JPH06182120A - Filtering or filtering/dust collecting base material - Google Patents

Filtering or filtering/dust collecting base material

Info

Publication number
JPH06182120A
JPH06182120A JP33754292A JP33754292A JPH06182120A JP H06182120 A JPH06182120 A JP H06182120A JP 33754292 A JP33754292 A JP 33754292A JP 33754292 A JP33754292 A JP 33754292A JP H06182120 A JPH06182120 A JP H06182120A
Authority
JP
Japan
Prior art keywords
filtering
filtration
base material
dust collecting
solid particles
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.)
Pending
Application number
JP33754292A
Other languages
Japanese (ja)
Inventor
Jingo Nakazawa
仁吾 中沢
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP33754292A priority Critical patent/JPH06182120A/en
Publication of JPH06182120A publication Critical patent/JPH06182120A/en
Pending legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

PURPOSE:To provide a filtering or filtering/dust collecting base material requiring no filter aid. CONSTITUTION:In the filtering or filtering/dust collecting base material formed into a thin almost disc shape having a through-hole at its almost central part and performing filtering or filtering/dust removal through the gaps formed between the adjacent base materials at the time of lamination, uniform unevenness is formed to both upper and rear surfaces thereof and degree of unevenness is set corresponding to the particle size of solid particles to be removed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、液体や気体等の各種
流体から混在する固体粒子を濾過又は濾過集塵するため
の濾過又は濾過集塵基材に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filtration or filtration dust collecting base material for filtering or dust collecting solid particles mixed from various fluids such as liquid and gas.

【0002】[0002]

【従来の技術】従来より、図4に示すような濾過又は濾
過集塵基材1(この明細書では併せて適宜単に濾過基材
1という)を積層し、隣接する前記基材1間で形成され
る間隙から液体や気体等の各種流体の流動層を通過さ
せ、間隙の夫々より大きな固体粒子を分離することによ
り濾過又は濾過集塵を行っている。
2. Description of the Related Art Conventionally, a filtration or filtration dust collecting base material 1 as shown in FIG. 4 (collectively referred to as a filtration base material 1 in this specification) is laminated and formed between adjacent base materials 1. The fluidized beds of various fluids such as liquids and gases are passed through the gaps to separate larger solid particles in the respective gaps, thereby performing filtration or filtration dust collection.

【0003】この濾過基材1は略中央部に通孔10を有
する薄板円盤状に形成されているとともに、その表裏両
面には前記流動層を通過させる間隙を形成するための複
数の突起5が突出形成されている。そして、図5に示す
ように、前記濾過基材1を複数枚同芯状に積層して円筒
状の濾材を形成せしめ、この円筒状の濾材の外周側に位
置せしめた流体から濾材の内周側へと、隣接する濾過基
材1間の夫々に於いて形成される間隙の各々より小さな
固体粒子及び流動層を通過させ濾過又は濾過集塵を行
う。隣接する基材1間で形成される間隙よりも更に小さ
な固体粒子まで除去する場合には、濾材の周囲に所望の
濾過粒径に応じた濾過助剤により濾過助剤層6を形成し
ておく。
This filtering substrate 1 is formed in a thin disk shape having a through hole 10 in its substantially central portion, and a plurality of projections 5 for forming gaps for passing the fluidized bed are formed on both front and back surfaces thereof. It is formed to project. Then, as shown in FIG. 5, a plurality of the filtration base materials 1 are laminated concentrically to form a cylindrical filter medium, and the inner periphery of the filter medium is separated from the fluid positioned on the outer peripheral side of the cylindrical filter medium. To the side, solid particles smaller than each of the gaps formed in each of the adjacent filter substrates 1 and a fluidized bed are passed to perform filtration or filter dust collection. When removing even solid particles smaller than the gap formed between the adjacent base materials 1, the filter aid layer 6 is formed around the filter medium with a filter aid according to the desired filter particle size. .

【0004】ところが、上記の様に濾過助剤を用いると
濾過基材間の間隙よりも小さな固体粒子の除去が可能と
なるが、作業が煩雑になるという不具合が生じる。
However, when the filter aid is used as described above, it is possible to remove solid particles smaller than the gap between the filtration base materials, but the work becomes complicated.

【0005】[0005]

【発明が解決しようとする課題】そこで、この発明で
は、濾過助剤を必要としない濾過又は濾過集塵基材を提
起することを課題とする。
Therefore, an object of the present invention is to provide a filtration or filtration dust collecting base material which does not require a filter aid.

【0006】[0006]

【課題を解決するための手段】前記課題を解決するため
に、この発明では次のような技術的手段を講じている。
即ち、略中央部に通孔10を有する薄板略円盤状に形成
され、積層した際に隣接し合うものの間で形成される間
隙により濾過又は濾過集塵を行う濾過又は濾過集塵基材
において、その表裏両面に一様に凹凸が形成されるとと
もに、前記凹凸の度合いは除去すべき固体粒子の粒径に
応じて設定されていることとした。
In order to solve the above problems, the present invention takes the following technical means.
That is, in a filtering or filtering dust collecting base material which is formed in a thin plate substantially disc shape having a through hole 10 at a substantially central portion and which filters or collects dust by a gap formed between adjacent ones when laminated, Irregularities are uniformly formed on both front and back surfaces, and the degree of the irregularities is set according to the particle size of the solid particles to be removed.

【0007】[0007]

【作用】上記の手段を採用した結果、この発明は以下の
ような作用を有する。この発明の濾過基材を積層して濾
過を行う際、隣接し合う濾過基材間には相互に当接すべ
き面に形成されている一様な凹凸により一定の間隙が生
じる。基材の表裏両面の凹凸の度合いは除去すべき固体
粒子の粒径に応じて設定されているので、所望の濾過粒
径に応じた間隙を得ることが出来る。
As a result of adopting the above means, the present invention has the following effects. When the filtration base materials of the present invention are laminated and filtered, a constant gap is formed between the adjacent filtration base materials due to the uniform unevenness formed on the surfaces to be brought into contact with each other. Since the degree of unevenness on the front and back surfaces of the substrate is set according to the particle size of the solid particles to be removed, it is possible to obtain a gap corresponding to the desired filtration particle size.

【0008】[0008]

【実施例】以下、この発明の濾過基材を実施例として示
した図面に従って説明する。図1はこの実施例の濾過基
材1を示すもので、セラミック材により略中央部に通孔
10を有する薄板円盤状に形成されている。その表裏両
面には一様に凹凸を形成しているとともに、前記凹凸の
度合いは除去すべき固体粒子の粒径に応じて設定してい
る。この実施例では前記凹凸を1μ程度の高さの梨地模
様として形成した。この濾過基材1を積層した際、隣接
し合うもの同士の間で形成される間隙により濾過又は濾
過集塵処理を行う。この実施例の濾過基材1では、粒径
が2μ程度以上の固体粒子を除去することが出来た。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The filtration substrate of the present invention will be described below with reference to the drawings shown as embodiments. FIG. 1 shows a filter substrate 1 of this embodiment, which is formed of a ceramic material in the shape of a thin disk having a through hole 10 at a substantially central portion. Irregularities are uniformly formed on both the front and back surfaces, and the degree of the irregularities is set according to the particle size of the solid particles to be removed. In this example, the unevenness was formed as a satin pattern having a height of about 1 μ. When the filtration base materials 1 are stacked, filtration or filtration dust collection processing is performed by the gaps formed between adjacent ones. In the filtration base material 1 of this example, solid particles having a particle size of about 2 μm or more could be removed.

【0009】この濾過基材1は、ジルコニア・セラミッ
クを焼成して製造することができる。図2及び図3は上
記のような濾過基材1を用いて構成した濾過装置の一例
であり、その構成を説明する。図3は濾過又は濾過集塵
により得られた流動層を導き出すための筒(以下、流動
層導出筒2という)を示している。この流動層導出筒2
は複数の穿孔20が各面に穿設され、円筒状に形成する
濾過基材1の積層体の内周側に挿入すべき中空の角筒2
Aと、この角筒2Aの両端に溶接により取付けられたボ
ルト部21とから成る。両端のボルト部21のうち流動
層の導出側のものにのみその軸芯方向に導孔22が穿設
され、この導孔22から濾過又は濾過集塵により得られ
た流動層が導き出される。
The filter substrate 1 can be manufactured by firing zirconia ceramic. FIG. 2 and FIG. 3 are examples of the filtering device configured by using the filtering substrate 1 as described above, and the configuration will be described. FIG. 3 shows a cylinder (hereinafter referred to as a fluidized bed outlet cylinder 2) for leading out a fluidized bed obtained by filtration or filtration dust collection. This fluidized bed outlet cylinder 2
Is a hollow square tube 2 having a plurality of perforations 20 formed on each surface thereof and to be inserted into an inner peripheral side of a laminated body of filtration base materials 1 formed in a cylindrical shape.
A and a bolt portion 21 attached to both ends of the square tube 2A by welding. A guide hole 22 is bored in the axial direction of only one of the bolt portions 21 at both ends on the fluidized bed outlet side, and the fluidized bed obtained by filtration or filter dust collection is led out from the guide hole 22.

【0010】導孔22を有するボルト部21はワッシャ
ー及びスプリングワッシャーを介してナットにより流動
層区画壁3に取付けられる。流動層区画壁3は濾過又は
濾過集塵以前の未処理の流体の収容槽(以下、未処理槽
3Aという)と処理済の流動層の収容槽(以下、処理済
槽3Bという)との混合を防止するためのものである。
The bolt portion 21 having the guide hole 22 is attached to the fluidized-bed partition wall 3 by a nut through a washer and a spring washer. The fluidized bed partition wall 3 is a mixture of an untreated fluid storage tank (hereinafter referred to as untreated tank 3A) and a treated fluidized bed storage tank (hereinafter referred to as treated tank 3B) before filtration or filtration dust collection. Is to prevent.

【0011】流動層導出筒2の外周側に濾過基材1の積
層体を形成する際には、前記ナットの螺合を解除して流
動層導出筒2を流動層区画壁3から取り外した後、その
他端側のボルト部21に螺合せしめたナットとワッシャ
ーとスプリングワッシャーとの間に、濾過基材1を積層
する。然る後、流動層区画壁3に固定する。流体を濾過
又は濾過集塵する際には、次の様にして行う。未処理槽
3Aの下端部近傍に設けた流入口30から濾過又は濾過
集塵すべき流体をこの未処理槽3Aに流入させる。未処
理槽3Aの流体にある程度圧力をかけていくと、濾材の
隣接する濾過基材1間の多層の間隙の夫々より大きな粒
径の固体粒子が分離され、前記間隙より小さな固体粒子
及び流動層のみを前記濾材の内周側へと通過させること
により濾過又は濾過集塵を行う。
When the laminated body of the filtration base material 1 is formed on the outer peripheral side of the fluidized bed lead-out tube 2, after the nut is unscrewed and the fluidized bed lead-out tube 2 is removed from the fluidized bed partition wall 3. The filter substrate 1 is laminated between the nut, the washer, and the spring washer screwed to the bolt portion 21 on the other end side. After that, it is fixed to the fluidized-bed partition wall 3. When the fluid is filtered or dust is collected by filtration, it is performed as follows. A fluid to be filtered or dust-collected is caused to flow into the untreated tank 3A from an inflow port 30 provided near the lower end of the untreated tank 3A. When a certain amount of pressure is applied to the fluid in the untreated tank 3A, solid particles having a larger particle size are separated from each other in the multi-layered gap between the adjacent filter base materials 1 of the filter medium, and the solid particles smaller than the gap and the fluidized bed are separated. Filtering or filtration dust collection is performed by passing only the inner side of the filter medium.

【0012】濾過基材1の積層体の内周側へと到った流
動層は、穿孔20を介して流動層導出筒2内に到り導孔
22から処理済槽3Bへと送られる。こうして、流体の
濾過又は濾過集塵を行うことができる。ある程度濾過又
は濾過集塵を行い濾滓が溜まってくると一旦この濾過操
作を中断し、所謂逆洗浄をおこなう。この濾過基材1を
積層して濾過を行う際、隣接し合う濾過基材1間には相
互に当接すべき面に形成されている一様な凹凸により一
定の間隙が生じる。基材1の表裏両面の凹凸の度合いは
除去すべき固体粒子の粒径に応じて設定されているの
で、所望の濾過粒径に応じた間隙を得ることが出来る。
従って、濾過助剤を必要としない濾過又は濾過集塵基材
1を得ることが出来る。
The fluidized bed which has reached the inner peripheral side of the laminated body of the filter substrate 1 reaches the fluidized bed outlet cylinder 2 through the perforations 20 and is sent from the guide hole 22 to the treated tank 3B. In this way, the fluid can be filtered or filtered and dust can be collected. After filtering or filtering dust to some extent and once the filter residue is collected, this filtering operation is once interrupted and so-called back washing is performed. When the filtration base materials 1 are stacked and filtered, a constant gap is formed between the adjacent filtration base materials 1 due to the uniform unevenness formed on the surfaces to be brought into contact with each other. Since the degree of unevenness on the front and back surfaces of the base material 1 is set according to the particle size of the solid particles to be removed, it is possible to obtain a gap according to the desired filtration particle size.
Therefore, it is possible to obtain the filtration or filtration dust collection substrate 1 which does not require a filter aid.

【0013】[0013]

【発明の効果】この発明は上述のような構成を有するも
のであり、所望の濾過粒径に応じた間隙を得ることが出
来るので、濾過助剤を必要としない濾過又は濾過集塵基
材を提供することが出来る。
EFFECTS OF THE INVENTION The present invention has the above-mentioned constitution, and since a gap corresponding to a desired filtration particle size can be obtained, a filtration or filtration dust collection base material which does not require a filter aid is provided. Can be provided.

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

【図1】この発明の濾過基材の全体斜視図。FIG. 1 is an overall perspective view of a filtration substrate of the present invention.

【図2】図1の濾過基材を用いて構成した濾過装置の一
例の使用状態を説明する断面図。
FIG. 2 is a cross-sectional view illustrating a usage state of an example of a filtering device configured by using the filtering base material of FIG.

【図3】図1の濾過基材を用いて構成する濾過装置の一
例に用いる流動層導出筒及び流動層区画壁の側面図。
FIG. 3 is a side view of a fluidized bed outlet cylinder and a fluidized bed partition wall used in an example of a filtration device configured using the filtration base material of FIG. 1.

【図4】従来の濾過基材の全体斜視図。FIG. 4 is an overall perspective view of a conventional filtration substrate.

【図5】図4の濾過基材を用いて構成した濾過装置の一
例の使用状態を説明する一部拡大断面図。
FIG. 5 is a partially enlarged cross-sectional view illustrating a usage state of an example of a filtering device configured using the filtering base material of FIG.

【符号の説明】[Explanation of symbols]

10 通孔 10 through holes

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 略中央部に通孔を有する薄板略円盤状に
形成され、積層した際に隣接し合うものの間で形成され
る間隙により濾過又は濾過集塵を行う濾過又は濾過集塵
基材において、 その表裏両面に一様に凹凸が形成されるとともに、前記
凹凸の度合いは除去すべき固体粒子の粒径に応じて設定
されていることを特徴とする濾過又は濾過集塵基材。
1. A filtering or filtering dust collecting base material which is formed in a thin plate substantially disk shape having a through hole at a substantially central portion and which filters or collects dust by a gap formed between adjacent ones when laminated. In the above, the filtration or filtration dust collecting substrate is characterized in that unevenness is uniformly formed on both front and back surfaces thereof, and the degree of the unevenness is set according to the particle diameter of the solid particles to be removed.
JP33754292A 1992-12-17 1992-12-17 Filtering or filtering/dust collecting base material Pending JPH06182120A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33754292A JPH06182120A (en) 1992-12-17 1992-12-17 Filtering or filtering/dust collecting base material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33754292A JPH06182120A (en) 1992-12-17 1992-12-17 Filtering or filtering/dust collecting base material

Publications (1)

Publication Number Publication Date
JPH06182120A true JPH06182120A (en) 1994-07-05

Family

ID=18309638

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33754292A Pending JPH06182120A (en) 1992-12-17 1992-12-17 Filtering or filtering/dust collecting base material

Country Status (1)

Country Link
JP (1) JPH06182120A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7344579B2 (en) 2004-01-06 2008-03-18 Powerchip Semiconductor Corp. Pipe trap
JP2015034786A (en) * 2013-08-09 2015-02-19 アズビル株式会社 Capacitive pressure sensor
CN105214363A (en) * 2015-10-26 2016-01-06 北京康洁之晨水处理技术有限公司 A kind of filter-specific lamination

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7344579B2 (en) 2004-01-06 2008-03-18 Powerchip Semiconductor Corp. Pipe trap
JP2015034786A (en) * 2013-08-09 2015-02-19 アズビル株式会社 Capacitive pressure sensor
CN105214363A (en) * 2015-10-26 2016-01-06 北京康洁之晨水处理技术有限公司 A kind of filter-specific lamination

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