JPH0256121B2 - - Google Patents
Info
- Publication number
- JPH0256121B2 JPH0256121B2 JP60046974A JP4697485A JPH0256121B2 JP H0256121 B2 JPH0256121 B2 JP H0256121B2 JP 60046974 A JP60046974 A JP 60046974A JP 4697485 A JP4697485 A JP 4697485A JP H0256121 B2 JPH0256121 B2 JP H0256121B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- tank
- cleaning
- valve
- air
- 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
Links
- 239000007788 liquid Substances 0.000 claims description 108
- 238000004140 cleaning Methods 0.000 claims description 36
- 238000001914 filtration Methods 0.000 claims description 23
- 238000012545 processing Methods 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 2
- 238000003860 storage Methods 0.000 description 18
- 230000000694 effects Effects 0.000 description 6
- 238000011001 backwashing Methods 0.000 description 5
- 238000004891 communication Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000002788 crimping Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 238000011086 high cleaning Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
<産業上の利用分野>
本発明は、メツキ処理液等の汚濁液を清浄にす
る濾過機において、その濾過部材の目詰まりを防
止するめに、濾過部材に詰まつた濾塵を除去する
濾過装置の濾過部材洗浄方法に関する。[Detailed Description of the Invention] <Industrial Application Field> The present invention provides a method for preventing clogging of the filtration member in a filtration machine that cleans a polluted liquid such as a plating solution. The present invention relates to a method for cleaning a filter member of a filter device for removing filter dust.
<従来技術>
濾過部材を濾過機から除去して洗浄するという
原始的で非能率な洗浄方法に換えて、これを濾過
機に装着したまま自動的に洗浄する方法がある。
この種の従来方法は、前記濾過部材で一旦浄化し
た清浄液をポンプ等で逆流させて洗浄したり、ま
たはエアーを逆方向から吹付けたりしているもの
である。<Prior Art> Instead of the primitive and inefficient cleaning method of removing the filter member from the filter and cleaning it, there is a method of automatically cleaning the filter member while it is attached to the filter.
In this type of conventional method, the cleaning liquid that has been purified by the filtering member is made to flow backwards using a pump or the like, or air is blown from the opposite direction.
<発明が解決しようとする問題点>
ところで前者の方法は単位時間当りの流量が小
さいから、長時間流しても思うような逆洗処理を
施すことができず、所定の洗浄を施すためには清
浄化した液を大量に使用することとなり、また駆
動時間が長く、大容量のポンプを要する等装置が
高価となる等の欠点がある。後者は濾過部材の出
口側の清浄な液を除去してから施す必要があつ
て、迅速さを欠き、かつ大きなエアー圧力を要
し、しかも濾過装置の構造が複雑となる等の欠点
があり、いずれの方法も効率的とはいえなかつ
た。<Problems to be Solved by the Invention> However, in the former method, the flow rate per unit time is small, so even if the flow is allowed to run for a long time, it is not possible to perform the desired backwashing process. This method requires a large amount of purified liquid, requires a long drive time, requires a large-capacity pump, and has disadvantages such as an expensive device. The latter method requires removal of the clean liquid from the outlet side of the filtration member before application, and has disadvantages such as being slow, requiring large air pressure, and complicating the structure of the filtration device. Neither method could be called efficient.
本発明は、簡易な構成で実現でき、かつ清浄液
の使用を可及的にすくなくでき、しかも洗浄効果
の高い洗浄方法の提供を目的とするものである。 An object of the present invention is to provide a cleaning method that can be realized with a simple configuration, can reduce the use of cleaning liquid as much as possible, and has a high cleaning effect.
<問題点を解決するための手段>
本発明は、処理液を供給する流入口と、処理液
を排出するドレイン口と、液面に作用する圧力空
気を導入するエアー通入弁とを備えたタンク内
に、上下方向に1〜複数個の液溜室を設け、前記
液溜室の下面開口に濾過部材を配設し、さらに前
記液溜室内を清浄液の流出口に連通してなる構成
の濾過装置であつて、前記濾過部材の洗浄を次の
工程で施すようにしたことを特徴とする濾過装置
の濾過部材洗浄方法である。<Means for Solving the Problems> The present invention includes an inlet for supplying a processing liquid, a drain port for discharging the processing liquid, and an air inlet valve for introducing pressurized air acting on the liquid surface. A structure in which one or more liquid storage chambers are provided in the vertical direction in the tank, a filtration member is disposed at the bottom opening of the liquid storage chamber, and the inside of the liquid storage chamber is communicated with an outlet for cleaning liquid. 1. A method of cleaning a filter member of a filter apparatus according to the present invention, wherein the filter member is cleaned in a next step.
第一工程
流入口と、流出口を遮断し、エアー通入弁を開
放して、前記タンク内の処理液をドレイン口から
抜く。First step: The inlet and outlet are shut off, the air inlet valve is opened, and the processing liquid in the tank is drained from the drain port.
第二工程
各液溜室に加圧空気を連通し、液溜室内の洗浄
液を濾過部材から下方へ流下する。Second step: Pressurized air is communicated to each liquid reservoir to cause the cleaning liquid in the liquid reservoir to flow downward from the filtration member.
<作用>
第一工程で流入口と、流出口を遮断し、エアー
通入弁からの圧力空気を液面に作用させてドレイ
ン口から前記タンク内の処理液を抜くと、空とな
つたタンク内の空気圧が、前記濾過部材の下面に
作用し、前記液溜室内の清浄液は流下することな
く、該液溜室内に閉じ込められる。<Function> In the first step, the inlet and outlet are shut off, and the process liquid in the tank is drained from the drain port by applying pressure air from the air inlet valve to the liquid surface. The air pressure inside acts on the lower surface of the filter member, and the cleaning liquid in the liquid reservoir is confined within the liquid reservoir without flowing down.
次の第二工程で、前記液溜室内に加圧空気が連
通すると、その圧力により急激に液溜室内の清浄
液が濾過部材から下方へ落下する。この清浄液の
逆流により濾過部材に詰まつた濾塵が除去されて
洗浄される。 In the next second step, when pressurized air is communicated into the liquid reservoir, the pressure causes the cleaning liquid in the liquid reservoir to rapidly fall downward from the filter member. The filter dust clogged in the filter member is removed and washed by the backflow of this cleaning liquid.
<実施例>
本発明の一実施例を添付図面について説明す
る。<Example> An example of the present invention will be described with reference to the accompanying drawings.
第1図において、1は上下に長いタンクであつ
て、管状本体2の上下に上面板3及び下面板4を
当て、該上面板3,下面板4に複数の連結杆1a
を差渡して固結することにより組付けられる。前
記下面板4の下面には截頭円錐形の液受筐5が配
設され、下面板4に形成された多数の通入孔6に
より前記タンク1内と連通している。前記液受筐
5の下部には、開閉弁8により開閉制御される流
入管9と連通する流入口7と、開閉弁11により
開閉制御されるドレイン口10とが設けられてい
る。 In FIG. 1, reference numeral 1 denotes a vertically long tank, in which an upper plate 3 and a lower plate 4 are placed on the upper and lower sides of a tubular body 2, and a plurality of connecting rods 1a are connected to the upper plate 3 and the lower plate 4.
It is assembled by passing and solidifying the parts. A truncated conical liquid receiving case 5 is disposed on the lower surface of the lower plate 4 and communicates with the inside of the tank 1 through a large number of through holes 6 formed in the lower plate 4 . An inlet 7 communicating with an inflow pipe 9 whose opening and closing are controlled by an on-off valve 8 and a drain port 10 whose opening and closing are controlled by an on-off valve 11 are provided at the lower part of the liquid receiving casing 5 .
また前記下面板4と、液受筐5の中央には、後
記する液溜室17と連通して清浄液を流下させる
管12が挿通している。 In addition, a pipe 12 is inserted through the center of the lower plate 4 and the liquid receiving case 5 to communicate with a liquid storage chamber 17, which will be described later, and allow the cleaning liquid to flow down.
また前記上面板3には、エアー通入弁13が設
けられている。前記エアー通入弁13の内部には
浮子14が設けられており、前記タンク1内に液
が充填している場合には、前記浮子14が、エア
ー通入弁13の流入口に圧接してこれを遮断し、
タンク1内の液が少し下降すると、前記浮子14
による遮閉作用が解除されて、前記流入口を大気
と連通し、前記タンク1内の液面に大気圧が圧力
空気として作用する。 Further, the upper surface plate 3 is provided with an air inlet valve 13. A float 14 is provided inside the air inlet valve 13, and when the tank 1 is filled with liquid, the float 14 comes into pressure contact with the inlet of the air inlet valve 13. block this,
When the liquid in the tank 1 descends a little, the float 14
The blocking effect is released, the inlet is communicated with the atmosphere, and atmospheric pressure acts on the liquid level in the tank 1 as pressurized air.
さらにまた、前記下面板4の中央部上には、上
方へ拡開する皿状の邪魔板15が乗載し、前記下
面板4に形成された、通入孔6上を覆つて、後記
するように、通入孔6から流入する処理液をタン
ク1の周方向へ案内するようにしている。前記邪
魔板15の中央部には短管16が設けられ、前記
下面板4への乗載状態で、前記管12と上下に一
致している。 Furthermore, a dish-shaped baffle plate 15 that expands upward is mounted on the center portion of the lower plate 4, and covers the through hole 6 formed in the lower plate 4, as will be described later. As such, the processing liquid flowing in from the through hole 6 is guided in the circumferential direction of the tank 1. A short tube 16 is provided at the center of the baffle plate 15, and vertically matches the tube 12 when mounted on the bottom plate 4.
前記管状本体2には、その中央で連結される陳
傘状の液溜室17が多数上下方向に配設されてい
る。 The tubular main body 2 has a large number of umbrella-shaped liquid storage chambers 17 arranged in the vertical direction and connected at the center thereof.
前記液溜室17の構成につき、第2図でさらに
詳しく説明する。 The structure of the liquid reservoir chamber 17 will be explained in more detail with reference to FIG.
前記液溜室17は、陳傘状枠体18の中央部に
接続管19a,19b,19cを配設し、該接続
管19a,19b,19cに外嵌した上部座板2
0aを前記枠体18の上部開口に溶接し、さらに
前記枠体18の下面開口を濾過部材21を遮蔽し
て構成される。ここで前記濾過部材21は、濾網
22と濾布23とからなり、前記接続管19a,
19b,19cに外嵌して該接続管に嵌着固定さ
れた下部座板20bに当て、その周縁を前記枠体
18の周縁と座環24で挾持して螺子固定するこ
とにより保持される。また前記液溜室17内は、
接続管19a,19b,19cに形成した連通孔
25により該接続管内と連通している。 The liquid reservoir chamber 17 has connecting pipes 19a, 19b, and 19c arranged in the center of the umbrella-shaped frame 18, and an upper seat plate 2 that is fitted onto the connecting pipes 19a, 19b, and 19c.
0a is welded to the upper opening of the frame 18, and the lower opening of the frame 18 is configured to shield the filter member 21. Here, the filter member 21 includes a filter net 22 and a filter cloth 23, and the connecting pipe 19a,
19b, 19c and is applied to the lower seat plate 20b which is fitted and fixed to the connecting pipe, and its periphery is held between the periphery of the frame 18 and the seat ring 24 and fixed with screws. Moreover, inside the liquid storage chamber 17,
Communication holes 25 formed in the connecting tubes 19a, 19b, and 19c communicate with the inside of the connecting tubes.
前記液溜室17は、形状の異なる接続管19
a,19b,19cを用いた三種類のものからな
る。すなわち第1,2図のように、細管状であつ
て、上下端が液溜室17の上下に少し突出してい
る接続管19aを有するものと、前記接続管19
aが挿入可能な大径状をしており、液溜室17の
上下への突出がない接続管19bを有するもの
と、また同じく大径状であり上端が液溜室17か
ら少し突出して、その管端が閉鎖されている接続
管19cを有するものとがある。 The liquid reservoir chamber 17 has a connecting pipe 19 having a different shape.
It consists of three types using a, 19b, and 19c. That is, as shown in FIGS. 1 and 2, there are two types of connecting tubes 19a, which are thin tube-shaped and whose upper and lower ends slightly protrude above and below the liquid reservoir chamber 17;
A has a large diameter shape that can be inserted, and has a connecting pipe 19b that does not protrude above and below the liquid reservoir chamber 17; Some have a connecting pipe 19c whose end is closed.
各液溜室17は、接続管19aを有する液溜室
17を邪魔板15の短管16に内嵌し、その上に
接続管19bを有する液溜室17を接続管19a
の上端に嵌入して乗載し、さらに接続管19aの
あるものと接続管19bのあるものとを交互に多
数段積重ね、その最上位置で接続管19cのある
液溜室17を乗載してから、前記上面板3の中央
部に螺装したハンドル螺子26を回転して、その
下端で前記接続管19cの上端を圧着することに
より、タンク1の中心部上下方向に強固に保持さ
れて積層される。 Each liquid reservoir chamber 17 is constructed by fitting the liquid reservoir chamber 17 having a connecting pipe 19a into the short pipe 16 of the baffle plate 15, and attaching the liquid reservoir chamber 17 having a connecting pipe 19b thereon to the connecting pipe 19a.
The liquid reservoir chamber 17 with the connecting pipe 19c is placed on top of the stack by inserting it into the upper end, and then stacking the connecting pipe 19a and the connecting pipe 19b in multiple stages alternately. Then, by rotating the handle screw 26 screwed into the center of the top plate 3 and crimping the upper end of the connecting pipe 19c with its lower end, the center of the tank 1 is firmly held in the vertical direction and stacked. be done.
かかる液溜室17群の積層により、前記接続管
19a〜19c,短管16及び管12によりタン
ク1の中心の上下方向に垂直管路27が配設され
る。また前記垂直管路27下端(管12下端)の
流出口27aには管路28が接続される。該管路
28には清浄液の流下を制御する開閉弁29と、
加圧空気を発生させるエアー源30への切換えを
制御する切換弁31が設けられている。 By stacking the group of liquid reservoir chambers 17, a vertical pipe line 27 is provided in the vertical direction of the center of the tank 1 by the connecting pipes 19a to 19c, the short pipe 16, and the pipe 12. Further, a pipe line 28 is connected to the outlet 27a at the lower end of the vertical pipe line 27 (the lower end of the pipe 12). The pipe line 28 includes an on-off valve 29 for controlling the flow of the cleaning liquid;
A switching valve 31 is provided to control switching to an air source 30 that generates pressurized air.
次に前記実施例の作用を説明する。 Next, the operation of the above embodiment will be explained.
開閉弁8及び開閉弁29を開放して流入口7か
ら処理液を流入すると、通入孔6からタンク1内
へ該洗浄液が流入する。かかる処理液は各液溜室
17内へ、濾過部材21を透過して流入して濾過
作用を受け、清浄液となる。このとき、前記通入
孔6は、邪魔板15により周方向へ、その流れを
案内されているから、該通入孔6に近い下部の液
溜室17に集中的に流入することなく、各液溜室
17に略均等に液が流入する。前記液溜室17の
濾過部材21により濾過された清浄液は、その接
続管19a,19b,19cの連通孔25から垂
直管路27に入り、該垂直管路27を流下して、
流出口27aから管路28を経て、所要部に流出
する。 When the on-off valve 8 and the on-off valve 29 are opened and the processing liquid flows in from the inlet 7, the cleaning liquid flows into the tank 1 through the inlet hole 6. The processing liquid flows into each liquid storage chamber 17 through the filtering member 21, undergoes a filtering action, and becomes a cleaning liquid. At this time, since the flow through the through hole 6 is guided in the circumferential direction by the baffle plate 15, each liquid does not flow intensively into the lower liquid storage chamber 17 near the through hole 6. The liquid flows into the liquid reservoir chamber 17 approximately evenly. The cleaning liquid filtered by the filter member 21 of the liquid storage chamber 17 enters the vertical pipe 27 through the communication holes 25 of the connecting pipes 19a, 19b, 19c, flows down the vertical pipe 27,
The water flows out from the outlet 27a through the pipe line 28 to the required part.
かかる濾過作業を連続すると、前記濾過部材2
1に目詰まりを生じ、前記タンク1内の水圧が上
昇する。かかる圧力上昇を公知の圧力検出手段に
より検知し、次の逆洗工程に入る。 When such filtration work is continued, the filtration member 2
1 becomes clogged, and the water pressure inside the tank 1 increases. This pressure increase is detected by a known pressure detection means, and the next backwashing step begins.
すなわち、まず開閉弁8及び開閉弁29を閉じ
て、処理液の流入を遮断してから、ドレイン口1
0の開閉弁11を開放する。前記開閉弁11を開
放しても、タンク1内の処理液は、タンク1内が
外気と遮断されているからドレイン口10からの
流出は、その当初において緩徐に生じる。ところ
が、前記エアー通入弁13の浮子14は、タンク
1の液位降下により、その遮閉作用を解除され、
その液面は外気と連通し、大気圧の作用を受け
る。而て、この後、処理液は急速にドレイン口1
0から排出される。かかるタンク1内の液が流下
した後において、各液溜室17内の清浄液は、開
閉弁29の閉鎖により閉じこめられ、かつ濾過部
材21下面に大気圧の作用を受け、濾過部材21
から下方へ流下することはない。 That is, first, the on-off valve 8 and the on-off valve 29 are closed to block the inflow of the processing liquid, and then the drain port 1 is closed.
Open the on-off valve 11 of 0. Even if the on-off valve 11 is opened, the processing liquid in the tank 1 will initially flow out slowly from the drain port 10 because the tank 1 is isolated from the outside air. However, the float 14 of the air inlet valve 13 is released from its blocking action due to the drop in the liquid level of the tank 1.
The liquid surface communicates with the outside air and is affected by atmospheric pressure. After that, the processing liquid rapidly flows to the drain port 1.
Ejected from 0. After the liquid in the tank 1 has flowed down, the cleaning liquid in each liquid storage chamber 17 is confined by closing the on-off valve 29, and is subjected to atmospheric pressure on the lower surface of the filtration member 21.
It does not flow downwards.
前記実施例において、前記エアー通入弁13を
設けず、かつドレイン口10を垂直路とすると、
タンク1内の液流下に際して、次の洗浄作用を生
ずる。 In the embodiment, if the air inlet valve 13 is not provided and the drain port 10 is a vertical passage,
When the liquid flows down in the tank 1, the following cleaning action occurs.
すなわち前記ドレイン口10の開放とともに、
該ドレイン口10から気泡が流入し、タンク1の
内圧が上昇する。このため、この圧力上昇分に対
応して該ドレイン口10からの液噴出が生じる。
かかる気泡の流入と、液流下とは交互に反覆して
生じ、これに伴いタンク内に激しい乱流を生じ
る。そこで、かかる乱流によりタンク1内が液位
降下とともに洗浄され、かつ前記濾過部材21の
外表面の洗浄もなされる。 That is, with the opening of the drain port 10,
Air bubbles flow in from the drain port 10, and the internal pressure of the tank 1 increases. Therefore, liquid is ejected from the drain port 10 in response to this pressure increase.
The inflow of air bubbles and the flow of liquid occur alternately, resulting in severe turbulence within the tank. Therefore, due to the turbulent flow, the inside of the tank 1 is cleaned as the liquid level drops, and the outer surface of the filter member 21 is also cleaned.
次に、前記切換弁31を切換え、エアー源30
から1Kg/cm2程度の加圧空気を作用させると、第
3図のように前記各液溜室17内及び垂直管路2
7内に残存した清浄液が、前記濾過部材21から
急速に落下する。 Next, the switching valve 31 is switched, and the air source 30
When pressurized air of about 1 kg/cm 2 is applied to
The cleaning liquid remaining in the filter member 7 rapidly falls from the filter member 21.
尚、数度の実験により、切換弁31の切換え当
初においては、表面張力の作用によつて、前記濾
過部材21の下面で液の膨隆が生じ、該表面張力
と空気加圧との均衝が破れると濾過部材21を透
過して清浄液が急速に流下する現象を示すことを
確認した。 In addition, several experiments have shown that at the beginning of switching the switching valve 31, the liquid swells on the lower surface of the filter member 21 due to the action of surface tension, and the balance between the surface tension and the air pressure is It has been confirmed that when the filter member ruptures, the cleaning liquid passes through the filter member 21 and rapidly flows down.
前記した液溜室17内からの清浄液の流下によ
り濾過部材21に詰まつた濾過物が流出し、濾過
部材21の洗浄がなされる。 As the cleaning liquid flows down from the liquid storage chamber 17 described above, the filtrate clogged in the filter member 21 flows out, and the filter member 21 is cleaned.
前記した清浄液の流出後、切換弁31を切換
え、かつ開閉弁29及び開閉弁8を開放すると、
タンク1内に処理液が流入して、濾過作業が再開
される。 After the above-mentioned cleaning liquid flows out, when the switching valve 31 is switched and the on-off valve 29 and the on-off valve 8 are opened,
The processing liquid flows into the tank 1 and the filtration work is restarted.
前記した開閉弁8,開閉弁11,切換弁31及
び開閉弁29は、夫々電磁弁により構成すること
ができ、各弁の開閉制御を前記タンク1内に設け
た圧力検出手段と関係させることにより、前記各
工程を全自動的に施すことできる。 The above-mentioned on-off valve 8, on-off valve 11, switching valve 31, and on-off valve 29 can each be constituted by a solenoid valve, and by relating the opening and closing control of each valve to the pressure detection means provided in the tank 1, , each of the above steps can be performed fully automatically.
前記実施例において、液溜室17の形状を陳傘
状としたが、円盤状等種々の形状とすることが可
能である。尚、円盤状とした場合には、前記液溜
室部体17間にスペーサを介装し、濾過部材21
下部に空間を生じさせる必要がある。 In the embodiment described above, the shape of the liquid reservoir chamber 17 was made into an umbrella shape, but it can be made into various shapes such as a disk shape. In addition, when it is made into a disk shape, a spacer is interposed between the liquid storage chamber body 17, and the filter member 21
It is necessary to create space at the bottom.
前記実施例において、各液溜室17内に、活性
炭、ガラス繊維、イオン交換樹脂等種々の材料を
選択的に充填することにより、濾過作用を、その
処理液の特性に適合する最適なものとすることが
可能となる。 In the embodiment described above, by selectively filling each liquid reservoir chamber 17 with various materials such as activated carbon, glass fiber, and ion exchange resin, the filtration effect can be optimized to suit the characteristics of the processing liquid. It becomes possible to do so.
前記実施例において、タンク1の液排出をドレ
イン口10により施したが、切換え弁を流入管9
に介装することにより前記流入管9で併用するこ
ともできる。また、エアー通入弁13により前記
タンク1内への液面に圧力空気として大気圧を作
用させるようにしたが、浮子を備えないエアー通
入弁にポンプを連通して、液面に大気圧以上の圧
力空気を作用させるようにしても良い。さらにま
た、液溜室17への加圧を管路28に連通するエ
アー源30によるエアー供給により施したが、そ
の加圧用管路を別異に設ける等種々の構成が提案
され得る。 In the embodiment described above, the liquid in the tank 1 was drained through the drain port 10, but the switching valve was connected to the inlet pipe 9.
It can also be used in conjunction with the inflow pipe 9 by interposing it in the inflow pipe 9. In addition, although atmospheric pressure is applied as pressurized air to the liquid level in the tank 1 through the air inlet valve 13, a pump is connected to the air inlet valve which does not have a float to apply atmospheric pressure to the liquid level. It is also possible to apply a higher pressure of air. Furthermore, although the liquid reservoir chamber 17 is pressurized by supplying air from the air source 30 communicating with the pipe line 28, various configurations may be proposed, such as providing a separate pressure pipe line.
また前記実施例は、複数の液溜室17を積層し
た、一本の濾過塔により構成したが、タンク1の
径を大きくして、該タンク1内に、数本の前記濾
過塔を設けるようにしてもよい。さらに、前記逆
洗作用を生じさせるには、液溜室17は必ずしも
複数必要はなく、単一の液溜室17により濾過装
置を構成することも可能である。 Further, in the above embodiment, a single filtration tower is constructed in which a plurality of liquid storage chambers 17 are stacked. You may also do so. Furthermore, in order to produce the above-mentioned backwashing effect, it is not necessarily necessary to have a plurality of liquid storage chambers 17, and it is also possible to configure the filtration device with a single liquid storage chamber 17.
さらにまた前記実施例では、流出口27aをタ
ンク1の下部に設けたが、該流出口27aをタン
ク1の上部に設け清浄液の取出しをタンク上方か
ら施すようにしてもよい。かかる場合にあつて、
各液溜室17に連通する加圧空気を大気圧とし、
前記エアー源30を排して、切換弁31により大
気を導入するようにしてもよい。かかる大気圧の
連通により、室内の液は自重により前記濾過部材
21から流下することとなる。 Furthermore, in the embodiment described above, the outlet 27a is provided at the lower part of the tank 1, but the outlet 27a may be provided at the upper part of the tank 1 so that the cleaning liquid can be taken out from above the tank. In such a case,
The pressurized air communicating with each liquid storage chamber 17 is set to atmospheric pressure,
The air source 30 may be exhausted and atmospheric air may be introduced through the switching valve 31. Due to this communication of atmospheric pressure, the liquid in the room flows down from the filter member 21 due to its own weight.
<発明の効果>
本発明は、上述したように、濾過部材21を下
面に設けた液溜室17を1〜複数個設け、前記濾
過部材21の洗浄を前記液溜室17内の清浄液を
流下させることにより施したものであるから、
1) 清浄液の逆流量、逆流時間等を制御する必
要がない。またその逆洗に際してタンクを開放
する等の作業が不要である。このため濾過制御
の自動化に最適となる。<Effects of the Invention> As described above, the present invention provides one or more liquid reservoir chambers 17 each having a filter member 21 on the bottom surface thereof, and cleans the filter member 21 by using a cleaning liquid in the liquid reservoir chamber 17. Since the cleaning solution is applied by flowing down, 1) There is no need to control the backflow amount, backflow time, etc. of the cleaning solution. Furthermore, there is no need to open the tank for backwashing. This makes it ideal for automating filtration control.
2) 洗浄時間が短かく、かつ使用する清浄液の
単位重量当りの洗浄効果が高い。2) The cleaning time is short and the cleaning effect per unit weight of the cleaning liquid used is high.
3) 清浄液の使用量が少なくて済む。3) The amount of cleaning fluid used can be reduced.
4) エアー源30は、その加圧空気により直接
洗浄させるものではないから小さな容量で済
む。または、前記加圧空気を大気圧とすれば、
エアー源30を不要とすることもできる。従つ
て、装置が低廉となる。4) The air source 30 does not need to be used for direct cleaning with its pressurized air, so only a small capacity is required. Or, if the pressurized air is at atmospheric pressure,
The air source 30 can also be made unnecessary. Therefore, the device is inexpensive.
等の優れた効果がある。It has excellent effects such as
添付図面は本発明の実施例を示し第1図は縦断
側面図、第2図は液溜室17の拡大縦断側面図、
第3図は逆洗作用を示す一部の縦断側面図であ
る。
1;タンク、6;通入孔、7;流入口、8;開
閉弁、10;ドレイン口、9;流入管、11;開
閉弁、12;管、13;エアー通入弁、14;浮
子、15;邪魔板、17;液溜室、18;枠体、
19a,19b,19c;接続管、21;濾過部
材、25;連通孔、27;垂直管路、27a;流
出口、28;管路、29;開閉弁、30;エアー
源。
The attached drawings show an embodiment of the present invention, and FIG. 1 is a longitudinal side view, and FIG. 2 is an enlarged longitudinal side view of the liquid storage chamber 17.
FIG. 3 is a partial longitudinal sectional side view showing the backwashing action. 1; tank, 6; through hole, 7; inlet, 8; on-off valve, 10; drain port, 9; inflow pipe, 11; on-off valve, 12; pipe, 13; air inlet valve, 14; float, 15; baffle plate, 17; liquid storage chamber, 18; frame,
19a, 19b, 19c; connecting pipe, 21; filtration member, 25; communication hole, 27; vertical pipe line, 27a; outlet, 28; pipe line, 29; on-off valve, 30; air source.
Claims (1)
るドレイン口と、液面に作用する圧力空気を導入
するエアー通入弁とを備えたタンク内に、上下方
向に1〜複数個の液溜室を設け、前記液溜室の下
面開口に濾過部材を配設し、さらに前記液溜室内
を清浄液の流出口に連通してなる構成の濾過装置
であつて、前記濾過部材の洗浄を次の工程で施す
ようにしたことを特徴とする濾過装置の濾過部材
洗浄方法。 第一工程 流入口と、流出口を遮断し、エアー通入弁を開
放して、前記タンク内の処理液をドレイン口から
抜く。 第二工程 各液溜室に加圧空気を連通し、液溜室内の洗浄
液を濾過部材から下方へ流下する。[Claims] 1. In a tank equipped with an inlet for supplying the processing liquid, a drain port for discharging the processing liquid, and an air inlet valve for introducing pressurized air acting on the liquid surface, A filtration device having one to a plurality of liquid reservoir chambers, a filtration member disposed at a lower opening of the liquid reservoir chamber, and further communicating the inside of the liquid reservoir chamber with an outlet of a cleaning liquid, A method for cleaning a filtration member of a filtration device, characterized in that the filtration member is cleaned in a next step. First step: The inlet and outlet are shut off, the air inlet valve is opened, and the processing liquid in the tank is drained from the drain port. Second step: Pressurized air is communicated to each liquid reservoir, and the cleaning liquid in the liquid reservoir flows downward from the filter member.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60046974A JPS61209019A (en) | 1985-03-09 | 1985-03-09 | Method for washing filter member of filter apparatus |
| US06/833,858 US4702833A (en) | 1985-03-09 | 1986-02-26 | Filter apparatus |
| EP86103178A EP0194632A3 (en) | 1985-03-09 | 1986-03-10 | Filter apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60046974A JPS61209019A (en) | 1985-03-09 | 1985-03-09 | Method for washing filter member of filter apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61209019A JPS61209019A (en) | 1986-09-17 |
| JPH0256121B2 true JPH0256121B2 (en) | 1990-11-29 |
Family
ID=12762215
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60046974A Granted JPS61209019A (en) | 1985-03-09 | 1985-03-09 | Method for washing filter member of filter apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61209019A (en) |
-
1985
- 1985-03-09 JP JP60046974A patent/JPS61209019A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61209019A (en) | 1986-09-17 |
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