JP3779245B2 - Screw type filter dehydrator - Google Patents

Screw type filter dehydrator Download PDF

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Publication number
JP3779245B2
JP3779245B2 JP2002230870A JP2002230870A JP3779245B2 JP 3779245 B2 JP3779245 B2 JP 3779245B2 JP 2002230870 A JP2002230870 A JP 2002230870A JP 2002230870 A JP2002230870 A JP 2002230870A JP 3779245 B2 JP3779245 B2 JP 3779245B2
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Japan
Prior art keywords
movable plate
annular
filter body
annular movable
screw
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Expired - Lifetime
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JP2002230870A
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Japanese (ja)
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JP2004066146A (en
Inventor
秀明 金谷
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Tsurumi Manufacturing Co Ltd
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Tsurumi Manufacturing Co Ltd
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  • Filtration Of Liquid (AREA)

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、濃縮工程を経由しない低濃度の状態により、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】
従来から、多数枚の環状濾過プレートを互に細隙を隔てて積層状に定着させ、上記各環状濾過プレート間にそれぞれ環状可動プレートを遊嵌させることにより上記各細隙を分離水流出溝とする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、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径方向への偏心回転運動を各環状可動プレートに生じさせるスクリュー式濾過脱水装置は公知である。
【0003】
そしてスクリューコンベアの駆動により、環状可動プレートが環状濾過プレート間の間隙に沿って偏心回転運動を行い、送り込み口から濾過体内へ送り込まれた汚泥原水はスクリューブレードに沿って旋回しながら軸方向へ前進する過程において、濾過された濾水は分離水流出溝より流出すると共に脱水されて含水比の低くなった脱水汚泥ケ−キは前方の送り出し口から順次排出されるのであるが、脱水効率を上げるために環状可動プレートの偏心回転運動量を大きくすれば、送り込み口および送り出し口近傍での汚泥のリーク量が多くなり、また、汚泥のリークを抑止するために環状可動プレートの偏心回転運動量を小さくすれば、脱水効率が低下することは避けられないというのが現状である。
【0004】
【発明の目的】
本発明の目的は、送り込み口および送り出し口近傍での汚泥のリークを抑止し得ると共に中間部での濾水流出効率を高めて、有効で適正な濾過脱水作業の行われるスクリュー式濾過脱水装置,更に詳述すれば、送り込み口近傍での低濃度段階では環状可動プレートが小さな偏心回転運動により汚泥フロックの破壊とリークを防止し、脱水効率を高めるべき濾過体中間部では環状可動プレートの大きな偏心回転運動により汚泥ケ−キに剪断力を加えて液分を多く排出させ、内圧の増大している送り出し口近傍では環状可動プレートが小さな偏心回転運動により汚泥のリークを抑止するという、極めて合理的な作動方式によって有効で適正な濾過脱水作業が行われるスクリュー式濾過脱水装置を提供することにある。
【0005】
【発明の構成】
本発明では、多数枚の環状濾過プレートを互に細隙を隔てて積層状に定着させ,上記各環状濾過プレート間にそれぞれ環状可動プレートを遊嵌させることにより上記各細隙を分離水流出溝とする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、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径方向への偏心回転運動を各環状可動プレートに生じさせるスクリュー式濾過脱水装置において、濾過体の中間部における環状可動プレートの内径が、送り込み口および送り出し口近傍における環状可動プレートの内径よりも小さく形成せられ、スクリューコンベア駆動時における環状可動プレートの径方向への前記偏心回転運動量が、濾過体の中間部では大きくなり送り込み口および送り出し口近傍では小さくなるよう構成した。
【0006】
【作用】
スクリューコンベアの駆動により、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、径方向への偏心回転運動を各環状可動プレートに生じさせる。そして送り込み口から濾過体内へ送り込まれた汚泥原水が、スクリューブレードに沿って旋回しながら軸方向へ前進する過程において、濾過された濾水は分離水流出溝より流出すると共に脱水されて含水比の低くなった脱水汚泥ケ−キは前方の送り出し口から順次排出されるのであるが、前記環状可動プレートの偏心回転運動量は、濾過体の中間部では大きく,送り込み口および送り出し口近傍では小さく作用する。従って、送り込み口近傍での低濃度段階における汚泥フロックの破壊とリークを抑止し、脱水効率を高めるべき中間部では汚泥ケ−キに剪断力を加えて液分を多く排出させ、内圧の増大している送り出し口近傍では汚泥のリーク量を抑止することになる。
【0007】
【実施例】
以下の図1ないし図6の実践例により説明をする。
【0008】
1は筒状の濾過体であり、多数枚の環状濾過プレート2・・2を所要の細隙を保持して積層状に定着させ、該環状濾過プレート2・・2の各積層間にそれぞれ環状可動プレート3・・3を遊嵌させることにより上記各細隙を分離水流出溝4・・4とし、各環状濾過プレート2・・2の外周には各環状可動プレート3・・3の外周偏心回転軌跡よりも外方へ張出された座部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。そして濾過体1の始端開口部は固液の送り込み口8となり終端開口部は脱水固分の送り出し口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の内径Vよりも大きく各環状濾過プレート2・・2の内径Wよりは小さく形成される。また、濾過体中間部1Bにおける環状可動プレート3B・・3Bの内径V‘が、送り込み口近傍1Aにおける環状可動プレート3A・・3Aおよび送り出し口近傍1Cにおける環状可動プレート3C・・3Cの内径Vよりも小さく形成せられ、スクリューコンベア11の駆動時に送り込み口近傍1Aにおける環状可動プレート3A・・3Aの偏心回転運動量は小さくなり、濾過体中間部1Bにおける環状可動プレート3B・・3Bの偏心回転運動量は大きくなり、送り出し口近傍1Cにおける環状可動プレート3C・・3Cの偏心回転運動量は小さくなるよう構成されている。
【0009】
原動機12を駆動させるとスクリューコンベア11が回転し,送り込み口8から濾過体1内へ送り込まれた汚水原水が、スクリューブレード11Bに沿って旋回しながら軸方向へ前進する過程において、濾過された濾水は分離水流出溝4・・4より流出すると共に脱水されて含水比の低くなった脱水汚泥ケ−キは前方の送り出し口9から順次排出されるのであるが、送り込み口近傍1Aでの低濃度段階においては環状可動プレート3A・・3Aの偏心回転運動量が小さくなることにより汚泥フロックの破壊とリークを防止し、脱水効率を高めるべき濾過体中間部1Bでは環状可動プレート3B・・3Bの偏心回転運動量が大きくなることにより汚泥ケ−キに剪断力を加えて液分を多く排出させ、内圧の増大している送り出し口近傍1Cでは環状可動プレート3C・・3Cの偏心回転運動量が小さくなって汚泥のリークを防止することになる。
【0010】
【発明の効果】
本発明スクリュー式濾過脱水装置によれば、送り込み口近傍での低濃度段階では環状可動プレートが小さな偏心回転運動により汚泥フロックの破壊とリークを防止し、脱水効率を高めるべき濾過体中間部では環状可動プレートの大きな偏心回転運動により汚泥ケ−キに剪断力を加えて液分を多く排出させ,内圧の増大している送り出し口近傍では環状可動プレートが小さな偏心回転運動により汚泥のリークを抑止するという、極めて合理的な作動方式によって有効で適正な濾過脱水作業が行われるのである。
【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】本発明装置における濾過体の要部縦断側面図である。
【図3】本発明装置における濾過体の送り込み口近傍での縦断正面図である。
【図4】本発明装置における濾過体中間部での縦断正面図である。
【図5】本発明装置における送り出し口近傍で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。
【符号の説明】
1 筒状の濾過体
1A 送り込み口近傍
1B 濾過体中間部
1C 送り出し口近傍
2 環状濾過プレート
3 環状可動プレート
3A 送り込み口近傍における環状可動プレート
3B 濾過体中間部における環状可動プレート
3C 送り出し口近傍における環状可動プレート
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
M スクリューブレードの外径
V 環状可動プレートの内径
V‘ 濾過体中間部における環状可動プレートの内径
W 環状濾過プレートの内径
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention, for example, a suspension containing suspended fine particles generated in a relatively small-scale sewage treatment operation represented by the oxidation ditch method, etc. The present invention relates to a screw-type filter dehydrator for separating fine particles.
[0002]
[Prior art and its problems]
Conventionally, a large number of annular filtration plates are fixed in a stacked manner with a gap between each other, and the respective annular movable plates are loosely fitted between the respective annular filtration plates, whereby each of the slits is separated from the separation water outflow groove. The outer diameter of the screw blade is larger than the inner diameter of the annular movable plate, with the starting end opening of the filter body serving as a solid-liquid feed port and the terminal opening serving as a dehydrated solid feed port. A screw conveyor formed smaller than the inner diameter of the annular filter plate 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 in the radial direction. A screw type filtration and dehydration device that generates an eccentric rotational motion of each annular movable plate is known.
[0003]
Then, by driving the screw conveyor, the annular movable plate performs an eccentric rotational movement along the gap between the annular filtration plates, and the raw sludge water fed into the filtration body from the feeding port advances along the screw blade while moving in the axial direction. In this process, the filtered filtrate flows out from the separated water outflow groove, and the dewatered sludge cake that has been dewatered and has a low water content ratio is sequentially discharged from the front delivery port, but the dewatering efficiency is increased. Therefore, if the eccentric rotational momentum of the annular movable plate is increased, the amount of sludge leakage near the inlet and outlet is increased, and the eccentric rotational momentum of the annular movable plate is reduced to suppress the sludge leakage. In the current situation, it is inevitable that the dewatering efficiency is lowered.
[0004]
OBJECT OF THE INVENTION
An object of the present invention is to provide a screw-type filtration and dehydration device capable of suppressing sludge leakage near the inlet and the outlet and increasing the drainage efficiency at the intermediate portion to perform an effective and appropriate filtration and dehydration operation. More specifically, in the low concentration stage near the inlet, the annular movable plate prevents the sludge floc from being broken and leaked by a small eccentric rotational motion, and in the middle part of the filter body where dewatering efficiency should be increased, the annular movable plate has a large eccentricity. Rotating motion applies a shearing force to the sludge cake to discharge a large amount of liquid, and the annular movable plate suppresses sludge leakage by a small eccentric rotating motion in the vicinity of the delivery port where the internal pressure is increasing. Another object of the present invention is to provide a screw-type filtration and dehydration apparatus in which an effective and appropriate filtration and dehydration operation is performed by a simple operation system.
[0005]
[Structure of the invention]
In the present invention, a large number of annular filtration plates are fixed in a stacked manner with gaps between each other, and the annular movable plates are loosely fitted between the annular filtration plates, thereby separating the slits into separate water outflow grooves. The outer diameter of the screw blade is larger than the inner diameter of the annular movable plate, with the opening at the start end of the filter body serving as a solid liquid feed port and the terminal opening as a dewatered solid feed port. A screw conveyor formed to be larger than the inner diameter of the annular filtration plate 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. In the screw type filter dehydrator that causes each annular movable plate to generate an eccentric rotational movement toward the center of the filter body, The eccentric rotational momentum in the radial direction of the annular movable plate when the screw conveyor is driven is increased in the middle portion of the filter body, and is formed at the intermediate portion of the filter body. It was configured to be small in the vicinity.
[0006]
[Action]
By driving the screw conveyor, the outer peripheral edge of the screw blade is brought into sliding contact with the inner peripheral edge of each annular movable plate, and an eccentric rotational movement in the radial direction is caused in each annular movable plate. In the process in which the sludge raw water fed from the feed port into the filter body advances in the axial direction while swirling along the screw blades, the filtered filtrate flows out from the separation water outflow groove and is dehydrated to have a water content ratio. The dewatered sludge cake that has been lowered is sequentially discharged from the front delivery port, but the eccentric rotational momentum of the annular movable plate is large in the middle part of the filter body and acts small in the vicinity of the feed port and the delivery port. . Therefore, the sludge floc breakage and leakage at the low concentration stage near the inlet are suppressed, and in the intermediate part where the dewatering efficiency should be increased, a shear force is applied to the sludge cake to discharge a large amount of liquid, increasing the internal pressure. The amount of sludge leakage is suppressed near the outlet.
[0007]
【Example】
This will be described with reference to the following practical examples shown in FIGS.
[0008]
Reference numeral 1 denotes a cylindrical filter body, in which a large number of annular filtration plates 2... 2 are fixed in a laminated form while holding required slits, and each annular filtration plate 2. By loosely fitting the movable plates 3, 3, the slits are separated into the water outlet grooves 4, 4, and the outer peripheries of the annular movable plates 3, 3 are eccentric to the outer periphery of the annular filtration plates 2, 2. It has a seat portion 5.. 5 projecting outward from the rotation trajectory, and a space holder 6.. 6 attached to the seat portion 5. Is set to be slightly larger than the wall thickness of each annular movable plate 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. The starting end opening of the filter body 1 serves as a solid-liquid feed port 8, and the terminal opening serves as a dehydrated solid feed port 9, and a screw conveyor 11 is fitted into 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 diameter V of each annular movable plate 3.. 3 and smaller than the inner diameter W of each annular filtration plate 2. Further, the inner diameter V ′ of the annular movable plates 3B... 3B in the filter intermediate part 1B is larger than the inner diameter V of the annular movable plates 3A... 3A in the vicinity of the feeding port 1A and the annular movable plates 3C. The eccentric rotational momentum of the annular movable plates 3A,... 3A in the vicinity of the inlet 1A when the screw conveyor 11 is driven is small, and the eccentric rotational momentum of the annular movable plates 3B,. The eccentric rotational momentum of the annular movable plates 3C... 3C in the vicinity of the delivery port 1C is increased and is reduced.
[0009]
When the prime mover 12 is driven, the screw conveyor 11 rotates, and the raw sewage water fed into the filter body 1 from the feed port 8 advances in the axial direction while turning along the screw blade 11B. The dewatered sludge cake that has flowed out of the separated water outflow grooves 4 and 4 and has been dewatered and has a low water content ratio is sequentially discharged from the front discharge port 9, but is low in the vicinity of the supply port 1 </ b> A. In the concentration stage, the eccentric rotational momentum of the annular movable plates 3A,... 3A is reduced to prevent the sludge floc from being broken and leaked. In the intermediate part 1B of the filter body to be improved in dewatering efficiency, the eccentricity of the annular movable plates 3B,. By increasing the rotational momentum, a shear force is applied to the sludge cake to discharge a large amount of liquid. It will prevent leakage of sludge eccentric rotation of the movable plate 3C · · 3C is decreased.
[0010]
【The invention's effect】
According to the screw type filter dehydrator of the present invention, the annular movable plate prevents the sludge floc from being broken and leaked by a small eccentric rotational motion at a low concentration stage near the inlet, and the intermediate part of the filter body to improve the dewatering efficiency is annular. A large eccentric rotational movement of the movable plate applies a shearing force to the sludge cake to discharge a large amount of liquid, and the annular movable plate suppresses sludge leakage by a small eccentric rotational movement in the vicinity of the delivery port where the internal pressure is increasing. An effective and proper filtration and dewatering operation is performed by an extremely rational operation system.
[Brief description of the drawings]
FIG. 1 is a vertical side view schematically showing a configuration of a screw type filtration dehydration apparatus to be an object of the present invention.
FIG. 2 is a longitudinal sectional side view of a main part of a filter body in the device of the present invention.
FIG. 3 is a longitudinal front view of a filter body in the vicinity of the inlet of the filter according to the present invention.
FIG. 4 is a longitudinal front view of the intermediate portion of the filter body in the device of the present invention.
FIG. 5 is a longitudinal front view in the vicinity of the delivery port in the apparatus of the present invention.
FIG. 6 is a longitudinal front view of a screw conveyor in the device of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Cylindrical filter body 1A Near feed port 1B Filter body intermediate part 1C Near feed port 2 Annular filtration plate 3 Annular movable plate 3A Annular movable plate 3B near an feed port Annular movable plate 3C in an intermediate part of an annular ring Movable plate 4 Separation water outflow groove 8 Solid liquid feed port 9 Dehydrated solid content feed port 10 Filter body central hole 11 Screw conveyor 11B Screw blade M Screw blade outer diameter V Ring movable plate inner diameter V 'Filter body intermediate part Inner diameter W of annular movable plate at

Claims (1)

多数枚の環状濾過プレートを互に細隙を隔てて積層状に定着させ、上記各環状濾過プレート間にそれぞれ環状可動プレートを遊嵌させることにより上記各細隙を分離水流出溝とする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、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径方向への偏心回転運動を各環状可動プレートに生じさせるスクリュー式濾過脱水装置において、濾過体の中間部における環状可動プレートの内径が、送り込み口および送り出し口近傍における環状可動プレートの内径よりも小さく形成せられ、スクリューコンベア駆動時における環状可動プレートの径方向への前記偏心回転運動量が、濾過体の中間部では大きくなり送り込み口および送り出し口近傍では小さくな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 cylindrical shape in which a large number of annular filtration plates are fixed to each other with a gap between each other, and each movable slit is loosely fitted between each of the annular filtration plates so that each of the slits serves as a separation water outflow groove. The filter body has a starting end opening as a solid-liquid inlet and a terminal opening as a 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 of the filter body is fitted in 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 and is eccentrically rotated in the radial direction. In the screw type filter dewatering device that causes the movement of each annular movable plate, the inner diameter of the annular movable plate in the middle part of the filter body is different from that of the feeding port and the feeding port. It is formed smaller than the inner diameter of the annular movable plate in the vicinity of the outlet, and the eccentric rotational momentum in the radial direction of the annular movable plate when the screw conveyor is driven becomes larger in the middle part of the filter body and in the vicinity of the inlet and outlet. A screw type filter dehydrator characterized by being configured to be small.
JP2002230870A 2002-08-08 2002-08-08 Screw type filter dehydrator Expired - Lifetime JP3779245B2 (en)

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JP3779245B2 true JP3779245B2 (en) 2006-05-24

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