JPS61192390A - Semi-fluidized bed type water treatment apparatus - Google Patents

Semi-fluidized bed type water treatment apparatus

Info

Publication number
JPS61192390A
JPS61192390A JP60034146A JP3414685A JPS61192390A JP S61192390 A JPS61192390 A JP S61192390A JP 60034146 A JP60034146 A JP 60034146A JP 3414685 A JP3414685 A JP 3414685A JP S61192390 A JPS61192390 A JP S61192390A
Authority
JP
Japan
Prior art keywords
fluidized bed
pipe
tank
air lift
treatment
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
JP60034146A
Other languages
Japanese (ja)
Other versions
JPH0225675B2 (en
Inventor
Hideki Iwabe
岩部 秀樹
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP60034146A priority Critical patent/JPS61192390A/en
Publication of JPS61192390A publication Critical patent/JPS61192390A/en
Publication of JPH0225675B2 publication Critical patent/JPH0225675B2/ja
Granted 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 enable continuous treatment by preventing clogging, by vertically providing an air lift pipe, into which air is sent, to the central part of a semi- fluidized bed type treatment tank and communicating a carrier particle introducing pipe to the lower end opening of the air lift pipe. CONSTITUTION:Raw water flowed in from a raw water supply pipe 4 is dispersed throughout the entire lower region of a tank from a porous dispersing plate 3 and rises between carrier particles to be flowed out from the apertures 15a of a press plate 15. At this time, carrier particles 14 are fluidized by the flow of raw water and a fixed bed part (a) is formed to the lower side of the press plate 15. A fluidized bed part (b) is formed below the fixed bed part (a) so as to reach the porous dispersing plate 3 and raw water receives treatment due to bacteria during passage through both beds (a), (b) while treated water rises through the apertures 15a of the press plate 15 and passes through a treated water sump 16 from a treated water outflow pipe 17 to be discharged out of the tank.

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、担体粒子の自動洗浄機構を備えた半流動層式
廃水処理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a semi-fluidized bed wastewater treatment apparatus equipped with an automatic cleaning mechanism for carrier particles.

「従来の技術」 廃水の微生物による処理において、下部が流動化され上
部が鋳止している微粒状の担体粒子の層を形成した半流
動層式廃水処理装置を使用することは知られている。こ
の半流動層による処理は、流動層部と固定層部とを併せ
もっことにより、流動層部での完全混合による高速処理
と固定層部での密な微生物層による仕上げ処理との双方
の長所が得られ、槽学位容積当りの微生物濃度を高める
ことかでき、高速処理とともに処理槽の小型化が可能と
なる、という利点がある。
"Prior Art" It is known to use a semi-fluidized bed wastewater treatment device in which a layer of fine carrier particles is formed, the lower part of which is fluidized and the upper part of which is cast, in the treatment of wastewater with microorganisms. . By combining a fluidized bed section and a fixed bed section, this semi-fluidized bed treatment has the advantages of both high speed processing due to complete mixing in the fluidized bed section and finishing treatment using a dense microbial layer in the fixed bed section. This method has the advantage of increasing the microbial concentration per tank volume, allowing high-speed processing, and downsizing of the processing tank.

しかし、この半流動層式の処理においては、処理が進む
につれて廃水中の浮遊物質或は担体粒子から剥離した微
生物フロックなどにより固定層部が閉塞され、廃水処理
を一時中断し、しばしば洗浄処理をしなければならない
という難点がある。
However, in this semi-fluidized bed type treatment, as the treatment progresses, the fixed bed becomes clogged with suspended solids in the wastewater or microbial flocs detached from carrier particles, causing the wastewater treatment to be temporarily interrupted and cleaning treatment often required. The problem is that it has to be done.

このような難点を解決するため、固定層部を拘束する多
孔板を上下に移動自在に設け、固定層部が閉塞されるよ
うになると多孔板を上昇させて固定層部の流動化を図り
、閉塞の原因をなしている浮遊物質や微生物フロックな
どを多孔板の目を通して排出させるようにするという提
案がなされた(%開昭55−106594号公報、特公
昭59−32197号公報等参照)。
In order to solve this problem, we installed a perforated plate that restrains the fixed layer section so that it can move up and down, and when the fixed layer section becomes blocked, the perforated plate is raised to fluidize the fixed layer section. A proposal has been made to discharge suspended solids, microbial flocs, etc. that cause blockages through the holes of a perforated plate (see % JP-A-55-106594, Japanese Patent Publication No. 59-32197, etc.).

しかし、その方法においても、多孔板を上昇して固定層
部を流動化するクリーニングサイクル時には廃水処理を
中断して洗浄しなければならず、依然として従来の難膚
を解決するということには至っていない。
However, even with this method, during the cleaning cycle in which the perforated plate is raised to fluidize the fixed bed, wastewater treatment must be interrupted for cleaning, and the conventional difficulties have not yet been solved. .

「本考案が解決しようとする問題点」 前述した廃水の半流動層による処理における大きな問題
点は、処理槽内の流動層部や固定層部に目詰まりが生じ
ることなく廃水の連続処理が能率よく行えるようにする
ことにある。本発明はかかる問題点を解決するためにな
されたもので、廃水の処理中において、固定層部の担体
粒子を逐次洗浄して返送する機構を処理槽中に設けるこ
とにより、固定層部の目詰りを防ぎつつ廃水の連続処理
を可能とし、廃水の微生物学的処理を能率的に行えるよ
うにするとともに、操作や保守が容易な半流動層式廃水
処理装置を提供しようとするものである。
``Problems to be solved by the present invention'' The major problem with the semi-fluidized bed treatment of wastewater mentioned above is that continuous treatment of wastewater is efficient without clogging the fluidized bed or fixed bed in the treatment tank. The goal is to be able to perform well. The present invention has been made to solve this problem, and by providing a mechanism in the treatment tank to sequentially wash and return the carrier particles in the fixed bed during wastewater treatment, the present invention improves the visibility of the fixed bed. The present invention aims to provide a semi-fluidized bed wastewater treatment device that enables continuous treatment of wastewater while preventing clogging, enables efficient microbiological treatment of wastewater, and is easy to operate and maintain.

[問題点を解決するための手段1 流動層部とその上部に固定層部を形成してなる半流動層
式処理槽の中心部に、気体の送入されるエアリフト管を
立設し、該エアリフト管の下端開口に、上端が固定層部
内に開口した担体粒子導入管を連通させるとともに、前
記エアリフト管の上端には、これより流出する担体を流
動層部に返送するとともに、流出する洗浄汚水を槽外へ
排出する手段を設けたことを特徴とするものである。
[Means for solving the problem 1: An airlift pipe through which gas is introduced is installed upright in the center of a semi-fluidized bed treatment tank consisting of a fluidized bed section and a fixed bed section above the fluidized bed section. A carrier particle introduction pipe whose upper end opens into the fixed bed section is connected to the lower end opening of the air lift pipe, and the carrier particles flowing out from the pipe are returned to the fluidized bed section, and the washed wastewater flowing out is connected to the upper end of the air lift pipe. This is characterized by providing a means for discharging the water out of the tank.

「実施例」 以下、本発明装置の実施例について図面を参照して説明
する。
"Embodiments" Hereinafter, embodiments of the apparatus of the present invention will be described with reference to the drawings.

図において1は上下方向に長く形成した処理槽で、その
下部には槽底2と所要の間隔を存して多孔分散板3が設
けられており、それらの間には原水供給管4が接続され
ている。また、処理槽1の中心部には、上下端が多孔分
散板3と天板5との間にそれぞれ所要の間隔をおいて開
口したエア1]フト管6が立設されており、エアリフト
管6の下端部には送気管7が突入している。この送気管
には天板5を通して処理槽の上端部内に連通した排ガス
管8がブロワ−9を介して接続されている。そして、処
理槽1の上部にはエアリフト管6の上部を囲んで分離筒
10が設けられており、その外側には、槽1外に設けた
排水溜12に至る排水管13を接続した排水越流室11
が設けられている。
In the figure, 1 is a treatment tank formed long in the vertical direction, and a porous distribution plate 3 is provided at the bottom of the tank at a required distance from the tank bottom 2, and a raw water supply pipe 4 is connected between them. has been done. Further, in the center of the processing tank 1, an air lift pipe 6 is installed, the upper and lower ends of which are opened at a required interval between the porous dispersion plate 3 and the top plate 5, respectively. An air supply pipe 7 protrudes into the lower end of the pipe 6. An exhaust gas pipe 8 communicating with the upper end of the processing tank through the top plate 5 is connected to this air supply pipe via a blower 9. A separation tube 10 is provided in the upper part of the treatment tank 1 to surround the upper part of the air lift pipe 6, and on the outside of the separation tube 10, a drainage pipe 13 leading to a drainage sump 12 provided outside the tank 1 is connected. Flow chamber 11
is provided.

処理槽1上部の槽壁と排水越流室11との間には槽1内
に収容された担体粒子14の流動を規制する抑え板15
が設けられ、これには担体粒子14より小径とした多数
の孔15 m 、15aが設けられており、その上部に
は処理槽1の外側に設けられた処理水溜16に至る処理
水流出管17が接続されている。
Between the tank wall at the top of the treatment tank 1 and the wastewater overflow chamber 11, there is a restraining plate 15 for regulating the flow of carrier particles 14 housed in the tank 1.
is provided with a large number of holes 15 m and 15a having a diameter smaller than that of the carrier particles 14, and a treated water outflow pipe 17 leading to a treated water reservoir 16 provided on the outside of the treatment tank 1 is provided above the hole. is connected.

きた、エアリフト管6の外側には、上端を抑え板15の
下方位置に開口18aさせるとともに、下端がエアリフ
ト管6の下端より下方に位置して底板により閉じられた
担体粒子導入管18が設けられ、その下端はエア1]フ
ト管6の下端と連通されている。そして、分離筒10の
下端には、担体粒子14の返送管19が導入管18の外
側を囲んで下方に延び、下端を処理槽1の下部に開口し
て設けられ、エア1】フト管6より流出した担体粒子1
4がこの返送管19内を流下して処理槽1の下部へ返送
されるようになっている。
On the outside of the air lift tube 6, there is provided a carrier particle introduction tube 18 whose upper end has an opening 18a located below the restraining plate 15, and whose lower end is located below the lower end of the air lift tube 6 and is closed by a bottom plate. , its lower end communicates with the lower end of the air 1/ft pipe 6. A return pipe 19 for the carrier particles 14 is provided at the lower end of the separation cylinder 10 so as to surround the outside of the introduction pipe 18, extend downward, and open its lower end to the lower part of the processing tank 1. Carrier particles 1 that flowed out
4 flows down in this return pipe 19 and is returned to the lower part of the processing tank 1.

なお、図中20は処理水の一部をポンプ21により処理
槽底部に供給するために設けられた循環管路である。
Note that 20 in the figure is a circulation pipe provided for supplying a portion of the treated water to the bottom of the treatment tank by a pump 21.

「作用」 前記構成の処理装置において、処理槽1内へは担体粒子
14が、従来の半流動処理槽におけると同様に収容され
る。この場合、担体粒子は比重差が若干ある2種類のも
のを使用するのがよい。原水供給管4より流入した原水
は、多孔分散板3より槽の下部全域分散され、担体粒子
間を上昇して抑え板15の孔15aより流出される。そ
の際、原水の流れによって担体粒子14は流動化し、担
体粒子14のうち軽いものは上昇して抑え版15により
流動化が抑制され、したがって、抑え板15の下側には
固定層部aが形成され、その固定層部aの下側には多孔
分散板3までの間に流動層部すが形成されることになり
、原水はそれらの各要部a、bを通る間に微生物による
処理をうけ、その処理水は抑え板15の孔15aを通っ
て上昇し、処理水流出管17より処理水溜16を通って
槽外に排出22されることになる。
"Operation" In the processing apparatus configured as described above, carrier particles 14 are accommodated in the processing tank 1 in the same manner as in a conventional semi-fluid processing tank. In this case, it is preferable to use two types of carrier particles with a slight difference in specific gravity. The raw water flowing in from the raw water supply pipe 4 is dispersed throughout the lower part of the tank by the porous dispersion plate 3, rises between the carrier particles, and flows out through the holes 15a of the restraining plate 15. At this time, the carrier particles 14 are fluidized by the flow of raw water, and the lighter ones of the carrier particles 14 rise, and the fluidization is suppressed by the holding plate 15. Therefore, a fixed layer portion a is formed below the holding plate 15. A fluidized bed section is formed below the fixed layer section a up to the porous dispersion plate 3, and the raw water is treated by microorganisms while passing through each of these main sections a and b. The treated water rises through the hole 15a of the holding plate 15, passes through the treated water reservoir 16 from the treated water outflow pipe 17, and is discharged 22 to the outside of the tank.

この原水処理により、原水中の汚濁物や生長した生物膜
或は脱落した生物膜は、次第に固定層部aに堆積して担
体粒子14間に目詰りが生じてくることとなることは、
従来処理槽におけると同様であるが、この処理中におい
て、送気管を介してエアリフト管6に気体を注入する。
Due to this raw water treatment, pollutants in the raw water and biofilms that have grown or fallen off will gradually accumulate on the fixed layer part a, causing clogging between the carrier particles 14.
As in the conventional processing tank, during this processing, gas is injected into the air lift pipe 6 via the air supply pipe.

実施例図のように、処理槽1を天板5で密閉した嫌気性
処理を行う方法のものにおいては、生物学的処理により
発生した消化ガス(メタン醗酵ガス)の一部をプロワ−
9により還流してエア1】フト管6へ注入するようにす
るが、好気性処理を行う場合は外気を注入する。
As shown in the example diagram, in the method of performing anaerobic treatment in which the treatment tank 1 is sealed with a top plate 5, a part of the digestion gas (methane fermentation gas) generated by the biological treatment is transferred to the processor.
The air is refluxed through 9 and injected into the air pipe 6, but when performing aerobic treatment, outside air is injected.

エアリフト管6への気体の注入により、エアI】フト作
用が生じ、上端開口18aより入った固定層部aの担体
粒子14と汚水等は、エアリフト管6の下端に導入され
て同管内を上昇し、担体粒子14は洗浄作用を受けてそ
れに付着している汚濁物や生物膜フロック等は分離され
てエアリフト管6の上端より流出されることになる。こ
こで、比重の重い担体粒子は沈降して行き、返送管18
を通ってその下端から槽下部の流動層部すに戻されるこ
とになる。また、汚水や汚濁物等は排水越流室11より
オーバーフローして排水管15より排水溜12を逆って
排出23されることになる。
By injecting gas into the air lift tube 6, an air lift effect is generated, and the carrier particles 14 and waste water in the fixed layer part a that entered through the upper end opening 18a are introduced into the lower end of the air lift tube 6 and rise inside the tube. However, the carrier particles 14 are subjected to a cleaning action, and the pollutants, biofilm flocs, etc. adhering thereto are separated and flowed out from the upper end of the air lift tube 6. Here, the carrier particles with heavy specific gravity settle down, and the return pipe 18
It is returned to the fluidized bed section at the bottom of the tank from its lower end. In addition, sewage, pollutants, etc. overflow from the drainage overflow chamber 11 and are discharged 23 through the drainage pipe 15 through the drainage basin 12.

このようにして、固定層部a及び流動層部すにある担体
粒子や汚濁物等は、原水の処理中において、エアリフト
管6を上昇する際の洗浄作用で洗浄、分離され、洗浄さ
れた担体粒子は再び槽の下部に返却され、汚濁物等は゛
槽外に排出除去されることになり、原廃水の生物学的処
理と固定槽部a1流動層部すの担体粒子の洗浄と汚濁物
等の除去とが同時に行われるのである。
In this way, carrier particles, pollutants, etc. in the fixed bed section a and the fluidized bed section are washed and separated by the washing action when ascending through the air lift tube 6 during raw water treatment, and the washed carrier particles The particles are returned to the lower part of the tank, and the pollutants are discharged and removed outside the tank.Biological treatment of the raw wastewater, cleaning of carrier particles in the fixed tank section A1, fluidized bed section, and pollutants, etc. This is done at the same time.

「発明の効果」 以上説明したように、本発明の処理装置は、流動層部と
その上部に固定層部を形成してなる半流動層式処理槽の
中心部に、気体の送入されるエアリフト管を立設し、該
エアリフト管の下端開口に、上端が固定層部内に開口し
た担体粒子導入管を連通させるとともに、前記エアリフ
ト管の上端には、これより流出する担体を流動層部に返
送するとともに、流出する洗浄汚水を槽外へ排出する手
段を設けたので、廃水の処理を行うと同時に、特に目詰
りを発生し易い固定層部の洗浄と汚濁物等の分離、排出
を行うことができ、常に目詰りの生じないようにして連
続した廃水処理が可能となり、廃水の微生物学的処理の
能率を著しく向上させることができる。
"Effects of the Invention" As explained above, in the processing apparatus of the present invention, gas is introduced into the center of the semi-fluidized bed processing tank, which has a fluidized bed section and a fixed bed section formed above the fluidized bed section. An air lift tube is installed upright, and a carrier particle introduction tube whose upper end opens into the fixed bed section is communicated with the lower end opening of the air lift tube, and at the same time, the carrier particles flowing out from the air lift tube are connected to the fluidized bed section at the upper end of the air lift tube. In addition to returning the washed wastewater, we have also provided a means to discharge the washing wastewater out of the tank, so that at the same time we treat the wastewater, we also wash the fixed bed section, which is particularly prone to clogging, and separate and discharge pollutants. This enables continuous wastewater treatment without clogging, and the efficiency of microbiological treatment of wastewater can be significantly improved.

しかも、固定層部の洗浄はエアリフト管に気体を注入す
るだけの手段で自動的に行われ、構造が簡単で操作や保
守も容易である等、優れた半流動層式処理槽理装置を提
供し得るものである。
In addition, the fixed bed section is automatically cleaned by simply injecting gas into the air lift tube, and the structure is simple and easy to operate and maintain, providing an excellent semi-fluidized bed treatment tank management system. It is possible.

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

第1図は本発明装置の一実施例を示す側断面図、第2図
は第1図A−A部分の切断平面図である。
FIG. 1 is a side sectional view showing an embodiment of the apparatus of the present invention, and FIG. 2 is a cutaway plan view taken along the line A--A in FIG.

Claims (1)

【特許請求の範囲】[Claims] 流動層部とその上部に固定層部を形成してなる半流動層
式処理層の中心部に、気体の送入されるエアリフト管を
立設し、該エアリフト管の下端開口に、上端が固定層部
内に開口した担体粒子導入管を連通させるとともに、前
記エアリフト管の上端には、これより流出する担体を流
動層部に返送するとともに、流出する洗浄汚水を槽外へ
排出する手段を設けたことを特徴とする、半流動層式水
処理装置。
An air lift pipe through which gas is fed is installed upright in the center of a semi-fluidized bed processing bed consisting of a fluidized bed part and a fixed bed part formed above the fluidized bed part, and the upper end is fixed to the lower end opening of the air lift pipe. A carrier particle inlet pipe opened into the bed part is communicated with the air lift pipe, and a means is provided at the upper end of the air lift pipe to return the carrier flowing out from the pipe to the fluidized bed part and to discharge the washing wastewater flowing out to the outside of the tank. A semi-fluidized bed water treatment device characterized by:
JP60034146A 1985-02-22 1985-02-22 Semi-fluidized bed type water treatment apparatus Granted JPS61192390A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60034146A JPS61192390A (en) 1985-02-22 1985-02-22 Semi-fluidized bed type water treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60034146A JPS61192390A (en) 1985-02-22 1985-02-22 Semi-fluidized bed type water treatment apparatus

Publications (2)

Publication Number Publication Date
JPS61192390A true JPS61192390A (en) 1986-08-26
JPH0225675B2 JPH0225675B2 (en) 1990-06-05

Family

ID=12406060

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60034146A Granted JPS61192390A (en) 1985-02-22 1985-02-22 Semi-fluidized bed type water treatment apparatus

Country Status (1)

Country Link
JP (1) JPS61192390A (en)

Also Published As

Publication number Publication date
JPH0225675B2 (en) 1990-06-05

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