JPS61141909A - Upward flow type filter apparatus with filter material washing apparatus - Google Patents

Upward flow type filter apparatus with filter material washing apparatus

Info

Publication number
JPS61141909A
JPS61141909A JP59263760A JP26376084A JPS61141909A JP S61141909 A JPS61141909 A JP S61141909A JP 59263760 A JP59263760 A JP 59263760A JP 26376084 A JP26376084 A JP 26376084A JP S61141909 A JPS61141909 A JP S61141909A
Authority
JP
Japan
Prior art keywords
filter material
water
sludge
filter
filter media
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
JP59263760A
Other languages
Japanese (ja)
Inventor
Toshihiro Watanabe
渡辺 寿広
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.)
Sankyo Kogyo Co Ltd
Original Assignee
Sankyo Kogyo Co Ltd
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 Sankyo Kogyo Co Ltd filed Critical Sankyo Kogyo Co Ltd
Priority to JP59263760A priority Critical patent/JPS61141909A/en
Publication of JPS61141909A publication Critical patent/JPS61141909A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the generation of a malodor, by providing a water stream type ejector for sucking a filter material and sludge and a cyclone type sand separator for taking in sludge and the filter material from upper flow to the lower part of a filter apparatus. CONSTITUTION:A mixture of a filter material and sludge is sucked and drawn out from the bottom part of a filter material accumulation layer 3 by a water stream type ejector 5. As water for operating the ejector 5, filtered treated water is used and introduced into the ejector 5 under pressure by a washing pump 4. The filter material and sludge pass through a rising pipe to enter a cyclone type sand separator 6. Conc. waste water of sludge is discharged from the upper flow of the sand separator and the filter material from the under flow thereof to be equally accumulated on the upper part of the filter material accumulation layer 3 by the action of a filter material distribution cone 7. Raw water is introduced under pressure from the interior of the filter material accumulation layer 3 and rises through the accumulation layer to be filtered.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は汚水や廃水の生物処理水に好適な濾過装置に
関し、完全に連続なp過運転が可能なンステムに関する
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a filtration device suitable for biologically treated sewage and wastewater, and relates to a system capable of completely continuous p-filtration operation.

従来の技術 サスペンション濃度の高い汚水や目づまりが生じやすい
ブスベンンヨンを含む汚水を濾過するには、濾過材の洗
浄・再利用を連続的に簡潔に円滑に効率よ〈実施し高能
率のろ過速度を保つ事が要求される。
Conventional technology In order to filter wastewater with a high concentration of suspension or wastewater containing pollutants that easily cause clogging, cleaning and reusing the filter media must be carried out continuously, simply, smoothly, and efficiently to maintain a high-efficiency filtration rate. things are required.

このような要求に応じた上向流濾過装置としては、エア
ーリフトによりサスペンションを捕捉した濾過材を大気
中に吹き上げ洗浄し、汚泥を溢流させ自然沈降するろ過
材を再使用する方式やブスベンンヨンを捕捉した濾過材
をポンプなどで取り出し、スクリューコンベア式洗浄器
に投入し、スクリューでろ過材を掻き上げる途中にンヤ
ワーをかけ濾過材に付着した汚泥を洗浄する方式などが
用いられている。
Upflow filtration devices that meet these demands include a method that uses an air lift to blow up the filter material that has captured the suspension into the atmosphere, cleans it, and allows the sludge to overflow and reuse the filter material that settles naturally. A method is used in which the captured filter media is taken out using a pump, etc., and placed in a screw conveyor washer, and while the screw is scraping up the filter media, the filter is stirred to remove the sludge that has adhered to the filter media.

発明の解決しようとする問題点 このような従来の方式では、汚水に臭気のある場合−の
発生・注入・排出に伴う騒音の発生が生じ、又ンヤワー
洗浄方式ではンヤワー用水が多量となυかつその笠せ廃
水となるなどの間踊がある。又悪臭などにより居住環境
に少なからず悪影響を与えやすい。従って設置場所が屋
内に制約される場合や密集地の屋外に設置する場合にf
″i%に不都合を生じ易い。又上記のような従来のろ過
材の洗浄・分離方式では排水中に濾過材が混入し流出す
るなどの問題もあり、効率的とはいえない。
Problems to be Solved by the Invention In such conventional methods, noise is generated due to the generation, injection, and discharge of sewage when it has an odor. There are dances such as the Kasase waste water. In addition, it tends to have a considerable negative impact on the living environment due to bad odors. Therefore, when the installation location is restricted to indoors or when installing outdoors in a crowded area, f
"i%" is likely to be inconvenient.Furthermore, the conventional cleaning/separation method for filter media as described above has problems such as the filter media being mixed into waste water and flowing out, and cannot be said to be efficient.

この発明は上記のような従来の方式の欠点を除去しかつ
簡単で故障せず、設備費・運転費を安価に提供する目的
のp過材洗浄装置付上向流濾過装置である。
The present invention is an upflow filtration device with a p filter material cleaning device that eliminates the drawbacks of the conventional system as described above, is simple, does not break down, and provides low equipment and operating costs.

問題点を解決するための手段 全体のンステムを構成するに当り、ilk低8に濾過操
作を終えたろ過材と汚泥との混合物を吸引・排出させる
水流式のエゼクタ−を設け、エゼクタ−効果により濾過
材から汚泥の洗浄を促しグl装置の一方にあるサンドセ
パレーターの入口に導く。アッパーフローからは濃厚な
汚泥を、アンダーフローからは濾過材を取り出t、z このように装置の一方にサイクロン式サンドセパレータ
ーを設ける事でアッパーフローからの濃厚な汚泥の排水
は完全に密閉系路内で行う事ができ、臭気の発散や騒音
の発生が生じない。又サイクロン式プントセパレーター
は従来より水中の砂分を除去するに広く利用され、その
効率性は衆知のものである。サンドセパレーターを採用
する事でろ過材の分離は完全に行え、アッパー70−か
ら流出する事はない。
In configuring the entire system to solve the problem, ILK LOW 8 is equipped with a water flow ejector that sucks and discharges the mixture of filter media and sludge after the filtration operation. The sludge is washed from the filter media and guided to the inlet of the sand separator on one side of the filter. Thick sludge is taken out from the upper flow, and filter material is taken out from the underflowt,z By installing a cyclone type sand separator on one side of the device, the drainage of thick sludge from the upper flow is completely sealed. It can be carried out in the street and does not emit odor or generate noise. Furthermore, the cyclone type Punto separator has been widely used to remove sand from water, and its efficiency is well known. By using a sand separator, the filter material can be completely separated and will not flow out from the upper 70-.

作用 ブイクロン式サンドセパレーターからのアンダーフロー
は上向流のろ過処理を終えた水中に落下し、濾過材の堆
積層上部に分配され下部方向に流動する。
The underflow from the buikron type sand separator falls into the water that has finished the upward flow filtration process, is distributed to the upper part of the sedimentary layer of the filter material, and flows downward.

原水はポンプにより濾過材の堆積層内に圧入され上向き
に濾過材の層を通過しながら清澄となり濾過材の層を離
れ上部から処理水として取り出す。
The raw water is forced into the layer of filter material by a pump, becomes clear as it passes upward through the layer of filter material, leaves the layer of filter material, and is taken out from the top as treated water.

以上のように濾過材は常に上部から下部に移動し、連続
的に排出され洗浄・分離の過程で再生し、目づまυによ
る濾過機能の低下が生じない。
As described above, the filter material always moves from the top to the bottom, is continuously discharged, and is regenerated during the washing and separation process, so that the filtration function does not deteriorate due to blinding υ.

実施例 以下図面に示す実施例でこの発明の詳細な説明する。Example The present invention will be described in detail below with reference to embodiments shown in the drawings.

以下の説明では本発明における濾過装置として最も単純
な構成をなす実施例から説明する。
In the following description, an embodiment of the filtering device according to the present invention having the simplest configuration will be explained.

第1図で5は水流式のエゼクタ−でろ過付堆積層3の底
部からろ過材と汚泥の混合物を吸引して抜き出す操作を
行わせる。エゼクタ−を作動させる水は濾過処理水を使
用し4の洗浄ポンプでエゼクタ−に圧入する。
In FIG. 1, reference numeral 5 denotes a water jet ejector that sucks and extracts a mixture of filter material and sludge from the bottom of the filtered sediment layer 3. The water used to operate the ejector is filtered water, which is pressurized into the ejector using a cleaning pump (4).

抜き出された濾過材と汚泥は上昇管を通過し6のサイク
ロン式サンドセパレーター人口に注入する。次にサンド
セパレーターのアッパーフローからは汚泥の濃厚なサス
ペンションが排出され洗浄排水となる。アンダーフロー
からは濾過材が排出し、濾過材堆積層3上層の清澄域に
沈降・落下し3の上部に設置した濾過材原水を圧入し、
3の堆積層を上昇し濾過されなから3を離れ上部より処
理水として取り出す。
The extracted filter material and sludge pass through the riser pipe and are injected into the cyclone type sand separator (6). Next, a thick suspension of sludge is discharged from the upper flow of the sand separator and becomes cleaning wastewater. The filter material is discharged from the underflow, settles and falls into the clear area above the filter material accumulation layer 3, and the filter material raw water installed above the layer 3 is injected under pressure.
It ascends the sedimentary layer of 3, leaves the unfiltered 3, and takes it out from the top as treated water.

第1図の実施例は濾過処理水の中に10%程度のサスペ
ンションの混入を認めても良く、施設費の軽減に重点を
おいた場合について述べたものだが、第2図に示す実施
例では濾過処理水の清澄度をよシ高くするための他の実
施例を示す図である。
The embodiment shown in Fig. 1 describes a case in which about 10% suspension may be allowed to be mixed in the filtered water, and the emphasis is on reducing facility costs, but the embodiment shown in Fig. 2 It is a figure which shows another Example for improving the clarity of filtered water.

サンドセパレーター6のアンダーフローから排出される
濾過材に一部混入する汚泥を再分離するに当り、アンダ
ーフローを直接p過処理光rの水域に投する事なく清澄
域内に再分離槽8を設置し、8の中で再分離させた後、
7を径3上部に堆積される。8の中は運転経過に伴い次
第に濃度が高くなるため定期的に排水する。
In order to re-separate the sludge that is partially mixed in the filtration material discharged from the underflow of the sand separator 6, a re-separation tank 8 is installed within the clarification area without directly dumping the underflow into the water area of the p-filtering light r. and after re-separation in 8,
7 is deposited on the top of diameter 3. As the concentration in the tank 8 gradually increases as the operation progresses, it is drained periodically.

この方式をとれば濾過水の清澄度を極めて高くとれる。By using this method, the clarity of the filtered water can be extremely high.

以上説明した通シ、濾過装置全体の構成に当シサイクロ
ン式サンドセパレーターを採用する事で、環境を乱さず
かつ経済的に効率よく連続濾過が実施できる。
By employing this cyclone type sand separator in the overall structure of the above-described filtering and filtration device, continuous filtration can be carried out economically and efficiently without disturbing the environment.

発明の効果 本装置を操作した一例を示すと、装置を室内に設置し濾
過装置本体の直径を30cmとし、原水を167、扮の
速度で流した。
Effects of the Invention To show an example of operating this device, the device was installed indoors, the diameter of the filtration device body was 30 cm, and raw water was flowed at a speed of 167 cm.

洗浄ポンプ5の吐出量は7のプントセパレーターの効率
が最上で機能する量とした。
The discharge amount of the cleaning pump 5 was set to the amount that would allow the Punto separator 7 to function at its highest efficiency.

その量はアッパーフローがt6L/分、アンダーフロー
は0.4t1分であった。
The amount of upper flow was t6L/min, and the underflow was 0.4t1min.

以上の操作でサスペン/コンの回収率は90チを維持し
、円滑に連続ヂ過を継続した。
Through the above operations, the recovery rate of Suspense/Con was maintained at 90 inches, and continuous passing continued smoothly.

又、装置からの悪臭の放出は全くなく濾過材洗浄排水量
は原水のサスベンンヨン濃度に関係なく1.6j/分で
円滑でかつ充分なヂ過機能を維持した。騒音源がなく装
置からの悪臭の放出もなく室内環境は良好であった。
In addition, no bad odor was emitted from the device, and the amount of drainage water for cleaning the filter material was 1.6 J/min, regardless of the concentration of sulphate in the raw water, maintaining a smooth and sufficient filtering function. The indoor environment was good, with no noise sources and no foul odors emitted from the equipment.

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

第1図は本発明の一実施例の構成を示す同第2図は他の
実施例の構成を示す図 A 原水槽 B 排水槽 C濾過処理水槽 1 原水ポンプ 2 原水圧入口 3 濾過付堆積層 4 洗浄ポンプ 5 水流式エゼクタ− 6サイクロン式すンドセパレー、a− 7濾過付分配カサ 8 再分離槽 図−1 コ                  舛図−2
Figure 1 shows the configuration of one embodiment of the present invention. Figure 2 shows the configuration of another embodiment. Raw water tank B Drainage tank C Filtration treatment tank 1 Raw water pump 2 Raw water pressure inlet 3 Sediment layer with filtration 4 Washing pump 5 Water type ejector 6 Cyclone type sund separator, a- 7 Distribution case with filtration 8 Re-separation tank diagram - 1 K Masu diagram - 2

Claims (1)

【特許請求の範囲】 ろ過材と捕捉した汚泥とを水にサスペンドさせた混合物
を注入し、アッパーフローから汚泥のサスペンションを
、アンダーフローからろ過材のサスペンションを取り出
すサイクロン式サンドセパレーターをろ過装置本体の一
方に設置し、他方に水流式のエゼクターをそなえる事を
特徴とする。 全体を構成するに当り、ろ過操作を終えたろ過材と汚泥
との混合物を上記エゼクターで吸引排出させ、配管で上
記サンドセパレーターに導き、サンドセパレーターのア
ンダーフローをろ過装置本体内のろ過処理を終えた水域
に混じ、ろ過槽内に堆積するろ過材の上部に分配する手
段と、ろ過材堆積層内に原水を注入する手段でろ過材の
層を上向きに通過させろ過処理を終えた水を取り出す手
段を採用したろ過装置。
[Claims] A cyclone-type sand separator is installed in the main body of the filtration device, which injects a mixture of filter media and captured sludge suspended in water, and takes out the suspension of sludge from the upper flow and the suspension of the filter media from the underflow. It is characterized by being installed on one side and having a water flow ejector on the other side. In configuring the whole, the mixture of filter media and sludge that has completed the filtration operation is suctioned and discharged by the ejector, guided to the sand separator through piping, and the underflow of the sand separator is discharged after the filtration process inside the filtration device body. Water that has been filtered through the layer of filter media is taken out by means of distributing it to the top of the filter media that is mixed with the water body and deposited in the filter tank, and by injecting raw water into the layer of filter media that passes upward through the layer of filter media. A filtration device that employs means.
JP59263760A 1984-12-15 1984-12-15 Upward flow type filter apparatus with filter material washing apparatus Pending JPS61141909A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59263760A JPS61141909A (en) 1984-12-15 1984-12-15 Upward flow type filter apparatus with filter material washing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59263760A JPS61141909A (en) 1984-12-15 1984-12-15 Upward flow type filter apparatus with filter material washing apparatus

Publications (1)

Publication Number Publication Date
JPS61141909A true JPS61141909A (en) 1986-06-28

Family

ID=17393896

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59263760A Pending JPS61141909A (en) 1984-12-15 1984-12-15 Upward flow type filter apparatus with filter material washing apparatus

Country Status (1)

Country Link
JP (1) JPS61141909A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52122966A (en) * 1976-04-08 1977-10-15 Takeda Chemical Industries Ltd Transfer layer type filtration method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52122966A (en) * 1976-04-08 1977-10-15 Takeda Chemical Industries Ltd Transfer layer type filtration method

Similar Documents

Publication Publication Date Title
KR101637562B1 (en) Apparatus for treating rain water
CN107803111A (en) A kind of desulfuration absorbing tower mist eliminator flushing water system for recycling
JPS61291099A (en) Downward flow type biological membrane purifying apparatus
CN2936380Y (en) Unpowered waste water filtering and sterilizing treating device
JP4633502B2 (en) Sand separation and cleaning equipment
JP2007144390A (en) Sand separating and washing device
KR100774583B1 (en) A screw-type high flow sand filter
CN110104852A (en) It is a kind of can be by the car wash water water supply device of wastewater from car washer cycling and reutilization
US6461509B1 (en) Method and installation for purifying contaminated water
JP2013212443A (en) Solid/liquid separator and method of cleaning solid/liquid separator
CN207576128U (en) A kind of desulfuration absorbing tower mist eliminator flushing water system for recycling
CN216918855U (en) Novel tunnel wastewater treatment multistage fine filtration system
KR20030059010A (en) Solid material and grit matter separator
US6149805A (en) Device for adding oxygen to water
JPS61141909A (en) Upward flow type filter apparatus with filter material washing apparatus
JP3175010B2 (en) Solid-liquid separation device
KR101799745B1 (en) Spiral Aerated Grit and FOG Remover System
JP2007090291A (en) Water filtration apparatus
KR200260371Y1 (en) Sedimentation Lifting and Cleaning Device
JPH1128490A (en) Fluidized bed type sewage treatment device
JP2006095413A (en) Sand separation/washing device
KR200242132Y1 (en) A waterjet cleaning apparatus for pulling up & washing sinked sand
JPH09271754A (en) Floating separation device
JPS6231634B2 (en)
CN209740858U (en) Recyclable furniture paint spraying wastewater treatment system