JP6527800B2 - Filter paper for filter and manufacturing method thereof - Google Patents

Filter paper for filter and manufacturing method thereof Download PDF

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JP6527800B2
JP6527800B2 JP2015188830A JP2015188830A JP6527800B2 JP 6527800 B2 JP6527800 B2 JP 6527800B2 JP 2015188830 A JP2015188830 A JP 2015188830A JP 2015188830 A JP2015188830 A JP 2015188830A JP 6527800 B2 JP6527800 B2 JP 6527800B2
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filter paper
organic binder
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polyglycidyl ether
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智彦 楚山
智彦 楚山
栄子 目黒
栄子 目黒
佐藤 正
正 佐藤
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Hokuetsu Corp
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本発明は、エアフィルタ用濾材、特に半導体、液晶、バイオ・食品工業関係のクリーンルーム、クリーンベンチ等、あるいはビル空調用エアフィルタにおいて気体中の不純物を濾過するために使用されるエアフィルタ用濾紙、あるいはエレクトロニクス分野、ケミカル分野、飲料・食品分野、水処理分野等に使用される液体フィルタ用濾紙に関するものである。   The present invention relates to a filter material for an air filter, particularly a filter paper for an air filter used to filter impurities in a gas in a semiconductor, liquid crystal, clean room for bio / food industry, clean bench etc, or an air filter for building air conditioning, Alternatively, the present invention relates to a filter paper for liquid filters used in the fields of electronics, chemicals, beverages / food, water treatment and the like.

従来、空気中のサブミクロン、あるいはミクロン単位の粒子を効率的に捕集・除去するためのエアフィルタ用濾紙、あるいは水、溶剤中の微粒子を効率的に捕集・除去するための液体フィルタ用濾紙に、主要構成物として平均繊維径がコンマ数μm〜数十μmのガラス繊維が用いられている。しかしガラス繊維はそれ自体、一般紙に使用されるパルプ繊維のような自己接着力がなく、このままでは後加工や使用の際の実用強度が無く、また、通風時にガラス繊維が飛散してしまうなどの問題が生じてしまう。   Conventionally, filter paper for air filters to efficiently collect and remove submicron or micron-sized particles in air, or liquid filter to efficiently collect and remove particulates in water and solvents For filter paper, glass fibers having an average fiber diameter of several micrometers to several tens of micrometers are used as a main component. However, glass fiber itself does not have self-adhesion like pulp fiber used for general paper, and as it is, there is no practical strength at the time of post-processing and use, and glass fiber is scattered during ventilation etc. Problems will arise.

従来、この問題を解決するためにガラス繊維基材に有機系バインダーを付与させる方法が用いられている。ここで、使用される有機系バインダーとしてはアクリル系樹脂、エポキシ系樹脂、ポリビニルアルコール、ウレタン系樹脂などがある。しかし、この方法で濾材の強度を上げようとするとバインダー付着量を増やす必要があるが、付着量を増やすとガラス繊維間にバインダーの水かき状膜が増えるため、濾紙の濾過効率が低下する。特にエアフィルタ用濾紙においては濾紙に対する難燃性の市場要望があるが、有機系バインダー付着量を増やすと濾紙が燃えやすくなり、付着量には限界がある。ちなみに、通常のエアフィルタ用濾材ではバインダー付着量は対基材約10質量%以下であり、特にHEPA・ULPA等の高性能・超高性能エアフィルタ用濾材では、MILスペックで可燃物量7質量%以下と規定されている。   Conventionally, in order to solve this problem, a method of applying an organic binder to a glass fiber substrate is used. Here, examples of the organic binder to be used include acrylic resin, epoxy resin, polyvinyl alcohol, urethane resin and the like. However, when it is necessary to increase the strength of the filter medium by this method, it is necessary to increase the binder adhesion amount, but when the adhesion amount is increased, the web-like film of the binder increases between the glass fibers, and the filtration efficiency of the filter paper decreases. In particular, in the case of filter paper for air filters, there is a market demand for flame retardancy with respect to the filter paper, but if the amount of adhesion of the organic binder is increased, the filter paper becomes easy to burn and the amount of adhesion is limited. By the way, the binder adhesion amount is less than about 10% by mass to the base material in ordinary filter media for air filters, and in particular, in the filter media for high performance and super performance air filters such as HEPA / ULPA, the amount of combustibles is 7% by mass in MIL specification It is prescribed as follows.

また近年、エアフィルタの多風量化に伴い濾材のミニプリーツ化が進んで濾紙強度を確保するとともに、濾過性能面においても、クリーンルーム、クリーンベンチ等に使用される送風機のランニングコスト低減の目的で、濾紙の濾過効率の向上に対する要望が高まっている。濾紙を高濾過効率化するためには、ガラス繊維の繊維径を細かくする方法があるが、繊維径が細かくなるほど濾紙の濾過抵抗が高まり、逆に送風機のランニングコストが掛かってしまう。一般に濾過抵抗の低減と濾過効率の向上とはトレードオフの関係にある。   Also, in recent years, with the increase in air volume of air filters, mini pleating of filter media has progressed to ensure filter paper strength, and also in terms of filtration performance, for the purpose of reducing running costs of blowers used in clean rooms, clean benches, etc. There is a growing demand for improvement in the filtration efficiency of filter paper. In order to increase the filtration efficiency of the filter paper, there is a method of reducing the fiber diameter of the glass fiber. However, the finer the fiber diameter, the higher the filtration resistance of the filter paper, and the higher the running cost of the blower. In general, there is a trade-off relationship between the reduction of filtration resistance and the improvement of filtration efficiency.

ガラス繊維を主体繊維としたエアフィルタ用濾紙の濾過効率を向上させる方法としては、濾紙を構成する繊維にバインダー及びシリコン樹脂を付着させる方法(例えば、特許文献1を参照。)、濾紙を構成する繊維にバインダー、フッ素樹脂及びシリコン樹脂を付着させる方法(例えば、特許文献2を参照。)が提案されている。   As a method of improving the filtration efficiency of the filter paper for air filters having glass fibers as its main fibers, a method of adhering a binder and a silicone resin to fibers constituting the filter paper (see, for example, Patent Document 1), filter paper is constructed. A method has been proposed in which a binder, a fluorocarbon resin and a silicone resin are attached to fibers (see, for example, Patent Document 2).

また、同じ課題に対して、濾紙を製造する工程において、ガラス繊維スラリーを酸性で調製した後、ヘッドボックスにおいてpH調整剤を添加することによってpHを約6〜9にして抄紙する方法が提案されている(例えば、特許文献3を参照。)。   In addition, to the same problem, in the process of producing filter paper, after preparing the glass fiber slurry with acidity, a method is proposed to make the pH about 6 to 9 by adding a pH adjuster in the headbox. (See, for example, Patent Document 3).

一方、液体フィルタ用濾紙において濾紙の濾過効率を向上させる方法として、ガラスファイバと2成分ファイバが混合され、これらが熱的に結合された不織構造の濾材であって、2成分ファイバはシース/コア構造を有するポリエチレンテレフタレート/ポリエチレンテレフタレートである濾材が提案されている(例えば、特許文献4を参照。)。   On the other hand, as a method of improving the filtration efficiency of filter paper in a filter paper for liquid filter, it is a non-woven filter medium in which glass fiber and bicomponent fiber are mixed and these are thermally bonded. A filter medium which is a polyethylene terephthalate / polyethylene terephthalate having a core structure has been proposed (see, for example, Patent Document 4).

特開平2−41499号公報JP-A-2-41499 特開平2−175997号公報JP-A-2-175997 国際公開第2004/094038号WO 2004/940038 特開2015−37783JP 2015-37783

しかし、特許文献1及び2の方法は、濾紙に付着したシリコン樹脂の成分がフィルタ使用時に微量揮発し、LSIや液晶など電子部品をつくる工程で製品に付着して、製品の歩留まりを大きく低下させる問題がある。   However, in the methods of Patent Documents 1 and 2, the component of the silicone resin attached to the filter paper volatilizes in a minute amount when the filter is used, adheres to the product in the process of making electronic components such as LSI and liquid crystal, and greatly reduces the product yield. There's a problem.

また、特許文献3の方法の実施例においては、濾材の製造時にバインダーが使用されていないことから、ここで得られた濾材は、実使用に必要とされる十分な強度を有していないことが容易に推定される。   Moreover, in the embodiment of the method of Patent Document 3, since the binder is not used at the time of production of the filter medium, the filter medium obtained here does not have sufficient strength required for practical use. Is easily estimated.

特許文献4の方法はバインダーとて、2成分ファイバのみ使用されているため、ガラス繊維の保持力が弱く、液体フィルタとして使用時にガラス繊維が脱落してしまう問題がある。ガラス繊維を主体とする濾紙では、有機系バインダーの使用が不可欠である。   In the method of Patent Document 4, since only a two-component fiber is used as a binder, the retention of glass fiber is weak, and there is a problem that the glass fiber is dropped when used as a liquid filter. In filter paper mainly composed of glass fiber, the use of an organic binder is essential.

従って本発明の課題は、現行濾紙に比べ、濾過抵抗を増加させずに、濾過効率が向上したフィルタ用濾紙を提供することである。   Therefore, an object of the present invention is to provide a filter paper for filter with improved filtration efficiency without increasing the filtration resistance as compared with the current filter paper.

本発明者らは、鋭意検討したところ、ガラス繊維を主体とするフィルタ用濾紙において、有機系バインダー及びソルビトールポリグリシジルエーテルを付着させることで上記課題が解決されることを見出し、本発明を完成させた。すなわち、本発明に係るフィルタ用濾紙は、ガラス繊維を主体とするフィルタ用濾紙において、前記ガラス繊維に、(1)有機系バインダー及びソルビトールポリグリシジルエーテル、(2)有機系バインダー、ソルビトールポリグリシジルエーテル及びこれらの架橋体、又は、(3)有機系バインダーとソルビトールポリグリシジルエーテルとの架橋体、が付着していることを特徴とする。   As a result of intensive investigations, the present inventors have found that the above-mentioned problems can be solved by depositing an organic binder and sorbitol polyglycidyl ether in filter paper mainly composed of glass fibers, and complete the present invention. The That is, the filter paper for filters according to the present invention is the filter paper mainly composed of glass fibers, wherein the glass fibers comprise (1) an organic binder and sorbitol polyglycidyl ether, (2) an organic binder, sorbitol polyglycidyl ether And a cross-linked product thereof, or (3) a cross-linked product of an organic binder and sorbitol polyglycidyl ether is attached.

本発明に係るフィルタ用濾紙では、圧力損失が500Pa以上であることが好ましい。圧力損失が大きい目が細かい濾紙に対して、ソルビトールポリグリシジルエーテルが有機系バインダーの水かき状膜の低減に効果的に働く。   In the filter paper for filters according to the present invention, the pressure loss is preferably 500 Pa or more. Sorbitol polyglycidyl ether works effectively to reduce the web-like film of the organic binder for filter paper with a large pressure loss and a fine eye.

本発明に係るフィルタ用濾紙では、前記ガラス繊維に、撥水剤が付着していてもよい。本発明に係るフィルタ用濾紙では、前記有機系バインダーが、エポキシ系樹脂、スチレン−ブタジエン樹脂、酢酸ビニル樹脂、エチレン−酢酸ビニル樹脂、ポリオレフィン樹脂、ポリビニルアルコール又はウレタン系樹脂であることが好ましい。 In the filter paper for filters which concerns on this invention, the water repellent may adhere to the said glass fiber. The filter paper filter according to the present invention, the organic binder is an epoxy resin, a styrene - butadiene resin, vinyl acetate resin, ethylene - vinyl acetate resins, polyolefin resins, is preferably a polyvinyl alcohol or a urethane resin.

本発明に係るフィルタ用濾紙の製造方法は、ガラス繊維を主体とするフィルタ用濾紙の製造方法において、前記ガラス繊維を含む濾材構成繊維が分散したスラリーを湿式抄紙して湿紙を得る工程と、湿式抄紙して得られた湿紙に、有機系バインダー及びソルビトールポリグリシジルエーテルを同時に又は別々に付着させる工程と、前記有機系バインダー及びソルビトールポリグリシジルエーテルを付着させた湿紙を乾燥させる工程と、を有することを特徴とする。   The method for producing filter paper according to the present invention is a process for producing a wet paper by wet papermaking of a slurry in which filter medium-constituting fibers containing the glass fibers are dispersed, in the method for producing filter paper mainly comprising glass fibers. A step of simultaneously or separately attaching an organic binder and sorbitol polyglycidyl ether to a wet paper web obtained by wet papermaking; and drying the wet paper onto which the organic binder and sorbitol polyglycidyl ether are attached; It is characterized by having.

本発明に係るフィルタ用濾紙の製造方法では、前記有機系バインダー及びソルビトールポリグリシジルエーテルを付着させた湿紙を乾燥させる工程において、前記有機系バインダーとソルビトールポリグリシジルエーテルとが架橋する形態を包含する。   In the method for producing filter paper for filters according to the present invention, in the step of drying the wet paper on which the organic binder and sorbitol polyglycidyl ether are attached, the organic binder and sorbitol polyglycidyl ether crosslink. .

本発明に係るフィルタ用濾紙の製造方法では、前記湿紙が乾燥する前に、該湿紙に前記有機系バインダー及びソルビトールポリグリシジルエーテルを付着させることが好ましい。十分な効果が得られる。   In the method for producing filter paper according to the present invention, the organic binder and sorbitol polyglycidyl ether are preferably adhered to the wet paper before the wet paper is dried. Sufficient effect is obtained.

本発明に係るフィルタ用濾紙の製造方法では、前記有機系バインダーに対するソルビトールポリグリシジルエーテルの付着量の割合は0.2〜20質量%であることが好ましい。この範囲において、配合量に応じた効果が得られる。   In the method for producing filter paper according to the present invention, the ratio of the adhesion amount of sorbitol polyglycidyl ether to the organic binder is preferably 0.2 to 20% by mass. In this range, an effect according to the compounding amount is obtained.

本発明に係るフィルタ用濾紙の製造方法では、前記有機系バインダーの前記濾材構成繊維に対する付着量の割合は、乾燥質量で、2〜10質量%であることが好ましい。有機系バインダーの水かき状膜の形成を抑えるとともに、濾材の十分な強度が確保できる。本発明に係るフィルタ用濾紙の製造方法では、前記有機系バインダーが、エポキシ系樹脂、スチレン−ブタジエン樹脂、酢酸ビニル樹脂、エチレン−酢酸ビニル樹脂、ポリオレフィン樹脂、ポリビニルアルコール又はウレタン系樹脂のラテックス又は溶液であることが好ましい。 In the method of manufacturing the filter paper for a filter according to the present invention, the ratio of the adhesion amount of the organic binder to the filter medium constituting fiber is preferably 2 to 10% by mass on a dry basis. While suppressing formation of the web-like film of an organic type binder, sufficient strength of a filter medium is securable. In the method for producing filter paper according to the present invention, the organic binder is a latex or solution of an epoxy resin, a styrene-butadiene resin, a vinyl acetate resin, an ethylene-vinyl acetate resin, a polyolefin resin, a polyvinyl alcohol or a urethane resin. Is preferred.

本発明のフィルタ用濾紙は、現行濾紙に比べ、濾過抵抗を増加させずに、エアフィルタや液体フィルタとしての濾過効率が向上したフィルタ用濾紙を提供できる。   The filter paper of the present invention can provide a filter paper with improved filtration efficiency as an air filter or a liquid filter without increasing the filtration resistance as compared with the current filter papers.

次に本発明について実施形態を示して詳細に説明するが、本発明はこれらの記載に限定して解釈されない。本発明の効果を奏する限り、実施形態は種々の変形をしてもよい。   EXAMPLES The present invention will next be described in detail by way of embodiments, which should not be construed as limiting the present invention. The embodiment may be variously modified as long as the effects of the present invention are exhibited.

本実施形態に係るフィルタ用濾紙は、ガラス繊維を主体とするフィルタ用濾紙において、ガラス繊維に、(1)有機系バインダー及びソルビトールポリグリシジルエーテル、(2)有機系バインダー、ソルビトールポリグリシジルエーテル及びこれらの架橋体、又は、(3)有機系バインダーとソルビトールポリグリシジルエーテルとの架橋体、が付着している。   The filter paper for filters according to the present embodiment is a filter paper mainly composed of glass fibers, which comprises (1) an organic binder and sorbitol polyglycidyl ether, (2) an organic binder, sorbitol polyglycidyl ether, and the like to glass fiber. Or a crosslinked product of (3) an organic binder and sorbitol polyglycidyl ether.

本発明のフィルタ用濾紙で用いられるソルビトールポリグリシジルエーテルは分子式C183010、分子量406.43の多官能エポキシ化合物である。ソルビトールポリグリシジルエーテルは反応性・水溶性に優れていることから、水溶性樹脂の架橋剤・不溶化剤、合成樹脂の改質剤、接着向上剤などに使用されている。 The sorbitol polyglycidyl ether used in the filter paper for filters of the present invention is a polyfunctional epoxy compound having a molecular formula C 18 H 30 O 10 and a molecular weight of 406.43. Sorbitol polyglycidyl ether is used as a crosslinker / insolubilizer for water-soluble resins, a modifier for synthetic resins, an adhesion improver, etc. because of its excellent reactivity and water solubility.

本発明は、このソルビトールポリグリシジルエーテルを、フィルタ用濾紙を構成するガラス繊維に付着させることにより、濾過性能が向上した新規な濾材の製造を可能とする。   The present invention makes it possible to produce a novel filter medium with improved filtration performance by attaching the sorbitol polyglycidyl ether to the glass fibers constituting the filter paper for filter.

ソルビトールポリグリシジルエーテルは、濾紙構成繊維表面と有機系バインダー分子との間あるいは有機系バインダー分子と有機系バインダー分子との間を架橋する働きをする。結果的に繊維どうしの結合をより強固にするため強度物性を大きく向上させる働きを持つ。従来のフィルタ用濾紙では繊維とバインダー分子との間の結合に関与しないバインダーが繊維間に水かき状膜を形成して濾材の目をふさぎ、これが濾過抵抗の増加及び濾過効率の低下を引き起こしている。しかし、ソルビトールポリグリシジルエーテルはより効果的に繊維とバインダー分子との間、あるいはバインダー分子とバインダー分子との間を三次元的に架橋するため、濾材の目を塞ぐような水かき状膜が減り、結果的に濾過抵抗の増加を防ぎ、濾過効率が高まるものと考えられる。したがって、ガラス繊維への付着形態は、(1)有機系バインダー及びソルビトールポリグリシジルエーテル、(2)有機系バインダー、ソルビトールポリグリシジルエーテル及びこれらの架橋体、又は、(3)有機系バインダーとソルビトールポリグリシジルエーテルとの架橋体、があるが、架橋体を含む形態が好ましい。   Sorbitol polyglycidyl ether functions to crosslink between the surface of the filter paper fiber and the organic binder molecule, or between the organic binder molecule and the organic binder molecule. As a result, it has a function to greatly improve the strength property in order to strengthen the bonding between fibers. In the conventional filter paper, the binder which does not participate in the binding between the fibers and the binder molecules forms a web-like membrane between the fibers and blocks the filter medium, which causes an increase in filtration resistance and a decrease in filtration efficiency. . However, sorbitol polyglycidyl ether more effectively crosslinks between the fiber and the binder molecule or between the binder molecule and the binder molecule in a three-dimensional manner, thereby reducing the web-like film which blocks the filter medium, As a result, it is considered that an increase in filtration resistance is prevented and the filtration efficiency is enhanced. Therefore, the adhesion form to glass fiber is (1) organic binder and sorbitol polyglycidyl ether, (2) organic binder, sorbitol polyglycidyl ether and crosslinked products thereof, or (3) organic binder and sorbitol poly Although there are cross-linked products with glycidyl ether, a form containing the cross-linked product is preferred.

濾材中において、有機系バインダーに対するソルビトールポリグリシジルエーテルの付着量の割合は0.2〜20質量%が好ましく、1〜10質量%がより好ましい。0.2質量%未満ではその効果が少なく、20質量%を超えると添加に見合った以上の効果が期待されずコスト高となる。   In a filter medium, 0.2-20 mass% is preferable, and, as for the ratio of the adhesion amount of sorbitol polyglycidyl ether with respect to an organic type binder, 1-10 mass% is more preferable. If the amount is less than 0.2% by mass, the effect is small, and if the amount is more than 20% by mass, the effect more than the addition to the addition is not expected and the cost increases.

また、ソルビトールポリグリシジルエーテルは単独で濾材構成繊維(以降、基材ともいう。)に使用しても濾過効率向上には効果がなく、有機系バインダーを併用することが必要である。ここで、使用される有機系バインダーとしては、通常濾材に使用しているアクリル酸エステル系樹脂、エポキシ系樹脂、スチレン−ブタジエン樹脂、酢酸ビニル樹脂、エチレン−酢酸ビニル樹脂、ポリオレフィン樹脂、ポリビニルアルコール、ウレタン系樹脂のラテックスまたは溶液を用いることが出来、基材に対する有機系バインダーの付着量の割合は好ましくは2質量%以上10質量%以下であり、さらに好ましくは3質量%以上7質量%以下である。2質量%より少ないと濾紙としての充分な強度が得られず、10質量%より多いとバインダーの水かき状膜が形成されやすくなり、本発明のソルビトールポリグリシジルエーテルの付着効果が低くなる。濾紙の強度については、エアフィルタ用濾紙ではMILスペックMIL−F−51079Cに示される引張強さが縦方向で0.44kN/m以上、横方向で0.35kN/m以上であることが好ましい。液体用濾紙では特に示される強度は無いが、実用強度以上を有することが必要である。   Further, even if sorbitol polyglycidyl ether is used alone as a filter medium-constituting fiber (hereinafter also referred to as a base material), there is no effect to improve the filtration efficiency, and it is necessary to use an organic binder in combination. Here, as the organic binder to be used, an acrylic ester resin, an epoxy resin, a styrene-butadiene resin, a vinyl acetate resin, an ethylene-vinyl acetate resin, a polyolefin resin, a polyvinyl alcohol, which is usually used for a filter medium A latex or solution of a urethane resin can be used, and the ratio of the adhesion amount of the organic binder to the substrate is preferably 2% by mass to 10% by mass, and more preferably 3% by mass to 7% by mass. is there. When the amount is less than 2% by mass, sufficient strength as filter paper can not be obtained, and when the amount is more than 10% by mass, a web-like film of a binder is easily formed, and the adhesion effect of the sorbitol polyglycidyl ether of the present invention becomes low. As for the strength of the filter paper, in the case of the filter paper for air filter, it is preferable that the tensile strength shown in MIL spec MIL-F-51079C is 0.44 kN / m or more in the longitudinal direction and 0.35 kN / m or more in the transverse direction. There is no particular strength shown in the case of liquid filter paper, but it is necessary to have a practical strength or higher.

本実施形態のフィルタ用濾紙をエアフィルタ用に使用する場合、要求に応じて、さらに撥水剤を付与してもその効果は変わりなく発揮される。ここで、撥水剤は一般に用いられるフッ素系撥水剤、ワックス系撥水剤、アルキルケテンダイマーあるいはこれら撥水剤を混合したものを使用することができる。濾材中において、有機系バインダーに対する撥水剤の付着量の割合は、1〜40質量%が好ましく、3〜20質量%がより好ましい。1質量%未満では十分な撥水性が得られにくく、40質量%を超えると濾材強度の低下を引き起こすおそれがある。   In the case of using the filter paper of the present embodiment for an air filter, even if a water repellent is further added according to the request, the effect is exhibited without change. Here, as the water repellent, a generally used fluorine-based water repellent, wax-based water repellent, alkyl ketene dimer or a mixture of these water repellents can be used. 1-40 mass% is preferable, and, as for the ratio of the adhesion amount of the water repellent with respect to the organic type binder in a filter medium, 3-20 mass% is more preferable. If the amount is less than 1% by mass, it is difficult to obtain sufficient water repellency, and if it exceeds 40% by mass, the strength of the filter medium may be reduced.

本実施形態で主体繊維として使用するのは平均繊維径0.2〜20μmのガラス繊維である。ガラス繊維には、グラスウールとチョップドガラス繊維とがある。グラスウールは、火焔延伸法やロータリー法で製造されるウール状のガラス繊維であり、繊維径は0.2〜6μm程度である。また、チョップドガラス繊維は溶融紡糸で得られたガラス糸を3〜20mm程度の繊維長に揃えて断裁されたもので、繊維径は6μm〜20μm程度である。要求されるフィルタ濾紙の濾過性能やその他物性に応じて、種々の繊維径を有するガラス繊維の中から適宜選定することができる。グラスウール単独、チョップドガラス繊維単独、又はグラスウールとチョップドガラス繊維との混合の形態がある。ガラス組成としては、フィルタ用途の大半はボロシリケートガラスであり、この中には耐酸性を有するCガラスや電気絶縁性を有するEガラス(無アルカリガラス)も含まれる。また、エアフィルタ分野で、半導体工程などにおけるボロン汚染を防止する目的で、ローボロンガラス繊維やシリカガラス繊維を使用することもできる。なお、本実施形態における主体繊維とは、全原料繊維配合の70質量%以上多くを占める繊維のことを示す。また、主体繊維以外に、目的によっては、有機合成繊維は、例えば、ビニロン主体繊維、アラミド繊維、炭素繊維、ポリエステル繊維、レーヨン繊維、ポリプロピレン繊維、ポリエステル繊維、アクリル繊維など、あるいは天然有機繊維、木材パルプ、コットンリンター繊維、麻繊維など、あるいはガラス繊維以外の無機繊維、例えばロックウール、アルミナ繊維、シリカ−アルミナ繊維などの配合も可能である。   In the present embodiment, glass fibers having an average fiber diameter of 0.2 to 20 μm are used as main fibers. Glass fibers include glass wool and chopped glass fibers. Glass wool is a wool-like glass fiber manufactured by a flame drawing method or a rotary method, and the fiber diameter is about 0.2 to 6 μm. In addition, the chopped glass fiber is a glass fiber obtained by melt spinning and is cut with the fiber length of about 3 to 20 mm, and the fiber diameter is about 6 μm to 20 μm. According to the filtration performance and other physical properties of the filter paper required, it can be suitably selected from glass fibers having various fiber diameters. There is a form of glass wool alone, chopped glass fiber alone, or a mixture of glass wool and chopped glass fiber. As the glass composition, the majority of filter applications are borosilicate glass, and among these, C glass having acid resistance and E glass (alkali-free glass) having electrical insulation are included. In the field of air filters, low boron glass fibers and silica glass fibers can also be used for the purpose of preventing boron contamination in semiconductor processes and the like. In addition, the main fiber in this embodiment shows the thing of the fiber which occupies 70 mass% or more of all the raw material fiber combination. In addition to main fibers, organic synthetic fibers may be, for example, vinylon main fibers, aramid fibers, carbon fibers, polyester fibers, rayon fibers, polypropylene fibers, polyester fibers, acrylic fibers, etc., or natural organic fibers or wood, depending on the purpose. Blends of pulp, cotton linter fibers, hemp fibers, etc., or inorganic fibers other than glass fibers, such as rock wool, alumina fibers, silica-alumina fibers, etc., are also possible.

濾紙を構成するガラス繊維の繊維径を変えることにより、目の粗い濾紙から精密濾過用の目の細かい濾紙ができる。濾紙の目の粗さは、濾紙の平均孔径、通気度、圧力損失などで示すことができる。例えば、目の粗い濾紙の圧力損失は低く、目の細かい濾紙の圧力損失は高くなる。また、目の粗い濾紙の通気度は高く、目の細かい濾紙の通気度は低くなる。   By changing the fiber diameter of the glass fiber constituting the filter paper, fine filter paper for precision filtration can be made from coarse filter paper. The coarseness of the filter paper can be indicated by the average pore diameter, air permeability, pressure loss, etc. of the filter paper. For example, the pressure drop of coarse filter paper is low and the pressure drop of fine filter paper is high. Also, the air permeability of the coarse filter paper is high and the air permeability of the fine filter paper is low.

圧力損失が低い目の粗い濾紙から圧力損失の高い精密濾過用の目の細かい濾紙までのいずれにおいても、本発明のソルビトールポリグリシジルエーテルの付着効果はあるが、圧力損失500Pa以上の濾紙に対しより効果的であり、圧力損失1000Pa以上の濾紙に対しさらに効果的である。これは、圧力損失がより高い濾紙になるほど、目がより細かいため、有機系バインダーの水かき状膜により覆われやすくなるが、ソルビトールポリグリシジルエーテルがこの水かき状膜低減に効果的に働くためである。圧力損失の上限は、特に制限はないが、例えば3000Paである。   From the coarse filter paper with low pressure drop to the fine filter paper with high pressure drop for precision filtration, although there is the adhesion effect of the sorbitol polyglycidyl ether of the present invention, the filter paper with pressure loss of 500 Pa or more is better It is effective, and more effective for filter paper with a pressure drop of 1000 Pa or more. This is because as the filter paper with higher pressure loss becomes finer, it becomes easier to be covered with the web-like film of the organic binder, but the sorbitol polyglycidyl ether works effectively for the reduction of the web-like film. . The upper limit of the pressure loss is not particularly limited, and is, for example, 3000 Pa.

また本実施形態に係る濾材は以下の製造方法で得ることができる。すなわち、ガラス繊維を含む濾材構成繊維をパルパーなど用いて水中に分散させる。これら原料繊維の分散工程では分散性を良くするために、硫酸酸性でpH2〜4の範囲で調整する方法をとるが、pH中性で分散剤などの界面活性剤を使用しても良い。次にこのスラリーを抄紙機で湿式抄紙して湿紙を得る。   Moreover, the filter medium which concerns on this embodiment can be obtained with the following manufacturing methods. That is, filter medium-constituting fibers containing glass fibers are dispersed in water using a pulper or the like. In the dispersion process of these raw material fibers, in order to improve the dispersibility, a method of adjusting in pH 2 to 4 with sulfuric acid acidity is adopted, but a surfactant such as a dispersing agent may be used at pH neutrality. Next, this slurry is subjected to wet paper making with a paper machine to obtain wet paper.

次にこの湿紙に前述の有機系バインダー、ソルビトールポリグリシジルエーテル、必要に応じて撥水剤等を付着させ、その後乾燥させる方法である。湿紙を乾燥した後にソルビトールポリグリシジルエーテル化合物を付与してもその効果は低く、湿紙乾燥前に付与することが望ましい。有機系バインダー、ソルビトールポリグリシジルエーテル、撥水剤は、それぞれ単独で付着させても、これら薬剤を同時に付着させても、また、これら薬剤を混合した溶液を付着させても効果は全く同じである。   Next, the above-mentioned organic binder, sorbitol polyglycidyl ether, if necessary, a water repellent agent and the like are adhered to the wet paper, and then dried. The effect is low even if the sorbitol polyglycidyl ether compound is applied after drying the wet paper, and it is desirable to apply it before the wet paper is dried. Even if the organic binder, sorbitol polyglycidyl ether, and the water repellent are each deposited alone, or even when these agents are simultaneously deposited, the effect is the same even if a mixed solution of these agents is deposited. .

有機系バインダー、ソルビトールポリグリシジルエーテル、撥水剤などの付着液の付与方法としては特に限定されるものでないが、湿紙を付着液に浸漬する方法、湿紙にスプレーで吹き付ける方法、ロールに付着液を付着させ湿紙に転写する方法などが上げられる。乾燥方法としては、熱風乾燥機、ロールドライヤーなどを使用し、110〜150℃で乾燥することが望ましい。   There is no particular limitation on the method of applying the adhesion liquid such as organic binder, sorbitol polyglycidyl ether, water repellent, etc., but a method of immersing the wet paper in the adhesion liquid, a method of spraying on the wet paper, adhesion to the roll There is a method of adhering the liquid and transferring it to a wet paper. As a drying method, it is desirable to dry at 110 to 150 ° C. using a hot air drier, a roll drier or the like.

次に、実施例を挙げて、本発明をより具体的に説明するが、本発明はこれら実施例に限定されるものではない。また、例中の「部」及び「%」は、特に断らない限り「質量部」及び「質量%」を示す。   EXAMPLES The present invention will next be described in more detail by way of examples, which should not be construed as limiting the invention thereto. Moreover, unless otherwise indicated, "part" and "%" in an example show a "mass part" and "mass%."

(実施例1)
平均繊維径0.50μmのグラスウール63質量%(ジョンマンビル社製)、平均繊維径2.70μm(ジョンマンビル社製)のグラスウール32質量%、平均繊維径11μm、繊維長6mmのガラスチョップド繊維(オーエンスコーニング社製)5質量%を濃度0.5%、硫酸酸性pH2.5にてパルパーで離解し、次いで抄紙機にて抄紙して湿紙を得た。次いで、付着液組成としてポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.0037質量%(対バインダー0.2質量%)(商品名:SR−SEP、坂本薬品工業社製)の付着液を湿紙に付与し、その後130℃のドライヤーで乾燥し、目付70g/mで付着液成分の付着量の割合が6.10%の濾紙を得た。なお、付着液成分の付着量の割合の求め方は次のとおりである。まず基材の質量を求め、基材を電気炉で525℃、30分の条件で加熱して付着液成分を燃焼させ(ガラス繊維分は燃焼しない)、基材の燃焼前後の基材質量から求めた可燃物(%)を付着液成分の付着量の割合とした。以降の実施例及び比較例も同様とした。なお、付着液に含まれる各成分の付着量の割合は、付着液の各成分の含有比率に応じるものとして算出することができる。
Example 1
63% by mass of glass wool with an average fiber diameter of 0.50 μm (manufactured by Johnmanville), 32% by mass of glass wool with an average fiber diameter of 2.70 μm (manufactured by Johnman Building), 11 μm in average fiber diameter, 6 μm in fiber length 5% by mass (manufactured by Owens Corning Co., Ltd.) was deagglomerated with a pulper at a concentration of 0.5% and sulfuric acid acidity pH 2.5, followed by paper making with a paper machine to obtain a wet paper. Next, as an adhesion liquid composition, polyacrylic ester 1.85 mass% (trade name: biniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), sorbitol polyglycidyl ether 0.0037 mass% (against binder 0.2 mass%) (commodity Name: SR-SEP (Sakamoto Yakuhin Kogyo Co., Ltd.) adhesion liquid is applied to a wet paper, then dried with a dryer at 130 ° C, and the ratio of the adhesion amount of the adhesion liquid component is 6.10% at a basis weight of 70 g / m 2 Filter paper was obtained. In addition, how to obtain | require the ratio of the adhesion amount of an adhesion liquid component is as follows. First, the mass of the base material is determined, and the base material is heated in an electric furnace at 525 ° C. for 30 minutes to burn the adhering liquid component (glass fiber does not burn), and the base material mass before and after combustion of the base material The obtained combustible (%) was taken as the ratio of the adhesion amount of the adhesion liquid component. The same applies to the following examples and comparative examples. In addition, the ratio of the adhesion amount of each component contained in adhesion liquid can be calculated as a thing according to the content ratio of each component of adhesion liquid.

(実施例2)
実施例1において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.056質量%(対バインダー3質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が6.15%の濾紙を得た。
(Example 2)
The composition of the adhesive solution in Example 1 is 1.85% by mass of polyacrylic ester (trade name: Biniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.056% by mass of sorbitol polyglycidyl ether (3% by mass of binder) A filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.15% was obtained in the same manner as in Example 1 except that trade name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例3)
実施例1において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.093質量%(対バインダー5質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が6.20%の濾紙を得た。
(Example 3)
The composition of the adhesive solution in Example 1 is 1.85 mass% of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.093 mass% of sorbitol polyglycidyl ether (5 mass% of binder) A filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.20% was obtained in the same manner as in Example 1 except that trade name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例4)
実施例1において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.37質量%(対バインダー20質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が6.18%の濾紙を得た。
(Example 4)
The composition of the adhesive solution in Example 1 is as follows: 1.85 mass% of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.37 mass% of sorbitol polyglycidyl ether (20 mass% to binder) A filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.18% was obtained in the same manner as in Example 1 except that trade name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例5)
実施例1において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.56質量%(対バインダー30質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が6.02%の濾紙を得た。
(Example 5)
The composition of the adhesive solution in Example 1 is 1.85% by mass of polyacrylic ester (trade name: Biniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.56% by mass of sorbitol polyglycidyl ether (30% by mass of binder) A filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.02% was obtained in the same manner as in Example 1 except that trade name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例6)
実施例1において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.00093質量%(対バインダー0.05質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が6.26%の濾紙を得た。
(Example 6)
The composition of the adhesive solution in Example 1 is 1.85% by mass of polyacrylic ester (trade name: Viniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.00093% by mass of sorbitol polyglycidyl ether (relative to 0.05% by mass of binder) ) (Trade name: SR-SEP, manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.) In the same manner as in Example 1, a filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.26% was obtained .

(実施例7)
実施例1において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.056質量%(対バインダー3質量%)(商品名:SR−SEP、坂本薬品工業社製)、フッ素系撥水剤0.11質量%(対バインダー6質量%)(商品名:アサヒガードAG−E061、旭硝子社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が6.24%の濾紙を得た。
(Example 7)
The composition of the adhesive solution in Example 1 is 1.85% by mass of polyacrylic ester (trade name: Biniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.056% by mass of sorbitol polyglycidyl ether (3% by mass of binder) Brand name: SR-SEP, manufactured by Sakamoto Yakuhin Kogyo Co., Ltd., 0.11% by mass of a fluorine-based water repellent (against binder 6% by mass) (trade name: Asahi Guard AG-E061, manufactured by Asahi Glass Co., Ltd.) In the same manner as in Example 1, a filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.24% was obtained.

(実施例8)
実施例1において付着液組成を、ポリアクリル酸エステル3.08質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.092質量%(対バインダー3質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が9.80%の濾紙を得た。
(Example 8)
The composition of the adhesive liquid in Example 1 is 3.08 mass% of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.092 mass% of sorbitol polyglycidyl ether (3 mass% to binder) A filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 9.80% was obtained in the same manner as in Example 1 except that trade name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例9)
平均繊維径0.26μmのグラスウール20質量%(ジョンマンビル社製)、平均繊維径0.32μmのグラスウール50質量%(ジョンマンビル社製)平均繊維径2.70μm(ジョンマンビル社)のグラスウール25質量%、平均繊維径11μm、繊維長6mmのガラスチョップド繊維(オーエンスコーニング社製)5質量%を濃度0.5%、硫酸酸性pH2.5にてパルパーで離解し、次いで抄紙機にて抄紙して湿紙を得た。次いで、付着液組成としてポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.0037質量%(対バインダー0.2質量%)(商品名:SR−SEP、坂本薬品工業社製)の付着液を湿紙に付与し、その後130℃のドライヤーで乾燥し、目付70g/mで付着液成分の付着量の割合が6.06%の濾紙を得た。
(Example 9)
20% by mass of glass wool with an average fiber diameter of 0.26 μm (manufactured by Johnman Building), 50% by mass of glass wool with an average fiber diameter of 0.32 μm (manufactured by Johnman Building), an average fiber diameter of 2.70 μm (Johnman Building) 5% by mass of glass chopped fiber (manufactured by Owens Corning Co., Ltd.) of 25% by mass of glass wool with an average fiber diameter of 11 μm and a fiber length of 6 mm is deagglomerated with a pulper at a concentration of 0.5% sulfuric acid pH 2.5 and then with a paper machine Papermaking gave a wet paper. Next, as an adhesion liquid composition, polyacrylic ester 1.85 mass% (trade name: biniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), sorbitol polyglycidyl ether 0.0037 mass% (against binder 0.2 mass%) (commodity Name: SR-SEP (Sakamoto Yakuhin Kogyo Co., Ltd.) adhesion solution is applied to a wet paper, then dried with a dryer at 130 ° C, and the proportion of the adhesion amount of the adhesion liquid component is 6.06% at a basis weight of 70 g / m 2 Filter paper was obtained.

(実施例10)
実施例9において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.093質量%対バインダー5質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例9と同様にして目付70g/mで付着液成分の付着量の割合が6.11%の濾紙を得た。
(Example 10)
The composition of the adhesive solution in Example 9 is as follows: 1.85 mass% of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.093 mass% of sorbitol polyglycidyl ether to 5 mass% of binder) Name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.) In the same manner as in Example 9, a filter paper with a basis weight of 70 g / m 2 was used to obtain a filter paper with a ratio of the adhesion amount of the adhesion liquid component of 6.11%.

(実施例11)
実施例9において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.185質量%(対バインダー10質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例9と同様にして目付70g/mで付着液成分の付着量の割合が6.25%の濾紙を得た。
(Example 11)
In Example 9, the composition of the adhesive liquid is 1.85 mass% of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.185 mass% of sorbitol polyglycidyl ether (relative to 10 mass% of binder) A filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.25% was obtained in the same manner as in Example 9 except for using trade name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例12)
実施例9において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.093質量%(対バインダー5質量%)(商品名:CR−5L、DIC社製)とした以外は実施例9と同様にして目付70g/mで付着液成分の付着量の割合が6.14%の濾紙を得た。
(Example 12)
In Example 9, the composition of the adhesive liquid is 1.85 mass% of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.093 mass% of sorbitol polyglycidyl ether (5 mass% of binder) A filter paper with a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.14% was obtained in the same manner as in Example 9 except that trade name: CR-5L, manufactured by DIC Corporation).

(実施例13)
平均繊維径0.65μmのグラスウール63質量%(ジョンマンビル社製)、平均繊維径2.70μm(ジョンマンビル社製)のグラスウール32質量%、平均繊維径11μm、繊維長6mmのガラスチョップド繊維(オーエンスコーニング社製)5質量%を濃度0.5%、硫酸酸性pH2.5にてパルパーで離解し、次いで抄紙機にて抄紙して湿紙を得た。次いで、付着液組成としてポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.056質量%(対バインダー3質量%)(商品名:SR−SEP、坂本薬品工業社製)の付着液を湿紙に付与し、その後130℃のドライヤーで乾燥し、目付70g/mで付着液成分の付着量の割合が6.26%の濾紙を得た。
(Example 13)
63% by mass of glass wool with an average fiber diameter of 0.65 μm (made by John Manville), 32% by mass of glass wool with an average fiber diameter of 2.70 μm (made by John Manville), a glass chopped fiber with an average fiber diameter of 11 μm and a fiber length of 6 mm 5% by mass (manufactured by Owens Corning Co., Ltd.) was deagglomerated with a pulper at a concentration of 0.5% and sulfuric acid acidity pH 2.5, followed by paper making with a paper machine to obtain a wet paper. Subsequently, polyacrylic acid ester 1.85 mass% (brand name: Binibran 2680, Nisshin Chemical Industry Co., Ltd. make), sorbitol polyglycidyl ether 0.056 mass% (against binder 3 mass%) (brand name :) as adhesion liquid composition. SR-SEP (Sakamoto Yakuhin Kogyo Co., Ltd.) adhesion solution is applied to a wet paper, then dried with a dryer at 130 ° C., and the basis weight 70 g / m 2 of filter paper with a ratio of adhesion amount of adhesion liquid component of 6.26% I got

(実施例14)
実施例1において付着液組成を、ポリアクリル酸エステル3.95質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.119質量%(対バインダー3質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が12.3%の濾紙を得た。
(Example 14)
The composition of the adhesive liquid in Example 1 was 3.95% by mass of polyacrylic ester (trade name: Biniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.119% by mass of sorbitol polyglycidyl ether (3% by mass of binder) A filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 12.3% was obtained in the same manner as in Example 1 except that trade name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例15)
実施例1において付着液組成を、エポキシ樹脂1.85質量%(商品名:エピクロン850、DIC社製)、ソルビトールポリグリシジルエーテル0.093質量%(対バインダー5質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が6.00%の濾紙を得た。
(Example 15)
The composition of the adhesive liquid in Example 1 is as follows: 1.85 mass% of epoxy resin (trade name: Epiclon 850, manufactured by DIC), 0.093 mass% of sorbitol polyglycidyl ether (5 mass% to binder) (trade name: SR-) A filter paper with a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 6.00% was obtained in the same manner as in Example 1 except that SEP was manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例16)
実施例1において付着液組成を、ポリアクリル酸エステル0.62質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.031質量%(対バインダー5質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が2.11%の濾紙を得た。
(Example 16)
The composition of the adhesive solution in Example 1 is 0.62% by mass of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.031% by mass of sorbitol polyglycidyl ether (relative to 5% by mass of binder) A filter paper having a basis weight of 70 g / m 2 and a ratio of an adhesion amount of an adhesion liquid component of 2.11% was obtained in the same manner as in Example 1 except that trade name: SR-SEP (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.).

(実施例17)
平均繊維径0.50μmのグラスウール63質量%(ジョンマンビル社製)、平均繊維径2.70μm(ジョンマンビル社製)のグラスウール37質量%を濃度0.5%、硫酸酸性pH2.5にてパルパーで離解し、次いで抄紙機にて抄紙して湿紙を得た。次いで、付着液組成としてポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.056質量%(対バインダー3.0質量%)(商品名:SR−SEP、坂本薬品工業社製)の付着液を湿紙に付与し、その後130℃のドライヤーで乾燥し、目付70g/mで付着液成分の付着量の割合が6.03%の濾紙を得た。
(Example 17)
63% by mass of glass wool with an average fiber diameter of 0.50 μm (made by John Manville), 37 mass% of glass wool with an average fiber diameter of 2.70 μm (made by John Manville) at a concentration of 0.5%, sulfuric acid pH 2.5 The mixture was disintegrated with a pulper and then made into paper by a paper machine to obtain wet paper. Next, as an adhesion liquid composition, polyacrylic ester 1.85 mass% (trade name: Binibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), sorbitol polyglycidyl ether 0.056 mass% (against binder 3.0 mass%) (commodity Name: SR-SEP (Sakamoto Yakuhin Kogyo Co., Ltd.) adhesion solution is applied to a wet paper, then dried with a dryer at 130 ° C, and the ratio of the adhesion amount of the adhesion liquid component is 6.03% at a basis weight of 70 g / m 2 Filter paper was obtained.

(実施例18)
平均繊維径11μm、繊維長6mmのガラスチョップド繊維(オーエンスコーニング社製)100質量%を濃度0.5%、硫酸酸性pH2.5にてパルパーで離解し、次いで抄紙機にて抄紙して湿紙を得た。次いで、付着液組成としてポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.056質量%(対バインダー3.0質量%)(商品名:SR−SEP、坂本薬品工業社製)の付着液を湿紙に付与し、その後130℃のドライヤーで乾燥し、目付70g/mで付着液成分の付着量の割合が7.07%の濾紙を得た。
(Example 18)
100% by mass of a glass chopped fiber (manufactured by Owens Corning Co., Ltd.) having an average fiber diameter of 11 μm and a fiber length of 6 mm is deaggregated with a pulper at a concentration of 0.5% and sulfuric acid acidity pH 2.5, I got Next, as an adhesion liquid composition, polyacrylic ester 1.85 mass% (trade name: Binibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), sorbitol polyglycidyl ether 0.056 mass% (against binder 3.0 mass%) (commodity Name: SR-SEP (Sakamoto Yakuhin Kogyo Co., Ltd.) adhesion solution is applied to a wet paper, then dried with a dryer at 130 ° C, and the ratio of the adhesion amount of the adhesion liquid component is 7.07% at 70 g / m 2 of fabric weight Filter paper was obtained.

(実施例19)
平均繊維径0.50μmのグラスウール63質量%(ジョンマンビル社製)、平均繊維径2.70μm(ジョンマンビル社製)のグラスウール32質量%、平均繊維径11μm、繊維長6mmのガラスチョップド繊維(オーエンスコーニング社製)5質量%を濃度0.5%、硫酸酸性pH2.5にてパルパーで離解し、次いで抄紙機にて抄紙して湿紙を得た。次いで、付着液組成としてポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)の付着液を湿紙に付与し、次にソルビトールポリグリシジルエーテル0.056質量%(対バインダー3.0質量%)(商品名:SR−SEP、坂本薬品工業社製)の付着液を湿紙に付与して、その後130℃のドライヤーで乾燥し、目付70g/mで付着液成分の付着量の割合が6.12%の濾紙を得た。
(Example 19)
63% by mass of glass wool with an average fiber diameter of 0.50 μm (manufactured by Johnmanville), 32% by mass of glass wool with an average fiber diameter of 2.70 μm (manufactured by Johnman Building), 11 μm in average fiber diameter, 6 μm in fiber length 5% by mass (manufactured by Owens Corning Co., Ltd.) was deagglomerated with a pulper at a concentration of 0.5% and sulfuric acid acidity pH 2.5, followed by paper making with a paper machine to obtain a wet paper. Then, an adhesion liquid of 1.85% by mass of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.) as an adhesion liquid composition is applied to a wet paper, and then 0.056% by mass of sorbitol polyglycidyl ether An adhesion solution of (3.0 mass% to binder) (trade name: SR-SEP, manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.) is applied to a wet paper and then dried with a dryer at 130 ° C. to adhere at a basis weight of 70 g / m 2 The ratio of the adhesion amount of a liquid component obtained the filter paper of 6.12%.

(実施例20)
平均繊維径0.50μmのグラスウール63質量%(ジョンマンビル社製)、平均繊維径2.70μm(ジョンマンビル社製)のグラスウール32質量%、平均繊維径11μm、繊維長6mmのガラスチョップド繊維(オーエンスコーニング社製)5質量%を濃度0.5%、硫酸酸性pH2.5にてパルパーで離解し、次いで抄紙機にて抄紙して湿紙を得て、この湿紙を130℃のドライヤーで乾燥して乾紙を得た。次いで、付着液組成としてポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、ソルビトールポリグリシジルエーテル0.056質量%(対バインダー3.0質量%)(商品名:SR−SEP、坂本薬品工業社製)の付着液を乾紙に付与して、その後130℃のドライヤーで乾燥し、目付70g/mで付着液成分の付着量の割合が6.08%の濾紙を得た。
Example 20
63% by mass of glass wool with an average fiber diameter of 0.50 μm (manufactured by Johnmanville), 32% by mass of glass wool with an average fiber diameter of 2.70 μm (manufactured by Johnman Building), 11 μm in average fiber diameter, 6 μm in fiber length 5% by mass (manufactured by Owens Corning Co., Ltd.) is deaggregated with a pulper at a concentration of 0.5% and sulfuric acid pH 2.5 with a pulper, and then made into a wet paper by a paper machine, and the wet paper is a dryer at 130 ° C. And dried to obtain a dry paper. Next, as an adhesion liquid composition, polyacrylic ester 1.85 mass% (trade name: Binibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), sorbitol polyglycidyl ether 0.056 mass% (against binder 3.0 mass%) (commodity Name: SR-SEP (Sakamoto Yakuhin Kogyo Co., Ltd.) adhesion solution is applied to dry paper and then dried with a dryer at 130 ° C, and the ratio of the adhesion amount of the adhesion liquid component is 6.08 at a basis weight of 70 g / m 2 % Filter paper was obtained.

(比較例1)
平均繊維径0.50μmのグラスウール63質量%(ジョンマンビル社製)、平均繊維径2.70μm(ジョンマンビル社製)のグラスウール32質量%、平均繊維径11μm、繊維長6mmのガラスチョップド繊維(オーエンスコーニング社製)5質量%を濃度0.5%、硫酸酸性pH2.5にてパルパーで離解し、次いで抄紙機にて抄紙して湿紙を得た。次いで、付着液組成としてポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)のみの付着液を湿紙に付与し、その後130℃のドライヤーで乾燥し、目付70g/mで付着液成分の付着量の割合が6.20%の濾紙を得た。
(Comparative example 1)
63% by mass of glass wool with an average fiber diameter of 0.50 μm (manufactured by Johnmanville), 32% by mass of glass wool with an average fiber diameter of 2.70 μm (manufactured by Johnman Building), 11 μm in average fiber diameter, 6 μm in fiber length 5% by mass (manufactured by Owens Corning Co., Ltd.) was deagglomerated with a pulper at a concentration of 0.5% and sulfuric acid acidity pH 2.5, followed by paper making with a paper machine to obtain a wet paper. Then, an adhesion liquid made of only 1.85% by mass of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.) as an adhesion liquid composition is applied to a wet paper, and then dried with a dryer at 130 ° C. The ratio of the adhesion amount of adhesion liquid component obtained the filter paper of 6.20% at 70 g / m < 2 >.

(比較例2)
比較例1において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)、フッ素系撥水剤0.11質量%(対バインダー6質量%)(商品名:アサヒガードAG−E061、旭硝子社製)とした以外は比較例1と同様にして目付70g/mで付着液成分の付着量の割合が5.94%の濾紙を得た。
(Comparative example 2)
The composition of the adhesive liquid in Comparative Example 1 is 1.85 mass% of polyacrylic ester (trade name: Viniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.), 0.11 mass% of fluorine-based water repellent (relative to 6 mass% of binder) A filter paper with a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 5.94% was obtained in the same manner as in Comparative Example 1 except that (trade name: Asahi Guard AG-E061, manufactured by Asahi Glass Co., Ltd.).

(比較例3)
実施例9において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)のみとした以外は実施例9と同様にして目付70g/mで付着液成分の付着量の割合が6.06%の濾紙を得た。
(Comparative example 3)
The coating weight was 70 g / m 2 in the same manner as in Example 9 except that the adhesive liquid composition in Example 9 was changed to only 1.85% by mass of polyacrylic ester (trade name: Viniblanc 2680, manufactured by Nisshin Chemical Industry Co., Ltd.). The ratio of the adhesion amount of the adhesion liquid component obtained the filter paper of 6.06%.

(比較例4)
実施例13において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)のみとした以外は実施例13と同様にして目付70g/mで付着液成分の付着量の割合が6.19% の濾紙を得た。
(Comparative example 4)
The coating weight was 70 g / m 2 in the same manner as in Example 13 except that the adhesive liquid composition in Example 13 was changed to only 1.85% by mass of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.). A filter paper with a ratio of the adhesion amount of the adhesion liquid component of 6.19% was obtained.

(比較例5)
実施例1において付着液組成を、ソルビトールポリグリシジルエーテル0.056質量%(対基材0.30質量%)(商品名:SR−SEP、坂本薬品工業社製)とした以外は実施例1と同様にして目付70g/mで付着液成分の付着量の割合が0.30%の濾紙を得た。
(Comparative example 5)
Example 1 and Example 1 except that the adhesion liquid composition is 0.056% by mass of sorbitol polyglycidyl ether (relative to base material 0.30% by mass) (trade name: SR-SEP, manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.) Similarly, a filter paper having a basis weight of 70 g / m 2 and a ratio of the adhesion amount of the adhesion liquid component of 0.30% was obtained.

(比較例6)
実施例18において付着液組成を、ポリアクリル酸エステル1.85質量%(商品名:ビニブラン2680、日信化学工業社製)のみとした以外は実施例18と同様にして目付70g/mで付着液成分の付着量の割合が7.03% の濾紙を得た。
(Comparative example 6)
The coating weight was 70 g / m 2 in the same manner as in Example 18 except that the adhesive liquid composition in Example 18 was changed to only 1.85% by mass of polyacrylic ester (trade name: Vinibran 2680, manufactured by Nisshin Chemical Industry Co., Ltd.). A filter paper with a ratio of adhesion amount of adhesion liquid component of 7.03% was obtained.

実施例および比較例において得た濾材の評価は、次に示す方法を用いて行った。   The evaluation of the filter media obtained in Examples and Comparative Examples was carried out using the following method.

圧力損失は、有効面積100cmの濾材に、空気が面風速5.3cm/秒で通過するときの差圧としてマノメーターを用いて測定した。 The pressure drop was measured on a filter medium having an effective area of 100 cm 2 using a manometer as a differential pressure when air passes at a surface air velocity of 5.3 cm / sec.

0.10−0.15μm透過率は、有効面積100cmの濾材に、ラスキンノズルで発生させたPAO粒子を含む空気が面風速5.3cm/秒で通過するときの上流及び下流のPAO粒子個数を、レーザーパーティクルカウンター(KC−18、リオン社製)を用いて測定し、その個数値から計算して求めた。なお、対象粒子径は、0.10〜0.15μmとした。 The 0.10-0.15 μm transmittance is the number of upstream and downstream PAO particles when air containing PAO particles generated by the Raskin nozzle passes at a surface velocity of 5.3 cm / sec in a filter medium having an effective area of 100 cm 2 Was measured using a laser particle counter (KC-18, manufactured by Rion Co., Ltd.), and calculated from the number value. The target particle diameter is 0.10 to 0.15 μm.

スラリー濾過効率は、試験粒子(ポリッシングパウダーGC♯30000,新潟精機社製)をイオン交換水中で分散させた濃度100ppmの試験液を用い、有効面積17.3cmの濾材をフィルタホルダに固定して吸引瓶に取り付け、吸引濾過前後の試験液濁度について濁度測定器COH400(日本電色工業社製)を用いて測定した。スラリー濾過効率を以下の式(数1)より計算した。
(数1)スラリー濾過効率[%] = 濾液濁度[%]/試験液濁度[%]×100
なお、実施例7及び比較例2は撥水剤を配合している。撥水性の付与についてはエアフィルタ用濾紙のみが対象となるため、スラリー濾過効率は測定しなかった。
For slurry filtration efficiency, use a test solution with a concentration of 100 ppm in which test particles (polishing powder GC # 30000, manufactured by Niigata Seiki Co., Ltd.) are dispersed in ion exchange water, and fix a filter medium with an effective area of 17.3 cm 2 to the filter holder. The test solution was attached to a suction bottle, and the turbidity of the test solution before and after suction filtration was measured using a turbidity measuring device COH400 (manufactured by Nippon Denshoku Kogyo Co., Ltd.). The slurry filtration efficiency was calculated from the following equation (Equation 1).
(Equation 1) Slurry filtration efficiency [%] = filtrate turbidity [%] / test liquid turbidity [%] x 100
In Example 7 and Comparative Example 2, a water repellent is blended. The slurry filtration efficiency was not measured because only the filter paper for air filter was targeted for imparting water repellency.

引張強さは、JIS P 8113:2006「紙及び板紙−引張特性の試験方法−第2部:低速伸張法」に準拠して、万能試験機(オートグラフAGS−X、島津製作所社製)を用いて測定した。なお、濾紙の縦方向は、抄紙機の流れ方向、横方向は前記流れ方向の直角方向とした。   The tensile strength is a universal testing machine (Autograph AGS-X, manufactured by Shimadzu Corporation) in accordance with JIS P 8113: 2006 "Paper and paperboard-Test method of tensile properties-Part 2: Low speed elongation method". It measured using. The longitudinal direction of the filter paper is the flow direction of the paper machine, and the transverse direction is the direction perpendicular to the flow direction.

以上の試験の測定結果を表1及び表2に示す。   Tables 1 and 2 show the measurement results of the above tests.

Figure 0006527800
Figure 0006527800

Figure 0006527800
Figure 0006527800

実施例1から6に示すとおり、本発明の有機系バインダーにソルビトールポリグリシジルエーテルを付与した濾紙は、比較例1に比べ、濾紙の濾過抵抗を示す圧力損失が同等であるにも関わらず、エアフィルタとしての性能を示す0.10−0.15μm透過率が小さくなっており、また、液体フィルタとしても性能を示すスラリー濾過効率が大きくなっている。濾紙としての性能が向上していることが分る。   As shown in Examples 1 to 6, the filter paper obtained by adding sorbitol polyglycidyl ether to the organic binder of the present invention has air compared with Comparative Example 1 despite the fact that the pressure loss showing the filtration resistance of the filter paper is equal. The 0.10-0.15 μm transmittance, which indicates the performance as a filter, is small, and the slurry filtration efficiency, which is also a performance as a liquid filter, is large. It can be seen that the performance as filter paper is improved.

同様に、圧力損失の異なる実施例9から12や、実施例13においても、比較例3、比較例4に比べ、0.10−0.15μm透過率やスラリー濾過効率への効果が見られ、濾紙としての性能が向上していることが分り、圧力損失が高くなるほど向上効果が高いことが分る。   Similarly, in Examples 9 to 12 and Example 13 with different pressure loss, as compared with Comparative Example 3 and Comparative Example 4, the effect on the 0.10 to 0.15 μm permeability and the slurry filtration efficiency is observed. It is understood that the performance as filter paper is improved, and it is understood that the higher the pressure loss, the higher the improvement effect.

実施例7はエアフィルタとしての応用を前提に撥水剤を併用した例であるが、比較例2に比べて0.10−0.15μm透過率が小さくなっており、濾紙としての性能が向上していることが分る。   Example 7 is an example in which a water repellent is used in combination on the premise of application as an air filter, but the transmittance of 0.10 to 0.15 μm is smaller than that of Comparative Example 2, and the performance as filter paper is improved. I understand that I am doing.

実施例2、実施例8、実施例14及び実施例16は、有機系バインダーの付着量の割合の影響を見た例である。有機系バインダーの付着量の割合が10%程度までは、本発明の有機系バインダーにソルビトールポリグリシジルエーテルを付与した効果が0.10−0.15μm透過率、スラリー濾過効率に見られるが、12%程度まで有機系バインダーの付着量の割合が増大すると、付着量に見合った効果が得られないことが解る。   Example 2, Example 8, Example 14 and Example 16 are the examples which saw the influence of the ratio of the adhesion amount of an organic type binder. The effect of applying sorbitol polyglycidyl ether to the organic binder of the present invention is seen in the permeability of 0.10 to 0.15 μm and the slurry filtration efficiency until the ratio of the adhesion amount of the organic binder is about 10%. It can be understood that when the ratio of the adhesion amount of the organic binder is increased to about%, an effect corresponding to the adhesion amount can not be obtained.

実施例15は、有機系バインダーとしてエポキシ樹脂を用いた例である。ポリアクリル酸エステルを用いた実施例3と同様の性能が得られた。   Example 15 is an example using an epoxy resin as an organic binder. The same performance as in Example 3 using a polyacrylate was obtained.

実施例17は、ガラス繊維としてグラスウールだけを配合し、ガラスチョップド繊維を配合しなかった例である。ガラスチョップド繊維を配合した実施例3と同様の性能が得られた。実施例18は、ガラス繊維としてグラスウールだけを配合せずに、ガラスチョップド繊維のみを配合した例である。比較例6と比較すると、0.10−0.15μm透過率やスラリー濾過効率への効果が見られ、濾紙としての性能が向上していることが分る。   Example 17 is an example which blended only glass wool as glass fiber, and did not blend glass chopped fiber. The same performance as in Example 3 in which glass chopped fibers were blended was obtained. Example 18 is an example where only glass chopped fiber was blended without blending only glass wool as glass fiber. As compared with Comparative Example 6, the effect on the 0.10 to 0.15 μm transmittance and the slurry filtration efficiency can be seen, and it can be seen that the performance as a filter paper is improved.

実施例19は、ポリアクリル酸エステルを含有する付着液とソルビトールポリグリシジルエーテルを含有する付着液を用いて、別々に湿紙に付与した例である。ポリアクリル酸エステルとソルビトールポリグリシジルエーテルの両方を含有する付着液を用いた実施例2と比較すると、これら薬剤を混合した溶液を付着させた場合と、混合せずに別々に付着させた場合とでは、効果は全く同じであることが確認できた。   Example 19 is an example in which the adhesion liquid containing a polyacrylic acid ester and the adhesion liquid containing sorbitol polyglycidyl ether were separately applied to wet paper. As compared with Example 2 in which the adhesion liquid containing both polyacrylic ester and sorbitol polyglycidyl ether was used, the case where the mixed solution of these agents was attached and the case where they were separately attached without being mixed So we could confirm that the effect is exactly the same.

実施例20は、湿紙を乾紙としてから、付着液を付与した例である。湿紙に付着液を付与した例である実施例2と比較すると、0.10−0.15μm透過率やスラリー濾過効率への効果があまり大きくないことが分る。
Example 20 is an example in which the adhesion liquid is applied after the wet paper has been made into a dry paper. It can be seen that the effect on the 0.10-0.15 [mu] m transmittance and the slurry filtration efficiency is not very large as compared with Example 2 in which the adhesion liquid is applied to the wet paper.

Claims (12)

ガラス繊維を主体とするフィルタ用濾紙において、
前記ガラス繊維に、(1)有機系バインダー及びソルビトールポリグリシジルエーテル、(2)有機系バインダー、ソルビトールポリグリシジルエーテル及びこれらの架橋体、又は、(3)有機系バインダーとソルビトールポリグリシジルエーテルとの架橋体、が付着していることを特徴とするフィルタ用濾紙。
In filter paper made mainly of glass fiber,
In the glass fiber, (1) organic binder and sorbitol polyglycidyl ether, (2) organic binder, sorbitol polyglycidyl ether and crosslinked products thereof, or (3) crosslinking of organic binder and sorbitol polyglycidyl ether Filter paper for filter characterized in that the body is attached.
圧力損失が500Pa以上であることを特徴とする請求項1に記載のフィルタ用濾紙。   The filter paper according to claim 1, wherein the pressure drop is 500 Pa or more. 前記ガラス繊維に、撥水剤が付着していることを特徴とする請求項1又は2に記載のフィルタ用濾紙。   The filter paper according to claim 1 or 2, wherein a water repellent agent is attached to the glass fiber. 前記有機系バインダーが、エポキシ系樹脂、スチレン−ブタジエン樹脂、酢酸ビニル樹脂、エチレン−酢酸ビニル樹脂、ポリオレフィン樹脂、ポリビニルアルコール又はウレタン系樹脂であることを特徴とする請求項1〜3のいずれか一つに記載のフィルタ用濾紙。 The organic binder is an epoxy resin, a styrene - butadiene resin, vinyl acetate resin, ethylene - vinyl acetate resins, polyolefin resins, any one of claims 1 to 3, wherein the polyvinyl alcohol or a urethane resin Filter paper described in 1). ガラス繊維を主体とするフィルタ用濾紙の製造方法において、
前記ガラス繊維を含む濾材構成繊維が分散したスラリーを湿式抄紙して湿紙を得る工程と、
湿式抄紙して得られた湿紙に、有機系バインダー及びソルビトールポリグリシジルエーテルを同時に又は別々に付着させる工程と、
前記有機系バインダー及びソルビトールポリグリシジルエーテルを付着させた湿紙を乾燥させる工程と、
を有することを特徴とするフィルタ用濾紙の製造方法。
In a method of producing filter paper mainly composed of glass fiber,
Wet-papering a slurry in which filter medium-constituting fibers including the glass fibers are dispersed to obtain a wet paper;
Attaching an organic binder and sorbitol polyglycidyl ether simultaneously or separately to the wet paper obtained by wet papermaking;
Drying the wet paper on which the organic binder and sorbitol polyglycidyl ether are attached;
A method of producing filter paper for a filter, comprising:
前記有機系バインダー及びソルビトールポリグリシジルエーテルを付着させた湿紙を乾燥させる工程において、前記有機系バインダーとソルビトールポリグリシジルエーテルとが架橋することを特徴とする請求項に記載のフィルタ用濾紙の製造方法。 The process for drying the wet paper on which the organic binder and the sorbitol polyglycidyl ether are adhered, the organic binder and the sorbitol polyglycidyl ether are cross-linked, the filter paper for the filter according to claim 5 being manufactured. Method. 前記湿紙が乾燥する前に、該湿紙に前記有機系バインダー及びソルビトールポリグリシジルエーテルを付着させることを特徴とする請求項又はに記載のフィルタ用濾紙の製造方法。 Wherein before the wet paper is dried, the manufacturing method of the filter paper filter of claim 5 or 6, characterized in that the deposition of the organic binder and sorbitol polyglycidyl ether wet web. 前記有機系バインダーに対するソルビトールポリグリシジルエーテルの付着量の割合は0.2〜20質量%であることを特徴とする請求項のいずれか一つに記載のフィルタ用濾紙の製造方法。 Method for producing filter paper filter according to any one of claims 5-7, wherein the ratio of the coating weight of sorbitol polyglycidyl ether with respect to the organic binder is 0.2 to 20 mass%. 前記有機系バインダーの前記濾材構成繊維に対する付着量の割合は、乾燥質量で、2〜10質量%であることを特徴とする請求項のいずれか一つに記載のフィルタ用濾紙の製造方法。 Ratio of coating weight for said filter media fibers constituting the organic binder on a dry weight, the production of filter paper for filter according to any one of claims 5-8, characterized in that 2-10 wt% Method. 湿式抄紙して得られた湿紙に、有機系バインダー及びソルビトールポリグリシジルエーテルに加えてさらに撥水剤を付着させることを特徴とする請求項のいずれか一つに記載のフィルタ用濾紙の製造方法。 The filter paper according to any one of claims 5 to 8 , characterized in that a water repellent is further adhered to the wet paper obtained by wet papermaking in addition to the organic binder and the sorbitol polyglycidyl ether. Manufacturing method. 前記有機系バインダー、ソルビトールポリグリシジルエーテル及び前記撥水剤の合計の前記濾材構成繊維に対する付着量の割合が、乾燥質量で、2〜10質量%であることを特徴とする請求項10に記載のフィルタ用濾紙の製造方法。 The organic binder, the proportion of adhesion amount with respect to the filter media fibers constituting the sum of sorbitol polyglycidyl ether and the water repellent, by dry weight, according to claim 10, characterized in that 2-10 wt% Method of manufacturing filter paper for filter. 前記有機系バインダーが、エポキシ系樹脂、スチレン−ブタジエン樹脂、酢酸ビニル樹脂、エチレン−酢酸ビニル樹脂、ポリオレフィン樹脂、ポリビニルアルコール又はウレタン系樹脂のラテックス又は溶液であることを特徴とする請求項11のいずれか一つに記載のフィルタ用濾紙の製造方法。 The organic binder is an epoxy resin, a styrene - butadiene resin, vinyl acetate resin, ethylene - vinyl acetate resins, polyolefin resins, claims 5 to 11, characterized in that a latex or solution of polyvinyl alcohol or a urethane resin The manufacturing method of the filter paper for filters as described in any one of these.
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