JP2000279715A - Solid-liquid separation apparatus - Google Patents

Solid-liquid separation apparatus

Info

Publication number
JP2000279715A
JP2000279715A JP11086269A JP8626999A JP2000279715A JP 2000279715 A JP2000279715 A JP 2000279715A JP 11086269 A JP11086269 A JP 11086269A JP 8626999 A JP8626999 A JP 8626999A JP 2000279715 A JP2000279715 A JP 2000279715A
Authority
JP
Japan
Prior art keywords
filter cloth
cleaning
self
solid
pressure
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.)
Pending
Application number
JP11086269A
Other languages
Japanese (ja)
Inventor
Kenichi Fujitani
健一 藤谷
Teruo Senda
輝雄 千田
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.)
Toray Industries Inc
Original Assignee
Toray 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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP11086269A priority Critical patent/JP2000279715A/en
Publication of JP2000279715A publication Critical patent/JP2000279715A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To surely prevent the clogging of a nozzle and filter cloth and to stabilize the separation and dehydration treatment capability of a solid component and liquid component by equipping the apparatus with a filter cloth washing means having the self-washing type nozzle and a washing fluid supplying means which is capable of intermittently changing the supply pressure of the washing fluid to the self-washing type nozzle. SOLUTION: The filter cloth 2 is circumferentially rotated by a drive roll 3 and a pressure reduction vessel 6 is internally decompressed by a pressure reduction blower 14. The original liquid supplied to a original liquid supply vessel 5 is forcibly sucked to the pressure reduction suction vessel 6 side via the filter cloth 2 to suck the liquid component in the original liquid by the pressure reduction suction vessel 6. The solid component is captured by the filter cloth. The liquid component is once stored in a sealing vessel 10. On the other hand, the solid component is transferred together with the filter cloth 2 to a pressure dehydrating means consisting of a metallic drum 7, a pressure roll 8, etc., and is transferred to the metallic drum 7 side, following which the solid component is scraped by a scraper 9 and is dropped to a cake receiving vessel 17. The surfaces of the filter cloth 2 are thereafter washed by the washing means 3 having the self-washing type nozzle.

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、懸濁物質等を含む
原液を固液分離するのに好適に用いられる固液分離装置
に関し、詳しくは、メンテナンスを軽減でき、かつ、濾
布の目詰まりを防止することができる固液分離装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid-liquid separation device which is suitably used for solid-liquid separation of an undiluted solution containing a suspended substance or the like, and more particularly to a device capable of reducing maintenance and clogging a filter cloth. The present invention relates to a solid-liquid separation device capable of preventing a solid-liquid separation.

【0002】[0002]

【従来の技術】従来から、アオコ等のプランクトン類
や、汚泥や土砂等のシルト質の微細な懸濁物質を含有す
る原液を連続的に固液分離するために、周回する濾布を
利用した脱水機や濾過機が用いられており、濾布の固液
分離効率が、懸濁物質の蓄積によって運転時間に伴って
低下するという問題がある。
2. Description of the Related Art Conventionally, a rotating filter cloth has been used to continuously and solid-liquid separate a stock solution containing planktonic species such as blue-green algae and fine silt-like suspended substances such as sludge and earth and sand. A dehydrator and a filter are used, and there is a problem that the solid-liquid separation efficiency of the filter cloth decreases with the operation time due to accumulation of suspended substances.

【0003】このような濾布による固液分離効率の低下
を抑制し、長時間連続運転可能にするため、濾布の周回
移動路の途中に洗浄ノズルを設置し、この洗浄ノズルか
ら洗浄用水を噴射して濾布を再生しながら運転すること
が知られている。
In order to suppress a decrease in the solid-liquid separation efficiency due to such a filter cloth and to enable continuous operation for a long time, a washing nozzle is installed in the middle of the orbital movement path of the filter cloth, and washing water is supplied from the washing nozzle. It is known to operate while spraying to regenerate the filter cloth.

【0004】この場合、濾布を効率よく再生するという
目的から、洗浄用水として懸濁物質を実質的に含まない
水を用いることが好ましいが、そのような水を供給する
ためには、脱水機や濾過機として使用できるところが制
限されたり、洗浄用水中の懸濁物質を除去するための別
の濾過機が新たに必要になる。
[0004] In this case, for the purpose of efficiently regenerating the filter cloth, it is preferable to use water substantially free of suspended substances as washing water. Or a filter that can be used as a filter, or another filter for removing suspended substances in washing water is newly required.

【0005】一方、節水のため、洗浄用水として多少懸
濁物質を含有する雑用水や洗浄排水をリサイクルして使
用している場合もある。しかしながら、この場合には、
水中に含有される懸濁物質により頻繁にノズルが詰ま
る。この結果、濾布の洗浄回復性が低下して処理性能や
安定性が欠け、また、ノズルのメンテナンスのために労
力、時間、費用が必要になり、さらにはそのメンテナン
スの間処理を停止しなくてはならないという問題があ
る。
[0005] On the other hand, in order to conserve water, there is a case where, as washing water, miscellaneous water or washing wastewater containing some suspended substances is recycled and used. However, in this case,
Frequently, nozzles are clogged by suspended matter contained in the water. As a result, the cleaning recovery of the filter cloth is reduced, and the processing performance and stability are lacking.Moreover, labor, time and cost are required for maintenance of the nozzle, and furthermore, the processing is not stopped during the maintenance. There is a problem that must not be.

【0006】[0006]

【発明が解決しようとする課題】本発明は、洗浄ノズル
の詰まりによるメンテナンスの負担を軽減するとともに
濾布の洗浄回復性の低下を防止し、同一濾布による長時
間の運転が可能な固液分離装置を提供することを目的と
する。
SUMMARY OF THE INVENTION The present invention reduces the burden of maintenance due to clogging of a washing nozzle, prevents a decrease in the recovery of the filter cloth from being washed, and enables a solid-liquid liquid that can be operated for a long time with the same filter cloth. It is an object to provide a separation device.

【0007】[0007]

【課題を解決するための手段】上記課題を達成するため
の本発明は、濾布走行手段と、濾布の表面側に設けた原
液供給手段と、濾布の裏面側で、かつ、原液供給手段に
対向して設けた減圧吸引手段と、濾布走行方向に関して
減圧吸引手段よりも下流側に設けた加圧脱水手段と、自
己洗浄型ノズルを備えた濾布洗浄手段と、自己洗浄型ノ
ズルへの洗浄流体の供給圧力を間欠的に変更可能な洗浄
流体供給手段とを有している固液分離装置を特徴とする
ものである。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention provides a filter cloth running means, a stock solution supply means provided on the front side of the filter cloth, and a stock solution supply means on the back side of the filter cloth. Pressure-reducing suction means provided in opposition to the means, pressure dehydrating means provided downstream of the pressure-reducing suction means with respect to the direction of travel of the filter cloth, filter cloth cleaning means having a self-cleaning nozzle, and self-cleaning nozzle A solid-liquid separator having cleaning fluid supply means capable of intermittently changing the supply pressure of the cleaning fluid to the solid-liquid separator.

【0008】ここで、自己洗浄型ノズルは、本体内に設
けた桃割れ自在な複数個のスプレーチップとばねとを有
し、複数個のスプレーチップは、スプレーチップに作用
する洗浄流体の圧力とばねの復元力とのバランスにより
上下に移動するとともに下方に位置するときに桃割れす
るように構成されていることが好ましく、複数個のスプ
レーチップは、スプレーチップに作用する洗浄流体の圧
力がばねの復元力よりも大きいときに合体し、洗浄流体
の圧力がばねの復元力よりも小さいときに桃割れするこ
とがより好ましい。また、使用後の洗浄流体の少なくと
も一部を自己洗浄型ノズルに還流させる還流手段を設け
たことや、自己洗浄型ノズルを、洗浄流体抜出弁を備え
たパイプに設けたこと、さらに、洗浄流体の流れ方向に
関して自己洗浄型ノズルよりも上流側にオートストレー
ナを設けたことが好ましい。
Here, the self-cleaning type nozzle has a plurality of peach-sprayable spray tips and springs provided in the main body, and the plurality of spray tips are adapted to the pressure of the cleaning fluid acting on the spray tips. It is preferable that the plurality of spray tips be configured to move up and down by a balance with the restoring force of the spring and to crack when located below. More preferably, when the cleaning fluid pressure is smaller than the spring restoring force, the cleaning fluid is united when the cleaning fluid is smaller than the spring restoring force. In addition, providing a reflux means for returning at least a part of the used cleaning fluid to the self-cleaning nozzle, providing the self-cleaning nozzle in a pipe provided with a cleaning fluid discharge valve, and further cleaning It is preferable to provide an auto strainer upstream of the self-cleaning nozzle with respect to the flow direction of the fluid.

【0009】そして、上記いずれかの固液分離装置を用
いる造水方法も好ましい。
[0009] A fresh water producing method using any of the above solid-liquid separation devices is also preferable.

【0010】[0010]

【発明の実施の形態】本発明の固液分離装置は、たとえ
ば図1の濾布走行式脱水機1に示すように、供給される
原液に含まれる固液を走行する濾布2によって分離する
固液分離手段と、自己洗浄型ノズルを設けた濾布の洗浄
手段13と、自己洗浄型ノズルに供給する洗浄流体の圧
力を間欠的に変更可能な、タイマー18を有するポンプ
12を備えているものである。
BEST MODE FOR CARRYING OUT THE INVENTION A solid-liquid separator of the present invention separates a solid-liquid contained in a supplied stock solution by a traveling filter cloth 2 as shown in, for example, a filter cloth traveling dehydrator 1 in FIG. The apparatus includes a solid-liquid separation unit, a filter cloth cleaning unit 13 provided with a self-cleaning nozzle, and a pump 12 having a timer 18 capable of intermittently changing the pressure of a cleaning fluid supplied to the self-cleaning nozzle. Things.

【0011】この濾布走行式脱水機1において、濾布2
は、駆動ロール3を含む複数のガイドロール4間に無端
状に連続周回するように設けられており、その濾布2の
表面に原液を供給する原液供給槽5が設けられている。
また、濾布2の裏面側で、かつ、原液供給槽5に対抗す
る位置には、減圧ブロワー14を有する減圧吸引槽6が
設けられており、さらに、濾布2の走行方向に関して減
圧吸引槽6よりも下流側に、濾布2を挟圧して脱水する
加圧脱水手段が設けられている。加圧脱水手段は、濾布
2を挟圧する金属ドラム7および加圧ロール8や、脱水
されて金属ドラム7に転写された固形成分を掻き取るス
クレーパー9、また、掻き取られた固形成分を受けるケ
ーク受槽17を備えている。このように固液分離手段が
構成されている。
In this filter cloth traveling dehydrator 1, the filter cloth 2
Is provided so as to continuously rotate endlessly between a plurality of guide rolls 4 including a drive roll 3, and a stock solution supply tank 5 for supplying a stock solution to the surface of the filter cloth 2 is provided.
In addition, a vacuum suction tank 6 having a vacuum blower 14 is provided on the back side of the filter cloth 2 and at a position opposite to the stock solution supply tank 5, and further, a vacuum suction tank with respect to the traveling direction of the filter cloth 2. Downstream from 6, a pressurized dewatering means for sandwiching and dewatering the filter cloth 2 is provided. The pressure dewatering means receives the metal drum 7 and the pressure roll 8 for pressing the filter cloth 2, the scraper 9 for scraping off the solid component dewatered and transferred to the metal drum 7, and receives the scraped solid component. A cake receiving tank 17 is provided. Thus, the solid-liquid separation means is configured.

【0012】そして、濾布走行方向に関して固液分離手
段の下流側には、内部に捕捉した異物を自動的に排出す
る自己洗浄型ノズルを有する濾布の洗浄手段13と、そ
の洗浄排水を受ける排水槽11とが設けられている。な
お、説明の便宜上、自己洗浄型ノズルを濾布の表洗手段
に設けた態様について説明するが、自己洗浄型ノズルは
濾布の表洗手段および逆洗手段のいずれに設けられてい
てもよく、また、両方に設けられていてもよい。
A filter cloth cleaning means 13 having a self-cleaning type nozzle for automatically discharging foreign matter trapped in the filter cloth downstream of the solid-liquid separation means with respect to the direction of travel of the filter cloth, and receives the cleaning drainage. A drain tank 11 is provided. In addition, for convenience of explanation, an embodiment in which the self-cleaning type nozzle is provided in the surface washing means of the filter cloth will be described, but the self-cleaning type nozzle may be provided in any of the surface cleaning means and the backwash means of the filter cloth. , Or both.

【0013】自己洗浄型ノズル32は、図2に示すよう
に、タイマー18を有するポンプ12を備え、かつ、洗
浄を停止したときに滞留する洗浄用水を排出するための
洗浄流体抜出弁34を備えたパイプ33に設けられてい
る。洗浄流体抜出弁34によって、洗浄用水に含まれる
懸濁物質がパイプ内にこびりつくのを防止できる。
As shown in FIG. 2, the self-cleaning type nozzle 32 includes a pump 12 having a timer 18 and a cleaning fluid discharge valve 34 for discharging cleaning water remaining when cleaning is stopped. The pipe 33 is provided. The cleaning fluid discharge valve 34 can prevent suspended substances contained in the cleaning water from sticking in the pipe.

【0014】自己洗浄型ノズル32は、図3、4に示す
ように、本体54に、複数個のスプレーチップ51と、
スプリング55とを内蔵しており、スプレーチップ51
に作用する洗浄流体の圧力とスプリング55の復元力と
のバランスにより、スプレーチップ51が上下に移動す
ると共に下方に位置するときに桃割れするように構成さ
れている。
As shown in FIGS. 3 and 4, the self-cleaning type nozzle 32 includes a plurality of spray tips 51 on a main body 54.
A spring 55 and a built-in spray tip 51
Due to the balance between the pressure of the cleaning fluid acting on the spray tip and the restoring force of the spring 55, the spray tip 51 moves up and down and cracks when it is located below.

【0015】スプレーチップ51は、図5に示すように
基部59を基点に桃割れするようになっており、図3、
4に示すように、この上からスプリング55をかぶせる
とともに、基部59にリング状弾性部材56をはめこん
で、本体54内に設けられている。この状態では、スプ
レーチップ51は、図3に示すように桃割れした状態で
ある。
As shown in FIG. 5, the spray tip 51 is designed to crack at a base 59 as a starting point.
As shown in FIG. 4, a spring 55 is placed from above, and a ring-shaped elastic member 56 is fitted to the base 59, and is provided in the main body 54. In this state, the spray tip 51 is in a state of peach cracks as shown in FIG.

【0016】しかし、この自己洗浄型ノズル32にある
一定以上の圧力の洗浄流体が送られると、スプレーチッ
プ51の基部59にスプリング55の復元力よりも大き
な洗浄流体圧力がかかるため、図4に示すようにスプレ
ーチップは上方に押し上げられるとともに、縮径してい
る本体54の内面に沿ってスプレーチップ先端が合体し
洗浄流体噴出口58を形成する。
However, when a cleaning fluid having a certain pressure or more is sent to the self-cleaning nozzle 32, a cleaning fluid pressure greater than the restoring force of the spring 55 is applied to the base 59 of the spray tip 51. As shown, the spray tip is pushed upward and the tip of the spray tip merges along the inner surface of the reduced diameter body 54 to form a cleaning fluid outlet 58.

【0017】そして、洗浄流体を再びある一定以下の圧
力に下げると、スプリング55の復元力がスプレーチッ
プ51の基部59にかかる圧力に勝るため、図3に示す
ようにスプレーチップは再び下方へ押し下げられるとと
もに桃割れする。
When the cleaning fluid is again reduced to a certain pressure or less, the restoring force of the spring 55 exceeds the pressure applied to the base 59 of the spray tip 51, so that the spray tip is pushed down again as shown in FIG. And peach cracks.

【0018】このような自己洗浄型ノズルは、タイマー
などによって、洗浄流体をある一定値以上の圧力で供給
することと、ある一定値以下の圧力で供給することとを
繰り返すことで自己洗浄される。流体圧力をある一定値
以下に降下させた場合には、スプレーチップが桃割れ
し、スプレーチップから異物がノズル外へ排出される。
また、洗浄流体の供給を停止した場合にも、残留流体、
および、再起動時の噴出口が形成されるまでに供給され
る洗浄流体によって、異物はノズル外へ排出される。
Such a self-cleaning type nozzle is self-cleaned by repeatedly supplying a cleaning fluid at a pressure not lower than a certain value and supplying the cleaning fluid at a pressure not higher than a certain value by a timer or the like. . When the fluid pressure is reduced to a certain value or less, the spray tip breaks pink and foreign matter is discharged from the spray tip to the outside of the nozzle.
Also, when the supply of the cleaning fluid is stopped, the residual fluid,
In addition, the foreign matter is discharged to the outside of the nozzle by the cleaning fluid supplied until the ejection port at the time of restart is formed.

【0019】そして、この濾布走行式脱水機1には、さ
らに、洗浄排水の少なくとも一部と、減圧吸引槽6の減
圧により得られた濾液とを貯留しつつ、減圧ブロワー1
4による減圧を維持するシール槽10が設けられてお
り、ここに貯留された洗浄排水および濾液がタイマ−1
8制御付きのポンプ12によって洗浄手段13に還流さ
れる。また、還流される流体に含まれる懸濁物質を除去
するためのオートストレーナ15、および、オートスト
レーナ15によって除去した懸濁物質の抜き出し電磁弁
23も設けられている。なお、この抜き出し電磁弁23
には、タイマー19を設け、自動制御する。
The filter cloth traveling dehydrator 1 further stores at least a part of the washing wastewater and the filtrate obtained by reducing the pressure of the reduced-pressure suction tank 6 while reducing the pressure of the reduced-pressure blower 1.
4 is provided with a sealing tank 10 for maintaining the reduced pressure, and the washing wastewater and the filtrate stored in the sealing tank 10 are supplied with a timer-1.
It is returned to the washing means 13 by a pump 12 with 8 controls. Further, an auto strainer 15 for removing suspended substances contained in the fluid to be refluxed, and a solenoid valve 23 for extracting the suspended substances removed by the auto strainer 15 are also provided. Note that this extraction solenoid valve 23
Is provided with a timer 19 for automatic control.

【0020】ここで、シール槽10には、洗浄排水を流
入させずに濾液および新水(別途懸濁物質が除去された
浄化水)を流入させ、その貯留された流体を用いて濾布
の洗浄を行ってもよいが、本発明の構成においては、既
に一度洗浄に用いられた洗浄排水を還流させて、その洗
浄排水および濾液を主体にして濾布の洗浄を行うことが
できる。このような洗浄排水および濾液主体の濾布洗浄
は、従来の装置構成では濾布の目詰まりや処理量の低下
を招くので安定運転が不可能であったが、自己洗浄型ノ
ズル32および間欠的に洗浄流体供給圧力を変化させる
ことのできる洗浄流体供給手段を用いることによって、
濾布の目詰まりや処理量低下を防ぐことができ、その結
果洗浄排水の大量リサイクルが可能になる。また、洗浄
流体の流れ方向に関して自己洗浄型ノズルよりも上流側
にオートストレーナ15を加え用いることによって、新
水を用いず濾液および洗浄排水のみで濾布の洗浄が可能
になる。したがって、従来の固液分離装置では必要であ
った濾布洗浄用水としての新水の供給が不要になり、資
源の大幅な節約が可能になる。
Here, the filtrate and fresh water (purified water from which suspended substances have been separately removed) are allowed to flow into the sealing tank 10 without flowing the washing wastewater, and the stored fluid is used to remove the filter cloth. Although washing may be performed, in the configuration of the present invention, the washing wastewater already used for washing can be refluxed, and the washing of the filter cloth can be performed mainly using the washing wastewater and the filtrate. Such a washing drainage and a filter cloth washing mainly comprising a filtrate cannot be stably operated because clogging of the filter cloth and reduction of the processing amount are caused in the conventional apparatus configuration. However, the self-cleaning nozzle 32 and the intermittent By using the cleaning fluid supply means that can change the cleaning fluid supply pressure to
It is possible to prevent clogging of the filter cloth and a reduction in the treatment amount, and as a result, it becomes possible to recycle a large amount of cleaning wastewater. Further, by adding and using the auto strainer 15 on the upstream side of the self-cleaning type nozzle with respect to the flow direction of the cleaning fluid, the filter cloth can be cleaned only with the filtrate and the cleaning drainage without using new water. Therefore, it is not necessary to supply fresh water as filter cloth washing water, which is required in the conventional solid-liquid separation device, and it is possible to largely save resources.

【0021】上記の濾布走行式脱水機1において、濾布
2は、駆動ロール3によって図中矢印方向に周回してお
り、また、減圧吸引槽6は、減圧ブロワー14によって
内部が減圧されている。したがって、固液分離は、原液
供給槽5に供給された原液を、濾布2を介して減圧吸引
槽6側に強制吸引して、原液中の液体成分を減圧吸引槽
6へ吸引するとともに、固体成分を濾布で捕捉して行
う。そして、減圧吸引により得られた液体成分は一旦シ
ール槽10に貯留される。
In the above-described filter cloth traveling dehydrator 1, the filter cloth 2 is circulated in the direction of the arrow by the drive roll 3 and the inside of the reduced pressure suction tank 6 is reduced in pressure by the reduced pressure blower 14. I have. Therefore, in the solid-liquid separation, the undiluted solution supplied to the undiluted solution supply tank 5 is forcibly sucked into the reduced-pressure suction tank 6 through the filter cloth 2, and the liquid component in the undiluted solution is sucked into the reduced-pressure suction tank 6. This is performed by capturing the solid components with a filter cloth. Then, the liquid component obtained by the suction under reduced pressure is temporarily stored in the seal tank 10.

【0022】一方、分離された固形成分は、濾布2と共
に金属ドラム7と加圧ロール8などからなる加圧脱水手
段へ移動し、金属ドラム7と加圧ロール8によって挟圧
されることにより、さらに脱水されて金属ドラム7側に
転写される。金属ドラム7に転写された固形成分はスク
レーパー9で掻き取られ、ケーク状となってケーク受槽
17に落下する。
On the other hand, the separated solid component moves together with the filter cloth 2 to a pressurizing and dehydrating means comprising a metal drum 7 and a pressurizing roll 8 and is pressed by the metal drum 7 and the pressurizing roll 8. Is further dehydrated and transferred to the metal drum 7 side. The solid component transferred to the metal drum 7 is scraped off by the scraper 9, falls into a cake shape, and falls into the cake receiving tank 17.

【0023】ケークが除去された濾布2は、その後、自
己洗浄型ノズルを備えた洗浄手段13によってその表面
を洗浄し、また、必要に応じて、洗浄手段20によって
濾布2を裏面から洗浄する。この際、濾布2の洗浄は、
自動タイマー18等を用いて間欠的に行うことが好まし
い。タイマーによって自動的に間欠洗浄することで、自
己洗浄型ノズル32の目詰まりを防止できるとともに、
濾布2の目詰まり、濾過性能低下を防ぐことができる。
なお、濾布洗浄時間は、処理原液や洗浄用水の汚濁濃度
等に依存するが、自己洗浄ノズルが完全に詰まる前(洗
浄用水圧の変化だけでは対応できなくなる前)に運転の
停止・再開を繰り返し、頻繁にノズルから異物を吐出す
ることが好ましい。
The filter cloth 2 from which the cake has been removed is then washed on its front surface by a washing means 13 having a self-cleaning type nozzle, and, if necessary, by washing the filter cloth 2 from its back face by a washing means 20. I do. At this time, washing of the filter cloth 2
It is preferable to perform the operation intermittently using the automatic timer 18 or the like. By performing intermittent cleaning automatically by a timer, clogging of the self-cleaning nozzle 32 can be prevented,
It is possible to prevent the filter cloth 2 from being clogged and a filter performance from being lowered.
The cleaning time of the filter cloth depends on the concentration of the undiluted solution and the water used for cleaning, but the operation must be stopped and restarted before the self-cleaning nozzle is completely clogged (before the change in cleaning water pressure alone can no longer cope with it). It is preferable to repeatedly and frequently discharge foreign matter from the nozzle.

【0024】そして、洗浄排水は、弁21、22の開度
調整により少なくとも一部が一旦シール槽10に貯留さ
れ、残りの洗浄排水が排水槽11へ送出される。このシ
ール槽10の水は、ポンプ12によって、減圧吸引によ
り得られた液体成分と共に洗浄用水として洗浄手段13
へ還流される。このとき、オートストレーナ15によっ
て、供給する洗浄用水に含まれる懸濁物質が除去され
る。なお、シール槽の水量が一定量以上になると、水が
オーバーフローして排水槽11に流出し、また、不足す
る場合にはボールタッブ弁16を通して新水が補給され
る。
At least a part of the washing wastewater is temporarily stored in the seal tank 10 by adjusting the opening degrees of the valves 21 and 22, and the remaining washing wastewater is sent to the drain tank 11. The water in the seal tank 10 is used as washing water together with a liquid component obtained by suction under reduced pressure by a pump 12 as washing water 13.
Refluxed to At this time, the suspended material contained in the supplied washing water is removed by the auto strainer 15. When the amount of water in the seal tank exceeds a certain amount, the water overflows and flows out to the drain tank 11, and when it becomes insufficient, fresh water is supplied through the ball-tub valve 16.

【0025】なお、本発明において、原水は予め凝集処
理されていても良い。また、本発明において用いられる
自己洗浄型ノズルを備えた濾布洗浄手段と自己洗浄型ノ
ズルへの洗浄流体の供給圧力を間欠的に変更可能な洗浄
流体供給手段とを、回転ドラム式濾過機など他の形式の
固液分離装置に用いても好ましい。
In the present invention, the raw water may be subjected to a coagulation treatment in advance. Further, a filter cloth cleaning means having a self-cleaning type nozzle used in the present invention and a cleaning fluid supply means capable of intermittently changing the supply pressure of the cleaning fluid to the self-cleaning type nozzle are provided by a rotary drum type filter or the like. It is preferable to use it for other types of solid-liquid separation devices.

【0026】[0026]

【実施例】自己洗浄型ノズルを設けた洗浄手段を用いて
表洗を行う図1に示す装置を用いて(ただし洗浄手段2
0を使用せず)汚泥(無薬注)の固液分離を行った。な
お、実験条件は以下のとおりであった。 <運転条件> ポンプ12の圧力:3kg/cm2 ポンプ12の設定;作動5分、停止5秒 (タイマー18の設定:作動5分、停止5秒) オートストレーナ15のメッシュ:40mesh 抜き出し電磁弁23の設定:開放10秒、閉鎖60分 洗浄流体:洗浄排水全量および濾液 (弁21:全閉、弁22:全開、新水は用いない) 上記の実験の結果、自己洗浄型ノズルの目詰まりは一度
もなく、連続720時間(30日間)の安定運転を行え
た。また、汚泥処理量は、20kg−DS/Hr(標準
量)、SS回収率は70%であった。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An apparatus shown in FIG.
The solid-liquid separation of sludge (no chemical injection) was performed. The experimental conditions were as follows. <Operating conditions> Pressure of pump 12: 3 kg / cm 2 Setting of pump 12: operation 5 minutes, stop 5 seconds (setting of timer 18: operation 5 minutes, stop 5 seconds) Mesh of auto strainer 15: 40 mesh Extraction solenoid valve 23 Setting: opening 10 seconds, closing 60 minutes Washing fluid: total washing drainage and filtrate (Valve 21: Fully closed, Valve 22: Fully open, do not use fresh water) As a result of the above experiment, clogging of the self-cleaning type nozzle Stable operation for 720 hours (30 days) was performed without any success. Further, the sludge treatment amount was 20 kg-DS / Hr (standard amount), and the SS recovery rate was 70%.

【0027】[0027]

【発明の効果】本発明の固液分離装置は、自己洗浄型ノ
ズルを備えた濾布洗浄手段と自己洗浄型ノズルへの洗浄
流体の供給圧力を間欠的に変更可能な洗浄流体供給手段
とを備えているので、ノズルや濾布の目詰まりを防止で
き、固体成分と液体成分の分離脱水処理能力が安定す
る。また、ノズル詰まりによるメンテナンスを軽減する
ことができる。さらに、濾布の洗浄用水としての新水量
を低減することができ、運転費用を低減することができ
る。
The solid-liquid separator of the present invention comprises a filter cloth cleaning means having a self-cleaning nozzle and a cleaning fluid supply means capable of intermittently changing the supply pressure of the cleaning fluid to the self-cleaning nozzle. Since it is provided, clogging of the nozzle and the filter cloth can be prevented, and the ability to separate and dehydrate solid components and liquid components can be stabilized. Further, maintenance due to nozzle clogging can be reduced. Further, the amount of new water as washing water for the filter cloth can be reduced, and the operating cost can be reduced.

【0028】ここで、自己洗浄型ノズルを洗浄流体抜出
弁を備えたパイプに設けた場合には、運転停止時に洗浄
用水がパイプ内に滞留してその洗浄用水に含まれる懸濁
物質が付着するのを防ぐことができる。また、使用後の
洗浄流体の少なくとも一部を自己洗浄型ノズルに還流さ
せる還流手段を設け、さらに洗浄流体の流れ方向に関し
て自己洗浄型ノズルよりも上流側にオートストレーナを
設けた場合には、資源を大幅に節約することができる。
Here, when the self-cleaning type nozzle is provided on the pipe provided with the cleaning fluid discharge valve, the cleaning water stays in the pipe when the operation is stopped, and the suspended substance contained in the cleaning water adheres. Can be prevented. Further, in the case where a recirculation means for recirculating at least a part of the used cleaning fluid to the self-cleaning nozzle is provided, and an auto-strainer is provided on the upstream side of the self-cleaning nozzle with respect to the flow direction of the cleaning fluid, resources Can be greatly saved.

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

【図1】本発明の一実施態様を示す固液分離装置の概略
図である。
FIG. 1 is a schematic diagram of a solid-liquid separation device showing one embodiment of the present invention.

【図2】図1の洗浄手段を示す概略図である。FIG. 2 is a schematic diagram showing the cleaning means of FIG.

【図3】図2の自己洗浄型ノズルのスプレーチップが桃
割れした状態(クリーニング時)を示す概略縦断面図で
ある。
FIG. 3 is a schematic longitudinal sectional view showing a state in which a spray tip of the self-cleaning type nozzle of FIG.

【図4】図3の自己洗浄型ノズルのスプレーチップが合
体した状態(濾布洗浄時)を示す概略縦断面図である。
FIG. 4 is a schematic longitudinal sectional view showing a state in which the spray tips of the self-cleaning type nozzle of FIG. 3 are combined (during filter cloth cleaning).

【図5】図2の自己洗浄型ノズルのスプレーチップを示
す概略斜視図である。
FIG. 5 is a schematic perspective view showing a spray tip of the self-cleaning nozzle of FIG. 2;

【符号の説明】[Explanation of symbols]

1:濾布走行式脱水機 2:濾布 3:駆動ロール 4:ガイドロール 5:原液供給槽 6:減圧吸引槽 7:金属ドラム 8:加圧ロール 9:スクレーパー 10:シール槽 11:排水槽 12:ポンプ 13:洗浄手段 14:減圧ブロワー 15:オートストレーナ 16:ボールタップ弁 17:ケーク受槽 18:タイマー 19:タイマー 20:洗浄手段 21:弁 22:弁 23:抜き出し電磁弁 32:自己洗浄型ノズル 33:パイプ 34:洗浄流体抜出弁 51:スプレーチップ 54:本体 55:スプリング 56:リング状弾性部材 58:噴口部 59:基部 1: filter cloth traveling dehydrator 2: filter cloth 3: drive roll 4: guide roll 5: stock solution supply tank 6: reduced pressure suction tank 7: metal drum 8: pressure roll 9: scraper 10: seal tank 11: drain tank 12: Pump 13: Cleaning means 14: Decompression blower 15: Auto strainer 16: Ball tap valve 17: Cake receiving tank 18: Timer 19: Timer 20: Cleaning means 21: Valve 22: Valve 23: Extraction solenoid valve 32: Self-cleaning nozzle 33: Pipe 34: Cleaning fluid extraction valve 51: Spray tip 54: Main body 55: Spring 56: Ring-shaped elastic member 58: Injection port 59: Base

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】濾布走行手段と、濾布の表面側に設けた原
液供給手段と、濾布の裏面側で、かつ、原液供給手段に
対向して設けた減圧吸引手段と、濾布走行方向に関して
減圧吸引手段よりも下流側に設けた加圧脱水手段と、自
己洗浄型ノズルを備えた濾布洗浄手段と、自己洗浄型ノ
ズルへの洗浄流体の供給圧力を間欠的に変更可能な洗浄
流体供給手段とを有していることを特徴とする固液分離
装置。
1. A filter cloth traveling means, a stock solution supply means provided on the front side of the filter cloth, a reduced pressure suction means provided on the back side of the filter cloth and opposed to the stock solution supply means, Pressure dewatering means provided downstream of the vacuum suction means in the direction, filter cloth cleaning means having a self-cleaning nozzle, and cleaning capable of intermittently changing the supply pressure of the cleaning fluid to the self-cleaning nozzle A solid-liquid separation device comprising: a fluid supply unit.
【請求項2】自己洗浄型ノズルは、本体内に設けた桃割
れ自在な複数個のスプレーチップとばねとを有し、複数
個のスプレーチップは、スプレーチップに作用する洗浄
流体の圧力とばねの復元力とのバランスにより上下に移
動するとともに下方に位置するときに桃割れするように
構成されている、請求項1に記載の固液分離装置。
2. The self-cleaning type nozzle has a plurality of peach-sprayable spray tips and a spring provided in a main body of the nozzle, and the plurality of spray tips includes a pressure of a cleaning fluid acting on the spray tip and a spring. 2. The solid-liquid separation device according to claim 1, wherein the solid-liquid separation device is configured to move up and down according to a balance with a restoring force and to be cracked when located below.
【請求項3】複数個のスプレーチップは、スプレーチッ
プに作用する洗浄流体の圧力がばねの復元力よりも大き
いときに合体し、洗浄流体の圧力がばねの復元力よりも
小さいときに桃割れする、請求項2に記載の固液分離装
置。
3. A plurality of spray tips unite when the pressure of the cleaning fluid acting on the spray tip is greater than the restoring force of the spring, and when the pressure of the cleaning fluid is smaller than the restoring force of the spring, the plurality of spray tips break. The solid-liquid separation device according to claim 2, wherein
【請求項4】使用後の洗浄流体の少なくとも一部を自己
洗浄型ノズルに還流させる還流手段を設けた、請求項1
〜3のいずれかに記載の固液分離装置。
4. A recirculation means for recirculating at least a part of the used cleaning fluid to the self-cleaning nozzle.
4. The solid-liquid separation device according to any one of claims 1 to 3.
【請求項5】自己洗浄型ノズルを、洗浄流体抜出弁を備
えたパイプに設けた、請求項1〜4のいずれかに記載の
固液分離装置。
5. The solid-liquid separation device according to claim 1, wherein the self-cleaning type nozzle is provided in a pipe provided with a cleaning fluid discharge valve.
【請求項6】洗浄流体の流れ方向に関して自己洗浄型ノ
ズルよりも上流側にオートストレーナを設けた、請求項
1〜5のいずれかに記載の固液分離装置。
6. The solid-liquid separation device according to claim 1, wherein an auto-strainer is provided upstream of the self-cleaning nozzle with respect to the flow direction of the cleaning fluid.
【請求項7】請求項1〜6のいずれかに記載の固液分離
装置を用いることを特徴とする造水方法。
7. A fresh water producing method using the solid-liquid separation device according to any one of claims 1 to 6.
JP11086269A 1999-03-29 1999-03-29 Solid-liquid separation apparatus Pending JP2000279715A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11086269A JP2000279715A (en) 1999-03-29 1999-03-29 Solid-liquid separation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11086269A JP2000279715A (en) 1999-03-29 1999-03-29 Solid-liquid separation apparatus

Publications (1)

Publication Number Publication Date
JP2000279715A true JP2000279715A (en) 2000-10-10

Family

ID=13882111

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2000279715A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020069630A (en) * 2001-02-27 2002-09-05 임창성 Method of drying industrial sludge through continuous suction process
KR20020069633A (en) * 2001-02-27 2002-09-05 임창성 Drying system of industrial sludge through continuous suction process
JP2010069390A (en) * 2008-09-17 2010-04-02 Ishigaki Co Ltd Method for operating and controlling belt type concentrator
JP2010137187A (en) * 2008-12-15 2010-06-24 Tsukishima Kikai Co Ltd Belt-type concentrator and method for operating the same
JP2010142740A (en) * 2008-12-19 2010-07-01 Tsukishima Kikai Co Ltd Belt-type concentrator and method for operating the same
JP2014144428A (en) * 2013-01-29 2014-08-14 Metawater Co Ltd Sludge dehydrating system
CN105498340A (en) * 2015-12-29 2016-04-20 徐旭 Solid-liquid separation method and solid-liquid separation device for water body
JP2016182582A (en) * 2015-03-27 2016-10-20 株式会社クボタ Belt cleaner of belt-type filtration thickener
WO2017107113A1 (en) * 2015-12-23 2017-06-29 陈良娟 Device for separating solids from liquids

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020069630A (en) * 2001-02-27 2002-09-05 임창성 Method of drying industrial sludge through continuous suction process
KR20020069633A (en) * 2001-02-27 2002-09-05 임창성 Drying system of industrial sludge through continuous suction process
JP2010069390A (en) * 2008-09-17 2010-04-02 Ishigaki Co Ltd Method for operating and controlling belt type concentrator
JP2010137187A (en) * 2008-12-15 2010-06-24 Tsukishima Kikai Co Ltd Belt-type concentrator and method for operating the same
JP2010142740A (en) * 2008-12-19 2010-07-01 Tsukishima Kikai Co Ltd Belt-type concentrator and method for operating the same
JP2014144428A (en) * 2013-01-29 2014-08-14 Metawater Co Ltd Sludge dehydrating system
JP2016182582A (en) * 2015-03-27 2016-10-20 株式会社クボタ Belt cleaner of belt-type filtration thickener
WO2017107113A1 (en) * 2015-12-23 2017-06-29 陈良娟 Device for separating solids from liquids
CN105498340A (en) * 2015-12-29 2016-04-20 徐旭 Solid-liquid separation method and solid-liquid separation device for water body

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