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JPH10128359A - Waste water treatment apparatus - Google Patents

Waste water treatment apparatus

Info

Publication number
JPH10128359A
JPH10128359A JP29382896A JP29382896A JPH10128359A JP H10128359 A JPH10128359 A JP H10128359A JP 29382896 A JP29382896 A JP 29382896A JP 29382896 A JP29382896 A JP 29382896A JP H10128359 A JPH10128359 A JP H10128359A
Authority
JP
Japan
Prior art keywords
carrier
aerobic
treatment
floating
tank
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.)
Granted
Application number
JP29382896A
Other languages
Japanese (ja)
Other versions
JP3688829B2 (en
Inventor
Tatsuhiko Suzuki
辰彦 鈴木
Susumu Ishikawa
進 石川
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.)
Maezawa Industries Inc
Original Assignee
Maezawa Industries Inc
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 Maezawa Industries Inc filed Critical Maezawa Industries Inc
Priority to JP29382896A priority Critical patent/JP3688829B2/en
Publication of JPH10128359A publication Critical patent/JPH10128359A/en
Application granted granted Critical
Publication of JP3688829B2 publication Critical patent/JP3688829B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PROBLEM TO BE SOLVED: To enhance nitration and denitrification efficiency while making use of characteristics of a compact fixed bed high in treatment capacity by filling the lower part of a waste water treatment tank with a fixed carrier and charging a floating carrier in water of the upper part of the tank above the fixed carrier. SOLUTION: An aerobic filter bed 10 being a fixed bed has the filter material packed part 12 of a tank lower part packed with a filter material 11 being a fixed carrier such as lightweight aggregate or anthracite and a carrier floating part 13 wherein a floating carrier A is charged in the water of a tank upper part above the filter material packed part 12. Raw water flowing in the aerobic filter bed 10 from a raw water inflow pipe 14 is subjected to nitration treatment in the carrier floating part 13 and subjected to aerobic treatment and filtering treatment in the filter material packed part 12 to be discharged from a treated water discharge part 21. At this time, air is continuously introduced for an air diffusion pipe 19 to hold the interior of the aerobic filter bed 10 to a printing aerobic state not only to certainly perform aerobic treatment in the filter material packed part 12 but also to stably grow a large amt. of nitrifying bacteria in the carrier floating part 13.

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】本発明は、排水処理装置に関
し、詳しくは、好気状態,微好気状態あるいは嫌気状態
で排水処理を行う固定床を有する排水処理装置に関す
る。
The present invention relates to a wastewater treatment apparatus, and more particularly to a wastewater treatment apparatus having a fixed floor for performing wastewater treatment in an aerobic state, a microaerobic state, or an anaerobic state.

【0002】[0002]

【従来の技術】固定床による排水処理法、特に好気性ろ
床法は、コンパクトであり、維持管理が容易なことか
ら、小規模な下排水処理施設に用いられることが多くな
っている。好気性ろ床法で使用するろ床(好気性ろ床)
として、従来は、アンスラサイト等のろ材(固定担体)
のみを充填した単床式が一般的であるが、ろ床の洗浄を
考慮すると、ろ材の充填高さは2m程度が限界であり、
上部を有効に活用することができなかった。
2. Description of the Related Art A fixed-bed wastewater treatment method, particularly an aerobic filter bed method, is often used in small-scale sewage treatment facilities because of its compactness and easy maintenance. Filter bed used in the aerobic filter method (aerobic filter bed)
Conventionally, filter media such as anthracite (fixed carrier)
A single bed type is generally used, but the height of the filter medium is limited to about 2 m in consideration of washing the filter bed.
The upper part could not be used effectively.

【0003】この点を改善したのが、図3に示す2床式
の好気性ろ床1である。この2床式の好気性ろ床1は、
アンスラサイト等のろ材2の上方に、空隙率の大きいプ
ラスチック製接触材3を充填したものであって、このプ
ラスチック製接触材3に微生物を保持させることによ
り、同じ設置面積のろ床内に多くの微生物を保持し、処
理効率を向上させるようにしている。
An improvement in this point is a two-bed aerobic filter bed 1 shown in FIG. This two-bed aerobic filter 1
A plastic contact material 3 having a high porosity is filled above a filter material 2 such as anthracite. By allowing the plastic contact material 3 to hold microorganisms, the plastic contact material 3 has a large amount in a filter bed having the same installation area. Of microorganisms to improve processing efficiency.

【0004】一方、最近は、比較的小規模な下排水処理
施設でも、窒素の除去を求められる場合が多くなり、維
持管理が容易なことから、嫌気好気ろ床法による窒素除
去が行われるようになってきている。
On the other hand, recently, even in relatively small-scale sewage treatment facilities, nitrogen removal is required in many cases, and maintenance is easy. Therefore, nitrogen removal is performed by an anaerobic aerobic filter method. It is becoming.

【0005】[0005]

【発明が解決しようとする課題】しかし、従来のろ床、
特に好気性ろ床は、流入水の汚濁物質の内、主にSS成
分,BOD成分の除去を目的としているので、十分な窒
素除去(硝化)を行うためには、処理水量を低く抑える
必要があった。2床式とすることによってある程度硝化
速度を向上させることは可能なものの、BOD酸化細菌
と硝化菌とが競合関係となるため、硝化菌を安定して多
量に成育させることは困難であった。したがって、通水
速度を10〜20m3 /m2 /日程度にしなければなら
ず、BOD除去のための好気性ろ床と比較すると約2倍
の施設容量を必要とする。
However, conventional filter beds,
In particular, the aerobic filter bed is intended to mainly remove the SS and BOD components of the pollutants in the inflow water. Therefore, in order to sufficiently remove nitrogen (nitrification), it is necessary to reduce the amount of treated water. there were. Although the nitrification rate can be improved to some extent by using a two-bed system, it is difficult to stably grow the nitrifying bacteria in large quantities because the BOD oxidizing bacteria and the nitrifying bacteria are in a competitive relationship. Therefore, the water flow rate must be about 10 to 20 m 3 / m 2 / day, which requires about twice the facility capacity as compared with the aerobic filter for removing BOD.

【0006】一方、近年、硝化菌を包括固定した担体を
使用したり、硝化菌が付着し易い担体を使用したりする
ことによって硝化能力を高め、比較的短時間で硝化脱窒
を行うことができる浮遊法が開発されている。
On the other hand, in recent years, it has been possible to increase the nitrification capacity by using a carrier entrapping and fixing nitrifying bacteria or using a carrier to which nitrifying bacteria are easily attached, and to perform nitrification denitrification in a relatively short time. A possible flotation method has been developed.

【0007】そこで本発明は、コンパクトで処理能力の
高い固定床の特性を活かしつつ、硝化脱窒効率を向上さ
せることができるろ床式の排水処理装置を提供すること
を目的としている。
Accordingly, an object of the present invention is to provide a filter bed type wastewater treatment apparatus capable of improving the nitrification and denitrification efficiency while utilizing the characteristics of a compact fixed bed having a high treatment capacity.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するた
め、本発明の排水処理装置は、排水処理槽の下部に固定
担体を充填し、該固定担体より上方の槽上部の水中に浮
遊担体を投入したことを特徴とするものであって、特
に、嫌気好気ろ床法により排水処理を行う好気性ろ床の
下部にろ過機能を有する固定担体を充填し、該固定担体
より上方の槽上部の水中に、硝化菌を包括固定した浮遊
担体あるいは硝化菌が付着し易い浮遊担体を投入したこ
とを特徴としている。
In order to achieve the above object, a wastewater treatment apparatus according to the present invention fills a lower part of a wastewater treatment tank with a fixed carrier and disposes a floating carrier in water in an upper part of the tank above the fixed carrier. In particular, the lower part of the aerobic filter bed which performs wastewater treatment by the anaerobic aerobic filter method is filled with a fixed carrier having a filtration function, and the upper part of the tank above the fixed carrier is introduced. The present invention is characterized in that a floating carrier entrapping and fixing nitrifying bacteria or a floating carrier to which nitrifying bacteria easily adhere is put into water.

【0009】[0009]

【発明の実施の形態】以下、本発明を、図面を参照して
さらに詳細に説明する。図1は、本発明の排水処理装置
の一例を示すもので、固定床である好気性ろ床に応用し
た例を示している。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail with reference to the drawings. FIG. 1 shows an example of a wastewater treatment apparatus according to the present invention, and shows an example in which the present invention is applied to an aerobic filter bed which is a fixed bed.

【0010】この好気性ろ床10は、従来と同様の軽量
骨材やアンスラサイト等の固定担体であるろ材11を充
填した槽下部のろ材充填部12と、ろ材充填部12より
上方の槽上部の水中に浮遊担体Aを投入した担体浮遊部
13とを有するもので、担体浮遊部13の上方には原水
流入管14が、担体浮遊部13の下部には担体流出防止
用のウェッジワイヤースクリーン15を備えた洗浄排水
排出管16がそれぞれ設けられ、ろ材充填部12の下方
のろ材支持層17内にはコンプレッサー18に接続した
散気管19が、槽底部の集水ノズル20の下方には処理
水排出管21がそれぞれ設けられている。
The aerobic filter bed 10 comprises a filter medium filling section 12 at the lower part of the tank filled with a filter medium 11 as a fixed carrier such as a lightweight aggregate or anthracite, and a tank upper part above the filter medium filling part 12 as in the prior art. A raw water inflow pipe 14 above the carrier floating part 13 and a wedge wire screen 15 for preventing carrier outflow below the carrier floating part 13. A drainage pipe 16 connected to a compressor 18 is provided in a filter medium support layer 17 below the filter medium filling section 12, and treated water is provided below a water collection nozzle 20 at the bottom of the tank. Discharge pipes 21 are provided respectively.

【0011】前記浮遊担体Aとしては、硝化菌を包括固
定した担体や、硝化菌の付着しやすい担体を用いてお
り、原水流入管14から好気性ろ床10内に流入した原
水は、担体浮遊部13で浮遊担体Aと接触し、浮遊担体
Aに担持された硝化菌により硝化処理される。
As the floating carrier A, a carrier entrapping and fixing nitrifying bacteria or a carrier to which nitrifying bacteria easily adhere is used. Raw water flowing into the aerobic filter bed 10 from the raw water inflow pipe 14 is used as the floating carrier A. The part 13 comes into contact with the floating carrier A and is subjected to nitrification treatment by the nitrifying bacteria carried on the floating carrier A.

【0012】すなわち、原水流入管14から好気性ろ床
10内に流入した原水は、担体浮遊部13で硝化処理さ
れ、ろ材充填部12で好気性処理及びろ過処理された
後、処理水排出管21から排出される。
That is, the raw water flowing into the aerobic filter bed 10 from the raw water inflow pipe 14 is subjected to nitrification treatment in the carrier floating part 13, aerobic treatment and filtration treatment in the filter material filling part 12, and then to the treated water discharge pipe. It is discharged from 21.

【0013】このとき、前記散気管19から空気を連続
的に導入して好気性ろ床10内を所定の好気状態に維持
することにより、ろ材充填部12における好気処理(B
OD除去等)を確実に行えるとともに、担体浮遊部13
において硝化菌を安定して多量に成育させることができ
るので、比較的短時間で硝化処理を行うことができる。
すなわち、好気性ろ床10の上部に硝化菌を保持した担
体を浮遊させて硝化処理を行うことにより、通水抵抗を
増加させることなく、高い処理効率で硝化を行うことが
可能となる。さらに、洗浄排水排出管16にウェッジワ
イヤースクリーン15を設けたことにより、ろ材11を
洗浄する際の洗浄排水と共に浮遊担体Aやろ材11が流
出することを防止できる。
At this time, air is continuously introduced from the air diffuser tube 19 to maintain the inside of the aerobic filter bed 10 in a predetermined aerobic state, so that the aerobic treatment (B
OD removal, etc.), and the carrier floating portion 13
Therefore, the nitrifying bacteria can be grown stably in a large amount, and thus the nitrification treatment can be performed in a relatively short time.
That is, by performing the nitrification treatment by suspending the carrier holding the nitrifying bacteria on the upper part of the aerobic filter bed 10, the nitrification can be performed with high treatment efficiency without increasing the water flow resistance. Further, the provision of the wedge wire screen 15 in the washing drainage pipe 16 can prevent the floating carrier A and the filter medium 11 from flowing out together with the washing wastewater when the filter medium 11 is washed.

【0014】なお、槽下部のろ材充填部12や散気管1
9,集水ノズル20等は、従来の好気性ろ床と同様の構
造を採用することができるので、これらの詳細な説明は
省略する。
The filter medium filling section 12 and the diffuser 1 at the bottom of the tank are provided.
9, the water collecting nozzle 20 and the like can adopt the same structure as a conventional aerobic filter bed, and therefore, detailed description thereof will be omitted.

【0015】図2は、上述の好気性ろ床を、嫌気好気ろ
床法に適用した一例を示すもので、処理原水の流れの上
流側から、スクリーン30aを有する原水槽30,原水
及び洗浄排水を貯留する洗浄排水槽31,嫌気性ろ床3
2,加圧浮上分離装置33,好気性ろ床34,処理水槽
35の順に配列したものであって、流入原水は、原水槽
30から洗浄排水槽31を経て嫌気性ろ床32に供給さ
れ、この嫌気性ろ床32で嫌気処理された後、加圧浮上
分離装置33で浮上処理され、さらに、好気性ろ床34
で好気処理された後、処理水槽35に送られる。
FIG. 2 shows an example in which the above-described aerobic filter is applied to the anaerobic filter method. The raw water tank 30 having the screen 30a, the raw water and the washing are arranged from the upstream side of the flow of the treated raw water. Cleaning drainage tank 31 for storing wastewater, anaerobic filter bed 3
2, a pressurized flotation device 33, an aerobic filter bed 34, and a treated water tank 35 are arranged in this order, and the inflowing raw water is supplied from the raw water tank 30 to the anaerobic filter bed 32 via the washing / draining tank 31; After being subjected to anaerobic treatment in this anaerobic filter bed 32, it is subjected to levitation treatment in a pressure flotation / separation device 33, and further subjected to an aerobic filter bed 34.
After being subjected to aerobic treatment in, the water is sent to the treated water tank 35.

【0016】嫌気性ろ床32は、下部が汚泥の沈殿部
で、上部に接触材を充填した形式のものであって、洗浄
排水槽31からの流入原水は、好気性ろ床34の中段か
ら抜出されて配管36を介して循環する硝化液と共に、
嫌気性ろ床32の下部に沈殿している汚泥を撹拌するよ
うに供給される。この嫌気性ろ床32では、主に、脱窒
及び有機物の嫌気的分解が行われる。また、この嫌気性
ろ床32は、原則として汚泥の引抜き及びろ床の洗浄は
行わず、汚泥をできるだけ長くろ床内に保持することに
より、汚泥の分解を促進して減量化を図ることができ
る。また、この嫌気性ろ床32には、ろ床内が過度の嫌
気状態になるのを防止するための散気装置32aが設け
られている。
The anaerobic filter bed 32 is of a type in which the lower part is a sludge sedimentation section and the upper part is filled with a contact material. Along with the nitrified liquid that is extracted and circulated through the pipe 36,
The sludge settled in the lower part of the anaerobic filter bed 32 is supplied so as to be stirred. In the anaerobic filter bed 32, denitrification and anaerobic decomposition of organic substances are mainly performed. In addition, in this anaerobic filter bed 32, sludge is not pulled out and the filter bed is not washed in principle, and the sludge is retained in the filter bed as long as possible, thereby promoting the decomposition of sludge and reducing the amount of sludge. it can. The anaerobic filter bed 32 is provided with a diffuser 32a for preventing the inside of the filter bed from becoming excessively anaerobic.

【0017】嫌気性ろ床32で処理された水は、リーク
する汚泥も含めて加圧浮上分離装置33に送られ、配管
37から供給される加圧空気混合水と混合されて槽内に
流入する。水中の懸濁成分は、加圧空気混合水から発生
する微細気泡の作用によって槽上部に浮上汚泥(フロ
ス)として浮上し、掻取機33aにより掻取られて汚泥
貯留槽38に送られる。
The water treated by the anaerobic filter bed 32, including the sludge that leaks, is sent to the pressurized flotation device 33, mixed with the pressurized air mixed water supplied from the pipe 37, and flows into the tank. I do. The suspended component in the water floats on the upper portion of the tank as floating sludge (floss) by the action of fine bubbles generated from the pressurized air mixed water, is scraped by the scraper 33a, and is sent to the sludge storage tank 38.

【0018】加圧浮上分離装置33で浮上処理された水
は、前述のように硝化菌を保持した担体が浮遊する担体
浮遊部13を有する好気性ろ床34に原水流入管14を
介して送られる。この好気性ろ床34では、上部の担体
浮遊部13で硝化処理された水(硝化液)の一部が、担
体浮遊部13の下部からウェッジワイヤースクリーン1
5を介して洗浄排水排出管16に抜き取られ、ポンプ3
6Pにより配管36に抜出されて嫌気性ろ床32に循環
し、下部のろ材充填部12で好気処理及びろ過処理され
た水が処理水排出管21から処理水槽35に送られる。
The water levitated by the pressurized flotation device 33 is sent via the raw water inflow pipe 14 to the aerobic filter bed 34 having the carrier floating part 13 in which the carrier holding nitrifying bacteria floats as described above. Can be In the aerobic filter bed 34, a part of the water (nitrified liquid) that has been nitrified in the upper carrier floating portion 13 is discharged from the lower portion of the carrier floating portion 13 to the wedge wire screen 1.
5 and drained to the washing drainage pipe 16 through the pump 3
The water that has been drawn out to the pipe 36 by the 6P and circulated to the anaerobic filter bed 32 is sent to the treated water tank 35 from the treated water discharge pipe 21 by the aerobic treatment and the filtration treatment in the lower filter material filling part 12.

【0019】また、好気性ろ床34で発生した汚泥は、
洗浄排水と共に洗浄排水排出管16及び配管39を介し
て洗浄排水槽31に戻し、原水と共に嫌気性ろ床32に
導入して減量化した後、加圧浮上分離装置33で処理す
るようにしている。したがって、通常の運転状態では、
汚泥の発生個所を加圧浮上分離装置33のみとすること
ができる。
The sludge generated in the aerobic filter bed 34 is:
The wastewater is returned to the washing drainage tank 31 via the washing drainage pipe 16 and the pipe 39 together with the washing wastewater, and introduced into the anaerobic filter bed 32 together with the raw water to reduce the volume. . Therefore, under normal operating conditions,
The place where sludge is generated can be only the pressure flotation device 33.

【0020】このように、嫌気性ろ床32,加圧浮上分
離装置33及び担体浮遊部13を有する好気性ろ床34
を組み合わせて嫌気好気処理を行うことにより、比較的
小規模な排水処理設備においても安定した状態で効率の
よい窒素除去を行うことができる。特に、加圧浮上分離
装置33を用いることにより、好気性ろ床34に送られ
る処理水の懸濁成分量を少なくすることができ、好気性
ろ床34の処理効率を向上させることができるととも
に、余剰汚泥の発生箇所を加圧浮上分離装置33に一本
化することができるので、汚泥の処理も容易になる。さ
らに、嫌気性ろ床32に散気装置32aを設けてろ床内
の嫌気度を調節することにより、安定した状態で確実に
嫌気処理を行うことができる。
As described above, the anaerobic filter bed 32, the pressurized flotation separator 33, and the aerobic filter 34 having the carrier floating section 13 are provided.
By performing anaerobic and aerobic treatment in combination with the above, efficient and efficient nitrogen removal can be performed even in a relatively small-scale wastewater treatment facility. In particular, by using the pressure flotation separator 33, the amount of suspended components of the treated water sent to the aerobic filter bed 34 can be reduced, and the treatment efficiency of the aerobic filter bed 34 can be improved. In addition, since the place where the excess sludge is generated can be unified into the pressure flotation / separation device 33, the treatment of the sludge becomes easy. Furthermore, by providing the air diffuser 32a to the anaerobic filter bed 32 and adjusting the anaerobic degree in the filter bed, anaerobic treatment can be performed reliably in a stable state.

【0021】なお、本発明の排水処理装置は、上述の各
形態例のように、好気性ろ床に適用するものに限らず、
微好気状態下や嫌気状態下で排水処理するものにも適用
でき、担体に保持させる菌類も、処理目的に応じて適宜
に選択することができる。また、嫌気好気処理における
設備構成も、上記形態例に限るものではない。
The wastewater treatment apparatus according to the present invention is not limited to the one applied to the aerobic filter bed as in the above embodiments,
The present invention can be applied to a wastewater treatment under a microaerobic condition or an anaerobic condition, and the fungi to be retained on the carrier can be appropriately selected according to the treatment purpose. Further, the equipment configuration in the anaerobic / aerobic treatment is not limited to the above embodiment.

【0022】[0022]

【発明の効果】以上説明したように、本発明の排水処理
装置によれば、好気状態,微好気状態あるいは嫌気状態
で排水処理を行う固定床の上部に浮遊担体を投入して排
水処理を行うようにしたので、処理効率を大幅に向上さ
せることができ、小規模な下排水処理施設においても高
度の処理を行うことが可能となる。
As described above, according to the wastewater treatment apparatus of the present invention, a floating carrier is put into the upper part of a fixed bed for performing wastewater treatment in an aerobic state, a microaerobic state or an anaerobic state. Therefore, the treatment efficiency can be greatly improved, and it is possible to perform advanced treatment even in a small-scale sewage treatment facility.

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

【図1】 本発明を適用した好気性ろ床の一例を示す説
明図である。
FIG. 1 is an explanatory diagram showing an example of an aerobic filter bed to which the present invention has been applied.

【図2】 本発明を嫌気好気ろ床法の好気性ろ床に適用
した例を示す系統図である。
FIG. 2 is a system diagram showing an example in which the present invention is applied to an aerobic filter using an anaerobic filter method.

【図3】 従来の好気性ろ床の一例を示す説明図であ
る。
FIG. 3 is an explanatory view showing an example of a conventional aerobic filter bed.

【符号の説明】[Explanation of symbols]

10…好気性ろ床、11…ろ材、12…ろ材充填部、1
3…担体浮遊部、14…原水流入管、15…ウェッジワ
イヤースクリーン、16…洗浄排水排出管、17…ろ材
支持層、18…コンプレッサー、19…散気管、20…
集水ノズル、21…処理水排出管、30…原水槽、31
…洗浄排水槽、32…嫌気性ろ床、33…加圧浮上分離
装置、34…好気性ろ床、35…処理水槽、38…汚泥
貯留槽、A…浮遊担体
10: aerobic filter bed, 11: filter medium, 12: filter medium filling section, 1
3 ... Carrier floating part, 14 ... raw water inflow pipe, 15 ... wedge wire screen, 16 ... wash drainage pipe, 17 ... filter medium support layer, 18 ... compressor, 19 ... aeration pipe, 20 ...
Water collecting nozzle, 21: treated water discharge pipe, 30: raw water tank, 31
... Washing drainage tank, 32 ... Anaerobic filter bed, 33 ... Pressurized flotation separator, 34 ... Aerobic filter bed, 35 ... Treatment tank, 38 ... Sludge storage tank, A ... Floating carrier

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 排水処理槽の下部に固定担体を充填し、
該固定担体より上方の槽上部の水中に浮遊担体を投入し
たことを特徴とする排水処理装置。
1. A fixed carrier is filled in a lower portion of a wastewater treatment tank,
A wastewater treatment apparatus, wherein a floating carrier is charged into water in an upper part of a tank above the fixed carrier.
【請求項2】 好気性排水処理を行う排水処理槽の下部
にろ過機能を有する固定担体を充填し、該固定担体より
上方の槽上部の水中に浮遊担体を投入したことを特徴と
する排水処理装置。
2. A wastewater treatment wherein a lower part of a wastewater treatment tank for performing aerobic wastewater treatment is filled with a fixed carrier having a filtering function, and a floating carrier is introduced into water in an upper part of the tank above the fixed carrier. apparatus.
【請求項3】 前記排水処理槽は、嫌気好気ろ床法によ
り排水処理を行う好気性ろ床であることを特徴とする請
求項2記載の排水処理装置。
3. The wastewater treatment apparatus according to claim 2, wherein the wastewater treatment tank is an aerobic filter bed that performs wastewater treatment by an anaerobic aerobic filter method.
【請求項4】 前記浮遊担体は、硝化菌を包括固定した
担体あるいは硝化菌が付着し易い担体であることを特徴
とする請求項2記載の排水処理装置。
4. The wastewater treatment apparatus according to claim 2, wherein the floating carrier is a carrier entrapping and fixing nitrifying bacteria or a carrier to which nitrifying bacteria easily adhere.
JP29382896A 1996-11-06 1996-11-06 Wastewater treatment equipment Expired - Fee Related JP3688829B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29382896A JP3688829B2 (en) 1996-11-06 1996-11-06 Wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29382896A JP3688829B2 (en) 1996-11-06 1996-11-06 Wastewater treatment equipment

Publications (2)

Publication Number Publication Date
JPH10128359A true JPH10128359A (en) 1998-05-19
JP3688829B2 JP3688829B2 (en) 2005-08-31

Family

ID=17799693

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29382896A Expired - Fee Related JP3688829B2 (en) 1996-11-06 1996-11-06 Wastewater treatment equipment

Country Status (1)

Country Link
JP (1) JP3688829B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2508488A1 (en) * 2011-04-04 2012-10-10 Veolia Water Solutions & Technologies Support Improved biological waste water purification reactor and method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2508488A1 (en) * 2011-04-04 2012-10-10 Veolia Water Solutions & Technologies Support Improved biological waste water purification reactor and method
WO2012136654A1 (en) * 2011-04-04 2012-10-11 Veolia Water Solutions & Technologies Support Improved biological waste water purification reactor and method
CN103547535A (en) * 2011-04-04 2014-01-29 威立雅水务解决方案与技术支持公司 Improved biological waste water purification reactor and method

Also Published As

Publication number Publication date
JP3688829B2 (en) 2005-08-31

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