JPH0126727B2 - - Google Patents

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Publication number
JPH0126727B2
JPH0126727B2 JP55114739A JP11473980A JPH0126727B2 JP H0126727 B2 JPH0126727 B2 JP H0126727B2 JP 55114739 A JP55114739 A JP 55114739A JP 11473980 A JP11473980 A JP 11473980A JP H0126727 B2 JPH0126727 B2 JP H0126727B2
Authority
JP
Japan
Prior art keywords
laminate
fiber
density
filter
filtration material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP55114739A
Other languages
Japanese (ja)
Other versions
JPS5738916A (en
Inventor
Tadashi Yokota
Yasufumi Doi
Satoru Saito
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DAINITSUKU KK
Original Assignee
DAINITSUKU KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by DAINITSUKU KK filed Critical DAINITSUKU KK
Priority to JP11473980A priority Critical patent/JPS5738916A/en
Publication of JPS5738916A publication Critical patent/JPS5738916A/en
Publication of JPH0126727B2 publication Critical patent/JPH0126727B2/ja
Granted legal-status Critical Current

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  • Filtering Materials (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は気体の濾過材料、更に詳しくはエアフ
イルター、エアクリーナー等と称される空気中の
塵埃を捕集除去するのに好ましく使用される許り
ではなく、その他空気清浄用或は空気以外の気体
の清浄用にも用いられる気体の濾過材料に関す
る。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is preferably used as a gas filtration material, more specifically, for collecting and removing dust in the air called an air filter, air cleaner, etc. The present invention relates to gas filtration materials that are used not only for cleaning air but also for cleaning gases other than air.

〔従来の技術〕[Conventional technology]

濾過スポンジ体を、特定形状のケース、すなわ
ち、吸入口から濾過済み空気出口に至るに従つて
漸次径が縮少されたケースに強制嵌入することに
よつて吸入口から空気出口に至るに従つてスポン
ジ体を漸次圧縮するようにした気体の濾過材料が
実公昭46−18535号公報により知られており、ま
た繊維を積層したフエルト状濾材の複数個を多孔
円筒の外周部において積層方向面を相互に密接し
た状態で放射方向に配設し、これを袋体で包被
し、この配設状態で各濾材は外側より内側にかけ
て漸次圧縮されてなる円筒濾材が実願昭48−
146905号(実開昭50−92466号)によつて知られ
ている。
By forcibly fitting the filtration sponge body into a case with a specific shape, that is, a case whose diameter gradually decreases from the inlet to the filtered air outlet, A gas filtration material in which a sponge body is gradually compressed is known from Japanese Utility Model Publication No. 18535/1983, and a plurality of felt filter media made of laminated fibers are arranged so that the lamination direction surfaces are mutually disposed on the outer periphery of a porous cylinder. A cylindrical filter medium was developed in 1973, in which the filter medium was arranged in a radial direction in close contact with the cylindrical filter medium, and this was covered with a bag body, and each filter medium was gradually compressed from the outside to the inside in this position.
It is known from No. 146905 (Utility Model Publication No. 50-92466).

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

これらのものにあつては例えば前者にあつては
濾過スポンジ体の部位に応じた圧縮度合を得るた
めには、それに応じた形状のケースを準備しなけ
ればならないものであり、また後者にあつては、
多孔円筒や袋体を必要としたり、また多数の濾材
を、積層方向面を相互に密接させた状態、すなわ
ち積層方向と直交する方向を放射方向に向けた状
態で配設し、これを袋体で包被して、袋体の両端
部を多孔円筒の端面に接着して集束することによ
つて濾材の外部から内部にかけて密度を高めるよ
うにしていることから、その製造は繁雑である。
For example, in the case of the former, in order to obtain the degree of compression that corresponds to the location of the filter sponge body, it is necessary to prepare a case with a corresponding shape, and in the case of the latter. teeth,
In some cases, a porous cylinder or bag is required, or a large number of filter media are arranged with their lamination direction surfaces in close contact with each other, that is, with the direction perpendicular to the lamination direction facing in the radial direction, and this is used as a bag. The manufacturing process is complicated because the density is increased from the outside to the inside of the filter medium by wrapping the bag with a porous cylinder and bonding both ends of the bag to the end faces of the porous cylinder.

これらのことからその製造が容易であるにかか
わらず捕集効率は良好であつて、その寿命が長
く、また予想される塵埃の大きさの分布状況に応
じた捕集が得る気体の濾過材料を提供することを
目的として本発明はなされたものである。
For these reasons, although it is easy to manufacture, it has good collection efficiency, has a long service life, and is suitable for gas filtration materials that can be collected according to the expected dust size distribution. The present invention has been made for the purpose of providing.

〔問題点を解決するための手段〕 本発明は前記した目的を達するため、繊維集積
密度が比較的均一な繊維集合体を多数積層した積
層体の中心に縦孔を穿つと共に、積層体の周縁か
ら縦孔に向つて傾斜する形状の傾斜押圧板で、こ
の積層体の上面を押圧することによつて積層体の
周面から縦孔に至るに従つて、繊維集積密度が粗
から密に変化している気体の濾過体とすることに
よつて、よくその目的を達し得ることを見出し本
発明を得たものである。
[Means for Solving the Problems] In order to achieve the above-mentioned object, the present invention creates a vertical hole in the center of a laminate in which a large number of fiber aggregates having a relatively uniform fiber density are stacked, and also holes in the periphery of the laminate. By pressing the top surface of this laminate with an inclined pressing plate having a shape that slopes from The present invention was achieved by discovering that the object can be well achieved by creating a filter for gases that are

〔作 用〕[Effect]

積層体を傾斜板で押圧することによつて、積層
体の周面から縦孔に至るに従つて繊維集積密度が
粗から密に変化した状態とすることができるもの
であり、この傾斜板の傾斜の程度により繊維集積
密度の変化の状態が任意にしかも容易に得られる
ものとなつた。
By pressing the laminate with an inclined plate, the fiber accumulation density can be changed from coarse to dense from the circumferential surface of the laminate to the vertical hole. Depending on the degree of inclination, the fiber accumulation density can be changed arbitrarily and easily.

〔実施例〕〔Example〕

添付図面について本発明の実施の一例を説明す
ると、Aは繊維集合体の1種である不織布であつ
て、これを多数積層して積層体Bとする。この積
層体Bの中心には縦孔Cが穿たれている。Dは傾
斜押圧板であつて、漏斗状をなし、積層体Bの縦
孔Cに相当する部分は円孔とされているが、この
円孔は持に設けられなくてもよい。この傾斜押圧
板Dの径は、積層体Bの径と等しくされていれば
都合が良いが必ずしもそうである必要はない。積
層体Bの上面に傾斜押圧板Dを置き、この傾斜押
圧板Dを押圧することによつて積層体Bは、その
周面Eから縦孔Cに至るに従つて繊維集積密度が
粗から密に変化したものとなる。このようにして
フイルターFが得られる。このフイルターFによ
れば塵埃を含有する空気はフイルターFの周面E
から入りフイルターFの縦孔Cに抜け、更に上方
或は下方に抜き去られるものでこの時空気中の塵
埃の粒径の大きいものは、フイルターの周面Eで
ある空気の入口側に近い区域Xにて捕捉され、粒
径の細かなものはフイルターの縦孔Cである空気
の出口側に近い区域Zで捕捉され、これらの中間
の粒径のものは、それらの中間の区域Yで捕捉さ
れる。以上の繊維集合体として不織布の積層体を
用い、その繊維集積密度に変化を与える手段とし
て1つの直線的な傾斜面からなる押圧板を用いた
場合を説明したが、これ以外にも種々の場合を挙
げることが出来るのでそのうちの少数例について
以下に説明するが、本発明はこれらの説明に限定
されることなく、本発明の精神を逸脱しない限り
自由であることは当然である。
An example of the implementation of the present invention will be described with reference to the accompanying drawings. A is a nonwoven fabric that is a type of fiber aggregate, and a laminate B is obtained by laminating a large number of nonwoven fabrics. A vertical hole C is bored in the center of this laminate B. Reference numeral D denotes an inclined pressing plate having a funnel shape, and the portion corresponding to the vertical hole C of the laminate B is a circular hole, but the circular hole does not have to be provided at all times. It is convenient if the diameter of the inclined pressing plate D is equal to the diameter of the laminate B, but this is not necessarily the case. An inclined pressing plate D is placed on the upper surface of the laminate B, and by pressing the inclined pressing plate D, the laminate B changes in fiber accumulation density from coarse to dense from the circumferential surface E to the vertical hole C. It will be changed to. In this way, filter F is obtained. According to this filter F, the air containing dust is removed from the circumferential surface E of the filter F.
The dust that enters the air, exits through the vertical hole C of the filter F, and is further removed upward or downward, and at this time, the large particles of dust in the air are removed from the area near the air inlet side, which is the circumferential surface E of the filter. Particles with small diameters are captured in area Z near the air outlet side, which is vertical hole C of the filter, and particles with intermediate sizes are captured in area Y between them. be done. Although the case where a laminate of nonwoven fabric is used as the fiber aggregate and a pressing plate consisting of one linear inclined surface is used as a means for changing the fiber accumulation density has been described above, there are various other cases as well. A few examples will be described below, but it is obvious that the present invention is not limited to these explanations and is free as long as it does not depart from the spirit of the present invention.

本発明に用いられる繊維集合体としては、前記
した不織布の積層体に限ることなく、これ以外に
もスポンジ或はフエルト類、繊維塊等の如き、単
一塊であつてもよく、これらを押圧することによ
つて、その単一塊の部分の繊維集積密度に変化が
与えられる。
The fiber aggregate used in the present invention is not limited to the above-mentioned nonwoven fabric laminate, but may also be a single lump such as a sponge, felt, fiber lump, etc., which can be pressed. This provides a variation in the fiber density of the single mass portion.

本発明の濾過材料である繊維集合体は、さきに
説明したように使用に際して押圧板の押圧によつ
て繊維集積密度に変化を与えるようにしても良い
が、これとは別に、第4図のイ,ロにその一例を
示すように繊維集積密度が比較的均一な繊維集合
体を、あらかじめ設定された繊維集積密度に各部
分がなるように押圧し、この押圧された状態を固
定して成形された集合体を濾過材料として用いる
ことも出来る。この場合にはあらかじめ想定され
た塵埃の粒径の分布の範囲内にしか適用できない
から、異なる粒径の分布に対しては期待する程の
有効性を示さないものと思われるから、想定に従
つて、数種類の繊維集積密度の分布の異なる集合
体を用意する必要がある。
The fiber aggregate, which is the filtration material of the present invention, may be used in such a way that the fiber aggregate density may be changed by pressing with a pressing plate as explained above, but apart from this, the fiber aggregate density as shown in FIG. As an example shown in A and B, a fiber aggregate with a relatively uniform fiber density is pressed so that each part has a preset fiber density, and this pressed state is fixed and molded. The resulting aggregate can also be used as a filtration material. In this case, since it can only be applied within the range of the dust particle size distribution assumed in advance, it is unlikely that it will be as effective as expected for different particle size distributions. Therefore, it is necessary to prepare several types of aggregates with different distributions of fiber accumulation densities.

また濾過材料である繊維集合体が押圧される
際、繊維集合体の気体の入口側から出口側にかけ
ての繊維集積密度が直線的に変化するようにする
ためには、押圧板の、気体の入口側から出口側に
かけての縦断面が直線として形成されたもので押
圧すればよく、この場合、この直線が入口から出
口にかけて1本の直線であるような押圧板であつ
てもよく、またこの直線が2本又はそれ以上の直
線で形成されるような押圧板であつてもよい。従
つて後者の場合は押圧板の縦断面は鋸歯状或はそ
れに類似する形状で表現される。この押圧板の縦
断面が直線であるような押圧板に限らず、これは
曲線であつてもよく、任意の曲線であるような押
圧板であつても差支えない。以上の説明は自動車
エンジン用のフイルターとして述べたがこれに限
らず、一般家庭用は勿論病院、工場等の空気濾過
に用いることが出来る許りではなく空気以外の気
体に適用できることも当然である。
In addition, when the fiber aggregate that is the filtration material is pressed, in order to make the fiber accumulation density change linearly from the gas inlet side to the outlet side of the fiber aggregate, it is necessary to It is sufficient to press with a plate whose vertical cross section from the side to the outlet side is a straight line. The pressing plate may be formed of two or more straight lines. Therefore, in the latter case, the longitudinal section of the pressing plate is expressed in a sawtooth shape or a shape similar to it. The press plate is not limited to a press plate whose vertical cross section is a straight line, but may be a curved line, or may have an arbitrary curved line. Although the above explanation has been made regarding a filter for automobile engines, it can be used not only for general household use but also for air filtration in hospitals, factories, etc., and can also be applied to gases other than air. .

次に本発明の濾過材料を得る製造方法の一例を
示すと、単糸繊度が6デニールで繊維長が51mmの
ポリエステル繊維を30%(重量比)と、単糸繊度
が3デニールで繊維長が51mmのポリエステル繊維
を30%(重量比)と、単糸繊度が3デニールで繊
維長が51mmのレーヨン繊維を40%(重量比)との
混綿をランダムウエバにかけ重量が80g/m2のウ
エブとし、これにアクリル酸エステル系の接着剤
を固形分付着量20g/m2となるように結合処理を
行い、製品重量100g/m2厚さ0.9mmの不織布を作
つた。この不織布のみかけの密度は0.111である。
この不織布を外径300mm、内径150mmのドーナツツ
状に打ち抜き、これを同心円状に70枚積層して不
織積層ドーナツツ板を形成し、内径面に環(従来
から自動車エンジン用エアークリーナーエレメン
ト内径面に用いられているものと同じ有孔板の
環)を内装し、ドーナツツ下面は平面ドーナツツ
板だが、上面に円心に向つてその勾配が約10゜に
傾斜するように成型した変形ドーナツツ状円盤を
置いて、下面の平面ドーナツツ板との間に、不織
積層ドーナツツ板をはさみ、外径部の上下板間隔
が58mm、内径部の間隔が45mmになるように押圧を
加えた状態で固定し、フイルターエレメントを作
つた。このフイルターエレメントは、外径部にお
ける不織積層体のみかけの密度は0.121、内径部
では0.156であり、外径部から内径部に流れる空
気流通径路長、約75mmの間、その密度は疎から密
へ連続的に変化している。
Next, an example of the manufacturing method for obtaining the filtration material of the present invention is shown in which 30% (weight ratio) of polyester fibers with a single yarn fineness of 6 denier and a fiber length of 51 mm are used. A mixture of 30% (weight ratio) of 51 mm polyester fiber and 40% (weight ratio) of rayon fiber with a single yarn fineness of 3 denier and a fiber length of 51 mm was applied to a random web to form a web with a weight of 80 g/m 2 . This was then bonded with an acrylic ester adhesive so that the solid content was 20 g/m 2 to produce a nonwoven fabric with a product weight of 100 g/m 2 and a thickness of 0.9 mm. The apparent density of this nonwoven fabric is 0.111.
This nonwoven fabric is punched into a donut shape with an outer diameter of 300 mm and an inner diameter of 150 mm, and 70 sheets of this are laminated concentrically to form a nonwoven laminated donut plate. The bottom surface of the donut is a flat donut plate, but the top surface has a deformed donut-shaped disk with an inclination of about 10 degrees toward the center of the circle. Place the non-woven laminated donut plate between the flat donut plate on the bottom surface and fix it under pressure so that the interval between the upper and lower plates on the outer diameter part is 58 mm and the interval on the inner diameter part is 45 mm, I made a filter element. In this filter element, the apparent density of the nonwoven laminate at the outer diameter part is 0.121, and at the inner diameter part it is 0.156. During the air flow path length of approximately 75 mm from the outer diameter part to the inner diameter part, the density varies from sparse to sparse. Continuously changing to denser.

〔発明の効果〕〔Effect of the invention〕

本発明の濾過材料は以上に詳細に説明したよう
に構成されているところから傾斜押圧板を選定す
るだけで同じ条件の積層体から、任意の繊維集積
密度の分布を有する種々の濾過材料が簡単に得ら
れるのみならず、捕集効率は良好でありその寿命
が長いものとなつたものである。
The filtration material of the present invention is constructed as described in detail above, and various filtration materials having arbitrary fiber accumulation density distributions can be easily produced from laminates under the same conditions by simply selecting an inclined pressing plate. Not only can this be achieved, but the collection efficiency is also good and its lifespan is long.

【図面の簡単な説明】[Brief explanation of drawings]

添付図面は本発明を説明するためのもので第1
図は本発明の濾過材料の実施の一例を示す側面
図、第2図は本発明に好ましく用いられる傾斜押
圧板の一例を示す側面図、第3図は積層体の一例
を示す斜視図、第4図イ,ロは共に他の実施の一
例を示す斜示図である。 A:繊維集合体、B:積層体、C:縦孔、D:
傾斜押圧板。
The attached drawings are for explaining the present invention and are the first drawings.
2 is a side view showing an example of an embodiment of the filter material of the present invention, FIG. 2 is a side view showing an example of an inclined pressing plate preferably used in the present invention, FIG. 3 is a perspective view showing an example of a laminate, Figures 4A and 4B are both perspective views showing an example of another embodiment. A: fiber aggregate, B: laminate, C: vertical hole, D:
Slanted pressure plate.

Claims (1)

【特許請求の範囲】 1 繊維集積密度が比較的均一な繊維集合体を多
数積層した積層体の中心に縦孔を穿つと共に、積
層体の周縁から縦孔に向つて傾斜する形状の傾斜
押圧板で、この積層体の上面を押圧することによ
つて積層体の周面から縦孔に至るに従つて、繊維
集積密度が粗から密に変化していることを特徴と
する気体の濾過材料。 2 繊維集合体は、不織布の積層体であることを
特徴とする特許請求の範囲第1項記載の気体の濾
過材料。 3 繊維集合体は、スポンジ、フエルト等の如き
単一塊であることを特徴とする特許請求の範囲第
1項記載の気体の濾過材料。
[Scope of Claims] 1. An inclined pressing plate having a vertical hole in the center of a laminate made of a large number of laminated fiber aggregates with relatively uniform fiber density, and having a shape that slopes from the periphery of the laminate toward the vertical hole. A gas filtration material characterized in that, by pressing the upper surface of the laminate, the fiber accumulation density changes from coarse to dense from the circumferential surface of the laminate to the vertical holes. 2. The gas filtration material according to claim 1, wherein the fiber aggregate is a laminate of nonwoven fabrics. 3. The gas filtration material according to claim 1, wherein the fiber aggregate is a single lump such as sponge or felt.
JP11473980A 1980-08-22 1980-08-22 Filter medium for gas Granted JPS5738916A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11473980A JPS5738916A (en) 1980-08-22 1980-08-22 Filter medium for gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11473980A JPS5738916A (en) 1980-08-22 1980-08-22 Filter medium for gas

Publications (2)

Publication Number Publication Date
JPS5738916A JPS5738916A (en) 1982-03-03
JPH0126727B2 true JPH0126727B2 (en) 1989-05-25

Family

ID=14645428

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11473980A Granted JPS5738916A (en) 1980-08-22 1980-08-22 Filter medium for gas

Country Status (1)

Country Link
JP (1) JPS5738916A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0634556B2 (en) * 1983-12-06 1994-05-02 日産自動車株式会社 Vehicle audio system
JPS61283320A (en) * 1985-05-01 1986-12-13 Nippon Denso Co Ltd Filter material for air purifier
US4661132A (en) * 1985-08-15 1987-04-28 Allied Corporation Themally formed gradient density filter
FR2804882B1 (en) * 2000-02-11 2002-05-10 Air Liquide ATMOSPHERIC AIR COMPRESSION PROCESS
DE102011117667A1 (en) 2011-11-03 2013-05-08 Eisenmann Ag Filter module and apparatus for separating overspray and installation with such
JP6955879B2 (en) * 2017-03-17 2021-10-27 東洋アルミエコープロダクツ株式会社 Filters and filter structures
JP6955878B2 (en) * 2017-03-17 2021-10-27 東洋アルミエコープロダクツ株式会社 filter

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5092466U (en) * 1973-12-24 1975-08-04

Also Published As

Publication number Publication date
JPS5738916A (en) 1982-03-03

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