JP3751578B2 - Screw type filter dehydrator - Google Patents

Screw type filter dehydrator Download PDF

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Publication number
JP3751578B2
JP3751578B2 JP2002184061A JP2002184061A JP3751578B2 JP 3751578 B2 JP3751578 B2 JP 3751578B2 JP 2002184061 A JP2002184061 A JP 2002184061A JP 2002184061 A JP2002184061 A JP 2002184061A JP 3751578 B2 JP3751578 B2 JP 3751578B2
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Japan
Prior art keywords
annular
movable plate
plate
annular movable
sliding contact
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JP2002184061A
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Japanese (ja)
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JP2004025008A (en
Inventor
正彦 福田
秀明 金谷
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Tsurumi Manufacturing Co Ltd
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Tsurumi Manufacturing Co Ltd
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Description

【0001】
【発明の技術分野】
本発明は例えば、オキシデーションディッチ法等に代表される比較的小規模の下水処理作業において発生する懸濁微粒子を含む懸濁液を、濾液と懸濁微粒子とに分離するためのスクリュー式濾過脱水装置に関するものである。
【0002】
【従来技術とその問題点】
多数枚の環状濾過プレートを所要の間隔を保持して積層状に定着させ、上記各環状濾過プレート間に細隙を形成させた態様で環状可動プレートをそれぞれ介装させて筒状の濾過体に形成し、該濾過体の始端開口部を固液の送り込み口とし終端開口部を脱水固分の送り出し口として中心孔にスクリューコンベアを嵌装し、該スクリューコンベアの回転と連動して環状可動プレートが偏心回転するよう構成されたスクリュー式濾過脱水装置は、特公平7−73642号公報等により公知である。
【0003】
そして各プレート間の細隙は分離水の流出溝となるものであり、これが狭すぎると水分の流出が悪くなり、広すぎると固分までが多量に流出し、いずれの場合も固液分離機能が低下することになる。従って、処理すべき固液の性質に対応させて各プレート間の細隙を適正な大きさに設定することが必要となる。前記特公平7−73642号公報記載の発明では、環状可動プレートの板面要所に細隙保持用凸子を配設することで、各プレート間に一定の細隙が確保される構造となっている。しかしこのような凸子をプレートの板面要所に配設することは難加工で製造コストを押し上げる要因となり、且っ摺接面積が小さくなるため早期に摩耗するという欠点がある。
【0004】
細隙保持用凸子を設けることなしに各プレート間の細隙を一定に保持させるための方策として、図7に示すよう筒状の濾過体101を傾斜状に配置することにより、環状可動プレート103を自重によって下方の環状濾過プレート102の上面102Aへ安定に重合させ、上方の環状濾過プレート102の下面102Bに確保される細隙Bgから分離水を流出させることが提案されている。しかし環状可動プレート103が自重によって下方の環状濾過プレート12の上面102Aへ安定的に重合するためには、濾過体101の傾斜が急勾配であると共に、環状可動プレート103の重量が大きく且っその内周面の滑りが良好となるように仕上られていなければならない。
【0005】
処理後の脱水ケーキは回収タンク内へ落下させ、或いはベルトコンベアにより次の処理場所へ搬送されて行くのであり、回収タンクやベルトコンベアとの連絡を円滑に行わせるためには脱水固分の送り出し口が固液の供給口よりも若干高位置に保持されるよう筒状の濾過体101を緩勾配の傾斜状に設置することが望ましい。しかしこれが急勾配に傾斜して固分の送り出し口が高位置に開口されていると、回収タンクやベルトコンベアとの連絡が不円滑となり、且っ濾過脱水装置自体の背高も大きくなって室内の高さの制約を受ける場所への設置に不都合となる。また、環状可動プレート103の重量を大きくするためにはその肉厚を厚くしなければならず、その結果として各細隙Bg・・Bg間の間隔Sが粗くなり、水分の流出が悪くなって固液分離機能が低下し、また、筒状の濾過体101も長くなり、それに伴ってスクリューコンベア111も長いものが必要とされ装置全体が長くなってしまう。環状プレートは一般にプレス機によって金属板を打抜いて作られるため、内周面および外周面は滑らかではない。しかし環状可動プレート103がその自重によりスクリューブレード111Bの外周に沿って下降させるためにはプレート内周面を滑面に仕上なければならず、細隙保持用凸子を設けるよりも却ってコストが嵩むことになる。更にまた、スクリューコンベア111に沿って固液が上昇すことによりその影響を受けて環状可動プレート103が浮上り、上方の環状濾過プレート102との間に形成されていた細隙Bgが不安定となるおそれもあり、濃度の高い汚泥を処理対象とする場合は特に不安がある。このように、環状可動プレート103の自重を利用して細隙の大きさを規整しようとする上述の提案技術の実用性には疑問がある。
【0006】
【発明の目的】
本発明の目的は、細隙保持用凸子を設けることなしに所要間隙の分離水流出溝が確保され、ローコストに製造し得られると共に固液分離機能に優れ、且っメンテナンス性も良好なスクリュー式濾過脱水装置を提供することにある。
【0007】
【発明の構成】
本発明に係るスクリュー式濾過脱水装置では、多数枚の環状濾過プレートを所要の間隔を保持して積層状に定着させ、上記各環状濾過プレート間に環状可動プレートをそれぞれ遊嵌させて筒状の濾過体に形成し、該濾過体の始端開口部を固液の送り込み口とし終端開口部を脱水固分の送り出し口として該送り出し口に吐出圧調整弁を付設し、スクリューブレードの外径が環状可動プレートの内径よりも大きく環状濾過プレートの内径よりは小さく形成されたスクリューコンベアを前記濾過体の中心孔に嵌装し、スクリューコンベアの駆動時にはスクリューブレードの外周縁が各環状可動プレートの内周縁へ摺接して偏心回転および揺振作動を各環状可動プレートに生じさせ、且っ固液の移動作用に伴う押圧力により揺振作動が抑止されて各環状可動プレートの前面が前方の環状濾過プレートの背面へ摺接すると共に各環状可動プレートの背面は後方の環状濾過プレートの前面から離隔して該離隔部に一定間隙の分離水流出溝が確保された状態で偏心回転が行われ、脱水固分の送り出し後は環状濾過プレートとの前記摺接状態は緩和されて環状可動プレートが偏心回転および揺振作動を起すことにより前面の一部が前方の環状濾過プレートの背面へ摺接すると共に背面の一部が後方の環状濾過プレートの前面へ摺接するよう構成した。
【0008】
【実施例】
以下実施例の図1ないし図6により説明をする。
【0009】
1は筒状の濾過体であり、複数の環状濾過プレート2・・2を互に細隙を隔てて積層状に配列させ、複数の環状可動プレート3・・3を上記環状濾過プレート2・・2の積層間に遊嵌させ、各環状濾過プレート2の外周には各環状可動プレート3の外径よりも大径に形成された座部5・・5を有し、該座部5・・5に付設された間隔保持具6・・6により、各環状濾過プレート2・・2間の間隔を各環状可動プレート3・・3の肉厚よりも僅かに大きく保持させるよう規整する。7・・7は各座部5・・5を支承する固定体であり、濾過体1の外側に沿うように各環状可動プレート3・・3と非接触状態を保って架設されている。なお、濾過体1の外周面は、要所に透孔を設けた外筒(図示せず)で囲うこともある。
【0010】
濾過体1の始端開口部は汚水原水等固液の送り込み口8となり終端開口部は脱水ケーキ等固分の送り出し口9となり、中心孔10にはスクリューコンベア11を嵌装する。12はスクリューコンベア11を駆動するための原動機、13は送り出し口9に付設された吐出圧調整弁である。スクリューコンベア11はスクリューブレード11Bの外径Mが各環状可動プレート3・・3の内周Bよりも大きく各環状濾過プレート2・・2の内径Aよりも小さく形成されいる。なお、環状濾過プレート2および環状可動プレート3はプレス機で打抜いたままで用いられ、内周面や外周面を殊更滑面に仕上る必要はない。
【0011】
【作用】
スクリューコンベア11の駆動により、スクリューブレード11Bの外周縁が各環状可動プレート3・・3の内周縁へ斜交状に摺接して偏心回転および揺振作動を各環状可動プレート3・・3に生じさせるが、送り込み口8から送り込まれた固液混合体が濾過体1内を移動するのに伴う押圧力により、各環状可動プレート3・・3の揺振作動が抑止されてその前面が前方の環状濾過プレート2の背面2Bへ摺接すると共に、各環状可動プレート3・・3の背面は後方の環状濾過プレート2の前面2Aから離隔して該離隔部に一定間隙の分離水流出溝4・・4が確保された状態で偏心回転が行われ、脱水固分の送り出し後は前方の環状濾過プレート2との前記摺接状態は緩和されて各環状可動プレート3・・3が偏心回転と共に揺振作動を起すことになる。
【0012】
このようにスクリューコンベア11の駆動による固液の移動中は、各環状濾過プレート2・・2の前面2Aにそれぞれ一定間隙の分離水流出溝4・・4が確保されているので、濾過水は該分離水流出溝4・・4を通って濾過体1の外部へ流出し、且っ各環状可動プレート3・・3の偏心回転運動によって分離水流出溝4・・4の目詰まりを防止する。前方の環状濾過プレート2の背面2Bと環状可動プレート3との摺接面には液等による潤滑膜が形成されるので、その潤滑作用によって上記偏心回転運動は極めて円滑に行われる。そして脱水固分は送り出し口9から送り出されるが、脱水固分の送り出し後は各環状可動プレート3の前面と各環状濾過プレート2の背面2Bとの摺接状態は緩和されるので、各環状可動プレート3が偏心回転および揺振作動を起すことにより前面の一部が前方の環状可動プレート2の背面2Bへ摺接すると共に背面の一部が後方の環状濾過プレート2の前面2Aと摺接することになる。従って汚泥排出後も暫時空運転を行わせ、その間洗浄水のフラッシングを併用させれば、濾過体1の洗浄が自動的に行われることになる。また、汚泥の排出完了と同時にスクリューコンベア11の運転を停止させた場合にも、環状濾過プレート2と環状可動プレート3との摺接状態は解除されるので該部分の手作業による清掃が可能である。
【0013】
【発明の効果】
本発明スクリュー式濾過脱水装置においては、細隙保持用凸子を設けることなしに所要間隙の分離水流出溝が確保され、ローコストに製造し得られると共に固液分離機能に優れ、且っ脱水固分排出後の洗浄作業も容易であってメンテナンス性も良好であるという利点がある。
【図面の簡単な説明】
【図1】 本発明の実施対象となるスクリュー式濾過脱水装置の構成を略示した縦断側面図である。
【図2】 本発明装置の要部縦断側面図であって、スクリューコンベアの駆動に伴う固液移動中の状態を略示したものである。
【図3】 本発明装置の要部横断平面図であって、脱水固分の送り出し後におけるスクリューコンベア駆動中の状態を略示したものである。
【図4】 本発明装置の縦断正面図である。
【図5】 本発明装置における濾過体の縦断正面図である。
【図6】 本発明装置におけるスクリューコンベアの縦断正面図である。
【図7】 細隙保持用凸子を設けることなしに各プレート間の間隙を一定に保持される構造として提案されたスクリュー式濾過脱水装置の要部縦断側面図である。
【符号の説明】
1 筒状の濾過体
2 環状濾過プレート
2A 環状濾過プレートの前面
2B 環状濾過プレートの背面
3 環状可動プレート
4 分離水流出溝
8 固液の送り込み口
9 脱水固分の送り出し口
10 濾過体の中心孔
11 スクリューコンベア
11B スクリューブレード
13 吐出圧調整弁
A 環状濾過プレートの内径
B 環状可動プレートの内径
M スクリューブレードの外径
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention is, for example, a screw-type filter dehydration for separating a suspension containing suspended fine particles generated in a relatively small-scale sewage treatment operation represented by an oxidation ditch method into filtrate and suspended fine particles. It relates to the device.
[0002]
[Prior art and its problems]
A large number of annular filtration plates are fixed in a stacked manner while maintaining a required interval, and a ring-shaped movable plate is interposed between the annular filtration plates to form a cylindrical filter body. And forming a screw conveyor in the center hole with the starting end opening of the filter body as a solid-liquid feeding port and the terminal opening as a dehydrating solids feeding port, and in conjunction with the rotation of the screw conveyor, an annular movable plate A screw type filter dehydrator configured to rotate eccentrically is known from Japanese Patent Publication No. 7-73642.
[0003]
The slits between the plates serve as the separation water outflow grooves. If this is too narrow, the outflow of moisture will worsen, and if it is too wide, a large amount of solids will flow out. Will drop. Accordingly, it is necessary to set the slits between the plates to an appropriate size in accordance with the properties of the solid liquid to be processed. In the invention described in the above Japanese Patent Publication No. 7-73642, a slit is provided on the plate surface of the annular movable plate so that a constant slit is secured between the plates. ing. However, disposing such protrusions at important points on the plate surface is a difficult process and increases the manufacturing cost, and has a drawback that the sliding contact area becomes small and wears out early.
[0004]
As a measure for keeping the slits between the plates constant without providing slits for holding the slits, an annular movable plate is formed by arranging the cylindrical filter body 101 in an inclined manner as shown in FIG. It has been proposed that 103 is stably polymerized to the upper surface 102A of the lower annular filtration plate 102 by its own weight, and the separated water flows out from the slit Bg secured on the lower surface 102B of the upper annular filtration plate 102. However, in order for the annular movable plate 103 to stably polymerize to the upper surface 102A of the lower annular filtration plate 12 by its own weight, the slope of the filter body 101 is steep, and the weight of the annular movable plate 103 is large. It must be finished so that the slip of the inner peripheral surface is good.
[0005]
The dewatered cake after the treatment is dropped into the collection tank or is transported to the next processing place by the belt conveyor. In order to smoothly communicate with the collection tank and the belt conveyor, the dehydrated solids are sent out. It is desirable to install the tubular filter body 101 in a gentle gradient so that the mouth is held at a slightly higher position than the solid-liquid supply port. However, if this slopes steeply and the solids outlet is open at a high position, the connection with the collection tank and belt conveyor becomes unsmooth, and the height of the filtration dehydrator itself increases and the room becomes thicker. This is inconvenient for installation in places subject to height restrictions. Further, in order to increase the weight of the annular movable plate 103, the thickness thereof must be increased. As a result, the interval S between the slits Bg and Bg becomes rough, and the outflow of moisture becomes worse. The solid-liquid separation function is lowered, and the cylindrical filter body 101 is also lengthened. Accordingly, a long screw conveyor 111 is required, and the entire apparatus is lengthened. Since the annular plate is generally made by punching a metal plate with a press machine, the inner peripheral surface and the outer peripheral surface are not smooth. However, in order for the annular movable plate 103 to move down along the outer periphery of the screw blade 111B by its own weight, the inner peripheral surface of the plate must be finished to be a smooth surface, which is more expensive than providing a slit holding convex. It will be. Furthermore, when the solid liquid rises along the screw conveyor 111, the annular movable plate 103 is lifted by the influence thereof, and the slit Bg formed between the upper annular filtration plate 102 is unstable. In particular, there is anxiety when treating sludge with a high concentration. As described above, there is a question about the practicality of the above-described proposed technique that attempts to regulate the size of the slit using the weight of the annular movable plate 103.
[0006]
OBJECT OF THE INVENTION
The object of the present invention is to provide a separation water outflow groove of a required gap without providing a slit holding convex, which can be manufactured at a low cost, has an excellent solid-liquid separation function, and has good maintainability. An object of the present invention is to provide a filter dewatering device.
[0007]
[Structure of the invention]
In the screw type filtration dewatering device according to the present invention, a large number of annular filtration plates are fixed in a laminated form while maintaining a required interval, and an annular movable plate is loosely fitted between the annular filtration plates, respectively, to form a cylindrical shape. Formed in the filter body, the starting end opening of the filter body is used as a solid-liquid feed port, the end opening is used as a dehydrated solids feed port, a discharge pressure adjusting valve is attached to the feed port, and the outer diameter of the screw blade is annular A screw conveyor formed to be larger than the inner diameter of the movable plate and smaller than the inner diameter of the annular filtration plate is fitted into the center hole of the filter body, and the outer peripheral edge of the screw blade is the inner peripheral edge of each annular movable plate when the screw conveyor is driven. In contact with each other to cause eccentric rotation and vibration operation on each annular movable plate, and the vibration is suppressed by the pressing force accompanying the movement of the solid liquid. The front surface of the movable plate is in sliding contact with the rear surface of the front annular filtration plate, and the rear surface of each annular movable plate is separated from the front surface of the rear annular filtration plate, and a separation water outflow groove with a fixed gap is secured in the separation portion. After the dehydrated solids are sent out, the sliding contact state with the annular filtration plate is relaxed, and the annular movable plate causes eccentric rotation and vibration operation, so that a part of the front surface is annularly filtered forward. The plate was slidably contacted with the back surface, and a part of the back surface was slidably contacted with the front surface of the rear annular filtration plate.
[0008]
【Example】
The embodiment will be described below with reference to FIGS.
[0009]
Reference numeral 1 denotes a cylindrical filter body, in which a plurality of annular filtration plates 2... 2 are arranged in a stacked manner with a gap therebetween, and a plurality of annular movable plates 3. 2 and has a seat portion 5.. 5 formed on the outer periphery of each annular filtration plate 2 larger in diameter than the outer diameter of each annular movable plate 3. The interval holders 6, 6 attached to 5 are regulated so that the interval between the annular filtration plates 2, 2 is held slightly larger than the wall thickness of the annular movable plates 3, 3. Reference numerals 7... 7 denote fixed bodies that support the respective seats 5... 5 and are constructed so as to be in contact with the annular movable plates 3. In addition, the outer peripheral surface of the filter body 1 may be surrounded by an outer cylinder (not shown) provided with through holes at important points.
[0010]
The starting end opening of the filter body 1 becomes a feed port 8 for solid liquid such as raw sewage water, and the end opening becomes a feed port 9 for solids such as dehydrated cake, and a screw conveyor 11 is fitted in the center hole 10. Reference numeral 12 denotes a prime mover for driving the screw conveyor 11, and 13 denotes a discharge pressure adjusting valve attached to the delivery port 9. The screw conveyor 11 is formed such that the outer diameter M of the screw blade 11B is larger than the inner circumference B of each annular movable plate 3.. 3 and smaller than the inner diameter A of each annular filtration plate 2. The annular filtration plate 2 and the annular movable plate 3 are used while being punched out by a press machine, and it is not necessary to finish the inner peripheral surface and the outer peripheral surface to a particularly smooth surface.
[0011]
[Action]
By driving the screw conveyor 11, the outer peripheral edge of the screw blade 11B slides obliquely on the inner peripheral edge of each annular movable plate 3, 3 to cause eccentric rotation and vibration operation on each annular movable plate 3,. However, due to the pressing force associated with the movement of the solid-liquid mixture fed from the feed port 8 in the filter body 1, the swinging operation of each of the annular movable plates 3,. While sliding in contact with the back surface 2B of the annular filtration plate 2, the back surface of each annular movable plate 3,... 3 is separated from the front surface 2A of the rear annular filtration plate 2, and a separated water outflow groove 4 with a fixed gap is formed in the separation portion. 4 is secured, and after the dehydrated solids are sent out, the sliding contact with the front annular filtration plate 2 is relaxed, and each of the annular movable plates 3. Wake up It becomes door.
[0012]
Thus, during the movement of the solid liquid by the drive of the screw conveyor 11, the separated water outflow grooves 4.. 4 of a certain gap are secured on the front surface 2 A of each annular filtration plate 2. It flows out of the filter body 1 through the separated water outflow grooves 4... 4, and the clogging of the separated water outflow grooves 4. . Since a lubricating film made of liquid or the like is formed on the sliding contact surface between the back surface 2B of the front annular filtration plate 2 and the annular movable plate 3, the eccentric rotational motion is performed very smoothly by the lubricating action. The dehydrated solids are sent out from the delivery port 9. After the dehydrated solids are sent out, the sliding contact state between the front surface of each annular movable plate 3 and the rear surface 2B of each annular filtration plate 2 is relaxed. By causing the plate 3 to be eccentrically rotated and oscillated, a part of the front surface comes into sliding contact with the rear surface 2B of the front annular movable plate 2, and a part of the rear surface comes into sliding contact with the front surface 2A of the rear annular filtration plate 2. Become. Therefore, if the idling operation is performed for a while after the sludge is discharged and flushing water is flushed during that time, the filter body 1 is automatically cleaned. Further, even when the operation of the screw conveyor 11 is stopped simultaneously with the completion of the sludge discharge, the sliding contact state between the annular filtration plate 2 and the annular movable plate 3 is released, so that this portion can be manually cleaned. is there.
[0013]
【The invention's effect】
In the screw type filtration dehydration apparatus of the present invention, a separation water outflow groove of a required gap is secured without providing a slit holding convex, which can be manufactured at a low cost and has an excellent solid-liquid separation function. There is an advantage that the cleaning operation after the discharge is easy and the maintainability is also good.
[Brief description of the drawings]
FIG. 1 is a longitudinal side view schematically showing the configuration of a screw-type filtration and dehydration apparatus that is an object of the present invention.
FIG. 2 is a longitudinal sectional side view of an essential part of the apparatus of the present invention, and schematically shows a state during solid-liquid movement accompanying driving of a screw conveyor.
FIG. 3 is a cross-sectional plan view of an essential part of the apparatus of the present invention, and schematically shows a state in which the screw conveyor is being driven after the dehydrated solids are sent out.
FIG. 4 is a longitudinal front view of the device of the present invention.
FIG. 5 is a longitudinal sectional front view of a filter body in the device of the present invention.
FIG. 6 is a longitudinal front view of a screw conveyor in the device of the present invention.
FIG. 7 is a longitudinal sectional side view of a main part of a screw-type filtration and dehydration apparatus proposed as a structure in which a gap between each plate is kept constant without providing a slit holding convex.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Cylindrical filter body 2 Annular filtration plate 2A Front surface of annular filtration plate 2B Rear surface of annular filtration plate 3 Annular movable plate 4 Separation water outflow groove 8 Solid liquid feed port 9 Dehydrated solid content feed port 10 Center hole of filter body 11 Screw conveyor 11B Screw blade
13 Discharge pressure adjustment valve A Inner diameter of annular filtration plate B Inner diameter of annular movable plate M Outer diameter of screw blade

Claims (1)

多数枚の環状濾過プレートを所要の間隔を保持して積層状に定着させ、上記各環状濾過プレート間に環状可動プレートをそれぞれ遊嵌させて筒状の濾過体に形成し、該濾過体の始端開口部を固液の送り込み口とし終端開口部を脱水固分の送り出し口として該送り出し口に吐出圧調整弁を付設し、スクリューブレードの外径が環状可動プレートの内径よりも大きく環状濾過プレートの内径よりは小さく形成されたスクリューコンベアを前記濾過体の中心孔に嵌装し、スクリューコンベアの駆動時にはスクリューブレードの外周縁が各環状可動プレートの内周縁へ摺接して偏心回転および揺振作動を各環状可動プレートに生じさせ、且っ固液の移動作用に伴う押圧力により揺振作動が抑止されて各環状可動プレートの前面が前方の環状濾過プレートの背面へ摺接すると共に各環状可動プレートの背面は後方の環状濾過プレートの前面から離隔して該離隔部に一定間隙の分離水流出溝が確保された状態で偏心回転が行われ、脱水固分の送り出し後は環状濾過プレートとの前記摺接状態は緩和されて環状可動プレートが偏心回転および揺振作動を起すことにより前面の一部が前方の環状濾過プレートの背面へ摺接すると共に背面の一部が後方の環状濾過プレートの前面へ摺接するよう構成したことを特徴とする、スクリュー式濾過脱水装置。A large number of annular filtration plates are fixed in a stacked manner while maintaining a required interval, and an annular movable plate is loosely fitted between the annular filtration plates to form a cylindrical filter body. A discharge pressure adjusting valve is attached to the outlet with the opening as the solid-liquid inlet and the terminal opening as the dehydrated solids outlet, and the outer diameter of the screw blade is larger than the inner diameter of the annular movable plate. A screw conveyor formed smaller than the inner diameter is fitted into the center hole of the filter body, and when the screw conveyor is driven, the outer peripheral edge of the screw blade is in sliding contact with the inner peripheral edge of each annular movable plate to perform eccentric rotation and vibration operation. Oscillating action is suppressed by the pressing force generated by the moving action of the solid liquid generated in each annular movable plate, and the front surface of each annular movable plate is the front annular filtration plate. And the back of each annular movable plate is separated from the front surface of the rear annular filtration plate, and eccentric rotation is performed with a separation water outflow groove having a fixed gap secured in the separation portion. After the feeding, the sliding contact state with the annular filtration plate is relaxed, and the annular movable plate causes eccentric rotation and vibration operation so that a part of the front surface is in sliding contact with the rear surface of the front annular filtration plate and A screw type filter dehydrating apparatus, wherein the portion is configured to be in sliding contact with the front surface of the rear annular filtration plate.
JP2002184061A 2002-06-25 2002-06-25 Screw type filter dehydrator Expired - Lifetime JP3751578B2 (en)

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CN108159770A (en) * 2018-02-01 2018-06-15 吴云萍 A kind of stacked solid-liquid separating equipment of double movable ring
KR102145039B1 (en) * 2020-02-26 2020-08-18 주식회사 우성테크 Disk Type Screen Dewatering Device
CN113149362B (en) * 2021-02-19 2022-10-25 国家电投集团远达水务有限公司 Zero-discharge treatment process and system for printing and dyeing wastewater
CN114642906B (en) * 2022-03-30 2023-07-18 陕西黑松环保科技有限公司 Intelligent internal compression solid-liquid separation device for sweeper
CN116534956B (en) * 2023-05-10 2024-03-29 郑楷集团有限公司 Efficient electrolysis device for sewage treatment and electrolysis method thereof

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