JPH0531308A - Multistage type filter for continuous operation - Google Patents
Multistage type filter for continuous operationInfo
- Publication number
- JPH0531308A JPH0531308A JP19199891A JP19199891A JPH0531308A JP H0531308 A JPH0531308 A JP H0531308A JP 19199891 A JP19199891 A JP 19199891A JP 19199891 A JP19199891 A JP 19199891A JP H0531308 A JPH0531308 A JP H0531308A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- filters
- valves
- unit
- shut
- 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
Links
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、流体、粉体の異物を除
去する濾過装置に関するものである。特に目詰りのしや
すい濾過物質を取扱う場合の濾過装置に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filtering device for removing foreign matters such as fluid and powder. Particularly, the present invention relates to a filter device for handling a filter substance that is easily clogged.
【0002】[0002]
【従来の技術】従来は濾過器に圧力検知器を、濾過器の
前後に閉止弁を、それぞれ設けてなる単位濾過装置を用
い、濾過器に取付ける濾材は濾過すべき物質の最小メッ
シュに合わせて設けていた。2. Description of the Related Art In the past, a pressure detector was installed in a filter, and shut-off valves were installed in front of and behind the filter, respectively. A unit filter device was used, and the filter material attached to the filter was adjusted to the minimum mesh of the substance to be filtered. It was provided.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、このよ
うな単位濾過装置においては目詰りのしやすい濾過物質
を取扱う場合は、濾過器の圧力検知器はすぐに詰りを知
らせて、濾材交換を頻繁に行なわなければならず、その
都度生産の流れを停止しなければならなかった。この場
合は更に濾材及び濾過物質の消耗損失も多く、不経済で
あり、又濾材に詰る異物の分析もやりにくかった。However, when handling a filter substance that is easily clogged in such a unit filtration device, the pressure detector of the filter immediately notifies the clogging, and frequent replacement of the filter medium is required. It had to be done, and the production flow had to be stopped each time. In this case, the filter material and the filter substance are also consumed in a large amount, which is uneconomical, and it is difficult to analyze foreign substances clogging the filter material.
【0004】本発明の目的は、前記した従来技術の欠点
を解消し、濾材の交換、点検で生産を停止することな
く、濾材の寿命を伸ばし、濾過物質の損失を少くし更に
濾材につまる異物の分析もやり易い濾過装置を提供する
ことにある。The object of the present invention is to solve the above-mentioned drawbacks of the prior art, to extend the life of the filter medium, to reduce the loss of the filter substance, and to prevent foreign substances from clogging the filter medium, without stopping the production by replacing or inspecting the filter medium. The object is to provide a filtration device that is easy to analyze.
【0005】[0005]
【課題を解決するための手段及び作用】本発明の上記目
的は、濾過器に圧力検知器を、濾過器の前後に閉止弁
を、それぞれ設けてなる単位濾過装置を、流路に並列に
三系統設置し、かつ各系統にそれぞれ直列に2基以上の
前記単位濾過装置を設置し、上流に設置する単位濾過装
置に装着する濾材メッシュを、下流に設置する単位濾過
装置に装着する濾材のメッシュよりも粗くし、かつ各系
統の単位濾過装置を各段毎に共通管によって連結し、交
互に切換えて使用することを特徴とする多段式連続運転
用濾過装置によって達成される。SUMMARY OF THE INVENTION The above object of the present invention is to provide a filter unit with a pressure detector, and a filter unit with front and rear shutoff valves. A filter mesh that is installed in a system and in which two or more unit filtration devices are installed in series in each system, and the filter media mesh that is installed in the unit filtration device that is installed upstream is installed in the unit filtration device that is installed in the downstream system. It is achieved by a multi-stage continuous operation filtration device which is characterized in that it is made coarser and unit filters of each system are connected by a common pipe for each stage and alternately switched.
【0006】本発明は、使用する濾過材の種類には特に
制限はなく用いることが出来る。The present invention can be used without any particular limitation on the type of filter material used.
【0007】本発明に用いる閉止弁としては電磁弁を用
いると自動制御に便利である。It is convenient for automatic control to use a solenoid valve as the stop valve used in the present invention.
【0008】本発明において単位濾過装置を、流路に並
列に三系統設けるということは、2系統を常時切換に、
1系統を予備に持つことによって、いかなることが生じ
ても濾過装置によって生産ラインを停止することをなく
すためのものである。又3系統を順次に切換えてもよ
い。In the present invention, the provision of three systems of the unit filtration device in parallel with the flow path means that the two systems are constantly switched,
By having one system as a backup, it is possible to prevent the production line from being stopped by the filtration device in any event. Also, the three systems may be switched sequentially.
【0009】本発明において上流に設置する単位濾過装
置に装着する濾材のメッシュを下流に設置する単位濾過
装置に装着する濾材のメッシュよりも粗くすることによ
って、前段の濾過装置で粗い粒子が濾過され、細い粒子
は次の濾過装置で濾過されるために、濾材の目詰りする
迄の時間が長くなり、即ち濾材の寿命が長く保たれ、か
つ更に後段の濾材を従来のメッシュよりも細く選定する
ことも可能となり、濾過効率を上げることが出来る。In the present invention, by making the mesh of the filter medium mounted on the upstream unit filtration device coarser than the mesh of the filter medium mounted on the downstream unit filtration device, coarse particles are filtered by the preceding filtration unit. Since fine particles are filtered by the next filtration device, the time until clogging of the filter medium becomes long, that is, the life of the filter medium is kept long, and the filter medium at the subsequent stage is selected to be finer than the conventional mesh. It is also possible to increase the filtration efficiency.
【0010】尚、各系統の単位濾過装置を各段毎に共通
管によって連結し、交互に切換えて使用することによっ
て、更に装置の運転の自由度を増すことが出来て、濾過
効率を上げることが出来る。By connecting the unit filtration devices of each system with a common pipe for each stage and alternately switching and using them, it is possible to further increase the degree of freedom of operation of the devices and increase the filtration efficiency. Can be done.
【0011】[0011]
【実施例】本発明の多段式連続運転用濾過装置の2段の
場合の一実施例を図を用いて説明する。但し本発明は本
実施例のみに限られない。3段でも4段でもよい。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the multi-stage continuous operation filtration device of the present invention having two stages will be described with reference to the drawings. However, the present invention is not limited to this embodiment. It may be 3 steps or 4 steps.
【0012】図1に示すように矢印は流体、粉体の流れ
の方向を示す。単位濾過装置の三系統としてはA、B、
Cの三系統で濾過器A1 (9)、濾過器B1 (10)、
濾過材C1 (11)にそれぞれ閉止弁A1 、A3 (3、
6)、閉止弁B1 、B3 (4、7)、閉止弁C1、C3
(5、8)を濾過器の前後に備えた配置になっており、
この3ケの単位濾過装置を第1段とする。濾過器の濾材
のメッシュは濾過器A1 (9)、濾過器B1 (10)、
濾過器C1 (11)は同じメッシュのものとし、第2段
の濾過器A2 (18)、濾過器B2 (19)、濾過器C
2 (20)の濾材メッシュより粗くする。As shown in FIG. 1, arrows indicate the directions of flow of fluid and powder. The three systems of unit filtration device are A, B,
Filters A1 (9), Filter B1 (10),
The filter media C1 (11) are provided with shut-off valves A1, A3 (3,
6), stop valves B1, B3 (4, 7), stop valves C1, C3
It is arranged with (5, 8) before and after the filter,
The three unit filtration devices are the first stage. The filter material mesh of the filter is a filter A1 (9), a filter B1 (10),
The filter C1 (11) has the same mesh, and the second stage filter A2 (18), filter B2 (19), and filter C
2 Make it coarser than the filter mesh of (20).
【0013】例えば閉止弁の開閉を表1のI、II、III
の順序に切換えることにより、連続運転を行うことが出
来る。この際第1段階はどの濾過系統を選んでもよく、
且つ、各系統の単位濾過装置の各段毎の共通管を用いて
第1段より第2段へ3つの濾過器のいずれかを通して流
体、粉体が流すことも出来る。For example, for opening and closing the shutoff valve, I, II and III in Table 1 are used.
Continuous operation can be performed by switching to the order of. At this time, any filtration system may be selected in the first stage,
In addition, the fluid and powder can be made to flow from any of the three filters from the first stage to the second stage by using a common pipe for each stage of the unit filtration device of each system.
【0014】[0014]
【表1】 [Table 1]
【0015】又第1表のIかIIの通常の流れとし、Iと
IIに異常のあった場合IIの状態にすることも出来る。濾
過装置の濾材に目詰りが起ると濾過器にかかる圧力が上
昇することによって判るので、各濾過器には、圧力検知
器21、22、23、24、25、26を取付け、使用
している濾過器についている閉止弁を電磁弁とし閉止弁
の開閉状況を電気的に第1表のごとく回路を組み、圧力
の高低で自動的にI、II、III の状況を選ぶようにす
る。即ち濾過器A1 を使用中卯圧力が上昇した場合IIの
状態にし、濾過器B1 を使用中に圧力が上昇した場合I
の状態にする。Iの状態からIIの状態へ、IIの状態から
Iの状態に切換える時1時的に両方の閉止弁を開く時間
をとっておく。III の変る時も同様である。第2段以降
も同じ原理に従う。濾過器の濾材のメッシュは段数が多
くなれば流れの下流のものほど細くする。濾過器の交
換、点検は濾過器前後の閉止弁が閉じている時に行う。
電気的回路が組めぬ場合は圧力検知器を見て閉止弁の開
閉を手動とすることもできる。In addition, in the normal flow of I or II in Table 1, I
If there is something wrong with II, you can put it in II state. When the filter material of the filter device is clogged, it can be seen that the pressure applied to the filter rises. Therefore, pressure detectors 21, 22, 23, 24, 25, 26 are attached to each filter and used. A solenoid valve is used as the shut-off valve attached to the filter, and a circuit is electrically constructed as shown in Table 1 to open and close the shut-off valve, so that I, II, and III situations are automatically selected depending on the pressure level. That is, when the pressure of the filter A1 is increased during use, the condition II is set, and when the pressure is increased during use of the filter B1 I
To the state of. When switching from the state I to the state II, and from the state II to the state I, it is necessary to temporarily set a time for opening both the closing valves. The same applies when III changes. The second and subsequent stages follow the same principle. As the number of stages of the filter medium of the filter increases, the mesh becomes thinner toward the downstream side of the flow. Replace and check the filter when the stop valves before and after the filter are closed.
When the electric circuit cannot be assembled, the shutoff valve can be opened and closed manually by looking at the pressure detector.
【0016】[0016]
【発明の効果】本発明の多段式連続運転用濾過装置によ
り 1 管路の流れを停止することなく濾過装置の交換点検
ができる。EFFECTS OF THE INVENTION The filtration apparatus for multistage continuous operation according to the present invention enables replacement and inspection of the filtration apparatus without stopping the flow of the pipe line.
【0017】2 濾過器にかかる負荷がメッシュ毎に大
から小に分けられるので、濾材交換回数がへる。(2) Since the load applied to the filter is divided into large and small for each mesh, the number of times the filter medium needs to be replaced is reduced.
【0018】3 圧力で検知するため、異物の除去作業
が均一化される。Since the pressure is used for detection, the foreign matter removing operation is made uniform.
【0019】4 異物の分析が、異物の大きさが一定し
ているため、やりやすい。4. Foreign matter analysis is easy because the size of the foreign matter is constant.
【0020】5 流体、粉体の流れを制御する機器を稼
働する時は、必ず各段のどれかの濾過器の閉止弁のバル
ブが開いていないと稼働できないように、連動させるこ
とができる。5 When the equipment for controlling the flow of fluid and powder is operated, it can be operated so that it cannot be operated unless the valve of the closing valve of any one of the filters of each stage is opened.
【図1】本発明の多段式連続運転用濾過装置の2段の装
置を示すフローシート図である。FIG. 1 is a flow sheet diagram showing a two-stage device of a multi-stage type continuous operation filtration device of the present invention.
1 主幹管 2 主幹弁 3 閉止弁A1 4 〃 B1 5 〃 C1 6 閉止弁A3 7 〃 B3 8 〃 C3 9 濾過器A1 10 〃 B1 11 〃 C1 12 閉止弁A2 13 〃 B2 14 〃 C2 15 閉止弁A4 16 〃 B4 17 〃 C4 18 濾過器A2 19 〃 B2 20 〃 C2 21 圧力検知器A1 22 〃 B1 23 〃 C1 24 〃 A2 25 〃 B2 26 〃 C2 1 main pipe 2 main valve 3 stop valve A1 4 〃 B1 5 〃 C1 6 stop valve A3 7 〃 B3 8 〃 C3 9 filter A1 10 〃 B1 11 〃 C1 12 stop valve A2 B2 15 〃 14 16 〃 B4 17 〃 C4 18 Filter A2 19 〃 B2 20 〃 C2 21 Pressure detector A1 22 〃 B1 23 〃 C1 24 〃 A2 25 〃 B2 26 〃 C2
Claims (1)
止弁を、それぞれ設けてなる単位濾過装置を流路に並列
し三系統設置し、かつ各系統はそれぞれ直列に2基以上
の前期単位濾過器を設置し、最初の上流に設置する単位
濾過装置に装着する濾材メッシュを、下流に設置する単
位濾過装置に装着する濾材のメツシュよりも粗くし、か
つ各系統の単位濾過装置を段毎に共通管によって連結
し、交互に切換えて使用することを特徴とする多段式連
続運転用濾過装置。Claim: What is claimed is: 1. A filter is provided with a pressure detector, a filter is provided with shut-off valves in front of and behind the filter, and three system units are installed in parallel in a flow path. In each case, two or more unit filtration units of the previous term are installed in series, and the filter medium mesh attached to the unit filtration device installed first upstream is made coarser than the mesh of the filter medium attached to the unit filtration device installed downstream, and A multistage continuous operation filtration device characterized in that the unit filtration devices of each system are connected by a common pipe for each stage and alternately switched.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19199891A JPH0531308A (en) | 1991-07-31 | 1991-07-31 | Multistage type filter for continuous operation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19199891A JPH0531308A (en) | 1991-07-31 | 1991-07-31 | Multistage type filter for continuous operation |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0531308A true JPH0531308A (en) | 1993-02-09 |
Family
ID=16283913
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19199891A Pending JPH0531308A (en) | 1991-07-31 | 1991-07-31 | Multistage type filter for continuous operation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0531308A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0995969A (en) * | 1995-10-03 | 1997-04-08 | Katsumi Kitanaka | Separation method of muddy water containing earth, sand, gravel, and the like and device thereof |
JP2002011310A (en) * | 2000-06-29 | 2002-01-15 | Japan Organo Co Ltd | Method of operating high temperature filtration apparatus |
WO2002066140A1 (en) * | 2001-02-19 | 2002-08-29 | E. Begerow Gmbh & Co. | Method and device for filtering liquids, especially drinks |
JP2012201729A (en) * | 2011-03-24 | 2012-10-22 | Nippon Shokubai Co Ltd | Method for producing thermoplastic resin containing reduced amount of foreign matter, method for producing thermoplastic resin composition containing reduced amount of foreign matter, and method for producing thermoplastic resin molded article containing reduced amount of foreign matter |
JP2016203115A (en) * | 2015-04-24 | 2016-12-08 | Icras株式会社 | Physical filtration device |
CN110170206A (en) * | 2019-06-03 | 2019-08-27 | 嘉兴莲衫服装有限公司 | A kind of production line production vaccine efficiently manages controlling terminal |
CN116173656A (en) * | 2023-04-25 | 2023-05-30 | 山东商博生物科技有限公司 | Feed production waste gas purification treatment equipment and process |
-
1991
- 1991-07-31 JP JP19199891A patent/JPH0531308A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0995969A (en) * | 1995-10-03 | 1997-04-08 | Katsumi Kitanaka | Separation method of muddy water containing earth, sand, gravel, and the like and device thereof |
JP2002011310A (en) * | 2000-06-29 | 2002-01-15 | Japan Organo Co Ltd | Method of operating high temperature filtration apparatus |
WO2002066140A1 (en) * | 2001-02-19 | 2002-08-29 | E. Begerow Gmbh & Co. | Method and device for filtering liquids, especially drinks |
US6951614B2 (en) | 2001-02-19 | 2005-10-04 | E. Begerow Gmbh & Co. | Method and device for filtering liquids, especially drinks |
JP2012201729A (en) * | 2011-03-24 | 2012-10-22 | Nippon Shokubai Co Ltd | Method for producing thermoplastic resin containing reduced amount of foreign matter, method for producing thermoplastic resin composition containing reduced amount of foreign matter, and method for producing thermoplastic resin molded article containing reduced amount of foreign matter |
JP2016203115A (en) * | 2015-04-24 | 2016-12-08 | Icras株式会社 | Physical filtration device |
CN110170206A (en) * | 2019-06-03 | 2019-08-27 | 嘉兴莲衫服装有限公司 | A kind of production line production vaccine efficiently manages controlling terminal |
CN116173656A (en) * | 2023-04-25 | 2023-05-30 | 山东商博生物科技有限公司 | Feed production waste gas purification treatment equipment and process |
CN116173656B (en) * | 2023-04-25 | 2023-07-04 | 山东商博生物科技有限公司 | Feed production waste gas purification treatment equipment and process |
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