JP3567392B2 - Sludge thickener - Google Patents

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JP3567392B2
JP3567392B2 JP05218496A JP5218496A JP3567392B2 JP 3567392 B2 JP3567392 B2 JP 3567392B2 JP 05218496 A JP05218496 A JP 05218496A JP 5218496 A JP5218496 A JP 5218496A JP 3567392 B2 JP3567392 B2 JP 3567392B2
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sludge
tank
floating
concentrated
water
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JPH09239400A (en
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護 皆方
正章 吉野
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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】
本発明は下水中の汚泥を濃縮する装置に係り、特に汚泥に加圧微細気泡を付着させることにより汚泥を加圧浮上させて濃縮する加圧浮上式汚泥濃縮装置に関するものである。
【0002】
【従来の技術】
図7は従来の加圧浮上式汚泥濃縮装置の一例を示すフロー説明図である。まず処理する原汚泥が、原汚泥貯留タンク21からポンプにより流入管26を通って汚泥濃縮装置23の汚泥槽24内に送り込まれる。このとき、流入管26途中に加圧空気溶解水タンク22から圧縮空気を溶解した加圧空気溶解水が供給路27より送り込まれ、原汚泥と混合される。汚泥槽24内において、汚泥には加圧空気溶解水中の微細気泡が付着し、この微細気泡の浮力により浮上汚泥28となって浮上する。浮上汚泥28は汚泥水面上部で堆積、濃縮し、汚泥水面上部に設けられた、エンドレスチェーン等に取り付けられた掻取り板25aを有する濃縮汚泥掻取り機25によって矢印方向に定期的に掻き取られる。掻き取られた浮上汚泥28は、脱気槽29に送られ、攪拌翼29aにより一定時間攪拌されて、付着した気泡を分離する、いわゆる脱気処理を行った後、濃縮汚泥として回収される。微細気泡が付着しなかった汚泥や比重の大きい汚泥は沈澱汚泥となって汚泥槽24の底部に設けた沈澱汚泥掻き寄せ機30により掻き寄せられ、回収される。また、これら浮上汚泥、沈澱汚泥から分離した加圧空気溶解水は分離水として回収される。
【0003】
【発明が解決しようとする課題】
上記の従来の汚泥濃縮装置では、以下の課題を有していた。
(1)濃縮汚泥掻取り機25による濃縮汚泥の掻き取り速度は濃縮汚泥に攪拌作用を起こさないような速度(例えば60cm/分程度)でなければならない。なぜなら汚泥水面上に堆積、濃縮された濃縮汚泥のうち、最も汚泥濃度が高いのは最上部の濃縮汚泥であり、この最上部の濃縮汚泥を掻き取るときに乱れが生じるとその下層の濃度の低い濃縮汚泥と混合してしまい、回収する濃縮汚泥の濃度が低くなってしまうからである。この掻き取り速度を速くすると、汚泥の処理時間は短くなるが、掻き取られる濃縮汚泥に乱れが生じ易くなり、回収される濃縮汚泥の濃度は低くなり、逆に分離水中の汚泥濃度は高くなってしまう。また、速度を遅くすると汚泥の処理時間は長くなり、また浮上汚泥の堆積量が多くなるため装置規模の大きいものが必要となる。その時々の原汚泥の濃度、状態は異なるためこの掻き取り速度値の決定は非常に困難なものとなっている。
(2)掻取り板25aの汚泥水面に対する高さ方向の位置は、汚泥水面に近づけた方が一度に掻き取る濃縮汚泥量が多くなり効率的であるが、大量の浮上汚泥を掻き取る間に汚泥が攪拌されてしまうため、前記同様、回収される汚泥の濃度が低くなってしまう。この掻取り板25aの位置設定も非常に困難なものとなる。
(3)浮上汚泥を掻き取った後に,攪拌、脱気処理工程(29)に回すので,いわゆる汚泥の濃縮フロー効率が悪いものとなっている。
(4)汚泥濃縮装置23内に流入した汚泥は、汚泥槽24の内壁に容易に付着、積層するために、頻繁に汚泥槽24の内壁を清掃する必要があった。
【0004】
本発明は上述の課題を解消するために創案されたものであり、簡単な構造で、濃縮汚泥を高濃度で回収でき、また濃縮汚泥中の微細気泡を取り除くいわゆる脱気処理を同時に行え、さらに頻繁に汚泥槽の内壁の清掃を行う必要のない汚泥濃縮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】
本発明は前記の目的を達成するために以下の手段を用いた。
まず、濃縮汚泥を高濃度で回収し、また同時に濃縮汚泥の脱気を行うための手段として、加圧空気溶解水を混入した汚泥水を導入する汚泥槽と、加圧空気と混和され、浮上した汚泥を汚泥槽内において凝集させる浮上汚泥凝集手段と、汚泥水の液面上に配設され、濃縮、堆積した汚泥を撥ね飛ばし脱気するための回転翼とを設けた。また、前記汚泥槽を、有底円筒形状の沈殿汚泥槽と、この沈殿汚泥槽に内嵌される有蓋円筒形状の浮上汚泥槽とにより構成し、前記沈殿汚泥槽には沈殿汚泥を排出するための沈殿汚泥排出管を接続し、また、前記浮上汚泥槽には脱気された汚泥を排出するための濃縮汚泥排出管を接続した。さらに、前記浮上汚泥凝集手段を、上下部が開放された汚泥ガイド板により構成し、この汚泥ガイド板は、その下端部を前記濃縮汚泥排出管の下端部より下側に位置する汚泥槽の内壁に固定、封止すると共に、その上端部を前記汚泥水の液面レベルより上に位置する浮上汚泥槽の内部に配設した。また、前記浮上汚泥槽の上部に、前記回転翼を回転駆動させるためのモータを載置した。
【0006】
また、汚泥槽内壁清掃の頻度低減のための手段として、前記沈殿汚泥槽に、前記モータにより回転駆動され、沈殿汚泥槽の内壁に沿って移動して、当該沈殿汚泥槽に付着した沈殿汚泥を掻き取る沈殿汚泥用スクレーパを設けた。また、前記浮上汚泥槽に、前記モータにより回転駆動され、浮上汚泥槽の内壁に沿って移動して、当該浮上汚泥槽に付着した濃縮汚泥を掻き取る濃縮汚泥用スクレーパを設けた。さらに、前記汚泥ガイド板に、前記モータにより回転駆動され、汚泥ガイド板の内壁に沿って移動して、当該汚泥ガイド板に付着した浮上汚泥を掻き取る浮上汚泥用スクレーパを設けた。
そして、装置全体を部品点数の少ない簡単な構造とするため、前記沈殿汚泥槽と浮上汚泥槽との間に、外部に分離水を排出するための通路を形成するように構成した。さらに、前記回転翼、濃縮汚泥用スクレーパ、浮上汚泥用スクレーパおよび沈澱汚泥用スクレーパを1台のモータの回転軸に取り付け、それぞれ異なる回転数で回転が可能となるようにした。
【0007】
また、浮上汚泥の浮上効率を上げる目的のため、加圧空気溶解水を作用させた汚泥水を汚泥槽内に噴出させる噴出口近傍に、前記汚泥水の流れを上部方向に導くための流れ方向規制部材を設けた。特に、この流れ方向規制部材を前記噴出口を囲む、上部が開口し、周側面および底面が閉塞された円筒形状の部材とした。
【0008】
【発明の実施の形態】
本発明の実施の形態を図面を参照して説明する。図1の(a)および(b)は本発明に係る汚泥濃縮装置の上面図および側面図、図2は図1におけるA−A断面図、図3は図1におけるB−B断面図、図4は図1におけるC−C断面図、図5は汚泥濃縮装置の全体斜視図、図6の(a)は同要部説明図であり、(b)は他の実施形態における一部説明図である。
これらの図中,符号1は汚泥濃縮装置を示す。この汚泥濃縮装置1は、処理する原汚泥を圧縮空気を水に溶解した加圧空気溶解水と共に噴出口10aから取り込み、汚泥槽18内部で汚泥を浮上、濃縮させ、その濃縮汚泥を濃縮汚泥排出管9へ、沈澱汚泥は沈澱汚泥排出管4へ、浮上または沈澱した汚泥から分離した分離水を分離水排出管7へ、それぞれ排出させるものである。
【0009】
汚泥槽18は、2つの筐体部材である沈澱汚泥槽2および浮上汚泥槽3により構成される。
沈澱汚泥槽2は上部が開口した有底円筒形状の部材で、その下方部において下部が狭まったテーパ形状を成し、底部において再び径の小さい円筒形状を形成している。この底部円筒部の側壁には沈澱汚泥を排出させるための孔2aが穿設され、沈澱汚泥排出管4が接続されている。沈澱汚泥槽2の上縁周囲には、分離水がその上縁から溢れ出たときの受けとして、断面L字状の分離水受枠5が全周にわたって取り付けられている。この分離水受枠5の一部は筐体6を形成しており、その底部には孔6aが穿設され、分離水排出管7が接続されている。
【0010】
浮上汚泥槽3は、下部が開口した有蓋円筒形状の部材であり、その外径は分離水の通路19を形成する程度に沈澱汚泥槽2の内径よりも小さい寸法で、固定部材(図示せず)により、沈澱汚泥槽2の内側に同心円状に内嵌、固定されている。浮上汚泥槽3の側壁には、脱気された汚泥を排出するための孔3aが穿設され、濃縮汚泥排出管9が接続されている。濃縮汚泥排出管9は、沈澱汚泥槽2の側壁に穿設された孔2bを貫通し(その接触部位は溶接等により封止され)、次処理工程に続いている。
【0011】
そして、浮上汚泥槽3の内部には、浮上汚泥凝集手段としての上下部が開放された円錐台形状の汚泥ガイド板8が配設される。この汚泥ガイド板8は、浮上汚泥を上方向に導き凝集させるため、および後述する回転翼16により撥ね飛ばされ、脱気された濃縮汚泥と前記浮上汚泥とを隔離させるためのものであり、その下端部は濃縮汚泥排出管9の下端部より下側に位置する浮上汚泥槽3の内壁に固定、封止されている。汚泥ガイド板8の上部は、その全周にわたって鉛直に立ち上がるつば部8aを形成している。このつば部8aは、図2および図6(a)に示すように汚泥濃縮装置1内に流入された汚泥水の液面レベル(W.L.)よりやや上に位置するように立ち上げてあり、液面上に凝集された浮上汚泥を堆積、濃縮させておくためのものである。
【0012】
濃縮汚泥排出管9と対向する側で汚泥ガイド板8の下端部から下に位置する沈澱汚泥槽2および浮上汚泥槽3の側壁には、それぞれ孔2c、3b(図2)が穿設され、これらの孔2c、3bに、加圧空気溶解水が混合された原汚泥が流れる汚泥流入管10が貫通し(その接触部位は溶接等により封止され)、汚泥濃縮装置1内部中央付近まで延出し、その先端を噴出口10aとしている。この汚泥流入管10は、原汚泥が貯留されている原汚泥タンク(図示せず)からポンプによって原汚泥を送る原汚泥流入管10bと、これに分岐接続され、原水に圧縮空気を高濃度で溶解した加圧空気溶解水をポンプにより送る加圧空気溶解水流入管10cとからなる。
【0013】
沈澱汚泥槽2の内部には、汚泥流入管10の噴出口10aから噴出する汚泥水の流れを上方向に導く流れ方向規制部材11を配設する。流れ方向規制部材11は、沈澱汚泥槽2と同一軸線上に設けた,上部が開口し,周側面および底面が閉塞された有底円筒形状の部材であり、その内方に噴出口10aが臨むように、側壁に穿設された孔に汚泥流入管10を貫通しており、その接触部位は溶接等により封止、固定されている。また、流れ方向規制部材11の底面中央には後述するモータ12に取り付けられたシャフト12aが貫通できるように孔が穿設されている。
【0014】
浮上汚泥槽3の上面の中心部にはモータ12が載置され、このモータ12に、図示しない変速機によってそれぞれ回転数を調整し得る第1、第2および第3の3つのシャフト12a、12b、12cを取り付ける。第1のシャフト12aは下方に伸び、前述の流れ方向規制部材11の底面に穿設された孔を貫通して沈澱汚泥槽2の底面に支承された軸受13に挿嵌している。これら回転数の異なる3つのシャフトにはそれぞれの目的を持った羽状の部材が取り付けられている。
【0015】
まず、第1のシャフト12aには上側と下側にそれぞれ複数本、本形態では4本のブラケット14a、15aがシャフト12aに対して直角に、そして互いに同一角度となるように放射状に取り付けられている。上側のブラケット14aの先端には、それぞれ汚泥ガイド板8の内壁に沿う形状および長さ寸法の板状部材からなる浮上汚泥用スクレーパ14が、また、下側のブラケット14bの先端には、それぞれ沈澱汚泥槽2のテーパ部の内壁に沿う形状および長さ寸法の板状部材からなる沈澱汚泥用スクレーパ15が取り付けられている。第1のシャフト12aを回転させることにより、浮上汚泥用スクレーパ14は汚泥ガイド板8の内壁に付着した浮上汚泥をその回転により汚泥ガイド板8の内壁に沿って移動し掻き取る。この浮上汚泥用スクレーパ14は図3に示すように、その回転方向側を汚泥ガイド板8の内壁に接するか、僅かの間隙(数mm程度)を形成するように近接して、汚泥ガイド板8の横断面円の接線方向に対して所定角度を成すようにブラケット14aに取り付けられている。
一方、沈澱汚泥用スクレーパ15は沈澱汚泥槽2のテーパの形成された内壁に付着した沈澱汚泥をその回転により内壁に沿って移動し掻き取る。この沈澱汚泥用スクレーパ15は、浮上汚泥用スクレーパ14と同様に、回転方向側を沈澱汚泥槽2のテーパ内壁に接するか,僅かの間隙を形成するように近接して、テーパ内壁の横断面円接線方向に対して所定角度を成すようにブラケット15aに取り付けられている。
シャフト12aの周辺速度は高速にすると浮上汚泥用スクレーパ14および沈澱汚泥用スクレーパ15によって掻き取られた汚泥が槽内で攪乱してしまうので適切ではなく、およそ2〜3m/分以下の低速回転が望ましい。
本形態では、浮上汚泥用スクレーパおよび沈澱汚泥用スクレーパを同じシャフトに取り付けたが、もちろんシャフトをもう1つ設けて、別々の回転数とした仕様にしてもよい。
【0016】
次に、第2のシャフト12bには複数枚、本形態では4枚の矩形板状部材の回転翼16がシャフト12bに対して直角に、そして互いに同一角度となるように放射状に取り付けられている。第2のシャフト12bを回転させることにより、この回転翼16は回転し、汚泥ガイド板8のつば部8a内に堆積された濃縮汚泥を浮上汚泥槽3の内壁に向かって撥ね飛ばして、脱気するものである。浮上汚泥を効率よく撥ね飛ばし、脱気するために、回転翼16の先端から、180度反対に位置する回転翼16の先端までの寸法(図6(a)におけるL寸法)はつば部8aの径と略同一寸法であり、また回転翼16の下縁とつば部8aの上縁の間隙寸法(図6(a)におけるH寸法)は0〜数mm程度である。
また気泡の付着している濃縮汚泥の脱気は、回転翼16との衝突力、および回転翼16の回転に対して接線方向に跳ねとばされたときの浮上汚泥槽3の内壁に対する衝突力により左右されるので、その衝突力を大きくすべくシャフト12bの回転速度は100rpm以上の高速回転が望ましい。
【0017】
第3のシャフト12cには複数本、本形態では4本のブラケット17aがシャフト12cに対して直角に、そして互いに直角に放射状に取り付けられている。ブラケット17aの先端には、それぞれ浮上汚泥槽3の内壁に沿う形状で、かつ、浮上汚泥槽3の内壁上端から既述の濃縮汚泥排出管9の開口部上縁近傍までの長さ寸法の矩形板状部材からなる濃縮汚泥用スクレーパ17が取り付けられている。第3のシャフト12cを回転することにより、この濃縮汚泥用スクレーパ17は、浮上汚泥槽3の上部内壁に付着した濃縮汚泥(前記回転翼16により脱気された汚泥)をその回転により浮上汚泥槽3の内壁に沿って移動し掻き取る。図4に示すように、濃縮汚泥用スクレーパ17は回転方向側を浮上汚泥槽3の内壁に接するか,僅かの間隙(数mm程度)を形成するように近接して、浮上汚泥槽3の横断面円の接線方向に対して所定角度を成すようにブラケット17aに取り付けられている。
濃縮汚泥用スクレーパ17は濃縮汚泥を掻き落とすだけなので高速回転である必要はなく、回転翼16により撥ね飛ばされ浮上汚泥槽3に付着する濃縮汚泥の量にもよるが、シャフト12cの周辺速度は2〜3m/分以下の低速回転が望ましい。
【0018】
次に、本装置の作用について説明する。
処理する原汚泥が貯留された原汚泥タンクからポンプによって原汚泥が原汚泥流入管10b内を流れる。一方、原水に圧縮空気が高濃度に溶解した加圧空気溶解水が貯留された加圧空気溶解水タンクからポンプによって加圧空気溶解水が空気溶解水流入管10c内を流れる。両者は、両管の接続部で混合し、噴出口10aから汚泥水として汚泥濃縮装置1内部へと噴出する。噴出した汚泥水はまず、流れ方向規制部材11の内壁に衝突する。流れ方向規制部材11の下面は閉塞されているので汚泥水は流れ方向規制部材11の内壁に沿って上方向へと流れを変える。また、汚泥水中の原汚泥には、槽内において、大気圧下で加圧空気溶解水から発生する微細気泡が付着する。原汚泥は付着した微細気泡の浮力により浮上汚泥となって浮上する。
ここで微細気泡と付着しなかった汚泥成分は沈澱汚泥となって沈降する。沈澱汚泥槽2のテーパ内壁に沈降した沈澱汚泥は、テーパ内壁に沿って回転移動する沈澱汚泥用スクレーパ15によって掻き取られる。沈澱汚泥用スクレーパ15は低速度で掻き取りを行うため、沈澱汚泥は汚泥水内で攪拌されることなく沈澱汚泥槽2の底部へと沈澱していく。そして、沈澱汚泥排出管4を介して沈澱汚泥処理工程へと搬送される。また、浮上汚泥および沈澱汚泥が分離した後の余剰の加圧空気溶解水は、分離水として、沈澱汚泥槽2の内壁と浮上汚泥槽3の外壁との間に形成された通路19を通って沈澱汚泥槽2の上縁から溢れ出て分離水受枠5内に流出する。そして、分離水受枠5の一部に形成された筐体6に流れて孔6aから分離水排出管7を介して分離水処理工程へと排出される。
【0019】
さて微細気泡の付着した浮上汚泥は、浮上汚泥凝集手段としての汚泥ガイド板8の内側を浮上しながら次第に凝集され、つば部8a内において堆積する。浮上途中、汚泥ガイド板8の内壁に付着した浮上汚泥は、その内壁に沿って回転移動する浮上汚泥用スクレーパ14によって掻き取られる。浮上汚泥用スクレーパ14は沈澱汚泥用スクレーパ15と同じ低速度で掻き取りを行うため、浮上汚泥は汚泥水内で攪拌されることなく、再びつば部8a付近の汚泥水面に向かって浮上し始める。図6(a)に示すように、浮上汚泥の堆積量を多くして汚泥を高濃度に濃縮させるため、汚泥水の液面レベルはつば部8aの、つば部8a立ち上がり近傍に位置している。この液面上まで浮上してきた浮上汚泥は堆積し、次第に濃縮される。そして、この堆積した濃縮汚泥のうち最も汚泥濃度の高い最上部の濃縮汚泥は高速度で回転する回転翼16によってその回転方向に撥ね飛ばされる。このとき汚泥は回転翼16との衝突による衝撃力および浮上汚泥槽3の内壁との衝突による衝撃力により容易に脱気される。浮上汚泥槽3の内壁に付着した濃縮汚泥は、浮上汚泥槽3の内壁に沿って回転移動する濃縮汚泥用スクレーパ17により随時掻き落とされるため壁面で乾燥、固化することがない。そして、掻き取られた濃縮汚泥は浮上汚泥槽3の壁面に穿設された孔3aを通って濃縮汚泥排出管9へ排出、回収される。
【0020】
さて、以上説明した本発明に係る汚泥濃縮装置では、モータに取り付けた各羽状部材、回転翼、濃縮汚泥用スクレーパ、浮上汚泥用スクレーパおよび沈澱汚泥用スクレーパを全て4枚ずつとしたが、もちろんこれに限られることなく、1枚としても構わない。通常は2〜4枚である。
なお、図6(b)に示すようにモータ回転軸に対し角度θだけ傾斜させて回転翼をシャフトに取り付ければ、回転翼に衝突した濃縮汚泥は水平方向より常に上方に撥ね飛ばされるため、つば部8aに堆積した濃縮汚泥に戻されることなく、効率の良い脱気処理が可能となる。
【0021】
また、流れ方向規制部材11は上述した円筒形状のものに限られるものでなく、汚泥槽内に流入してくる汚泥水の流れを上部方向に導く態様のものであればよい。
【0022】
【発明の効果】
上述の構成からなる本発明の汚泥濃縮装置によれば、以下のような効果を奏する。
(1)汚泥水面に堆積、濃縮した汚泥のうち、十分な濃縮がなされた最上部の濃縮汚泥のみを回転翼により高速で撥ね飛ばすため、乱れが生じず、下層の濃度の低い汚泥と混ざることなく、極めて高濃度の濃縮汚泥を回収することができる。
(2)微細気泡の付着した濃縮汚泥の脱気処理を汚泥の濃縮と同時に行うことができるので、脱気処理槽を別個に設ける必要がなくなり、汚泥の濃縮フロー効率が向上する。(3)汚泥槽内壁に付着した濃縮汚泥、浮上汚泥、沈澱汚泥をそれぞれ掻き取るスクレーパを設けたので、汚泥槽内壁の清掃頻度が低減される。
(4)汚泥槽を略円筒形状として、上述の回転翼、各スクレーパを1台のモータにより回転駆動させる構造としたため、コンパクトかつ機器点数の少ない装置が実現される。
(5)汚泥槽内に流入する汚泥水の流れを上部方向に導く流れ方向規制部材を設けたので、汚泥槽内の汚泥水に乱れが生じることがなく、浮上汚泥の浮上効率が上がる。
【図面の簡単な説明】
【図1】(a)および(b)は本発明に係る汚泥濃縮装置の上面図および側面図である。
【図2】図1におけるA−A断面図である。
【図3】図1におけるB−B断面図である。
【図4】図1におけるC−C断面図である。
【図5】汚泥濃縮装置の全体斜視図である。
【図6】(a)は要部説明図であり、(b)は他の実施形態における要部説明図である。
【図7】従来の加圧浮上式汚泥濃縮装置の一例を示すフロー説明図である。
【符号の説明】
1 汚泥濃縮装置
2 沈澱汚泥槽
3 浮上汚泥槽
4 沈澱汚泥排出管
5 分離水受枠
6 筐体
7 分離水排出管
8 汚泥ガイド板
9 濃縮汚泥排出管
10 汚泥流入管
10a 噴出口
10b 原汚泥流入管
10c 空気溶解水流入管
11 流れ方向規制部材
12 モータ
12a,12b,12c シャフト
13 軸受
14 浮上汚泥用スクレーパ
14a ブラケット
15 沈澱汚泥用スクレーパ
15a ブラケット
16 回転翼
17 濃縮汚泥用スクレーパ
17a ブラケット
18 汚泥槽
19 通路
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an apparatus for concentrating sludge in sewage, and more particularly to a press-floating type sludge concentrating apparatus for condensing sludge under pressure by attaching pressurized fine bubbles to the sludge.
[0002]
[Prior art]
FIG. 7 is a flow explanatory diagram showing an example of a conventional pressurized floating sludge concentrator. First, raw sludge to be treated is sent from a raw sludge storage tank 21 into a sludge tank 24 of a sludge concentrating device 23 through an inflow pipe 26 by a pump. At this time, pressurized air-dissolved water obtained by dissolving compressed air from the pressurized air-dissolved water tank 22 is fed into the inlet pipe 26 from the supply path 27 and mixed with the raw sludge. In the sludge tank 24, the fine bubbles in the pressurized air-dissolved water adhere to the sludge, and float up as floating sludge 28 by the buoyancy of the fine bubbles. The floating sludge 28 is deposited and concentrated at the upper part of the sludge water surface, and is periodically scraped in the direction of the arrow by a concentrated sludge scraper 25 having a scraper plate 25a attached to an endless chain or the like provided at the upper part of the sludge water surface. . The scraped floating sludge 28 is sent to a deaeration tank 29, and is stirred for a certain period of time by a stirring blade 29a. After performing a so-called deaeration process for separating attached bubbles, the sludge is collected as a concentrated sludge. Sludge to which fine bubbles have not adhered or sludge having a large specific gravity is settled as sludge and is collected by the settling sludge scraper 30 provided at the bottom of the sludge tank 24 and collected. The pressurized air-dissolved water separated from the floating sludge and the settled sludge is recovered as separated water.
[0003]
[Problems to be solved by the invention]
The above-described conventional sludge concentrator has the following problems.
(1) The speed of scraping the concentrated sludge by the concentrated sludge scraper 25 must be a speed (for example, about 60 cm / min) that does not cause a stirring action on the concentrated sludge. Because the concentrated sludge with the highest concentration among the concentrated sludge deposited and concentrated on the sludge water surface is the concentrated sludge at the top, and if the turbulence occurs when scraping the concentrated sludge at the top, the concentration of the lower layer is reduced. This is because they are mixed with low concentrated sludge, and the concentration of concentrated sludge to be recovered becomes low. When the scraping speed is increased, the sludge treatment time is shortened, but the concentrated sludge to be scraped is easily disturbed, the concentration of the concentrated sludge to be recovered is low, and the concentration of the sludge in the separation water is high. Would. If the speed is reduced, the sludge treatment time becomes longer, and the amount of floating sludge deposited increases, so that a large-scale apparatus is required. Since the concentration and condition of the raw sludge at each time differ, it is very difficult to determine the scraping speed value.
(2) As for the position of the scraping plate 25a in the height direction with respect to the sludge water surface, the closer to the sludge water surface, the more the concentrated sludge to be scraped at a time and the more efficient it is. Since the sludge is agitated, the concentration of the recovered sludge decreases as described above. It is also very difficult to set the position of the scraping plate 25a.
(3) Since the floating sludge is scraped and then passed to the stirring and deaeration step (29), the so-called sludge concentration flow efficiency is poor.
(4) The sludge that has flowed into the sludge concentrator 23 has to be frequently cleaned on the inner wall of the sludge tank 24 in order to easily adhere to and stack on the inner wall of the sludge tank 24.
[0004]
The present invention has been devised in order to solve the above-described problems, has a simple structure, can collect concentrated sludge at a high concentration, and can simultaneously perform a so-called deaeration process for removing fine bubbles in the concentrated sludge. It is an object of the present invention to provide a sludge concentrating device that does not need to frequently clean the inner wall of a sludge tank.
[0005]
[Means for Solving the Problems]
The present invention uses the following means to achieve the above object.
First, as a means for collecting concentrated sludge at a high concentration and simultaneously degassing the concentrated sludge, a sludge tank for introducing sludge water mixed with pressurized air-dissolved water is mixed with pressurized air and floated. Floating sludge aggregating means for agglomerating the collected sludge in the sludge tank, and a rotary blade disposed on the liquid surface of the sludge water for repelling and degassing the concentrated and accumulated sludge are provided. In addition, the sludge tank is constituted by a bottomed cylindrical sedimentation sludge tank, and a closed cylindrical floating sludge tank fitted inside the sedimentation sludge tank, for discharging the sedimentation sludge to the sedimentation sludge tank. The concentrated sludge discharge pipe for discharging the degassed sludge was connected to the floating sludge tank. Further, the floating sludge aggregating means is constituted by a sludge guide plate having upper and lower portions opened, and the lower end portion of the sludge guide plate has an inner wall located below the lower end portion of the concentrated sludge discharge pipe. And the upper end was disposed inside a floating sludge tank located above the liquid level of the sludge water. Further, a motor for rotating and driving the rotor was mounted on the upper part of the floating sludge tank.
[0006]
Further, as means for reducing the frequency of cleaning the inner wall of the sludge tank, the settling sludge tank is rotated and driven by the motor, moves along the inner wall of the settling sludge tank, and deposits the sludge attached to the settling sludge tank. A scraper for settling sludge to be scraped was provided. In addition, the floating sludge tank is provided with a concentrated sludge scraper that is rotated by the motor, moves along the inner wall of the floating sludge tank, and scrapes the concentrated sludge attached to the floating sludge tank. Further, the sludge guide plate is provided with a floating sludge scraper that is driven to rotate by the motor, moves along the inner wall of the sludge guide plate, and scrapes the floating sludge attached to the sludge guide plate.
Then, in order to make the entire apparatus a simple structure with a small number of parts, a passage for discharging separated water to the outside is formed between the settling sludge tank and the floating sludge tank. Further, the rotary blade, the scraper for concentrated sludge, the scraper for floating sludge, and the scraper for settled sludge are mounted on the rotating shaft of one motor so that they can be rotated at different rotation speeds.
[0007]
In addition, for the purpose of increasing the floating efficiency of the floating sludge, a flow direction for guiding the flow of the sludge water upward in the vicinity of an ejection port for ejecting the sludge water to which the pressurized air dissolved water has been applied into the sludge tank. A regulating member was provided. In particular, the flow direction regulating member is a cylindrical member that surrounds the spout and has an open top and closed peripheral side and bottom surfaces.
[0008]
BEST MODE FOR CARRYING OUT THE INVENTION
An embodiment of the present invention will be described with reference to the drawings. 1A and 1B are a top view and a side view of a sludge concentrating apparatus according to the present invention, FIG. 2 is a sectional view taken along line AA in FIG. 1, FIG. 3 is a sectional view taken along line BB in FIG. 4 is a cross-sectional view taken along the line CC in FIG. 1, FIG. 5 is an overall perspective view of the sludge concentrator, FIG. 6 (a) is an explanatory view of the main part, and FIG. 6 (b) is a partial explanatory view in another embodiment. It is.
In these figures, reference numeral 1 indicates a sludge concentrator. This sludge concentrator 1 takes in raw sludge to be treated together with pressurized air-dissolved water obtained by dissolving compressed air in water from an ejection port 10a, floats and concentrates sludge inside a sludge tank 18, and discharges the concentrated sludge into concentrated sludge. The settled sludge is discharged to the settled sludge discharge pipe 4 to the pipe 9 and the separated water separated from the floated or settled sludge to the separated water discharge pipe 7.
[0009]
The sludge tank 18 is constituted by a settling sludge tank 2 and a floating sludge tank 3 which are two housing members.
The sedimentation sludge tank 2 is a cylindrical member with a bottom and an open top. The lower part has a tapered shape with a lower part narrowed, and the bottom part again has a small diameter cylindrical shape. A hole 2a for discharging the settled sludge is formed in the side wall of the bottom cylindrical portion, and a settled sludge discharge pipe 4 is connected to the hole 2a. Around the upper edge of the settling sludge tank 2, a separated water receiving frame 5 having an L-shaped cross section is attached around the entire circumference as a receiver when the separated water overflows from the upper edge. A part of the separated water receiving frame 5 forms a housing 6, and a hole 6 a is formed at the bottom thereof, and a separated water discharge pipe 7 is connected to the housing 6.
[0010]
The floating sludge tank 3 is a closed cylindrical member having an open lower part, the outer diameter of which is smaller than the inner diameter of the sedimentation sludge tank 2 so as to form the passage 19 for the separated water, and a fixing member (not shown). ), It is fitted and fixed concentrically inside the settling sludge tank 2. A hole 3a for discharging degassed sludge is formed in the side wall of the floating sludge tank 3, and a concentrated sludge discharge pipe 9 is connected to the hole 3a. The concentrated sludge discharge pipe 9 penetrates a hole 2b formed in the side wall of the settling sludge tank 2 (the contact portion is sealed by welding or the like) and continues to the next processing step.
[0011]
Inside the floating sludge tank 3, there is disposed a frusto-conical sludge guide plate 8 having upper and lower portions opened as floating sludge aggregating means. The sludge guide plate 8 is for guiding the floating sludge upward and coagulating, and for separating the floating sludge from the concentrated sludge degassed and degassed by the rotating blades 16 described later. The lower end is fixed and sealed to the inner wall of the floating sludge tank 3 located below the lower end of the concentrated sludge discharge pipe 9. The upper part of the sludge guide plate 8 forms a brim portion 8a that rises vertically over the entire circumference. As shown in FIG. 2 and FIG. 6 (a), the flange portion 8a rises so as to be located slightly above the liquid level (WL) of the sludge water flowing into the sludge concentration device 1. Yes, it is for accumulating and condensing the floating sludge aggregated on the liquid surface.
[0012]
Holes 2 c and 3 b (FIG. 2) are formed in the side walls of the settling sludge tank 2 and the floating sludge tank 3 located below the lower end of the sludge guide plate 8 on the side facing the concentrated sludge discharge pipe 9, respectively. Through these holes 2c and 3b, a sludge inflow pipe 10 through which raw sludge mixed with pressurized air-dissolved water flows penetrates (the contact portion is sealed by welding or the like) and extends to near the center of the sludge concentration device 1. The tip is formed as a jet port 10a. This sludge inflow pipe 10 is connected to a raw sludge inflow pipe 10b for sending raw sludge by a pump from a raw sludge tank (not shown) in which raw sludge is stored, and is connected to the sludge inflow pipe 10b so that compressed air is supplied to raw water at a high concentration. And a pressurized air dissolved water inflow pipe 10c for sending the dissolved compressed air dissolved water by a pump.
[0013]
Inside the settling sludge tank 2, a flow direction regulating member 11 for guiding the flow of the sludge water spouting from the spout 10a of the sludge inflow pipe 10 upward is provided. The flow direction regulating member 11 is a bottomed cylindrical member provided on the same axis as the sedimentation sludge tank 2 and having an open upper part and a closed peripheral side surface and bottom surface. As described above, the sludge inflow pipe 10 penetrates the hole formed in the side wall, and the contact portion is sealed and fixed by welding or the like. A hole is formed in the center of the bottom surface of the flow direction regulating member 11 so that a shaft 12a attached to a motor 12 described later can pass therethrough.
[0014]
A motor 12 is mounted on the center of the upper surface of the floating sludge tank 3, and the motor 12 has first, second and third shafts 12a and 12b whose rotation speed can be adjusted by a transmission (not shown). , 12c. The first shaft 12a extends downward, passes through a hole formed in the bottom surface of the flow direction regulating member 11, and is inserted into a bearing 13 supported on the bottom surface of the settling sludge tank 2. These three shafts having different rotation speeds are provided with wing-shaped members having respective purposes.
[0015]
First, a plurality of, in this embodiment, four brackets 14a, 15a are attached to the first shaft 12a at upper and lower sides, respectively, at right angles to the shaft 12a and radially so as to be at the same angle to each other. I have. At the tip of the upper bracket 14a, a floating sludge scraper 14 composed of a plate-like member having a shape and a length dimension along the inner wall of the sludge guide plate 8, respectively, and at the tip of the lower bracket 14b, A settling sludge scraper 15 made of a plate-like member having a shape and a length dimension along the inner wall of the tapered portion of the sludge tank 2 is attached. By rotating the first shaft 12a, the floating sludge scraper 14 moves and scrapes the floating sludge attached to the inner wall of the sludge guide plate 8 along the inner wall of the sludge guide plate 8 by the rotation. As shown in FIG. 3, the floating sludge scraper 14 has its rotation direction side in contact with the inner wall of the sludge guide plate 8 or comes close to form a slight gap (about several mm). The bracket 14a is attached to the bracket 14a so as to form a predetermined angle with respect to the tangential direction of the cross-sectional circle of FIG.
On the other hand, the settled sludge scraper 15 moves along the inner wall of the settled sludge tank 2 and scrapes the settled sludge attached to the tapered inner wall of the settled sludge tank 2 by its rotation. The scraper 15 for settling sludge, like the scraper 14 for floating sludge, contacts the rotating direction side with the tapered inner wall of the settling sludge tank 2 or approaches so as to form a slight gap, and has a circular cross section of the tapered inner wall. It is attached to the bracket 15a so as to form a predetermined angle with respect to the tangential direction.
If the peripheral speed of the shaft 12a is set to a high speed, the sludge scraped off by the floating sludge scraper 14 and the settled sludge 15 is disturbed in the tank, so it is not appropriate, and the low-speed rotation of about 2-3 m / min or less is not possible. desirable.
In this embodiment, the floating sludge scraper and the settled sludge scraper are attached to the same shaft. However, it is needless to say that another shaft may be provided and the number of rotations may be different.
[0016]
Next, a plurality of, in this embodiment, four, rectangular plate-like rotating blades 16 are attached to the second shaft 12b at right angles to the shaft 12b and radially so as to be at the same angle to each other. . By rotating the second shaft 12b, the rotary blade 16 rotates, and the concentrated sludge deposited in the flange portion 8a of the sludge guide plate 8 is repelled toward the inner wall of the floating sludge tank 3 to be deaerated. Is what you do. In order to efficiently repel floating sludge and deaerate the sludge, the dimension (L dimension in FIG. 6A) from the tip of the rotary blade 16 to the tip of the rotary blade 16 located 180 ° opposite to that of the flange 8a is The gap dimension (H dimension in FIG. 6A) between the lower edge of the rotary blade 16 and the upper edge of the flange 8a is approximately 0 to several mm.
The degassing of the concentrated sludge to which the air bubbles are attached is caused by the impact force against the rotating blade 16 and the impact force against the inner wall of the floating sludge tank 3 when the sludge is flipped tangentially to the rotation of the rotating blade 16. The rotational speed of the shaft 12b is desirably high-speed rotation of 100 rpm or more in order to increase the collision force.
[0017]
A plurality of, in this embodiment, four, brackets 17a are radially attached to the third shaft 12c at right angles to the shaft 12c and at right angles to each other. At the tip of the bracket 17a, a rectangle is formed along the inner wall of the rising sludge tank 3 and has a length from the upper end of the inner wall of the rising sludge tank 3 to the vicinity of the upper edge of the opening of the concentrated sludge discharge pipe 9 described above. A concentrated sludge scraper 17 made of a plate-like member is attached. By rotating the third shaft 12c, the concentrated sludge scraper 17 removes the concentrated sludge (sludge deaerated by the rotary blade 16) attached to the upper inner wall of the floating sludge tank 3 by the rotation thereof. Move along the inner wall of No. 3 and scrape it. As shown in FIG. 4, the scraper 17 for concentrated sludge crosses the floating sludge tank 3 on the rotation direction side in contact with the inner wall of the floating sludge tank 3 or close to form a slight gap (about several mm). It is attached to the bracket 17a so as to form a predetermined angle with respect to the tangential direction of the plane circle.
Since the concentrated sludge scraper 17 only scrapes off the concentrated sludge, it does not need to be rotated at a high speed. It depends on the amount of the concentrated sludge which is repelled by the rotating blades 16 and adheres to the floating sludge tank 3. A low speed rotation of 2-3 m / min or less is desirable.
[0018]
Next, the operation of the present device will be described.
The raw sludge flows through the raw sludge inflow pipe 10b from the raw sludge tank storing the raw sludge to be treated by a pump. On the other hand, the pressurized air-dissolved water flows through the air-dissolved water inflow pipe 10c from a pressurized air-dissolved water tank in which the compressed air-dissolved water in which the compressed air is dissolved in the raw water at a high concentration is stored. Both are mixed at the connection part of both pipes, and are ejected from the ejection port 10a as sludge water into the sludge concentration device 1. The ejected sludge first collides with the inner wall of the flow direction regulating member 11. Since the lower surface of the flow direction regulating member 11 is closed, the sludge water changes its flow upward along the inner wall of the flow direction regulating member 11. Further, fine bubbles generated from pressurized air-dissolved water at atmospheric pressure adhere to the raw sludge in the sludge water in the tank. The raw sludge floats as floating sludge due to the buoyancy of the attached fine bubbles.
Here, the sludge component that has not adhered to the fine bubbles is settled as settled sludge. The settled sludge settled on the tapered inner wall of the settled sludge tank 2 is scraped off by the settled sludge scraper 15 rotating and moving along the tapered inner wall. Since the settling sludge scraper 15 scrapes at a low speed, the settling sludge settles to the bottom of the settling sludge tank 2 without being stirred in the sludge water. And it is conveyed to the settling sludge treatment process via the settling sludge discharge pipe 4. Excess pressurized air-dissolved water after the floating sludge and the settled sludge are separated passes through a passage 19 formed between the inner wall of the settled sludge tank 2 and the outer wall of the settled sludge tank 3 as separated water. The sediment sludge overflows from the upper edge of the tank 2 and flows out into the separation water receiving frame 5. Then, the water flows into the casing 6 formed in a part of the separated water receiving frame 5 and is discharged from the hole 6a to the separated water treatment step via the separated water discharge pipe 7.
[0019]
The floating sludge to which the fine bubbles adhere is gradually aggregated while floating inside the sludge guide plate 8 as floating sludge aggregating means, and is accumulated in the collar portion 8a. During the floating, the floating sludge adhering to the inner wall of the sludge guide plate 8 is scraped off by the floating sludge scraper 14 rotating and moving along the inner wall. Since the floating sludge scraper 14 scrapes off at the same low speed as the settled sludge scraper 15, the floating sludge starts to float again toward the sludge water surface near the flange 8a without being stirred in the sludge water. As shown in FIG. 6A, the liquid level of the sludge water is located near the rising edge of the flange 8a in order to increase the amount of floating sludge deposited and concentrate the sludge at a high concentration. . The floating sludge that has risen to the liquid level accumulates and is gradually concentrated. Then, of the accumulated concentrated sludge, the uppermost concentrated sludge having the highest concentration of sludge is repelled in the rotating direction by the rotating blade 16 rotating at a high speed. At this time, the sludge is easily degassed by the impact force due to the collision with the rotating blade 16 and the impact force due to the collision with the inner wall of the floating sludge tank 3. The concentrated sludge adhering to the inner wall of the floating sludge tank 3 is scraped off as needed by the concentrated sludge scraper 17 rotating and moving along the inner wall of the floating sludge tank 3, so that it does not dry and solidify on the wall surface. Then, the concentrated sludge that has been scraped is discharged to the concentrated sludge discharge pipe 9 through a hole 3a formed in the wall surface of the floating sludge tank 3 and collected.
[0020]
By the way, in the sludge concentrating apparatus according to the present invention described above, each of the blade-like members attached to the motor, the rotating blades, the scraper for the concentrated sludge, the scraper for the floating sludge, and the scraper for the settled sludge are all four sheets. The present invention is not limited to this, and one sheet may be used. Usually, it is 2 to 4 sheets.
If the rotor is attached to the shaft at an angle θ with respect to the motor rotation axis as shown in FIG. 6B, the concentrated sludge that has collided with the rotor is always repelled upward from the horizontal direction. Efficient deaeration can be performed without being returned to the concentrated sludge accumulated in the section 8a.
[0021]
In addition, the flow direction regulating member 11 is not limited to the above-described cylindrical shape, and may be any mode that guides the flow of the sludge water flowing into the sludge tank in the upward direction.
[0022]
【The invention's effect】
According to the sludge concentrator of the present invention having the above-described configuration, the following effects can be obtained.
(1) Of the sludge accumulated and concentrated on the sludge water surface, only the uppermost concentrated sludge, which has been sufficiently concentrated, is repelled by the rotating blades at a high speed, so that there is no turbulence and the sludge is mixed with the lower-concentration sludge. And a very high concentration of concentrated sludge can be recovered.
(2) Since the deaeration treatment of the concentrated sludge to which the microbubbles adhere can be performed simultaneously with the concentration of the sludge, there is no need to separately provide a deaeration treatment tank, and the efficiency of the sludge concentration flow is improved. (3) Since a scraper is provided to scrape off the concentrated sludge, floating sludge and settled sludge attached to the inner wall of the sludge tank, the frequency of cleaning the inner wall of the sludge tank is reduced.
(4) Since the sludge tank has a substantially cylindrical shape and the above-described rotary blades and each scraper are driven to rotate by one motor, a compact device with a small number of devices can be realized.
(5) Since the flow direction regulating member for guiding the flow of the sludge water flowing into the sludge tank to the upper direction is provided, the sludge water in the sludge tank is not disturbed, and the floating efficiency of the floating sludge is increased.
[Brief description of the drawings]
1 (a) and 1 (b) are a top view and a side view of a sludge concentrator according to the present invention.
FIG. 2 is a sectional view taken along the line AA in FIG.
FIG. 3 is a sectional view taken along line BB in FIG.
FIG. 4 is a sectional view taken along line CC in FIG. 1;
FIG. 5 is an overall perspective view of a sludge concentration device.
FIG. 6A is an explanatory view of a main part, and FIG. 6B is an explanatory view of a main part in another embodiment.
FIG. 7 is a flowchart illustrating an example of a conventional pressurized floating type sludge concentrator.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Sludge concentrating apparatus 2 Settling sludge tank 3 Floating sludge tank 4 Settling sludge discharge pipe 5 Separated water receiving frame 6 Housing 7 Separated water discharge pipe 8 Sludge guide plate 9 Concentrated sludge discharge pipe 10 Sludge inflow pipe 10a Spout port 10b Raw sludge inflow pipe 10c Air-dissolved water inflow pipe 11 Flow direction regulating member 12 Motor 12a, 12b, 12c Shaft 13 Bearing 14 Scraper for floating sludge 14a Bracket 15 Scraper for precipitated sludge 15a Bracket 16 Rotating blade 17 Scraper for concentrated sludge 17a Bracket 18 Sludge tank 19 Passage

Claims (11)

加圧空気溶解水を混入した汚泥水を導入する汚泥槽と、加圧空気と混和され、浮上した汚泥を汚泥槽内において凝集させる浮上汚泥凝集手段と、汚泥水の液面上に配設され、濃縮、堆積した汚泥を撥ね飛ばし脱気するための回転翼とを備えることを特徴とする汚泥濃縮装置。A sludge tank for introducing sludge water mixed with pressurized air dissolved water, floating sludge aggregating means for mixing the floated sludge mixed with the pressurized air in the sludge tank, and disposed on the liquid surface of the sludge water. A sludge concentrator, comprising: a rotating blade for repelling and deaerating the concentrated and accumulated sludge. 前記汚泥槽を、有底円筒形状の沈殿汚泥槽と、この沈殿汚泥槽に内嵌される有蓋円筒形状の浮上汚泥槽とにより構成し、前記沈殿汚泥槽には沈殿汚泥を排出するための沈殿汚泥排出管を接続し、また、前記浮上汚泥槽には脱気された汚泥を排出するための濃縮汚泥排出管を接続してなる請求項1に記載の汚泥濃縮装置。The sludge tank is constituted by a bottomed cylindrical sedimentation sludge tank and a covered cylindrical floating sludge tank fitted inside the sedimentation sludge tank. The sludge concentrator according to claim 1, wherein a sludge discharge pipe is connected, and a concentrated sludge discharge pipe for discharging degassed sludge is connected to the floating sludge tank. 前記浮上汚泥凝集手段を、上下部が開放された汚泥ガイド板により構成し、この汚泥ガイド板は、その下端部を前記濃縮汚泥排出管の下端部より下側に位置する汚泥槽の内壁に固定、封止すると共に、その上端部を前記汚泥水の液面レベルより上に位置する浮上汚泥槽の内部に配設してなる請求項1または請求項2に記載の汚泥濃縮装置。The floating sludge aggregating means is constituted by a sludge guide plate having upper and lower portions opened, and the lower end portion of the sludge guide plate is fixed to the inner wall of a sludge tank located below the lower end portion of the concentrated sludge discharge pipe. The sludge concentrator according to claim 1 or 2, wherein the sludge concentrator is sealed, and an upper end thereof is disposed inside a floating sludge tank located above a liquid level of the sludge water. 前記浮上汚泥槽の上部に、前記回転翼を回転駆動させるためのモータを載置してなる請求項1ないし請求項3のいずれかに記載の汚泥濃縮装置。The sludge concentrator according to any one of claims 1 to 3, wherein a motor for rotating and driving the rotary blade is mounted on an upper part of the floating sludge tank. 前記沈殿汚泥槽に、前記モータにより回転駆動され、沈殿汚泥槽の内壁に沿って移動して、当該沈殿汚泥槽に付着した沈殿汚泥を掻き取る沈殿汚泥用スクレーパを設けてなる請求項2ないし請求項4のいずれかに記載の汚泥濃縮装置。The sludge tank for settling sludge which is rotated and driven by the motor and moves along the inner wall of the settling sludge tank to scrape the settling sludge attached to the settling sludge tank is provided in the settling sludge tank. Item 5. A sludge concentrating device according to any one of Items 4. 前記浮上汚泥槽に、前記モータにより回転駆動され、浮上汚泥槽の内壁に沿って移動して、当該浮上汚泥槽に付着した濃縮汚泥を掻き取る濃縮汚泥用スクレーパを設けてなる請求項2ないし請求項4のいずれかに記載の汚泥濃縮装置。3. The floating sludge tank is provided with a concentrated sludge scraper that is rotated by the motor, moves along the inner wall of the floating sludge tank, and scrapes the concentrated sludge attached to the floating sludge tank. Item 5. A sludge concentrating device according to any one of Items 4. 前記汚泥ガイド板に、前記モータにより回転駆動され、汚泥ガイド板の内壁に沿って移動して、当該汚泥ガイド板に付着した浮上汚泥を掻き取る浮上汚泥用スクレーパを設けてなる請求項2ないし請求項4のいずれかに記載の汚泥濃縮装置。The sludge guide plate is provided with a floating sludge scraper which is driven to rotate by the motor, moves along an inner wall of the sludge guide plate, and scrapes floating sludge attached to the sludge guide plate. Item 5. A sludge concentrating device according to any one of Items 4. 前記沈殿汚泥槽と浮上汚泥槽との間に、外部に分離水を排出するための通路を形成してなる請求項2ないし請求項7のいずれかに記載の汚泥濃縮装置。The sludge concentrator according to any one of claims 2 to 7, wherein a passage for discharging separated water to the outside is formed between the settling sludge tank and the floating sludge tank. 前記回転翼、濃縮汚泥用スクレーパ、浮上汚泥用スクレーパおよび沈澱汚泥用スクレーパは1台のモータの回転軸に取り付けられ、それぞれ異なる回転数で回転が可能となっていることを特徴とする請求項2ないし請求項7のいずれかに記載の汚泥濃縮装置。3. The scraper for concentrated sludge, the scraper for floating sludge, and the scraper for settled sludge are attached to a rotating shaft of one motor, and are capable of rotating at different rotational speeds. A sludge concentrator according to any one of claims 1 to 7. 加圧空気溶解水を作用させた汚泥水を汚泥槽内に噴出させる噴出口近傍に、前記汚泥水の流れを上部方向に導くための流れ方向規制部材を設けたことを特徴とする請求項1ないし請求項9のいずれかに記載の汚泥濃縮装置。The flow direction regulating member for guiding the flow of the sludge water upward is provided in the vicinity of an ejection port for ejecting the sludge water that has been acted on by the pressurized air dissolved water into the sludge tank. A sludge concentrator according to any one of claims 9 to 9. 前記流れ方向規制部材は前記噴出口を囲む、上部が開口し、周側面および底面が閉塞された円筒形状の部材であることを特徴とする請求項1ないし請求項9のいずれかに記載の汚泥濃縮装置。The sludge according to any one of claims 1 to 9, wherein the flow direction regulating member is a cylindrical member that surrounds the jet port, is open at an upper portion, and has a closed peripheral side surface and a bottom surface. Concentrator.
JP05218496A 1996-03-11 1996-03-11 Sludge thickener Expired - Fee Related JP3567392B2 (en)

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KR100374442B1 (en) * 2001-08-02 2003-03-08 인효석 Circular settling tank
KR100906310B1 (en) * 2009-03-31 2009-07-07 가람환경기술(주) Integrated type waste water treating apparatus using a minute bubble generator
CN103833196A (en) * 2014-02-20 2014-06-04 镇江市水业总公司 supermatant discharge system and sludge condensation method
US20160185639A1 (en) * 2014-12-31 2016-06-30 ClearCove Systems, Inc. Method and apparatus for optimization of a conventional waste water treatment plant
CN107935357B (en) * 2017-12-27 2023-12-05 北京东方园林环境股份有限公司 On-site dredging sediment treatment system and treatment method
CN111661991B (en) * 2020-06-01 2022-04-12 湖北众堃科技股份有限公司 Integration sludge thickening pond

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