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JPS5931390B2 - wastewater treatment equipment - Google Patents
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JPS5931390B2 - wastewater treatment equipment - Google Patents

wastewater treatment equipment

Info

Publication number
JPS5931390B2
JPS5931390B2 JP55057666A JP5766680A JPS5931390B2 JP S5931390 B2 JPS5931390 B2 JP S5931390B2 JP 55057666 A JP55057666 A JP 55057666A JP 5766680 A JP5766680 A JP 5766680A JP S5931390 B2 JPS5931390 B2 JP S5931390B2
Authority
JP
Japan
Prior art keywords
water
tank
pressurized
wastewater
sludge
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
Application number
JP55057666A
Other languages
Japanese (ja)
Other versions
JPS56152780A (en
Inventor
賢 本郷
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.)
Sanken Setsubi Kogyo Co Ltd
Original Assignee
Sanken Setsubi 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 Sanken Setsubi Kogyo Co Ltd filed Critical Sanken Setsubi Kogyo Co Ltd
Priority to JP55057666A priority Critical patent/JPS5931390B2/en
Publication of JPS56152780A publication Critical patent/JPS56152780A/en
Publication of JPS5931390B2 publication Critical patent/JPS5931390B2/en
Expired legal-status Critical Current

Links

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  • Physical Water Treatments (AREA)
  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明は廃水処理装置に関する。[Detailed description of the invention] The present invention relates to wastewater treatment equipment.

更に詳しくは、生物学的に処理された廃水中の汚泥を分
離する装置に関する。
More specifically, the present invention relates to an apparatus for separating sludge in biologically treated wastewater.

回転円板(バイオサーフ)等から送られてきた汚泥を含
有する廃水に気泡を含有する水を加えて槽(加圧浮上槽
と呼ぶことにする)の下部より噴出させると気泡表面に
汚泥が付着して槽の水面に浮上し、浮上した汚泥をフロ
ススクレーパで1取って除去し、残りの水を隣接槽に送
り、該槽内に設けられた濾過面に長い毛が多数設けられ
た回転ドラム式長毛濾過機(ロータリー・スピッツ)で
濾過することにより汚泥を除去する廃水処理装置がある
When water containing air bubbles is added to wastewater containing sludge sent from a rotating disk (Biosurf), etc., and it is ejected from the bottom of a tank (we will call it a pressurized flotation tank), sludge forms on the surface of the air bubbles. The sludge that adheres to the water surface of the tank is removed by removing it with a floss scraper, and the remaining water is sent to an adjacent tank. There is a wastewater treatment device that removes sludge by filtering it with a drum-type long-hair filter (rotary spitz).

この装置にあっては、間欠的あるいは連続的にロータリ
ー・スピッツの濾過面を逆洗することにより、濾過面の
長毛に付着した汚泥を除去する必要がある。
In this device, it is necessary to remove sludge adhering to the long bristles of the filter surface by backwashing the filter surface of the rotary spitz intermittently or continuously.

逆洗に際しては、ドラムを回転させながら、濾過面近く
に設けた吸引口から水を多量に吸引するので、逆洗に際
して多量の汚水が発生し、その結果として処理されるべ
き廃水の量が著しく増大するという欠点があり、逆洗に
より発生する汚水の量を流入水の15%以下に抑えるの
に、かなりの技術的困難を伴うのが実情であった。
During backwashing, a large amount of water is sucked in from the suction port installed near the filter surface while rotating the drum, so a large amount of wastewater is generated during backwashing, and as a result, the amount of wastewater to be treated is significantly reduced. In reality, it is difficult to suppress the amount of wastewater generated by backwashing to 15% or less of the inflow water.

本発明はこのような問題点を解決するためになされたも
のであって、その要旨は加圧浮上槽、該加圧浮上槽の水
面に浮上した汚泥を掻き取るスクレーパ、スクレーパで
汚泥を除いたあとの水を流入せしめる第二水槽、該第二
水槽内に設けた回転ドラム式長毛濾過機、回転ドラム式
長毛7慮過機の濾過面近くに設けた逆洗用吸引口、該吸
引口と配管で連結された加圧ポンプ、加圧空気を水に溶
解して貯える空気溶解槽、前記加圧ポンプと前記空気溶
解槽とを連結する配管、回転円板(バイオサーフ)等か
らの汚泥を含有する廃水を前記加圧浮上槽に供給する廃
水供給管、前記空気溶解槽と前記廃水供給管とを減圧弁
を介して連結する加圧水供給管、を具備する廃水処理装
置にある。
The present invention was made to solve these problems, and its gist is to provide a pressurized flotation tank, a scraper for scraping off sludge floating on the water surface of the pressurized flotation tank, and a scraper for removing the sludge with the scraper. A second water tank into which the remaining water flows, a rotating drum type long hair filter installed in the second water tank, a backwash suction port provided near the filtering surface of the rotating drum type long hair 7 filter, and the suction port. Sludge from a pressurizing pump connected by piping, an air dissolving tank that dissolves and stores pressurized air in water, piping connecting the pressurizing pump and the air dissolving tank, a rotating disk (Biosurf), etc. The wastewater treatment apparatus includes a wastewater supply pipe that supplies wastewater contained in the pressurized flotation tank to the pressurized flotation tank, and a pressurized water supply pipe that connects the air dissolution tank and the wastewater supply pipe via a pressure reducing valve.

図面は本発明の一実施例を示す図である。The drawings are diagrams showing one embodiment of the present invention.

1は加圧浮上槽、2は該加圧浮上槽の水面に浮上した汚
泥を掻き取るフロススクレーパ、3は第二水槽である。
1 is a pressurized flotation tank, 2 is a floss scraper for scraping off sludge floating on the water surface of the pressurized flotation tank, and 3 is a second water tank.

該第二水槽3は隔壁11により加圧浮上槽1と隔てられ
ている。
The second water tank 3 is separated from the pressurized flotation tank 1 by a partition wall 11.

4は回転ドラム式長毛濾過機(ロータリー・スピッツ)
、5は加圧ポンプである。
4 is a rotating drum type long hair filter (rotary spitz)
, 5 is a pressure pump.

9は回転ドラム式長毛濾過機40回転ドラム面の近くに
該ドラム面の幅一杯に設けられた逆洗用吸引口であり、
該吸引口9と加圧ポンプ5とは配管で連結されている。
9 is a backwash suction port provided near the 40-rotating drum surface of the rotary drum type long hair filter and spanning the entire width of the drum surface;
The suction port 9 and the pressure pump 5 are connected through piping.

6は空気溶解槽、10は加圧ポンプ5と空気溶解槽6と
を連結する配管である。
6 is an air dissolving tank, and 10 is a pipe connecting the pressurizing pump 5 and the air dissolving tank 6.

7は回転円板(バイオサーフ)等からの汚泥を含有する
廃水を加圧浮上槽1に供給する廃水供給管で、その一端
は加圧浮上槽1内下部に突出し、複数個の廃水噴出用ノ
ズル12が設けられている。
Reference numeral 7 denotes a wastewater supply pipe that supplies wastewater containing sludge from a rotating disk (Biosurf), etc. to the pressurized flotation tank 1, one end of which protrudes into the lower part of the pressurized flotation tank 1, and is used to spout multiple wastewaters. A nozzle 12 is provided.

8は空気溶解槽6から廃水供給管7に空気を多量に含ん
だ加圧水を供給するだめの加圧水供給管、13は減圧弁
である。
8 is a pressurized water supply pipe for supplying pressurized water containing a large amount of air from the air dissolving tank 6 to the waste water supply pipe 7, and 13 is a pressure reducing valve.

14は空気圧縮機、15は圧縮空気を水に供給するだめ
の圧縮空気供給管、16はフロス槽、17は汚泥ポンプ
、18は汚泥を脱水設備へ送る配管である。
14 is an air compressor, 15 is a compressed air supply pipe for supplying compressed air to water, 16 is a floss tank, 17 is a sludge pump, and 18 is a pipe for sending sludge to dewatering equipment.

また19は回転ドラム式長毛濾過機4で濾過して得た処
理水を排出する排出管である。
Further, 19 is a discharge pipe for discharging the treated water obtained by filtering with the rotary drum type long-hair filter 4.

次に作用を説明する。Next, the action will be explained.

廃水供給管7により、回転円板(バイオサーフ)等から
の廃水は加圧浮上槽1へ流入する直前に、加圧水供給管
8から減圧弁13を経て送られてきた空気を多量に含ん
だ水と合流する。
Immediately before the wastewater from the rotating disk (Biosurf), etc. flows into the pressurized flotation tank 1 through the wastewater supply pipe 7, the water containing a large amount of air is sent from the pressurized water supply pipe 8 via the pressure reducing valve 13. join with.

この水は加圧下に空気を溶解することにより常圧下で溶
解できるよりも多量の空気を溶解したものであるから、
減圧弁13を経て廃水と合流した際、圧力の低下に伴っ
て多量の気泡を発生する。
This water has a larger amount of air dissolved in it under pressure than can be dissolved under normal pressure.
When the waste water passes through the pressure reducing valve 13 and joins with the waste water, a large amount of bubbles are generated as the pressure decreases.

従って、廃水噴出用ノズル12からは廃水が多量の気泡
と共に噴出する。
Therefore, waste water is ejected from the waste water ejecting nozzle 12 together with a large amount of bubbles.

廃水中の汚泥が気泡の表面に付着して加圧浮上槽1内を
水面まで浮上してフロススクレーパ2で掻き取られる。
Sludge in the wastewater adheres to the surface of the bubbles, floats up to the water surface in the pressurized flotation tank 1, and is scraped off by the floss scraper 2.

掻き取られた汚泥はフロス槽16へ集められ汚泥ポンプ
17により、配管18を経て脱水設備へ送られる。
The scraped sludge is collected in a floss tank 16 and sent by a sludge pump 17 to a dewatering facility via piping 18.

一方、加圧浮上槽1で浮上した汚泥を除いたあとの廃水
は隔壁11をオーバーフローして第二水槽3に流入し、
回転ドラム式長毛罐過機4で濾過され、濾過された処理
水は回転ドラム式長毛濾過機4のドラムの回転軸(中空
になっている)を経て排出管19から排出される。
On the other hand, the wastewater after removing the sludge floated in the pressurized flotation tank 1 overflows the partition wall 11 and flows into the second water tank 3.
The filtered treated water is filtered by the rotary drum type long hair filter 4, and is discharged from the discharge pipe 19 through the rotary shaft (hollow) of the drum of the rotary drum type long hair filter 4.

回転ドラム式長毛濾過機4の濱過面の逆洗を行なう際に
は、加圧ポンプ5を作動させて、ドラムを回転させなが
ら洗滌水と壇過面の長毛に付着した汚泥とを吸引口9か
ら吸引すると共に、該加圧ポンプ5で洗滌水を配管10
により空気溶解槽6へ圧送する。
When backwashing the filtration surface of the rotary drum type long hair filter 4, the pressurizing pump 5 is operated to rotate the drum and remove the washing water and the sludge attached to the long hairs of the filtration surface from the suction port. 9, and the pressurized pump 5 supplies washing water to the pipe 10.
The air is fed to the air dissolving tank 6 under pressure.

この際、空気圧縮機14により得られた圧縮空気を配管
10の洗滌水の中へ注入し、空気溶解槽6で空気を水に
溶解させる。
At this time, compressed air obtained by the air compressor 14 is injected into the washing water in the pipe 10, and the air is dissolved in the water in the air dissolving tank 6.

空気溶解槽6で得られた空気を多量に含んだ加圧水は、
前述の如く、加圧水供給管8及び減圧弁13を経て、廃
水と合流する。
The pressurized water containing a large amount of air obtained in the air dissolution tank 6 is
As mentioned above, it passes through the pressurized water supply pipe 8 and the pressure reducing valve 13 and joins with the waste water.

回転ドラム式長毛濾過機4の逆洗に用いる水の量は通常
、装置へ送られてくる廃水の25〜40%程度(例えば
約1/3)である。
The amount of water used for backwashing the rotary drum type long-hair filter 4 is usually about 25 to 40% (for example, about 1/3) of the wastewater sent to the device.

本発明の装置では回転ドラム式長毛濾過機の逆洗に際し
充分な量の洗滌水を用いることができ、しかも洗滌水が
空気を多量に含む加圧水として再利用されるので、水の
使用に無駄がなく、処理すべき廃水の量の増大が避けら
れるという特長がある。
With the device of the present invention, a sufficient amount of washing water can be used for backwashing a rotary drum type long-hair filter, and since the washing water is reused as pressurized water containing a large amount of air, there is no waste in water usage. It has the advantage of avoiding an increase in the amount of wastewater to be treated.

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

図面は本発明に係る廃水処理装置の一実施例の概略断面
図である。 1・・・・・・加圧浮上槽、2・・・・・・スクレーパ
、3・・・・・・第二水槽、4・・・・・・回転ドラム
式長毛濾過機、5・・・・・・加圧ポンプ、6・・・・
・・空気溶解槽、7・・・・・・廃水供給管、8・・・
・・・加圧水供給管、9・・・・・・逆洗用吸引口、1
0・・・・・・加圧ポンプと空気溶解槽とを連結する配
管、13・・・・・・減圧弁。
The drawing is a schematic sectional view of one embodiment of the wastewater treatment device according to the present invention. 1... Pressurized flotation tank, 2... Scraper, 3... Second water tank, 4... Rotating drum type long hair filter, 5... ...pressure pump, 6...
...Air dissolution tank, 7...Wastewater supply pipe, 8...
... Pressurized water supply pipe, 9 ... Backwash suction port, 1
0... Piping connecting the pressurizing pump and the air dissolving tank, 13... Pressure reducing valve.

Claims (1)

【特許請求の範囲】[Claims] 1 加圧浮上層と、該加圧浮上槽の水面に浮上した汚泥
を掻き取るスクレーパ、と、スクレーパで汚泥を除いた
あとの水を流入せしめる第二水槽と、該第二水槽内に設
けた回転ドラム式長毛濾過機と、回転ドラム式長毛濾過
機の濾過面近くに設けた逆洗用吸引口と、該吸引口と配
管で連結された加圧ポンプと、加圧空気を水に溶解して
貯える空気溶解槽と、前記加圧ポンプと前記空気溶解槽
とを連結する配管と、汚泥を含有する廃水を前記加圧浮
上槽に供給する廃水供給管と、前記空気溶解槽と前記廃
水供給管とを減圧弁を介して連結する加圧水供給管と、
を具備することを特徴とする廃水処理装置。
1 A pressurized flotation layer, a scraper that scrapes the sludge floating on the water surface of the pressurized flotation tank, a second water tank into which the water after removing the sludge with the scraper flows, and a rotating mechanism provided in the second water tank. A drum-type long-hair filter, a backwash suction port provided near the filter surface of the rotating drum-type long-hair filter, a pressure pump connected to the suction port via piping, and a pressurized air dissolved in water. an air dissolving tank for storing, piping connecting the pressurizing pump and the air dissolving tank, a wastewater supply pipe supplying wastewater containing sludge to the pressurized flotation tank, and the air dissolving tank and the wastewater supply pipe. a pressurized water supply pipe connecting the two via a pressure reducing valve;
A wastewater treatment device comprising:
JP55057666A 1980-04-30 1980-04-30 wastewater treatment equipment Expired JPS5931390B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55057666A JPS5931390B2 (en) 1980-04-30 1980-04-30 wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55057666A JPS5931390B2 (en) 1980-04-30 1980-04-30 wastewater treatment equipment

Publications (2)

Publication Number Publication Date
JPS56152780A JPS56152780A (en) 1981-11-26
JPS5931390B2 true JPS5931390B2 (en) 1984-08-01

Family

ID=13062224

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55057666A Expired JPS5931390B2 (en) 1980-04-30 1980-04-30 wastewater treatment equipment

Country Status (1)

Country Link
JP (1) JPS5931390B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0629683U (en) * 1992-09-14 1994-04-19 オルガノ株式会社 Solid-liquid separation device
FI116833B (en) * 2002-04-15 2006-03-15 Reino Jorma Johanne Janatuinen Purification procedure for wastewater from fish farming
KR100506037B1 (en) * 2002-12-02 2005-08-09 임창성 Apparatus for disposing waste water
JP2014009567A (en) * 2012-07-03 2014-01-20 Nagaoka International Corp Clogging removal device for infiltration gallery

Also Published As

Publication number Publication date
JPS56152780A (en) 1981-11-26

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