JP3698297B2 - Filter media cleaning and recycling equipment - Google Patents

Filter media cleaning and recycling equipment Download PDF

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Publication number
JP3698297B2
JP3698297B2 JP23546699A JP23546699A JP3698297B2 JP 3698297 B2 JP3698297 B2 JP 3698297B2 JP 23546699 A JP23546699 A JP 23546699A JP 23546699 A JP23546699 A JP 23546699A JP 3698297 B2 JP3698297 B2 JP 3698297B2
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Japan
Prior art keywords
filter medium
filter
water
filtration tank
tank
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Expired - Fee Related
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JP23546699A
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Japanese (ja)
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JP2001058106A (en
Inventor
享 森
重幸 藤村
修 山下
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Ishigaki Co Ltd
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Ishigaki Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Description

【0001】
【発明の属する技術分野】
この発明は、浮上性のろ材を用いたろ過装置及び生物膜ろ過装置のろ材層の洗浄再生装置の改良に関する。
【0002】
【従来の技術】
従来、比重が1.0以下で1.0に近い浮上性のろ材を用いたろ過装置は、ろ過槽内の上部にろ材支持部を設け、その下側に浮上性のろ材を装填してろ材層を形成し、原水を上向流又は下向流で通液してろ過を行ない、ろ材の洗浄の際はろ材層の下部より洗浄水と空気を供給する方法がよく知られている。特開平11−114319号公報に記載の発明はその一例であり、この方法はろ材と洗浄水の混合物を上下に旋回させる手段としてろ過槽の中心部に同心状にドラフトチューブを立設させたり、又、撹拌用の散気ノズルをろ過槽の底部に中心から偏心させて設けている。また、特開平10−85515号公報の発明は、上部ろ材支持部の下面に沿って、洗浄時に散気を行なう領域と散気を行なわない領域とを分割するように下向に延びる仕切部材を設け、交互に切換えて散気を行ない、旋回流の方向を変えるようにしている。
【0003】
【発明が解決しょうとする課題】
しかしながら、特開平11−114319号公報の発明ではろ過槽の形状は下部円錐型の円筒槽に限定している。そして、例えば、コンクリート製の大容量のろ過槽ではドラフトチューブを設けたり、散気ノズルを偏心させて取付けたりするだけでは、ろ材層全体に旋回流を起こして充分な撹拌が出来難いという問題がある。また、特開平10−85515号公報の発明ではろ材支持部の下面に仕切部材を設け、洗浄時に散気を行なう領域と散気を行なわない領域に分割して、交互に散気撹拌する方法は浮上性ろ材の洗浄再生方法としては優れているが、洗浄に時間がかかるという問題がある。
【0004】
【課題を解決するための手段】
本発明は上記の従来技術の課題を解決したものであって、その要旨とするところは、上部にろ材流出防止網を設けたろ過槽と、前記ろ材流出防止網の下面及びろ過槽の中間部に垂直方向に水流案内板を配設し、前記ろ材流出防止網の下方に浮上ろ材によるろ材層を形成し、ろ過槽の下部には原水及びろ材の洗浄水を供給する手段と、洗浄時にろ材層を解し、ろ材を旋回させるための散気装置を設け、ろ過槽の上部には処理水の取出管及び洗浄排水の取出管を設けたものである
【0005】
前述のろ過槽に装填するろ材としては、素材が芯をポリプロピレン、鞘をポリエチレンとした熱融着性複合繊維で、繊度が18〜65デニールである第一フィラメントと素材がポリプロピレン繊維で、繊度が3〜10デニールである第二フィラメントと、素材が芯をポリプロピレン、鞘をポリエチレンとした熱融着性複合繊維で、繊度が1.5〜6デニールである第三フィラメントを混綿したウェッブをニードルパンチング法により布形化し、両面のウェッブ起毛状態を平滑化することなく加熱処理し、前記ウェッブの重量が200〜800g/平方メートル、厚みが2〜8mmの布形化板状体を製作し、この布形化板状体を5〜30mmの矩形に裁断したものを用い、このろ材をろ過槽に装填したとき、ろ材層高と水層高との比率が65:35〜50:50として装填されているとともに、処理水の一部が原水供給口に循環するようにしたものである。
【0006】
【発明の実施の形態】
この発明は上述のように構成してあり、例えば、コンクリート製の大型のろ過槽に装填したろ材層が目詰まりした場合、このろ材層を洗浄再生するにあたり、まず、ろ過槽の底部に堆積した沈殿物を排出した後、ろ材層の下方より空気と洗浄水を供給することにより、ろ材を撹拌洗浄して、洗浄排水をろ過槽の上部より取出すようにしたものである。このとき、散気空気は左右の壁面近く、あるいは、ろ過槽の中心付近から供給するようにしている。そして、ろ過槽上部にはろ材流出防止網を設け、このろ材流出防止網の下面と、ろ過槽の中間部に垂直方向に板状もしくは略楔状の水流案内板を設けているので、ろ過槽の左右の壁面に添って上昇した水とろ材の混合物は、ろ材流出防止網によってろ過槽の中央に向かう流れに変えられ、さらに、水流案内板によって下方に向かう流れに変えられるので、ろ過槽の半分は時計廻り、他の半分は反時計廻りの旋回流が生じ、槽内のろ材全体を撹拌洗浄することができるものである。また、ろ過槽の中心付近から散気空気を送る時は、ろ材と水の混合物は中央付近で上昇し、水流案内板によって左右に二分され、夫々、ろ材流出防止網に沿って左右の壁面に向かう流れとなり、左右の壁面によって今度は下方に向かう流れに変えられ上下方向の旋回流が生じる。
【0007】
また、ろ過槽内に装填するろ材としては、軽量で空隙が大きく、耐圧・耐食性を有し強度の有るものが望ましく、これらの条件を満たすものとして、つぎのような合成樹脂からなるろ材を用いている。即ち、素材が芯をポリプロピレン、鞘をポリエチレンとした熱融着性複合繊維で、繊度が18〜65デニールである第一フィラメントと素材がポリプロピレン繊維で、繊度が3〜10デニールである第二フィラメントと、素材が芯をポリプロピレン、鞘をポリエチレンとした熱融着性複合繊維で、繊度が1.5〜6デニールである第三フィラメントを混綿したウェッブをニードルパンチング法により布形化し、両面のウェッブ起毛状態を平滑化することなく加熱処理し、前記ウェッブの重量が200〜800g/平方メートル、厚みが2〜8mmの布形化板状体を製作し、この布形化板状体を5〜30mmの矩形に裁断したものである。
【0008】
上記のように構成したろ材をろ過槽に装填する際には、洗浄撹拌時の流動性を考慮して、ろ過槽内におけるろ材層高と水層高との比率が65:35〜50:50となるように装填量を調整すれば、ろ材洗浄の際には、効率よくろ材を撹拌洗浄することができるものである。以下、図面に基づいてこの発明を具体的に説明する。
【0009】
【実施例】
図1はこの発明に係るろ過装置の縦断側面図であり、この図に基いてろ材の洗浄再生方法の操作を説明する。ろ過槽2の上部にろ材流出防止網3を設け、このろ材流出防止網3の下方に浮上性のろ材を装填してろ材層1を形成し、ろ過槽2下部の原水供給口10から原水を供給し、上向流でろ材層1を通液してろ過を行ない、処理水はろ過槽2の上部に設けた集水トラフ4に集められ、集水トラフ4に接続した処理水配管12を通って処理水槽14に流入する。この処理水槽14が満杯になると処理水取出管15から溢流して外部に取出される。
【0010】
上記の操作によって、ろ材層1で捕集された固形物や汚泥によってろ材が目詰まりしたときには、原水の供給を停止し、処理水弁11を閉止し、ろ過槽2の底部に堆積した沈殿物を引抜管16から抜き取る。次に、ブロワー5に連結している散気装置6から空気をろ過槽2内に注入する。図1では散気装置6はろ過槽2の左右の壁面近くに設けている。又、ろ材流出防止網3の下面及びろ過槽2の中間部に垂直方向に板状もしくは略楔状の水流案内板7a、7bを配設している。図3の水流案内板7aはろ材流出防止網3の下面に設けたものであり、略楔形状をしているが、左右それぞれ内側に湾曲しているものである。そして、散気装置6から注入された空気は気泡となってろ過槽2の左右の壁面に沿って上昇し、ろ材層1の下部及びろ材流出防止網3に当った気泡はろ過槽2の中央に向かう流れに変えられ、更に中央部では水流案内板7a、7bによって下向に流れを変えられ、上下方向の旋回流を生じる。図1の左半分では時計廻りの旋回流となり、右半分では反時計廻りの旋回流となる。この動作を3〜10分間継続することにより、目詰まりして硬化しているろ材層1はほぐされ、充分に撹拌される。次に、上記の散気撹拌を継続しながら、洗浄水ポンプ9を駆動して処理水槽14に貯留されている処理水を洗浄水配管8を通り、ろ過槽2の下部よりろ過槽2内に供給する。ろ過槽2内に供給された洗浄水はろ材と共に旋回流となり、ろ材の洗浄を行ないろ材に捕集されている固形物や汚泥等の目詰まり物を剥離して、この目詰まり物と一緒に、ろ材流出防止網3を通過し、集水トラフ4に溢流し、洗浄排水管13を通って外部に排出される。この時の洗浄水速度は速すぎれば旋回しているろ材をろ材流出防止網3に押し付け、洗浄が不充分となる。又、遅すぎればろ材を洗浄再生するのに時間がかかる。ろ材の洗浄速度としては10〜30m/Hrが最適値であることが実験データーより判明している。
【0011】
又、ろ過槽2内に装填するろ材は、素材が芯をポリプロピレン、鞘をポリエチレンとした熱融着性複合繊維で、繊度が18〜65デニールである第一フィラメントと素材がポリプロピレン繊維で、繊度が3〜10デニールである第二フィラメントと、素材が芯をポリプロピレン、鞘をポリエチレンとした熱融着性複合繊維で、繊度が1.5〜6デニールである第三フィラメントを混綿したウェッブをニードルパンチング法により布形化し、両面のウェッブ起毛状態を平滑化することなく加熱処理し、前記ウェッブの重量が200〜800g/平方メートル、厚みが2〜8mmの布形化板状体を製作し、この布形化板状体を5〜30mmの矩形に裁断したものを用いており、この合成樹脂製の繊維ろ材は軽量で空隙が大きく、耐圧・耐食性があり、強度を有しているので、撹拌により損耗や変形が無く、ろ材として好適なものである。
【0012】
上記のろ材をろ過槽2に装填する量としては、このろ材層1が目詰まりして洗浄撹拌操作によって旋回流を生じさせて、このろ材層1を解きほぐす際の流動性を考慮すれば、ろ過槽2内におけるろ材層高と水層高との比率は65:35〜50:50となるように装填量を調整すれば、効率よくろ材を撹拌洗浄することができるものである。
【0013】
図2は、この発明に係る他の実施例のろ過装置の縦断側面図であり、散気装置6を水流案内板7a、7bを延長した垂線を挟んで左右に配設しているので、図1における実施例とは逆回転の旋回流が生じるものである。尚、平面が長方形の大きなろ過槽2の場合には複数個所に水流案内板7a、7b…を設ければよく、ろ過槽2の壁面と最初の水流案内板7a、7b及び最初の水流案内板7a、7bと2番目の水流案内板7a、7b…n番目の水流案内板7a、7bと(n+1)番目の水流案内板7a、7bそして(n+1)番目の水流案内板7a、7bと壁面までの間隔を1〜3mとするものであり、好ましくは2mとするのが実験データーから最適である。
【0014】
【発明の効果】
本発明のろ過装置におけるろ材の洗浄再生方法により目詰まりしたろ材層を散気による旋回流で撹拌して、充分にほぐした後、洗浄水を供給することによりろ材から固形物や汚泥等の目詰まり物を容易に剥離し、洗浄効果を高め、洗浄時間の短縮による洗浄水量の低減が図れるものであり、大規模のろ過槽でも、一度に効率よくろ材の洗浄再生が行なえるものであり、従来のこの種ろ過装置のろ材洗浄時の課題を解決したものである。
【図面の簡単な説明】
【図1】 本発明に係るろ過装置の縦断側面図である。
【図2】 本発明に係る他の実施例のろ過装置の縦断側面図である。
【図3】 上部の水流案内板の一例を示す側面図である。
【符号の説明】
1 ろ材層
2 ろ過槽
3 ろ材流出防止網
4 集水トラフ
5 ブロワ
6 散気装置
7a、7b 水流案内板
8 洗浄水配管
9 洗浄水ポンプ
10 原水供給口
11 処理水弁
12 処理水配管
13 洗浄排水管
14 処理水槽
15 処理水取出管
16 引抜管
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an improvement in a filtration apparatus using a floatable filter medium and an apparatus for cleaning and regenerating a filter medium layer of a biofilm filtration apparatus.
[0002]
[Prior art]
Conventionally, a filtering device using a floatable filter medium having a specific gravity of 1.0 or less and close to 1.0 is provided with a filter medium support part in the upper part of the filtration tank, and a filter medium with a floatable material is loaded on the lower side thereof. A method is well known in which a layer is formed, raw water is passed in an upward flow or a downward flow for filtration, and cleaning water and air are supplied from the bottom of the filter medium layer when the filter medium is washed. The invention described in Japanese Patent Application Laid-Open No. 11-114319 is an example thereof, and this method allows a draft tube to be installed concentrically in the center of the filtration tank as a means for turning the mixture of the filter medium and the washing water up and down, Further, an aeration nozzle for stirring is provided eccentrically from the center at the bottom of the filtration tank. Further, the invention of Japanese Patent Laid-Open No. 10-85515 includes a partition member extending downward so as to divide a region where air is diffused during cleaning and a region where air is not diffused along the lower surface of the upper filter medium support. It is provided and switched alternately to perform aeration and change the direction of the swirl flow.
[0003]
[Problems to be solved by the invention]
However, in the invention of Japanese Patent Application Laid-Open No. 11-114319, the shape of the filtration tank is limited to the lower cone type cylindrical tank. And, for example, in a large-capacity filter tank made of concrete, there is a problem that it is difficult to sufficiently stir by causing a swirling flow to the entire filter medium layer only by installing a draft tube or attaching an aeration nozzle eccentrically. is there. Further, in the invention of Japanese Patent Laid-Open No. 10-85515, a partition member is provided on the lower surface of the filter medium support portion, and the method of dividing and agitating alternately by dividing into a region where air is diffused during cleaning and a region where air is not diffused is as follows. Although it is excellent as a cleaning and regeneration method for floating filter media, there is a problem that it takes time for cleaning.
[0004]
[Means for Solving the Problems]
The present invention solves the above-mentioned problems of the prior art, and the gist of the invention is a filtration tank provided with a filter medium outflow prevention net on the top, a lower surface of the filter medium outflow prevention net, and an intermediate part of the filtration tank A flow guide plate is arranged in the vertical direction, a filter medium layer is formed by a floating filter medium below the filter medium outflow prevention net, a means for supplying raw water and cleaning water for the filter medium to the lower part of the filter tank, and a filter medium at the time of cleaning construed layer, a diffuser for pivoting the filter material is provided, in an upper portion of the filtration tank is provided with a take-out tube and detergent drain take-out pipe of the treated water.
[0005]
The filter medium to be loaded into the filtration tank is a heat-fusible composite fiber with a polypropylene core and polyethylene sheath, and a first filament with a fineness of 18 to 65 denier and a polypropylene fiber with a fineness of fine. Needle punching a web consisting of 3 to 10 denier second filament and a heat-fusible composite fiber with a core of polypropylene and a sheath of polyethylene, and a third filament with a fineness of 1.5 to 6 denier The cloth is made into a cloth by the method, and heat treatment is carried out without smoothing the web raised state on both sides to produce a cloth-like plate-like body having a weight of 200 to 800 g / m 2 and a thickness of 2 to 8 mm. When the shaped plate was cut into a 5-30 mm rectangle and this filter medium was loaded into a filtration tank, the ratio of the height of the filter medium layer to the height of the water layer was 65: 5-50: with is loaded as a 50, a portion of the treated water was made to circulate in the raw water supply port.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
The present invention is configured as described above. For example, when a filter medium layer loaded in a large concrete filter tank is clogged, the filter medium layer is first deposited at the bottom of the filter tank in order to wash and regenerate the filter medium layer. After discharging the precipitate, the filter medium is stirred and washed by supplying air and washing water from below the filter medium layer, and the washing waste water is taken out from the upper part of the filtration tank. At this time, the diffused air is supplied from the left and right wall surfaces or from the vicinity of the center of the filtration tank. A filter medium outflow prevention net is provided at the upper part of the filtration tank, and a plate-like or substantially wedge-shaped water flow guide plate is provided in the vertical direction at the lower surface of the filter medium outflow prevention net and in the middle part of the filter tank. The mixture of water and filter media that has risen along the left and right wall surfaces is converted into a flow toward the center of the filtration tank by the filter medium outflow prevention net, and further to a downward flow by the water flow guide plate. Produces a swirling flow in the clockwise direction and the other half in the counterclockwise direction, and the entire filter medium in the tank can be stirred and washed. When air is sent from the center of the filtration tank, the mixture of filter medium and water rises near the center and is divided into right and left by the water flow guide plate. It becomes the flow which goes to, and is changed into the flow which goes to the downward direction by the left and right wall surfaces, and the vertical swirl flow is generated.
[0007]
In addition, the filter medium to be loaded in the filtration tank is preferably lightweight, has a large gap, has pressure resistance / corrosion resistance, and has strength. To satisfy these conditions, a filter medium made of the following synthetic resin is used. ing. That is, a heat-fusible conjugate fiber with a polypropylene core and polyethylene sheath and a first filament with a fineness of 18 to 65 denier and a second filament with a polypropylene fiber and a fineness of 3 to 10 denier And a material made of polypropylene with a core and polyethylene with a sheath and a heat-fusible conjugate fiber, and a cotton blended with a third filament with a fineness of 1.5 to 6 denier is made into a cloth by the needle punching method. The raised state is heat-treated without smoothing, and a cloth-like plate-like body having a web weight of 200 to 800 g / square meter and a thickness of 2 to 8 mm is produced. This cloth-like plate-like body is 5 to 30 mm. It is cut into rectangles.
[0008]
When the filter medium configured as described above is loaded into the filtration tank, the ratio of the height of the filter medium layer to the height of the water layer in the filter tank is 65:35 to 50:50 in consideration of the fluidity during washing and stirring. If the loading amount is adjusted so that, the filter medium can be efficiently agitated and washed at the time of washing the filter medium. The present invention will be specifically described below with reference to the drawings.
[0009]
【Example】
FIG. 1 is a longitudinal side view of a filtration apparatus according to the present invention, and the operation of a filter medium cleaning and regenerating method will be described based on this figure. A filter medium outflow prevention net 3 is provided at the upper part of the filtration tank 2, and a filter medium layer 1 is formed by loading a floatable filter medium below the filter medium outflow prevention net 3, and raw water is supplied from the raw water supply port 10 at the lower part of the filter tank 2. The filtered water layer 1 is supplied and filtered through the filter medium layer 1, and the treated water is collected in a water collection trough 4 provided in the upper part of the filtration tank 2, and a treated water pipe 12 connected to the water collection trough 4 is connected to the treated water pipe 12. It flows into the treated water tank 14 through. When the treated water tank 14 becomes full, it overflows from the treated water take-out pipe 15 and is taken out to the outside.
[0010]
When the filter medium is clogged by solid matter or sludge collected by the filter medium layer 1 by the above operation, the raw water supply is stopped, the treated water valve 11 is closed, and the sediment deposited on the bottom of the filter tank 2 Is extracted from the drawing tube 16. Next, air is injected into the filtration tank 2 from the air diffuser 6 connected to the blower 5. In FIG. 1, the air diffuser 6 is provided near the left and right wall surfaces of the filtration tank 2. Further, plate-shaped or substantially wedge-shaped water flow guide plates 7 a and 7 b are arranged in the vertical direction on the lower surface of the filter medium outflow prevention net 3 and the middle portion of the filtration tank 2. The water flow guide plate 7a in FIG. 3 is provided on the lower surface of the filter medium outflow prevention net 3, and has a substantially wedge shape, but is curved inward on the left and right sides. The air injected from the air diffuser 6 becomes bubbles and rises along the left and right wall surfaces of the filtration tank 2, and the bubbles that hit the lower part of the filter medium layer 1 and the filter medium outflow prevention net 3 are in the center of the filter tank 2. In the center, the flow is changed downward by the water flow guide plates 7a and 7b, and a swirling flow in the vertical direction is generated. In the left half of FIG. 1, the swirl flow is clockwise, and in the right half, the swirl flow is counterclockwise. By continuing this operation for 3 to 10 minutes, the clogged and hardened filter medium layer 1 is loosened and sufficiently stirred. Next, while continuing the aeration stirring, the cleaning water pump 9 is driven to pass the processing water stored in the processing water tank 14 through the cleaning water pipe 8 and into the filtering tank 2 from the lower part of the filtering tank 2. Supply. The washing water supplied into the filtration tank 2 becomes a swirl flow together with the filter medium, and the filter medium is washed to remove clogged substances such as solids and sludge collected in the filter medium, and together with the clogged substances. Then, it passes through the filter medium outflow prevention network 3, overflows into the water collection trough 4, and is discharged to the outside through the washing drain pipe 13. If the washing water speed at this time is too high, the swirling filter medium is pressed against the filter medium outflow prevention net 3, and the washing becomes insufficient. If it is too slow, it takes time to wash and regenerate the filter medium. From experimental data, it has been found that 10-30 m / Hr is the optimum value for the cleaning speed of the filter medium.
[0011]
The filter medium loaded in the filtration tank 2 is a heat-fusible composite fiber whose material is polypropylene and whose sheath is polyethylene, the first filament whose fineness is 18 to 65 denier and the material is polypropylene fiber, and the fineness. Needle with a second filament of 3 to 10 denier and a heat-fusible conjugate fiber with a core of polypropylene and a sheath of polyethylene, and a third filament with a fineness of 1.5 to 6 denier Fabricated by punching method, heat-treated without smoothing the web brushed state on both sides, producing a cloth-shaped plate-like body having a weight of 200 to 800 g / m2 and a thickness of 2 to 8 mm. Fabricated plate is cut into a 5-30mm rectangle, and this synthetic resin fiber filter is lightweight, has large gaps, and has pressure and corrosion resistance. , Since it has a strength, without wear and deformation by stirring, it is suitable as a filter material.
[0012]
The amount of the filter medium to be loaded into the filtration tank 2 is that if the filter medium layer 1 is clogged and a swirling flow is generated by a washing and stirring operation, and the fluidity when unraveling the filter medium layer 1 is taken into consideration, the filtration medium 2 is filtered. By adjusting the loading so that the ratio of the height of the filter medium layer to the height of the water layer in the tank 2 is 65:35 to 50:50, the filter medium can be efficiently stirred and washed.
[0013]
FIG. 2 is a vertical side view of a filtration device according to another embodiment of the present invention, and the air diffuser 6 is disposed on the left and right sides with a perpendicular extending from the water flow guide plates 7a and 7b. In the embodiment of No. 1, a swirling flow of reverse rotation is generated. In the case of a large filtration tank 2 having a rectangular plane, water flow guide plates 7a, 7b... May be provided at a plurality of locations, and the wall surface of the filtration tank 2, the first water flow guide plates 7a, 7b, and the first water flow guide plate. 7a, 7b and the second water flow guide plates 7a, 7b... To the nth water flow guide plates 7a, 7b, the (n + 1) th water flow guide plates 7a, 7b and the (n + 1) th water flow guide plates 7a, 7b and the wall surface. The interval is set to 1 to 3 m, and preferably 2 m is optimal from experimental data.
[0014]
【The invention's effect】
The filter medium layer clogged by the cleaning and regenerating method of the filter medium in the filtration device of the present invention is stirred with a swirling flow by aeration, sufficiently loosened, and then supplied with cleaning water to remove solids, sludge, etc. from the filter medium. The clogging material can be easily peeled off, the cleaning effect can be improved, the amount of cleaning water can be reduced by shortening the cleaning time, and even in a large-scale filtration tank, the filter media can be cleaned and regenerated efficiently at once. It solves the problem at the time of filter medium cleaning of the conventional seed filtration device.
[Brief description of the drawings]
FIG. 1 is a longitudinal side view of a filtration device according to the present invention.
FIG. 2 is a longitudinal side view of a filtration device according to another embodiment of the present invention.
FIG. 3 is a side view showing an example of an upper water flow guide plate.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Filter medium layer 2 Filtration tank 3 Filter medium outflow prevention network 4 Catchment trough 5 Blower 6 Air diffuser 7a, 7b Water flow guide plate 8 Washing water piping 9 Washing water pump 10 Raw water supply port 11 Treating water valve 12 Treating water piping 13 Washing drainage Pipe 14 Treated water tank 15 Treated water take-out pipe 16 Pull-out pipe

Claims (3)

上部にろ材流出防止網(3)を設けたろ過槽(2)と、前記ろ材流出防止網(3)の下面及びろ過槽(2)の中間部に垂直方向に水流案内板(7a,7b)を配設し、前記ろ材流出防止網(3)の下方に浮上ろ材によるろ材層(1)を形成し、ろ過槽(2)の下部には原水及びろ材の洗浄水を供給する手段と、洗浄時にろ材層(1)をほぐし、ろ材を旋回させるための散気装置(6)を設け、ろ過槽(2)の上部には処理水の取出管(12)及び洗浄排水の取出管(13)を設けたことを特徴とするろ材層の洗浄再生装置。A filtration tank (2) provided with a filter medium outflow prevention net (3) at the top, and a water flow guide plate (7a, 7b) perpendicular to the lower surface of the filter medium outflow prevention net (3) and the middle part of the filter tank (2) disposed of, the filter media outflow prevention network (3) filter media layer (1) formed by floating filter media under the, means for supplying wash water of the raw water and filter material at the bottom of the filtration tank (2), washed An air diffuser (6) for loosening the filter medium layer (1) and swirling the filter medium is sometimes provided, and a treated water discharge pipe (12) and a washing drainage discharge pipe (13) are provided above the filtration tank (2). An apparatus for cleaning and regenerating a filter medium layer, comprising: 素材が芯をポリプロピレン、鞘をポリエチレンとした熱融着性複合繊維で、繊度が18〜65デニールである第一フィラメントと素材がポリプロピレン繊維で、繊度が3〜10デニールである第二フィラメントと、素材が芯をポリプロピレン、鞘をポリエチレンとした熱融着性複合繊維で、繊度が1.5〜6デニールである第三フィラメントを混綿したウェッブをニードルパンチング法により布形化し、両面のウェッブ起毛状態を平滑化することなく加熱処理し、前記ウェッブの重量が200〜800g/平方メートル、厚みが2〜8mmの布形化板状体を製作し、この布形化板状体を5〜30mmの矩形に裁断したものをろ材として装填した請求項1に記載のろ材層の洗浄再生装置。A heat-fusible conjugate fiber with a polypropylene core and polyethylene sheath, and a first filament whose fineness is 18 to 65 denier and a second filament whose material is polypropylene fiber and whose fineness is 3 to 10 denier; A heat-fusible conjugate fiber with a core of polypropylene and a sheath of polyethylene, and a web blended with a third filament with a fineness of 1.5 to 6 denier is made into a cloth by the needle punching method, and the web is raised on both sides The fabric is made into a rectangular plate having a weight of 200 to 800 g / square meter and a thickness of 2 to 8 mm. The apparatus for washing and regenerating a filter medium layer according to claim 1 , wherein the filter medium is loaded as a filter medium. 上記ろ材をろ過槽(2)に装填したとき、ろ材層(1)高と水層高との比率が65:35〜50:50として装填されているとともに、処理水の一部が原水供給口(10)に循環するようにしていることを特徴とする請求項1に記載のろ材層の洗浄再生装置。When the filter medium is loaded into the filtration tank (2), the ratio of the height of the filter medium layer (1) to the height of the water layer is 65:35 to 50:50, and a part of the treated water is supplied to the raw water supply port. The apparatus for washing and regenerating a filter medium layer according to claim 1 , wherein the apparatus is circulated in (10).
JP23546699A 1999-08-23 1999-08-23 Filter media cleaning and recycling equipment Expired - Fee Related JP3698297B2 (en)

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JP4519878B2 (en) * 2007-04-26 2010-08-04 財団法人塩事業センター Filtration device
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