JPS6157043B2 - - Google Patents

Info

Publication number
JPS6157043B2
JPS6157043B2 JP55162569A JP16256980A JPS6157043B2 JP S6157043 B2 JPS6157043 B2 JP S6157043B2 JP 55162569 A JP55162569 A JP 55162569A JP 16256980 A JP16256980 A JP 16256980A JP S6157043 B2 JPS6157043 B2 JP S6157043B2
Authority
JP
Japan
Prior art keywords
liquid
superconcentrator
tank
discharge pipe
liquid discharge
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
JP55162569A
Other languages
Japanese (ja)
Other versions
JPS5787808A (en
Inventor
Akemasa Yoshimoto
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP55162569A priority Critical patent/JPS5787808A/en
Publication of JPS5787808A publication Critical patent/JPS5787808A/en
Publication of JPS6157043B2 publication Critical patent/JPS6157043B2/ja
Granted legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 この発明は、浄水場や下水等における汚泥の
過濃縮装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for superconcentrating sludge in water purification plants, sewage, etc.

この種の過濃縮装置として、従来より真空
過機、加圧過機、過床等が一般的に使用され
ている。しかしながら、真空過機や加圧過機
は、材に対し被過液を強制的に通過させるた
め、材の目にケーキが詰まつたり、あるいは
材上に積層したケーキが材面に近くなる程濃度
が高くなつたりするため、経時的に過抵抗が大
きくなる欠点がある。また、過床は、被過液
に対し機械的強制力は必要としないが、過層か
らケーキを分離する際ケーキに過層を構成する
砂利等が混入して排出されたり、設備規模が大き
くなるため、保守が面倒となる欠点がある。
As this type of superconcentration apparatus, vacuum filtration machines, pressure filtration machines, overbeds, etc. have been commonly used. However, since vacuum filtration machines and pressure filtration machines force the liquid to pass through the material, cakes may become clogged in the pores of the material, or cakes stacked on the material may become too close to the surface of the material. Since the concentration increases, there is a drawback that over-resistance increases over time. In addition, overbeds do not require mechanical forcing on the liquid to be filtrated, but when separating the cake from the overlayer, gravel, etc. that make up the overlayer may be mixed with the cake and discharged, or the equipment size is large. Therefore, there is a drawback that maintenance is troublesome.

このような従来の過濃縮装置の欠点を除去す
るため、出願人は、先に、吸液性過板を過濃
縮槽内に配置し、この過板の内部に液排出管
を挿通してこの過排出管を過濃縮槽の底部よ
り外部へ導出するよう構成することにより、被
過液中の水分を過板の毛管作用により過板に
吸収し液排出管を介して外部へ排出することが
でき、過板における目詰まりもなくしかも過
液に付着するケーキの剥離も容易となる過濃縮
装置を開発し、特許出願を行つた。
In order to eliminate such drawbacks of conventional superconcentrators, the applicant first places a liquid-absorbing filter plate in the superconcentrator tank, and inserts a liquid discharge pipe into the interior of the filter plate to drain the liquid. By configuring the over-discharge pipe to lead out from the bottom of the over-concentrator tank, the moisture in the over-concentrating liquid can be absorbed into the over-plate by the capillary action of the over-concentrator and then discharged to the outside via the liquid discharge pipe. We have developed a superconcentration device that does not clog the overplate, and also makes it easy to peel off the cake adhering to the overflowing liquid, and have filed a patent application.

しかしながら、前記特許出願に係る過濃縮装
置は、吸液性過板より導出する液排出管を
過濃縮槽の下方へ指向させて自然排水するよう構
成するため、過液に起生する過圧は下部ほど
高くなり、過液に付着するケーキは下部ほど厚
く生成し、この結果過面における過特性が不
均一となり過能力が低下する難点がある。ま
た、過板と液排出管の接続部が過濃縮槽の
底部となるため、過板の交換に際しての着脱操
作が不便となる欠点があつた。
However, the superconcentrator according to the patent application is configured to direct the liquid discharge pipe leading from the liquid-absorbing overplate toward the bottom of the superconcentrator tank for natural drainage, so the overpressure generated in the superconcentrator is reduced. The cake becomes higher at the lower part, and the cake that adheres to the liquid is formed thicker at the lower part.As a result, the filtration characteristics on the filtration surface become uneven and the filtration capacity is reduced. Furthermore, since the connecting portion between the overplate and the liquid discharge pipe forms the bottom of the superconcentration tank, there is a drawback that it is inconvenient to attach and remove the overplate when replacing it.

そこで、本発明者は、前述した従来の過濃縮
装置の問題点を全て克服すべく種々検討並びに試
作を重ねた結果、過板の上部に液排出管を挿
通してこの過排出管を過濃縮槽の外周部に取
出し、しかもこの過排出管を所定長さのサイホ
ン管に接続して過板に吸収された液を自然力
により吸引排水するように構成することにより、
過板全体の過圧力を均一に保持することがで
きると共に過板の着脱操作も簡便となり、前記
問題点を一挙に解消し得ることを突き止めた。
In order to overcome all the problems of the conventional superconcentrator described above, the inventor of the present invention conducted various studies and made prototypes, and as a result, the present inventor inserted a liquid discharge pipe into the upper part of the superconcentrator and used the superconcentrator to remove the superconcentrator. By extracting the liquid from the outer periphery of the tank and connecting this over-discharge pipe to a siphon pipe of a predetermined length, the liquid absorbed by the over-board is suctioned and drained by natural force.
It has been found that the overpressure of the entire overplate can be maintained uniformly, and the operation of attaching and detaching the overplate becomes simple, and the above problems can be solved at once.

従つて、本発明の目的は、過板全体の過圧
力を均一に保持すると共にケーキの分離除去を容
易にして過能力を向上し、しかも過板の着脱
操作が容易にして保守作業に便利な過濃縮装置
を提供するにある。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to maintain uniform overpressure across the overplate, facilitate separation and removal of cake, and improve overcapacity, and also facilitate maintenance work by making it easy to attach and remove the overplate. To provide superconcentration equipment.

前記の目的を達成するため、本発明において
は、過濃縮槽内に吸液性過板を配置し、過
板に液排出管の一端部を連通接続し、液排出
管の他端部を過濃縮槽の外部に設けたサイホン
管に連通接続することを特徴とする。
In order to achieve the above object, in the present invention, a liquid-absorbing filter plate is arranged in a superconcentrator tank, one end of a liquid discharge pipe is connected to the filter plate, and the other end of the liquid discharge pipe is connected to the filter plate. It is characterized by being communicatively connected to a siphon pipe provided outside the concentration tank.

前記の過濃縮装置において、液排出管は、
分離可能な接続部を設けて水平に配置し、サイホ
ン管の上部に接続すれば好適である。
In the above superconcentrator, the liquid discharge pipe is
It is advantageous if a separable connection is provided, arranged horizontally and connected to the upper part of the siphon tube.

また、サイホン管は、上端部に空気抜弁を設け
ると共に下端部にトラツプを設ければ好適であ
る。
Further, it is preferable that the siphon pipe is provided with an air vent valve at its upper end and a trap at its lower end.

次に、本発明に係る過濃縮装置を実施例につ
き、添付図面を参照しながら以下詳細に説明す
る。
Next, embodiments of the superconcentrator according to the present invention will be described in detail with reference to the accompanying drawings.

第1図において、参照符号10は過濃縮槽を
示し、この過濃縮槽10内には、少なくとも1
枚の吸液性過板12を配設する。吸液性過板
12は、ナイロン、テトロンあるいは金属繊維等
の不織布やスポンジまたは砂などを所定厚さの板
体に加工したもので、好ましくは前記板体の両側
面に布を貼設したものが好適に使用される。こ
のように構成した過板12は、過濃縮槽10
内に位置させ、その外周部全体に亘つて被過液
が流通し得るように過濃縮槽10の液面下に位
置決めする。なお、過濃縮槽10の底部は、適
宜ホツパ状に構成しその下端部にケーキ排出弁1
4を備えたケーキ排出口16を設ける。
In FIG. 1, reference numeral 10 indicates a superconcentrator tank, and in this superconcentrator tank 10 there is at least one
Two liquid-absorbing overboards 12 are provided. The liquid-absorbing overboard 12 is made of a nonwoven fabric such as nylon, Tetron, or metal fiber, sponge, or sand processed into a board of a predetermined thickness, and preferably has cloth pasted on both sides of the board. is preferably used. The superplate 12 configured in this way is used as the superconcentrator tank 10.
It is positioned below the liquid level of the superconcentration tank 10 so that the liquid to be permeated can flow over the entire outer circumference thereof. The bottom of the superconcentrator tank 10 is suitably shaped like a hopper, and a cake discharge valve 1 is installed at the lower end.
A cake outlet 16 with 4 is provided.

一方、過板12の上部には液排出管18の
一端部を挿通配置すると共に液排出管18の他
端部は適宜分離可能な接続部20を介して過濃
縮槽10の外部へ導出する。なお、液排出管1
8は、過濃縮槽10に対し水平に取付け、前記
接続部20において分離し、過濃縮槽10の上
部から過板12を簡便に取外すことができるよ
う構成する。過濃縮槽10の外部に導出した
液排出管18の他端部は、垂直に配置したサイホ
ン管22の上部に連通接続する。サイホン管22
の上端部には空気抜弁24を設けて大気開放し、
またサイホン管22の下部にはトラツプ26を設
けて管内に空気が逆流し空気圧が生成してサイホ
ン効果を減じないよう構成する。なお、サイホン
管22の一部には適宜開閉弁28を設けて液の
排出を制御し得るようにする。また、サイホン管
22の長さは、過板12に対する必要な減圧力
すなわち過圧力に応じて任意に設定することが
できる。
On the other hand, one end of a liquid discharge pipe 18 is inserted through the upper part of the overboard 12, and the other end of the liquid discharge pipe 18 is led out to the outside of the superconcentration tank 10 via a connection part 20 which can be separated as appropriate. In addition, liquid discharge pipe 1
8 is attached horizontally to the superconcentrating tank 10 and is separated at the connection part 20, so that the superconcentrating plate 12 can be easily removed from the upper part of the superconcentrating tank 10. The other end of the liquid discharge pipe 18 led out to the outside of the superconcentration tank 10 is connected to the upper part of a vertically arranged siphon pipe 22 . siphon tube 22
An air vent valve 24 is provided at the upper end to open the air to the atmosphere.
Further, a trap 26 is provided at the lower part of the siphon pipe 22 to prevent air from flowing back into the pipe and generating air pressure, thereby preventing the siphon effect from being reduced. Note that an on-off valve 28 is appropriately provided in a part of the siphon pipe 22 to control the discharge of the liquid. Further, the length of the siphon pipe 22 can be arbitrarily set depending on the required reduced pressure or overpressure on the overplate 12.

前述した構成からなる本発明に係る過濃縮装
置は、過開始初期において、サイホン管22の
上端部に設けた空気抜弁24を開放することによ
り、過板12内の空気は、槽内水圧により短時
間に液排出管18を経て外部へ排出することが
できる。次いで、空気抜弁24を閉じ、サイホン
管22に設けた開閉弁28を開放すれば、液は
サイホン管22によるサイホン効果によつて下方
へ自然流下し、トラツプ26を経て外部へ排出さ
れる。この場合、液の排出量は比較的少量であ
るが、サイホン管22の下端部をトラツプ26に
より液封しているため、サイホン効果が減じるこ
となく常に安定した液の排出を確保することが
できる。
The superconcentrator according to the present invention having the above-mentioned configuration opens the air vent valve 24 provided at the upper end of the siphon pipe 22 at the initial stage of overconcentration, so that the air in the overplate 12 is shortened by the water pressure in the tank. In time, the liquid can be discharged to the outside via the liquid discharge pipe 18. Next, when the air vent valve 24 is closed and the on-off valve 28 provided in the siphon pipe 22 is opened, the liquid naturally flows downward due to the siphon effect of the siphon pipe 22 and is discharged to the outside through the trap 26. In this case, the amount of liquid discharged is relatively small, but since the lower end of the siphon tube 22 is sealed with liquid by the trap 26, stable liquid discharge can always be ensured without reducing the siphon effect. .

このように、本発明に係る過濃縮装置は、槽
内のヘツド圧とサイホン効果による減圧とによ
り、液板内は全て同一圧力に保持することがで
き、過板の全面において過圧力を均一にする
ことができる。従つて、液板には、常に均一な
厚さのケーキを形成することができ、ケーキ剥離
も容易となることから、過板の過能力を常に
一定に保持することができる。
As described above, the superconcentrator according to the present invention can maintain the same pressure in all the liquid plates by using the head pressure in the tank and the reduced pressure due to the siphon effect, and the overpressure can be uniformly distributed over the entire surface of the liquid plate. can do. Therefore, a cake of uniform thickness can always be formed on the liquid plate, and the cake can be easily peeled off, so that the overcapacity of the overplate can always be kept constant.

また、本発明に係る過濃縮装置は、過板の
上部より液を排出する構成とし、サイホン効果
により液を自然流下させるものであるから、
過能力の増大を図ることができることは勿論のこ
と、過板および液排出管の着脱操作を過濃
縮槽の上部から簡便に行うことができ、保守作業
が容易となるばかりでなく、過開始初期におけ
る過板内の空気抜きも迅速に達成される等この
種の過濃縮装置の性能の向上に寄与する効果は
極めて大きい。
In addition, the superconcentration device according to the present invention has a structure in which the liquid is discharged from the upper part of the overboard, and the liquid is allowed to flow down by gravity due to the siphon effect.
Not only can the overcapacity be increased, but the overconcentrator plate and liquid discharge pipe can be easily attached and removed from the top of the overconcentrator tank, which not only simplifies maintenance work but also improves the initial stage of overconcentration. The effect of contributing to improving the performance of this type of superconcentrator is extremely large, such as the fact that the air in the superconcentrator plate can be quickly removed.

以上、本発明の好適な実施例について説明した
が、本発明の精神を逸脱しない範囲内において
種々の設計変更をなし得ることは勿論である。
Although the preferred embodiments of the present invention have been described above, it goes without saying that various design changes can be made without departing from the spirit of the present invention.

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

第1図は本発明に係る過濃縮装置の実施例を
示す構成配置図である。 10……過濃縮槽、12……過板、14…
…ケーキ排出弁、16……ケーキ排出口、18…
…液排出管、20……接続部、22……サイホ
ン管、24……空気抜弁、26……トラツプ、2
8……開閉弁。
FIG. 1 is a structural layout diagram showing an embodiment of a superconcentrator according to the present invention. 10... superconcentrator tank, 12... superplate, 14...
...Cake discharge valve, 16...Cake discharge port, 18...
...liquid discharge pipe, 20...connection section, 22...siphon pipe, 24...air vent valve, 26...trap, 2
8...Opening/closing valve.

Claims (1)

【特許請求の範囲】 1 過濃縮槽内に吸液性過板を配置し、過
板に液排出管の一端部を連通接続し、液排出
管の他端部を過濃縮槽の外部に設けたサイホン
管に連通接続することを特徴とする過濃縮装
置。 2 特許請求の範囲第1項記載の過濃縮装置に
おいて、液排出管は分離可能な接続部を設けて
水平に配設し、サイホン管の上部に接続してなる
過濃縮装置。 3 特許請求の範囲第1項または第2項記載の
過濃縮装置において、サイホン管は上端部に空気
抜弁を設けると共に下端部にトラツプを設けてな
る過濃縮装置。
[Scope of Claims] 1. A liquid-absorbing overplate is arranged in a superconcentration tank, one end of a liquid discharge pipe is connected to the overplate, and the other end of the liquid discharge pipe is provided outside the superconcentration tank. A superconcentration device characterized by being connected in communication with a siphon pipe. 2. The superconcentrator according to claim 1, wherein the liquid discharge pipe is horizontally arranged with a separable connection part and is connected to the upper part of the siphon pipe. 3. The superconcentrator according to claim 1 or 2, wherein the siphon pipe has an air vent valve at its upper end and a trap at its lower end.
JP55162569A 1980-11-20 1980-11-20 Filtrating-condensing equipment Granted JPS5787808A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55162569A JPS5787808A (en) 1980-11-20 1980-11-20 Filtrating-condensing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55162569A JPS5787808A (en) 1980-11-20 1980-11-20 Filtrating-condensing equipment

Publications (2)

Publication Number Publication Date
JPS5787808A JPS5787808A (en) 1982-06-01
JPS6157043B2 true JPS6157043B2 (en) 1986-12-05

Family

ID=15757074

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55162569A Granted JPS5787808A (en) 1980-11-20 1980-11-20 Filtrating-condensing equipment

Country Status (1)

Country Link
JP (1) JPS5787808A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6339607A (en) * 1986-08-05 1988-02-20 Fuji Electric Co Ltd Operating method for filtering and concentrating device for sludge
JPH04267905A (en) * 1991-02-21 1992-09-24 Takuma Co Ltd Water purification device

Also Published As

Publication number Publication date
JPS5787808A (en) 1982-06-01

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