JP2016087498A - Electret filter medium - Google Patents

Electret filter medium Download PDF

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JP2016087498A
JP2016087498A JP2014221452A JP2014221452A JP2016087498A JP 2016087498 A JP2016087498 A JP 2016087498A JP 2014221452 A JP2014221452 A JP 2014221452A JP 2014221452 A JP2014221452 A JP 2014221452A JP 2016087498 A JP2016087498 A JP 2016087498A
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dielectric sheet
porous dielectric
electret filter
aqueous solution
filter material
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JP6565166B2 (en
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卓也 中澤
Takuya Nakazawa
卓也 中澤
増森 忠雄
Tadao Masumori
忠雄 増森
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Toyobo Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide an electret filter medium using a porous dielectric sheet made from a polyolefin resin that has been sufficiently and highly converted into an electret, including the inside.SOLUTION: In an electret filter medium, a value of O/C which is a molar ratio of an oxygen atom (O) and a carbon atom (C) on the surface of a porous dielectric sheet made from a polyolefin resin is 0.003-0.03.SELECTED DRAWING: None

Description

本発明は、気体中の微粒子の捕捉に用いられる改良されたエレクトレット濾過材に関する。   The present invention relates to an improved electret filter medium used for capturing fine particles in a gas.

多孔性誘電体シートをエレクトレット化する従来の技術として、水流噴霧荷電法等が挙げられる。   A conventional technique for electretizing a porous dielectric sheet includes a water spray charging method.

水の噴流または水滴流を多孔性誘電体シートに衝突させることによりエレクトレット化する方法が例えば特許文献1に開示されている。多孔性誘電体シートに衝突させる水としては、蒸留水、イオン交換水といったより純度の高い水を使用するのが好ましいとの記載がある。しかし、そのような高純度の水では、多孔性誘電体シートと水との接触による荷電効果は低く、多孔性誘電体シートを高度にエレクトレット化することはできない。   For example, Patent Document 1 discloses a method of electretizing a water jet or water droplet by colliding with a porous dielectric sheet. There is a description that it is preferable to use higher-purity water such as distilled water or ion-exchanged water as the water to collide with the porous dielectric sheet. However, such high-purity water has a low charging effect due to the contact between the porous dielectric sheet and water, and the porous dielectric sheet cannot be highly electretized.

非導電性シートに水と水溶性有機溶剤との混合溶液を付与し、次いで該非導電性シートを乾燥するエレクトレット加工品の製造方法について例えば特許文献2に開示されている。水と水溶性有機溶剤との混合溶液において、水としては、蒸留水、イオン交換水といったより純度の高い水を使用するのが好ましいとの記載があるが、そのような水では、非導電性シートと混合溶液との接触による荷電効果は低い。また、非導電性シートへの浸透性を高める目的で水溶性有機溶剤を混合しているため、非導電性シートと混合溶液との接触角が小さくなり、シート上の蓄積電荷が混合溶液中に流出しやすくなる。その結果、非導電性シートを高度にエレクトレット化できないという欠点を有する。   For example, Patent Document 2 discloses a method for manufacturing an electret processed product in which a mixed solution of water and a water-soluble organic solvent is applied to a non-conductive sheet, and then the non-conductive sheet is dried. In a mixed solution of water and a water-soluble organic solvent, there is a description that it is preferable to use higher-purity water such as distilled water or ion-exchanged water, but in such water, non-conductive The charging effect due to the contact between the sheet and the mixed solution is low. Moreover, since a water-soluble organic solvent is mixed for the purpose of increasing the permeability to the non-conductive sheet, the contact angle between the non-conductive sheet and the mixed solution is reduced, and the accumulated charge on the sheet is contained in the mixed solution It becomes easy to leak. As a result, there is a drawback that the non-conductive sheet cannot be highly electretized.

コロナ荷電処理を行った非導電性多孔性誘電体シートにpH7を超える水溶液を噴射し、次いで、乾燥するエレクトレット濾過材の製造方法が例えば特許文献3に開示されている。水を噴射する前にコロナ荷電処理を行い、表面に電荷を蓄積させるのが好ましいとの記載があるが、コロナ荷電処理で与えた電荷は水溶液の噴射により消失するという欠点がある。   For example, Patent Document 3 discloses a method for producing an electret filter material in which an aqueous solution exceeding pH 7 is sprayed onto a non-conductive porous dielectric sheet subjected to corona charging treatment, and then dried. There is a description that it is preferable to perform corona charging treatment before water is jetted to accumulate charges on the surface. However, there is a drawback that charges given by corona charging treatment are lost by jetting an aqueous solution.

上述のとおり、多孔性誘電体シートを用いたエレクトレット濾過材において、その内部まで十分に、かつ高度にエレクトレット化されたエレクトレット濾過材は見当たらないのが現状である。   As described above, in the electret filtering material using the porous dielectric sheet, there is no electret filtering material that is sufficiently electretized to the inside of the electret filtering material.

特表平9−501604号公報Japanese National Patent Publication No. 9-501604 特開2002−115177号公報JP 2002-115177 A 特開2004−66027号公報JP 2004-66027 A

本発明は上記従来の問題点を鑑みて、ポリオレフィン系樹脂からなる多孔性誘電体シートを用いたエレクトレット濾過材において、その内部まで十分に、かつ高度にエレクトレット化されたエレクトレット濾過材を提供することを課題とするものである。   In view of the above-mentioned conventional problems, the present invention provides an electret filtration material that is sufficiently electretized to a high degree in an electret filtration material using a porous dielectric sheet made of polyolefin resin. Is an issue.

本発明者らは上記課題を解決するため、鋭意研究した結果、遂に本発明を完成するに到った。すなわち本発明は、以下の通りである。
1.ポリオレフィン系樹脂からなる多孔性誘電体シート表面の酸素原子(O)と炭素原子(C)のモル比であるO/Cの値が0.003〜0.03であるエレクトレット濾過材。
2.多孔性誘電体シートがヒンダードフェノール系安定剤、硫黄系安定剤、リン系安定剤、脂肪酸金属塩、および結晶核剤から選ばれる少なくとも一種類の添加剤を含有し、その含有量が前記多孔性誘電体シート100重量部に対して0.01〜5重量部である上記1に記載のエレクトレット濾過材。
3.ポリオレフィン系樹脂からなる多孔性誘電体シートにオゾン酸化処理、液相酸化処理、およびプラズマ酸化処理から選ばれる少なくとも1つの処理を施した後、pHが7を超える水溶液を噴射し、乾燥させる上記1または2に記載のエレクトレット濾過材の製造方法。
As a result of intensive studies to solve the above problems, the present inventors have finally completed the present invention. That is, the present invention is as follows.
1. An electret filter material in which the value of O / C, which is the molar ratio of oxygen atoms (O) to carbon atoms (C) on the surface of a porous dielectric sheet made of a polyolefin-based resin, is 0.003 to 0.03.
2. The porous dielectric sheet contains at least one additive selected from a hindered phenol stabilizer, a sulfur stabilizer, a phosphorus stabilizer, a fatty acid metal salt, and a crystal nucleating agent, and the content thereof is the porous 2. The electret filter material according to 1 above, which is 0.01 to 5 parts by weight with respect to 100 parts by weight of the conductive dielectric sheet.
3. The porous dielectric sheet made of polyolefin resin is subjected to at least one treatment selected from ozone oxidation treatment, liquid phase oxidation treatment, and plasma oxidation treatment, and then sprayed with an aqueous solution having a pH exceeding 7, and dried. Or the manufacturing method of the electret filter material of 2.

本発明によるポリオレフィン系樹脂からなる多孔性誘電体シートを用いたエレクトレット濾過材は、そのシート表面に酸素原子を導入することにより、その内部まで高度にエレクトレット化されており、優れた濾過性能を付与できるという利点を有する。   The electret filter material using the porous dielectric sheet made of polyolefin resin according to the present invention is highly electretized by introducing oxygen atoms into the sheet surface, and provides excellent filtration performance. It has the advantage of being able to.

以下、本発明を詳細に説明する。本発明で使用するポリオレフィン系樹脂からなる多孔性誘電体シートとしては、繊維シート(例えば、織物、編物、不織布、またはこれらの複合体)、多孔フィルム(例えば、穴開きフィルム)、発泡体、またはこれらの複合体などがある。なかでも好ましくは、メルトブロー法により製造された極細繊維不織布である。極細繊維不織布は繊維表面積が大きいため、濾過材の粒子捕集効率が向上する。   Hereinafter, the present invention will be described in detail. Examples of the porous dielectric sheet made of a polyolefin resin used in the present invention include a fiber sheet (for example, a woven fabric, a knitted fabric, a nonwoven fabric, or a composite thereof), a porous film (for example, a perforated film), a foam, These complexes are included. Among them, an ultrafine fiber nonwoven fabric produced by a melt blow method is preferable. Since the ultrafine fiber nonwoven fabric has a large fiber surface area, the particle collection efficiency of the filter medium is improved.

ポリオレフィン系樹脂からなる多孔性誘電体シートは、一枚、または複数枚積層した構成であってもよい。また、シート強度を高めるためにスパンボンド不織布等の補強材を積層して使用してもよい。   The porous dielectric sheet made of a polyolefin-based resin may have a configuration in which one sheet or a plurality of sheets are laminated. Further, in order to increase the sheet strength, a reinforcing material such as a spunbond nonwoven fabric may be laminated and used.

ポリオレフィン系樹脂からなる多孔性誘電体シートの材質としては、一種類、または複数の種類の材質から構成されてもよいが、電荷保持の点から体積抵抗率1014Ωcm以上の材質を少なくとも一種類以上含むことが好ましい。多孔性誘電体シートが体積抵抗率1014Ωcm未満の材質のみで構成されていれば、電荷が蓄積しにくく、高度にエレクトレット化することが困難となり、濾過材の電荷寿命が極端に短くなってしまうという問題が生じる。ポリオレフィン系樹脂のなかでもポリプロピレンが好ましい。 The material of the porous dielectric sheet made of polyolefin-based resin may be composed of one kind or a plurality of kinds of materials, but at least one kind of material having a volume resistivity of 10 14 Ωcm or more from the viewpoint of charge retention. It is preferable to include the above. If the porous dielectric sheet is composed only of a material having a volume resistivity of less than 10 14 Ωcm, it is difficult to accumulate charges, making it highly difficult to make electrets, and the charge life of the filter medium becomes extremely short. Problem arises. Among polyolefin resins, polypropylene is preferable.

ポリオレフィン系樹脂からなる多孔性誘電体シートが、ポリプロピレンからなるメルトブロー不織布の場合、目付は5〜100g/m2が好ましく、10〜60g/m2がより好ましい。メルトブロー不織布を構成する繊維の平均繊維径は1〜20μmが好ましく、1〜10μmがより好ましい。 Porous dielectric sheet made of polyolefin resin, if the melt blown nonwoven fabric made of polypropylene, basis weight is preferably 5~100g / m 2, 10~60g / m 2 is more preferable. 1-20 micrometers is preferable and, as for the average fiber diameter of the fiber which comprises a melt blown nonwoven fabric, 1-10 micrometers is more preferable.

ポリオレフィン系樹脂からなる多孔性誘電体シート表面の酸素原子(O)と炭素原子(C)のモル比であるO/C比の値は0.003〜0.03であり、好ましくは0.003〜0.02、より好ましくは0.003〜0.015である。O/C比の値が0.003未満の場合、多孔性誘電体シートに電荷を捕捉できないため、十分にエレクトレット化できない。また、0.03を超える場合には、多孔性誘電体シートの親水性が増大し、水との長時間の接触により、多孔性誘電体シートに与えた電荷が消失する。   The O / C ratio, which is the molar ratio of oxygen atoms (O) to carbon atoms (C) on the surface of the porous dielectric sheet made of polyolefin resin, is 0.003 to 0.03, preferably 0.003. It is -0.02, More preferably, it is 0.003-0.015. When the value of the O / C ratio is less than 0.003, electric charges cannot be trapped in the porous dielectric sheet, so that it cannot be sufficiently electretized. On the other hand, when it exceeds 0.03, the hydrophilicity of the porous dielectric sheet increases, and the charge applied to the porous dielectric sheet disappears due to long-term contact with water.

ポリオレフィン系樹脂からなる多孔性誘電体シートにはヒンダードフェノール系安定剤、硫黄系安定剤、リン系安定剤、脂肪酸金属塩、および結晶核剤から選ばれる少なくとも一種類の添加剤を含有していることが好ましい。これら添加剤を含有することにより、多孔性誘電体シートのエレクトレット性が飛躍的に向上する。   The porous dielectric sheet made of polyolefin resin contains at least one additive selected from a hindered phenol stabilizer, a sulfur stabilizer, a phosphorus stabilizer, a fatty acid metal salt, and a crystal nucleating agent. Preferably it is. By containing these additives, the electret property of the porous dielectric sheet is dramatically improved.

ヒンダードフェノール系添加剤としては、特に限定されるわけではないが、ペンタエリスリチル−テトラキス[3−(3,5−ジ−t−ブチル−4−ヒドロキシフェニル)プロピオネート](Irganox1010、BASF社製)、オクタデシル−3−(3,5−ジ−t−ブチル−4−ヒドロキシフェニル)プロピオネート(Irganox1076、BASF社製)、トリス−(3,5−ジ−t−ブチル−4−ヒドロキシベンジル)−イソシアヌレイト(Irganox3114、BASF社製)、3,9−ビス−{2−[3−(3−t−ブチル−4−ヒドロキシ−5−メチルフェニル)−プロピオニルオキシ]−1,1−ジメチルエチル}−2,4,8,10−テトラオキサスピロ−[5,5]ウンデカン(スミライザーGA−80、住友化学社製)等が挙げられる。   The hindered phenol-based additive is not particularly limited, but pentaerythrityl-tetrakis [3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate] (Irganox 1010, manufactured by BASF) ), Octadecyl-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate (Irganox 1076, manufactured by BASF), tris- (3,5-di-t-butyl-4-hydroxybenzyl)- Isocyanurate (Irganox 3114, manufactured by BASF), 3,9-bis- {2- [3- (3-t-butyl-4-hydroxy-5-methylphenyl) -propionyloxy] -1,1-dimethylethyl } -2,4,8,10-tetraoxaspiro- [5,5] undecane (Sumilyzer GA-80 Sumitomo Chemical Co., Ltd.), and the like.

硫黄系安定剤としては、特に限定されるわけではないが、ジ−ラウリル−3,3−チオジプロピオン酸エステル(DLTDP)、ジ−ステアリル−3,3−チオジプロピオン酸エステル(DSTDP)等が挙げられる。   Although it does not necessarily limit as a sulfur type stabilizer, Di-lauryl-3,3-thiodipropionic acid ester (DLTDP), di-stearyl-3,3-thiodipropionic acid ester (DSTDP), etc. Is mentioned.

リン系安定剤としては、特に限定されるわけではないが、トリス(2,4−ジ−t−ブチルフェニル)フォスファイト(Irgafos168、BASF社製)、ジ(2,6−ジ−t−ブチル−4−メチルフェニル)−ペンタエリストール−ジフォスファイト(PEP−36、ADEKA社製)、9,10−ジヒドロ−9−オキサ−10−フォスファフェナントレン−10−オキサイド(HCA、三光社製)等が挙げられる。   The phosphorus stabilizer is not particularly limited, but tris (2,4-di-t-butylphenyl) phosphite (Irgafos168, manufactured by BASF), di (2,6-di-t-butyl). -4-methylphenyl) -pentaerythritol diphosphite (PEP-36, manufactured by ADEKA), 9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide (HCA, manufactured by Sanko) Etc.

脂肪酸金属塩としては、特に限定されるわけではないが、直鎖状脂肪酸基を有するものが好ましい。また、脂肪酸基は炭素数10〜20のものが好ましい。具体的には、ラウリル酸アルミニウム、ミリスチン酸アルミニウム、パルミチン酸アルミニウム、ステアリン酸アルミニウム、ラウリル酸マグムシウム、ミリスチン酸マグムシウム、パルミチン酸マグムシウム、ステアリン酸マグムシウム等が挙げられる。   Although it does not necessarily limit as a fatty-acid metal salt, What has a linear fatty acid group is preferable. The fatty acid group preferably has 10 to 20 carbon atoms. Specific examples include aluminum laurate, aluminum myristate, aluminum palmitate, aluminum stearate, magnesium laurate, magnesium myristate, magnesium palmitate, and magnesium stearate.

結晶核剤としては、特に限定されるわけではないが、リン酸ビス(4−t−ブチルフェニル)ナトリウム(NA−10、ADEKA社製)、リン酸2,2'−メチレンビス(4,6−ジ−t−ブチルフェニル)ナトリウム(NA−11、ADEKA社製)、ロジン系結晶核剤パインクリスタルKM−1500(荒川化学工業社製)等が挙げられる。   The crystal nucleating agent is not particularly limited, but sodium bis (4-t-butylphenyl) phosphate (NA-10, manufactured by ADEKA), 2,2′-methylenebisphosphate (4,6- Di-t-butylphenyl) sodium (NA-11, manufactured by ADEKA), rosin crystal nucleating agent pine crystal KM-1500 (manufactured by Arakawa Chemical Industries), and the like.

上記添加剤の含有量は、多孔性誘電体シート100重量部に対して、0.01〜5重量部であることが好ましく、0.025〜2.5重量部であることがより好ましく、0.05〜2重量部であることがさらに好ましい。含有量が少ないとエレクトレット化効果が十分ではなく、逆に含有量が多くても効果は飽和し、ブリードアウトする。   The content of the additive is preferably 0.01 to 5 parts by weight, more preferably 0.025 to 2.5 parts by weight with respect to 100 parts by weight of the porous dielectric sheet. More preferably, it is 0.05 to 2 parts by weight. If the content is small, the electretization effect is not sufficient. Conversely, even if the content is large, the effect is saturated and bleeds out.

ポリオレフィン系樹脂からなる多孔性誘電体シート表面への酸素の導入方法については、特に限定されるわけではないが、オゾン雰囲気での曝露、硝酸や次亜塩素酸ナトリウム溶液等の酸化性液体との接触、プラズマ処理等が挙げられる。   The method of introducing oxygen to the surface of the porous dielectric sheet made of polyolefin resin is not particularly limited, but exposure to an ozone atmosphere, oxidation liquid such as nitric acid or sodium hypochlorite solution, etc. Examples thereof include contact and plasma treatment.

ポリオレフィン系樹脂からなる多孔性誘電体シートに噴射する水溶液は、pHが7を超えることが好ましい。pHが7以下の水溶液を使用した場合は、多孔性誘電体シートを高度にエレクトレット化することが困難である。水溶液の種類については、特に限定されるわけではないが、好ましくは水酸化ナトリウム、水酸化カリウム、次亜塩素酸塩、アンモニア、アンモニウム塩、アミン類、炭酸塩、炭酸水素塩等が溶解している水溶液が挙げられる。なお、界面活性剤や有機溶剤は多孔性誘電体シートへの水溶液の浸透性を高めるだけでなく、多孔性誘電体シート表面に被膜を形成し、多孔性誘電体シートの高エレクトレット化を妨げるため、該水溶液中に含有されるべきではない。   The aqueous solution sprayed onto the porous dielectric sheet made of polyolefin resin preferably has a pH exceeding 7. When an aqueous solution having a pH of 7 or less is used, it is difficult to highly electretize the porous dielectric sheet. The type of the aqueous solution is not particularly limited, but preferably sodium hydroxide, potassium hydroxide, hypochlorite, ammonia, ammonium salt, amines, carbonate, bicarbonate, etc. are dissolved. Aqueous solution. Surfactants and organic solvents not only increase the permeability of the aqueous solution to the porous dielectric sheet, but also form a film on the surface of the porous dielectric sheet to prevent high electrets of the porous dielectric sheet. Should not be contained in the aqueous solution.

ポリオレフィン系樹脂からなる多孔性誘電体シートに前記水溶液を噴射する場合、シートを通気度50〜400cm3/cm2/秒の網状支持体に載せ、この上方より水溶液を噴射するとともに、該網状支持体の下方を減圧状態とすることが好ましい。前記通気度はJIS L1096に記載のフランジール形試験機を用いて測定される。網状支持体とは、具体的には金属ヤーンやプラスチックヤーンの織物からなる多孔構造物であり、平織り、綾織り、朱子織りなどの織り形状が挙げられる。金属素材としてはステンレス、ブロンズ等、またプラスチック素材としてはポリプロピレン、ポリエステル、ポリウレタン、ナイロン、ポリフェニレンサルファイドなどが挙げられる。 When spraying the aqueous solution onto a porous dielectric sheet made of a polyolefin resin, the sheet is placed on a mesh-like support having an air permeability of 50 to 400 cm 3 / cm 2 / second, and the aqueous solution is jetted from above to support the mesh-like support. The lower part of the body is preferably in a reduced pressure state. The air permeability is measured using a frangole type tester described in JIS L1096. The net-like support is specifically a porous structure made of a metal yarn or plastic yarn woven material, and examples thereof include plain weave, twill weave and satin weave. Examples of the metal material include stainless steel and bronze, and examples of the plastic material include polypropylene, polyester, polyurethane, nylon, and polyphenylene sulfide.

水溶液の噴射は、ポリオレフィン系樹脂からなる多孔性誘電体シートの数cm上方に設置したシートの幅方向に沿って、多数のオリフィスを有するノズルより、水溶液が該シートを通過するのに十分な圧力で噴射する。通過するのに十分な圧力は、多孔性誘電体シートの目付によって異なる。例えば、目付が5〜20g/m2のものでは0.3〜2MPa、20〜50g/m2のものでは0.6〜3MPa、50〜100g/m2のものでは1〜4MPaであることが好ましい。圧力が高すぎると、多孔性誘電体シートにピンホールが開き、濾過性能が低下してしまう。また圧力が低すぎることで多孔性誘電体シート内を水溶液が十分に通過することができなければ多孔性誘電体シートを高度にエレクトレット化することができない。ノズルは直径0.05〜0.2mmのオリフィスをピッチ0.5〜3mmで1列、または複数列配置したものが好ましい。また網状支持体を可動とし、多孔性誘電体シートをその長手方向に搬送させることにより噴射処理を連続的に行うことができる。その搬送速度は特に限定されないが、好ましい範囲を挙げると1〜100m/分である。また最適な噴射回数や処理面(片面か両面か)は多孔性誘電体シートの目付や平均繊維径に依存するため特に限定されない。 The injection of the aqueous solution is a pressure sufficient to allow the aqueous solution to pass through the sheet from a nozzle having a large number of orifices along the width direction of the sheet placed several cm above the porous dielectric sheet made of polyolefin resin. Inject with. The pressure sufficient to pass depends on the basis weight of the porous dielectric sheet. For example, when the basis weight is 5 to 20 g / m 2 , 0.3 to 2 MPa, 20 to 50 g / m 2 is 0.6 to 3 MPa, and 50 to 100 g / m 2 is 1 to 4 MPa. preferable. If the pressure is too high, pinholes will open in the porous dielectric sheet and the filtration performance will deteriorate. Further, if the aqueous solution cannot sufficiently pass through the porous dielectric sheet because the pressure is too low, the porous dielectric sheet cannot be highly electretized. The nozzle is preferably one in which orifices having a diameter of 0.05 to 0.2 mm are arranged in one or more rows with a pitch of 0.5 to 3 mm. Further, the jetting process can be continuously performed by making the mesh support movable and transporting the porous dielectric sheet in the longitudinal direction. Although the conveyance speed is not particularly limited, a preferable range is 1 to 100 m / min. Further, the optimum number of injections and the treatment surface (one side or both sides) are not particularly limited because they depend on the basis weight of the porous dielectric sheet and the average fiber diameter.

また水溶液の噴射と同時に、網状支持体の下方を、排気ブロアー等を用いて減圧状態とすることが好ましい。吸引負圧は特に限定されないが、200〜2000mmAqが好ましい。減圧状態にすると、多孔性誘電体シート内を水溶液が十分に通過でき、多孔性誘電体シートを高度にエレクトレット化することができる。   At the same time as the injection of the aqueous solution, it is preferable that the lower portion of the mesh support is brought into a reduced pressure state using an exhaust blower or the like. The suction negative pressure is not particularly limited, but 200 to 2000 mmAq is preferable. When the pressure is reduced, the aqueous solution can sufficiently pass through the porous dielectric sheet, and the porous dielectric sheet can be highly electretized.

多孔性誘電体シートに水溶液噴射処理した後の乾燥方法については、従来公知の方法が使用可能である。例えば、熱風乾燥法、真空乾燥法、または自然乾燥法等の方法が適用可能である。なかでも熱風乾燥法は、連続処理が可能であるため好ましい。熱風乾燥法の場合、乾燥温度としてはエレクトレットを消失させない程度の温度にする必要がある。好ましくは120℃以下、より好ましくは100℃以下、さらに好ましくは80℃以下にするのがよい。また、熱風乾燥前に、予備乾燥として、ニップロール、吸水ロール、またはサクション吸引等によって過剰な水分を取り除いておくとより好ましい。   A conventionally known method can be used as a drying method after the aqueous solution is sprayed onto the porous dielectric sheet. For example, a method such as a hot air drying method, a vacuum drying method, or a natural drying method is applicable. Of these, the hot air drying method is preferable because continuous processing is possible. In the case of the hot air drying method, the drying temperature needs to be a temperature that does not cause the electret to disappear. Preferably it is 120 degrees C or less, More preferably, it is 100 degrees C or less, More preferably, it is good to set it as 80 degrees C or less. Moreover, it is more preferable to remove excess moisture by nip roll, water absorbing roll, suction suction or the like as preliminary drying before hot air drying.

以下、実施例によって本発明の作用効果をより具体的に示す。下記では多孔性誘電体として従来公知の方法で製造されるメルトブロー不織布を使用したが、これは本発明方法を限定する性質のものではなく、前・後記の趣旨に沿って設計変更することはいずれも本発明の技術的範囲に含まれるものである。   Hereinafter, the effects of the present invention will be described more specifically by way of examples. In the following, a melt blown nonwoven fabric produced by a conventionally known method is used as the porous dielectric, but this is not a property that limits the method of the present invention, and any design changes may be made in accordance with the purpose described above or below. Is also included in the technical scope of the present invention.

(O/C比の測定法)
ESCAにて、多孔性誘電体シートの表面の酸素の1s軌道に起因するスペクトル強度を、炭素の1s軌道に起因するスペクトル強度で除することで、その多孔性誘電体シートのO/C比を算出した。
(O / C ratio measurement method)
By dividing the spectral intensity caused by the 1s orbital of oxygen on the surface of the porous dielectric sheet by ESCA by the spectral intensity caused by the 1s orbital of carbon, the O / C ratio of the porous dielectric sheet is obtained. Calculated.

(水溶液のpH測定方法)
電極として低導電率水・非水溶媒用pH電極(HORIBA社製6377−10D)を使用し、JIS−Z8802に記載のpH測定方法に準じて、水温25℃の条件で、調製した水溶液のpHを測定した。
(Method for measuring pH of aqueous solution)
The pH of the aqueous solution prepared using a low conductivity water / nonaqueous solvent pH electrode (6377-10D manufactured by HORIBA) as the electrode and under the condition of a water temperature of 25 ° C. according to the pH measurement method described in JIS-Z8802. Was measured.

(水溶液噴射処理)
多孔性誘電体シートを通気度120cm3/cm2/秒の網状支持体(96メッシュ)に載せ、不織布の上方3cmに位置する直径0.1mmφ、ピッチ0.6mmのノズルから2MPaの圧力で水溶液噴射処理を行った。なおベースとなる水は、一般的な水道水を二段の逆浸透膜処理、次いでイオン交換膜処理を施した高純度の水とし、そのベース水に炭酸カリウム(ナカライテスク社製)を10ppm溶解させ、pHが9.6の噴射水溶液を調製した。支持体の搬送速度を3m/分とし、ノズル直下の網状支持体の下方を600mmAqの減圧状態とした。この処理をシートの表面について3回行った。その後このシートを自然乾燥、または80℃の熱風オーブン中に1分間滞留させて乾燥した。
(Aqueous solution injection treatment)
A porous dielectric sheet is placed on a reticulated support (96 mesh) having an air permeability of 120 cm 3 / cm 2 / sec, and an aqueous solution at a pressure of 2 MPa from a nozzle having a diameter of 0.1 mmφ and a pitch of 0.6 mm located 3 cm above the nonwoven fabric. An injection process was performed. The base water is high-purity water obtained by subjecting general tap water to two-stage reverse osmosis membrane treatment and then ion exchange membrane treatment, and 10 ppm of potassium carbonate (manufactured by Nacalai Tesque) dissolved in the base water. And an aqueous jet solution having a pH of 9.6 was prepared. The conveyance speed of the support was 3 m / min, and the lower part of the net-like support just below the nozzle was in a reduced pressure state of 600 mmAq. This treatment was performed 3 times on the surface of the sheet. Thereafter, the sheet was naturally dried or kept in a hot air oven at 80 ° C. for 1 minute to dry.

(濾過特性の評価)
圧力損失(PD)は、エレクトレット濾過材試料をダクト内に設置し、濾材通過線速度が10cm/秒になるようコントロールし、エレクトレット濾材上流、下流の静圧差を圧力計で読み取り求めた。また粒子捕集効率E(%)の評価は粒子径0.3μmの大気塵粒子を用い、10cm/秒にて行った。圧力損失PD(mmAq)と粒子捕集効率E(%)を用いて、下記数式より濾材品質係数QFを算出した。
QF=−LN((100−E)/100)/PD
(Evaluation of filtration characteristics)
The pressure loss (PD) was obtained by installing an electret filter medium sample in a duct and controlling the linear passage speed of the filter medium to 10 cm / second, and reading the static pressure difference upstream and downstream of the electret filter medium with a pressure gauge. The particle collection efficiency E (%) was evaluated at 10 cm / second using atmospheric dust particles having a particle diameter of 0.3 μm. Using the pressure loss PD (mmAq) and the particle collection efficiency E (%), the filter medium quality factor QF was calculated from the following formula.
QF = -LN ((100-E) / 100) / PD

(平均繊維径の評価)
SEM写真により拡大した繊維100本について繊維径を測定し、その平均値Dfs[μm]を求めた。
(Evaluation of average fiber diameter)
The fiber diameter was measured for 100 fibers enlarged by SEM photographs, and the average value Dfs [μm] was determined.

<実施例1>
メルトフローインデックス700のポリプロピレン樹脂(プライムポリマー社製)100重量部に対して、Irganox1010を0.05重量部配合し、目付20g/m2、平均繊維径(Dfs)1.1μmのメルトブロー不織布を作製した。無声放電により発生した6.8ppmのオゾンを含有した空気を20cm/秒で30分、メルトブロー不織布に通過させた。その後、水溶液噴射処理を行い、エレクトレット濾過材を得た。得られたエレクトレット濾過材の評価結果を表1に示した。
<Example 1>
0.05 part by weight of Irganox 1010 is blended with 100 parts by weight of polypropylene resin (manufactured by Prime Polymer Co., Ltd.) having a melt flow index 700, and a melt blown nonwoven fabric having a basis weight of 20 g / m 2 and an average fiber diameter (Dfs) of 1.1 μm is produced. did. Air containing 6.8 ppm of ozone generated by silent discharge was passed through the melt blown nonwoven fabric at 20 cm / sec for 30 minutes. Then, the aqueous solution injection process was performed and the electret filter material was obtained. The evaluation results of the obtained electret filter material are shown in Table 1.

<実施例2>
実施例1で用いたメルトブロー不織布に、エタノール(ナカライテスク社製;純度99.5%)を含浸させ、次いで、次亜塩素酸ナトリウムを5%含有する水溶液(和光純薬工業社製)に浸すことで、内部まで該水溶液を含浸させ、80℃、30分、酸化処理を行った。その後、水溶液噴射処理を行い、エレクトレット濾過材を得た。得られたエレクトレット濾過材の評価結果を表1に示した。
<Example 2>
The meltblown nonwoven fabric used in Example 1 is impregnated with ethanol (manufactured by Nacalai Tesque, Inc .; purity 99.5%), and then immersed in an aqueous solution (made by Wako Pure Chemical Industries, Ltd.) containing 5% sodium hypochlorite. Thus, the aqueous solution was impregnated to the inside, and oxidation treatment was performed at 80 ° C. for 30 minutes. Then, the aqueous solution injection process was performed and the electret filter material was obtained. The evaluation results of the obtained electret filter material are shown in Table 1.

<実施例3>
実施例1で用いた樹脂に対して、Irganox1010を3重量部配合し、目付20g/m2、平均繊維径(Dfs)1.1μmのメルトブロー不織布を作製した。無声放電により発生した6.8ppmのオゾンを含有した空気を20cm/秒で30分、メルトブロー不織布に通過させた。その後、水溶液噴射処理を行い、エレクトレット濾過材を得た。得られたエレクトレット濾過材の評価結果を表1に示した。
<Example 3>
3 parts by weight of Irganox 1010 was blended with the resin used in Example 1 to prepare a melt blown nonwoven fabric having a basis weight of 20 g / m 2 and an average fiber diameter (Dfs) of 1.1 μm. Air containing 6.8 ppm of ozone generated by silent discharge was passed through the melt blown nonwoven fabric at 20 cm / sec for 30 minutes. Then, the aqueous solution injection process was performed and the electret filter material was obtained. The evaluation results of the obtained electret filter material are shown in Table 1.

<実施例4>
実施例1で用いた樹脂に、何も配合せず、目付20g/m2、平均繊維径(Dfs)1.1μmのメルトブロー不織布を作製した。直流コロナ荷電を−20kV/cmの条件で15秒印加し、水溶液噴射処理を行い、エレクトレット濾過材を得た。得られたエレクトレット濾過材の評価結果を表1に示した。
<Example 4>
Nothing was blended with the resin used in Example 1, and a melt blown nonwoven fabric having a basis weight of 20 g / m 2 and an average fiber diameter (Dfs) of 1.1 μm was produced. A direct current corona charge was applied for 15 seconds under the condition of −20 kV / cm, and an aqueous solution injection treatment was performed to obtain an electret filter material. The evaluation results of the obtained electret filter material are shown in Table 1.

<比較例1>
実施例1で用いたメルトブロー不織布に何も処理せず、水溶液噴射処理を行い、エレクトレット濾過材を得た。得られたエレクトレット濾過材の評価結果を表1に示した。
<Comparative Example 1>
The melt-blown nonwoven fabric used in Example 1 was not subjected to any treatment, and an aqueous solution injection treatment was performed to obtain an electret filter material. The evaluation results of the obtained electret filter material are shown in Table 1.

<比較例2>
実施例1で用いたメルトブロー不織布に、直流コロナ荷電を−10kV/cmの条件で15秒印加し、水溶液噴射処理を行い、エレクトレット濾過材を得た。得られたエレクトレット濾過材の評価結果を表1に示した。
<Comparative Example 2>
A direct current corona charge was applied to the meltblown nonwoven fabric used in Example 1 for 15 seconds under the condition of −10 kV / cm, and an aqueous solution injection treatment was performed to obtain an electret filter material. The evaluation results of the obtained electret filter material are shown in Table 1.

表1より明らかなように、実施例1〜4では高い粒子捕集効率を示した。これに対してO/C比が低い比較例1および2は、実施例1〜4に比べ低い粒子捕集効率およびQFに留まり、高度にエレクトレット化できないことが確認できた。   As is clear from Table 1, Examples 1-4 showed high particle collection efficiency. In contrast, Comparative Examples 1 and 2 having a low O / C ratio remained low in particle collection efficiency and QF as compared with Examples 1 to 4, and it was confirmed that they could not be highly electretized.

本発明によるポリオレフィン系樹脂からなる多孔性誘電体シートを用いたエレクトレット濾過材は、そのシート表面に酸素原子を導入することにより、その内部まで高度にエレクトレット化されており、優れた濾過性能を付与でき、産業界への寄与大である。   The electret filter material using the porous dielectric sheet made of polyolefin resin according to the present invention is highly electretized by introducing oxygen atoms into the sheet surface, and provides excellent filtration performance. It can make a great contribution to the industry.

Claims (3)

ポリオレフィン系樹脂からなる多孔性誘電体シート表面の酸素原子(O)と炭素原子(C)のモル比であるO/Cの値が0.003〜0.03であるエレクトレット濾過材。   An electret filter material in which the value of O / C, which is the molar ratio of oxygen atoms (O) to carbon atoms (C) on the surface of a porous dielectric sheet made of a polyolefin-based resin, is 0.003 to 0.03. 多孔性誘電体シートがヒンダードフェノール系安定剤、硫黄系安定剤、リン系安定剤、脂肪酸金属塩、および結晶核剤から選ばれる少なくとも一種類の添加剤を含有し、その含有量が前記多孔性誘電体シート100重量部に対して0.01〜5重量部である請求項1に記載のエレクトレット濾過材。   The porous dielectric sheet contains at least one additive selected from a hindered phenol stabilizer, a sulfur stabilizer, a phosphorus stabilizer, a fatty acid metal salt, and a crystal nucleating agent, and the content thereof is the porous The electret filter material according to claim 1, wherein the content is 0.01 to 5 parts by weight with respect to 100 parts by weight of the conductive dielectric sheet. ポリオレフィン系樹脂からなる多孔性誘電体シートにオゾン酸化処理、液相酸化処理、およびプラズマ酸化処理から選ばれる少なくとも1つの処理を施した後、pHが7を超える水溶液を噴射し、乾燥させる請求項1または2に記載のエレクトレット濾過材の製造方法。   A porous dielectric sheet made of a polyolefin resin is subjected to at least one treatment selected from ozone oxidation treatment, liquid phase oxidation treatment, and plasma oxidation treatment, and then an aqueous solution having a pH of more than 7 is sprayed and dried. The manufacturing method of the electret filter material of 1 or 2.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63151326A (en) * 1986-12-17 1988-06-23 Asahi Chem Ind Co Ltd Electret body
JPH0899007A (en) * 1994-09-29 1996-04-16 Toyobo Co Ltd Electret filter
JPH08155230A (en) * 1994-12-06 1996-06-18 Nitto Denko Corp Electret filter and its preparation
JP2003311112A (en) * 2002-04-23 2003-11-05 Toyobo Co Ltd Electret filter medium
JP2004066027A (en) * 2002-08-01 2004-03-04 Toyobo Co Ltd Production method of electret filter medium
JP2004195357A (en) * 2002-12-18 2004-07-15 Toyobo Co Ltd Method for producing electret filter medium

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63151326A (en) * 1986-12-17 1988-06-23 Asahi Chem Ind Co Ltd Electret body
JPH0899007A (en) * 1994-09-29 1996-04-16 Toyobo Co Ltd Electret filter
JPH08155230A (en) * 1994-12-06 1996-06-18 Nitto Denko Corp Electret filter and its preparation
JP2003311112A (en) * 2002-04-23 2003-11-05 Toyobo Co Ltd Electret filter medium
JP2004066027A (en) * 2002-08-01 2004-03-04 Toyobo Co Ltd Production method of electret filter medium
JP2004195357A (en) * 2002-12-18 2004-07-15 Toyobo Co Ltd Method for producing electret filter medium

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