JPS6146163B2 - - Google Patents

Info

Publication number
JPS6146163B2
JPS6146163B2 JP58099193A JP9919383A JPS6146163B2 JP S6146163 B2 JPS6146163 B2 JP S6146163B2 JP 58099193 A JP58099193 A JP 58099193A JP 9919383 A JP9919383 A JP 9919383A JP S6146163 B2 JPS6146163 B2 JP S6146163B2
Authority
JP
Japan
Prior art keywords
sludge
level
rotating drum
rotating
suction
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
JP58099193A
Other languages
Japanese (ja)
Other versions
JPS59225714A (en
Inventor
Takuo Mochizuki
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP58099193A priority Critical patent/JPS59225714A/en
Publication of JPS59225714A publication Critical patent/JPS59225714A/en
Publication of JPS6146163B2 publication Critical patent/JPS6146163B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明は主として含水量の比較的多い汚泥例え
ばヘドロ等を脱水処理する装置に関し、目的とす
るところは、優れた脱水機能を具備すると共に連
続的且つ能率良く脱水処理可能な装置を提供する
ことにある。
DETAILED DESCRIPTION OF THE INVENTION The present invention mainly relates to a device for dewatering sludge with a relatively high water content, such as sludge, etc., and an object thereof is to have an excellent dewatering function and to be able to dewater continuously and efficiently. The goal is to provide a device that is

汚泥脱水処理手段には、遠心分離、沈澱、布
或いはストレーナ表面への吸着等があるが、本発
明は布面或いはストレーナ表面への吸着手段を
利用するものである。従来のこの種の汚泥脱水装
置は、吸着面での吸着ロスと真空度形成と維持が
悪いために、吸着量と脱水量が少く、従つて処理
能率が著しく低かつた。
Sludge dewatering treatment methods include centrifugation, sedimentation, adsorption to cloth or strainer surfaces, and the present invention utilizes adsorption means to cloth surfaces or strainer surfaces. Conventional sludge dewatering equipment of this type has a low adsorption amount and a low dewatering amount due to adsorption loss on the adsorption surface and poor vacuum formation and maintenance, resulting in extremely low treatment efficiency.

本発明装置は斯る欠点を解消するものであつ
て、汚泥の供給及びオーバーフローにより所定の
レベルに汚泥水を貯留するようにした留箱上に、
回転周面をストレーナとし内部流体を吸引するた
めの吸引管を具備させた回転ドラムが、その回転
ドラムの回転周面が留箱のレベル下を通過する位
置に回転自在に軸支され、回転ドラムのレベル下
進入がわ周面に、終端がレベル下となる通気防止
カバーが摺接され、通気防止カバーの始端部で若
しくは回転ドラムに布ベルトを掛けた際には始
端部から終端部間で迂回させた布ベルトの表面
で、吸着汚泥を剥離除去する構成とし且つ吸引管
の他端がジエツトポンプを用いた真空発生装置の
吸引がわへ配管されていることを特徴とする汚泥
脱水処理装置を要旨としており、図示例において
説明すると以下の通りである。
The device of the present invention solves these drawbacks, and has a storage box on which sludge water is stored at a predetermined level through sludge supply and overflow.
A rotating drum is equipped with a suction tube for sucking internal fluid using its rotating circumferential surface as a strainer, and is rotatably supported at a position where the rotating circumferential surface of the rotating drum passes below the level of the fastening box. A ventilation prevention cover whose terminal end is below the level is slid on the peripheral surface of the entrance below the level. A sludge dewatering device is characterized in that the adsorbed sludge is peeled off and removed on the surface of a detoured cloth belt, and the other end of the suction pipe is connected to the suction side of a vacuum generator using a jet pump. The summary is as follows, and the explanation using the illustrated example is as follows.

第1図は回転ドラム1の周面に摺接させた通気
防止カバー2の始端部に掻板3を設け、該部分で
吸着汚泥を剥離除去する場合である。
FIG. 1 shows a case where a scraper plate 3 is provided at the starting end of a ventilation prevention cover 2 that is in sliding contact with the circumferential surface of a rotating drum 1, and the adsorbed sludge is peeled off and removed at this part.

即ち、回転ドラム1は、支軸4及び中空支軸
4′を突設した円盤5,5′が回転表面となるスト
レーナ6を挾んで対設固定され、支軸4にはスプ
ロケツト7が軸着された構成である。このスプロ
ケツト7へ変速可能な駆動源(図示せず)から動
力が伝達される。
That is, the rotary drum 1 is fixed in opposition to the disks 5, 5' having a support shaft 4 and a hollow support shaft 4' projecting therebetween, sandwiching a strainer 6 which serves as a rotating surface, and a sprocket 7 is attached to the support shaft 4. This is the configuration. Power is transmitted to the sprocket 7 from a variable speed drive source (not shown).

留箱8は比較的浅い上端開口の皿形をしてお
り、一側部に所定の汚水レベル9を形成するため
のオーバーフロー口10を具備している。
The retainer box 8 is dish-shaped with a relatively shallow upper opening, and is provided with an overflow port 10 on one side for forming a predetermined sewage level 9.

11はフレームであつて、前記回転ドラム1と
留箱8とを、回転ドラム1の回転周面が留箱8の
汚水レベル9下を通過する関係に両者を支持する
と共に、回転ドラム1のレベル下進入がわ12の
周面に沿つて摩擦抵抗の小なる部材例えばテフロ
ン(登録商標)製の通気防止カバー2と該通気防
止カバー2の始端部の掻板3を支持している。
Reference numeral 11 denotes a frame that supports the rotating drum 1 and the retaining box 8 in such a manner that the rotating peripheral surface of the rotating drum 1 passes below the sewage level 9 of the retaining box 8; Along the circumferential surface of the lower entryway 12, a member having low frictional resistance, such as a ventilation prevention cover 2 made of Teflon (registered trademark), and a scraper plate 3 at the starting end of the ventilation prevention cover 2 are supported.

通気防止カバー2は、その始端部が留箱8の開
口縁より上方にあつて且つ終端部が汚水のレベル
9より下方となる範囲で回転ドラム1の回転周面
に摺接されている。
The ventilation prevention cover 2 is in sliding contact with the rotating circumferential surface of the rotary drum 1 in such a range that its starting end is above the opening edge of the fastening box 8 and its terminal end is below the level 9 of the dirty water.

13は吸引管であつて、回転ドラム1の中空支
軸4′を通して一端の吸水口14を回転ドラム1
の内部で開口させ、他端は真空発生装置25に配
管されている。
Reference numeral 13 denotes a suction pipe, which connects the water suction port 14 at one end to the rotary drum 1 through the hollow support shaft 4' of the rotary drum 1.
The other end is piped to the vacuum generator 25.

15は汚泥槽であつて、ポンプPによつて留箱
8へ汚水を供給するところの汚水供給管16と、
留箱8のオーバーフロー口10へ配管された復水
管17を備えている。
15 is a sludge tank, and a sewage supply pipe 16 that supplies sewage to the storage box 8 by a pump P;
A condensate pipe 17 is provided which is piped to an overflow port 10 of the retention box 8.

真空発生源25は(第2図)底部に排泥用バル
ブ26を介してジエツトノズル34を用いた排制
排泥ポンプ27を具備した排出部28を有する吸
引水用タンク29の上部に、吸水管配管口30と
ポンプ連結口31を具備し、ポンプ連結口31に
は、吸込管32と吐出管33の結合部にジエツト
ノズル34に連続する保護管35を吐出管33の
中心に向けて結合したジエツトポンプ36の吸込
管32が配管され、給水タンク37からポンプ3
8で高圧水とした水をノズル34へ供給し、吐出
管33の終端を給水タンク37に至らした構成と
なつている。39は保護管35に配管した空気導
入管であつて開閉自在となつている。
The vacuum source 25 (FIG. 2) is connected to a water suction pipe at the top of a suction water tank 29 which has a discharge section 28 equipped with a discharge pump 27 using a jet nozzle 34 at the bottom via a mud discharge valve 26. A jet pump is equipped with a piping port 30 and a pump connection port 31, and the pump connection port 31 has a protective tube 35 connected to a joint between a suction pipe 32 and a discharge pipe 33 and connected to a jet nozzle 34 toward the center of the discharge pipe 33. 36 suction pipes 32 are connected to the pump 3 from the water supply tank 37.
Water made into high-pressure water at step 8 is supplied to the nozzle 34, and the end of the discharge pipe 33 reaches a water supply tank 37. Reference numeral 39 denotes an air introduction pipe connected to the protection tube 35, which can be opened and closed.

尚、通気防止カバー2は、回転ドラムの回転周
面に摺接することにより摩耗するが、第4図の如
く厚みを持たせて、常に回転周面へ摺接するよう
スプリング等で付勢させる構成でフレーム等に保
持させるようにすることが好ましい。
Note that the ventilation prevention cover 2 wears out due to sliding contact with the rotating circumferential surface of the rotating drum, but as shown in FIG. It is preferable to hold it in a frame or the like.

第3図の実施例は、回転ドラム1の回転周面の
ストレーナ6に布ベルト18を掛けた場合であ
つて、レベル下進入がわ12の回転ドラム周面に
摺接した通気防止カバー2の始端部において、
布ベルト18が回転周面から離れ、迂回ロール1
9,20,21を回つて通気防止カバー2の終端
部で回転ドラム1の回転周面に巻掛け、吸着汚泥
の除去は、迂回ロール19の表面の曲率変化若し
くは掻板3によつて行う構造である。
In the embodiment shown in FIG. 3, a cloth belt 18 is hung around the strainer 6 on the rotating circumferential surface of the rotating drum 1, and the ventilation prevention cover 2 is in sliding contact with the rotating drum circumferential surface on the lower level entry side 12. At the starting end,
The cloth belt 18 separates from the rotating circumferential surface, and the detour roll 1
9, 20, and 21, and is wrapped around the rotating peripheral surface of the rotary drum 1 at the terminal end of the ventilation prevention cover 2, and the adsorbed sludge is removed by changing the curvature of the surface of the detour roll 19 or by using the scraping plate 3. It is.

尚、真空発生装置25は、第2図の実施例とは
別に第5図に示す如く、ジエツトポンプ36の吸
込管32に回転ドラム1の吸引管13を直結する
構成、或いは第6図の如く高圧水供給用のポンプ
45を分離タンク47内に設けると共に、ジエツ
トポンプ36の吐出管33を分離タンク47内に
臨出させ、回転ドラム1の吸引管10をジエツト
ポンプ36の吸込管32に結合する構成の場合も
ある。
In addition to the embodiment shown in FIG. 2, the vacuum generator 25 has a structure in which the suction pipe 13 of the rotary drum 1 is directly connected to the suction pipe 32 of the jet pump 36, as shown in FIG. 5, or a high-pressure generator as shown in FIG. The pump 45 for water supply is provided in the separation tank 47, the discharge pipe 33 of the jet pump 36 is exposed into the separation tank 47, and the suction pipe 10 of the rotating drum 1 is connected to the suction pipe 32 of the jet pump 36. In some cases.

以上本発明装置の実施例とその各部についての
具体例を図示説明したが、その作用を第1図及び
第2図において説明すると以下の通りである。
The embodiment of the device of the present invention and specific examples of its respective parts have been illustrated and explained above, and the operation thereof will be explained below with reference to FIGS. 1 and 2.

即ち、本発明装置は汚泥槽15から留箱8へ汚
泥供給するにおいて、まず真空発生源25を作動
させて回転ドラム1内を真空圧にする。始動時に
はストレーナ6は通気状態にあるから、非通気性
の帯材を吸着させておき、汚泥を吸着させながら
この帯材を外し全周面が汚泥で塞がれた段階で回
転ドラム1の連続回転を開始させる。ストレーナ
6に吸着された汚泥は一回転する間に吸水され
て、通気防止カバー2の始端部に設けた掻板3に
よつて剥離され、脱水汚泥用シユートから搬送コ
ンベアで所定位置へ移送される。吸着汚泥が剥離
されたストレーナ面は通気状態になるが、掻板3
の直後から留箱8のレベル9下まで通気防止カバ
ー2が摺接されているので、これを吸収するよう
になり、回転ドラム1内の真空度低下を招来する
ことなく汚泥の吸着を為す。回転ドラム1内に吸
引された汚水は吸水用タンク29内へ吸引され
る。この吸水用タンク29は常に絶対真空に近い
真空度に維持される。これは吸水用タンク29の
上部に設けたジエツトポンプ36の作用によるも
のであつて、ジエツトノズル34から噴射される
高圧水が、空気導入管39を備えた保護管35か
ら吐出管33内へ突入する際に、導入空気によつ
てキヤビテーシヨンを生ずることなく突入する。
即ち、エネルギー損失少く噴射されるので、極め
て高い吐出真空圧力を吸引管32内に生じさせる
からである。このため必ずしも吸水用タンク29
を介在させず、第2図における吸水管配管口30
をポンプ連結口31に直結する構成とした第4
図、第5図の如きとしても良いのである。
That is, when the apparatus of the present invention supplies sludge from the sludge tank 15 to the retention box 8, the vacuum source 25 is first activated to create a vacuum inside the rotating drum 1. Since the strainer 6 is in a ventilated state at the time of startup, a non-breathable strip material is adsorbed, and this strip material is removed while adsorbing sludge, and when the entire circumference is covered with sludge, the rotation of the rotating drum 1 is continued. Start the rotation. The sludge adsorbed by the strainer 6 absorbs water during one rotation, is peeled off by the scraping plate 3 provided at the starting end of the ventilation prevention cover 2, and is transferred from the dehydrated sludge chute to a predetermined position by a conveyor. . The strainer surface from which the adsorbed sludge has been removed becomes ventilated, but the scraping plate 3
Since the ventilation prevention cover 2 is slidably contacted from immediately after to below the level 9 of the retaining box 8, it absorbs the sludge and adsorbs the sludge without causing a decrease in the degree of vacuum inside the rotating drum 1. The dirty water sucked into the rotating drum 1 is sucked into the water absorption tank 29. This water absorption tank 29 is always maintained at a degree of vacuum close to absolute vacuum. This is due to the action of the jet pump 36 provided at the upper part of the water suction tank 29, and when the high pressure water jetted from the jet nozzle 34 rushes into the discharge pipe 33 from the protection pipe 35 equipped with the air introduction pipe 39. The air enters the air without causing cavitation due to the introduced air.
That is, since the fuel is injected with little energy loss, an extremely high discharge vacuum pressure is generated within the suction tube 32. For this reason, it is not necessary to use the water absorption tank 29.
The water suction pipe piping port 30 in FIG.
The fourth pump is configured to be directly connected to the pump connection port 31.
It may be as shown in FIG.

以上のように本発明装置は、回転ドラムの周面
の汚水中進入がわに通気防止カバーを摺接しその
始端部に吸着汚泥剥離手段を設けると共に留箱の
汚水レベル下を終端部としたから、真空度低下ロ
スが解消され、強力な吸引によつて脱水作用が継
続し優れた脱水効果が得られる。このような優れ
た脱水処理効果が回転ドラムの回転によつて連続
継続されるので、汚泥の脱水処理能率は著しく向
上する。又、回転ドラムの周面がストレーナ若し
くはストレーナと布ベルトであつて回転ドラム
内から真空圧による吸引力を作用させる構造であ
るから、回転ドラム内部は一切仕切り等がない簡
単なものとなり、全体の装置構造は著しく簡単と
なつて製作においても保守管理においても最適の
処理装置となる。
As described above, in the device of the present invention, a ventilation prevention cover is placed in sliding contact with the peripheral surface of the rotating drum where the sewage enters, and an adsorption sludge removal means is provided at the starting end of the cover, and the terminating end is below the sewage level of the retention box. , the vacuum loss is eliminated, and the strong suction continues the dehydration action, resulting in excellent dehydration effects. Since such an excellent dewatering effect is continuously maintained by the rotation of the rotating drum, the sludge dewatering efficiency is significantly improved. In addition, since the circumferential surface of the rotating drum is made of a strainer or a strainer and a cloth belt, and the suction force is applied by vacuum pressure from within the rotating drum, the interior of the rotating drum is simple with no partitions, etc., and the overall The device structure is extremely simple, making it an optimal processing device both in terms of manufacturing and maintenance.

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

図面は本発明装置並びに各部の実施例であつ
て、第1図は構成略図、第2図は真空発生装置と
結合した断面図、第3図は布ベルトを用いた
例、第4図は通気防止カバーを摩耗に順応するよ
うにした例、第5図、第6図は真空発生装置と関
係の他の例を示す略図である。 1……回転ドラム、2……通気防止カバー、3
……掻板、6……ストレーナ、8……留箱、9…
…レベル、12……進入がわ、13……吸水管、
25……真空発生装置。
The drawings show an example of the present invention device and each part, and Fig. 1 is a schematic diagram of the configuration, Fig. 2 is a cross-sectional view of the device combined with a vacuum generator, Fig. 3 is an example using a cloth belt, and Fig. 4 is an example of ventilation. FIGS. 5 and 6 are schematic diagrams showing other examples of the vacuum generating device and its relationship, in which the protective cover is adapted to wear. 1... Rotating drum, 2... Ventilation prevention cover, 3
...Scraper board, 6...Strainer, 8...Block box, 9...
...Level, 12...Entry side, 13...Water intake pipe,
25...Vacuum generator.

Claims (1)

【特許請求の範囲】[Claims] 1 汚泥の供給及びオーバーフローにより所定の
レベルに汚泥水を貯留するようにした留箱上に、
回転周面をストレーナとし内部流体を吸引するた
めの吸引管を具備させた回転ドラムが、その回転
ドラムの回転周面が留箱のレベル下を通過する位
置に回転自在に軸支され、回転ドラムのレベル下
進入がわ周面に、終端がレベル下となる通気防止
カバーが摺接され、通気防止カバーの始端部で若
しくは回転ドラムに布ベルトを掛けた際には始
端部から終端部間で迂回させた布ベルトの表面
で、吸着汚泥を剥離除去する構成とし且つ吸引管
の他端がジエツトポンプの吸引がわへ直接若しく
は真空タンクを介して配管されていることを特徴
とする汚泥脱水処理装置。
1. On a storage box that stores sludge water at a predetermined level through sludge supply and overflow,
A rotating drum is equipped with a suction tube for sucking internal fluid using its rotating circumferential surface as a strainer, and is rotatably supported at a position where the rotating circumferential surface of the rotating drum passes below the level of the fastening box. A ventilation prevention cover whose terminal end is below the level is slid on the peripheral surface of the entrance below the level. A sludge dewatering device configured to peel and remove adsorbed sludge on the surface of a detoured cloth belt, and characterized in that the other end of a suction pipe is connected directly to the suction side of a jet pump or via a vacuum tank. .
JP58099193A 1983-06-02 1983-06-02 Sludge dehydrating apparatus Granted JPS59225714A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58099193A JPS59225714A (en) 1983-06-02 1983-06-02 Sludge dehydrating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58099193A JPS59225714A (en) 1983-06-02 1983-06-02 Sludge dehydrating apparatus

Publications (2)

Publication Number Publication Date
JPS59225714A JPS59225714A (en) 1984-12-18
JPS6146163B2 true JPS6146163B2 (en) 1986-10-13

Family

ID=14240807

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58099193A Granted JPS59225714A (en) 1983-06-02 1983-06-02 Sludge dehydrating apparatus

Country Status (1)

Country Link
JP (1) JPS59225714A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0420483Y2 (en) * 1986-07-25 1992-05-11
JP5914113B2 (en) * 2012-03-30 2016-05-11 株式会社フジタ Solid-liquid separator
CN111501728A (en) * 2020-03-31 2020-08-07 温州大学 Vacuum preloading device and vacuum preloading method based on container treatment slurry

Also Published As

Publication number Publication date
JPS59225714A (en) 1984-12-18

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