JPS6295196A - Contact oxidation biological filter device - Google Patents

Contact oxidation biological filter device

Info

Publication number
JPS6295196A
JPS6295196A JP60234296A JP23429685A JPS6295196A JP S6295196 A JPS6295196 A JP S6295196A JP 60234296 A JP60234296 A JP 60234296A JP 23429685 A JP23429685 A JP 23429685A JP S6295196 A JPS6295196 A JP S6295196A
Authority
JP
Japan
Prior art keywords
water
funnel
treated
filter media
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.)
Pending
Application number
JP60234296A
Other languages
Japanese (ja)
Inventor
Katsumi Iida
飯田 克已
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP60234296A priority Critical patent/JPS6295196A/en
Publication of JPS6295196A publication Critical patent/JPS6295196A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To improve treating capacity by providing a cylindrical partition plate having a perforated part in the upper part to the center of a treatment tank which has a funnel-shape bottom and is provided with a perforated plate in the upper part of the funnel, supplying water to be treated and air to the partition plate and packing contact filter media in the treatment tank. CONSTITUTION:The cylindrical partition plate 4 having the perforated part 3 in the upper part is provided to the center of the treatment tank 1 which has the funnel-shape bottom and is provided with the perforated plate 2 in the upper part of the funnel. A discharge port 10 of a nozzle 6 for injecting air-liquid mixed water to be treated which supplies pressure-fed water 8 to be treated and air 7 from an air intake pipe 5 is provided to the plate 4. The small piece meshed contact filter media 11 made of a synthetic resin having the specific gravity equal to the specific gravity of water or slightly lower than the same are packed in an adequate amt. into the tank 1. An injection nozzle 17 for cleaning the contact filter media 11 is further installed in the tank 1. As a result, the treating capacity is improved and since the implantation, hypertrophy, exfoliation and desorption of microorganisms are alternately executed with good balance at all times in the various parts of the contact filter media, stable treated water is always available.

Description

【発明の詳細な説明】 本発明は主として観賞池、庭園池、公園池、養魚池、つ
り堀、活魚いけす、つり餌いけす等の循環ろ過の低濃度
汚水に対し、効果的な浸漬ろ床接触酸化生物ろ過装置で
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides effective immersion filter bed contact for low-concentration wastewater mainly used for circulation filtration of ornamental ponds, garden ponds, park ponds, fish ponds, fishing ponds, live fish cages, fishing bait cages, etc. It is an oxidizing biological filtration device.

従来の庭園池、海水及び淡水活魚いけすの循環ろ過にi
よ、ろ材として砂、砕石、活性炭、貝殻等が使用されて
いるが、砂は空隙率が少さく、有機汚濁により、目詰り
が短時間で起き、頻繁に逆洗をとが必要で、多大な動力
が要ると共に相互の擦れ合いが起り、生物着床の余地が
少ない。
I for circulating filtration of conventional garden ponds, seawater and freshwater live fish cages
Sand, crushed stone, activated carbon, shells, etc. are used as filter media, but sand has a low porosity, and due to organic contamination, clogging occurs in a short period of time, and frequent backwashing is required, resulting in a large amount of waste. This requires a lot of power and causes mutual friction, leaving little room for biological implantation.

小石や砕石は重量があり、空隙率が少さく、石の表面の
みが有効で、石の内部は水処理に役に立たず、水流、水
圧、にて水路の拡大、変化は起きず閉塞が起り易く、貝
殻は水処理過程の有機酸に侵され、圧壊粉砕が起き、活
性炭は目詰りが激しく生 定期的に再成又は取り替えの必要があり、いずれのる材
も常時逆洗を行なわなければならず、濃縮された逆洗汚
水を製造しているようなもので、強力な高圧水を要し、
省エネとは言いがたいものである。
Pebbles and crushed stones are heavy and have low porosity, so only the surface of the stone is effective, and the inside of the stone is useless for water treatment, and the waterway does not expand or change due to water flow or water pressure, and blockages are likely to occur. Shells are attacked by organic acids during water treatment, resulting in crushing and crushing. Activated carbon becomes severely clogged and must be periodically regenerated or replaced, and all materials must be constantly backwashed. It is like producing concentrated backwash wastewater, which requires powerful high-pressure water.
This cannot be called energy saving.

本発明は接触ろ材として水より少し軽い程度の樹脂製の
一辺が2〜7センチ角、厚さ0.3〜1センチの扁平状
の網状短管(第3図)を使用し、通水をよくすると共に
接触面積の増加を考慮したもので、網の素線の太さ05
〜1ミリ、網目の大きさ2〜10ミリのものである。
The present invention uses a flat mesh short tube (Fig. 3) made of a resin that is slightly lighter than water and has a side of 2 to 7 cm square and a thickness of 0.3 to 1 cm as a contact filter medium. The thickness of the wire of the net is 05.
~1 mm, with a mesh size of 2 to 10 mm.

子もよく捕え、砂ろ過以上の清澄な処理水が得られるも
のである。
It also captures many young children and produces treated water that is clearer than sand filtration.

該樹脂扁平短管接触ろ材は比重(0,95〜097)の
硬質ポリエチレン樹脂が最適で、押出成形による安価な
量産品である。
The resin flat short tube contact filter medium is optimally made of hard polyethylene resin with a specific gravity of (0.95 to 0.97), and is an inexpensive mass-produced product by extrusion molding.

該ろ材の大きさ、網目の大きさは被処理水の種類により
選定し、養魚池の如く、エサを投与し、比較的汚濁負荷
の大きいものは、網目の大きなものを、エサを投与しな
い活魚蓄養いけす等の汚濁負荷の少さいものは網目の少
さいろ材を使用し、扁平な小片短管の形状は、単位体積
当りの収容数を大きくとるため、即ち接触面積の増大を
考えたものである。
The size of the filter medium and the size of the mesh are selected depending on the type of water to be treated, and for ponds where feed is applied, such as fish ponds, where the pollution load is relatively large, filters with large meshes are selected, and for live fish that are not fed with feed. For those with a low pollution load, such as farming cages, filter media with a small mesh size are used, and the shape of the flat small pieces and short tubes is designed to accommodate a large number of fish per unit volume, that is, to increase the contact area. be.

置が変り、攪拌洗滌できるものである。The location can be changed and the cleaning can be done by stirring.

該ろ材の接触面積は網の素線の囲りすべてか有効で、素
線に生物が付着すればする程接触面積が増能力があるこ
とであり、生物量の絶対数が大きければ大きいほど処理
能力が向上するのである。
The contact area of the filter media is effective if it covers the entire area surrounding the strands of the net, and the more living organisms adhere to the strands, the more the contact area increases, and the larger the absolute number of biomass, the more effective the treatment. Your abilities will improve.

該ろ材は網であるため、水流は縦横無尽にどの方向にも
通ることができ、水流がよく通るところは獣 微生物の繁殖がよく、早く目が詰まるが、詰まれば水流
は他の方向へ流れ、詰まった個所は水流がこなくなるた
め、酸素も栄養も運ばれてこないの生・物は水流に乗っ
て次の接触ろ材にたどりつき着床し、着床できない老廃
物的な汚泥は順次接触ろ材の下へ下へと循環水流にて運
ばれ、運ばれる途中にフロックが生長し、より大きな塊
となり、処理に接触ろ材のあちこちで微生物の@禾肥大
、剥離離脱が交互にバランスよく行われるため、逆洗回
数は従来の装置の数十分の1になり、徹底的に情夫 洗滌しても、該網ろ材の素線のどこかに微生物の種が残
り、通水すれば無数の水路が得られ、瞬時のうちに繁殖
し、立ち上がりが早く、いつも安定より、汚泥の消化が
進み、余剰汚泥は飛躍的に減少し、池等で発生するアオ
コ等も該ろ材にて捕捉吸着され、高等多細胞生物のワム
シ、ミジンコ等に食されることによりいつも清澄が保た
れるのである。
Since the filter media is a net, water can pass in any direction in all directions, and where the water flows through well, animal microorganisms breed well and the filters become clogged quickly, but if they become clogged, the water flows in other directions. Since the water flow is no longer flowing to the clogged area, neither oxygen nor nutrients are carried in. Living organisms and substances ride the water flow and reach the next contact filter media and settle there.The waste sludge that cannot be deposited is sequentially transferred to the contact filter media. The flocs are transported downward by the circulating water current, and as they are being transported, the flocs grow and become larger clumps, and microorganisms are alternately enlarged and exfoliated in a well-balanced manner throughout the filter media in contact with the treatment. The number of times of backwashing is reduced to a few tenths of that of conventional equipment, and even after thorough cleaning, microbial seeds remain somewhere in the strands of the mesh filter material, and countless waterways open when water is passed through. sludge is obtained, reproduces instantly, stands up quickly, and is always stable.The digestion of sludge progresses, excess sludge is dramatically reduced, and blue-green algae, etc. that occur in ponds etc. are also captured and adsorbed by the filter medium, resulting in high Because it is eaten by multicellular organisms such as rotifers and daphnia, it always remains clear.

本装置を図面を追いながら説明すると、底部が漏戸状の
処理槽(L)、(1)に漏戸上部有孔板(2) 、 (
2)の上部で処理槽(1)の中央部に、上部に有孔部(
3) 、 (3)を有した筒状の仕切板(4)、(4)
を設置し、その仕切板(4)の中央部より少し下部に空
気吸入管(5)i5)を持つ被処理水噴射ノズル(6)
 、 (6)より吸入空気(7)と被処理水(8)の気
液混合噴射水(9)の上向きの吐出口(10)(10)
を設け、仕切板(4)の外側と処理槽(1)の内側に接
触ろ材(印、 (11)を充填した装置である。
To explain this device while following the drawings, there is a processing tank (L) with a funnel-shaped bottom, (1) a perforated plate (2) above the funnel, (
2) in the center of the treatment tank (1), and the upper part has a perforated part (
3) Cylindrical partition plates (4), (4) with (3)
and a water injection nozzle (6) having an air suction pipe (5) i5) slightly below the center of the partition plate (4).
, (6) upward discharge ports (10) (10) of gas-liquid mixed jet water (9) of intake air (7) and water to be treated (8)
This is a device in which contact filter media (marked (11)) are filled on the outside of the partition plate (4) and inside the processing tank (1).

ポンプにて送られて来る被処理水(8)は被処理水噴射
ノズル(6)より噴出するが、このノズル(6)の周囲
は減圧状になり、空気吸入管(5)より導かれた多量の
空気(7)を吸引し、噴射水(9)に少さな気泡が混入
され、気泡の上昇と噴射水のと向流(12)、 (12
)により循環水流(13)、 (13)が発生し、接触
ろ材(11)を通り抜ける際に生物酸化接触処理が行わ
れるものである。
The water to be treated (8) sent by the pump is jetted out from the water injection nozzle (6), but the area around this nozzle (6) is under reduced pressure, and the water is guided through the air suction pipe (5). A large amount of air (7) is sucked in, small air bubbles are mixed into the jet water (9), and the air bubbles rise and the jet water flows countercurrently (12).
) generates circulating water flows (13), (13), which undergo biological oxidation contact treatment when passing through the contact filter medium (11).

従来のろ過装置では処理槽に圧送するのみであるが、本
発明装置は被処理水供給に要する圧送エネルギーを利用
し、エジェクタ一方式によるエアレーションを行い、気
泡の上昇によるエアリフト及び噴射水の上向流(12)
による循環水流(13)を多量に発生させ、接触ろ材(
11)の接触効率を高め、被処理水供給と同時にエアレ
ーションを兼ね備えた生物酸化省エネ装置である。
Conventional filtration equipment only pumps the water into the treatment tank, but the device of the present invention utilizes the pumping energy required to supply the water to be treated, performs aeration with a one-way ejector, and increases the air lift due to the rise of bubbles and the upward movement of the injected water. flow (12)
A large amount of circulating water flow (13) is generated by the contact filter medium (
This is a biological oxidation energy saving device that increases the contact efficiency of 11) and provides aeration as well as supply of water to be treated.

被処理水噴射ノズル(6)に供給された圧送被処理水(
8)は空気吸入管(5)より空気(7)を吸引し、細か
い気泡を含む混気噴射水(9)となり、吐出口(10)
より吐出され、仕切板(4)内を上昇し、上部有孔部(
3)より該ろ材(11)が浸漬されている側へと移り、
循環水流(13を形成し、処理水出口有孔管(14)、
 (14)より水位(15)。
The pressure-fed treated water (
8) sucks air (7) from the air suction pipe (5), turns it into mixed air jet water (9) containing fine air bubbles, and sends it to the discharge port (10).
It is discharged from the upper perforated part (
3) move to the side where the filter medium (11) is immersed;
forming a circulating water flow (13) and a treated water outlet perforated pipe (14);
Water level (15) from (14).

(15)を保持するため立ち上げられた処理水出口管(
16(16)より排水されるのである。
(15) The treated water outlet pipe (
The water is drained from 16 (16).

接触ろ材の洗滌は高圧水を利用し、処理槽(1)の内側
に沿って噴射できる数個の洗滌用噴射ノズル(17(1
7)より噴流を発生させ、攪拌水流(18)、 (18
)を生ぜしめ、ろ材を攪拌移動させて水流とろ材相互の
擦れ合いにより洗滌するのである。
Cleaning of the contact filter media uses high-pressure water, which can be sprayed along the inside of the treatment tank (1) using several cleaning spray nozzles (17 (1)
7) generate a jet stream and stir water stream (18), (18
), the filter media is stirred and moved, and the water flow and the filter media rub against each other to wash them.

剥離汚泥は処理槽(1)の漏戸状下部の汚泥沈澱部(1
9(19)に沈澱し、汚泥引抜き弁(2D)、 (20
)にて排出するものである。
The peeled sludge is deposited in the sludge settling section (1) at the funnel-shaped lower part of the treatment tank (1).
9 (19), sludge extraction valve (2D), (20
).

洗滌用噴射ノズルt17)は吐出「」の先を平たくした
もの、又は吐出口の先を絞った樹脂管の安価なものでよ
く、高圧水はバルブの切替えにて被処理水供給ポンプを
利用し、三方コック(21)、(21)の切替えにて洗
滌水(22)、 (22)iよ排出するものである。
The cleaning injection nozzle t17) may be an inexpensive one with a flattened discharge end or a resin pipe with a narrowed discharge opening, and high-pressure water can be supplied using a water supply pump by switching a valve. The cleaning water (22) and (22)i are discharged by switching the three-way cocks (21) and (21).

番号(23)は処理水であり、番号(24)は本装置の
据付は安定をよくするための足架台である。
The number (23) is the treated water, and the number (24) is a footrest to improve the stability of the installation of this device.

該ろ材(11)は空隙率が大きく、多大な接触面積を有
〉 いほど、多量の被処理水を供給することが必要で)  
接触面積が大きければ大きいほど処理滞留時間は短かく
ても処理出来るのである。
The larger the porosity of the filter medium (11) and the larger the contact area, the more water to be treated needs to be supplied.
The larger the contact area, the shorter the treatment residence time can be.

本装置は圧送被処理水と同時に空気の供給を受は償 微生物にとっては多量の食へ物と酸素を繰返し繰ノ能力
が大きく、処理能力が多大なものである。
This device receives a supply of air at the same time as the water to be treated under pressure, and has a large capacity to repeatedly supply a large amount of food and oxygen to the microorganisms, and has a large processing capacity.

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

Claims (1)

【特許請求の範囲】[Claims] 底部が漏戸状になり、漏戸上部に有孔板(2)を設けた
処理槽(1)の中央に、上部に有孔部(3)を有する筒
状の仕切板(4)を設け、該仕切板(4)に圧送被処理
水(8)と空気吸入管(5)より空気(7)を供給する
気液混合被処理水噴射ノズル(6)の吐出口(10)を
設け、処理槽(1)内に比重が水に等しいか、水より少
し軽い程度の合成樹脂製の網目状の小片の接触ろ材(1
1)の適量を充填させたもので、接触ろ材(11)の洗
滌用噴射ノズル(17)を処理槽(1)内に設置したこ
とを特徴とする接触酸化生物ろ過装置
A cylindrical partition plate (4) having a perforated portion (3) at the top is provided in the center of a treatment tank (1) having a funnel-shaped bottom and a perforated plate (2) above the funnel. , the partition plate (4) is provided with a discharge port (10) of a gas-liquid mixed treated water injection nozzle (6) for supplying pressure-fed treated water (8) and air (7) from an air suction pipe (5); In the treatment tank (1), there is a contact filter medium (1
A contact oxidizing biological filtration device filled with an appropriate amount of 1), and characterized in that an injection nozzle (17) for cleaning the contact filter medium (11) is installed in the treatment tank (1).
JP60234296A 1985-10-18 1985-10-18 Contact oxidation biological filter device Pending JPS6295196A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60234296A JPS6295196A (en) 1985-10-18 1985-10-18 Contact oxidation biological filter device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60234296A JPS6295196A (en) 1985-10-18 1985-10-18 Contact oxidation biological filter device

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP60276431A Division JPS6295197A (en) 1985-12-09 1985-12-09 Contact oxidation biological filter device

Publications (1)

Publication Number Publication Date
JPS6295196A true JPS6295196A (en) 1987-05-01

Family

ID=16968766

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60234296A Pending JPS6295196A (en) 1985-10-18 1985-10-18 Contact oxidation biological filter device

Country Status (1)

Country Link
JP (1) JPS6295196A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004526561A (en) * 2001-03-09 2004-09-02 カウンシル・オブ・サイエンティフィック・アンド・インダストリアル・リサーチ Process and backflow loop reactor for sewage purification

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004526561A (en) * 2001-03-09 2004-09-02 カウンシル・オブ・サイエンティフィック・アンド・インダストリアル・リサーチ Process and backflow loop reactor for sewage purification

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