングし、パーティクルカウンター8を用い0.3~0.5μmの粒径の粒子数をカウントした。粒子捕集効率(E)は下記の式(2)を用いて算出した。
粒子捕集効率 E(%)={1-(下流粒子数/上流粒子数)}×100・・・(2)
<Thickness>
The thickness (mm) was measured at a load of 0.7 kPa.
<Pressure loss/particle collection efficiency>
Using the particle collection efficiency evaluation equipment 200 shown in FIG. 2, the sample 12 is set in the duct 4, air is flowed at a linear velocity of 10 cm/sec, and the differential pressure upstream and downstream of the filter material is measured with the differential pressure gauge 7. It was taken as pressure loss. Furthermore, the air on the upstream and downstream sides was sampled, and the number of particles with a particle size of 0.3 to 0.5 μm was counted using a particle counter 8. Particle collection efficiency (E) was calculated using the following formula (2).
Particle collection efficiency E (%) = {1-(number of downstream particles/number of upstream particles)}×100...(2)

<吸水性>
JIS L 1907:2004におけるパイレック法による吸水度で評価した。
<Water absorption>
The water absorption was evaluated by the Pyrex method according to JIS L 1907:2004.

<撥水性>
表面張力としてJIS K 6768に基づき、ぬれ張力試験用混合液の液滴を滴下し、30秒間接触させて、液滴の浸透の有無を確認した。
<Water repellency>
Based on JIS K 6768 for surface tension, a droplet of a mixed liquid for wetting tension test was dropped and brought into contact for 30 seconds to check whether or not the droplet had penetrated.

<難燃性>
図4に示す燃焼性試験設備400を用いて、JIS L 1091:1999 A-1法(45°ミクロバーナ法)に準拠して実施した。
<Flame retardancy>
The test was carried out in accordance with JIS L 1091:1999 A-1 method (45° microburner method) using the flammability test equipment 400 shown in FIG.

<NaCl潮解時の再飛散率>
有効通風面積が82cm (10.2cmφ)になるようサンプルを切り抜いた後、乾燥重量を測定し「初期重量」(W)とした。次に予め乾燥後粉砕し、400メッシュ(目の開き37μm)の篩いを通過させたNaCl粒子を約0.3g付着させた後、乾燥重量を測定し「NaCl付着後重量」(W)とした。このときWとWの差をNaCl付着量(W)とした。気温20℃、相対湿度90%に調節した実験室内に設置した図3に示す塩分再飛散率評価設備300に、NaClを付着させたサンプルをサンプルホルダー8に装着、風速が13cm/s(風量3.84m/hr)となるように流量計9で調節しながら送風機11により通風し、8時間放置した。なお、通風する空気はHEPAフィルター13で無塵空気とした。放置後、サンプルを試験装置より取り出し、乾燥後重量を測定し「NaCl再飛散後の重量」(W)とした。NaClの再飛散量WはWとWの差で表される。NaCl潮解時の再飛散率は下記式(3)で表される。
NaCl再飛散率=W/W ×100・・・(3)
<Re-entrainment rate during NaCl deliquescence>
After cutting out the sample so that the effective ventilation area was 82 cm 2 (10.2 cmφ), the dry weight was measured and defined as the "initial weight" (W 0 ). Next, about 0.3 g of NaCl particles, which had been previously dried and pulverized and passed through a 400-mesh (opening 37 μm) sieve, was attached, and the dry weight was measured and the "weight after adhesion of NaCl" (W 1 ) was determined. did. At this time, the difference between W 1 and W 0 was defined as the amount of NaCl attached (W). The sample with NaCl attached was attached to the sample holder 8 in the salt re-entrainment rate evaluation equipment 300 shown in FIG. Ventilation was carried out using a blower 11 while adjusting the flow rate using a flow meter 9 so that the flow rate was 0.84 m 2 /hr), and left for 8 hours. Note that the ventilated air was made dust-free using a HEPA filter 13. After standing, the sample was taken out from the test device, and its weight after drying was measured and defined as "weight after re-encrusting NaCl" (W 2 ). The re-entrainment amount W3 of NaCl is expressed as the difference between W1 and W2 . The re-entrainment rate during NaCl deliquescence is expressed by the following equation (3).
NaCl re-entrainment rate = W 3 /W × 100... (3)

次に、実施例及び比較例の濾材の製造方法を説明する。
(1)支持繊維層
上流側に配置される支持繊維層の作製について説明する。
ポリエステル繊維2.2T×51mmをミニチュアカードにかけてウェブ化し、小型ニードルパンチ機で弱く繊維間を交絡させ、目付46g/mの不織布を得た。これをアクリル系バインダー「DICNAL E-8290N」(DIC株式会社製)を分散させた水溶液に含浸し、マングルで絞った後110℃で乾燥させ、支持繊維層を得た。支持繊維層を乾燥後、物性について測定したところ、目付55~60g/m、厚み0.7mm、引張強度6kgf/5cm、吸水度35mmであった。
(2)メルトブロー不織布層
下流側に配置されるメルトブロー不織布層については、市販品のメルトブロー不織布(三井化学製MPEA04:目付20g/m、厚み0.24mm、通気性58cc/cm/sec)を用い、撥水剤としてポリテトラフルオロエチレンのソルベントに含浸させ、取出後、揮発分を蒸発させ、メルトブロー不織布層を得た。メルトブロー不織布層において、ポリテトラフルオロエチレンの添加量は2g/mで、表面張力は30mN/mであった。
(3)濾材の接合方法
A:スプレー法
支持繊維層上に「スプレーのり77」(スリーエム・ジャパン株式会社製)を2±0.5g/m噴射して添着させ、その上にメルトブロー不織布層を積層し、軽く手で押さえて接合させた。
B:接着繊維を使用する方法
接着繊維(ダイナックLNS-0010)を支持繊維層上に載せ、メルトブロー不織布層をその上に置き、130℃設定のアイロンで支持繊維層の上から1分間押さえて接合させた。
(4)荷電処理
アース側:アルミ板に厚さ2mmのシリコンシートを敷設した。
電極側:針間隔10mmの針電極
電極-アース間距離:針先端からシリコンシートまで10mm
印加電圧:20kV
荷電時間:30秒
荷電は接着後の濾材をアース側に敷設して実施した。
Next, methods for manufacturing filter media of Examples and Comparative Examples will be explained.
(1) Support fiber layer The production of the support fiber layer disposed on the upstream side will be explained.
Polyester fibers of 2.2 T x 51 mm were formed into a web by passing them through a miniature card, and the fibers were weakly entangled with a small needle punch machine to obtain a nonwoven fabric with a basis weight of 46 g/m 2 . This was impregnated with an aqueous solution in which an acrylic binder "DICNAL E-8290N" (manufactured by DIC Corporation) was dispersed, squeezed with a mangle, and dried at 110° C. to obtain a supporting fiber layer. After drying the supporting fiber layer, physical properties were measured and found to be a basis weight of 55 to 60 g/m 2 , a thickness of 0.7 mm, a tensile strength of 6 kgf/5 cm, and a water absorption of 35 mm.
(2) Melt-blown non-woven fabric layer For the melt-blown non-woven fabric layer disposed on the downstream side, a commercially available melt-blown non-woven fabric (Mitsui Chemicals MPEA04: basis weight 20 g/m 2 , thickness 0.24 mm, air permeability 58 cc/cm 2 /sec) was used. It was impregnated with a polytetrafluoroethylene solvent as a water repellent, and after being taken out, volatile components were evaporated to obtain a melt-blown nonwoven fabric layer. In the melt-blown nonwoven fabric layer, the amount of polytetrafluoroethylene added was 2 g/m 2 and the surface tension was 30 mN/m.
(3) Method for joining filter media A: Spray method Spray 2±0.5 g/ m2 of "Spray Glue 77" (manufactured by 3M Japan Co., Ltd.) onto the support fiber layer to adhere it, and then apply the melt-blown nonwoven fabric layer on top of it. were laminated and pressed lightly with hand to join them.
B: Method using adhesive fiber Place the adhesive fiber (Dynac LNS-0010) on the support fiber layer, place the melt-blown nonwoven fabric layer on top of it, and press the top of the support fiber layer with an iron set at 130°C for 1 minute to join. I let it happen.
(4) Charge treatment Earth side: A silicone sheet with a thickness of 2 mm was laid on an aluminum plate.
Electrode side: needle electrode with needle spacing of 10 mm Electrode-ground distance: 10 mm from needle tip to silicone sheet
Applied voltage: 20kV
Charging time: 30 seconds Charging was carried out by laying the bonded filter medium on the ground side.

(実施例1~3、比較例1,2)
上記得られた支持繊維層を、リン酸系難燃剤(アピノン307:三和化学製)の水溶液に含侵し、マングルにて脱水後、120°Cで10分間乾燥させた。乾燥後、当該支持繊維層と上記得られたメルトブロー不織布層とを上記スプレー法にて接合し、上記荷電処理そして濾材を得た。
支持繊維層の難燃剤添着量、吸水度、濾材の目付、厚み、圧力損失、粒子捕集効率、塩分再飛散率、難燃区分を表1に示す。
(実施例5、比較例5)
上記得られた支持繊維層を、リン酸系難燃剤(フランTTC:大和化学製)の水溶液に含侵し、マングルにて脱水後、120°Cで10分間乾燥させた。乾燥後、当該支持繊維層と上記得られたメルトブロー不織布層とを上記スプレー法にて接合し、上記荷電処理をして濾材を得た。
支持繊維層の難燃剤添着量、吸水度、濾材の目付、厚み、圧力損失、粒子捕集効率、塩分再飛散率、難燃区分を表1に示す。
(実施例4)
上記得られた支持繊維層を、リン酸系難燃剤(アピノン307:三和化学製)の水溶液に含侵し、マングルにて脱水後、120°Cで10分間乾燥させた。乾燥後に、当該支持繊維層と上記得られたメルトブロー不織布とを上記接着繊維を使用する方法にて接合し、上記荷電処理をして濾材を得た。
支持繊維層の難燃剤添着量、吸水度、濾材の目付、厚み、圧力損失、粒子捕集効率、塩分再飛散率、難燃区分を表1に示す。
(比較例3)
上記得られた支持繊維層を少量の界面活性剤(ノニオン系)を含んだ水にリン酸系難燃剤(MPP-B:三和ケミカル製)を分散させた水浴中に含侵し、マングルにて脱水後、120°Cで10分間乾燥させた。乾燥後、当該支持繊維層と上記得られたメルトブロー不織布とを上記スプレー法にて接合し、上記荷電処理して濾材を得た。
支持繊維層の難燃剤添着量、吸水度、濾材の目付、厚み、圧力損失、粒子捕集効率、塩分再飛散率、難燃区分を表1に示す。
(比較例4)
上記得られた支持繊維層を少量の界面活性剤(ノニオン系)を含んだ水にリン酸系難燃剤(タイエンK:太平化学製)を分散させた水浴中に含侵し、マングルにて脱水後、120°Cで10分間乾燥させた。乾燥後に当該支持繊維層と上記得られたメルトブロー不織布とを上記スプレー法にて接合し、上記荷電処理をして濾材を得た。
支持繊維層の難燃剤添着量、吸水度、濾材の目付、厚み、圧力損失、粒子捕集効率、塩分再飛散率、難燃区分を表1に示す。
(Examples 1 to 3, Comparative Examples 1 and 2)
The support fiber layer obtained above was impregnated with an aqueous solution of a phosphoric acid flame retardant (Apinon 307, manufactured by Sanwa Chemical Industries, Ltd.), dehydrated using a mangle, and then dried at 120° C. for 10 minutes. After drying, the support fiber layer and the melt-blown nonwoven fabric layer obtained above were joined by the above spray method, subjected to the above charging treatment, and a filter medium was obtained.
Table 1 shows the amount of flame retardant impregnated in the support fiber layer, water absorption, basis weight of filter medium, thickness, pressure loss, particle collection efficiency, salt re-entrainment rate, and flame retardant classification.
(Example 5, Comparative Example 5)
The supporting fiber layer obtained above was impregnated with an aqueous solution of a phosphoric acid flame retardant (Furan TTC: manufactured by Yamato Chemical), dehydrated with a mangle, and then dried at 120° C. for 10 minutes. After drying, the support fiber layer and the melt-blown nonwoven fabric layer obtained above were joined by the above-mentioned spray method and subjected to the above-mentioned charging treatment to obtain a filter medium.
Table 1 shows the amount of flame retardant impregnated in the support fiber layer, water absorption, basis weight of filter medium, thickness, pressure loss, particle collection efficiency, salt re-entrainment rate, and flame retardant classification.
(Example 4)
The support fiber layer obtained above was impregnated with an aqueous solution of a phosphoric acid flame retardant (Apinon 307, manufactured by Sanwa Chemical Industries, Ltd.), dehydrated using a mangle, and then dried at 120° C. for 10 minutes. After drying, the support fiber layer and the obtained melt-blown nonwoven fabric were joined by the method using the adhesive fibers, and the charging treatment was performed to obtain a filter medium.
Table 1 shows the amount of flame retardant impregnated in the support fiber layer, water absorption, basis weight of filter medium, thickness, pressure loss, particle collection efficiency, salt re-entrainment rate, and flame retardant classification.
(Comparative example 3)
The supporting fiber layer obtained above was impregnated in a water bath containing a phosphoric acid flame retardant (MPP-B: manufactured by Sanwa Chemical Co., Ltd.) dispersed in water containing a small amount of surfactant (nonionic). After dehydration, it was dried at 120°C for 10 minutes. After drying, the supporting fiber layer and the melt-blown nonwoven fabric obtained above were joined by the above-mentioned spray method, and subjected to the above-mentioned charging treatment to obtain a filter medium.
Table 1 shows the amount of flame retardant impregnated in the support fiber layer, water absorption, basis weight of filter medium, thickness, pressure loss, particle collection efficiency, salt re-entrainment rate, and flame retardant classification.
(Comparative example 4)
The supporting fiber layer obtained above is impregnated in a water bath containing a small amount of surfactant (nonionic) and a phosphoric acid flame retardant (Tyen K: manufactured by Taihei Kagaku) dispersed therein, and then dehydrated using a mangle. , and dried at 120°C for 10 minutes. After drying, the supporting fiber layer and the melt-blown nonwoven fabric obtained above were joined by the above-mentioned spray method and subjected to the above-mentioned charging treatment to obtain a filter medium.
Table 1 shows the amount of flame retardant impregnated in the support fiber layer, water absorption, basis weight of filter medium, thickness, pressure loss, particle collection efficiency, salt re-entrainment rate, and flame retardant classification.

表1から、実施例1~5は、比較例1~5に対して塩分再飛散率が低く、難燃性に優れていることがわかる。 From Table 1, it can be seen that Examples 1 to 5 have lower salt re-entrainment rates and superior flame retardancy than Comparative Examples 1 to 5.

本発明によって得られたフィルター用濾材は、一般空調用フィルター用濾材の厚みと同等で塩分捕集、再飛散防止機能があり、これまでの効率や通気抵抗を有する濾材が得られる。かつ、難燃機能を付与したためフィルター設置後の火災に対する安全性も確保される。圧損や効率が通常の空調設備フィルターと同じなので通常品からの置き換えして提案できる。空調用途におけるプリーツタイプの分野では置き換え用途では非常に有効である。 The filter medium obtained according to the present invention has the same thickness as the filter medium for general air conditioning filters, has salt trapping and re-entrainment prevention functions, and has the efficiency and ventilation resistance of the conventional filter medium. Moreover, since it has flame retardant function, safety against fire after the filter is installed is also ensured. Since the pressure loss and efficiency are the same as regular air conditioning equipment filters, we can propose it as a replacement for regular products. It is very effective as a replacement in the field of pleated type air conditioning applications.

1 : 支持繊維層(上流側)
2 : メルトブロー不織布層(下流側)
3 : ダクト
4 : 上流側サンプリング管
5 : 下流側サンプリング管
6 : 差圧計
7 : パーティクルカウンター
8 : 流量計
9 : バルブ
10: ブロアー
11: 評価サンプル
12: HEPAフィルター
13: 試験片
14: ガスバーナー
100:塩害対策濾材
200:粒子捕集効率評価設備
300:塩分再飛散率評価設備
400:燃焼性試験設備
1: Support fiber layer (upstream side)
2: Melt-blown nonwoven fabric layer (downstream side)
3: Duct 4: Upstream sampling pipe 5: Downstream sampling pipe 6: Differential pressure gauge 7: Particle counter 8: Flow meter 9: Valve 10: Blower 11: Evaluation sample 12: HEPA filter 13: Test piece 14: Gas burner 100 : Salt damage prevention filter media 200 : Particle collection efficiency evaluation equipment 300 : Salt re-entrainment rate evaluation equipment 400 : Combustibility test equipment

Claims (6)

通気の上流側に配置される支持繊維層と下流側に配置されるメルトブロー不織布層とを備えた塩害対策濾材において、
前記支持繊維層は吸湿性と難燃性とを有し、
前記前記メルトブロー不織布層は撥水処理されており、
前記メルトブロー不織布層と前記支持繊維層とは接着剤にて接合されていること特徴とする塩害対策濾材。
In a salt damage prevention filter medium comprising a support fiber layer disposed on the upstream side of ventilation and a melt-blown nonwoven fabric layer disposed on the downstream side,
The supporting fiber layer has hygroscopicity and flame retardancy,
The melt-blown nonwoven fabric layer is treated to be water repellent,
A filter medium for preventing salt damage, characterized in that the melt-blown nonwoven fabric layer and the supporting fiber layer are bonded together with an adhesive.
前記支持繊維層は、JIS L 1907:2004におけるパイレック法による吸水度が10mm以上であることを特徴とする請求項1に記載の塩害対策濾材。 The filter medium for preventing salt damage according to claim 1, wherein the support fiber layer has a water absorption of 10 mm or more according to the Pyrex method according to JIS L 1907:2004. 上記支持繊維層は、繊維重量に対して15~35重量%の難燃性物質を含有することを特徴とする請求項1または2に記載の塩害対策濾材。 The filter medium for preventing salt damage according to claim 1 or 2, wherein the support fiber layer contains a flame retardant substance in an amount of 15 to 35% by weight based on the weight of the fibers. 前記メルトブロー不織布層は、帯電化されており、かつ、表面張力が34mN/m以下であることを特徴とする請求項1~3のいずれか1に記載の塩害対策濾材。 The filter medium for preventing salt damage according to any one of claims 1 to 3, wherein the melt-blown nonwoven fabric layer is electrically charged and has a surface tension of 34 mN/m or less. 前記メルトブロー不織布層は、ポリオレフィン系メルトブロー不織布の表面にフッ素系化合物が付着されて成ることを特徴とする請求項1~4のいずれか1に記載の塩害対策濾材。 The filter medium for preventing salt damage according to any one of claims 1 to 4, wherein the melt-blown non-woven fabric layer is formed by adhering a fluorine-based compound to the surface of a polyolefin-based melt-blown non-woven fabric. 請求項1~5のいずれか1に記載の塩害対策濾材を用いたプリーツ型フィルター。 A pleated filter using the salt damage prevention filter medium according to any one of claims 1 to 5.
JP2022043061A 2022-03-17 2022-03-17 Filter medium for measure against salt damage, and pleat type filter Pending JP2023137062A (en)

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