JPH11267678A - Carrier added biologically treating device - Google Patents

Carrier added biologically treating device

Info

Publication number
JPH11267678A
JPH11267678A JP10074517A JP7451798A JPH11267678A JP H11267678 A JPH11267678 A JP H11267678A JP 10074517 A JP10074517 A JP 10074517A JP 7451798 A JP7451798 A JP 7451798A JP H11267678 A JPH11267678 A JP H11267678A
Authority
JP
Japan
Prior art keywords
carrier
reaction tank
microorganism
tank
separating means
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
JP10074517A
Other languages
Japanese (ja)
Inventor
Tomoaki Tanaka
倫明 田中
Atsushi Watanabe
敦 渡辺
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP10074517A priority Critical patent/JPH11267678A/en
Publication of JPH11267678A publication Critical patent/JPH11267678A/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

PROBLEM TO BE SOLVED: To increase a microorganism holding amount of a carrier adding biologically treating device and to separate the microorganism carrier from a treated water without causing a clogging at a carrier separating means. SOLUTION: This treating device is provided with a reaction tank 10 in which a microorganism carrier 12 is packed and also to which a raw water supply means 11 is connected, a cylindrical carrier separating means 14 immersing in the tank while positioning its upper end on a liq. surface of the reaction tank 10 and provided with a waste water discharge means 16 discharging a treated water flowed inside to the outside of the tank 10, a carrier removing means 19 revoluting around an outer periphery surface of the carrier separating means and having a gap between the carrier separating means 14 and the means 19 kept smaller than the particle size of the microorganism carrier and an agitating means 13 agitating the liq. in the reaction tank and the microorganism carrier at an under side of the carrier separating means.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、硝化、脱窒、発
酵等の生物処理を反応槽内に充填した微生物担体によっ
て行う担体添加生物処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a carrier-added biological treatment apparatus for performing biological treatment such as nitrification, denitrification, and fermentation by using a microorganism carrier filled in a reaction vessel.

【0002】[0002]

【従来の技術】生物処理は、反応槽内に保持した微生物
により処理を行うため、槽内での微生物の保持濃度を高
めることで高負荷化が可能になる。反応槽内の微生物保
持量を増加させる方法として、反応槽に微生物を担持す
る担体を添加する方法があるが、処理水を担体と分離す
る担体分離手段が担体によって閉塞されやすいという問
題点がある。
2. Description of the Related Art In biological treatment, since microorganisms are treated in a reaction vessel, the load can be increased by increasing the concentration of microorganisms retained in the vessel. As a method of increasing the amount of microorganisms held in the reaction tank, there is a method of adding a carrier that supports microorganisms to the reaction tank, but there is a problem that the carrier separation means for separating treated water from the carrier is easily blocked by the carrier. .

【0003】[0003]

【発明が解決しようとする課題】例えば曝気を伴う方式
では、硝化槽内に微生物を坦持したゲル状担体を添加
し、担体分離手段としてウェッジワイヤスクリーンを用
い、ウェッジワイヤスクリーン面を曝気することでゲル
状担体がウェッジワイヤスクリーンを閉塞するのを防止
するのであるが、ウェッジワイヤスクリーンを通過する
処理水の通過流速が大きくなると、閉塞が生じた。又、
脱窒等の曝気を伴わない方式では、曝気を利用できない
ため、底を有する円筒形のウェッジワイヤからなる担体
分離筒を反応槽に浸漬して該分離筒の上端部を水面上に
突出させ、この担体分離筒のなかに微生物を坦持したゲ
ル状担体を充填し、分離筒の内周に沿って担体除去翼を
旋回し、ゲル状担体がウェッジワイヤ間の間隙を内側か
ら閉塞しようとするのを掻き取って防止することが行わ
れているが、ゲル状担体が弾力性を有する場合は閉塞が
生じ易い。それは、図3に示すように担体除去翼の旋回
によるゲル状担体の進行方向をウェッジワイヤのスクリ
ーン面が遮ることになるため、ゲル状担体はスクリーン
面に押付けられ、担体の一部が弾性変形してウェッジワ
イヤの間隙に押し込まれ、詰るからである。
For example, in a method involving aeration, a gel carrier carrying microorganisms is added to a nitrification tank, and a wedge wire screen is used as a carrier separation means, and the wedge wire screen surface is aerated. This prevents the gel-like carrier from blocking the wedge wire screen. However, when the flow rate of the treated water passing through the wedge wire screen increases, the wedge wire screen is blocked. or,
In the method that does not involve aeration such as denitrification, because aeration cannot be used, a carrier separation cylinder made of a cylindrical wedge wire having a bottom is immersed in a reaction tank, and the upper end of the separation cylinder is projected above the water surface. This carrier separation tube is filled with a gel-like carrier carrying microorganisms, and the carrier removal wing is swirled along the inner periphery of the separation tube, and the gel-like carrier tries to close the gap between the wedge wires from the inside. Although the prevention is carried out by scraping, when the gel-like carrier has elasticity, blockage tends to occur. As shown in FIG. 3, the screen surface of the wedge wire blocks the traveling direction of the gel-like carrier due to the rotation of the carrier removing blade, so that the gel-like carrier is pressed against the screen surface, and a part of the carrier is elastically deformed. Then, it is pushed into the gap between the wedge wires and becomes clogged.

【0004】[0004]

【課題を解決するための手段】本発明は、反応槽内の微
生物の保持量を高めると共に、担体の閉塞を防止できる
機構を持つ担体添加生物処理装置を提供することを目的
に開発されたもので、微生物担体を充填すると共に、原
水の供給手段が接続された反応槽と、上端部を反応槽の
液面上に位置させて槽内に浸漬して設けられ、内部に流
入する処理水を反応槽の外に排出する排水手段を備えた
円筒型の担体分離手段と、該担体分離手段の外周面を旋
回し、担体分離手段との隙間を微生物担体の粒径より小
さくした担体除去手段と、担体分離手段の下で反応槽の
液及び微生物担体を攪拌する攪拌手段とを備えているこ
とを特徴とする。
SUMMARY OF THE INVENTION The present invention has been developed with the object of providing a carrier-added biological treatment apparatus having a mechanism capable of increasing the amount of microorganisms held in a reaction tank and preventing blockage of the carrier. In the reaction vessel connected to the raw water supply means while filling the microbial carrier, and provided with the upper end positioned immersed in the vessel with the upper end positioned on the liquid surface of the reaction vessel, the treated water flowing into the inside A cylindrical carrier separation means provided with a drainage means for discharging outside of the reaction tank, and a carrier removal means in which the outer peripheral surface of the carrier separation means is swirled and a gap between the carrier separation means and the particle diameter of the microorganism carrier is made smaller. And a stirring means for stirring the liquid in the reaction tank and the microorganism carrier under the carrier separating means.

【0005】[0005]

【発明の実施の形態】10は槽内底部に原水が供給管1
1で供給される反応槽で、槽内にはゲル状微生物担体1
2が添加され、攪拌羽根13で攪拌される。ゲル状微生
物担体12は、ポリアクリルアミド、カラギーナン、寒
天、ポリビニールアルコール、アルギン酸ナトリウム、
ポリエチレングリコールなどを主成分とするもので、直
径0.1〜10.0mm、好ましくは1.0〜5.0m
m、比重0.5〜3.0g/cm3 、好ましくは0.9
〜1.1g/cm3 で表面に微細な凹凸を有し、且つゼ
オライトなどの粒径5〜40μmの無機物粒子を、乾燥
時の担体重量の1〜10%程度付着させたものが好まし
い。添加量は反応槽の見かけ容積で0.1〜80%、好
ましくは10〜50%とする。又、担体が担持する微生
物は、一般従属栄養細菌、硝化細菌、脱窒細菌、メタン
菌、酵母、或いはそれらの混合系など、生物処理の目的
に応じ適切に定める。尚、攪拌羽根13の回転速度は3
RPM程度である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Reference numeral 10 designates a feed pipe 1 at the bottom of a tank.
1. The reaction tank supplied in 1 and contains a gel-like microorganism carrier 1 in the tank.
2 is added and stirred by the stirring blade 13. The gel-like microorganism carrier 12 is made of polyacrylamide, carrageenan, agar, polyvinyl alcohol, sodium alginate,
It is mainly composed of polyethylene glycol or the like, and has a diameter of 0.1 to 10.0 mm, preferably 1.0 to 5.0 m.
m, specific gravity 0.5-3.0 g / cm 3 , preferably 0.9
It is preferable that inorganic particles having a particle size of 5 to 40 [mu] m, such as zeolite, having fine irregularities on the surface of about 1.1 g / cm < 3 > and adhering about 1 to 10% of the weight of the carrier when dried. The amount of addition is 0.1 to 80%, preferably 10 to 50% by apparent volume of the reaction tank. The microorganisms carried by the carrier are appropriately determined depending on the purpose of biological treatment, such as general heterotrophic bacteria, nitrifying bacteria, denitrifying bacteria, methane bacteria, yeast, or a mixed system thereof. The rotation speed of the stirring blade 13 is 3
It is about RPM.

【0006】反応槽の内部上方には、担体の粒径よりも
小さい空隙を有するウェッジワイヤやパンチングメタル
のスクリーンで円筒面が構成された有底の担体分離筒1
4を、その上端部が反応槽の水面から上に突出すよう
に、例えば放射状の支持部材15により支持し、槽内に
浸漬する。そして、担体分離筒14の底には、反応槽の
外への処理水の排水管16を接続する。担体分離筒14
は中心に中空部17を有し、この中空部には反応槽の中
心沿いに設けたモータなどで回転される回転軸18が貫
通支持され、回転軸の下端部には前述の攪拌羽根13が
取付けられている。
[0006] Above the inside of the reaction vessel, a bottomed carrier separation cylinder 1 having a cylindrical surface formed by a wedge wire or a punched metal screen having a void smaller than the particle size of the carrier.
4 is supported by, for example, a radial support member 15 so that its upper end projects upward from the water surface of the reaction tank, and is immersed in the tank. Then, a drain pipe 16 of the treated water to the outside of the reaction tank is connected to the bottom of the carrier separation tube 14. Carrier separation tube 14
Has a hollow portion 17 at the center, a rotary shaft 18 rotated by a motor or the like provided along the center of the reaction tank is penetrated and supported in the hollow portion, and the above-described stirring blade 13 is provided at the lower end of the rotary shaft. Installed.

【0007】上記回転軸18には担体分離筒14を直径
方向に跨いで、該分離筒の外周面を旋回する逆U字形の
担体分離翼19が固定してある。担体分離翼19の、担
体分離筒14の外周に対向する面19′にはゴム板状の
ものを取付け、分離筒の外周面を旋回する際に弾力的に
接触して撫でるようにしてもよいが、担体分離筒の外周
面との間に隙間を保つ場合はその隙間は微生物担体の粒
径より小にする。
[0007] An inverted U-shaped carrier separation wing 19 is fixed to the rotating shaft 18 so as to straddle the carrier separation tube 14 in the diameter direction and rotate around the outer peripheral surface of the separation tube. A rubber plate may be attached to the surface 19 ′ of the carrier separation blade 19 facing the outer periphery of the carrier separation tube 14, and may be elastically contacted and stroked when turning the outer periphery of the separation tube. However, when a gap is maintained between the carrier separation tube and the outer peripheral surface, the gap is made smaller than the particle size of the microorganism carrier.

【0008】供給管11から反応槽内の底部に供給され
た原水は攪拌翼13で攪拌されながら槽内に添加された
ゲル状微生物担体12と接触し、原水中の生物分解物質
は微生物により分解され生物処理水となり、ゲル状微生
物担体を円周面のウェッジワイヤやパンチングメタルで
分離しながら担体分離筒14に流入し、排水管16から
反応槽の外に取出される。
[0008] The raw water supplied from the supply pipe 11 to the bottom of the reaction tank comes into contact with the gel-like microbial carrier 12 added to the tank while being stirred by the stirring blades 13, and the biodegradable substances in the raw water are decomposed by microorganisms. Then, the microorganism-like microorganism carrier flows into the carrier separation tube 14 while being separated by a wedge wire or punching metal on the circumferential surface, and is taken out of the reaction tank from the drain pipe 16.

【0009】生物処理水が担体分離筒14を経て排水管
16から流出する流れによって担体分離筒14の外周の
ウェッジワイヤスクリーンやパンチングメタルのスクリ
ーン面の外にはゲル状微生物担体が集まり、スクリーン
面を閉塞して生物処理水が担体分離筒14の内部に流入
するのを阻害しようとする。しかし、担体分離筒の外周
にはスクリーン面に沿って旋回する逆U字形の担体除去
翼19が、該筒14を直径方向に横切って設けてあり、
該除去翼19の、担体分離筒の外周に対向する面19′
は外周を撫でるか、又は離れているにせよその間隙はゲ
ル状微生物担体の粒子よりも小である。これにより担体
除去翼19の回転によるゲル状微生物担体12の進行方
向は図1(B)に示したように広く空いているため、担
体が担体分離筒のスクリーン面に押付けられることはな
い。従って、担体が弾性変形してスクリーン面に詰り、
処理水が担体分離筒内に流入するのを閉塞して阻害する
ことは無い。
Due to the flow of the biologically treated water flowing out of the drain pipe 16 through the carrier separation tube 14, the gel-like microbial carriers collect outside the wedge wire screen or the perforated metal screen surface of the carrier separation tube 14, and the screen surface. To prevent the biologically treated water from flowing into the carrier separation tube 14. However, on the outer periphery of the carrier separation cylinder, an inverted U-shaped carrier removal blade 19 that rotates along the screen surface is provided across the cylinder 14 in the diameter direction,
The surface 19 'of the removing blade 19 facing the outer periphery of the carrier separation cylinder.
The gaps are smaller than the particles of the gel-like microbial carrier, whether stroking the periphery or apart. As a result, the traveling direction of the gel-like microorganism carrier 12 due to the rotation of the carrier removing blade 19 is widely vacant as shown in FIG. 1B, so that the carrier is not pressed against the screen surface of the carrier separating cylinder. Therefore, the carrier is elastically deformed and clogs the screen surface,
It does not obstruct the flow of the treated water into the carrier separation cylinder.

【0010】そして、この実施例のように攪拌羽根13
と、担体除去翼19を共通の回転軸18に取付けて回転
駆動することにより構造は簡易になり、且つ動力コスト
も節減できる。
Then, as in this embodiment, the stirring blade 13
By attaching the carrier removing blade 19 to the common rotating shaft 18 and driving the same to rotate, the structure is simplified and the power cost can be reduced.

【0011】反応槽10内に微生物を坦持したポリエチ
レングリコール系の直径4mmのゲルを見掛け容量で5
0%添加し、72時間通水後に担体分離筒の外周のウェ
ッジワイヤースクリーン面の閉塞状態を調査した。尚、
ウェッジワイヤーのスクリーン面の目開きは1.5m
m、開口率は50%であった。尚、装置の脱窒負荷は
2.0kg−N/m3 ・日、HRTは1.5時間、スク
リーン目開き2.0mm/2.0mm(スクリーン開口
部幅/ウェッジワイヤー幅)、スクリーン通過流速40
m/時であった。
A polyethylene glycol-based gel having a diameter of 4 mm and carrying microorganisms in the reaction tank 10 has an apparent volume of 5 mm.
0% was added, and after passing water for 72 hours, the closed state of the wedge wire screen surface on the outer periphery of the carrier separation cylinder was examined. still,
The aperture of the screen surface of the wedge wire is 1.5m
m, and the aperture ratio was 50%. The denitrification load of the apparatus was 2.0 kg-N / m 3 · day, the HRT was 1.5 hours, the screen aperture was 2.0 mm / 2.0 mm (screen opening width / wedge wire width), and the screen passing flow rate 40
m / hr.

【0012】図3のように担体分離筒の内周に沿って担
体除去翼を旋回させた場合のスクリーンの閉塞率は5.
8%であるのに対し、図1(B)に示すように担体分離
筒の外周に沿って担体除去翼を旋回させた場合のスクリ
ーンの閉塞率は0.1%で、殆ど閉塞は生じなかった。
As shown in FIG. 3, when the carrier removing blade is turned along the inner periphery of the carrier separating cylinder, the screen closing rate is 5.
In contrast to 8%, when the carrier removing blade is turned along the outer circumference of the carrier separation cylinder as shown in FIG. 1 (B), the screen blocking rate is 0.1%, and almost no blocking occurs. Was.

【0013】[0013]

【発明の効果】以上で明らかなように、本発明では反応
槽内に担体によって微生物を添加するので微生物保持量
が増大し、高負荷の処理を安定して行えると共に、反応
槽を小型化し設置面積を小さくできる。そして、微生物
担体を処理水と分離する担体分離手段の閉塞が生じな
い。
As is clear from the above, in the present invention, the microorganisms are added to the reaction tank by the carrier, so that the microorganism holding amount is increased, the processing with a high load can be performed stably, and the reaction tank is downsized and installed. The area can be reduced. Further, the carrier separation means for separating the microorganism carrier from the treated water does not become blocked.

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

【図1】Aは本発明の装置の一実施形態の縦断面図、B
は担体分離手段からの担体の分離状況の説明図。
FIG. 1A is a longitudinal sectional view of one embodiment of the device of the present invention, FIG.
FIG. 4 is an explanatory diagram of a state of separation of a carrier from a carrier separating means.

【図2】図1の実施形態の要部の拡大斜視図。FIG. 2 is an enlarged perspective view of a main part of the embodiment of FIG. 1;

【図3】従来の装置の担体分離手段からの担体の分離状
況の説明図。
FIG. 3 is an explanatory view of a state of separating a carrier from a carrier separating means of a conventional apparatus.

【符号の説明】[Explanation of symbols]

10 反応槽 11 原水の供給管(供給手段) 12 微生物担体 13 攪拌翼(攪拌手段) 14 担体分離筒(担体分離手段) 15 支持部材 16 処理水の排水管(排水手段) 17 担体分離筒の中空部 18 回転軸 19 担体除去翼(担体除去手段) DESCRIPTION OF SYMBOLS 10 Reaction tank 11 Raw water supply pipe (supply means) 12 Microorganism carrier 13 Stirring blade (stirring means) 14 Carrier separation tube (carrier separation means) 15 Support member 16 Drainage pipe of treated water (drainage means) 17 Hollow of carrier separation cylinder Part 18 Rotation axis 19 Carrier removal wing (carrier removal means)

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成10年4月9日[Submission date] April 9, 1998

【手続補正1】[Procedure amendment 1]

【補正対象書類名】図面[Document name to be amended] Drawing

【補正対象項目名】図1[Correction target item name] Fig. 1

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【図1】 FIG.

【手続補正2】[Procedure amendment 2]

【補正対象書類名】図面[Document name to be amended] Drawing

【補正対象項目名】図3[Correction target item name] Figure 3

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【図3】 FIG. 3

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 微生物担体を充填すると共に、原水の供
給手段が接続された反応槽と、上端部を反応槽の液面上
に位置させて槽内に浸漬して設けられ、内部に流入する
処理水を反応槽の外に排出する排水手段を備えた円筒型
の担体分離手段と、該担体分離手段の外周面を旋回し、
担体分離手段との隙間を微生物担体の粒径より小さくし
た担体除去手段と、担体分離手段の下で反応槽の液及び
微生物担体を攪拌する攪拌手段とを備えていることを特
徴とする担体添加生物処理装置。
1. A reaction tank filled with a microbial carrier and connected to a raw water supply means, and an upper end portion is provided by being immersed in the tank with the upper end positioned above the liquid surface of the reaction tank and flowing into the inside. Cylindrical carrier separation means provided with a drainage means for discharging the treated water out of the reaction tank, and turning the outer peripheral surface of the carrier separation means,
A carrier removing means provided with a carrier removing means in which a gap with the carrier separating means is smaller than the particle diameter of the microorganism carrier, and a stirring means for stirring the liquid in the reaction tank and the microorganism carrier under the carrier separating means. Biological treatment equipment.
JP10074517A 1998-03-23 1998-03-23 Carrier added biologically treating device Pending JPH11267678A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10074517A JPH11267678A (en) 1998-03-23 1998-03-23 Carrier added biologically treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10074517A JPH11267678A (en) 1998-03-23 1998-03-23 Carrier added biologically treating device

Publications (1)

Publication Number Publication Date
JPH11267678A true JPH11267678A (en) 1999-10-05

Family

ID=13549611

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10074517A Pending JPH11267678A (en) 1998-03-23 1998-03-23 Carrier added biologically treating device

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013062057A1 (en) * 2011-10-28 2013-05-02 株式会社クラレ Screen device for wastewater treatment tank and wastewater treatment method
KR101307441B1 (en) * 2013-05-16 2013-09-11 (주) 영동엔지니어링 Multistage rotating biological contactor having drum form for method of rotating biological contactor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013062057A1 (en) * 2011-10-28 2013-05-02 株式会社クラレ Screen device for wastewater treatment tank and wastewater treatment method
JP2013107075A (en) * 2011-10-28 2013-06-06 Kankyo System Kaihatsu:Kk Screen device for wastewater treatment tank, and wastewater treatment method
KR101307441B1 (en) * 2013-05-16 2013-09-11 (주) 영동엔지니어링 Multistage rotating biological contactor having drum form for method of rotating biological contactor

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