JPS629929Y2 - - Google Patents

Info

Publication number
JPS629929Y2
JPS629929Y2 JP1980143812U JP14381280U JPS629929Y2 JP S629929 Y2 JPS629929 Y2 JP S629929Y2 JP 1980143812 U JP1980143812 U JP 1980143812U JP 14381280 U JP14381280 U JP 14381280U JP S629929 Y2 JPS629929 Y2 JP S629929Y2
Authority
JP
Japan
Prior art keywords
sludge
tank
raw water
water supply
filter bed
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
JP1980143812U
Other languages
Japanese (ja)
Other versions
JPS5766606U (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 JP1980143812U priority Critical patent/JPS629929Y2/ja
Publication of JPS5766606U publication Critical patent/JPS5766606U/ja
Application granted granted Critical
Publication of JPS629929Y2 publication Critical patent/JPS629929Y2/ja
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は、難濃縮性の汚泥を効果的に濃縮する
ことができる沈殿濃縮装置に関するものである。
[Detailed Description of the Invention] The present invention relates to a sedimentation and concentration apparatus that can effectively concentrate sludge that is difficult to thicken.

従来の汚泥濃縮装置は単なる重力沈降により汚
泥を沈降濃縮するものであるため、生物フロツク
(活性汚泥の余剰汚泥、アオコ類など)とか金属
水酸化物の沈殿などは沈殿濃縮性が悪く、簡単に
は濃縮できない欠点がある。
Conventional sludge thickening equipment sediments and concentrates sludge by simple gravity sedimentation, so biological flocs (excess sludge from activated sludge, blue-green algae, etc.) and metal hydroxides have poor sedimentation and concentration properties and are easily removed. has the disadvantage that it cannot be concentrated.

本考案は、このような欠点を解消し、難濃縮性
の汚泥をコンパクトな装置でも効果的に、かつ、
安定して濃縮できると共に清澄な液が得られ
る、過と汚泥濃縮の両作用を兼れ備えた有用な
る廃水処理装置を提供することを目的とするもの
である。
The present invention eliminates these drawbacks and allows difficult-to-thicken sludge to be effectively processed using a compact device.
It is an object of the present invention to provide a useful wastewater treatment device that can perform both filtration and sludge concentration functions and can stably concentrate and obtain a clear liquid.

本考案は、上部に処理水流出管を、底部中央に
汚泥ピツト及び該汚泥ピツトと連通する排泥管を
設けた沈殿槽内の上部中央に上端が前記沈殿槽の
液面上に達するように前記沈殿槽の槽壁と同心的
にかつ垂直方向に筒状の隔壁を配設して原水供給
室と清澄分離部を区画形成し、前記原水供給室に
原水供給管を開口配備すると共に、前記汚泥ピツ
トの外側に環状の濾床を形成し、また該濾床底部
に濾液集水部を設け、さらに前記濾床上部及び前
記汚泥ピツト内に汚泥掻取機を設けると共に、前
記沈殿槽外に濾液貯留槽を設けて該濾液貯留槽と
前記濾液集水部とを濾液集水路を介して連通せし
めたことである。
The present invention has a sedimentation tank with a treated water outflow pipe at the top, a sludge pit at the center of the bottom, and a sludge drainage pipe communicating with the sludge pit. A cylindrical partition wall is disposed concentrically and perpendicularly to the tank wall of the settling tank to partition a raw water supply chamber and a clarification/separation section, and a raw water supply pipe is opened and disposed in the raw water supply chamber, and the An annular filter bed is formed on the outside of the sludge pit, a filtrate collection part is provided at the bottom of the filter bed, a sludge scraper is provided in the upper part of the filter bed and in the sludge pit, and a sludge scraper is provided outside the settling tank. A filtrate storage tank is provided, and the filtrate storage tank and the filtrate collection section are communicated via a filtrate collection channel.

本考案の実施例を図面により説明すれば、槽4
の上部に処理水流出管1、底部中央に汚泥ピツト
2、該ピツトに連通する排泥管3を設け、前記槽
4の上部中央に、上端が槽4の液面L上に達する
円筒状の隔壁5を槽4の槽壁4′と同心的にかつ
垂直方向に配設することにより、槽4内に原水供
給室6、清澄分離部7を区画形成し、原水供給室
6には原水供給管8を開口配備している。前記汚
泥ピツト2は垂直方向に設けた円筒状の隔壁9a
(前記槽壁4′と同心的に配設)により形成される
集泥ピツト2aと、前記隔壁9aの下部に連なる
逆円錐状の隔壁9bにより形成される排泥ピツト
2bによつて構成されている。さらに、前記隔壁
9aの外側の環状部に砂利、砂などを充填して
床10を形成すると共に床10の底部に複数
の、前記液集水部としての集水管11を放射状
に配備し、槽4の底部内側周辺を隔壁12で囲つ
て液集水路13を形成して該集水路を槽4の外
部に設けた液貯留槽14と連通せしめ、該貯留
槽の液面L′が常に槽4の前記液面Lよりも充分下
方にあるようにするための液排出ポンプ15
(例えば水中ポンプ)を配設し、さらに、前記
床10の表面の汚泥を集泥ピツト2aに掻き寄せ
排泥管3から濃縮汚泥Dを排出するための掻寄機
16を設けた構造のものとなつている。
To explain the embodiment of the present invention with reference to the drawings, the tank 4
A treated water outflow pipe 1 is installed at the top of the tank 4, a sludge pit 2 is installed at the center of the bottom, and a sludge drainage pipe 3 is installed to communicate with the pit. By arranging the partition wall 5 concentrically and vertically with the tank wall 4' of the tank 4, a raw water supply chamber 6 and a clarification/separation section 7 are partitioned into the tank 4, and the raw water supply chamber 6 is provided with raw water. The tube 8 is arranged in an open manner. The sludge pit 2 has a cylindrical partition wall 9a provided vertically.
(arranged concentrically with the tank wall 4'), and a mud removal pit 2b formed by an inverted conical partition wall 9b continuous to the lower part of the partition wall 9a. There is. Further, the outer annular portion of the partition wall 9a is filled with gravel, sand, etc. to form a floor 10, and a plurality of water collection pipes 11 as the liquid collection portion are arranged radially at the bottom of the floor 10, and a tank A liquid collecting channel 13 is formed by surrounding the inner periphery of the bottom of the tank 4 with a partition wall 12, and the collecting channel is communicated with a liquid storage tank 14 provided outside the tank 4, so that the liquid level L' of the storage tank is always equal to the liquid level L' of the tank 4. a liquid discharge pump 15 for ensuring that the liquid level is sufficiently below the liquid level L of
(for example, a submersible pump), and a scraper 16 for scraping the sludge on the surface of the floor 10 into the sludge collecting pit 2a and discharging the concentrated sludge D from the sludge draining pipe 3. It is becoming.

なお、ポンプ15は液貯留槽14の底部に配
設され、その液面L′が常に前記底部附近にあるよ
うに制御するためのレベルスイツチが接続されて
いる。また、原水供給管8に連なる原水供給ポン
プ(図示せず)には同様に、槽4の液面Lが槽壁
4′の上端より多少下方にあるように制御するた
めのレベルスイツチが接続されている。
The pump 15 is disposed at the bottom of the liquid storage tank 14, and is connected to a level switch for controlling the liquid level L' so that it is always near the bottom. Similarly, a level switch is connected to a raw water supply pump (not shown) connected to the raw water supply pipe 8 to control the liquid level L of the tank 4 to be slightly lower than the upper end of the tank wall 4'. ing.

しかして、原水Aが原水供給管8から原水供給
室6に供給され槽4内に均等に分配される。原水
A中の汚泥は沈降して床10の上部に沈殿した
のち掻寄機16により集泥ピツト2aに掻き寄せ
られ、排泥ピツト2bを経て排泥管3から系外へ
排出される。一方、液Cは集水管11、液集
水路13を経てポンプ15により系外へ排出され
る。また上澄水Bは処理水流出管1から排出され
る。
Thus, the raw water A is supplied from the raw water supply pipe 8 to the raw water supply chamber 6 and is evenly distributed within the tank 4. After the sludge in the raw water A settles and settles on the upper part of the bed 10, it is scraped up into the sludge collection pit 2a by the scraper 16, and is discharged from the sludge pipe 3 to the outside of the system via the sludge pit 2b. On the other hand, the liquid C is discharged out of the system by the pump 15 through the water collection pipe 11 and the liquid collection channel 13. Further, the supernatant water B is discharged from the treated water outflow pipe 1.

この場合、床10上の汚泥には汚泥の自重の
ほかに前記液面LとL′との差による圧密圧力が加
わるために効果的に濃縮される。
In this case, the sludge on the bed 10 is effectively concentrated because, in addition to the sludge's own weight, consolidation pressure is applied due to the difference between the liquid levels L and L'.

前記実施例では排泥ピツト2bは槽4の底板
4″よりも下方に突出した形状にしてあるが、底
板4″を槽4全体について平板状とし、底板4″上
に隔壁9bのみを又は隔壁9a,9bを連設状態
で植設してもよい。また、集水管11は環状の集
水室としてもよい。
In the embodiment described above, the sludge pit 2b has a shape that protrudes downward from the bottom plate 4'' of the tank 4, but the bottom plate 4'' is made into a flat plate for the entire tank 4, and only the partition wall 9b or the partition wall is placed on the bottom plate 4''. 9a and 9b may be installed in a continuous manner.Furthermore, the water collection pipe 11 may be a ring-shaped water collection chamber.

以上述べたように、本考案の汚泥濃縮装置は従
来型のシツクナに新しく水頭差による強制濃縮機
構を加えたものであるため、単なる重力沈降のみ
でなく汚泥層内を通過する液による下向力に基
づく汚泥層の圧密作用が伴うので、従来濃縮が難
しい難濃縮性スラリを効果的に濃縮でき排泥濃度
が従来型に比べて大幅に高まり、したがつて後続
する汚泥処理工程が著しく合理化され、また、圧
力を増加すると濾過量が減少する濾液集水部へ濾
過集水路を介して連通した濾液貯留槽が設けられ
水面を汚泥の種類に応じて自在に調整できるよう
にしてあるので圧力を増加すると濾過量が減少す
るような難濾過性汚泥を濾過圧力の制御で効果的
に濃縮・脱水することが可能となり、さらに、
過作用と沈降分離作用が単一の槽によつて円滑に
行なわれ、しかも装置全体はコンパクトで構造も
簡単であるなどの利益が得られるものである。
As mentioned above, the sludge thickening device of the present invention is a conventional sludge thickener with a new forced thickening mechanism based on the water head difference, so it is not only caused by gravity settling but also by the downward force caused by the liquid passing through the sludge layer. Because it involves the consolidation action of the sludge layer based on the conventional method, it is possible to effectively concentrate the difficult-to-thicken slurry that is difficult to thicken in the past, and the sludge concentration is significantly increased compared to the conventional type, thereby significantly streamlining the subsequent sludge treatment process. In addition, a filtrate storage tank is provided that communicates with the filtrate collection section through a filtration collection channel, where the amount of filtration decreases when the pressure is increased, and the water surface can be freely adjusted depending on the type of sludge. By controlling the filtration pressure, it is possible to effectively concentrate and dewater difficult-to-filter sludge, where the amount of filtration decreases when the amount of filtration increases.
The advantages include that overaction and sedimentation/separation can be carried out smoothly in a single tank, and that the entire apparatus is compact and simple in structure.

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

図面は本考案の実施例を示す縦断面図である。 1……処理水流出管、2……汚泥ピツト、2a
……集泥ピツト、2b……排泥ピツト、3……排
泥管、4……槽、4′……槽壁、4″……底板、5
……隔壁、6……原水供給室、7……清澄分離
部、8……原水供給管、9a,9b……隔壁、1
0……床、11……集水管、12……隔壁、1
3……液集水路、14……液貯留槽、15…
…ポンプ、16……掻寄機。
The drawing is a longitudinal sectional view showing an embodiment of the present invention. 1... Treated water outflow pipe, 2... Sludge pit, 2a
...Mud collecting pit, 2b...Sludge removal pit, 3...Sludge removal pipe, 4...Tank, 4'...Tank wall, 4''...Bottom plate, 5
... Partition wall, 6 ... Raw water supply chamber, 7 ... Clarification separation section, 8 ... Raw water supply pipe, 9a, 9b ... Partition wall, 1
0...Floor, 11...Water collection pipe, 12...Bulkhead, 1
3...Liquid collection channel, 14...Liquid storage tank, 15...
...pump, 16... scraper.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 上部に処理水流出管を、底部中央に汚泥ピツト
及び該汚泥ピツトと連通する排泥管を設けた沈殿
槽内の上部中央に上端が前記沈殿槽の液面上に達
するように前記沈殿槽の槽壁と同心的にかつ垂直
方向に筒状の隔壁を配設して原水供給室と清澄分
離部を区画形成し、前記原水供給室に原水供給管
を開口配備すると共に、前記汚泥ピツトの外側に
環状の濾床を形成し、また該濾床底部に濾液集水
部を設け、さらに前記濾床上部及び前記汚泥ピツ
ト内に汚泥掻取機を設けると共に、前記沈殿槽外
に濾液貯留槽を設けて該濾液貯留槽と前記濾液集
水部とを濾液集水路を介して連通せしめたことを
特徴とする廃水処理装置。
The sedimentation tank is equipped with a treated water outflow pipe at the top, a sludge pit at the center of the bottom, and a drainage pipe communicating with the sludge pit. A cylindrical partition wall is disposed concentrically and vertically with the tank wall to partition a raw water supply chamber and a clarification/separation section, and a raw water supply pipe is opened in the raw water supply chamber, and the outside of the sludge pit is provided with a raw water supply pipe. A ring-shaped filter bed is formed in the filter bed, a filtrate collection part is provided at the bottom of the filter bed, a sludge scraper is provided in the upper part of the filter bed and in the sludge pit, and a filtrate storage tank is provided outside the settling tank. A wastewater treatment apparatus characterized in that the filtrate storage tank and the filtrate collection section are provided in communication with each other via a filtrate collection channel.
JP1980143812U 1980-10-08 1980-10-08 Expired JPS629929Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1980143812U JPS629929Y2 (en) 1980-10-08 1980-10-08

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1980143812U JPS629929Y2 (en) 1980-10-08 1980-10-08

Publications (2)

Publication Number Publication Date
JPS5766606U JPS5766606U (en) 1982-04-21
JPS629929Y2 true JPS629929Y2 (en) 1987-03-09

Family

ID=29503549

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1980143812U Expired JPS629929Y2 (en) 1980-10-08 1980-10-08

Country Status (1)

Country Link
JP (1) JPS629929Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5651927Y2 (en) * 1976-03-23 1981-12-04

Also Published As

Publication number Publication date
JPS5766606U (en) 1982-04-21

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