JPH0128867Y2 - - Google Patents

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Publication number
JPH0128867Y2
JPH0128867Y2 JP1983194910U JP19491083U JPH0128867Y2 JP H0128867 Y2 JPH0128867 Y2 JP H0128867Y2 JP 1983194910 U JP1983194910 U JP 1983194910U JP 19491083 U JP19491083 U JP 19491083U JP H0128867 Y2 JPH0128867 Y2 JP H0128867Y2
Authority
JP
Japan
Prior art keywords
tank
air lift
pipe
air
water
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
JP1983194910U
Other languages
Japanese (ja)
Other versions
JPS60104293U (en
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 filed Critical
Priority to JP1983194910U priority Critical patent/JPS60104293U/en
Publication of JPS60104293U publication Critical patent/JPS60104293U/en
Application granted granted Critical
Publication of JPH0128867Y2 publication Critical patent/JPH0128867Y2/ja
Granted legal-status Critical Current

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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

Description

【考案の詳細な説明】 本考案は、槽内に微生物付着用担体として粒状
固体を懸濁させ、槽内に配備したエアリフト管を
使用して気体撹拌を行いながら前記粒状固体を槽
内で循環流動させる汚水の生物処理装置に関する
ものである。
[Detailed description of the invention] This invention suspends granular solids in a tank as a carrier for microbial attachment, and circulates the granular solids in the tank while stirring the gas using an air lift tube installed in the tank. This invention relates to a biological treatment device for fluidized wastewater.

最近、活性汚泥法におけるバルキング現象や維
持管理の複雑さを解消したものとして、チユーブ
接触酸化法、回転円板法、粒状固体流動床法など
を採用した各種の生物膜式汚水処理装置が実用化
されている。これらのうち、槽内に懸濁させた粒
状固体の表面に微生物を付着させ、槽内に配備し
たエアリフト管を介して気体撹拌を行いながら槽
内で前記粒状固体を循環流動させて汚水と接触さ
せることにより汚水中の汚濁物質を除去する粒状
固体流動床法は、他の生物膜法に比べて微生物の
付着に供する粒状固体の表面積が飛躍的に大きく
とれるために槽内に多量の微生物を保持できる
点、粒状固体が槽内を循環流動しているので目詰
りや部分的な嫌気化などのトラブルが起こらない
点など、多くの利点を有しているため注目を集め
ている。
Recently, various biofilm-type sewage treatment systems have been put into practical use that use tube catalytic oxidation, rotating disk method, granular solid fluidized bed method, etc. to solve the bulking phenomenon and complexity of maintenance in the activated sludge method. has been done. Among these methods, microorganisms are attached to the surface of granular solids suspended in a tank, and the granular solids are circulated and flowed in the tank while gas agitation is carried out through an air lift pipe installed in the tank, and the solids come into contact with wastewater. Compared to other biofilm methods, the granular solid fluidized bed method, which removes pollutants from wastewater, allows for a much larger surface area of the granular solids for microorganisms to adhere to, so it is possible to collect a large amount of microorganisms in the tank. It is attracting attention because it has many advantages, such as the ability to hold solids, and because the granular solids circulate and flow within the tank, problems such as clogging and partial anaerobic formation do not occur.

このような粒状固体流動床法では、微生物付着
用として砂、アンスラサイト、活性炭、ゼオライ
ト、プラスチツク球などの微生物の付着に適して
おり、かつ槽内を円滑に循環流動するに適した比
重、粒径を持つた粒状固体が用いられるが、通
常、価格、入手の難易なども考慮して粒径0.1〜
0.4mm程度の砂が多く用いられており、このよう
な粒状固体の槽内投入量は、運転条件などにより
適宜決定されるが、通常槽容量の5〜20%が投入
される。
In this granular solid fluidized bed method, materials such as sand, anthracite, activated carbon, zeolite, and plastic spheres are suitable for attaching microorganisms, and particles with specific gravity and particles suitable for smooth circulation and fluidization within the tank are used. A granular solid with a certain diameter is used, but usually the particle size is 0.1 to
Sand of about 0.4 mm is often used, and the amount of such granular solids added to the tank is appropriately determined depending on the operating conditions, but usually 5 to 20% of the tank capacity is added.

また、前記エアリフト管はその下部に空気導入
管が連結されており、管内に吹込まれた空気のエ
アリフト作用により、粒状固体がエアリフト管の
内外を循環流動しており、槽下部はこの循環流動
を円滑たらしめるように、通常下方に向けて横断
面積が縮少するように傾斜している。
In addition, the air lift tube has an air introduction tube connected to its lower part, and due to the air lift action of the air blown into the tube, granular solids circulate inside and outside the air lift tube, and the lower part of the tank absorbs this circulating flow. To ensure smoothness, it is usually sloped so that the cross-sectional area decreases downward.

エアリフト管の配備された槽の上方の1部又は
全周は、上端が水面上にあり下端が水面下にある
隔壁にて循環部と分離部とが区画形成されてお
り、槽内の懸濁液の一部は、この分離部を上昇す
る間に、粒状固体を分離し、上方より流出水とし
て取り出される。さらに、通常この流出水は後処
理装置としての凝集沈殿、砂ろ過装置などに送ら
れ、該流出水中のSS,BOD,COD除去等の処理
を受け、最終処理水となる。
A part or the entire circumference above the tank in which the air lift pipe is installed is divided into a circulation part and a separation part by a partition wall whose upper end is above the water surface and whose lower end is below the water surface. A portion of the liquid separates granular solids while rising through this separation section, and is taken out from above as effluent water. Furthermore, this effluent is usually sent to a coagulation sedimentation, sand filter, etc. as a post-treatment device, and undergoes treatment such as removing SS, BOD, and COD from the effluent, and becomes the final treated water.

ところで、このような粒状固体流動床法は、多
くの利点を有する反面、粒状固体の循環流動をエ
アリフト管内に吹き込んだ空気のエアリフト作用
にのみ依存しているところから、空気吹込み条件
の変化、又は補修、停電等による空気吹込みの停
止時には、槽内の粒状固体が槽底に沈積し、通常
その堆積粒子面はエアリフト管吸込下端より上方
となり、該吸込下端及び槽下部とエアリフト管と
の間隙を塞ぐ状態となる。
Incidentally, although such a granular solid fluidized bed method has many advantages, it relies only on the airlift action of the air blown into the airlift tube to circulate the granular solid, so it is difficult to change the air blowing conditions. Or, when air blowing is stopped due to repairs, power outages, etc., granular solids in the tank will settle on the bottom of the tank, and the surface of the deposited particles will usually be above the lower end of the air lift pipe suction, and there will be a gap between the lower end of the suction, the lower part of the tank, and the air lift pipe. This will close the gap.

そして、再起動時には、この沈積した粒状固体
を再び流動化させる必要があるが、単に空気を吹
き込んだだけでは、この沈積粒子を流動させるに
足る液流速が得られず、起動不能という流動床法
にとつて致命的な事態となる。
When restarting, it is necessary to fluidize the deposited granular solids again, but simply blowing in air does not provide enough liquid flow rate to fluidize the deposited particles, making startup impossible. This is a fatal situation for.

このために従来法では、この沈積粒子を流動化
させ、エアリフトによる輸送を可能とするため、
槽底より沈積粒子を流動化するに足る十分量の起
動水を吹き込み、一旦沈積粒子を膨張、流動させ
てから空気吹込みを開始し、再起動する方法が一
般的にとられており、この起動水吹込み方法並び
に吹込み構造について種々の工夫がなされてき
た。
For this purpose, in the conventional method, these deposited particles are fluidized so that they can be transported by air lift.
Generally, a sufficient amount of startup water is blown from the bottom of the tank to fluidize the sedimented particles, and once the sedimented particles are expanded and fluidized, air injection is started and restarted. Various ideas have been made regarding starting water injection methods and injection structures.

しかしながら、これらの方法は、第1に多量の
起動用水量を使用することが必要で、この水量確
保のための設備を要する点、すなわち、この水を
外部に求めると大規模な貯水槽が必要となり、ま
た、これを槽内上部より採取する方式とすれば、
槽内粒子の吸い込みにより起動水の吹込み部(ノ
ズル、デイストリビユータ、散水管等)の閉塞を
引き起こしたりするなどの難点があり、また第2
には、微生物が付着して密に沈積した粒子を槽全
体に均一に流動化させることが仲々困難で、確実
な流動を達成するために、ノズルやデイストリビ
ユータを数多く用いたり、起動水吹込み用ポンプ
として高圧高水量のものを必要としたりするな
ど、構造的にも複雑で不経済なものとならざるを
得なかつた。
However, these methods first require the use of a large amount of water for startup, and require equipment to secure this amount of water. In other words, if this water is obtained externally, a large-scale water tank is required. And if this is collected from the upper part of the tank,
There are drawbacks such as the suction of particles in the tank, which can cause blockages in the starting water injection parts (nozzles, distributors, water pipes, etc.).
It is difficult to uniformly fluidize the particles, which are densely deposited with microorganisms, throughout the tank, and in order to achieve reliable fluidization, many nozzles and distributors are used, and starting water spray is used. The structure was complicated and uneconomical, as it required a high-pressure, high-flow water pump.

本考案は、この様な従来装置で起こりがちなト
ラブルを排除し、簡易にして確実な再起動を行わ
せることができる新しい流動床生物処理装置を提
供することを目的とするものである。
The purpose of the present invention is to provide a new fluidized bed biological treatment apparatus that eliminates the troubles that tend to occur with conventional apparatuses and allows for simple and reliable restarting.

本考案は、原水流入部及び処理水排出部を有し
かつ微生物付着用の粒状固体を収容した槽内に、
上端が水面上で下端が槽底より離隔した隔壁にて
循環部と分離部とを区画形成し、前記循環部内に
上端が水面下で下端がほぼ槽底付近にあり、かつ
下端付近に空気導入管を連結したエアリフト管を
配備した流動床生物処理装置であつて、前記エア
リフト管の少なくとも下端を昇降可能たらしめた
ことを特徴とするものである。
The present invention has a tank that has a raw water inlet and a treated water outlet and contains granular solids for adhering to microorganisms.
A circulation part and a separation part are defined by a partition wall having an upper end above the water surface and a lower end separated from the tank bottom, and into the circulation part, the upper end is below the water surface and the lower end is almost near the tank bottom, and air is introduced near the lower end. The present invention is a fluidized bed biological treatment apparatus equipped with an airlift tube in which pipes are connected, and is characterized in that at least the lower end of the airlift tube is movable up and down.

本考案の一実施例を図面を参照しながら説明す
れば、第1図示例は槽内で粒状固体が沈積した状
態を示し、原水流入管1が開口し、上方に処理水
の流出部2を有し、かつ微生物付着用の粒状固体
3を収容した槽4内には、上端が水面上で下端が
槽底より離隔した隔壁5によつて粒状固体2の循
環部6と分離部7とが区画形成されている。循環
部6のほぼ中心付近には、上端が水面下にあり下
端が槽底より離隔したエアリフト管8が配備さ
れ、エアリフト管8の下方部に空気導入管9が開
口連結されている。
To explain one embodiment of the present invention with reference to the drawings, the first illustrated example shows a state in which granular solids are deposited in the tank, and the raw water inflow pipe 1 is opened and the treated water outlet 2 is opened upward. In the tank 4 containing the granular solids 3 for adhesion of microorganisms, a circulation part 6 and a separation part 7 for the granular solids 2 are separated by a partition wall 5 whose upper end is above the water surface and whose lower end is separated from the tank bottom. Compartments are formed. An air lift pipe 8 having an upper end below the water surface and a lower end spaced apart from the tank bottom is disposed approximately in the vicinity of the center of the circulation section 6, and an air introduction pipe 9 is open-connected to the lower part of the air lift pipe 8.

さらにエアリフト管8は、少なくともその下端
を昇降可能たらしめるが、エアリフト管8全体を
水面下において昇降可能たらしめるもよいが、図
示例のような構造にするのもよい。すなわち、図
示例のようにエアリフト管8を内外二重構造と
し、内外何れか一方を固定し、この固定管8′に
昇降管8″を摺動可能に嵌合し、昇降管8″を螺桿
10に適宜螺合させ、槽外のハンドル11又は図
示しない他の動力源によつて固定管8′と摺動昇
降させるようにしたものである。
Further, at least the lower end of the air lift tube 8 is made to be able to be raised and lowered, but the entire air lift tube 8 may be made to be able to be raised and lowered below the water surface, or it may be structured as shown in the illustrated example. That is, as shown in the illustrated example, the air lift pipe 8 has a double structure inside and outside, and either the outside or the outside is fixed, and the elevator pipe 8'' is slidably fitted into the fixed pipe 8', and the elevator pipe 8'' is screwed into a screw rod. 10, and is slid up and down on the fixed tube 8' using a handle 11 outside the tank or another power source (not shown).

また、第2図示例のように、昇降管8″を下端
に大径管を組合せた二重管構造としたものでもよ
い。
Further, as in the second illustrated example, the elevator pipe 8'' may have a double pipe structure in which a large diameter pipe is combined at the lower end.

なお、空気導入管9はエアリフト管8の下方部
に開口連結されているために、エアリフト管の昇
降に追随するように、その少なくとも一部を可撓
管12たらしめると便利である。
In addition, since the air introduction pipe 9 is open-connected to the lower part of the air lift pipe 8, it is convenient to make at least a part of it a flexible pipe 12 so as to follow the rise and fall of the air lift pipe.

次にその作用を説明すれば、通常の処理運転時
においては、エアリフト管8内下方に空気導入管
9より吹き込まれた空気のエアリフト作用によつ
て、粒状固体3を懸濁した槽内液がエアリフト管
8の下端より管内に流入し、上端から吐き出され
て循環部6下降し、再びエアリフト管8下端より
管内に流入する循環流動状態が形成されている。
そして、原水流入管1から槽4内に導かれた汚水
は、前記のように槽内を循環流動する間に、粒状
固体3の表面に付着した微生物の好気的作用によ
つて汚水中の汚濁成分が分解除去され、この循環
流動する液の一部は隔壁5の下端をくぐつて分離
部7に流入し、ここで粒状固体3が沈降分離さ
れ、処理水として流出部2から槽外へ流出する。
Next, to explain its effect, during normal processing operation, the tank liquid in which the granular solids 3 are suspended is caused by the air lift effect of the air blown into the air lift tube 8 downward from the air introduction tube 9. A circulating flow state is formed in which air flows into the air lift tube 8 from the lower end thereof, is discharged from the upper end, descends into the circulation section 6, and then flows back into the air lift tube 8 from the lower end.
The sewage introduced into the tank 4 from the raw water inflow pipe 1 is circulated through the tank as described above, and the aerobic action of the microorganisms attached to the surface of the granular solids 3 causes the sewage to become The pollutant components are decomposed and removed, and a part of this circulating liquid passes through the lower end of the partition wall 5 and flows into the separation section 7, where the granular solids 3 are sedimented and separated, and are discharged from the outflow section 2 to the outside of the tank as treated water. leak.

いま、何らかの理由により、空気導入管9から
の空気の吹込みが停止すると、槽4内の粒状固体
3は、第1図示の如く槽底に沈積し、エアリフト
管8の下端部及びエアリフト管8と槽壁の間を塞
いだ状態になる。この沈積した粒状固体3を再び
循環流動させるには、エアリフト管8全体を水面
下において上方に引き上げるか、あるいは図示例
の昇降管8″を引き上げてエアリフト管8の下端
が沈積した粒状固体3の界面との間に適当な距離
になる位置に設定する。しかして、空気導入管9
から空気を吹き込むと、界面付近に生じた水流に
よつて、界面付近の粒子がエアリフト管8の内外
を循環流動するようになる。そこで、エアリフト
管8の下端を徐々に下げてゆけば、次第に多くの
沈積粒子がエアリフト管8内に吸い込まれて循環
するようになり、遂には全沈積粒子を循環流動さ
せることができる。
Now, if the blowing of air from the air introduction pipe 9 is stopped for some reason, the granular solids 3 in the tank 4 will be deposited on the bottom of the tank as shown in the first figure, and the lower end of the air lift pipe 8 and the air lift pipe 8 will be deposited. The space between the tank and the tank wall is blocked. In order to circulate and flow the deposited granular solids 3 again, the entire air lift tube 8 must be lifted upwards under the water surface, or the lifting tube 8'' in the illustrated example can be pulled up to remove the deposited granular solids 3 from the lower end of the air lift tube 8. Set it at a position where there is an appropriate distance between the air introduction pipe 9 and the interface.
When air is blown in, particles near the interface circulate inside and outside the air lift tube 8 due to the water flow generated near the interface. Therefore, by gradually lowering the lower end of the air lift tube 8, more and more of the deposited particles will be sucked into the air lift tube 8 and circulated, eventually making it possible to circulate and flow all the deposited particles.

なお、第1図に示すように、槽4底部付近に起
動用散水管13を付設して、これからの起動水吹
込みを併用すれば、一層短時間で効果的な起動を
達成することができる。
In addition, as shown in Fig. 1, if a starting water pipe 13 is attached near the bottom of the tank 4 and used in conjunction with the future starting water injection, effective starting can be achieved in a shorter time. .

以上述べたように本考案によれば、エアリフト
管の下端を昇降可能たらしめた簡単な構造によつ
て、流動床生物処理装置の起動を容易、確実に行
うことができ、起動水を節減し、効率よくかつ信
頼性の高い運転を可能にすることができるもので
ある。
As described above, according to the present invention, the simple structure in which the lower end of the air lift tube can be raised and lowered allows the fluidized bed biological treatment equipment to be started easily and reliably, thereby saving startup water. , which enables efficient and reliable operation.

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

第1図は本考案の一実施例を示す縦断面図で、
第2図はエアリフト管下端部の一例を示す斜視図
である。 1……原水流入管、2……流出管、3……粒状
固体、4……槽、5……隔壁、6……循環部、7
……分離部、8……エアリフト管、8′………固
定管、8″……昇降管、9……空気導入管、12
……可撓管、13……起動水散水管。
FIG. 1 is a longitudinal sectional view showing an embodiment of the present invention.
FIG. 2 is a perspective view showing an example of the lower end of the air lift tube. DESCRIPTION OF SYMBOLS 1... Raw water inflow pipe, 2... Outflow pipe, 3... Granular solid, 4... Tank, 5... Partition wall, 6... Circulation part, 7
... Separation section, 8 ... Air lift pipe, 8' ... Fixed pipe, 8'' ... Lifting pipe, 9 ... Air introduction pipe, 12
... Flexible pipe, 13 ... Starting water sprinkler pipe.

Claims (1)

【実用新案登録請求の範囲】 1 原水流入部及び処理水流出部を有しかつ微生
物付着用の粒状固体を収容した槽内に、上端が
水面上で下端が槽底より離隔した隔壁にて循環
部と分離部とを区画形成し、前記循環部内に上
端が水面下で下端がほぼ槽底付近にあり、かつ
下端付近に空気導入管を連結したエアリフト管
を配備した流動床生物処理装置であつて、前記
エアリフト管の少なくとも下端を昇降可能たら
しめたことを特徴とする流動床生物処理装置。 2 前記エアリフト管を二重構造として互に摺動
可能たらしめたものである実用新案登録請求の
範囲第1項記載の流動床生物処理装置。
[Scope of Claim for Utility Model Registration] 1. In a tank having a raw water inlet and a treated water outlet and containing granular solids for adhesion of microorganisms, circulation is carried out through a partition whose upper end is above the water surface and whose lower end is separated from the bottom of the tank. The fluidized bed biological treatment apparatus is provided with an air lift pipe having an upper end below the water surface and a lower end substantially near the bottom of the tank, and an air inlet pipe connected to the lower end near the lower end. A fluidized bed biological treatment apparatus characterized in that at least the lower end of the air lift tube is movable up and down. 2. The fluidized bed biological treatment apparatus according to claim 1, wherein the air lift tube has a double structure and is slidable relative to each other.
JP1983194910U 1983-12-20 1983-12-20 Fluidized bed biological treatment equipment Granted JPS60104293U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1983194910U JPS60104293U (en) 1983-12-20 1983-12-20 Fluidized bed biological treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1983194910U JPS60104293U (en) 1983-12-20 1983-12-20 Fluidized bed biological treatment equipment

Publications (2)

Publication Number Publication Date
JPS60104293U JPS60104293U (en) 1985-07-16
JPH0128867Y2 true JPH0128867Y2 (en) 1989-09-01

Family

ID=30418794

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1983194910U Granted JPS60104293U (en) 1983-12-20 1983-12-20 Fluidized bed biological treatment equipment

Country Status (1)

Country Link
JP (1) JPS60104293U (en)

Also Published As

Publication number Publication date
JPS60104293U (en) 1985-07-16

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