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JP4249855B2 - Moving bed type filtration equipment using floating media - Google Patents

Moving bed type filtration equipment using floating media Download PDF

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Publication number
JP4249855B2
JP4249855B2 JP24514599A JP24514599A JP4249855B2 JP 4249855 B2 JP4249855 B2 JP 4249855B2 JP 24514599 A JP24514599 A JP 24514599A JP 24514599 A JP24514599 A JP 24514599A JP 4249855 B2 JP4249855 B2 JP 4249855B2
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Japan
Prior art keywords
filter medium
filter
tank
storage tank
water
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JP24514599A
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JP2001062208A (en
Inventor
実 土屋
護 皆方
進 石川
郁子 馬場
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Maezawa Industries Inc
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Maezawa Industries Inc
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Description

【0001】
【発明の属する技術分野】
本発明は、浮上ろ材を用いた移床式ろ過装置に関し、詳しくは、比重が水よりも小さな浮上ろ材を使用して下排水等のろ過処理を行う移床式ろ過装置に関する。
【0002】
【従来の技術】
比重が水よりも小さな浮上ろ材、例えば発泡ポリスチレン製のろ材を使用した移床式ろ過装置として、特開平10−216756号公報等に記載されてものが知られている。通常の移床式ろ過装置は、浮上ろ材を充填したろ過槽の上部から原水を下降流で供給し、浮上ろ材と接触して濁質が除かれた処理水をろ過槽の下部から取出すようにしている。濁質を捕捉した浮上ろ材の洗浄は、ろ材引抜工程とろ材移送工程とによって行われる。
【0003】
ろ材引抜工程は、ろ過槽上部に設けたろ材貯留槽に、ろ過槽内のろ材の一部をろ材流入管を通して引抜く工程であり、ろ材移送工程は、ろ材貯留槽に引抜いたろ材をろ材移送管を通してろ過槽底部に移送する工程である。このろ材移送工程において、ろ材移送管内の乱流によりろ材と濁質とが分離しやすい状態となってろ過槽底部に移送され、ろ過槽底部で濁質を分離したろ材は、ろ過槽底部からろ過槽上部に上昇し、分離した濁質は、洗浄排水とともにろ過槽底部から排出される。なお、引抜工程及び移送工程を行っている間も、原水の流入は原則として継続されており、ろ過処理は連続して行われている。
【0004】
このような浮上ろ材を使用した移床式ろ過装置では、例えば、30〜60分を1サイクルとし、ろ過工程を20〜40分、ろ材引抜工程を1〜2分、ろ材移送工程を10〜20分にそれぞれ設定して運転を行っている。
【0005】
【発明が解決しようとする課題】
しかし、従来のろ過装置では、ろ材引抜工程におけるろ材流入管内で、上昇するろ材と下降する水とが入れ替わる状態になるため、所定量のろ材をろ材貯留槽に引抜くために比較的長い時間を必要とするだけでなく、ろ材と水との入れ替わりの過程でろ材から濁質が分離し、濁質が水とともにろ過槽内に戻されてしまうこともあった。また、ろ過槽上部にろ材流入管を介してろ材貯留槽を連設しているため、装置高さが大きくなり、設置場所が限られてしまうこともあった。
【0006】
そこで本発明は、ろ材引抜工程の所要時間を短縮するとともに、洗浄効果の向上が図れ、さらに装置の小型化も図れる移床式ろ過装置を提供することを目的としている。
【0007】
【課題を解決するための手段】
上記目的を達成するため、本発明の浮上ろ材を用いた移床式ろ過装置は、上部に原水流入部を、下部に処理水流出部を有するろ過槽と、該ろ過槽の頂部にろ材流入弁を有するろ材流入管を介して接続したろ材貯留槽と、該ろ材貯留槽の頂部に設けられたろ材吸引部と、ろ材移送水を前記ろ材吸引部に送水する移送水ポンプを有する移送水管と、ろ材吸引部でろ材貯留槽内のろ材を吸引同伴したろ材移送水を前記ろ過槽の底部に移送するろ材移送管とを備えた移床式ろ過装置であって、前記ろ材貯留槽に接続したろ材流入管の上端開口部を、ろ材貯留槽内に突出させて上向きに開口して前記ろ材貯留槽底部より上方に位置させるとともに、ろ材貯留槽の底部に排水管を接続したことを特徴としている。
【0008】
さらに、本発明の移床式ろ過装置は、前記ろ材流入管の開口高さがろ材貯留槽内において調節可能であること、前記ろ過槽の底部にろ材と洗浄排水とを分離する洗浄排水分離部を設けたこと、前記ろ過槽内にろ層の膨張を防止するためのグリッド押えを設けたことを特徴としている。
【0009】
また、前記ろ過槽に、ろ層の膨張を検知したときにろ過速度調整又はろ材洗浄開始を行う手段を設けたこと、前記ろ材貯留槽から移送水管を経てろ過槽へのろ材の移送が終了したことを検知し、ろ材移送運転を終了させる手段を設けたこと、前記ろ材流入弁を開いてろ過槽からろ材貯留槽にろ材を流入させるときに、原水流入位置の変更又は原水の流入停止を行う手段を設けたことを特徴としている。
【0010】
さらに、前記ろ過槽の下部に散気手段を設けたこと、前記ろ材貯留槽を前記ろ過槽の側方位置に併設するとともに、前記ろ材流入管を、ろ過槽の頂部から下方に屈曲してろ材貯留槽の下部に接続したことを特徴としている。
【0011】
【発明の実施の形態】
図1は、本発明の移床式ろ過装置の第1形態例を示す系統図である。この移床式ろ過装置は、上部に上下一対の原水流入部11a,11bを、下部に処理水流出部12を有するろ過槽10と、該ろ過槽10の頂部にろ材流入弁13を有するろ材流入管14を介して接続したろ材貯留槽15と、該ろ材貯留槽15の頂部に設けられたろ材吸引部であるエジェクター16と、ろ過槽10から引き抜いた処理水の一部をろ材移送水として前記エジェクター16に送水するための移送水ポンプ17、移送弁18及び移送水調整弁19を有する移送水管20と、エジェクター16でろ材貯留槽15内のろ材を吸引同伴したろ材移送水をろ過槽10の底部に設けた洗浄排水分離部21に移送するためのろ材移送弁22を有するろ材移送管23と、ろ材貯留槽15の底部に排水弁24及び排水調整弁25を介して接続された排水管26とを備えている。
【0012】
前記原水流入部11a,11bは、供給切換弁27a,27b及び逆止弁28a,28bを介して原水ポンプ29及び流量計30を有する原水流入管31に接続されている。また、洗浄排水分離部21には、ろ材と洗浄排水との分離を促進する複数の傾斜板32が設けられており、底部には、洗浄排水弁33及び洗浄排水調整弁34を有する洗浄排水排出管35が接続されている。さらに、前記処理水流出部12に接続する処理水流出管36、前記排水管26及び洗浄排水排出管35は、それぞれ所定高さの越流堰36a,26a,35aを備えている。また、前記移送水管20の移送水調整弁19の上流側からは、ろ材貯留槽15にろ材押出水を注入するための押出水調整弁37を有する押出水管38が分岐している。さらに、原水流入管31には圧力計39が設けられている。なお、その他の弁40,41,42,43は、通常は全開状態となっている。
【0013】
そして、前記ろ材貯留槽15に接続したろ材流入管14は、その上端開口部14aがろ材貯留槽15内に突出して上向きに開口しており、ろ材貯留槽底部より所定高さ上方に位置するようにしている。このように、ろ材貯留槽15において、ろ材流入管14の上端開口部14aをろ材貯留槽15の底部より上方に上向きに開口させるとともに、ろ材貯留槽15の底部に排水管26を接続したことにより、ろ過槽10からろ材貯留槽15へのろ材の流入を円滑に行うことができる。
【0014】
すなわち、ろ材流入弁13及び排水弁24を開いてろ材引抜工程を開始すると、ろ過槽10からろ材流入弁13を通り、ろ材流入管14を経てろ材貯留槽15内に流入するろ材に相当する量の水が、所定開度に調整された排水調整弁25及び排水弁24を通り、排水管26から越流堰26aを超えて流出するので、従来のようなろ材流入管14部分でのろ材と水との入れ替わり現象が発生することがなくなる。また、上端開口部14aをろ材貯留槽15の底部より上方にもうけたので、排水管26からろ材が流出することもない。したがって、ろ材貯留槽15内へのろ材の流入が円滑に行われ、ろ材引抜工程を短時間で終了させることができるとともに、ろ材から分離した濁質がろ過槽10に戻されることもなくなる。
【0015】
さらに、ろ材引抜工程において、ろ材貯留槽15内のろ材量が、ろ材流入管14の上端開口部14aにまで達すると、ろ材間の抵抗によってこれ以上のろ材は流入できない状態になるので、上端開口部14aの開口高さを上下に調節可能に形成しておくことにより、ろ過槽10からのろ材引抜き量を、処理条件に応じて最適な量に調整することができる。なお、上下調節可能な構造としては、二重管によるスライド構造や蛇腹管による伸縮構造等を採用することができる。
【0016】
ろ材移送工程では、ろ材流入弁13及び排水弁24を閉じた後、移送弁18及びろ材移送弁22を開いてポンプ17を作動させ、処理水流出管36を流れる処理水の一部を移送水管20から移送水としてエジェクター16に供給することにより、ろ材貯留槽15内のろ材がエジェクター16に吸引され、移送水とともにろ材移送管23を通って洗浄排水分離部21に移送される。このとき、移送水管20の水の一部が押出水管38に分岐し、押出水としてろ材貯留槽15に流入し、ろ材をエジェクター16に押出すことにより、ろ材の移送を効率よく行うことができる。なお、移送水と押出水との流量バランスは、移送水調整弁19と押出水調整弁37とによって行うことができる。
【0017】
洗浄排水分離部21は、ろ材移送管23内の乱流の作用で分離しやすい状態となったろ材と濁質とを分離し、ろ材をろ過槽10内に上昇させるとともに、濁質を含む移送水及びろ過槽底部の処理水の一部を洗浄排水として洗浄排水排出管35から排出するものであって、ろ材とともに濁質がろ過槽10に上昇することを防止するために設けられている。
【0018】
この洗浄排水分離部21では、複数の傾斜板32によって洗浄排水分離部21内の実質的な流路長を長くすることにより、洗浄排水分離部21でのろ材の滞留時間を長くしてろ材と濁質との分離を促進するようにしている。さらに、ろ材移送管23からの流入水量よりも洗浄排水排出管35からの排出水量を多くし、ろ過槽10から処理水の一部を洗浄排水分離部21内に流入させることにより、洗浄排水分離部21内に下降流を形成することができるので、ろ材の上昇速度を低く抑えることができる。
【0019】
これにより、比重が極めて小さく、浮上速度がかなり高いろ材を用いた場合でも、分離した濁質がろ材とともにろ過槽10内に上昇して処理水中に取り込まれることがなくなるので、清澄な処理水を安定して得ることができる。
【0020】
洗浄排水分離部21の形状としては、図2の断面図に示すように、内部にバッフル板や多孔板51を設けたものや、図3に示すように、スクリュー部材52を設けたものでもよく、また、図3に示すように、洗浄排水分離部21の上部に絞り部53を設けることにより、ろ過槽10から流入する処理水の流速を高めることも効果的であり、図2に示すように、洗浄排水分離部21の上部に調整弁54を設けて処理水の流入量を調節することもできる。
【0021】
洗浄排水排出管35からの排出水量の調整は、越流堰35aの位置及び洗浄排水調整弁34によって設定することができ、洗浄排水の排出水量を多くすれば、濁質の分離をより確実に行うことができるが、処理水の一部が洗浄排水として排出されるため、排出水量を多くしすぎると、ろ過効率が低下することになる。したがって、上述のような洗浄排水分離部21を設けることにより、洗浄排水として排出される処理水量の割合を小さくすることができ、十分な洗浄効果を得ながらろ過効率も高めることができる。
【0022】
また、本形態例では、ろ過槽10内の処理水流出部12の上方に、ろ層の膨張を防止するためのグリッド押え55を設けている。このようなグリッド押え55を設けることにより、ろ層が処理水流出部12の近傍に至ることを防止でき、ろ材に捕捉されない状態の濁質が処理水中にリークすることを防止できる。
【0023】
さらに、このグリッド押え55の上部近傍に、ろ層の膨張を検知する検知手段を設け、該検知手段がろ層の膨張を検知したときに、流量計30の設定を変更して原水流入量を少なくすることによりろ過速度を低くしたり、あるいは、原水の流入を停止させたり、あるいは、ろ材を洗浄するためにろ材引抜工程を開始してろ材流入弁13を開いたりするような手段、例えばコンピューター等の制御手段を設けておくことにより、ろ層の膨張によって濁質が処理水中にリークすることを防止できる。
【0024】
すなわち、従来は、タイマーで定期的にろ材の洗浄を行ったり、原水供給部でのろ過抵抗の上昇を検知したりしてろ材の洗浄を開始する制御を行っていた。しかし、タイマーによる制御では、原水の性状によっては、ろ材の洗浄が不必要に多く行われて洗浄排水として排出される処理水の分だけろ過効率が低下したり、逆に洗浄が不足して濁質のリークが発生したりするおそれがあった。一方、ろ過抵抗の上昇を検知する制御では、まれにではあるが、ろ過抵抗の上昇が少ないにもかかわらず、ろ層が膨張することがあり、濁質のリークが生じるおそれがあった。
【0025】
したがって、ろ層の膨張を直接検知することにより、最適なタイミングでろ材の洗浄を開始することができ、濁質のリークを確実に防止できるとともに、従来に比べてろ過効率を向上させることができる。なお、ろ過速度を低くしたり、原水の流入を停止させたりする場合は、タイマーによってろ材の洗浄を開始したり、警報等によって手動で洗浄を開始したりするようにしておけばよい。また、ろ層の膨張を検知する手段としては、浮力を利用したものや、光学的なもの、超音波を利用したものなどを使用することができる。
【0026】
さらに、前記ろ材貯留槽15や移送水管23に、これらの内部のろ材の有無を検知する手段を設け、該検知手段がろ材の無いことを検知したときに、すなわち、ろ材の移送が終了したことを検知したときに、ポンプ17を停止させるとともに、移送弁18及びろ材移送弁22を閉じてろ材移送工程を終了させる手段、例えばコンピューター等の制御手段を設けておくことにより、ポンプ17の消費動力の低減や洗浄排水量の低減が図れる。
【0027】
ろ材の移送に要する時間は、濁質の捕捉状況等によって変動し、同じ量のろ材を移送する場合でも、所要時間は必ずしも一定にはならない。このため、従来は、実際の移送時間よりも少し長い時間にタイマーを設定していたので、ろ材の移送が終了した後にもポンプが作動して動力が無駄に消費され、その分、洗浄排水も多くなっていた。
【0028】
したがって、ろ材の移送が終了したことを直接検知してろ材移送運転を終了させることにより、消費動力の低減やろ過効率の向上が図れることになる。また、ろ材の有無を検知する手段としては、光学的なもの、超音波を利用したものなどを使用することができる。
【0029】
さらに、ろ材引抜工程の開始とともに、供給切換弁27a,27bを切換開閉して原水の供給位置を通常のろ過運転時の原水流入部11aから、下方に位置する原水流入部11bに変更することにより、ろ過槽10内からろ材貯留槽15に向けて上昇するろ材を流入水の流れで撹拌することがなくなるので、捕捉した濁質をろ材に保持させたままで上昇させることができる。すなわち、ろ材引抜工程では下方の原水流入部11bから原水を流入させることにより、ろ材に捕捉された濁質の排除を十分に行うことができ、良好な処理水質を維持することができる。なお、ろ材引抜工程は、前記排水管26を設置した効果によって短時間で終了するので、原水流入部を一箇所のみとし、ろ材引抜工程では原水の供給を停止するようにしても同様の効果が期待できる。
【0030】
また、ろ過槽10の下部やろ層内に散気手段を設けて好気性生物膜による浄化機能を付加した生物膜ろ過装置とすることもできる。なお、本形態例に示す構造のろ過槽の場合は、ろ過槽10の上部に、ろ材を通過させないスクリーンを介して空気抜きを設けておく。
【0031】
図4は、本発明の移床式ろ過装置の第2形態例を示す系統図である。なお、以下の説明において、前記第1形態例の構成要素と同一の構成要素には同一の符号を付して詳細な説明は省略する。
【0032】
この移床式ろ過装置は、装置高さを低くするために、ろ材貯留槽15をろ過槽10の側方位置に併設するとともに、ろ材流入管14をろ過槽10の頂部から下方に屈曲させてろ材貯留槽15の下部に接続するようにしている。また、ろ過槽10の上方を開放し、ろ過槽内上部にろ材を捕集する円錐状のスクリーン61及び逆円錐状の分散板62を設けるとともに、ろ過槽内下部にコンプレッサー63に接続した散気装置64を設け、生物膜ろ過装置として機能するようにしている。
【0033】
通常のろ過運転時には、全ての弁が閉じられた状態で、原水ポンプ29及びコンプレッサー63が作動し、原水が原水流入部11a,11bから下降流としてろ過槽10内に供給されるとともに、散気装置64からの散気が行われ、生物膜ろ過装置としての処理が行われる。処理水は、処理水流出部12から処理水流出管36、越流堰36aを経て流出する。このとき、ろ層内を上昇した気泡は、分散板62で槽外周側にガイドされた後、スクリーン61を通過してろ過槽10の上方に排気される。また、散気やろ過抵抗の増加によって水面が上昇した場合は、オーバーフロー管65から排出される。
【0034】
ろ材引抜工程は、ろ材流入弁13及び排水弁24を開くことにより行われ、スクリーン61に捕集されて中央上部に浮上したろ材は、ろ材貯留槽15内の水が、排水弁24、排水管26及び越流堰26aを経て排出されることによる水流に伴われた状態で、ろ材流入管14、ろ材流入弁13を経てろ材貯留槽15の所定位置に開口した上端開口部14aからろ材貯留槽15内に流入する。
【0035】
また、この他のろ材引抜方法としては、例えば、弁67,68を開き、ポンプ17を運転してろ材貯留槽15内の水を排出することによっても行うことができる。さらに、ろ過槽10が散気を行わない密閉構造の場合は、ポンプ29からの流入水でろ材を押し出すようにすることもできる。
【0036】
ろ材移送工程は、ろ材流入弁13及び排水弁24を閉じた状態で、遮断弁66、移送弁18及びろ材移送弁22を開いてポンプ17を作動させることにより行われる。これにより、ろ過槽10の底部から遮断弁66を通って抜き出された移送水が、移送水管20を通ってエジェクター16に供給され、ろ材貯留槽15内からろ材を吸引してろ材移送管23を通り、ろ過槽10の底部に設けられた洗浄排水分離部21に移送される。移送水と押出水との流量バランスは、移送水調整弁19と押出水調整弁37とにより、前記同様に調整することができる。このろ材移送工程により洗浄排水分離部21でろ材から分離した濁質は、洗浄排水分離部21の下部から洗浄排水排出管35を経て移送水及び処理水の一部とともに排出される。
【0037】
このように、形成した本形態例の移床式ろ過装置は、前記第1形態例のものと同等の機能を有しながら、ろ材貯留槽15をろ過槽10の側方位置に併設したので、ろ過装置の上部構造を簡素化することができ、装置高さを低くすることができる。さらに、ろ材貯留槽15の近傍に設けられる各弁の調整や操作性が向上するという利点もある。
【0038】
なお、設置面積が大きくなることが懸念されるが、ろ過槽10に比べてろ材貯留槽15が小さいことや、架台が簡素化できることから、装置全体としては小型化を図ることができる。
【0039】
【発明の効果】
以上説明したように、本発明の浮上ろ材を用いた移床式ろ過装置によれば、ろ材引抜工程の時間短縮が図れるとともに、濁質がろ過槽に戻されることもなくなり、ろ過効率を上昇させることができる。また、ろ材移送工程におけるろ材と濁質との分離も確実に行うことができ、清澄な処理水を安定して得ることができる。さらに、ろ材引抜工程をろ層の状態に応じて開始することにより、処理水質の悪化を防止でき、ろ材移送工程をろ材の有無に応じて終了することにより、動力費の節減や洗浄排水量の低減が図れる。また、ろ材貯留槽をろ過槽の側方位置に併設することにより、装置高さを低くして装置全体の小型化が図れる。
【図面の簡単な説明】
【図1】 本発明の移床式ろ過装置の第1形態例を示す系統図である。
【図2】 洗浄排水分離部の他の形状例を示す断面図である。
【図3】 洗浄排水分離部のさらに他の形状例を示す断面図である。
【図4】 本発明の移床式ろ過装置の第2形態例を示す系統図である。
【符号の説明】
10…ろ過槽、11a,11b…原水流入部、12…処理水流出部、13…ろ材流入弁、14…ろ材流入管、14a…上端開口部、15…ろ材貯留槽、16…エジェクター、17…移送水ポンプ、18…移送弁、19…移送水調整弁、20…移送水管、21…洗浄排水分離部、22…ろ材移送弁、23…ろ材移送管、24…排水弁、25…排水調整弁、26…排水管、26a…越流堰、27a,27b…供給切換弁、28a,28b…逆止弁、29…原水ポンプ、30…流量計、31…原水流入管、32…傾斜板、33…洗浄排水弁、34…洗浄排水調整弁、35…洗浄排水排出管、35a…越流堰、36…処理水流出管、36a…越流堰、37…押出水調整弁、38…押出水管、39…圧力計、51…多孔板、52…スクリュー部材、53…絞り部、54…調整弁、55…グリッド押え、61…スクリーン、62…分散板、63…コンプレッサー、64…散気装置、65…オーバーフロー管、66…遮断弁
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a moving bed type filtration apparatus using a floating filter medium, and more particularly to a moving bed type filtration apparatus that performs filtration treatment of sewage using a floating filter medium having a specific gravity smaller than that of water.
[0002]
[Prior art]
As a moving bed type filtration apparatus using a floating filter medium having a specific gravity smaller than that of water, for example, a filter medium made of polystyrene foam, one described in JP-A-10-216756 is known. Normal moving bed filtration equipment supplies raw water from the upper part of the filtration tank filled with the floating filter medium in a downward flow, and takes out treated water from which turbidity has been removed by contact with the floating filter medium from the lower part of the filtration tank. ing. Washing of the floating filter medium that has captured the suspended matter is performed by a filter medium drawing process and a filter medium transfer process.
[0003]
The filter medium drawing process is a process of drawing a part of the filter medium in the filter tank through the filter medium inflow pipe to the filter medium storage tank provided in the upper part of the filter tank, and the filter medium transfer process transfers the filter medium extracted to the filter medium storage tank. It is a process of transferring to the bottom of the filtration tank through a tube. In this filter medium transfer step, the filter medium and turbidity are easily separated by the turbulent flow in the filter medium transfer pipe and transferred to the bottom of the filtration tank, and the filter medium separated from the turbidity at the bottom of the filter tank is filtered from the bottom of the filter tank. The suspended turbidity rising to the top of the tank is discharged from the bottom of the filtration tank along with the washing waste water. In addition, while performing the drawing-out process and the transfer process, inflow of raw water is continued in principle, and the filtration process is continuously performed.
[0004]
In the moving bed type filtration apparatus using such a floating filter medium, for example, 30 to 60 minutes is one cycle, the filtration process is 20 to 40 minutes, the filter medium drawing process is 1 to 2 minutes, and the filter medium transfer process is 10 to 20 Set each minute to drive.
[0005]
[Problems to be solved by the invention]
However, in the conventional filtration device, the rising filter medium and the falling water are switched in the filter medium inflow pipe in the filter medium drawing process, so that a relatively long time is required to draw a predetermined amount of the filter medium into the filter medium storage tank. Not only is it necessary, but turbidity is separated from the filter medium in the process of replacement of the filter medium and water, and the turbidity may be returned to the filtration tank together with water. In addition, since the filter medium storage tank is connected to the upper part of the filter tank via the filter medium inflow pipe, the height of the apparatus is increased, and the installation location is sometimes limited.
[0006]
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a moving bed type filtration device that can shorten the time required for the filter medium drawing step, improve the cleaning effect, and further reduce the size of the device.
[0007]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, the moving bed type filtration apparatus using the floating filter medium of the present invention comprises a filtration tank having a raw water inflow part at the top and a treated water outflow part at the bottom, and a filter medium inflow valve at the top of the filtration tank. A filter medium storage tank connected via a filter medium inflow pipe, a filter medium suction part provided at the top of the filter medium storage tank, a transfer water pipe having a transfer water pump for supplying filter medium transfer water to the filter medium suction part, A filter media transfer device comprising a filter media transport pipe for transporting filter media transported water suctioning the filter media in the filter media storage tank to the bottom of the filter tank in the filter media suction section, and connected to the filter media storage tank The upper end opening of the inflow pipe protrudes into the filter medium storage tank and opens upward to be positioned above the bottom of the filter medium storage tank, and a drain pipe is connected to the bottom of the filter medium storage tank.
[0008]
Further, in the moving bed type filtration apparatus of the present invention, the opening height of the filter medium inflow pipe can be adjusted in the filter medium storage tank, and the washing drainage separation part for separating the filter medium and the cleaning wastewater at the bottom of the filter tank. And a grid presser for preventing expansion of the filter layer in the filtration tank.
[0009]
Moreover, when the expansion of the filter layer was detected in the filtration tank, a means for adjusting the filtration rate or starting the filter medium cleaning was provided, and the transfer of the filter medium from the filter medium storage tank to the filter tank via the transfer water pipe was completed. When the filter medium inflow valve is opened and the filter medium flows from the filter tank into the filter medium storage tank, the raw water inflow position is changed or the raw water inflow is stopped. It is characterized by providing means.
[0010]
In addition, air filter means is provided at the lower part of the filtration tank, the filter medium storage tank is provided at a side position of the filter tank, and the filter medium inflow pipe is bent downward from the top of the filter tank. It is connected to the lower part of the storage tank.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a system diagram showing a first embodiment of the moving bed filtration apparatus of the present invention. This moving bed type filtration apparatus has a filter tank 10 having a pair of upper and lower raw water inflow portions 11a, 11b in the upper part and a treated water outflow part 12 in the lower part, and a filter medium inflow valve 13 at the top of the filter tank 10. The filter medium storage tank 15 connected through the pipe 14, the ejector 16 that is a filter medium suction section provided at the top of the filter medium storage tank 15, and a part of the treated water drawn from the filter tank 10 as the filter medium transfer water. A transfer water pipe 20 having a transfer water pump 17 for supplying water to the ejector 16, a transfer valve 18, and a transfer water adjusting valve 19, and a filter medium transfer water that sucks and entrains the filter medium in the filter medium storage tank 15 by the ejector 16. A filter medium transfer pipe 23 having a filter medium transfer valve 22 for transfer to a washing drainage separator 21 provided at the bottom, and a drain connected to the bottom of the filter medium storage tank 15 via a drain valve 24 and a drain adjustment valve 25. And a tube 26.
[0012]
The raw water inflow portions 11a and 11b are connected to a raw water inflow pipe 31 having a raw water pump 29 and a flow meter 30 through supply switching valves 27a and 27b and check valves 28a and 28b. The cleaning / drainage separation unit 21 is provided with a plurality of inclined plates 32 for promoting separation of the filter medium and the cleaning / draining water, and the drainage of the cleaning / drainage having the cleaning / drainage valve 33 and the cleaning / drainage adjustment valve 34 at the bottom. A tube 35 is connected. Further, the treated water outflow pipe 36 connected to the treated water outflow section 12, the drainage pipe 26 and the washing drainage discharge pipe 35 are provided with overflow weirs 36a, 26a and 35a having predetermined heights, respectively. Further, from the upstream side of the transfer water adjustment valve 19 of the transfer water pipe 20, an extrusion water pipe 38 having an extrusion water adjustment valve 37 for injecting the filter medium extrusion water into the filter medium storage tank 15 is branched. Furthermore, a pressure gauge 39 is provided in the raw water inflow pipe 31. The other valves 40, 41, 42 and 43 are normally fully open.
[0013]
The upper end opening 14a of the filter medium inflow pipe 14 connected to the filter medium storage tank 15 protrudes into the filter medium storage tank 15 and opens upward, and is positioned at a predetermined height above the bottom of the filter medium storage tank. I have to. As described above, in the filter medium storage tank 15, the upper end opening 14 a of the filter medium inflow pipe 14 is opened upward from the bottom of the filter medium storage tank 15, and the drain pipe 26 is connected to the bottom of the filter medium storage tank 15. Moreover, the inflow of the filter medium from the filter tank 10 to the filter medium storage tank 15 can be performed smoothly.
[0014]
That is, when the filter medium inflow valve 13 and the drain valve 24 are opened to start the filter medium drawing process, the amount corresponding to the filter medium flowing from the filter tank 10 through the filter medium inflow valve 13 and into the filter medium storage tank 15 through the filter medium inflow pipe 14. Water flows through the drainage adjustment valve 25 and the drainage valve 24 adjusted to a predetermined opening degree and flows out from the drainage pipe 26 over the overflow weir 26a. The phenomenon of replacement with water does not occur. Moreover, since the upper end opening 14 a is provided above the bottom of the filter medium storage tank 15, the filter medium does not flow out from the drain pipe 26. Therefore, the flow of the filter medium into the filter medium storage tank 15 is smoothly performed, the filter medium drawing process can be completed in a short time, and the suspended matter separated from the filter medium is not returned to the filter tank 10.
[0015]
Furthermore, in the filter medium drawing process, when the amount of the filter medium in the filter medium storage tank 15 reaches the upper end opening 14a of the filter medium inflow pipe 14, no further filter medium can flow in due to the resistance between the filter medium. By forming the opening height of the portion 14a so as to be adjustable up and down, the amount of the filter medium withdrawn from the filtration tank 10 can be adjusted to an optimum amount according to the processing conditions. In addition, as a structure which can be adjusted up and down, the slide structure by a double tube, the expansion-contraction structure by a bellows tube, etc. are employable.
[0016]
In the filter medium transfer step, after the filter medium inflow valve 13 and the drainage valve 24 are closed, the transfer valve 18 and the filter medium transfer valve 22 are opened to operate the pump 17, and a part of the treated water flowing through the treated water outflow pipe 36 is transferred to the transfer water pipe. By supplying the transfer water from 20 to the ejector 16, the filter medium in the filter medium storage tank 15 is sucked into the ejector 16, and transferred to the washing / drainage separation unit 21 through the filter medium transfer pipe 23 together with the transfer water. At this time, a part of the water in the transfer water pipe 20 branches to the extruded water pipe 38, flows into the filter medium storage tank 15 as extruded water, and the filter medium is pushed out to the ejector 16, whereby the filter medium can be efficiently transferred. . The flow rate balance between the transfer water and the extrusion water can be performed by the transfer water adjustment valve 19 and the extrusion water adjustment valve 37.
[0017]
The washing waste water separation unit 21 separates the filter medium and turbidity that are easily separated by the action of turbulent flow in the filter medium transfer pipe 23, raises the filter medium into the filtration tank 10, and transfers the turbid substance. Water and a part of the treated water at the bottom of the filtration tank are discharged from the cleaning drainage pipe 35 as cleaning wastewater, and are provided to prevent the turbidity from rising to the filtration tank 10 together with the filter medium.
[0018]
In this cleaning / drainage separation unit 21, the substantial flow path length in the cleaning / drainage separation unit 21 is increased by the plurality of inclined plates 32, thereby increasing the residence time of the filter medium in the cleaning / drainage separation unit 21. The separation from turbidity is promoted. Further, the amount of discharged water from the washing drainage discharge pipe 35 is made larger than the amount of inflowing water from the filter medium transfer pipe 23, and a part of the treated water is allowed to flow into the washing drainage separation unit 21 from the filtration tank 10. Since a downward flow can be formed in the part 21, the ascending speed of the filter medium can be kept low.
[0019]
As a result, even when a filter medium having a very small specific gravity and a considerably high ascent rate is used, the separated suspended matter will not rise into the filtration tank 10 together with the filter medium and be taken into the treated water. It can be obtained stably.
[0020]
As shown in the sectional view of FIG. 2, the shape of the washing / drainage part 21 may be one provided with a baffle plate or porous plate 51 inside, or one provided with a screw member 52 as shown in FIG. 3. Further, as shown in FIG. 3, it is also effective to increase the flow rate of the treated water flowing from the filtration tank 10 by providing a throttle 53 in the upper part of the washing waste water separation unit 21, as shown in FIG. In addition, it is possible to adjust the inflow amount of the treated water by providing a regulating valve 54 in the upper part of the washing waste water separation unit 21.
[0021]
Adjustment of the amount of discharged water from the cleaning drainage discharge pipe 35 can be set by the position of the overflow weir 35a and the cleaning drainage adjustment valve 34. If the amount of drainage of the cleaning drainage is increased, the separation of turbidity is more reliably performed. Although it can be performed, since a part of the treated water is discharged as cleaning wastewater, if the amount of discharged water is excessively increased, the filtration efficiency is lowered. Therefore, by providing the washing waste water separation part 21 as described above, the ratio of the amount of treated water discharged as washing waste water can be reduced, and the filtration efficiency can be enhanced while obtaining a sufficient washing effect.
[0022]
In this embodiment, a grid presser 55 is provided above the treated water outflow portion 12 in the filtration tank 10 to prevent the filter layer from expanding. By providing such a grid retainer 55, it is possible to prevent the filter layer from reaching the vicinity of the treated water outflow portion 12, and it is possible to prevent turbidity that is not captured by the filter medium from leaking into the treated water.
[0023]
Further, a detection means for detecting the expansion of the filter layer is provided in the vicinity of the upper portion of the grid retainer 55, and when the detection means detects the expansion of the filter bed, the setting of the flow meter 30 is changed to reduce the raw water inflow amount. A means for reducing the filtration rate by reducing the flow rate, stopping the inflow of raw water, or starting the filter medium drawing process to open the filter medium inflow valve 13 for washing the filter medium, for example, a computer By providing such control means, it is possible to prevent turbidity from leaking into the treated water due to the expansion of the filter bed.
[0024]
That is, conventionally, the control of starting the cleaning of the filter medium is performed by periodically cleaning the filter medium with a timer or detecting an increase in the filtration resistance in the raw water supply unit. However, with the control by the timer, depending on the properties of the raw water, the filtration efficiency is reduced by the amount of treated water that is unnecessarily washed and discharged as washing wastewater. There was a risk of quality leaks. On the other hand, in the control for detecting the increase in filtration resistance, the filtration layer may expand despite the fact that the increase in filtration resistance is small, which may cause turbidity leakage.
[0025]
Therefore, by directly detecting the expansion of the filter layer, it is possible to start the cleaning of the filter medium at an optimal timing, to surely prevent the leakage of turbidity, and to improve the filtration efficiency compared to the conventional case. . In addition, what is necessary is just to start washing | cleaning of a filter medium by a timer, or to start washing | cleaning manually by an alarm etc., when reducing a filtration rate or stopping inflow of raw | natural water. Moreover, as a means for detecting the expansion of the filter layer, a device using buoyancy, an optical device, a device using ultrasonic waves, or the like can be used.
[0026]
Furthermore, the filter medium storage tank 15 and the transfer water pipe 23 are provided with means for detecting the presence or absence of the filter medium inside them, and when the detection means detects that there is no filter medium, that is, the transfer of the filter medium is completed. When the pump 17 is stopped, the pump 17 is stopped, and the transfer valve 18 and the filter medium transfer valve 22 are closed to end the filter medium transfer process, for example, a control means such as a computer is provided. Reduction and the amount of washing wastewater can be reduced.
[0027]
The time required for transferring the filter medium varies depending on the trapped state of turbidity, and the required time is not necessarily constant even when the same amount of filter medium is transferred. For this reason, in the past, the timer was set at a time slightly longer than the actual transfer time, so even after the transfer of the filter media was completed, the pump was operated and the power wasted wasted. It was a lot.
[0028]
Therefore, by directly detecting the end of the transfer of the filter medium and ending the filter medium transfer operation, it is possible to reduce power consumption and improve the filtration efficiency. Moreover, as a means for detecting the presence or absence of a filter medium, an optical device, a device using ultrasonic waves, or the like can be used.
[0029]
Further, with the start of the filter medium drawing process, the supply switching valves 27a and 27b are switched to open and close to change the raw water supply position from the raw water inflow part 11a during normal filtration operation to the raw water inflow part 11b located below. Since the filter medium rising from the inside of the filtration tank 10 toward the filter medium storage tank 15 is not stirred by the flow of the inflowing water, the trapped suspended matter can be raised while being held by the filter medium. That is, in the filter medium extraction step, raw water is allowed to flow from the lower raw water inflow portion 11b, whereby turbidity trapped by the filter medium can be sufficiently removed, and good treated water quality can be maintained. In addition, since the filter medium extraction process is completed in a short time due to the effect of installing the drain pipe 26, the same effect can be obtained even if the raw water inflow portion is only one place and the supply of raw water is stopped in the filter medium extraction process. I can expect.
[0030]
Moreover, it can also be set as the biofilm filtration apparatus which provided the aeration means in the lower part and filtration layer of the filtration tank 10, and added the purification | cleaning function by an aerobic biofilm. In the case of the filtration tank having the structure shown in this embodiment, an air vent is provided in the upper part of the filtration tank 10 through a screen that does not allow the filter medium to pass therethrough.
[0031]
FIG. 4 is a system diagram showing a second embodiment of the moving bed type filtration apparatus of the present invention. In the following description, the same components as those of the first embodiment are designated by the same reference numerals, and detailed description thereof is omitted.
[0032]
In order to reduce the height of the apparatus, the moving bed type filtration apparatus is provided with a filter medium storage tank 15 at a side position of the filter tank 10 and a filter medium inflow pipe 14 bent downward from the top of the filter tank 10. It connects with the lower part of the filter medium storage tank 15. FIG. Further, the upper part of the filtration tank 10 is opened, and a conical screen 61 for collecting the filter medium and an inverted conical dispersion plate 62 are provided in the upper part of the filtration tank, and an air diffuser connected to the compressor 63 in the lower part of the filtration tank. A device 64 is provided to function as a biofilm filtration device.
[0033]
During normal filtration operation, the raw water pump 29 and the compressor 63 are operated with all the valves closed, and the raw water is supplied into the filtration tank 10 as a downward flow from the raw water inflow portions 11a and 11b and diffused. Aeration from the device 64 is performed, and processing as a biofilm filtration device is performed. The treated water flows out from the treated water outflow portion 12 through the treated water outflow pipe 36 and the overflow weir 36a. At this time, the air bubbles rising in the filter layer are guided to the outer peripheral side of the tank by the dispersion plate 62, then pass through the screen 61 and exhausted above the filtration tank 10. Further, when the water level rises due to an aeration or an increase in filtration resistance, the water is discharged from the overflow pipe 65.
[0034]
The filter medium extraction step is performed by opening the filter medium inflow valve 13 and the drain valve 24. The filter medium collected by the screen 61 and floated to the upper center is the water in the filter medium storage tank 15, the drain valve 24, and the drain pipe. 26 and the filter medium storage tank from the upper end opening 14a opened to a predetermined position of the filter medium storage tank 15 through the filter medium inflow pipe 14 and the filter medium inflow valve 13 in a state accompanied by the water flow discharged through the overflow weir 26a. 15 flows in.
[0035]
Further, as another method for pulling out the filter medium, for example, the valves 67 and 68 are opened, the pump 17 is operated, and the water in the filter medium storage tank 15 is discharged. Furthermore, when the filtration tank 10 has a sealed structure that does not diffuse, the filter medium can be pushed out by the inflow water from the pump 29.
[0036]
The filter medium transfer process is performed by opening the shutoff valve 66, the transfer valve 18 and the filter medium transfer valve 22 and operating the pump 17 with the filter medium inflow valve 13 and the drain valve 24 closed. Thereby, the transfer water extracted from the bottom of the filtration tank 10 through the shutoff valve 66 is supplied to the ejector 16 through the transfer water pipe 20, and the filter medium is sucked from the filter medium storage tank 15 to filter the transfer medium transfer pipe 23. , And is transferred to a washing / drainage separation unit 21 provided at the bottom of the filtration tank 10. The flow rate balance between the transfer water and the extrusion water can be adjusted by the transfer water adjustment valve 19 and the extrusion water adjustment valve 37 in the same manner as described above. The turbidity separated from the filter medium by the cleaning / drainage separation unit 21 in this filtering medium transfer step is discharged from the lower part of the cleaning / drainage separation unit 21 through the cleaning / drainage discharge pipe 35 together with a part of the transfer water and the treated water.
[0037]
Thus, the formed bed moving type filtration apparatus of the present embodiment has the same function as that of the first embodiment, but the filter medium storage tank 15 is provided side by side at the side position of the filtration tank 10, The upper structure of the filtration device can be simplified, and the height of the device can be reduced. Furthermore, there is an advantage that adjustment and operability of each valve provided in the vicinity of the filter medium storage tank 15 are improved.
[0038]
In addition, although there is a concern that the installation area becomes large, since the filter medium storage tank 15 is smaller than the filtration tank 10 and the gantry can be simplified, the entire apparatus can be downsized.
[0039]
【The invention's effect】
As described above, according to the moving bed type filtration apparatus using the floating filter medium of the present invention, it is possible to shorten the time of the filter medium drawing process, and the turbidity is not returned to the filter tank, thereby increasing the filtration efficiency. be able to. Moreover, the filter medium and the suspended matter can be reliably separated in the filter medium transfer step, and clear treated water can be obtained stably. Furthermore, by starting the filter medium drawing process according to the state of the filter layer, it is possible to prevent the quality of the treated water from being deteriorated, and by ending the filter medium transfer process depending on the presence or absence of the filter medium, power costs are reduced and the amount of washing wastewater is reduced. Can be planned. Moreover, by arranging the filter medium storage tank at the side position of the filtration tank, the apparatus height can be lowered and the entire apparatus can be downsized.
[Brief description of the drawings]
FIG. 1 is a system diagram showing a first embodiment of a moving bed type filtration apparatus of the present invention.
FIG. 2 is a cross-sectional view showing another example of the shape of the cleaning / drainage separation unit.
FIG. 3 is a cross-sectional view showing still another example of the shape of the cleaning / drainage separation unit.
FIG. 4 is a system diagram showing a second embodiment of the moving bed type filtration apparatus of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 10 ... Filtration tank, 11a, 11b ... Raw water inflow part, 12 ... Treated water outflow part, 13 ... Filter medium inflow valve, 14 ... Filter medium inflow pipe, 14a ... Upper end opening part, 15 ... Filter medium storage tank, 16 ... Ejector, 17 ... Transfer water pump, 18 ... Transfer valve, 19 ... Transfer water adjustment valve, 20 ... Transfer water pipe, 21 ... Washing drain separator, 22 ... Filter medium transfer valve, 23 ... Filter medium transfer pipe, 24 ... Drain valve, 25 ... Drain adjustment valve , 26 ... drain pipe, 26 a ... overflow weir, 27 a and 27 b ... supply switching valve, 28 a and 28 b ... check valve, 29 ... raw water pump, 30 ... flow meter, 31 ... raw water inflow pipe, 32 ... inclined plate, 33 ... Washing drain valve, 34 ... Washing drain adjustment valve, 35 ... Washing drain discharge pipe, 35a ... Overflow weir, 36 ... Treated water outflow pipe, 36a ... Overflow weir, 37 ... Extrusion water regulation valve, 38 ... Extrusion water pipe, 39 ... Pressure gauge, 51 ... Perforated plate, 52 ... Screw member, 53 Throttle unit, 54 ... regulator, 55 ... grid presser, 61 ... screen, 62 ... distribution plate, 63 ... compressor, 64 ... air diffuser, 65 ... overflow pipe, 66 ... shutoff valve

Claims (9)

上部に原水流入部を、下部に処理水流出部を有するろ過槽と、該ろ過槽の頂部にろ材流入弁を有するろ材流入管を介して接続したろ材貯留槽と、該ろ材貯留槽の頂部に設けられたろ材吸引部と、ろ材移送水を前記ろ材吸引部に送水する移送水ポンプを有する移送水管と、ろ材吸引部でろ材貯留槽内のろ材を吸引同伴したろ材移送水を前記ろ過槽の底部に移送するろ材移送管とを備えた移床式ろ過装置であって、前記ろ材貯留槽に接続したろ材流入管の上端開口部を、ろ材貯留槽内に突出させて上向きに開口して前記ろ材貯留槽底部より上方に位置させるとともに、ろ材貯留槽の底部に排水管を接続したことを特徴とする浮上ろ材を用いた移床式ろ過装置。A filtration tank having a raw water inflow part at the top, a treated water outflow part at the bottom, a filter medium storage tank connected to the top of the filtration tank through a filter medium inflow pipe having a filter medium inflow valve, and a top of the filter medium storage tank The filter medium suction part provided, a transfer water pipe having a transfer water pump for feeding the filter medium transfer water to the filter medium suction part, and the filter medium transport water that sucks and entrains the filter medium in the filter medium storage tank in the filter medium suction part of the filter tank. a Utsuriyuka type filtration apparatus having a filter medium transfer tube for transferring the bottom, said top opening of the filter material filter material inflow tube connected to the reservoir, opens upward to be protruded to the filter material reservoir in the A floor moving type filtration apparatus using a floating filter medium, wherein the filter medium storage tank is positioned above the bottom of the filter medium storage tank, and a drain pipe is connected to the bottom of the filter medium storage tank. 前記ろ材流入管の開口高さがろ材貯留槽内において調節可能であることを特徴とする請求項1記載の浮上ろ材を用いた移床式ろ過装置。The moving bed type filtration apparatus using a floating filter medium according to claim 1, wherein the opening height of the filter medium inflow pipe is adjustable in the filter medium storage tank. 前記ろ過槽の底部に、ろ材と洗浄排水とを分離する洗浄排水分離部を設けたことを特徴とする請求項1記載の浮上ろ材を用いた移床式ろ過装置。The moving bed type filtration apparatus using the floating filter medium according to claim 1, wherein a washing drainage separation part for separating the filter medium and the washing drainage is provided at the bottom of the filtration tank. 前記ろ過槽内に、ろ層の膨張を防止するためのグリッド押えを設けたことを特徴とする請求項1記載の浮上ろ材を用いた移床式ろ過装置。2. The floor moving type filtration apparatus using the floating filter medium according to claim 1, wherein a grid presser for preventing expansion of the filter layer is provided in the filtration tank. 前記ろ過槽に、ろ層の膨張を検知したときに、ろ過速度調整又はろ材洗浄開始を行う手段を設けたことを特徴とする請求項1記載の浮上ろ材を用いた移床式ろ過装置。The moving bed type filtration apparatus using the floating filter medium according to claim 1, wherein the filtration tank is provided with means for adjusting the filtration rate or starting the filter medium washing when the expansion of the filter layer is detected. 前記ろ材貯留槽から移送水管を経てろ過槽へのろ材の移送が終了したことを検知し、ろ材移送運転を終了させる手段を設けたことを特徴とする請求項1記載の浮上ろ材を用いた移床式ろ過装置。The transfer using the floating filter medium according to claim 1, further comprising means for detecting that the transfer of the filter medium from the filter medium storage tank to the filter tank through the transfer water pipe is completed and terminating the filter medium transfer operation. Floor type filtration device. 前記ろ材流入弁を開いてろ過槽からろ材貯留槽にろ材を流入させるときに、原水流入位置の変更又は原水の流入停止を行う手段を設けたことを特徴とする請求項1記載の浮上ろ材を用いた移床式ろ過装置。The floating filter medium according to claim 1, further comprising means for changing the raw water inflow position or stopping the flow of raw water when the filter medium inflow valve is opened to allow the filter medium to flow from the filter tank into the filter medium storage tank. The moving bed type filtration device used. 前記ろ過槽の下部に散気手段を設けたことを特徴とする請求項1記載の浮上ろ材を用いた移床式ろ過装置。The moving bed type filtration apparatus using the floating filter medium according to claim 1, wherein a diffuser is provided at a lower portion of the filtration tank. 前記ろ材貯留槽が、前記ろ過槽の側方位置に併設されており、前記ろ材流入管は、ろ過槽の頂部から下方に屈曲してろ材貯留槽の下部に接続されていることを特徴とする請求項1記載の浮上ろ材を用いた移床式ろ過装置。The filter medium storage tank is provided side by side in the filtration tank, and the filter medium inflow pipe is bent downward from the top of the filter tank and connected to the lower part of the filter medium storage tank. A moving bed type filtration apparatus using the floating filter medium according to claim 1.
JP24514599A 1999-08-31 1999-08-31 Moving bed type filtration equipment using floating media Expired - Fee Related JP4249855B2 (en)

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