JPS58143810A - Apparatus for washing filter chamber in waste water purification apparatus - Google Patents

Apparatus for washing filter chamber in waste water purification apparatus

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Publication number
JPS58143810A
JPS58143810A JP57023897A JP2389782A JPS58143810A JP S58143810 A JPS58143810 A JP S58143810A JP 57023897 A JP57023897 A JP 57023897A JP 2389782 A JP2389782 A JP 2389782A JP S58143810 A JPS58143810 A JP S58143810A
Authority
JP
Japan
Prior art keywords
water
pipe
chamber
waste water
filter
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
JP57023897A
Other languages
Japanese (ja)
Inventor
Shigeo Takeuchi
竹内 茂夫
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.)
Takeuchi Tekko KK
Original Assignee
Takeuchi Tekko 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 Takeuchi Tekko KK filed Critical Takeuchi Tekko KK
Priority to JP57023897A priority Critical patent/JPS58143810A/en
Publication of JPS58143810A publication Critical patent/JPS58143810A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To provide the titled efficient apparatus simple in constitution, constituted by mechanism wherein purified water obtained by filtering purified waste water is introduced into the lower part of a filter chamber from a washing water supply pipe through a three-way opening and closing valve and raised along with jet air to wash a filter material. CONSTITUTION:In a waste water purification apparatus wherein waste water introduced from a waste water storage chamber 6 by a raw water pump 11 is supplied to an electrolytic purification chamber 15 to separate and remove impurities (a) therein by electrolysis while the obtained partially treated water is introduced into a filter chamger 16 through a separation chamber 28, a waste water pipe 36 and a flooding tank 34 to finally remove fine mixed substances by a filter material and the obtained purified water is flowed into a purified water tank T from a water introducing pipe 44, in washing the above mentioned filter mateial 39, a purified water pump 2 is operated while the opening and closing valve 51 of a washing water supply pipe 3 is closed to supply the purified water to the lower part of the filter chamber 16 through a branched pipe 45, a three-way opening and closing valve 46 and a water introducing pipe 44 and air supplied from a pressure air source 4 is further introduced from a jet pipe 40 to wash the filter material 39 in a floated state while washing waste water is discharged to a waste water sump 7 through a discharge pipe 49.

Description

【発明の詳細な説明】 本発明は廃水を浄化して再利用できるようにした、廃水
浄化装置における濾過室の洗滌装置に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a cleaning device for a filtration chamber in a wastewater purification device that purifies and reuses wastewater.

従来節水の目的で、洗滌後の廃水を浄化して再利用する
廃水浄化装置が知られている。この、J: 5な装置は
一般に廃水中に混入する洗剤、塵埃、油成分などの不純
物を、不純物分離装置により分離除去した後、さらにそ
の廃水中に残存する微細物を濾過装置によって分離除去
するようになっている。ところで前記濾過装置はその内
部に収容されそのためその濾利を定期的に清掃する必要
があるが、従来ではか\る濾拐の能率のよい清掃手段が
存在しなかった。
Conventionally, wastewater purification devices are known that purify and reuse wastewater after washing for the purpose of saving water. This J: 5 equipment generally separates and removes impurities such as detergents, dust, and oil components mixed into wastewater using an impurity separator, and then separates and removes fine particles remaining in the wastewater using a filtration device. It looks like this. By the way, the filtration device is housed inside the filtration device, and therefore, it is necessary to periodically clean the filtration tray, but conventionally, there has been no efficient cleaning means for such filtration.

本発明は上記実情にかんがみてなされたもので廃水浄化
装置の一部の機器を利用してきわめて能率よく自動的に
前記濾材の洗滌を行うようにした構成簡単な廃水浄化装
置における濾過室洗滌装置を提供することを主な目的と
するものである。
The present invention has been made in view of the above-mentioned circumstances, and is a filtration chamber cleaning device in a wastewater purification device with a simple configuration, which uses a part of the equipment of the wastewater purification device to automatically and efficiently wash the filter medium. The main purpose is to provide

以下、図面により本発明の1実施例について説明する。Hereinafter, one embodiment of the present invention will be described with reference to the drawings.

第1図において据付面上に廃水浄化装置Cが設置され、
該装置Cの一側(第1図左側)の据付面下には、未浄化
の廃水および分離後の不純物を収容するためのピッ)P
が設けられ、また前記浄化槽Cの他側には浄化後の清浄
水を収容するための清浄水槽1゛が設置される。清浄水
槽T内には、新水の注水口1が開口され、この注水1]
1より清浄水槽T内に新水を補給できるようになってい
る。
In Fig. 1, wastewater purification device C is installed on the installation surface,
Under the installation surface on one side of the device C (left side in Figure 1) is a pit (P) for storing unpurified wastewater and impurities after separation.
A clean water tank 1' is installed on the other side of the septic tank C to store clean water after purification. A fresh water inlet 1 is opened in the clean water tank T, and this water inlet 1]
1, fresh water can be replenished into the clean water tank T.

また清浄水槽T内には、洗浄水ポンプ2が収容され、該
ポンプ2の吐11月」に洗滌水供給管3が接続される。
A cleaning water pump 2 is housed in the clean water tank T, and a cleaning water supply pipe 3 is connected to the discharge port of the pump 2.

前記ピッ’pp内は隔壁5によって廃水貯留室6と廃水
溜Iとに区画され、さらに廃水貯留室6内は一次フィル
タ8によって第1室61と第2室62とに区画され、第
1室6□内には二次フィルタ9が設けられ、該フィルタ
9に原水ポンプ11の吸込口に連なる吸込管10が接続
され、ビットI”内の廃水は一次、二次フィルタ8,9
によって一次。
The interior of the pi'pp is divided by a partition wall 5 into a wastewater storage chamber 6 and a wastewater reservoir I, and the inside of the wastewater storage chamber 6 is further divided by a primary filter 8 into a first chamber 61 and a second chamber 62. A secondary filter 9 is provided inside the bit 6□, and a suction pipe 10 connected to the suction port of the raw water pump 11 is connected to the filter 9.
By primary.

二次的に濾過された後、原水ポンプ11によって吸上げ
られろ。
After being secondarily filtered, it is sucked up by the raw water pump 11.

次に本発明廃水浄化装置Cの内部構造について主に第2
〜4図を参照して説明する。
Next, we will mainly discuss the internal structure of the wastewater purification device C of the present invention.
This will be explained with reference to Figures 4 to 4.

浄化槽13内は縦方向の隔壁14によって電解浄化室1
5と濾過室16とに区画されろ。電解浄化室15内の上
部には、塩化ビニール樹脂等の絶縁材よりなる上、下面
開放の電解槽18が設けられ、この電解槽18内には、
多数枚の陽電極板191.19.・・と陰電極板19□
 、19□・・と 5− を適当な間隔を存して交互に並設して構成した電解電極
抜群19が収容される。陽電極板191としてはアルミ
ニウム板が用いられ、また陰電極板192としてはアル
ミニウム板もしくはステンレス板が用いられる。電解槽
18の上面は開口さ才ζまたその下面には電解槽18内
に通じる未浄化廃水の噴入室20が形成され、この噴入
室20の底壁には先細りの重量物落下口21が開口され
る。
The interior of the septic tank 13 is divided into an electrolytic purification chamber 1 by a vertical partition wall 14.
5 and a filtration chamber 16. In the upper part of the electrolytic purification chamber 15, an electrolytic cell 18 made of an insulating material such as vinyl chloride resin and open at the bottom is provided, and inside this electrolytic cell 18,
Multiple positive electrode plates 191.19. ...and cathode plate 19□
, 19□, . . . and 5- are arranged side by side alternately at appropriate intervals to accommodate the electrolytic electrodes 19. An aluminum plate is used as the positive electrode plate 191, and an aluminum plate or a stainless steel plate is used as the negative electrode plate 192. The upper surface of the electrolytic cell 18 has an opening ζ, and the lower surface thereof is formed with an injection chamber 20 for unpurified wastewater that communicates with the inside of the electrolytic cell 18, and the bottom wall of this injection chamber 20 is opened with a tapered heavy object drop port 21. be done.

前記噴入室20内には、電解槽18の縦中心線L−Lよ
りも一側(第3図右側)に偏らせて廃水噴射装置Sが設
けられる。この装置Sは略水平に配置されろ噴出管22
を有し、該噴出管22には前記電解槽18内に向けて多
数の噴出口23が開口されている。前記噴出管22の中
間部には送水管24の上端が接続され、この送水管24
の下端には、電解槽1B下に据付けられろチェック弁伺
の前記原水ポンプ11の吐出口が接続されている。
In the injection chamber 20, a waste water injection device S is provided so as to be biased to one side (the right side in FIG. 3) with respect to the vertical center line LL of the electrolytic cell 18. This device S is arranged approximately horizontally.
The ejection pipe 22 has a large number of ejection ports 23 opened toward the inside of the electrolytic cell 18 . The upper end of a water pipe 24 is connected to the middle part of the jet pipe 22.
The discharge port of the raw water pump 11 installed below the electrolytic cell 1B is connected to the check valve.

−〇 − 原水ポンプ11には水抜き用の開閉弁26が°付設され
る。原水ポンプ11の吸込口には前記吸込管10が接続
され、この吸込管10の他端は前記ピットT内の第2室
62内に開口されろ。前記送水管24の途中にはエゼク
タ25が介在されており、このエゼクタ25に大気に開
口するエア導入管27が接続されている。したがって原
水ポンプ11を駆動すると、第2室62内の廃水が吸上
げられて送水管24に圧送されるが、その際前記エゼク
タ250作用により送水管24内には大気がエア導入管
27を通って吸い込まれて廃水内に混入し、噴出管22
の噴水[123より廃水とともに気泡となって噴出する
-〇- The raw water pump 11 is provided with an on-off valve 26 for draining water. The suction pipe 10 is connected to the suction port of the raw water pump 11, and the other end of the suction pipe 10 is opened into the second chamber 62 in the pit T. An ejector 25 is interposed in the middle of the water pipe 24, and an air introduction pipe 27 that opens to the atmosphere is connected to the ejector 25. Therefore, when the raw water pump 11 is driven, the waste water in the second chamber 62 is sucked up and sent to the water pipe 24 under pressure. It is sucked in and mixed into the wastewater, and the ejection pipe 22
Bubbles are ejected from the fountain [123] along with waste water.

浄化槽13内において、電解槽18に接して分離室28
が形成され、この分離室′28は電解槽18の一側壁で
形成される仕切壁29によって仕切られている。仕切壁
29の上端には堰30が形成され、この堰30を通して
電解槽18内の凝集不純物αが分離室28内に溢流する
ようになっている。
In the septic tank 13, a separation chamber 28 is in contact with the electrolytic tank 18.
This separation chamber '28 is partitioned by a partition wall 29 formed by one side wall of the electrolytic cell 18. A weir 30 is formed at the upper end of the partition wall 29, and the aggregated impurities α in the electrolytic cell 18 overflow into the separation chamber 28 through this weir 30.

また分離室28内上部には、前記堰3oに相対向して不
純物受容槽31が設けられ、この不純物受容槽31の上
縁は、前記堰30の峰3oaよりも高位にあって堰30
を溢流した廃水中の分離浮遊不純物が、この不純物受容
槽31内に流入貯留されるようになっている。不純物受
容槽31の底壁には排出管32が接続されろ。
Further, an impurity receiving tank 31 is provided in the upper part of the separation chamber 28 so as to face the weir 3o.
Separated floating impurities in the overflowing wastewater flow into this impurity receiving tank 31 and are stored therein. A discharge pipe 32 is connected to the bottom wall of the impurity receiving tank 31.

浄化槽13の底壁13aは漏斗状に形成されてその下端
には他の排出管33に接続され、この排出管33の端部
には開閉弁33′が設けられろ。
The bottom wall 13a of the septic tank 13 is formed into a funnel shape, and its lower end is connected to another discharge pipe 33, and the end of this discharge pipe 33 is provided with an on-off valve 33'.

第2図に明瞭に示すように隔壁14の上部には溢流槽3
4が設けられ、この溢流槽34には、流入口35が開口
され、この流入口35に廃水管36の上端が接続される
。廃水管36は、前記分離室28内を下方にのびており
、その下端は該室28内下部に開口している。
As clearly shown in FIG.
4, an inlet 35 is opened in the overflow tank 34, and the upper end of a waste water pipe 36 is connected to the inlet 35. The waste water pipe 36 extends downward within the separation chamber 28, and its lower end opens into the lower portion of the chamber 28.

第2,4図に示すように前記溢流槽34の」三方におい
て、隔壁14の上縁には、前記堰30の峰30αよりも
高レベル位置において凹状の逆流路37が切欠かれてお
り、この逆流路37の下縁には、電解槽18と濾過室1
6とに跨って整流案内板38が設けられ、この整流案内
板38は電解槽18に向って若干下向きに傾斜され、濾
過室16内上位の水が、前記逆流路37を通って電解槽
18内に逆流できるようになっている。
As shown in FIGS. 2 and 4, on three sides of the overflow tank 34, a concave reverse flow path 37 is cut out in the upper edge of the partition wall 14 at a level higher than the peak 30α of the weir 30, At the lower edge of this reverse flow path 37, an electrolytic cell 18 and a filtration chamber 1 are provided.
A rectifying guide plate 38 is provided astride between the filtration chamber 16 and the electrolytic cell 18. It allows for reflux to flow inside.

前記濾過室16の下部には、粒状の濾材39が収容され
、との濾材39は上層、中間層および下層よりなる三層
をなしており、上層および下層は粗の濾材よりなり、ま
た中間層はそれよりも密の濾材よりなる。濾材39の上
、下中間部には、多数の噴気口を穿設した空気噴出管4
0が挿入されており、この空気噴出管40はアキュムレ
ータ等−〇 − の圧力空気源41に開閉弁42を介して接続され、必要
に応じて濾材39内に圧力空気を噴出することができる
。濾過室16の下部には、流出口43が開口され、この
流出口43には導水管44の一端が接続され、この導水
管44はその他端が前記清浄水槽T内に開口される。導
水管44の途中には、洗浄水ポンプ2に連なる洗滌水供
給管3の途中から分岐される分岐管45が接続され、そ
の三叉接続部に三方開閉弁46が設けられる。分岐管4
5の途中にはチェック弁47が接続され、このチェック
弁47は洗滌水供給管3から導水管44への水の流れを
許容する。導水管44の下部には水抜用の開閉弁48が
付設される。分岐管45の下流側の洗滌水供給管3には
開閉弁51が介装される。濾過室16の濾材39の上方
と前記廃水溜1間は排水管49をもって連通され、この
排水管49の途中にはシリンダ弁50が介在される。ま
10− たそのシリンダ弁50よりも下流の排水管4.9には、
前記不純物受容槽31に連通される排出管32が接続さ
れろ。
A granular filter medium 39 is housed in the lower part of the filtration chamber 16, and the filter medium 39 has three layers consisting of an upper layer, an intermediate layer, and a lower layer.The upper layer and the lower layer are made of coarse filter medium, and the intermediate layer consists of a denser filter medium. At the upper and lower intermediate parts of the filter medium 39, there is an air jet pipe 4 having a large number of blowholes.
0 is inserted, and this air jetting pipe 40 is connected to a pressure air source 41 such as an accumulator through an on-off valve 42, and can jet pressurized air into the filter medium 39 as necessary. An outflow port 43 is opened in the lower part of the filtration chamber 16, one end of a water conduit 44 is connected to this outflow port 43, and the other end of this water conduit 44 is opened into the clean water tank T. A branch pipe 45 branched from the middle of the washing water supply pipe 3 connected to the washing water pump 2 is connected to the middle of the water guide pipe 44, and a three-way opening/closing valve 46 is provided at the three-pronged connection part. Branch pipe 4
A check valve 47 is connected in the middle of the cleaning water supply pipe 5, and this check valve 47 allows water to flow from the washing water supply pipe 3 to the water conduit pipe 44. An on-off valve 48 for draining water is attached to the lower part of the water conduit 44. An on-off valve 51 is interposed in the washing water supply pipe 3 on the downstream side of the branch pipe 45 . A drain pipe 49 communicates between the upper part of the filter medium 39 of the filter chamber 16 and the waste water reservoir 1, and a cylinder valve 50 is interposed in the middle of the drain pipe 49. M10- In the drain pipe 4.9 downstream of the cylinder valve 50,
A discharge pipe 32 communicating with the impurity receiving tank 31 is connected.

尚、図中52は制御盤、53は覗き窓である。In the figure, 52 is a control panel, and 53 is a viewing window.

次に本発明の実施例の作用について説明する。Next, the operation of the embodiment of the present invention will be explained.

■ 原水ポンプ11の駆動により、廃水貯留室6内の、
洗剤および水性ワックスを含んだ洗滌廃水は一次、二次
フィルタ8,9を通過して粗大物、塵埃などが除去され
た後、浄化槽13内に吸上げられる。
■ By driving the raw water pump 11, inside the wastewater storage chamber 6,
The cleaning wastewater containing detergent and aqueous wax passes through primary and secondary filters 8 and 9 to remove coarse substances, dust, and the like, and is then sucked into the septic tank 13.

■ 原水ポンプ11からの加圧廃水は送水管24を通っ
て廃水噴射装置Sの噴出管22に圧送されるが、その際
エゼクタ25によりエア導入管27より大気が送水管2
4内に吸い込まれて圧送廃水内に混入され気泡となって
廃水とともに電解槽18に向けて噴出される。
■ The pressurized wastewater from the raw water pump 11 is forced to pass through the water pipe 24 to the jet pipe 22 of the waste water injection device S, but at this time, the ejector 25 releases atmospheric air from the air introduction pipe 27 into the water pipe 2.
The gas is sucked into the electrolytic cell 18 and mixed into the pumped wastewater, forms bubbles, and is ejected together with the wastewater toward the electrolytic cell 18.

■ 加圧廃水は気泡の上昇とともに陽電極板191と陰
電極板192間の間隙を通って電解槽18内を上昇する
。ところでこの上昇過程において、廃水中に混在する洗
剤等のアニオン界面活性剤は陽電極板19.に、また廃
水中に混在する油成分等のカチオン界面活性剤は陰電極
板19□に引寄せられ、電極板であるアルミニウム電極
板から発生する水酸化アルミニウムにより、前記洗剤お
よび油成分は他の不純物とともに凝集し、その凝集不純
物αは廃水内の気泡の上昇に伴って水面上に浮上する。
(2) The pressurized wastewater passes through the gap between the positive electrode plate 191 and the negative electrode plate 192 and rises inside the electrolytic cell 18 as the bubbles rise. By the way, during this rising process, anionic surfactants such as detergents mixed in the wastewater are removed from the positive electrode plate 19. In addition, cationic surfactants such as oil components mixed in the wastewater are attracted to the negative electrode plate 19□, and the detergent and oil components are attracted to the cathode plate 19□ by aluminum hydroxide generated from the aluminum electrode plate. It coagulates with impurities, and the coagulated impurity α floats to the surface of the water as the bubbles in the wastewater rise.

一方重量不純物は電解槽18下の落下口21を通って浄
化槽13下に沈殿ずろ。
On the other hand, heavy impurities pass through the drop port 21 under the electrolytic tank 18 and settle under the septic tank 13.

■ 電解槽18の水面上に浮上した、洗剤、油成分その
他の凝集不純物aは気泡と混合状態で電解槽1B内の上
層の廃水とともに該槽18内の上昇流によって第1,3
図左方へ押し流され堰30を乗り越えて分離室28内に
流入する。分離室28内では、廃水上に浮遊する凝集不
純物aが不純物受容槽31内に流入するとともに電解槽
18内では浮」二できなかった凝集不純物aも二次的に
分離浮」ニして不純物受容槽31内に流入し、核種31
より排出管32、および排水管49を通ってピッl−P
内の廃水溜7に流れ、そこより図示しない油水分離槽等
を経て廃棄される。
■ Detergents, oil components, and other coagulated impurities (a) that have surfaced on the water surface of the electrolytic cell 18 are mixed with air bubbles and are transported to the first and third layers by the upward flow in the electrolytic cell 18 together with the waste water in the upper layer of the electrolytic cell 1B.
It is pushed to the left in the figure, overcomes the weir 30, and flows into the separation chamber 28. In the separation chamber 28, the flocculated impurities a floating on the waste water flow into the impurity receiving tank 31, and the flocculated impurities a that could not be floated in the electrolytic cell 18 are also secondarily separated and converted into impurities. Flows into the receiving tank 31, and the nuclide 31
The pill-P is then passed through the discharge pipe 32 and the drain pipe 49.
The wastewater flows into the wastewater reservoir 7 inside the tank, and from there it is disposed of via an oil-water separation tank (not shown) or the like.

■ 分離室28内では廃水よりも重い不純物が漸次沈澱
し、この沈澱不純物は開閉弁33′の開弁により外部に
排出される。而して第3図に明瞭に示すように空気の噴
出管22は、電解槽18の縦中心線L−Lを境として分
離室28から離ざかる側(第3図右側)に配設されてい
るので電解槽18内の廃水の流れは分離室28に向う一
方向流となって電解槽18上の不純物を不純物受容槽3
1へ向けて押し13− 出すことができ、不純物の分離作用が能率よく行われる
(2) Impurities heavier than the waste water gradually settle in the separation chamber 28, and the precipitated impurities are discharged to the outside by opening the on-off valve 33'. As clearly shown in FIG. 3, the air jet pipe 22 is arranged on the side away from the separation chamber 28 (the right side in FIG. 3) with the vertical center line LL of the electrolytic cell 18 as the boundary. Therefore, the flow of waste water in the electrolytic cell 18 becomes a unidirectional flow toward the separation chamber 28, and the impurities on the electrolytic cell 18 are transferred to the impurity receiving tank 3.
1, and the impurities can be efficiently separated.

■ 分離室28内で前述のように不純物の分離された廃
水は、漸次下降し、分離室28内下部に開口する廃水管
36を上昇して溢流槽34内に流入し、核種34を溢流
して濾過室16内に流下する。
■ The wastewater from which impurities have been separated as described above in the separation chamber 28 gradually descends, ascends the wastewater pipe 36 that opens at the bottom of the separation chamber 28, flows into the overflow tank 34, and overflows the nuclide 34. It flows down into the filtration chamber 16.

■ 濾過室16内の廃水は濾材39内を下降通過して最
終的に微細な混入物を分離除去された後、導水管44、
および三方開閉弁46を通って清浄水槽T内に流入して
清浄水ポンプ2の駆動により洗滌水供給管3に供給され
、適宜の被洗滌物を洗滌する。           
  ′前述のようにして廃水の浄化が継続されると、濾
過室16内の濾材39に目詰りが生じる。か\る場合に
は次の作用によりその目詰りが自動的に除去される。
■ The wastewater in the filtration chamber 16 passes down through the filter medium 39 and finally, fine contaminants are separated and removed, and then the wastewater is passed through the water conduit pipe 44,
The water then flows into the clean water tank T through the three-way opening/closing valve 46, and is supplied to the cleaning water supply pipe 3 by driving the clean water pump 2 to wash appropriate objects to be washed.
'If wastewater purification is continued as described above, the filter medium 39 in the filtration chamber 16 will become clogged. In such a case, the clogging will be automatically removed by the following action.

14− ■ 開閉弁51を閉じ、三方開閉弁46を切換えた後、
シリンダ弁50を開放し、濾過室16内の濾月39上の
水を排出する。
14- ■ After closing the on-off valve 51 and switching the three-way on-off valve 46,
The cylinder valve 50 is opened and the water on the filter moon 39 in the filter chamber 16 is discharged.

■ 排水が終了したらシリンダ弁50を閉じた後清浄水
ポンプを駆動して清浄水槽T内の水を導水管44を通し
て濾材39内にその下部より圧送すると同時に開閉弁4
2の開弁によりアキュムレータ等の圧力空気源41内の
圧力空気を空気噴出管40を通して濾材39内に噴入す
る。濾材39は洗滌水と空気との加圧上昇流により浮遊
状態となって洗滌される。
■ After draining is finished, close the cylinder valve 50 and drive the clean water pump to pump the water in the clean water tank T through the water conduit 44 and into the filter medium 39 from the bottom, and at the same time close the on-off valve 4.
By opening the valve 2, pressurized air in a pressure air source 41 such as an accumulator is injected into the filter medium 39 through the air jet pipe 40. The filter medium 39 is washed in a floating state by the pressurized upward flow of the washing water and air.

濾過室16が満水になる前に、清浄水ポンプ2の駆動を
停止して水の供給を停止するとともに開閉弁42を閉弁
して圧力空気の供給を停止する。
Before the filtration chamber 16 becomes full of water, the drive of the clean water pump 2 is stopped to stop the supply of water, and the on-off valve 42 is closed to stop the supply of pressurized air.

■ 浮遊状態となった濾材39が沈下するのを待ってシ
リンダ弁50を開放し、濾過室16内の不純物の混入し
た水を排水管49を通して排出する。
(2) After waiting for the floating filter medium 39 to sink, the cylinder valve 50 is opened, and the impurity-containing water in the filtration chamber 16 is discharged through the drain pipe 49.

C) 前記■、および■の操作を数回繰り返して行う。C) Repeat the operations ① and ① several times.

■ 排水が終了したらシリンダ弁5oを閉じ、空気の供
給を止めたまX再び清浄水ポンプ2を運転して濾過室1
6内に洗滌水だけを噴入して、濾材39上の不純物をそ
の上方へ押上げるとともに濾材39中に残留した空気を
その上方へ押し出し濾材39を整える。この際濾過室1
6内に流入した洗滌水は前記逆流路37を通って濾過室
16を溢流し、整流案内板38に案内されて電解槽18
内に流入し該槽18内に排出されずに残留した浮遊不純
物を不純物受容槽31内へ追い込み排出する。
■ When the drainage is finished, close the cylinder valve 5o, stop the air supply, and operate the clean water pump 2 again to fill the filtration chamber 1.
Only washing water is injected into the filter 6 to push up impurities on the filter medium 39 upwards, and push out air remaining in the filter medium 39 upwards to prepare the filter medium 39. At this time, filtration chamber 1
The cleaning water flowing into the filtration chamber 16 passes through the reverse flow path 37, overflows the filtration chamber 16, is guided by the rectification guide plate 38, and flows into the electrolytic cell 18.
Floating impurities that flow into the tank 18 and remain without being discharged are driven into the impurity receiving tank 31 and discharged.

■ 清浄水ポンプ2の運転を停止し、開弁したシリンダ
弁50より濾材39上に残留する水を排水する。
(2) Stop the operation of the clean water pump 2, and drain the water remaining on the filter medium 39 through the opened cylinder valve 50.

■ 次にシリンダ弁50を閉じる。■ Next, close the cylinder valve 50.

■ 最後に開閉弁51を開弁し、三方開閉弁46を元に
切換えて全作業を終了する。
■Finally, open the on-off valve 51 and switch based on the three-way on-off valve 46 to complete the entire work.

而して前記作業のうち■〜■は制御盤52内の電気制御
機器により自動的に行うことができる。
Of the above-mentioned operations, steps (1) to (2) can be automatically performed by the electric control equipment in the control panel 52.

以上のように本発明によれば、被洗滌物に清浄水を圧送
するための清浄水ポンプ2および清浄水槽Tと濾過室1
6とを接続する導水管44を利用して濾過室16内の濾
材39を自動的に洗滌することかできるので、濾材39
の目詰りを防止して常に能率のよい濾過作用を営ませる
ことができ、しかも人手による濾過室16内のメンテナ
ンスが不要になり、さらに濾過室洗滌装置の全体の構成
の簡素化を図ることができる。
As described above, according to the present invention, the clean water pump 2 for pumping clean water to the object to be washed, the clean water tank T, and the filtration chamber 1
Since the filter medium 39 in the filtration chamber 16 can be automatically washed using the water conduit 44 connecting the filter medium 39 with
It is possible to prevent clogging of the filtration chamber 16 and ensure efficient filtration at all times, and there is no need for manual maintenance of the inside of the filtration chamber 16, and furthermore, the overall configuration of the filtration chamber cleaning device can be simplified. can.

また濾過室16内の濾材39内には、圧力空気源41に
連なる空気噴出管40を挿入したので濾17− 材39内には洗滌水とともに圧力空気を噴入して濾材3
9を遊離状態にして洗滌することができ濾材39の洗滌
効果を著しく高めることができるとともにその洗滌を迅
速に行うことができる。
In addition, an air jet pipe 40 connected to a pressure air source 41 is inserted into the filter medium 39 in the filter chamber 16, so that pressurized air is injected into the filter medium 39 together with washing water.
9 can be washed in a free state, the cleaning effect of the filter medium 39 can be significantly enhanced, and the cleaning can be carried out quickly.

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

第1図は本発明装置の全体概略側面図、第2図は廃水浄
化装置の要部縦断正面図、第3図は、該装置の要部縦断
側面図、第4図は第2図IV−TV線断面図である。 T・・・清浄水槽、3・・・洗滌水供給管、15・・・
電解浄化室、16・・・濾過室、39・・・濾材、4o
・・・空気噴出管、41・・・圧力空気源、42・・・
開閉弁、44・・・導水管、45・・・分岐管、46・
・・三方開閉弁、49・・・排水管、51川開閉弁。 
  ゛特許出願人 竹内鉄工株式会社 手続補正書(自発) 昭和57年6月12日 1、事件の表示 昭和57年 特 願第23897号 2、発明の名称 廃水浄化装置における濾過室洗滌装置 3、補正をする者 事件との関係 特許出願人 名称竹内鉄工株式会社 4、代   理   人  〒104 5、補正の対象 別  紙  の  通  り 補正の内容 ■。明細書第4頁第15行、 ・・・「洗浄水ポンプ−1・・・・・・とあるを、・・
・「清a)水ポンプ」・・・・・・と訂正する。 2、明細書第6頁第2行、 ・・・[解電極抜群−1・・・・・・とあろを、・・・
[解電極板好−1・・・・・・と訂正する。 3、明細書第10頁第7行、 ・・・「洗浄水ポンプ」 ・・・とあるな、・・・「清
浄水ポンプ」・・・・・と訂正する。 4、明細書第13頁第12行、 ・・[空気−1・・・・・・とあるを、・・・「加圧廃
水」・・・・・・と訂正する。 5、明細書第13頁第14行、 ・・・「離」・・・・・・とあるな、 ・・・「遠」・・・・・・と訂正する。 6、明細書第15頁第5行、  1− ・・・「清浄水ポンプ]・・・・・・とあるを、・・・
「清浄水ポンプ2」・・・・・・と訂正する。 7、明細書第15頁第8行、 ・・・「アキュムレータ等の」・・・・・とあるを削除
ずろ。 8、明細書第15頁第10行、第16頁第7行、第18
頁第1行、 ・・・「洗浄水」・・・・・・とあろを、・・・「清浄
水」・・・・・・と訂正する。 9、明細書第16頁第11行、 ・・・「に流入した洗滌」・・・・・・とあるを、・・
・[が清浄水で満されると、その清浄]・・・・・と訂
正する。 10、明細書第18頁第2行、 ・・・「遊離状態]・・・・・・とあるを、・・ 「浮
遊状態」・・・・・・と訂正する。 11、明細書第18頁第6〜第9行を下記の通り訂正す
る。 −2〜 「第1図は本発明装置の全体概略側面図、第2図は廃水
浄化装置の要部縦断側面図、第3図は該装置の要部縦断
正面図、第4図は第2図IV−TV線断面図である。」 以上  3−
FIG. 1 is an overall schematic side view of the device of the present invention, FIG. 2 is a vertical sectional front view of the main part of the wastewater purification device, FIG. 3 is a vertical sectional side view of the main part of the device, and FIG. It is a sectional view taken along the TV line. T...Clean water tank, 3...Washing water supply pipe, 15...
Electrolytic purification chamber, 16...filtration chamber, 39...filter material, 4o
...Air jet pipe, 41...Pressure air source, 42...
Opening/closing valve, 44... Water pipe, 45... Branch pipe, 46.
... Three-way on-off valve, 49... Drain pipe, 51 River on-off valve.
゛Patent applicant: Takeuchi Tekko Co., Ltd. Procedural amendment (voluntary) June 12, 1980 1, Indication of the case 1982, Patent Application No. 23897 2, Title of invention: Filtration chamber cleaning device in waste water purification device 3, Amendment Relationship with the case of a person who makes a patent application Name of patent applicant: Takeuchi Tekko Co., Ltd. 4, Agent: 104 5, Subject of amendment Contents of amendment as shown in the attached sheet■. Page 4, line 15 of the specification: ``Washing water pump-1''...
・Correct it as "clean a) water pump"... 2. Specification, page 6, line 2, ...[Excellent electrolysis electrode-1......Toaro...
[Corrected as Electrolytic Electrode Plate Good-1...] 3. In the specification, page 10, line 7, it says ``Washing water pump.'' Correct it to ``Clean water pump.'' 4. In the specification, page 13, line 12, ...[Air-1...] is corrected to..."pressurized wastewater"... 5. In the specification, page 13, line 14, it says ``to''... It should be corrected to ``to''... 6. Specification, page 15, line 5, 1-..."Clean water pump"......
“Clean water pump 2”... Corrected. 7. In the specification, page 15, line 8, the words ``accumulator, etc.'' should be deleted. 8. Specification page 15, line 10, page 16, line 7, 18
In the first line of the page, ``Clean water''... Correct the word ``Clean water'' to ``Clean water''. 9. In the specification, page 16, line 11, it says... “Cleansing that flowed into”...
・[If it is filled with clean water, it becomes clean]... Correct. 10. In the second line of page 18 of the specification, the statement ``free state'' is corrected to ``floating state''. 11. Lines 6 to 9 of page 18 of the specification are corrected as follows. -2~ "Figure 1 is an overall schematic side view of the apparatus of the present invention, Figure 2 is a longitudinal side view of the main part of the wastewater purification apparatus, Figure 3 is a longitudinal sectional front view of the main part of the apparatus, and Figure 4 is the main part of the wastewater purification apparatus. It is a sectional view taken along the line IV-TV.'' 3-

Claims (1)

【特許請求の範囲】[Claims] 廃水を吸入し、その廃水中に混在する不純物を分離除去
する浄化室(15)と、不純物分離後の廃水を濾過する
濾過室(16)と、その濾過後の清浄化水を受容する清
浄水槽(7゛)と、該清浄水槽(T)内に設けられ、清
浄水を洗滌水供給管(3)を通して適宜の被洗滌物へ圧
送するようにした清浄水ポンプ(2)とを少なくとも備
えた廃水浄化装置において、前記洗滌水供給管(3)の
途中に分岐管(45)を分岐させ、この分岐管(45)
を、三方開閉弁(46)を介して、前記濾過室(16)
の底部と清浄水槽(T)の上部とを連通ずる導水管(4
4)の途中に接続し、°また前記洗滌水供給管(3)の
、前記分岐管(45)よりも下流側には開閉弁(51)
を介在し、さらに前記濾過室(16)内に収容されろ濾
4”l’(39)の底部に空気噴出管(40)を挿入し
、該管(40)の外端を圧力空気源(41)に開閉弁(
42)を介して接続し、また濾過室(16)の濾材(3
9)の上方に排水管(49)を連通してなる、廃水浄化
装置における濾過室洗滌装置。
A purification chamber (15) that sucks in wastewater and separates and removes impurities mixed in the wastewater, a filtration chamber (16) that filters the wastewater after impurity separation, and a clean water tank that receives the purified water after the filtration. (7゛), and a clean water pump (2) installed in the clean water tank (T) and configured to pump clean water to appropriate objects to be washed through the cleaning water supply pipe (3). In the wastewater purification device, a branch pipe (45) is branched in the middle of the washing water supply pipe (3), and this branch pipe (45)
into the filtration chamber (16) via the three-way on-off valve (46).
A water pipe (4) connecting the bottom of the tank and the top of the clean water tank (T)
4), and an on-off valve (51) is connected to the washing water supply pipe (3) on the downstream side of the branch pipe (45).
An air jet pipe (40) is inserted into the bottom of the filter 4''l' (39) housed in the filter chamber (16), and the outer end of the pipe (40) is connected to a pressure air source ( 41) has an on-off valve (
42), and the filter medium (3) of the filtration chamber (16).
9) A filtration chamber cleaning device in a wastewater purification device, which is formed by communicating a drain pipe (49) above the filtration chamber.
JP57023897A 1982-02-17 1982-02-17 Apparatus for washing filter chamber in waste water purification apparatus Pending JPS58143810A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57023897A JPS58143810A (en) 1982-02-17 1982-02-17 Apparatus for washing filter chamber in waste water purification apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57023897A JPS58143810A (en) 1982-02-17 1982-02-17 Apparatus for washing filter chamber in waste water purification apparatus

Publications (1)

Publication Number Publication Date
JPS58143810A true JPS58143810A (en) 1983-08-26

Family

ID=12123244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57023897A Pending JPS58143810A (en) 1982-02-17 1982-02-17 Apparatus for washing filter chamber in waste water purification apparatus

Country Status (1)

Country Link
JP (1) JPS58143810A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS571127A (en) * 1980-06-04 1982-01-06 Oomiya Mokuzai Kogyo Kk Article feed equipment
JPS58119311A (en) * 1982-06-15 1983-07-15 Takeuchi Tekko Kk Impurity remover of rinsing/purifying chamber in filter chamber for waste water cleaner

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS571127A (en) * 1980-06-04 1982-01-06 Oomiya Mokuzai Kogyo Kk Article feed equipment
JPS58119311A (en) * 1982-06-15 1983-07-15 Takeuchi Tekko Kk Impurity remover of rinsing/purifying chamber in filter chamber for waste water cleaner

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