JP3832330B2 - Outer cylinder rotary concentrator and sludge separation and concentration method - Google Patents

Outer cylinder rotary concentrator and sludge separation and concentration method Download PDF

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Publication number
JP3832330B2
JP3832330B2 JP2001384577A JP2001384577A JP3832330B2 JP 3832330 B2 JP3832330 B2 JP 3832330B2 JP 2001384577 A JP2001384577 A JP 2001384577A JP 2001384577 A JP2001384577 A JP 2001384577A JP 3832330 B2 JP3832330 B2 JP 3832330B2
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Prior art keywords
outer cylinder
sludge
outlet opening
peripheral surface
screw
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JP2003181216A (en
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謙三 菅谷
国彦 土田
雅義 片山
照久 加治
方康 西野
博一 河崎
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Ishigaki Co Ltd
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Ishigaki Co Ltd
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Description

【0001】
【発明の属する技術分野】
この発明は、外筒回転型濃縮機および汚泥の分離濃縮方法に関し、特に、前処理でポリマー凝集した下水汚泥を濾過分離方式で濃縮し、排出する外筒回転型の濃縮機および汚泥の分離濃縮方法に関するものである。
【0002】
【従来の技術】
下水汚泥等の濃縮に使用される濃縮機としては、円筒周面をスクリーン(濾材)により構成された外筒にスクリューが同心配置され、水平配置の外筒内に入れられた汚泥をスクリューの回転によって外筒の軸線方向に移送しつつ濾過分離方式で濃縮排出するもの(実開平7−9406号公報)が知られている。
【0003】
また、円筒周面をスクリーンにより構成された外筒と外筒内に同心配置されたスクリューとが互いに逆方向に回転して水平配置の外筒内に入れられた汚泥をスクリューによって外筒の軸線方向に移送しつつ濾過分離方式で濃縮排出する外筒回転型濃縮機(特開2001−179492号公報)が知られている。
【0004】
【発明が解決しようとする課題】
外筒回転型濃縮機は、外筒とスクリューとが逆回転するので、汚泥の送り出しがよく、濃縮効率が高いと云う特徴を有するが、従来の外筒回転型濃縮機は、外筒内に汚泥を入れる汚泥入口と外筒内より外筒外へ汚泥を排出する汚泥出口がスクリューの円筒状中心軸の周面に形成されているため、汚泥入口や汚泥出口のサイズを大きくすることができず、しかも、汚泥の流れが直線的でないため、濃縮汚泥の排出抵抗が大きく、前処理でポリマー凝集した下水汚泥の場合、汚泥中のポリマー凝縮フロックを破壊する虞れがあり、安定した濃縮処理を行うことができない。その他、汚泥が詰まり易いと云う問題もある。
【0005】
また、従来の外筒回転型濃縮機は、外筒内における汚泥の滞留時間を調整することが難しく、汚泥の濃縮処理の調整性に欠けている。
【0006】
この発明は、上述の如き問題点を解消するためになされたもので、濃縮汚泥の排出抵抗が少なく、汚泥中のポリマー凝集フロックを破壊する虞れがなく、安定した濃縮処理を行うことができ、汚泥がスムーズに流れて詰まりを生じ難く、しかも、外筒内における汚泥の滞留時間を容易に調整することができる外筒回転型濃縮機、およびその外筒回転型濃縮機を使用した好適な汚泥の分離濃縮方法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】
上述の目的を達成するために、この発明による外筒回転型濃縮機は、両端を円盤状のフランジ板により閉じられて円筒周面を金属濾材(パンチングメタル)等によるスクリーンにより構成された外筒と、前記外筒内に同心配置されたスクリューとを有し、前記外筒と前記スクリューとが互いに逆方向に回転駆動される外筒回転型濃縮機において、前記スクリューは外周面にスクリュー羽根を有する円筒状中心軸を有し、前記円筒状中心軸が前記外筒内の一端側に位置する部分の軸周面に被処理物であるポリマー凝集汚泥を当該円筒状中心軸の中空筒部より前記外筒内に導入する入口開口が設けられ、前記外筒の他端側の前記フランジ板に出口開口が形成され、前記出口開口の開口面積を増減調節する出口開口度調節機構が前記外筒に設けられ、前記出口開口の外筒外周側の開口縁がスクリーンによる前記円筒周面と前記外筒の径方向に見てほぼ同一位置であり、ポリマー凝集フロックは破壊されることなく、濃縮汚泥は前記出口開口より大きい排出抵抗を受けることなく外筒外に排出されることを特徴とする。
【0008】
上述した構成による外筒回転型濃縮機によれば、円筒状中心軸の入口開口より外筒内に導入されたポリマー凝集汚泥の被処理物の濃縮が、外筒とスクリューとの逆回転によって高効率で行われ、濃縮汚泥等はスクリュー回転による移送方向(外筒の軸線方向)の正面に位置するフランジ板に形成された出口開口より大きい排出抵抗を受けることなく外筒外に排出される。また、この出口開口の開口面積の増減調節により、外筒内における汚泥の滞留時間を調整することができる。さらに、前記出口開口の外筒外周側の開口縁がスクリーンによる前記円筒周面と前記外筒の径方向に見てほぼ同一位置であり、運転終了後に、外筒内に汚泥が溜まることがなく、清掃が容易になる。
【0009】
出口開口度調節機構としては、前記出口開口を形成されたフランジ板の重り合って配置されて当該フランジ板に対して回転変位可能なシャッタ板を含み、当該シャッタ板の前記フランジ板に対する回転変位位置に応じて当該シャッタ板による前記出口開口の塞ぎ量を増減する構造のものとすることができる。
【0010】
また、上述の目的を達成するために、この発明による汚泥の分離濃縮方法は、両端を円盤状のフランジ板により閉じられて円筒周面をスクリーンにより構成された外筒を実質的に水平な自身の中心軸線周りに回転させると共に、前記外筒内に同心配置されたスクリューを前記外筒の回転方向とは逆方向に回転させ、被処理物であるポリマー凝集汚泥を前記スクリューの円筒状中心軸の中空筒部に供給し、当該汚泥を前記円筒状中心軸が前記外筒内の一端側に位置する部分の軸周面に設けられた入口開口より前記外筒内に上部空間を残した態様で導入し、前記外筒の外部上方から洗浄液を前記外筒の円筒周面に向けて噴射し、前記スクリーンの洗浄を連続的又は間欠的に行いつつ、前記円筒状中心軸の外周面に設けられているスクリュー羽根によって前記外筒内の汚泥を前記外筒の一端側より他端側に移送して前記外筒の他端側のフランジ位置に形成されている出口開口より排出する過程で、前記スクリーンによって汚泥の濾過を行なうとともに、前記出口開口の開口面積を増減調節して前記外筒内の汚泥滞留時間を調整し、ポリマー凝集フロックは破壊されることなく、濃縮汚泥は前記出口開口より大きい排出抵抗を受けることなく外筒外に排出されることを特徴とする。
【0011】
この発明による汚泥の分離濃縮方法では、汚泥の分離濃縮効率を良好に保ってスクリーンの洗浄回復をよくするために、前記外筒内の汚泥の充填率を50%以上、90%以下とする。
【0012】
【発明の実施の形態】
以下に添付の図を参照してこの発明の実施の形態を詳細に説明する。
【0013】
図1〜図4はこの発明による外筒回転型濃縮機の一つの実施の形態を示している。
【0014】
架台1は左右の側板3、5を有し、側板3、5には軸受スリーブ7と軸受ブラケット9とが一つの水平軸線X上に固定されている。軸受スリーブ7と軸受ブラケット9は軸受部材11、13によって外筒15を回転可能に支持している。
【0015】
外筒15は、両端を円盤状のフランジ板17、19により閉じられて円筒周面をパンチングメタル等によるメタルスクリーン21により構成されている。一方(左側)のフランジ板17には短軸スリーブ23が固定されており、短軸スリーブ23の内周側に軸受部材11が取り付けられている。他方(右側)のフランジ板19には長軸スリーブ25が固定されており、長軸スリーブ25の外周側には軸受部材13が取り付けられている。
【0016】
円筒状のメタルスクリーン21は、図2、図3に示されているように、半割形状で、ボルト・ナット29によって互いに締結される2つの半円環状部材27A、27Bに両端部に固定され、左右の半円環状部材27A、27Bが各々ボルト・ナット31によってフランジ板17、19に締結されている。左右の半円環状部材27A、27Bの間には複数個のタイバー33が掛け渡されており、各タイバー33の軸線方向の中間部にメタルスクリーン21の軸線方向中間部を外側から補助支持する複数個の支持リング35が取り付けられている。
【0017】
長軸スリーブ25には外筒回転駆動用のスプロケット37が固定されている。スプロケット37は、図示されていない外筒回転駆動用の電動機と駆動連結され、外筒15を例えば反時計廻り方向(図5参照)に回転駆動する。
【0018】
外筒15内にはスクリュー39が回転可能に同心配置されている。スクリュー39は、円筒状中心軸41と、円筒状中心軸41の外周面に設けられた螺旋形状のスクリュー羽根43と、円筒状中心軸41の閉じ端部(右端部)に同心連結された回転駆動軸45とを有している。
【0019】
円筒状中心軸41は、外筒15内にあり、一端側(左側)が軸受スリーブ7内に延出し、その延出軸部47を軸受部材49によって長軸スリーブ7より回転可能に支持されている。延出軸部47の先端面は開口しており、開口端が汚泥(被処理物)の投入口51になっている。
【0020】
円筒状中心軸41が外筒15内の一端側(フランジ板17側)に位置する部分の軸周面には被処理物の汚泥を円筒状中心軸41の中空筒部53より外筒15内に導入する入口開口55が2つ設けられている。なお、円筒状中心軸41の中空筒部53には入口開口55の位置より被処理物の汚泥が中空筒部53内を図1にて右側へ侵入することを禁止するための閉じ板57が固定されている。
【0021】
回転駆動軸45は、長軸スリーブ25を軸線方向に貫通し、長軸スリーブ25より回転可能に支持されており、図示されていないスクリュー回転駆動用の電動機と駆動連結され、スクリュー39を例えば時計廻り方向に回転駆動する。
【0022】
スクリュー羽根43は、スクリュー39の時計廻り方向に回転により、外筒15内の汚泥を図1にて左側(フランジ板17側)より右側(フランジ板19側)へ移送する。スクリュー羽根43の外周縁は、汚泥がショートパスしないようメタルスクリーン21の内周面との間に微小間隙をおいて対向している。なお、必要に応じてスクリュー羽根43にスクレーパを取り付け、かき落としによってメタルスクリーン21の再生回復を行うこともできる。
【0023】
フランジ板19には外筒15内の濃縮汚泥を外筒15外へ排出する複数個の出口開口59が開口形成されている。出口開口59は、外筒15の中心と同心の円弧形状の開口であり、外筒外周側の開口縁61がメタルスクリーン21による円筒周面(内周面)と外筒15の径方向に見てほぼ同一位置になっている。これは、メタルスクリーン21に内周面と出口開口59との間に堰がないことを意味する。これにより、運転終了後に、外筒15内に汚泥が溜まることがなく、清掃が容易になる。
【0024】
フランジ板19には出口開口59の開口面積(有効面積)を増減調節する出口開口度調節機構として、図4によく示されているように、フランジ板19の外側面の重り合って配置されたシャッタ板63がボルト65によってフランジ板17に対して回転変位可能に固定されている。シャッタ板63は、各出口開口59毎に翼形状部67を有し、フランジ板19に対する回転変位位置(回転方向の固定位置)に応じて翼形状部67による出口開口59の塞ぎ量を一様に増減する。なお、シャッタ板63に形成されているボルト65の通し孔69は外筒15の中心と同心の円弧形状の長孔になっており、通し孔69の範囲内で、ボルト65によってシャッタ板63をフランジ板19に対して任意の回転角位置で固定できる。
【0025】
外筒15の外部上方には洗浄液噴出用の洗浄管71が左右の側板3、5間に掛け渡された態様で固定配置されている。洗浄管71は、洗浄管71より噴射された洗浄液が効率よくメタルスクリーンにかかるよう、外筒15の直上位置より少し外筒15の回転方向遅れ側に偏倚した位置に配置されている。
【0026】
つぎに、上述の構成による外筒回転型濃縮機を使用した汚泥の分離濃縮方法について説明する。
【0027】
外筒15を反時計廻り方向に、スクリュー39を外筒15の回転方向とは逆の時計廻り方向に各々回転駆動し、前処理で例えば高分子ポリマーを加えてポリマー凝集した汚泥を延出軸部47の投入口51より中空筒部53内に連続投入する。この汚泥は、中空筒部53を通って入口開口55より外筒15内に入り、回転しているスクリュー羽根43によって外筒15の一端側(左側)より他端側(右側)に移送される。
【0028】
この移送過程で、汚泥中の液成分(濾液)がメタルスクリーン21を透過して外筒15の下方への分離流出し、汚泥の濃縮が行われ、濃縮された汚泥は移送方向(軸線方向)を変更されることなく、各出口開口59より外筒15の外部へスムーズに排出される。
【0029】
これにより、濃縮汚泥を大きい排出抵抗を受けることなく外筒15外に排出することができ、ポリマー凝集したフロックを壊すことがない。また、シャッタ板63によって出口開口59の有効面積を増減することにより、外筒15内の汚泥滞留時間を容易に調整することができる。
【0030】
上述した汚泥濃縮過程において、外筒15の外部上方の洗浄管71により洗浄液が外筒15の円筒周面をなすメタルスクリーン21へ噴射することにより、メタルスクリーン21の洗浄が行われ、外筒15が回転することで、メタルスクリーン21による外筒濾過面積全体(全周)が有効に作用し、処理能力が飛躍的に向上する。この場合、汚泥の分離濃縮効率を良好に保ってメタルスクリーン21の洗浄回復をよくするために、図5に示されているように、外筒15内の汚泥の充填率を50%以上、90%以下とすることが好ましい。
【0031】
また、スクリュー回転による濃縮汚泥の搬送効果と、外筒濾面(メタルスクリーン21)と逆方向に回転するスクリュー羽根43先端の差速による濾面の掻き取り効果により、連続した効率的な汚泥濃縮が行われる。外筒15とスクリュー39との逆回転差速は汚泥に応じて最適設定でき、4RPM以上が望ましい。また、洗浄は常に連続的に行われるものであるが、濾過性がよい場合には、連続的でなく間欠的に行うようにしてもよい。さらに濾過性が非常によい場合には洗浄水は不要にすることも可能である。
【0032】
【発明の効果】
以上の説明から理解される如く、この発明による外筒回転型濃縮機および汚泥の分離濃縮方法によれば、円筒状中心軸の入口開口より外筒内に導入されたポリマー凝集汚泥等の被処理物の濃縮が、外筒とスクリューとの逆回転によって高効率で行われ、濃縮汚泥等はスクリュー回転による移送方向(外筒の軸線方向)の正面に位置するフランジ板に形成された出口開口より大きい排出抵抗を受けることなく外筒外に排出されるから、汚泥中のポリマー凝集フロックを破壊する虞れがなく、安定した濃縮処理を行うことができ、汚泥がスムーズに流れて詰まりも生じ難くなる。また、この出口開口の開口面積の増減調節により、外筒内における汚泥の滞留時間を調整することができる。この発明による外筒回転型濃縮機においてはさらに、前記出口開口の外筒外周側の開口縁がスクリーンによる前記円筒周面と前記外筒の径方向に見てほぼ同一位置であり、運転終了後に、外筒内に汚泥が溜まることがなく、清掃が容易になる。
【図面の簡単な説明】
【図1】 この発明による外筒回転型濃縮機の一つの実施の形態を示す断面図である。
【図2】 この発明による外筒回転型濃縮機のメタルスクリーン部分の正面図である。
【図3】 図2の線III−III断面図である。
【図4】 この発明による外筒回転型濃縮機の外筒の端面図である。
【図5】 この発明による外筒回転型濃縮機の使用状態を示す説明図である。
【符号の説明】
1 架台
15 外筒
17、19 フランジ板
21 メタルスクリーン
39 スクリュー
41 円筒状中心軸
43 スクリュー羽根
55 入口開口
59 出口開口
63 シャッタ板
[0001]
BACKGROUND OF THE INVENTION
TECHNICAL FIELD The present invention relates to an outer cylinder rotary type concentrator and a sludge separation and concentration method, and in particular, an outer cylinder rotary type concentrator and sludge separation and concentration for concentrating and discharging sewage sludge that has been polymer-agglomerated in a pretreatment by a filtration separation method It is about the method.
[0002]
[Prior art]
As a concentrator used for concentrating sewage sludge, etc., a screw is concentrically placed on an outer cylinder composed of a screen (filter medium) on the cylindrical circumference, and the sludge placed in a horizontally arranged outer cylinder is rotated by the screw. Is known to be concentrated and discharged by a filtration separation method while being transferred in the axial direction of the outer cylinder (Japanese Utility Model Laid-Open No. 7-9406).
[0003]
In addition, an outer cylinder constituted by a screen on a cylindrical peripheral surface and a screw arranged concentrically in the outer cylinder rotate in opposite directions to each other and sludge placed in the outer cylinder arranged horizontally is screwed into the axis of the outer cylinder. An outer cylinder rotary type concentrator (Japanese Patent Application Laid-Open No. 2001-179492) is known which concentrates and discharges by a filtration separation method while being transferred in the direction.
[0004]
[Problems to be solved by the invention]
The outer cylinder rotary type concentrator has the feature that the outer cylinder and the screw rotate in the reverse direction, so that the sludge is sent out well and the concentration efficiency is high. The sludge inlet and the sludge outlet for discharging sludge from the inside of the outer cylinder to the outside of the outer cylinder are formed on the peripheral surface of the cylindrical central axis of the screw, so the size of the sludge inlet and sludge outlet can be increased. In addition, since the sludge flow is not linear, the concentrated sludge discharge resistance is large, and in the case of sewage sludge that has been polymer agglomerated in the pretreatment, there is a risk of destroying the polymer condensation flocs in the sludge. Can not do. In addition, there is a problem that sludge is easily clogged.
[0005]
Moreover, the conventional outer cylinder rotary type concentrator is difficult to adjust the sludge residence time in the outer cylinder, and lacks the adjustability of the sludge concentration process.
[0006]
The present invention has been made to solve the above-described problems, and has a low concentration resistance of concentrated sludge, there is no possibility of destroying the polymer flocs in the sludge, and a stable concentration treatment can be performed. The sludge flows smoothly and is not easily clogged, and the sludge residence time in the outer cylinder can be easily adjusted. The object is to provide a method for separating and concentrating sludge.
[0007]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, an outer cylinder rotary type concentrator according to the present invention has an outer cylinder in which both ends are closed by disk-shaped flange plates and the cylindrical peripheral surface is constituted by a screen made of a metal filter medium (punching metal) or the like. And a screw arranged concentrically in the outer cylinder, wherein the outer cylinder and the screw are driven to rotate in directions opposite to each other. A polymer central sludge which is a material to be treated on a shaft peripheral surface of a portion where the cylindrical central axis is located at one end side in the outer cylinder from the hollow cylindrical portion of the cylindrical central axis. An inlet opening to be introduced into the outer cylinder is provided, an outlet opening is formed in the flange plate on the other end side of the outer cylinder, and an outlet opening degree adjusting mechanism for adjusting the opening area of the outlet opening is increased or decreased. Provided in The Der substantially the same position opening edge of the outer tube outer peripheral side when viewed in the radial direction of the outer cylinder and the cylindrical circumferential surface by the screen of the outlet opening is, without the polymer flocs are broken, the concentrated sludge is the outlet It is characterized by being discharged out of the outer cylinder without receiving a discharge resistance larger than the opening .
[0008]
According to the outer cylinder rotating type concentrator having the above-described configuration, the concentration of the polymer agglomerated sludge to be treated introduced into the outer cylinder from the inlet opening of the cylindrical central shaft is increased by the reverse rotation of the outer cylinder and the screw. Concentrated sludge and the like are discharged outside the outer cylinder without receiving a larger discharge resistance than the outlet opening formed in the flange plate located in front of the transfer direction by the screw rotation (axial direction of the outer cylinder). In addition, the sludge residence time in the outer cylinder can be adjusted by adjusting the opening area of the outlet opening. Furthermore, the opening edge on the outer cylinder outer peripheral side of the outlet opening is substantially at the same position as seen in the radial direction of the cylindrical peripheral surface by the screen and the outer cylinder, and sludge does not accumulate in the outer cylinder after the operation is completed. Easy to clean.
[0009]
The outlet opening degree adjusting mechanism includes a shutter plate that is disposed so as to overlap with the flange plate formed with the outlet opening and can be rotationally displaced with respect to the flange plate, and the rotational displacement position of the shutter plate with respect to the flange plate Accordingly, the amount of closing of the outlet opening by the shutter plate can be increased or decreased.
[0010]
In order to achieve the above object, the method for separating and concentrating sludge according to the present invention has a substantially horizontal self-contained outer cylinder having both ends closed by disk-shaped flange plates and a cylindrical peripheral surface constituted by a screen. And rotating the screw concentrically arranged in the outer cylinder in the direction opposite to the rotation direction of the outer cylinder, and the polymer agglomerated sludge as the object to be treated is made into the cylindrical central axis of the screw. A mode in which the sludge is left in the outer cylinder from the inlet opening provided on the axial peripheral surface of the portion where the cylindrical central axis is located on one end side in the outer cylinder. The cleaning liquid is sprayed from the upper outside of the outer cylinder toward the cylindrical peripheral surface of the outer cylinder, and is provided on the outer peripheral surface of the cylindrical central shaft while continuously or intermittently cleaning the screen. On the screw blades In the process of transferring the sludge in the outer cylinder from one end side of the outer cylinder to the other end side and discharging it from the outlet opening formed at the flange position on the other end side of the outer cylinder, In addition, the sludge retention time in the outer cylinder is adjusted by increasing or decreasing the opening area of the outlet opening , the polymer flocs floc is not destroyed, and the concentrated sludge has a larger discharge resistance than the outlet opening. It is characterized by being discharged out of the outer cylinder without receiving .
[0011]
In the sludge separation and concentration method according to the present invention, the sludge filling rate in the outer cylinder is set to 50% or more and 90% or less in order to maintain the sludge separation and concentration efficiency and improve the cleaning recovery of the screen.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below in detail with reference to the accompanying drawings.
[0013]
1 to 4 show one embodiment of an outer cylinder rotary type concentrator according to the present invention.
[0014]
The gantry 1 has left and right side plates 3 and 5, and a bearing sleeve 7 and a bearing bracket 9 are fixed to the side plates 3 and 5 on one horizontal axis X. The bearing sleeve 7 and the bearing bracket 9 rotatably support the outer cylinder 15 by bearing members 11 and 13.
[0015]
The outer cylinder 15 is composed of a metal screen 21 made of punched metal or the like with its both ends closed by disk-shaped flange plates 17 and 19 and its cylindrical peripheral surface. The short shaft sleeve 23 is fixed to one (left side) flange plate 17, and the bearing member 11 is attached to the inner peripheral side of the short shaft sleeve 23. A long shaft sleeve 25 is fixed to the other (right) flange plate 19, and a bearing member 13 is attached to the outer peripheral side of the long shaft sleeve 25.
[0016]
As shown in FIGS. 2 and 3, the cylindrical metal screen 21 has a half shape and is fixed at both ends to two semicircular members 27 </ b> A and 27 </ b> B fastened to each other by bolts and nuts 29. The left and right semi-annular members 27A and 27B are fastened to the flange plates 17 and 19 by bolts and nuts 31, respectively. A plurality of tie bars 33 are spanned between the left and right semi-annular members 27A, 27B, and a plurality of axially intermediate portions of the metal screen 21 are auxiliary-supported from the outside to the intermediate portions of the tie bars 33 in the axial direction. A single support ring 35 is attached.
[0017]
A sprocket 37 for rotating the outer cylinder is fixed to the long shaft sleeve 25. The sprocket 37 is drivingly connected to an electric motor for rotationally driving an outer cylinder (not shown), and rotationally drives the outer cylinder 15 in, for example, a counterclockwise direction (see FIG. 5).
[0018]
A screw 39 is concentrically disposed in the outer cylinder 15 so as to be rotatable. The screw 39 is concentrically connected to a cylindrical central shaft 41, a helical screw blade 43 provided on the outer peripheral surface of the cylindrical central shaft 41, and a closed end (right end) of the cylindrical central shaft 41. And a drive shaft 45.
[0019]
The cylindrical central shaft 41 is in the outer cylinder 15, and one end side (left side) extends into the bearing sleeve 7, and the extending shaft portion 47 is rotatably supported by the long shaft sleeve 7 by the bearing member 49. Yes. The front end surface of the extending shaft portion 47 is open, and the open end is an inlet 51 for sludge (object to be processed).
[0020]
The sludge of the object to be processed is placed in the outer cylinder 15 from the hollow cylinder portion 53 of the cylindrical central shaft 41 on the shaft peripheral surface of the portion where the cylindrical central shaft 41 is located on one end side (flange plate 17 side) in the outer cylinder 15. There are provided two inlet openings 55 to be introduced into the. The hollow cylindrical portion 53 of the cylindrical central shaft 41 has a closing plate 57 for preventing sludge of the object to be processed from entering the hollow cylindrical portion 53 to the right side in FIG. It is fixed.
[0021]
The rotary drive shaft 45 penetrates the long shaft sleeve 25 in the axial direction, and is rotatably supported by the long shaft sleeve 25. The rotary drive shaft 45 is drivingly connected to an electric motor for screw rotation drive (not shown). It is driven to rotate in the direction of rotation.
[0022]
The screw blades 43 transfer the sludge in the outer cylinder 15 from the left side (flange plate 17 side) to the right side (flange plate 19 side) in FIG. 1 by rotating the screw 39 in the clockwise direction. The outer peripheral edge of the screw blades 43 is opposed to the inner peripheral surface of the metal screen 21 with a minute gap so that the sludge does not short pass. If necessary, a scraper can be attached to the screw blade 43 and the metal screen 21 can be regenerated and recovered by scraping.
[0023]
A plurality of outlet openings 59 for discharging the concentrated sludge in the outer cylinder 15 to the outside of the outer cylinder 15 is formed in the flange plate 19. The outlet opening 59 is an arc-shaped opening concentric with the center of the outer cylinder 15, and the opening edge 61 on the outer peripheral side of the outer cylinder is seen in the radial direction of the cylindrical peripheral surface (inner peripheral surface) by the metal screen 21 and the outer cylinder 15. Are almost in the same position. This means that the metal screen 21 has no weir between the inner peripheral surface and the outlet opening 59. Thereby, after the operation is finished, the sludge does not accumulate in the outer cylinder 15 and cleaning becomes easy.
[0024]
As shown in FIG. 4, the flange plate 19 is arranged so as to overlap the outer surface of the flange plate 19 as an outlet opening degree adjusting mechanism for increasing or decreasing the opening area (effective area) of the outlet opening 59. The shutter plate 63 is fixed to the flange plate 17 by bolts 65 so as to be capable of rotational displacement. The shutter plate 63 has a blade shape portion 67 for each outlet opening 59, and the amount of closing of the outlet opening 59 by the blade shape portion 67 is uniform according to the rotational displacement position (fixed position in the rotation direction) with respect to the flange plate 19. Increase or decrease. The through hole 69 of the bolt 65 formed in the shutter plate 63 is an arc-shaped long hole concentric with the center of the outer cylinder 15, and the shutter plate 63 is moved by the bolt 65 within the range of the through hole 69. It can be fixed at an arbitrary rotational angle position with respect to the flange plate 19.
[0025]
A cleaning pipe 71 for jetting cleaning liquid is fixedly disposed above the outer cylinder 15 in such a manner as to span between the left and right side plates 3 and 5. The cleaning pipe 71 is disposed at a position slightly deviated from the position directly above the outer cylinder 15 toward the rotation direction of the outer cylinder 15 so that the cleaning liquid sprayed from the cleaning pipe 71 is efficiently applied to the metal screen.
[0026]
Next, a method for separating and concentrating sludge using the outer cylinder rotary concentrator having the above-described configuration will be described.
[0027]
The outer cylinder 15 is rotated in the counterclockwise direction and the screw 39 is rotated in the clockwise direction opposite to the rotation direction of the outer cylinder 15, respectively. The material is continuously charged into the hollow cylindrical portion 53 from the charging port 51 of the portion 47. This sludge enters the outer cylinder 15 through the inlet opening 55 through the hollow cylinder portion 53 and is transferred from one end side (left side) to the other end side (right side) of the outer cylinder 15 by the rotating screw blades 43. .
[0028]
In this transfer process, the liquid component (filtrate) in the sludge permeates the metal screen 21 and separates and flows out downward of the outer cylinder 15 to concentrate the sludge. The concentrated sludge is transferred in the transfer direction (axial direction). Without being changed, each outlet opening 59 is smoothly discharged to the outside of the outer cylinder 15.
[0029]
Thereby, concentrated sludge can be discharged | emitted out of the outer cylinder 15, without receiving large discharge resistance, and the floc which the polymer aggregated is not broken. Moreover, the sludge residence time in the outer cylinder 15 can be easily adjusted by increasing / decreasing the effective area of the outlet opening 59 by the shutter plate 63.
[0030]
In the above-described sludge concentration process, the cleaning liquid is sprayed onto the metal screen 21 forming the cylindrical peripheral surface of the outer cylinder 15 by the cleaning pipe 71 located above the outer cylinder 15, thereby cleaning the metal screen 21. As a result of the rotation, the entire outer cylinder filtering area (entire circumference) by the metal screen 21 acts effectively, and the processing capability is dramatically improved. In this case, in order to maintain the sludge separation / concentration efficiency at a good level and improve the recovery of the cleaning of the metal screen 21, as shown in FIG. % Or less is preferable.
[0031]
Concentrated sludge is continuously and efficiently concentrated due to the effect of conveying the concentrated sludge by rotating the screw and the effect of scraping the filter surface by the differential speed of the tip of the screw blade 43 rotating in the opposite direction to the outer cylinder filter surface (metal screen 21). Is done. The reverse rotational speed difference between the outer cylinder 15 and the screw 39 can be optimally set according to the sludge, and is preferably 4 RPM or more. Moreover, although washing | cleaning is always performed continuously, when filterability is good, you may make it perform intermittently instead of continuously. Furthermore, when the filterability is very good, it is possible to dispense with washing water.
[0032]
【The invention's effect】
As will be understood from the above description, according to the outer cylinder rotary concentrator and the sludge separation and concentration method according to the present invention, the polymer agglomerated sludge and the like to be treated introduced into the outer cylinder from the inlet opening of the cylindrical central shaft. Concentration of the material is performed with high efficiency by reverse rotation of the outer cylinder and the screw, and the concentrated sludge and the like are from an outlet opening formed in a flange plate located in front of the transfer direction by the screw rotation (axial direction of the outer cylinder). Because it is discharged outside the outer cylinder without receiving a large discharge resistance, there is no risk of destroying the polymer flocs in the sludge, stable concentration treatment can be performed, and the sludge flows smoothly and hardly clogs. Become. In addition, the sludge residence time in the outer cylinder can be adjusted by adjusting the opening area of the outlet opening. In the outer cylinder rotary concentrator according to the present invention, the opening edge of the outlet opening on the outer cylinder outer peripheral side is substantially in the same position when viewed in the radial direction of the cylinder outer surface by the screen and the outer cylinder, and after the operation is finished. The sludge does not accumulate in the outer cylinder, and cleaning becomes easy.
[Brief description of the drawings]
FIG. 1 is a sectional view showing an embodiment of an outer cylinder rotary concentrator according to the present invention.
FIG. 2 is a front view of a metal screen portion of an outer cylinder rotary concentrator according to the present invention.
3 is a cross-sectional view taken along line III-III in FIG.
FIG. 4 is an end view of the outer cylinder of the outer cylinder rotary type concentrator according to the present invention.
FIG. 5 is an explanatory view showing a usage state of the outer cylinder rotary concentrator according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Stand 15 Outer cylinder 17, 19 Flange board 21 Metal screen 39 Screw 41 Cylindrical center axis 43 Screw blade 55 Inlet opening 59 Outlet opening 63 Shutter board

Claims (4)

両端を円盤状のフランジ板により閉じられて円筒周面をスクリーンにより構成された外筒と、前記外筒内に同心配置されたスクリューとを有し、前記外筒と前記スクリューとが互いに逆方向に回転駆動される外筒回転型濃縮機において、前記スクリューは外周面にスクリュー羽根を有する円筒状中心軸を有し、前記円筒状中心軸が前記外筒内の一端側に位置する部分の軸周面に被処理物であるポリマー凝集汚泥を当該円筒状中心軸の中空筒部より前記外筒内に導入する入口開口が設けられ、前記外筒の他端側の前記フランジ板に出口開口が形成され、前記出口開口の開口面積を増減調節する出口開口度調節機構が前記外筒に設けられ、前記出口開口の外筒外周側の開口縁がスクリーンによる前記円筒周面と前記外筒の径方向に見てほぼ同一位置であり、ポリマー凝集フロックは破壊されることなく、濃縮汚泥は前記出口開口より大きい排出抵抗を受けることなく外筒外に排出されることを特徴とする外筒回転型濃縮機。An outer cylinder having both ends closed by disk-shaped flange plates and a cylindrical peripheral surface constituted by a screen, and a screw concentrically disposed in the outer cylinder, the outer cylinder and the screw being in opposite directions to each other In the outer cylinder rotary type concentrator that is rotationally driven, the screw has a cylindrical central axis having screw blades on the outer peripheral surface, and the cylindrical central axis is located at one end side in the outer cylinder. An inlet opening for introducing the polymer agglomerated sludge , which is an object to be processed, into the outer cylinder from the hollow cylinder portion of the cylindrical central shaft is provided on the peripheral surface, and an outlet opening is provided in the flange plate on the other end side of the outer cylinder. An outlet opening degree adjusting mechanism that is formed and adjusts the opening area of the outlet opening to be increased or decreased is provided in the outer cylinder, and an opening edge on the outer cylinder outer peripheral side of the outlet opening is a diameter of the cylindrical peripheral surface by the screen and the outer cylinder. Almost identical when viewed in the direction Der is, without the polymer flocs are broken, the concentrated sludge is external cylinder rotary concentrator, characterized in that it is discharged to the outside of the outer tube without being the outlet opening is greater than the discharge resistance. 請求項1記載の外筒回転型濃縮機において、前記出口開口度調節機構は前記出口開口を形成されたフランジ板の重り合って配置されて当該フランジ板に対して回転変位可能なシャッタ板を含み、当該シャッタ板の前記フランジ板に対する回転変位位置に応じて当該シャッタ板による前記出口開口の塞ぎ量を増減することを特徴とする外筒回転型濃縮機。  2. The outer cylinder rotary type concentrator according to claim 1, wherein the outlet opening degree adjusting mechanism includes a shutter plate that is disposed so as to overlap with a flange plate in which the outlet opening is formed and is rotatable and displaceable with respect to the flange plate. An outer cylinder rotary type concentrator that increases or decreases the closing amount of the outlet opening by the shutter plate according to the rotational displacement position of the shutter plate with respect to the flange plate. 両端を円盤状のフランジ板により閉じられて円筒周面をスクリーンにより構成された外筒を実質的に水平な自身の中心軸線周りに回転させると共に、前記外筒内に同心配置されたスクリューを前記外筒の回転方向とは逆方向に回転させ、被処理物であるポリマー凝集汚泥を前記スクリューの円筒状中心軸の中空筒部に供給し、当該汚泥を前記円筒状中心軸が前記外筒内の一端側に位置する部分の軸周面に設けられた入口開口より前記外筒内に上部空間を残した態様で導入し、前記外筒の外部上方から洗浄液を前記外筒の円筒周面に向けて噴射し、前記スクリーンの洗浄を連続的又は間欠的に行いつつ、前記円筒状中心軸の外周面に設けられているスクリュー羽根によって前記外筒内の汚泥を前記外筒の一端側より他端側に移送して前記外筒の他端側のフランジ位置に形成されている出口開口より排出する過程で、前記スクリーンによって汚泥の濾過を行なうとともに、前記出口開口の開口面積を増減調節して前記外筒内の汚泥滞留時間を調整し、ポリマー凝集フロックは破壊されることなく、濃縮汚泥は前記出口開口より大きい排出抵抗を受けることなく外筒外に排出されることを特徴とする汚泥の分離濃縮方法。Both ends are closed by disk-shaped flange plates, and the outer cylinder constituted by the screen with the cylindrical peripheral surface is rotated about its own central axis, and the screw disposed concentrically in the outer cylinder is Rotating in the direction opposite to the rotation direction of the outer cylinder, supplying the polymer agglomerated sludge as the object to be processed to the hollow cylinder portion of the cylindrical central axis of the screw, and the cylindrical central axis is inside the outer cylinder Introduced in such a manner that an upper space is left in the outer cylinder from an inlet opening provided on a shaft peripheral surface of a portion located on one end side of the outer cylinder, and cleaning liquid is introduced into the cylindrical peripheral surface of the outer cylinder from above the outer cylinder. The sludge in the outer cylinder is removed from the one end side of the outer cylinder by screw blades provided on the outer peripheral surface of the cylindrical central axis, while continuously or intermittently cleaning the screen. Transferred to the end side of the outer cylinder In the course of discharging from an outlet opening formed in the flange position of the end side, performs a filtering of the sludge by said screen, said increases or decreases adjusting the opening area of the outlet opening by adjusting the sludge residence time in the outer tube The method for separating and concentrating sludge, characterized in that the polymer coagulation floc is not destroyed and the concentrated sludge is discharged outside the outer cylinder without receiving a discharge resistance larger than the outlet opening . 請求項3記載の汚泥の分離濃縮方法において、前記外筒内の汚泥の充填率を50%以上、90%以下とすることを特徴とする汚泥の分離濃縮方法。  4. The method for separating and concentrating sludge according to claim 3, wherein the sludge filling rate in the outer cylinder is 50% or more and 90% or less.
JP2001384577A 2001-12-18 2001-12-18 Outer cylinder rotary concentrator and sludge separation and concentration method Expired - Lifetime JP3832330B2 (en)

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