JP2000062833A - Solid and liquid separating device - Google Patents

Solid and liquid separating device

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Publication number
JP2000062833A
JP2000062833A JP10234303A JP23430398A JP2000062833A JP 2000062833 A JP2000062833 A JP 2000062833A JP 10234303 A JP10234303 A JP 10234303A JP 23430398 A JP23430398 A JP 23430398A JP 2000062833 A JP2000062833 A JP 2000062833A
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JP
Japan
Prior art keywords
filtration
solid
water
filtering
tank
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
JP10234303A
Other languages
Japanese (ja)
Inventor
Masaaki Yoshino
正章 吉野
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.)
Maezawa Industries Inc
Original Assignee
Maezawa 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 Maezawa Industries Inc filed Critical Maezawa Industries Inc
Priority to JP10234303A priority Critical patent/JP2000062833A/en
Publication of JP2000062833A publication Critical patent/JP2000062833A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a solid and liquid separating device capable of attaining a sufficient filtering area even under a narrow mounting area, capable of providing a sufficient filtering rate and further capable of easily performing its maintenance work. SOLUTION: Two planer filtering members are faced against to each other by a predetermined space. Within a solid liquid separating tank 3 is mounted a filtering device 2 in which a plurality of filter modules having their outer circumferential portions sealingly closed by a frame member are held by a spacer in a predetermined space. The inside part of the filtering modules and the outside part of the solid liquid separating tank are communicated with a water supplying port, and at the same time there is provided a cleaning nozzle 4 for injecting cleaning water toward the filtering surface of each of the filtering modules.

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は、固液分離装置に関
し、特に、下水処理場の二次処理水中に含まれる浮遊性
固形物を分離除去するための高度処理に用いるのに最適
な固液分離装置に関する。 【0002】 【従来の技術】下水処理においては、従来の二次処理に
加え、水資源の再利用,親水域の創出等、高度処理の重
要性が高まってきている。下水の高度処理の第一歩は、
ろ過による浮遊性固形物の除去であり、一般的に急速ろ
過法やマイクロストレーナーが用いられている。 【0003】 【発明が解決しようとする課題】しかしながら、急速ろ
過法では、ろ過速度に限度があり、装置のコンパクト化
が困難で、広い面積を必要とする。また、マイクロスト
レーナーは、ろ過速度は高いものの、ろ過面積が水中に
浸漬している円筒面のみであるため、大量の処理を行う
場合には、同様に広い設置面積を必要とする。 【0004】そこで本発明は、狭い設置面積でも十分な
ろ過面積を得ることができ、ろ過速度に優れるととも
に、メンテナンスも容易に行うことができる固液分離装
置を提供することを目的としている。 【0005】 【課題を解決するための手段】上記目的を達成するた
め、本発明の固液分離装置は、2枚の面状ろ過材を所定
間隔で向い合わせ、その外周部を枠材で密閉した複数の
ろ過モジュールをスペーサーにより所定間隔で保持して
固液分離槽内に設置し、前記ろ過モジュール内と固液分
離槽外とを通水口により連通させるとともに、ろ過モジ
ュールのろ過面に向けて洗浄水を噴出する洗浄ノズルを
設けたことを特徴としている。 【0006】 【発明の実施の形態】図1乃至図4は、本発明の固液分
離装置の一形態例を示すもので、図1は固液分離装置の
周辺機器の設置例を示す系統図、図2はろ過ユニットの
側面図、図3は同じく平面図、図4は固液分離装置の使
用例を示す系統図である。 【0007】この固液分離装置1は、複数枚の面状ろ過
材を使用したろ過ユニット2を固液分離槽3内に設置す
るとともに、ろ過ユニット2の上方に洗浄ノズル4を設
けたものである。 【0008】ろ過ユニット2は、図2及び図3に示すよ
うに、微細目スクリーンやろ布等の面状ろ過材5を2枚
向い合わせにしてその外周部を枠材6で密閉した複数の
ろ過モジュール7を、スペーサー8により所定間隔で保
持して鉛直方向に配置したものであって、ろ過モジュー
ル7の側方の枠材6の一部には、スリット状の通水口9
が形成されている。また、前記洗浄ノズル4は、ろ過モ
ジュール7の両面のろ過面に向けて洗浄水を散布するこ
とができるような位置に設置されている。 【0009】前記通水口9は、固液分離槽3の側壁に設
けた開口10を介して固液分離槽3内を所定以上の水位
に保つための溢流室11に接続されており、面状ろ過材
5を通過した処理水は、溢流室11の堰11aをオーバ
ーフローして処理水槽12に流下するように形成されて
いる。 【0010】また、固液分離槽3の上部には、原水流入
弁13Vを備えた原水流入経路13が設けられ、固液分
離槽3の底部には、排水弁14Vを備えた排水経路14
が設けられている。さらに、排水経路14の下方には、
洗浄排水等を受ける排水槽15が設けられており、排水
槽15には、揚水ポンプ16Pを備えた排水導出経路1
6が設けられている。 【0011】前記処理水槽12には、処理水流出経路1
7が設けられるとともに、処理水の一部を前記洗浄ノズ
ル4に供給するための洗浄ポンプ18P,洗浄弁18V
を有する洗浄経路18が設けられている。さらに、この
洗浄経路18には、薬液ポンプ19P,薬液供給弁19
Vを有する薬液供給経路19を介して薬液貯留槽20が
接続されている。 【0012】このように形成した固液分離装置1は、図
4の系統図に示すように、下水処理場の最終沈殿池21
の後段に設けられ、最終沈殿池21で処理した二次処理
水の三次処理を行う装置として用いることができる。 【0013】すなわち、最終沈殿池21の越流堰22か
ら越流した二次処理水は、前記原水流入経路13を経て
固液分離槽3内に自然流下により流入し、二次処理水中
に残存した浮遊性固形物をろ過ユニット2の面状ろ過材
で分離除去する三次処理が行われる。固液分離装置1で
処理された三次処理水は、処理水槽(三次処理水槽)1
2から処理水路23を経て河川等に放流される。これに
より、下水処理場における高度処理が行われ、水資源の
再利用等に寄与することができる。 【0014】図5乃至図9は、固液分離装置1における
一連の処理操作を示すものである。なお、図5乃至図9
では、主要部分のみを説明する。 【0015】まず、図5は、通常のろ過工程の状態を示
すもので、原水流入弁13Vが開、排水弁14Vが閉で
あり、揚水ポンプ16P及び洗浄ポンプ18Pは停止し
ている。原水流入経路13から固液分離槽3内に流入し
た原水(二次処理水)は、ろ過ユニット2の面状ろ過材
でろ過処理され、溢流室11を経て処理水槽(三次処理
水槽)12に流出する。 【0016】このとき、二次処理水中の浮遊性固形物の
うち、大きさの小さいものは、ろ過処理の初期において
ろ過材を通過するが、ろ過面上に汚泥ケーキ層が形成さ
れると、該汚泥ケーキ層でもろ過が行われるため、ろ過
運転開始後、短時間で良好な処理水が得られる。 【0017】ろ過処理の進行に伴い、ろ過面が抑留懸濁
物によって閉塞されてくると、図6に示すように、固液
分離槽3内の水位が次第に上昇してくる。この水位の上
昇をフロートスイッチ等により検出し、設定水位に達し
たときにろ過運転を停止し、ろ過面の洗浄工程に移る。 【0018】洗浄工程は、まず、図7に示すように、原
水流入弁13Vを閉じて排水弁14Vを開き、固液分離
槽3内の水を排水槽15に排出してろ過ユニット2のろ
過面を露出させる排水操作を行う。また、揚水ポンプ1
6Pを運転して排水槽15内の排水を沈砂池や最初沈殿
池に戻す。 【0019】次に、洗浄ポンプ18Pを運転して処理水
槽12内の処理水を洗浄ノズル4に供給し、図8に示す
ように、洗浄ノズル4からろ過面に向けて処理水(洗浄
水)を噴出させる。これにより、ろ過面の抑留懸濁物が
洗浄水により洗い流され、洗浄後の水と共に排水経路1
4から排水槽15に流れ落ち、沈砂池等の前処理設備に
戻される。 【0020】このとき、洗浄ノズル4から噴出する洗浄
水がろ過面に対して略平行な方向に流れるので、洗浄水
がろ過面に向かって強く当たることがなく、ろ過材に損
傷を与えることがほとんどないから、ある程度の高圧洗
浄水を用いて効果的な洗浄を行うことができる。さら
に、ろ過面を気相に露出させて行うので、洗浄水が有す
る運動量をろ過面に直接作用させることができ、洗浄効
率に優れており、ろ過面表面の抑留懸濁物を短時間で除
去することができる。 【0021】また、ろ過ユニット2を固液分離槽3内に
設置したまま、弁やポンプを操作するだけでろ過面の洗
浄を行うことができるので、自動的に、かつ、短時間で
行うことができるとともに、洗浄時に汚泥等が飛散して
も外部に飛び散ることがない。しかも、洗浄水として、
処理水槽12に貯留した処理水を用いるので、洗浄ノズ
ル4に目詰まりが発生することはほとんどなく、維持管
理も容易である。 【0022】所定の洗浄操作を終了したら、洗浄ポンプ
18Pを停止するとともに、排水弁14Vを閉じて原水
流入弁13Vを開く。これにより、原水流入経路13か
ら固液分離槽3内に二次処理水が流入し、最初の図5に
示した状態に戻る。なお、揚水ポンプ16Pは、排水槽
15内の状況に応じて適当に停止させればよい。 【0023】このように、最終沈殿池21の越流堰22
の水位と処理水路23の水位とに適当な水位差があり、
さらに、水路内に適当な空間がある場合は、固液分離装
置1からなるろ過設備を処理水路内に組み込むことがで
きる。この場合、二次処理水は、自然流下によりろ過設
備を流れるため、新たに揚水設備を設置する必要がな
い。特に、最終沈殿池21の後段の限られたスペースの
水路内であっても、多数の面状ろ過材を狭い間隔で平行
に設置するため、ろ過面積を大きくとることができ、大
量の二次処理水をろ過処理することができる。 【0024】一方、長時間のろ過運転により、ろ過面に
微生物が繁殖すると、最悪の場合、ろ過材を閉塞させて
しまう。したがって、適当な時期に薬液等によりろ過面
の微生物(生物スライム)を除去する処理を行う必要が
ある。 【0025】この生物スライムの除去は、ろ過ユニット
2を薬液洗浄槽等に移して行うこともできるが、次亜塩
素酸ナトリウム溶液やオゾン溶解水等の薬液を前記薬液
貯留槽20から薬液供給経路19を介して洗浄ノズル4
に供給し、ろ過面に向けて噴出させることによって行う
ことができる。また、薬液に代えて高温水や高温蒸気等
を用いることもでき、これらを併用することもできる。 【0026】この薬液洗浄においても、ろ過面を気相に
露出させた状態で洗浄ノズル4から散布することにより
行えるので、薬液の使用量も少なくて済み、使用後の薬
液の処理も容易となる。 【0027】また、薬液洗浄を行うときには、その前後
に水洗浄を行う必要があるが、前述のような洗浄工程を
行うことによって同等の効果が得られるので、特別な水
洗浄を行う必要がなくなり、薬液洗浄に要する時間や労
力を削減できる。 【0028】なお、洗浄ノズル4の設置位置や設置数
は、ろ過ユニット2の大きさなどによって任意に選択す
ることができ、側方あるいは下方にも設置することがで
きるが、メンテナンスや目詰まり、洗浄水の飛散等を考
慮すると、ろ過ユニット2の上方が最適である。また、
洗浄水には任意の水を用いることができ、洗浄ノズル4
の形状も任意であるが、洗浄水をろ過面全体にスプレー
できる形式のものが好ましく、ヘッドが自動的に首振り
を行うものを使用することもできる。 【0029】さらに、隣接するろ過モジュール7を所定
間隔に保持するスペーサー8は、棒状のもののほか、ピ
ース状のものを適当な位置に適当な個数設置するように
してもよい。 【0030】 【発明の効果】以上説明したように、本発明の固液分離
装置によれば、ろ過材の洗浄を極めて容易に効率よく行
うことができるので、ろ過材の間隔を大幅に狭めること
ができる。したがって、狭い設置面積でも十分なろ過面
積を得ることができ、ろ過速度にも優れるとともに、メ
ンテナンスも容易に行うことができる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid-liquid separation apparatus, and more particularly to a solid-liquid separation apparatus for separating and removing suspended solids contained in secondary treatment water in a sewage treatment plant. The present invention relates to a solid-liquid separation device optimal for use in advanced processing. 2. Description of the Related Art In sewage treatment, in addition to the conventional secondary treatment, the importance of advanced treatment such as reuse of water resources and creation of a hydrophilic area is increasing. The first step in advanced sewage treatment is
This is removal of suspended solids by filtration, and a rapid filtration method and a microstrainer are generally used. [0003] However, in the rapid filtration method, the filtration speed is limited, it is difficult to make the apparatus compact, and a large area is required. In addition, although the microstrainer has a high filtration speed, the filtration area is only a cylindrical surface immersed in water, so that a large installation area is required when performing a large amount of processing. [0004] Therefore, an object of the present invention is to provide a solid-liquid separator capable of obtaining a sufficient filtration area even with a small installation area, having an excellent filtration speed, and easily performing maintenance. [0005] In order to achieve the above object, a solid-liquid separation device of the present invention faces two planar filter media at a predetermined interval, and seals the outer peripheral portion thereof with a frame material. A plurality of filtration modules are held at predetermined intervals by a spacer and installed in a solid-liquid separation tank, and the inside of the filtration module and the outside of the solid-liquid separation tank are communicated with each other through a water inlet, and the filtration module is directed toward the filtration surface of the filtration module. It is characterized in that a washing nozzle for jetting washing water is provided. 1 to 4 show an embodiment of a solid-liquid separator according to the present invention. FIG. 1 is a system diagram showing an example of installation of peripheral devices of the solid-liquid separator. FIG. 2 is a side view of the filtration unit, FIG. 3 is a plan view of the same, and FIG. 4 is a system diagram showing an example of use of the solid-liquid separation device. The solid-liquid separation device 1 is provided with a filtration unit 2 using a plurality of sheet filtration materials in a solid-liquid separation tank 3 and a washing nozzle 4 provided above the filtration unit 2. is there. As shown in FIG. 2 and FIG. 3, the filtration unit 2 includes a plurality of filtration media 5 in which two planar filter media 5 such as a fine mesh screen and a filter cloth are opposed to each other and the outer periphery thereof is sealed with a frame 6. The module 7 is vertically arranged while being held at a predetermined interval by a spacer 8, and a part of the frame member 6 on the side of the filtration module 7 is provided with a slit-shaped water passage 9
Are formed. Further, the washing nozzle 4 is installed at a position where the washing water can be sprayed toward the filtration surfaces on both sides of the filtration module 7. The water passage 9 is connected to an overflow chamber 11 for keeping the inside of the solid-liquid separation tank 3 at a predetermined water level or higher through an opening 10 provided in a side wall of the solid-liquid separation tank 3. The treated water that has passed through the filter medium 5 is formed so as to overflow the weir 11 a of the overflow chamber 11 and flow down to the treated water tank 12. A raw water inflow path 13 having a raw water inflow valve 13V is provided above the solid / liquid separation tank 3, and a drainage path 14 having a drain valve 14V is provided at the bottom of the solid / liquid separation tank 3.
Is provided. Further, below the drainage path 14,
A drainage tank 15 for receiving washing drainage and the like is provided, and the drainage tank 15 has a drainage lead-out path 1 equipped with a pumping pump 16P.
6 are provided. The treated water tank 12 has a treated water outflow path 1
7 and a cleaning pump 18P and a cleaning valve 18V for supplying a part of the treatment water to the cleaning nozzle 4.
Is provided. Further, the cleaning path 18 includes a chemical solution pump 19P and a chemical solution supply valve 19.
A chemical storage tank 20 is connected via a chemical supply path 19 having V. As shown in the system diagram of FIG. 4, the solid-liquid separation device 1 formed as described above has a final sedimentation basin 21 of a sewage treatment plant.
It can be used as a device that is provided at the subsequent stage and performs tertiary treatment of the secondary treated water treated in the final sedimentation basin 21. That is, the secondary effluent flowing from the overflow weir 22 of the final sedimentation basin 21 flows into the solid-liquid separation tank 3 via the raw water inflow path 13 by natural flow, and remains in the secondary effluent. A tertiary treatment of separating and removing the suspended solids thus separated by the planar filter material of the filtration unit 2 is performed. The tertiary treated water treated by the solid-liquid separator 1 is treated in a treated water tank (tertiary treated water tank) 1
From 2 the water is discharged to a river or the like via the treated water channel 23. Thereby, the advanced treatment in the sewage treatment plant is performed, which can contribute to the reuse of water resources and the like. FIGS. 5 to 9 show a series of processing operations in the solid-liquid separation device 1. FIG. 5 to 9.
Now, only the main part will be described. First, FIG. 5 shows a state of a normal filtration step. The raw water inflow valve 13V is open, the drain valve 14V is closed, and the water pump 16P and the washing pump 18P are stopped. Raw water (secondary treated water) flowing into the solid-liquid separation tank 3 from the raw water inflow path 13 is filtered by the planar filter material of the filtration unit 2, passed through the overflow chamber 11, and treated water tank (tertiary treated water tank) 12. Leaked to At this time, among the suspended solids in the secondary treatment water, those having a small size pass through the filter medium at the beginning of the filtration treatment, but when a sludge cake layer is formed on the filtration surface, Since the sludge cake layer is also filtered, good treated water can be obtained in a short time after the start of the filtration operation. As the filtration process progresses, when the filtration surface is clogged with the suspended matter, the water level in the solid-liquid separation tank 3 gradually rises as shown in FIG. This rise in the water level is detected by a float switch or the like, and when the water level reaches the set water level, the filtration operation is stopped, and the process proceeds to the step of cleaning the filtration surface. In the cleaning step, first, as shown in FIG. 7, the raw water inflow valve 13V is closed, the drain valve 14V is opened, the water in the solid-liquid separation tank 3 is discharged to the drain tank 15, and the filtration of the filtration unit 2 is performed. Perform drainage operation to expose the surface. In addition, pump 1
6P is operated to return the wastewater in the drainage tank 15 to the settling basin or the first settling basin. Next, the cleaning pump 18P is operated to supply the processing water in the processing water tank 12 to the cleaning nozzle 4, and as shown in FIG. 8, the processing water (cleaning water) flows from the cleaning nozzle 4 toward the filtration surface. Squirt. As a result, the suspended matter on the filtration surface is washed away by the washing water, and together with the washed water, the drainage path 1 is removed.
From 4, it flows down to a drain tank 15 and is returned to pretreatment equipment such as a sand basin. At this time, since the washing water ejected from the washing nozzle 4 flows in a direction substantially parallel to the filtering surface, the washing water does not strongly hit the filtering surface, and the filter material may be damaged. Since there is almost no washing, effective washing can be performed using a certain amount of high-pressure washing water. Furthermore, since the filtration surface is exposed to the gas phase, the momentum of the washing water can be directly applied to the filtration surface, and the cleaning efficiency is excellent, and the suspended solids on the filtration surface can be removed in a short time. can do. In addition, since the filtration surface can be washed only by operating a valve or a pump while the filtration unit 2 is installed in the solid-liquid separation tank 3, the filtration can be performed automatically and in a short time. And even if sludge or the like scatters during washing, it does not scatter outside. And as washing water,
Since the treated water stored in the treated water tank 12 is used, clogging of the washing nozzle 4 hardly occurs, and maintenance is easy. When the predetermined washing operation is completed, the washing pump 18P is stopped, the drain valve 14V is closed, and the raw water inflow valve 13V is opened. As a result, the secondary treated water flows into the solid-liquid separation tank 3 from the raw water inflow path 13 and returns to the initial state shown in FIG. Note that the pump 16P may be appropriately stopped according to the situation in the drainage tank 15. As described above, the overflow weir 22 of the final sedimentation basin 21
There is an appropriate water level difference between the water level of
Further, when there is an appropriate space in the water channel, a filtration facility including the solid-liquid separation device 1 can be incorporated in the treatment water channel. In this case, since the secondary treated water flows through the filtration equipment by natural flow, it is not necessary to newly install a pumping equipment. In particular, even in the water channel of the limited space after the final sedimentation basin 21, since a large number of planar filter media are installed in parallel at narrow intervals, the filtration area can be increased, and a large amount of secondary The treated water can be filtered. On the other hand, if microorganisms proliferate on the filtration surface due to a long filtration operation, in the worst case, the filtration material will be blocked. Therefore, it is necessary to perform a treatment for removing microorganisms (biological slime) on the filtration surface by using a chemical solution or the like at an appropriate time. This biological slime can be removed by moving the filtration unit 2 to a chemical washing tank or the like. However, a chemical such as sodium hypochlorite solution or ozone-dissolved water is supplied from the chemical storage tank 20 to the chemical supply path. Washing nozzle 4 through 19
And ejecting it toward the filtration surface. In addition, high-temperature water, high-temperature steam, or the like can be used instead of the chemical solution, and these can be used together. This chemical cleaning can also be performed by spraying from the cleaning nozzle 4 in a state where the filtration surface is exposed to the gas phase, so that the amount of the chemical used can be reduced, and the treatment of the chemical after use becomes easy. . When the chemical cleaning is performed, it is necessary to perform water cleaning before and after the cleaning. However, since the same effect can be obtained by performing the above-described cleaning process, it is not necessary to perform a special water cleaning. In addition, the time and labor required for chemical cleaning can be reduced. The installation position and the number of the washing nozzles 4 can be arbitrarily selected depending on the size of the filtration unit 2 and the like, and can be installed on the side or below. The upper part of the filtration unit 2 is optimal in consideration of scattering of washing water. Also,
Arbitrary water can be used for the cleaning water.
The shape is arbitrary, but a type in which the washing water can be sprayed over the entire filtration surface is preferable, and a type in which the head automatically swings can also be used. Further, the spacers 8 for holding the adjacent filtration modules 7 at a predetermined interval may be provided in an appropriate number of pieces at a suitable position in addition to a rod-like spacer. As described above, according to the solid-liquid separation apparatus of the present invention, the filtration material can be washed very easily and efficiently, so that the interval between the filtration materials can be greatly reduced. Can be. Therefore, a sufficient filtration area can be obtained even with a small installation area, the filtration speed is excellent, and the maintenance can be easily performed.

【図面の簡単な説明】 【図1】 固液分離装置の周辺機器の設置例を示す系統
図である。 【図2】 ろ過ユニットの一形態例を示す側面図であ
る。 【図3】 同じく平面図である。 【図4】 固液分離装置の使用例を示す系統図である。 【図5】 ろ過工程の状態を示す説明図である。 【図6】 ろ過工程終了時の状態を示す説明図である。 【図7】 洗浄工程前の排水操作の状態を示す説明図で
ある。 【図8】 洗浄工程の状態を示す説明図である。 【図9】 洗浄工程からろ過工程に切替わる状態を示す
説明図である。 【符号の説明】 1…固液分離装置、2…ろ過ユニット、3…固液分離
槽、4…洗浄ノズル、5…面状ろ過材、6…枠材、7…
ろ過モジュール、8…スペーサー、9…通水口、10…
開口、11…溢流室、12…処理水槽、13…原水流入
経路、14…排水経路、15…排水槽、16…排水導出
経路、17…処理水流出経路、18…洗浄経路、19…
薬液供給経路、20…薬液貯留槽、21…最終沈殿池、
22…越流堰、23…処理水路
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a system diagram showing an installation example of peripheral devices of a solid-liquid separation device. FIG. 2 is a side view showing one embodiment of a filtration unit. FIG. 3 is a plan view of the same. FIG. 4 is a system diagram showing an example of using a solid-liquid separation device. FIG. 5 is an explanatory diagram showing a state of a filtration step. FIG. 6 is an explanatory diagram showing a state at the end of a filtration step. FIG. 7 is an explanatory diagram showing a state of a drain operation before a cleaning step. FIG. 8 is an explanatory view showing a state of a cleaning step. FIG. 9 is an explanatory diagram showing a state in which a washing step is switched to a filtration step. [Description of Signs] 1 ... solid-liquid separation device, 2 ... filtration unit, 3 ... solid-liquid separation tank, 4 ... washing nozzle, 5 ... planar filter material, 6 ... frame material, 7 ...
Filtration module, 8 ... spacer, 9 ... water inlet, 10 ...
Opening, 11: Overflow chamber, 12: Treated water tank, 13: Raw water inflow path, 14: Drainage path, 15: Drainage tank, 16: Drainage discharge path, 17: Treated water outflow path, 18: Washing path, 19 ...
Chemical solution supply path, 20 ... chemical solution storage tank, 21 ... final sedimentation basin,
22: overflow weir, 23: treated water channel

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 29/38 520C 560 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (Reference) B01D 29/38 520C 560

Claims (1)

【特許請求の範囲】 【請求項1】 2枚の面状ろ過材を所定間隔で向い合わ
せ、その外周部を枠材で密閉した複数のろ過モジュール
をスペーサーにより所定間隔で保持して固液分離槽内に
設置し、前記ろ過モジュール内と固液分離槽外とを通水
口により連通させるとともに、ろ過モジュールのろ過面
に向けて洗浄水を噴出する洗浄ノズルを設けたことを特
徴とする固液分離装置。
Claims: 1. Solid-liquid separation by holding a plurality of filtration modules with two sheet filters facing each other at a predetermined interval and sealing the outer peripheral portions of the filtration modules at a predetermined interval with a spacer. A liquid nozzle provided in the tank, and having a water inlet communicating with the inside of the filtration module and the outside of the solid-liquid separation tank, and a washing nozzle for jetting washing water toward a filtration surface of the filtration module. Separation device.
JP10234303A 1998-08-20 1998-08-20 Solid and liquid separating device Pending JP2000062833A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10234303A JP2000062833A (en) 1998-08-20 1998-08-20 Solid and liquid separating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10234303A JP2000062833A (en) 1998-08-20 1998-08-20 Solid and liquid separating device

Publications (1)

Publication Number Publication Date
JP2000062833A true JP2000062833A (en) 2000-02-29

Family

ID=16968893

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10234303A Pending JP2000062833A (en) 1998-08-20 1998-08-20 Solid and liquid separating device

Country Status (1)

Country Link
JP (1) JP2000062833A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002320827A (en) * 2001-04-25 2002-11-05 Maezawa Ind Inc Solid-liquid separation equipment
CN103931734A (en) * 2014-04-23 2014-07-23 昆山市富众网络科技有限公司 Magnetic filter device for crab shell enzymolytic tank
CN103931733A (en) * 2014-04-23 2014-07-23 昆山市富众网络科技有限公司 Filter device for crab shell enzymolysis pool
CN108452564A (en) * 2018-01-31 2018-08-28 河南桑达能源环保有限公司 A kind of vertical sewage treatment device with self-cleaning function
CN115057504A (en) * 2022-06-29 2022-09-16 山东通广环保设备有限公司 Novel built-in back flush micro-filter

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002320827A (en) * 2001-04-25 2002-11-05 Maezawa Ind Inc Solid-liquid separation equipment
CN103931734A (en) * 2014-04-23 2014-07-23 昆山市富众网络科技有限公司 Magnetic filter device for crab shell enzymolytic tank
CN103931733A (en) * 2014-04-23 2014-07-23 昆山市富众网络科技有限公司 Filter device for crab shell enzymolysis pool
CN108452564A (en) * 2018-01-31 2018-08-28 河南桑达能源环保有限公司 A kind of vertical sewage treatment device with self-cleaning function
CN108452564B (en) * 2018-01-31 2021-02-02 河南桑达能源环保有限公司 Vertical sewage treatment ware with from clearance function
CN115057504A (en) * 2022-06-29 2022-09-16 山东通广环保设备有限公司 Novel built-in back flush micro-filter

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