JP4081759B2 - Screw press - Google Patents

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Publication number
JP4081759B2
JP4081759B2 JP2003163238A JP2003163238A JP4081759B2 JP 4081759 B2 JP4081759 B2 JP 4081759B2 JP 2003163238 A JP2003163238 A JP 2003163238A JP 2003163238 A JP2003163238 A JP 2003163238A JP 4081759 B2 JP4081759 B2 JP 4081759B2
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Japan
Prior art keywords
screw
screen
screw shaft
outer cylinder
filtration
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JP2003163238A
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Japanese (ja)
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JP2004358549A (en
Inventor
謙三 菅谷
幸利 三谷
伸夫 本田
学 山下
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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】
本発明は、濃縮ゾーンの外筒を回転させながらろ過脱水を行うスクリュープレスに関し、詳しくは、低濃度汚泥でもスクリーンの目詰まりを防止しながら濃縮脱水が行え、脱水効率を向上させるスクリュープレスの改良に関するものである。
【0002】
【従来の技術】
従来、下水、し尿等の有機性汚泥をスクリュープレスで脱水処理する場合には、汚泥に高分子凝集剤を添加撹拌して、フロックを生成させ、この凝集汚泥をスクリュープレスに供給して脱水処理を行っている。しかし、固形物濃度の低い汚泥では、外筒スクリーンの前段部で多量の分離液を効率よく高速で排水することは困難であった。特に、この前段部は高分子凝集剤による薄膜がスクリーン内面に発生し、排水性が阻害されることにより残渣が付着して、目詰まりが発生し易いものである。このため、低濃度汚泥を遠心濃縮機や浮上濃縮機等の濃縮機により、濃縮した後、濃縮汚泥をスクリュープレスでろ過・脱水する方法がとられている。しかし、濃縮機とスクリュープレスを使用することにより、設置面積が大きく、駆動電力費も高くなるという問題があった。そして、維持管理にも人手がかかるという問題もある。
【0003】
上記の問題を解消するために、外筒スクリーンの前半部を濃縮ゾーン、後半部をろ過・脱水ゾーンに構成し、この濃縮ゾーンの外筒スクリーンをスクリュー軸の回転方向に対して、差速回転させることにより、濃縮機能をもたせたスクリュープレスは公知である。しかし、前記濃縮機能をもったスクリュープレスにおいても、固形物濃度の低い汚泥では、外筒スクリーン前段の濃縮部には高分子凝集剤による薄膜がスクリーン内面に発生し、排水性が阻害されることにより残渣が付着して、目詰まりが発生し多量の分離液を効率よく高速で排水することは困難である。
【0004】
【特許文献1】
特公平3−78123号公報
【特許文献2】
特開昭64−2920号公報
【0005】
【発明が解決しょうとする課題】
前記、従来技術の問題を解決するために、外筒スクリーンを回転させながら連続して洗浄水を噴射することで外筒スクリーンの目詰まりを防止する方法が特許文献1に記載されている。しかし、特許文献1における方法では噴射された洗浄水がスクリーンの小孔を貫通して外筒内部に進入し、濃縮された汚泥が希釈され、濃縮効果が半減する恐れがあり、ろ過・脱水ゾーンにおける脱水効率やケーキ含水率にも影響を及ぼす恐れがある。
【0006】
特許文献2には、外筒スクリーンの目詰まりを防止する方法として、スクリーンを断面が略三角形状をしたウエッジワイヤーで内周面側を狭く、外周面側が広いスリットで構成することにより、高圧搾が可能で、スリット部に入り込んだ夾雑物は漸次、外部に抜け出るため目詰まりを防止できるとの記載がある。さらに、特許文献2においては、スクリュー軸の後端部を外周面にスクリーンを張設した円筒状に形成して、ろ過部とし脱水効率を向上するようにした記載がある。
【0007】
しかし、上記特許文献2においては、高分子凝集剤によって凝集された低濃度の汚泥を前段部に供給した場合、狭いスリットから多量のろ液を高速で排水することは困難であり、さらに、外筒スクリーンの内面とスクリュー軸のスクリーン外面には高分子凝集剤による薄膜が形成され、排水性が悪化して脱水効率が低下する恐れがある。そして、スクリュー軸のスクリーン面から内部に流入したろ液を排出するために真空ポンプで吸引しており、精度の高いシール構造が必要となったり、電力費等のランニングコストが嵩むといった課題がある。
【0008】
【課題を解決するための手段】
本発明は上記の従来技術における課題を解決したものであって、その要旨とするところは、スクリーンを張設した外筒を前半部の回転自在な濃縮ゾーンと後半部のろ過・脱水ゾーンに分割して、この分割した外筒内にスクリュー羽根を巻き掛けたスクリュー軸を内設し、前記濃縮ゾーンの外筒の始端部に供給したスラリーをスクリュー軸を回転させながら、ろ過・脱水を行ない、外筒のスクリーンからろ液を分離して、ろ過・脱水ゾーンの外筒の終端部からケーキを取出すスクリュープレスにおいて、上記スクリュー軸を後端部で前後方向に分割し、この後端部のスクリュー軸にスクリーンを張設し、前記スクリュー羽根の外周部に始端から後端に渡ってスクレーパーを配設するとともに、スクリュー羽根の内周部にも前記スクリュー軸のスクリーン面に対設してスクレーパーを配設し、このスクレーパーを外筒の内周面及びスクリュー軸のスクリーン面に弾圧的に摺接させて、スクリュー軸を回転させながらろ過・脱水を行い、さらに、前記外筒の分割部にクラッチを配設し、濃縮ゾーンとろ過・脱水ゾーンとを連結解離自在としたスクリュープレスである。
【0009】
そして、前記分割したスクリュー軸のスクリーンを張設した後端部を固定とし、他端部を回転自在としたり、スクリュー軸に張設したスクリーンとしてウエッジワイヤーを用い、該ウエッジワイヤーのスリット側をろ過面とした。また、スクリュー軸を駆動させる駆動軸を中空とし、この駆動軸の外周部に前記スクリュー軸のスクリーンの内周面に対設する位置に複数の洗浄ノズルを配設し、前記スクリーンを洗浄するようにしたスクリュープレスである。
【0010】
【発明の実施の形態】
この発明に係るスクリュープレスは上述のように構成しており、下水、し尿等の有機性汚泥に高分子凝集剤を添加撹拌して、凝集フロックを生成させた汚泥をスクリュープレスの供給口に圧送すると、汚泥は外筒始端側のスクリュー軸の供給路に流入し、スクリュー軸に開口している供給孔より濃縮ゾーンのスクリュー羽根の間に供給されるので、凝集フロックがスクリュー羽根の影響を受けて破壊されることなく外筒の始端部に流入する。
【0011】
濃縮ゾーンに供給された汚泥は、回転するスクリュー羽根で移送されながら外筒のスクリーンからろ液が排出され、濃縮が行われる。濃縮ゾーンの外筒をスクリュー軸とは逆方向に回転させることにより、相対的にスクリュー羽根の回転数が多くなり、スクリュー羽根の先端部に配設しているスクレーパーとスクリーンとの摺接回数が増加し、スクリーンに堆積してくるケーキ層や高分子凝集剤による薄膜を掻取って、目詰まりしようとするろ過面を再生して多量のろ液を排出することができる。そして、スクリーンの目詰まりをスクレーパーで未然に防止しながらスクリュー羽根で汚泥を移送させるので、固形物濃度が低く水負荷の大きい汚泥でも効率良く濃縮が行えるものである。
【0012】
次に濃縮ゾーンで濃縮された汚泥は、ろ過・脱水ゾーンへと移送され、後半部のスクリュー羽根でろ過・脱水される。この時、濃縮ゾーンの外筒とろ過・脱水ゾーンの外筒を連続した円筒状に形成し、この外筒内に始端部から後端部に向かってテーパー状にその径を拡大させたスクリュー軸を配設して、外筒とスクリュー軸との間隙を後端側に向かって相対的に減少させるようにしているので、スクリュー羽根間の体積が漸減し、汚泥への加圧力が増大し、終端部の排出口から脱水されたケーキを取り出すことができるものである。さらに、スクリュー軸の後端部は円筒状に形成し、外周面にスクリーンを張設して、ろ過面としており、このスクリーン面に対接するスクリュー羽根にはスクレーパーを配設しているので、目詰まりを防止しながら外筒とスクリュー軸のスクリーンで両面ろ過が行え、更に、低含水率の脱水ケーキが得られ、汚泥の処理量も増加するものである。以下、図面に基づいて本発明に係るスクリュープレスの実施例について詳述する。
【0013】
【実施例】
図1は本発明に係るスクリュープレスの縦断側面図であって、スクリュープレス1が前後のフレーム2,3に支架されており、濃縮ゾーンAとろ過・脱水ゾーンBに分割した外筒4の周部にはスクリーン5を張設し、この外筒4内に始端部から後端部に向かってテーパー状にその径を拡大させ、外周面にスクリュー羽根6を巻き掛けたスクリュー軸7をフレーム2,3で軸支している。該スクリュー軸7は駆動機8によって回転自在としている。濃縮ゾーンAとろ過・脱水ゾーンBに分割された外筒4は分割部に配設したクラッチ9によって、連結解離自在になっている。通常の濃縮、ろ過・脱水運転時においては、外筒4は解離された状態になっており、濃縮ゾーンAの外筒4aだけが、駆動機10によって回動し、ろ過・脱水ゾーンBの外筒4bは固定した状態になっている。外筒4aの回転方向は後述するスクリュー軸7の回転方向とは逆方向に回転するようにしている。
【0014】
高分子凝集剤によって凝集された汚泥をスクリュー軸7の先端部に開口している供給口11から供給し、スクリュー軸7の外周面に開口した供給孔12から、外筒4の濃縮ゾーンAの始端部内に流入させる。流入した凝集汚泥は、前記スクリュー羽根6で移送されながら、外筒4のスクリーン5からろ液が分離・排出され濃縮される。前半部の濃縮ゾーンAの外筒4aをスクリュー軸7とは逆回転させることにより、スクリュー羽根6の先端部に配設しているスクレーパー13a(後述する)とスクリーン5との摺接回数が増加し、スクリーン5の内周面に堆積するケーキ層や高分子凝集剤による薄膜を掻取って、スクリーン5面を再生するので、目詰まり防止ができ、連続してろ液を排出できる。そして、スクリーン5を開口率の大きい(略20〜40%)パンチングプレートで構成しているので、多量のろ液を排出することができ、固形物濃度が低く水負荷の大きい汚泥でも効率良く、濃縮が行える。濃縮ゾーンAで濃縮された汚泥は、スクリュー羽根6によってろ過・脱水ゾーンBへと移送され、スクリーン5からさらにろ液を排出して加圧・脱水されながら、後端部へと移動する。スクリュー軸7は後端部で分割しており、後端部のスクリュー軸14は円筒状に形成し、外周面にはスクリーン15を張設して、ろ過面としている。
【0015】
図2に基づき、前記後端部のスクリュー軸14について説明する。円筒状に形成したスクリュー軸14の外周面には断面が略三角形状をした部材を多数並列して構成したウエッジワイヤーからなるスクリーン15を張設しており、スクリーン5とスクリーン15による両面ろ過ゾーンCを形成し、該両面ろ過ゾーンCで内外面から脱水を行うようにしているため、より低含水の脱水ケーキを排出口16より取り出すことができる。排出口16にはプレッサー17が対設してあり、脱水ケーキに背圧を加えながら、排出口16の開口量を調節するようにしている。前記ウエッジワイヤーは図5に示すようにスリット側を外周面になるように張設しており、該スリットは図3及び図4のように、スクリュー軸14の軸芯と平行あるいは直交する方向のいずれでもよい。尚、スクリュー軸14の終端部でプレッサー17の先端部と接する部分には盲板18を張設している。
【0016】
次に、図2〜図4に基づき、スクリュー軸7,14について詳述する。スクリュー軸7の終端部には側板19を固着しており、側板19には駆動軸20が螺着されている。該駆動軸20を回転させることにより、スクリュー軸7も回転するようになっている。この際、スクリュー軸14は回転せず固定状態であり、摺動部材21,22によって側板19と駆動軸20に摺接している。前記駆動軸20は中空形状をしており、駆動軸20の外周部にはスクリーン15を洗浄するための洗浄ノズル23を、スクリーン15の内周面に対設するように等ピッチに複数配設している。スクリュー軸7、14の外周面にはスクリュー軸7の始端部からスクリュー軸14の後端部まで、同一ピッチのスクリュー羽根6を連続して巻き掛けており、スクリュー軸7部のスクリュー羽根6はスクリュー軸7に溶接している。スクリュー軸14部のスクリュー羽根6はスクリーン15面とわずかな間隙を設けており、スクリュー羽根6だけが、スクリュー軸7と一体で回転するようになっている。そして、スクリュー羽根6は外筒4に張設しているスクリーン5の内面ともわずかな間隙を設けており、スクリュー羽根6とスクリーン5,15との接触による磨耗を防ぐようにしている。
【0017】
スクリュー羽根6にはスクリーン5,15の目詰まりを防止するために、図5に示すスクレーパー13a、13bを配設している。スクレーパー13aはスクリーン5の内面に押圧するように、スクリュー羽根6の外周面部に始端から終端に渡って連続して配設している。スクレーパー13aは一連の帯状に構成しており、スクリュー羽根6の外周部に押え板24で挟み込んで等ピッチでボルト25とナット26で固定されている。押え板24もスクレーパー13aと同様に、スクリュー羽根6の始端から終端に渡って連続した一連の帯状に構成している。そして、スクレーパー13bはスクリュー軸14のスクリーン15の外面に押圧するように、スクリュー羽根6の内周面部に連続して配設している。スクレーパー13bは前記スクレーパー13aと同様に、スクリュー羽根6の内周部に押え板27で挟み込んで等ピッチでボルト25とナット26で固定している。押え板27も連続した一連の帯状に構成している。尚、スクレーパー13a、13bはゴム、樹脂等の弾性材を用いており、ボルト25の貫通部は長孔にしているので、スクリーン5,15との摺接による磨耗のため、押圧力が弱くなった場合には、押圧力の調節が容易にできるようにしている。
【0018】
ろ過・脱水運転終了後やスクリーン5,15に目詰まりが発生した場合には、濃縮ゾーンAとろ過・脱水ゾーンBに分割された外筒4をクラッチ9により一体に連結し、該外筒4を回転しながら、洗浄管28から洗浄水を外筒4のスクリーン5外面に向けて噴射するとともに、中空の駆動軸20の始端部に接続した洗浄水供給口29からも洗浄水を供給して、駆動軸20を回転させながら洗浄ノズル23から洗浄水をスクリーン15の内面に向けて噴射することにより、スクリーン5,15の再生が行える。スクリュー軸14内に落水した洗浄排水やろ液は排水管30から排水トラフ31に排水される。尚、スクリーン5の洗浄排水やろ過運転中のろ液も上記排水トラフ31に集水され、排水口32より機外に排出されるものである。
【0019】
【発明の効果】
本発明のスクリュープレスは上述のように構成してあり、濃縮ゾーンの外筒をスクリュー軸とは逆回転させることにより、濃縮ゾーンのスクリュー羽根の回転数が相対的に多くなり、スクリュー羽根の外周部に配設したスクレーパーによって、外筒のスクリーン面に堆積して目詰まりを起こそうとするケーキ層や高分子凝集剤による薄膜を掻取って、ろ過面を再生するので、固形物濃度が低く水負荷の大きい汚泥でも効率良く濃縮・脱水が行える。そして、スクリュー軸を後端部で分割し、後端部のスクリュー軸の外周面にスクリーンを張設し、このスクリーンに対面するスクリュー羽根の内周部にはスクレーパーを配設して、このスクリーン面を再生するようにしているので、脱水ケーキへの加圧力が高くなる後端部において、脱水ケーキの内外面から両面ろ過を行い、効率良くろ液の排出が行え、低含水率の脱水ケーキを取出すことができ、汚泥の処理量も増大できるものである。
【図面の簡単な説明】
【図1】本発明に係るスクリュープレスの一部縦断側面図である。
【図2】本発明に係るスクリュープレスの要部の縦断側面図である。
【図3】同じく、スクリーンを張設したスクリュー軸の概略斜面図である。
【図4】同じく、スクリーンを張設したスクリュー軸の他の実施例の概略斜面図である。
【図5】同じく、スクリュー羽根に取付けたスクレーパーの一部縦断側面図である。
【符号の説明】
1 スクリュープレス
4、4a、4b 外筒
5、15 スクリーン
6 スクリュー羽根
7、14 スクリュー軸
9 クラッチ
13a、13b スクレーパー
20 駆動軸
23 洗浄ノズル
A 濃縮ゾーン
B ろ過・脱水ゾーン
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a screw press that performs filtration and dewatering while rotating an outer cylinder of a concentration zone, and more specifically, an improvement of a screw press that can perform concentration and dewatering while preventing clogging of a screen even with low-concentration sludge, thereby improving dewatering efficiency. It is about.
[0002]
[Prior art]
Conventionally, when organic sludge such as sewage and human waste is dehydrated with a screw press, a polymer flocculant is added to the sludge and agitated to generate floc, and this coagulated sludge is supplied to the screw press for dehydration. It is carried out. However, with sludge having a low solids concentration, it has been difficult to efficiently drain a large amount of separated liquid at the front stage of the outer cylinder screen at high speed. In particular, in the former stage, a thin film of a polymer flocculant is generated on the inner surface of the screen, and the drainage is hindered, so that residues are attached and clogging is likely to occur. For this reason, after concentrating low concentration sludge with concentrators, such as a centrifugal concentrator and a flotation | concentration concentrator, the method of filtering and dewatering a concentrated sludge with a screw press is taken. However, the use of a concentrator and a screw press has a problem in that the installation area is large and the driving power cost is high. In addition, there is a problem that maintenance is also required.
[0003]
In order to solve the above problems, the outer half screen of the outer cylinder screen is configured as a concentrating zone, and the latter half is configured as a filtration / dehydration zone. Thus, screw presses having a concentration function are known. However, even in a screw press having the above-mentioned concentration function, in sludge with a low solid matter concentration, a thin film made of a polymer flocculant is generated on the inner surface of the screen in the concentration part in front of the outer cylinder screen, and the drainage performance is inhibited As a result, residue adheres and clogging occurs, and it is difficult to efficiently drain a large amount of separation liquid at high speed.
[0004]
[Patent Document 1]
Japanese Patent Publication No. 3-78123 [Patent Document 2]
JP-A 64-2920
[Problems to be solved by the invention]
In order to solve the above-mentioned problems of the prior art, Patent Document 1 discloses a method for preventing clogging of the outer cylinder screen by continuously injecting cleaning water while rotating the outer cylinder screen. However, in the method in Patent Document 1, the sprayed washing water penetrates through the small hole of the screen and enters the outer cylinder, the concentrated sludge is diluted, and the concentration effect may be reduced by half. May affect the dewatering efficiency and water content of the cake.
[0006]
In Patent Document 2, as a method of preventing clogging of the outer cylinder screen, a high-pressure squeezing is performed by configuring the screen with a wedge wire having a substantially triangular cross section and a narrow inner peripheral surface side and a wide outer peripheral surface side slit. There is a description that impurities entering the slit can be prevented from being clogged because they gradually escape to the outside. Further, in Patent Document 2, there is a description in which the rear end portion of the screw shaft is formed in a cylindrical shape with a screen stretched on the outer peripheral surface, so that a dehydrating efficiency is improved as a filtering portion.
[0007]
However, in Patent Document 2, when low-concentration sludge aggregated by the polymer flocculant is supplied to the front stage, it is difficult to drain a large amount of filtrate from a narrow slit at a high speed. A thin film made of a polymer flocculant is formed on the inner surface of the tube screen and the outer surface of the screw shaft, which may deteriorate the drainage and reduce the dewatering efficiency. And, in order to discharge the filtrate flowing into the inside from the screen surface of the screw shaft, it is sucked by a vacuum pump, and there is a problem that a highly accurate seal structure is required and running costs such as power costs increase. .
[0008]
[Means for Solving the Problems]
The present invention solves the above-mentioned problems in the prior art, and the gist of the invention is to divide an outer cylinder with a screen stretched into a rotatable concentration zone in the first half and a filtration / dehydration zone in the second half. Then, a screw shaft around which screw blades are wound is provided in the divided outer cylinder, and the slurry supplied to the starting end of the outer cylinder in the concentration zone is filtered and dehydrated while rotating the screw shaft. In a screw press that separates the filtrate from the screen of the outer cylinder and takes out the cake from the end of the outer cylinder of the filtration / dehydration zone, the screw shaft is divided in the front-rear direction at the rear end, and the screw at the rear end A screen is stretched on the shaft, and a scraper is disposed on the outer peripheral portion of the screw blade from the start end to the rear end, and the screw shaft scraper is also provided on the inner peripheral portion of the screw blade. A scraper is arranged opposite to the lean surface, and this scraper is elastically slidably contacted with the inner peripheral surface of the outer cylinder and the screen surface of the screw shaft, and filtration and dehydration are performed while rotating the screw shaft. A screw press in which a clutch is disposed in a division part of the outer cylinder so that the concentration zone and the filtration / dehydration zone can be freely connected and disconnected.
[0009]
Then, the rear end portion of the divided screw shaft screen is fixed and the other end portion is rotatable, or a wedge wire is used as a screen stretched on the screw shaft, and the slit side of the wedge wire is filtered. The surface. Further, the drive shaft for driving the screw shaft is hollow, and a plurality of cleaning nozzles are disposed on the outer peripheral portion of the drive shaft at a position facing the inner peripheral surface of the screen of the screw shaft so as to clean the screen. It is a screw press.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
The screw press according to the present invention is configured as described above, and a polymer flocculant is added to and stirred in organic sludge such as sewage and human waste, and the sludge that has generated flocs flocs is pumped to the screw press supply port. Then, the sludge flows into the supply path of the screw shaft on the outer cylinder start end side and is supplied between the screw blades in the concentration zone through the supply hole opened in the screw shaft, so that the aggregate floc is affected by the screw blades. It flows into the start end of the outer cylinder without being destroyed.
[0011]
The sludge supplied to the concentration zone is concentrated by being discharged from the screen of the outer cylinder while being transferred by the rotating screw blades. By rotating the outer cylinder of the concentrating zone in the direction opposite to the screw shaft, the number of rotations of the screw blade is relatively increased, and the number of sliding contacts between the scraper and the screen disposed at the tip of the screw blade is reduced. A large amount of the filtrate can be discharged by scraping the cake layer and the thin film of the polymer flocculant, which are increased and deposited on the screen, to regenerate the filtration surface to be clogged. And since sludge is transferred with screw blades while preventing clogging of the screen with a scraper, it is possible to efficiently concentrate even sludge with a low solids concentration and a large water load.
[0012]
Next, the sludge concentrated in the concentration zone is transferred to the filtration / dehydration zone and filtered / dehydrated by the screw blades in the latter half. At this time, the outer cylinder of the concentration zone and the outer cylinder of the filtration / dehydration zone are formed into a continuous cylindrical shape, and the diameter of the screw shaft is increased in a tapered shape from the start end to the rear end in the outer cylinder. Since the gap between the outer cylinder and the screw shaft is relatively reduced toward the rear end side, the volume between the screw blades is gradually reduced, and the pressure applied to the sludge is increased. The dehydrated cake can be taken out from the discharge port at the end. Furthermore, the rear end of the screw shaft is formed in a cylindrical shape, and a screen is stretched around the outer peripheral surface to form a filtration surface. A scraper is disposed on the screw blade that contacts the screen surface. While preventing clogging, both sides can be filtered with a screen of an outer cylinder and a screw shaft, and a dehydrated cake with a low water content can be obtained, and the amount of sludge treated is also increased. Embodiments of a screw press according to the present invention will be described in detail below with reference to the drawings.
[0013]
【Example】
FIG. 1 is a longitudinal side view of a screw press according to the present invention, in which a screw press 1 is supported by front and rear frames 2 and 3, and a circumference of an outer cylinder 4 divided into a concentration zone A and a filtration / dehydration zone B. A screen 5 is stretched on the part, and the diameter of the outer cylinder 4 is increased in a tapered manner from the start end to the rear end, and a screw shaft 7 having screw blades 6 wound around the outer peripheral surface is attached to the frame 2. , 3. The screw shaft 7 is freely rotatable by a driving machine 8. The outer cylinder 4 divided into the concentration zone A and the filtration / dehydration zone B can be connected and disengaged by a clutch 9 disposed in the division part. During normal concentration, filtration / dehydration operation, the outer cylinder 4 is in a dissociated state, and only the outer cylinder 4a of the concentration zone A is rotated by the drive unit 10 and is outside the filtration / dehydration zone B. The cylinder 4b is in a fixed state. The rotating direction of the outer cylinder 4a is rotated in the direction opposite to the rotating direction of the screw shaft 7 described later.
[0014]
The sludge aggregated by the polymer flocculant is supplied from the supply port 11 opened at the tip of the screw shaft 7, and from the supply hole 12 opened at the outer peripheral surface of the screw shaft 7, the concentration zone A of the outer cylinder 4 Let it flow into the beginning. The infiltrated coagulated sludge is separated and discharged from the screen 5 of the outer cylinder 4 while being transferred by the screw blade 6 and concentrated. By rotating the outer cylinder 4a of the concentration zone A in the first half in the reverse direction to the screw shaft 7, the number of sliding contacts between the scraper 13a (described later) disposed at the tip of the screw blade 6 and the screen 5 increases. Then, the cake layer deposited on the inner peripheral surface of the screen 5 or a thin film made of the polymer flocculant is scraped to regenerate the screen 5 surface, so that clogging can be prevented and the filtrate can be discharged continuously. Since the screen 5 is composed of a punching plate having a large aperture ratio (approximately 20 to 40%), a large amount of filtrate can be discharged, and even sludge with a low solids concentration and a large water load can be efficiently used. It can be concentrated. The sludge concentrated in the concentration zone A is transferred to the filtration / dehydration zone B by the screw blade 6, and further moves to the rear end while discharging the filtrate from the screen 5 and depressurizing / dehydrating. The screw shaft 7 is divided at the rear end portion, the screw shaft 14 at the rear end portion is formed in a cylindrical shape, and a screen 15 is stretched around the outer peripheral surface to form a filtration surface.
[0015]
Based on FIG. 2, the screw shaft 14 at the rear end will be described. On the outer peripheral surface of the screw shaft 14 formed in a cylindrical shape, a screen 15 made of a wedge wire composed of a large number of members each having a substantially triangular cross section is stretched. Since C is formed and dehydration is performed from the inner and outer surfaces in the double-sided filtration zone C, a dehydrated cake having a lower water content can be taken out from the discharge port 16. A presser 17 is provided opposite to the discharge port 16 so that the opening amount of the discharge port 16 is adjusted while applying back pressure to the dehydrated cake. As shown in FIG. 5, the wedge wire is stretched so that the slit side becomes an outer peripheral surface, and the slit is parallel to or orthogonal to the axis of the screw shaft 14 as shown in FIGS. 3 and 4. Either is acceptable. A blind plate 18 is stretched at the end of the screw shaft 14 in contact with the tip of the presser 17.
[0016]
Next, the screw shafts 7 and 14 will be described in detail with reference to FIGS. A side plate 19 is fixed to an end portion of the screw shaft 7, and a drive shaft 20 is screwed to the side plate 19. By rotating the drive shaft 20, the screw shaft 7 is also rotated. At this time, the screw shaft 14 does not rotate and is in a fixed state, and is in sliding contact with the side plate 19 and the drive shaft 20 by the sliding members 21 and 22. The drive shaft 20 has a hollow shape, and a plurality of cleaning nozzles 23 for cleaning the screen 15 are arranged at equal pitches on the outer peripheral portion of the drive shaft 20 so as to face the inner peripheral surface of the screen 15. is doing. The screw blades 6 having the same pitch are continuously wound around the outer peripheral surfaces of the screw shafts 7 and 14 from the start end portion of the screw shaft 7 to the rear end portion of the screw shaft 14. It is welded to the screw shaft 7. The screw blade 6 of the screw shaft 14 part has a slight gap with the screen 15 surface, and only the screw blade 6 rotates integrally with the screw shaft 7. The screw blade 6 is also provided with a slight gap on the inner surface of the screen 5 stretched on the outer cylinder 4 so as to prevent wear due to contact between the screw blade 6 and the screens 5 and 15.
[0017]
The screw blades 6 are provided with scrapers 13a and 13b shown in FIG. 5 in order to prevent the screens 5 and 15 from being clogged. The scraper 13 a is continuously disposed on the outer peripheral surface portion of the screw blade 6 from the start end to the end so as to press against the inner surface of the screen 5. The scraper 13a is formed in a series of strips, and is sandwiched between the outer periphery of the screw blade 6 by a presser plate 24 and fixed by bolts 25 and nuts 26 at an equal pitch. Similarly to the scraper 13a, the presser plate 24 is configured in a series of strips continuous from the start end to the end of the screw blade 6. And the scraper 13b is continuously arrange | positioned by the internal peripheral surface part of the screw blade | wing 6 so that the outer surface of the screen 15 of the screw shaft 14 may be pressed. Similar to the scraper 13a, the scraper 13b is sandwiched between the inner peripheral portions of the screw blades 6 by a pressing plate 27 and fixed with bolts 25 and nuts 26 at an equal pitch. The holding plate 27 is also formed in a continuous series of strips. The scrapers 13a and 13b are made of an elastic material such as rubber or resin, and the penetrating portion of the bolt 25 is a long hole, so that the pressing force is weakened due to wear due to sliding contact with the screens 5 and 15. In this case, the pressing force can be easily adjusted.
[0018]
After the filtration / dehydration operation is completed or when the screens 5 and 15 are clogged, the outer cylinder 4 divided into the concentration zone A and the filtration / dehydration zone B is integrally connected by the clutch 9, and the outer cylinder 4 The cleaning water is sprayed from the cleaning tube 28 toward the outer surface of the screen 5 of the outer cylinder 4 and the cleaning water is also supplied from the cleaning water supply port 29 connected to the starting end of the hollow drive shaft 20. The screens 5 and 15 can be regenerated by spraying cleaning water from the cleaning nozzle 23 toward the inner surface of the screen 15 while rotating the drive shaft 20. The washing waste water and filtrate that have fallen into the screw shaft 14 are drained from the drain pipe 30 to the drain trough 31. Incidentally, the washing drainage of the screen 5 and the filtrate during the filtration operation are also collected in the drainage trough 31 and discharged from the drainage port 32 to the outside of the apparatus.
[0019]
【The invention's effect】
The screw press of the present invention is configured as described above, and by rotating the outer cylinder of the concentration zone in the direction opposite to the screw shaft, the rotation speed of the screw blades in the concentration zone is relatively increased, and the outer periphery of the screw blades The scraper placed in the section scrapes off the cake layer that accumulates on the screen surface of the outer cylinder and causes clogging and thins the polymer flocculant to regenerate the filtration surface. Efficient concentration and dewatering can be achieved even with sludge with a large water load. Then, the screw shaft is divided at the rear end portion, a screen is stretched on the outer peripheral surface of the screw shaft at the rear end portion, and a scraper is disposed on the inner peripheral portion of the screw blade facing the screen. Since the surface is regenerated, both sides of the dehydrated cake are filtered from the inner and outer surfaces of the dehydrated cake at the rear end where the pressure applied to the dehydrated cake is high, and the filtrate can be discharged efficiently, and the dehydrated cake has a low water content. The amount of sludge can be increased.
[Brief description of the drawings]
FIG. 1 is a partially longitudinal side view of a screw press according to the present invention.
FIG. 2 is a longitudinal side view of a main part of a screw press according to the present invention.
FIG. 3 is a schematic oblique view of a screw shaft with a screen stretched in the same manner.
FIG. 4 is a schematic perspective view of another embodiment of a screw shaft with a screen stretched thereon.
FIG. 5 is a partially longitudinal side view of a scraper attached to a screw blade.
[Explanation of symbols]
1 Screw press 4, 4a, 4b Outer cylinder 5, 15 Screen 6 Screw blade 7, 14 Screw shaft 9 Clutch 13a, 13b Scraper 20 Drive shaft 23 Cleaning nozzle A Concentration zone B Filtration / dehydration zone

Claims (5)

スクリーン(5)を張設した外筒(4)を前半部の回転自在な濃縮ゾーン(A)と後半部のろ過・脱水ゾーン(B)に分割して、この分割した外筒(4)内にスクリュー羽根(6)を巻き掛けたテーパー状のスクリュー軸(7)を内設し、前記濃縮ゾーン(A)の外筒(4a)の始端部に供給したスラリーをスクリュー軸(7)を回転させながら、ろ過・脱水を行ない、スクリーン(5)からろ液を分離して、ろ過・脱水ゾーン(B)の外筒(4b)の終端部からケーキを取出すスクリュープレス(1)において、上記スクリュー軸(7)を後端部で分割し、この後端部のスクリュー軸(14)を円筒状に形成し、外周面にスクリーン(15)を張設し、前記スクリュー羽根(6)の外周部に始端から終端に渡ってスクレーパー(13a)を配設するとともに、スクリュー羽根(6)の内周部にも前記スクリュー軸(14)のスクリーン(15)面に対設してスクレーパー(13b)を配設し、このスクレーパー(13a、13b)を外筒(4)の内周面及びスクリュー軸(14)のスクリーン(15)面に弾圧的に摺接させて、スクリュー軸(7)を回転させながらろ過・脱水を行うことを特徴とするスクリュープレス。The outer cylinder (4) with the screen (5) stretched is divided into a rotatable concentration zone (A) in the first half and a filtration / dehydration zone (B) in the second half, and the inside of the divided outer cylinder (4) A taper-shaped screw shaft (7) around which a screw blade (6) is wound is installed, and slurry supplied to the start end of the outer cylinder (4a) of the concentration zone (A) is rotated by the screw shaft (7). In the screw press (1) that performs filtration and dehydration, separates the filtrate from the screen (5), and takes out the cake from the end of the outer cylinder (4b) of the filtration and dehydration zone (B), The shaft (7) is divided at the rear end portion, the screw shaft (14) at the rear end portion is formed in a cylindrical shape, a screen (15) is stretched on the outer peripheral surface, and the outer peripheral portion of the screw blade (6) Scraper (13a) from start to end In addition, a scraper (13b) is disposed on the inner peripheral portion of the screw blade (6) so as to face the screen (15) surface of the screw shaft (14), and the scraper (13a, 13b) is removed. A screw press characterized by elastically slidingly contacting the inner peripheral surface of the cylinder (4) and the screen (15) surface of the screw shaft (14), and performing filtration and dehydration while rotating the screw shaft (7). . 上記スクリュー軸(7)を回転自在とし、後端部のスクリュー軸(14)を固定としたことを特徴とする請求項1に記載のスクリュープレス。The screw press according to claim 1, wherein the screw shaft (7) is rotatable and the screw shaft (14) at the rear end portion is fixed. 上記スクリュー軸(14)に張設したスクリーン(15)としてウエッジワイヤーを用い、該ウエッジワイヤーのスリット側をろ過面としたことを特徴とする請求項1又は請求項2に記載のスクリュープレス。The screw press according to claim 1 or 2, wherein a wedge wire is used as the screen (15) stretched around the screw shaft (14), and the slit side of the wedge wire is used as a filtration surface. 上記スクリュー軸(7)を駆動させる駆動軸(20)を中空とし、この駆動軸(20)の外周部にスクリュー軸(14)のスクリーン(15)の内周面に対設する位置に複数の洗浄ノズル(23)を配設し、前記スクリーン(15)を洗浄するようにしたことを特徴とする請求項1乃至請求項3の何れか1項に記載のスクリュープレス。The drive shaft (20) for driving the screw shaft (7) is hollow, and a plurality of positions are provided on the outer peripheral portion of the drive shaft (20) so as to face the inner peripheral surface of the screen (15) of the screw shaft (14). The screw press according to any one of claims 1 to 3, wherein a cleaning nozzle (23) is provided to clean the screen (15). 上記外筒(4)の分割部にクラッチ(9)を配設し、濃縮ゾーン(A)とろ過・脱水ゾーン(B)とを連結解離自在としたことを特徴とする請求項1乃至請求項4の何れか1項に記載のスクリュープレス。The clutch (9) is arranged in the division part of the outer cylinder (4), and the concentration zone (A) and the filtration / dehydration zone (B) are connected and disengaged freely. The screw press according to any one of 4.
JP2003163238A 2003-06-09 2003-06-09 Screw press Expired - Fee Related JP4081759B2 (en)

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JP4493031B2 (en) * 2005-10-12 2010-06-30 月島機械株式会社 Filtration device
JP5048726B2 (en) * 2009-07-17 2012-10-17 株式会社日立プラントテクノロジー Sediment separation dehydrator
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KR20160143520A (en) * 2015-06-05 2016-12-14 (주)에이알케이 Sludge dehydrator equipped with main-axis screw conveyer section and non-axis screw conveyer section
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