JPS6034328Y2 - filter body - Google Patents

filter body

Info

Publication number
JPS6034328Y2
JPS6034328Y2 JP3709280U JP3709280U JPS6034328Y2 JP S6034328 Y2 JPS6034328 Y2 JP S6034328Y2 JP 3709280 U JP3709280 U JP 3709280U JP 3709280 U JP3709280 U JP 3709280U JP S6034328 Y2 JPS6034328 Y2 JP S6034328Y2
Authority
JP
Japan
Prior art keywords
furnace
furnace material
gap
materials
inflow side
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
JP3709280U
Other languages
Japanese (ja)
Other versions
JPS56137718U (en
Inventor
正人 小池
Original Assignee
和興産業株式会社
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 和興産業株式会社 filed Critical 和興産業株式会社
Priority to JP3709280U priority Critical patent/JPS6034328Y2/en
Publication of JPS56137718U publication Critical patent/JPS56137718U/ja
Application granted granted Critical
Publication of JPS6034328Y2 publication Critical patent/JPS6034328Y2/en
Expired legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【考案の詳細な説明】 本考案は、濾過体の改良に関する。[Detailed explanation of the idea] The present invention relates to improvements in filter bodies.

従来複数の炉材を組み合わせた濾過体においては、流体
の流入側炉材の背面に圧力を加え、該炉材の両面間の圧
力差を減少させて塵埃の捕捉能率を増大させる手段をと
ったものは提案されてはいるが、流出側炉材の濾過面積
を充分広くとることができず表面積が小さいことから必
然的に炉口を粗くしなければならない。
Conventionally, in filter bodies that combine multiple furnace materials, pressure is applied to the back side of the furnace material on the fluid inflow side to reduce the pressure difference between both sides of the furnace material and increase the dust trapping efficiency. Although such methods have been proposed, since the filtration area of the outflow side furnace material cannot be made sufficiently large and the surface area is small, the furnace mouth must necessarily be made rough.

このように濾過効率は流入側炉材により向上し得たとし
てもバイパス孔を通過する流体(油または空気)中に大
粒の塵埃が混入しておらないという保証は全くなく、こ
れら大粒の塵埃が回転、摺動体などに損傷を与え焼付事
故や早期摩耗などをおこさせるものであって、このよう
な濾過体を通過した流体などが各滑動部に直接供給され
るものには不適切である。
Even if the filtration efficiency could be improved by using the inlet furnace material, there is no guarantee that large particles of dust will not be mixed into the fluid (oil or air) passing through the bypass hole, and these large particles may It damages the rotating and sliding parts, causing seizure accidents and early wear, and is not suitable for applications where fluid that has passed through such a filter is directly supplied to each sliding part.

本考案はこのような実情に対応すべくなされたもので、
簡単な而も合理的手段によって従来の欠点を完全に除去
せしめ、濾過効率、塵埃の捕捉効率の向上を計ると共に
長寿命で高濾過性能の濾過体を提供せんとするものであ
る。
This invention was developed in response to these circumstances.
The object of the present invention is to completely eliminate the conventional drawbacks by simple and rational means, improve filtration efficiency and dust trapping efficiency, and provide a filter body with long life and high filtration performance.

第1,2図について実施例の詳細を説明すると、上下端
板1,2の中心部間に死守円筒3をとりつけ、該死守円
筒3の外周に濾紙などの密な素材によって構成された2
枚の菊花状炉材4,5をその板面が重合しないように同
心状に配設し、両炉材4,5間に大きな空間部6を構成
する。
To explain the details of the embodiment with reference to FIGS. 1 and 2, a dead protection cylinder 3 is attached between the centers of the upper and lower end plates 1 and 2, and a protection cylinder 3 made of a dense material such as filter paper is attached to the outer periphery of the protection cylinder 3.
Two pieces of chrysanthemum-shaped furnace materials 4 and 5 are arranged concentrically so that their plate surfaces do not overlap, and a large space 6 is formed between the two furnace materials 4 and 5.

そして第1図に示すように流体の流入側炉材5を流出側
炉材4より若干背低即ち短尺に形成し、この炉材5の上
端縁と上部端板1との間に間隙部7を設け、この間隙部
7を上記空間部6に連通させたものである。
As shown in FIG. 1, the fluid inflow side furnace material 5 is formed to be slightly lower or shorter than the outflow side furnace material 4, and a gap 7 is formed between the upper edge of this furnace material 5 and the upper end plate 1. , and the gap 7 is communicated with the space 6.

またこの間隙部7を形成した側の端板1の外周部を段階
的にプレスし、この低い側の端板部1′によって流入側
炉材5の上端面の一部を保持せしめる。
Further, the outer periphery of the end plate 1 on the side where the gap 7 is formed is pressed in stages, and a part of the upper end surface of the inlet side furnace material 5 is held by the lower end plate 1'.

図中8はスペーサーを兼ねたバンドである。8 in the figure is a band that also serves as a spacer.

また第3図に示すように間隙部7に臨む端板1をプレス
加工することなしに従来のま)使用し、大きな間隙を形
成してもよい。
Alternatively, as shown in FIG. 3, the end plate 1 facing the gap 7 may be used as is in the conventional manner without being press-worked to form a large gap.

次に第4〜9図について他の実施例の詳細を説明すると
、上下端板1,2の中心部間に死守円筒3をとりつけ、
該死守円筒3の外周に戸紙など密な素材によって構成さ
れた2枚の菊花状炉材4゜5を互いに噛み合うように重
合的且つ同心状に配設し、両炉材4,5間に強制的に空
間部6を形成せしめる。
Next, the details of another embodiment will be explained with reference to FIGS.
Two pieces of chrysanthemum-shaped furnace materials 4.5 made of a dense material such as door paper are arranged on the outer periphery of the dead guard cylinder 3 in a polymeric and concentric manner so as to interlock with each other, and between the two furnace materials 4 and 5. The space portion 6 is forcibly formed.

そして第4図に示すように流体の流入側炉材5を流出側
炉材4より若干背高を低く即ち短尺に形威し、この炉材
5の上端縁と上部端板1との間に構成せる間隙部7を上
記空間部6に連通させたものである。
Then, as shown in FIG. 4, the fluid inflow side furnace material 5 is shaped to have a slightly lower height than the outflow side furnace material 4, that is, to have a shorter length, and between the upper edge of this furnace material 5 and the upper end plate 1. A gap 7 that can be configured is communicated with the space 6.

また上記流入、流出側炉材4,5間に強制的に空間部6
を構成するための手段としては、第6図に示すように流
入側炉材5の折ヒダ長さを流出側胛材4の折ヒダ長さよ
り短かくすることによって両炉材4,5の谷部間に空間
部6を形成せしめ、また第7図のように上記第6図と逆
に炉材のヒダ長を決定することにより両炉材4,5の頂
部間に空間部6を構成する。
Also, a space 6 is forced between the inflow and outflow side furnace materials 4 and 5.
As a means for configuring this, as shown in FIG. A space 6 is formed between the tops of both the furnace materials 4 and 5 by determining the pleat length of the furnace materials in the opposite manner to that shown in FIG. 6, as shown in FIG.

更に第8,9図に示されているように、流入側または流
出側胛材の何れか一方に凹部または凸部8を形成し、こ
の凹または凸部8によって炉材4.5間に空間部6を形
成するものである。
Furthermore, as shown in FIGS. 8 and 9, a recess or a convex part 8 is formed on either the inflow side or the outflow side material, and this concave or convex part 8 creates a space between the furnace materials 4.5. 6.

上記実施例では炉材を2枚重合したものを示したが、3
枚以上の炉材を重合的に設けてもよく、この場合流出側
の炉材を除いた他の全ての炉材を流出側胛材より短尺と
なし、これら流入側炉材の上端と上部端板との間に空間
部6に通ずる間隙部7を設ける。
In the above example, two furnace materials were polymerized, but three
More than one piece of furnace material may be provided in a polymerized manner. In this case, all the furnace materials other than the outflow side furnace material are made shorter than the outflow side furnace material, and the upper ends of these inflow side furnace materials and the upper end plate A gap 7 communicating with the space 6 is provided between the two.

また上記各実施例では間隙部7を流入側炉材5の上端縁
と上部端板との間に形成したが、これとは逆に流入側炉
材5の下端縁と下部端板2との間に形成するか或は上下
に形成してもよいので、間隙部7の構成個所については
実施例のものに特定されることはない。
Further, in each of the above embodiments, the gap 7 is formed between the upper edge of the inflow side furnace material 5 and the upper end plate, but on the contrary, the gap 7 is formed between the lower edge of the inflow side furnace material 5 and the lower end plate 2. Since the gap 7 may be formed between the two or above and below, the location of the gap 7 is not limited to that of the embodiment.

次に上記両実施例の濾過作用について説明すると、流体
は流入側炉材5の表面及び流体の一部は間隙部7を通り
炉材間の空間部6に入り更に流出側胛材4により除塵に
必要な塵埃が完全に濾過され死守円筒3より流出し所要
個所に流体は供給される。
Next, to explain the filtration action of both of the above embodiments, the fluid passes through the surface of the inflow side furnace material 5 and a part of the fluid passes through the gap 7 into the space 6 between the furnace materials, and is further removed by the outflow side fencing material 4. Necessary dust is completely filtered and flows out from the protection cylinder 3, and fluid is supplied to the required locations.

この際流入側炉材5端に間隙部7を設けることによりこ
の炉材5の内外両側の圧力差が減ぜられ、この圧力差が
少ないことにより塵埃の捕捉性能は著しく向上され、こ
のようにして流入側炉材の表面に堆積した微細塵埃は更
に堆積し炉材のもつ炉口よりも微細な塵埃も捕捉しうる
At this time, by providing a gap 7 at the end of the furnace material 5 on the inflow side, the pressure difference between the inside and outside of the furnace material 5 is reduced, and this small pressure difference significantly improves the dust trapping performance. The fine dust deposited on the surface of the furnace material on the inlet side is further deposited, and even finer dust than the furnace mouth of the furnace material can be captured.

しかしこの場合炉材の濾過抵抗は次第に大きくなり炉材
を流れる流量は小さくなるが、バイパス濾過体などの実
験によればその量は例えばエンジン潤滑油の場合、エン
ジン中を流れる通油量の3%程度あれば充分にその効果
を果している。
However, in this case, the filtration resistance of the furnace material gradually increases and the flow rate flowing through the furnace material decreases, but experiments using bypass filters have shown that, for example, in the case of engine lubricating oil, the amount of flow through the furnace material is 3 times the amount of oil flowing through the engine. If it is about %, the effect is sufficiently achieved.

勿論この場合その3%の油はきわめて清浄な油になって
いることが必要である。
Of course, in this case, the 3% oil must be extremely clean.

このように第1段階の流入側炉材5の通油抵抗が大きく
なるに従ってその濾紙に形成された間隙部7を通り流出
側胛材5に至る量が多くなることになるが、この状態が
通常の一重菊花折型のエレメントの作用となり塵埃の堆
積が次第に増加するが、前記流入側炉材5のバイパス濾
過的効果は流出側胛材4の詰まりを著しく遅らせ長寿命
で高濾過性能の濾過体が得られる。
In this way, as the oil flow resistance of the inflow side furnace material 5 in the first stage increases, the amount of oil that passes through the gap 7 formed in the filter paper and reaches the outflow side furnace material 5 increases, but this state is normal. Due to the action of the single chrysanthemum folded type element, the accumulation of dust gradually increases, but the bypass filtration effect of the inflow side furnace material 5 significantly delays the clogging of the outflow side furnace material 4, resulting in a filter body with a long life and high filtration performance. can get.

このように本考案によれば、流入側炉材のバイパス濾過
的効果により多量の塵埃捕捉能力を備え、加えて流出側
胛材は通常の菊花折型と同等の取除く必要粒子の絶対濾
過的効果を濾過体ケース内において高効率、高精度を有
し且つ長寿命が確保しうる。
As described above, according to the present invention, the inflow side furnace material has a bypass filtration effect, which has a large amount of dust trapping ability, and in addition, the outflow side furnace material has the same absolute filtration effect on the particles that need to be removed as the ordinary chrysanthemum folding type. It is possible to ensure high efficiency, high precision, and long life in the filter case.

更に流入側炉材に形成せる間隙部はこの炉材を流出側の
炉材より短尺とすることによって構成されるものである
ため、炉材の側面に小孔を穿設形成するものに比べて加
工が容易であり且つ材料の節約も計りうるなと実用上の
効果は大きい。
Furthermore, since the gap formed in the inflow side furnace material is constructed by making this furnace material shorter than the outflow side furnace material, it is smaller than the gap formed by drilling small holes on the side of the furnace material. It has great practical effects as it is easy to process and saves on materials.

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

第1図は縦断正面図、第2図は同上横断面図、第3図は
別例の縦断正面図、第4図は更に別例の縦断正面図、第
5図は同上平面図、第6〜9図は炉材の一部切欠平面図
である。 1.2・・・・・・端板、3・・・・・・死守円筒、4
,5・・・・・・炉材、6・・・・・・空間部、7・・
・・・・間隙部。
Fig. 1 is a longitudinal sectional front view, Fig. 2 is a transverse sectional view of the same as above, Fig. 3 is a longitudinal sectional front view of another example, Fig. 4 is a longitudinal sectional front view of yet another example, Fig. 5 is a plan view of the same as above, and Fig. 6 is a longitudinal sectional front view of another example. 9 are partially cutaway plan views of the furnace material. 1.2... End plate, 3... Dead guard cylinder, 4
, 5...Furnace material, 6...Space, 7...
...Gap area.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 上下端板の中心部間にとりつけられた死守円筒の外周に
少くとも2枚の菊花状炉材を同心状に配設すると)もに
上記炉材間に空間部を構成した濾過体において、上記炉
材のうち流体の流入側炉材を流出側炉材より短尺となし
、この流入側炉材の端部と端板との間に間隙部を形成し
、これを上記炉材間に構成された空間部に連通させたこ
とを特徴とする濾過体。
When at least two chrysanthemum-shaped furnace materials are arranged concentrically around the outer periphery of a dead cylinder installed between the centers of the upper and lower end plates, the above-mentioned Among the furnace materials, the furnace material on the inflow side of the fluid is made shorter than the furnace material on the outflow side, and a gap is formed between the end of the inflow side furnace material and the end plate, and this is formed between the furnace materials. A filter body characterized by communicating with a space portion.
JP3709280U 1980-03-19 1980-03-19 filter body Expired JPS6034328Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3709280U JPS6034328Y2 (en) 1980-03-19 1980-03-19 filter body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3709280U JPS6034328Y2 (en) 1980-03-19 1980-03-19 filter body

Publications (2)

Publication Number Publication Date
JPS56137718U JPS56137718U (en) 1981-10-19
JPS6034328Y2 true JPS6034328Y2 (en) 1985-10-14

Family

ID=29632667

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3709280U Expired JPS6034328Y2 (en) 1980-03-19 1980-03-19 filter body

Country Status (1)

Country Link
JP (1) JPS6034328Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6028218B2 (en) * 2011-05-27 2016-11-16 パナソニックIpマネジメント株式会社 Humidifier

Also Published As

Publication number Publication date
JPS56137718U (en) 1981-10-19

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