JP3772598B2 - Filter press - Google Patents

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JP3772598B2
JP3772598B2 JP21844699A JP21844699A JP3772598B2 JP 3772598 B2 JP3772598 B2 JP 3772598B2 JP 21844699 A JP21844699 A JP 21844699A JP 21844699 A JP21844699 A JP 21844699A JP 3772598 B2 JP3772598 B2 JP 3772598B2
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Prior art keywords
filter
filter press
filtration chamber
plate
press according
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JP21844699A
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Japanese (ja)
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JP2001058107A (en
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栄一 石垣
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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、無機質や繊維質を多く含有する汚泥の圧搾脱水装置に関し、特に、ケーキ洗浄も可能とする間歇型のフイルタープレスに関する。
【0002】
【従来の技術】
従来、間歇型の圧搾脱水機として、ろ過室を形成する前後のろ板間に一対のろ布を配設し、このろ布間に原液を圧入して圧搾脱水し、ろ板間を解放してケーキをろ板下方に排出するフイルタープレスがあり、例えば、実公平7−21204号公報に記載してあるように公知である。また、ろ過室内にドーナツ状のろ過板と回転自在な撹拌板を狭い間隔で交互に配列し、ろ過室に圧入した汚泥をろ過板の間隙を縫って移動させながら、撹拌板の前後のろ過板から分離液を排出し、掃流ろ過を行いながら、ろ過脱水したケーキを連続的に他端から取出すようにしたロータリーフイルタープレスも、例えば、特開平10−165721号公報に記載してあるようによく知られている。
【0003】
【発明が解決しようとする課題】
しかしながら、上記従来のフイルタープレスは大容量処理と高圧搾脱水が可能であるが、多数並列したろ板を開閉させるために複雑な構造の装置となり、広い設置スペースが必要であった。そして、消耗品であるろ布を定期的に交換する必要があり、また、目詰まりしたろ布の再生のために多量の洗浄水が必要であった。また、この従来のロータリーフイルタープレスは、原液を撹拌することによりろ過板の目詰まりが防止され、連続的にケーキが得られるものであるが、撹拌板を比較的高速で回転させるので、撹拌された有機物がコロイド状となり、ろ過板からコロイド状の汚泥がろ液と一緒に流出する恐れがあり、ケーキの含水率も比較的に高かった。この発明は、前述の従来の問題点に鑑みてなされたもので、その目的は、ろ過室に圧入した汚泥を、ろ過室と共に移動させながら両面ろ過を行い、ろ過面に積層するケーキと汚泥の接触面で発生するズリ抵抗をろ過力として、低含水率のケーキを回収する圧搾脱水装置を提供するものである。
【0004】
【課題を解決するための手段】
この発明の要旨は、回転自在な駆動軸に配設した2枚の円盤状のろ過板と、ろ過板の外周部に摺接させた外周環とでろ過室を形成し、ろ過室の下方部の外周環に逆止板を止着して、この逆止板の側縁をろ過板に近接させ、その先端部を駆動軸に摺設させると共に、逆止板で規制するろ過室の始端側に汚泥の供給口と、その終端側にケーキの取出口を開口し、この取出口に開閉弁を設けたもので、ろ過室に圧入した汚泥は、両面ろ過を行いながら濃縮汚泥を移動させ、ろ材の接触面とのズリ抵抗で汚泥を脱水し、開閉弁を閉塞して脱水したケーキに背圧を加えながら圧搾脱水を行うものである。
【0005】
そして、上記ろ過室の汚泥の供給口に連結した汚泥供給管に切替自在に洗浄水管と圧縮空気管を連結して、脱水ケーキのケーキ洗浄と、洗浄したケーキのフィードブローを行うようにしたものである。また、上記逆止板に配設した洗浄水供給管の噴射口をろ過板に対設して、必要時にろ過室の内側からろ過板を洗浄し、ろ過面を再生するようにしたものである。上記取出口側の逆止板は、ろ過板に近接させた側縁部と、駆動軸に摺設させた先端部を切刃状に突出させて、ケーキをろ過室の壁面から剥離させるものである。また、上記取出口側の逆止板の壁面を放物線状に湾曲させておけば、逆止板が圧搾脱水されたケーキの排出の抵抗とならないものである。なお、供給口を設けたろ過室の始端部に、ろ過板の外周面に対設して洗浄管を配設しておけば、ろ板を洗浄することができるものである。
【0006】
そして、上記ろ過板は多数の微細孔を有する円盤状のメタルスクリーンと、このメタルスクリーンを嵌入した格子状のリブを接合一体化した外環支持枠とからなり、2枚の円盤状のろ過板がボス状の内環支持体に連結され、この内環支持体が回転自在な駆動軸に嵌着されて、ろ材の取付けが容易となり、強度も増加されるものである。なお、上記ろ過板の内環支持体にメタルスクリーンを張設すれば、ろ過面積が増加されるものである。また、上記開閉弁は、ケーキの取出口の回動軸に止着したダンパーと、ダンパーの回動軸に連結した回動レバーと、回動レバーに枢着したシリンダーとから構成されており、外周環の取出口からダンパーの開口度を調節し、ろ過のための背圧を加えながら圧搾脱水して取出口から均一な含水率のケーキを排出することができる。なお、上記ろ過室を駆動軸に複数並列し、この複数のろ過室を軸支した駆動軸の両端部をフレームに支架させて、駆動軸を駆動機に連動連結すれば、並列多室構成となり、汚泥の大容量処理が可能となり、両面ろ過のろ過室が生かされて、占有スペースも小さくなるものである。
【0007】
【発明の実施の形態】
この発明に係る装置は上記のように構成してあり、ケーキ取出口の開閉弁を閉塞し、ろ過室を微速回転させながら供給口から汚泥を圧入すると、圧入直後の供給口の近傍の濃縮ゾーンでは、主に圧入圧力でろ過板の両面からろ液が分離されて汚泥は濃縮される。汚泥は濃縮されながらろ過室の回転とともに脱水ゾーンに移送され、ろ過室の回転によりろ材の接触面との摩擦抵抗で汚泥が脱水され、ろ過板のろ過面にケーキ層が徐々に形成される。やがて、汚泥は流動性を失いろ過面のケーキ層と中心部の比較的柔らかい汚泥との間にせん断摩擦抵抗力が発生し脱水が促進される。圧搾ゾーンに移送されたケーキに、取出口からケーキに背圧を加えながらさらに脱水が行なわれる。そして、ろ過室に脱水されたケーキが充満してくると、ろ過室への汚泥の供給を中止し、引続きろ過板を回転させながら、ろ過室の汚泥の供給口に洗浄水管を連結し、脱水ケーキに洗浄水を圧入してケーキに含有する有効成分、或いは不用な成分を洗浄して分離する。ケーキ洗浄後、汚泥の供給口の洗浄水管を切替えて、圧縮空気管を連結し、洗浄した脱水ケーキに圧縮空気を吹込み、ケーキのフイート゛ブローを行って水分を排出するものである。次に、開閉弁を開放すれば、ろ過板の回転によるろ材の接触面との摩擦抵抗でケーキを取出口から排出することができる。ケーキの排出終了時に、ろ過板に付着した汚泥を両面から洗浄清掃して、運転再開に備えることができるものである。
【0008】
【実施例】
この発明に係るフイルタープレスを図面に基づき詳述すると、まず、図1において、符号1はフイルタープレスであって、両側のフレーム2、2に支架された架台3に軸受4が固定され、この軸受4に軸支された駆動軸5が、駆動機6で回転させるようにしてある。そして、フイルタープレス1の下部には、汚泥供給管7に連結された供給口8と、ケーキの取出口9とが設けてある。フイルタープレス1の構造を図2及び図3に基づき詳述すると、駆動軸5に内環支持体10が嵌着してあり、この内環支持体10に2枚の円盤状のろ過板11、11の内周縁が止着してある。このろ過板11が駆動軸5とともにゆっくりと回転させるようにしてある。ろ過板11の周部には外周環12が配設してあり、2枚のろ過板11、11と外周環12でその内部にろ過室13が形成されている。ろ過板11の周面には、ろ過板11を覆うカバー14が設けてあり、このカバー14の外周端が外周環12に止着されている。そして、カバー14の内周縁が軸受4で駆動軸5に軸支されて、ろ過室13の外周部にろ液室15を形成してある。なお、カバー14の背面が架台3に固定され、外周環12がろ過板11と一緒に供回りしないようになっている。符号16はろ液の排液管である。
【0009】
ろ過室13の汚泥の供給口8とケーキの取出口9の間には、図2に示すように、ろ過室13を分断する逆止板17が設けてあり、ろ過板11を回転させて(矢印イ方向)、ろ過室13の供給口8から供給された汚泥は圧入初期には濃縮ゾーンAで、主に圧入圧で固液分離され、濃縮された汚泥は脱水ゾーンBで、ろ過室13の回転によりろ材の接触面とのズリ抵抗と、ろ過面のケーキ層と中心部の比較的柔らかい汚泥との間のせん断摩擦抵抗力により脱水促進させる。そして、ろ過室13はさらに回転してケーキの取出口9近傍の圧搾ゾーンCに移送するようにしてある。上記汚泥の供給口8に連結した汚泥供給管7には図4に示すように、電磁弁V1が介装してあり、電磁弁V1の後方の汚泥供給管7から分岐させて洗浄水管18と圧縮空気管19が連結してある。洗浄水管18と圧縮空気管19には電磁弁V2、V3が介装してあり、それぞれの電磁弁V1、V2、V3の開閉を切替えてろ過室13への汚泥供給と、ケーキ中に含まれる有効成分または不用な成分を分離するためのケーキ洗浄、及びケーキ洗浄をおこなったケーキに圧縮空気を吹込んで水分を排出させるフイードブローが行えるようにしてある。
【0010】
また、逆止板17には、図4に示すように、ろ過室13の内側からろ過板11に対向する目詰まり解消用の洗浄水供給管20が設けてあり、洗浄水供給管20の噴射口21が回転しているろ過板11に高圧水を噴射するようにしてある。また、供給口8を設けたろ過室13の始端部には、図3及び図4に示すように、ろ過板11の外周面に対向して洗浄水供給管22を配設してあり、洗浄水供給管22の噴射口23から圧力水を噴射して、ろ過板に付着した汚泥を外面から洗浄清掃できるようにしてあり、ろ過板11の両面洗浄ができるようにしてある。そして、取出口9側の逆止板17は、図5に示すように、ろ過板11に近接させた側縁部17aと、駆動軸5に摺設させた先端部17bが切刃状に突出させてあり、ろ過室13から取出口9に排出するケーキをろ過室13から剥離させるようにしてある。なお、ろ過室13の取出口9に対向する逆止板17の壁面を図2及び図4に示すように、放物線状に湾曲させておけば、ケーキがろ過板11の回転接線方向に案内されて、逆止板17が圧搾脱水されたケーキの排出の抵抗とならないものである。
【0011】
ろ過室13のケーキの取出口9には、図2及び図3に示すように開閉弁24が設けてあり、開閉弁24は、取出口9の一端に軸支した回動軸25に連結したダンパー26と、ダンパー26の回動軸25に連結した回動レバー27と、回動レバー27に枢着したシリンダー28とからなっており、シリンダー28のピストン29を伸縮させて、ケーキの取出口9を開閉するようにしてあり、ピストン29を伸長させて、ダンパー26を回動して取出口9を閉塞させて圧搾ゾーンCに背圧を加えるようにしてある。そして、先ず取出口9を閉塞し、原液をろ過室13の供給口8から連続的に供給しながら、汚泥を濃縮し、圧搾脱水した後、原液の供給を停止してろ過室13の取出口9を解放し、引き続きろ過室13を回転させながらケーキを取出すようにしてある。
【0012】
上記ろ過板11は、図6及び図7に示すように、ウエッジワイヤー30aと裏面に貼着したサポートロッド30bとから構成されたドーナツ状のメタルスクリーン30が、格子状のリブ31aを接合一体化した外環支持枠31に嵌入してあり、容易にろ材交換が行えるようにしてある。なお、ろ過室13の内周縁を止着した内環支持体10にもメタルスクリーン32を張設すれば、ろ過面積が増加するものであり、汚泥の脱水性も良くなるものである。そして、ろ過室13から分離したろ液をろ液室15に排水できるように複数の排水路33…が穿設してある。図8に示す連続圧搾脱水装置は、上記のフイルタープレスを複数台並列した他の実施例であって、各ろ過室13…を形成するろ過板11を駆動軸5aに連結して多室構成としてある。また、前後のろ過室13を支持筒34で連結して、前端部と後端部の支持筒34a、34aをフレーム2a、2aで支架させ、駆動軸5aに嵌着したプーリー35を駆動機6aに連動連結して、複数のろ過板を回転させるようにしてある。なお、符号15aはろ過板11からろ液を分離するろ液室である。このように、並列多室構成とすれば、汚泥の大容量処理が可能となり、占有スペースも小さくなるものである。
【0013】
【発明の効果】
以上の説明で明らかなように、この発明に係るフイルタープレスは、ろ過室に圧入した汚泥を、2枚のろ過板と汚泥をゆっくりと供回りさせながら両面ろ過を行うので、ろ過板と汚泥との間に発生する摩擦抵抗と、ろ過面に積層するケーキと中心部の比較的柔らかい汚泥との間にせん断摩擦抵抗力を発生させ、汚泥を濃縮脱水するものである。即ち、従来のフイルタープレスにあっては、複雑なろ板開閉装置と広い設置スペースが必要であり、ロータリーフイルタープレスにあっては、撹拌板を高速回転させるために、ろ過板からコロイド状の汚泥がろ液と一緒に流出する恐れがあつたものであるが、この発明にあっては、ろ過板と汚泥の摩擦抵抗を発生させて脱水したケーキに、引続きろ過室を回転させながら、ろ過室に高圧水と圧縮空気を供給するので、ケーキに含まれる成分が分離され、洗浄されたケーキの水分が分離できるものである。そして、逆止板とろ過室の汚泥の供給側にろ過板の洗浄水配管を設けたので、ろ過板の再生が可能となるものである。
【図面の簡単な説明】
【図1】この発明に係るフイルタープレスの概略正面図である。
【図2】この発明に係るろ過室の構造を示す概略縦断正面図である。
【図3】この発明に係るろ過室を図1のA−A線に沿って切断した縦断側面図である。
【図4】この発明に係るろ過室に圧力水と圧縮空気を供給するための配管類を示す概念図である。
【図5】ろ過室の圧搾ゾーンから見た逆止板の正面図である。
【図6】ウエッジワイヤースクリーンの平面図である。
【図7】ウエッジワイヤースクリーンを支持枠に嵌入したろ過板の正面図である。
【図8】この発明に係るろ過室を並列多室構成としたフイルタープレスの縦断側面図である。
【符号の説明】
2a フレーム
5、5a 駆動軸
6、6a 駆動機
7 汚泥供給管
8 供給口
9 取出口
10 内環支持体
11 ろ過板
12 外周環
13 ろ過室
17 逆止板
17a 側縁部
17b 先端部
18 洗浄水管
19 圧縮空気管
20 洗浄水供給管
21 噴射口
22 洗浄水供給管
21 噴射口
24 開閉弁
25 回動軸
26 ダンパー
27 回動レバー
28 シリンダー
30、32 メタルスクリーン
31 外環支持枠
31a リブ
[0001]
BACKGROUND OF THE INVENTION
TECHNICAL FIELD The present invention relates to a sludge squeezing and dewatering apparatus containing a large amount of minerals and fibers, and more particularly to an intermittent filter press that enables cake washing.
[0002]
[Prior art]
Conventionally, as an intermittent press dehydrator, a pair of filter cloths are arranged between the filter plates before and after forming the filtration chamber, and the stock solution is press-fitted between the filter cloths to dehydrate and release between the filter plates. There is a filter press for discharging the cake to the lower side of the filter plate, and it is known, for example, as described in Japanese Utility Model Publication No. 7-21204. In addition, donut-shaped filter plates and rotatable stirring plates are alternately arranged in the filtration chamber at narrow intervals, and the sludge pressed into the filtration chamber is moved by sewing the gap between the filtration plates. The rotary filter press in which the separated liquid is discharged from the water and the filtered and dehydrated cake is continuously taken out from the other end while performing the sweep filtration is also disclosed in, for example, JP-A-10-165721. well known.
[0003]
[Problems to be solved by the invention]
However, although the above conventional filter press can perform large-capacity processing and high-pressure squeezing and dehydration, it has a complicated structure for opening and closing a large number of parallel filter plates, and requires a large installation space. In addition, it is necessary to periodically replace the filter cloth, which is a consumable item, and a large amount of washing water is required to regenerate the clogged filter cloth. In addition, this conventional rotary filter press prevents the clogging of the filter plate by stirring the stock solution and continuously obtains the cake, but it is stirred because the stir plate is rotated at a relatively high speed. The organic matter became colloidal, and colloidal sludge might flow out from the filter plate together with the filtrate, and the moisture content of the cake was relatively high. The present invention has been made in view of the above-described conventional problems, and its purpose is to perform double-side filtration while moving the sludge press-fitted into the filtration chamber together with the filtration chamber, and to laminate the cake and sludge laminated on the filtration surface. An object of the present invention is to provide a pressing and dewatering device that collects a cake having a low water content by using the shear resistance generated on the contact surface as a filtering force.
[0004]
[Means for Solving the Problems]
The gist of the present invention is that a filter chamber is formed by two disk-shaped filter plates disposed on a rotatable drive shaft and an outer ring which is in sliding contact with the outer periphery of the filter plate, and a lower portion of the filter chamber. A check plate is fastened to the outer peripheral ring of the filter plate, the side edge of the check plate is brought close to the filter plate, and its tip is slid on the drive shaft, and the start side of the filtration chamber regulated by the check plate The sludge supply port and the cake outlet on the end side are opened, and an open / close valve is provided at the outlet.The sludge that is press-fitted into the filtration chamber moves the concentrated sludge while performing double-sided filtration, The sludge is dehydrated by slip resistance with the contact surface of the filter medium, and the pressure dehydration is performed while applying back pressure to the dehydrated cake by closing the on-off valve.
[0005]
And, the washing water pipe and the compressed air pipe are connected to the sludge supply pipe connected to the sludge supply port of the filtration chamber so that the cake can be washed and the blown cake of the washed cake can be fed. It is. In addition, the washing water supply pipe injection port disposed on the check plate is provided on the filter plate, and the filter plate is washed from the inside of the filtration chamber when necessary to regenerate the filtration surface. . The check plate on the outlet side has a side edge portion close to the filtration plate and a tip portion slid on the drive shaft protruding in a cutting edge shape to peel the cake from the wall surface of the filtration chamber. is there. Further, if the wall surface of the check plate on the outlet side is curved in a parabolic shape, the check plate does not serve as a resistance to discharging the pressed and dehydrated cake. In addition, the filter plate can be washed by disposing a cleaning tube at the starting end of the filtration chamber provided with the supply port so as to face the outer peripheral surface of the filter plate.
[0006]
And the said filter plate consists of a disk-shaped metal screen which has many fine holes, and the outer ring support frame which joined and integrated the grid | lattice-like rib which inserted this metal screen, and two disk-shaped filter plates Is connected to a boss-like inner ring support, and this inner ring support is fitted to a rotatable drive shaft, so that the filter medium can be easily attached and the strength is increased. In addition, if a metal screen is stretched on the inner ring support of the filter plate, the filtration area is increased. The on-off valve is composed of a damper fixed to the rotating shaft of the cake outlet, a rotating lever connected to the rotating shaft of the damper, and a cylinder pivotally attached to the rotating lever. It is possible to discharge the cake having a uniform moisture content from the outlet by adjusting the degree of opening of the damper from the outlet of the outer ring and applying pressure and back pressure for filtration. A plurality of filtration chambers arranged in parallel with the drive shaft, both ends of the drive shaft that pivotally supports the plurality of filtration chambers supported on the frame, and the drive shaft linked to the drive machine are connected in a parallel multi-chamber configuration. Thus, a large volume of sludge can be treated, and a double-sided filtration chamber can be utilized to reduce the occupied space.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
The apparatus according to the present invention is configured as described above. When the sludge is press-fitted from the supply port while closing the opening / closing valve of the cake outlet and rotating the filtration chamber at a slow speed, the concentration zone near the supply port immediately after the press-fitting Then, the filtrate is separated from both sides of the filter plate mainly by press-fitting pressure, and the sludge is concentrated. The sludge is transferred to the dehydration zone as the filtration chamber rotates while being concentrated, and the sludge is dehydrated by the frictional resistance with the contact surface of the filter medium by the rotation of the filtration chamber, and a cake layer is gradually formed on the filtration surface of the filter plate. Eventually, the sludge loses its fluidity, and shear friction resistance is generated between the cake layer on the filtration surface and the relatively soft sludge at the center, thereby promoting dehydration. The cake transferred to the pressing zone is further dehydrated while applying back pressure to the cake from the outlet. When the dehydrated cake is filled in the filtration chamber, supply of the sludge to the filtration chamber is stopped, and while the filter plate is continuously rotated, a washing water pipe is connected to the sludge supply port of the filtration chamber, Washing water is injected into the cake, and the active ingredient contained in the cake or unnecessary ingredient is washed and separated. After washing the cake, the washing water pipe at the sludge supply port is switched, the compressed air pipe is connected, compressed air is blown into the washed dehydrated cake, and the cake is blown to discharge moisture. Next, if the on-off valve is opened, the cake can be discharged from the outlet by the frictional resistance with the contact surface of the filter medium due to the rotation of the filter plate. At the end of the discharge of the cake, the sludge adhering to the filter plate can be washed and cleaned from both sides to prepare for the resumption of operation.
[0008]
【Example】
The filter press according to the present invention will be described in detail with reference to the drawings. First, in FIG. 1, reference numeral 1 denotes a filter press, and a bearing 4 is fixed to a pedestal 3 supported on frames 2 and 2 on both sides. The drive shaft 5 supported by the shaft 4 is rotated by the drive device 6. In the lower part of the filter press 1, a supply port 8 connected to the sludge supply pipe 7 and a cake outlet 9 are provided. The structure of the filter press 1 will be described in detail with reference to FIGS. 2 and 3. An inner ring support 10 is fitted to the drive shaft 5, and two disk-shaped filter plates 11 are attached to the inner ring support 10. The inner peripheral edge of 11 is fixed. The filter plate 11 is rotated slowly with the drive shaft 5. An outer peripheral ring 12 is disposed on the peripheral portion of the filter plate 11, and a filtration chamber 13 is formed in the inside of the two filter plates 11 and 11 and the outer peripheral ring 12. A cover 14 that covers the filter plate 11 is provided on the peripheral surface of the filter plate 11, and an outer peripheral end of the cover 14 is fixed to the outer ring 12. An inner peripheral edge of the cover 14 is supported by the drive shaft 5 by the bearing 4, and a filtrate chamber 15 is formed in the outer peripheral portion of the filtration chamber 13. In addition, the back surface of the cover 14 is fixed to the gantry 3 so that the outer peripheral ring 12 does not rotate with the filter plate 11. Reference numeral 16 denotes a filtrate drain pipe.
[0009]
As shown in FIG. 2, a check plate 17 for dividing the filtration chamber 13 is provided between the sludge supply port 8 of the filtration chamber 13 and the cake outlet 9, and the filtration plate 11 is rotated ( The sludge supplied from the supply port 8 of the filtration chamber 13 is in the concentration zone A at the beginning of press-fitting, and is solid-liquid separated mainly by the press-fitting pressure. The concentrated sludge is in the dehydration zone B, and the filtration chamber 13 Of the filter medium and the shear friction resistance force between the cake layer on the filtration surface and the relatively soft sludge at the center, thereby promoting dehydration. The filtration chamber 13 is further rotated and transferred to the squeezing zone C in the vicinity of the cake outlet 9. As shown in FIG. 4, the sludge supply pipe 7 connected to the sludge supply port 8 is provided with an electromagnetic valve V1, which is branched from the sludge supply pipe 7 behind the electromagnetic valve V1 and is connected to the washing water pipe 18. A compressed air pipe 19 is connected. The washing water pipe 18 and the compressed air pipe 19 are provided with solenoid valves V2 and V3, and the solenoid valves V1, V2 and V3 are opened and closed to supply sludge to the filtration chamber 13 and included in the cake. The cake washing for separating the active ingredient or the unnecessary ingredient, and the feed blow for blowing moisture to the cake after the cake washing can be performed.
[0010]
Further, as shown in FIG. 4, the check plate 17 is provided with a cleaning water supply pipe 20 for clogging elimination facing the filter plate 11 from the inside of the filtration chamber 13, and jetting of the cleaning water supply pipe 20. High pressure water is jetted onto the filter plate 11 with the mouth 21 rotating. Further, as shown in FIGS. 3 and 4, a cleaning water supply pipe 22 is disposed at the start end of the filtration chamber 13 provided with the supply port 8 so as to face the outer peripheral surface of the filter plate 11. Pressure water is injected from the injection port 23 of the water supply pipe 22 so that the sludge adhering to the filter plate can be washed and cleaned from the outer surface, and the double-sided cleaning of the filter plate 11 can be performed. As shown in FIG. 5, the check plate 17 on the outlet 9 side has a side edge portion 17 a close to the filter plate 11 and a tip end portion 17 b slidably provided on the drive shaft 5 projecting into a cutting edge shape. The cake discharged from the filtration chamber 13 to the outlet 9 is peeled off from the filtration chamber 13. If the wall surface of the check plate 17 facing the outlet 9 of the filtration chamber 13 is curved parabolically as shown in FIGS. 2 and 4, the cake is guided in the rotational tangential direction of the filter plate 11. Thus, the check plate 17 does not serve as a resistance to discharge of the press-dehydrated cake.
[0011]
As shown in FIGS. 2 and 3, an opening / closing valve 24 is provided at the cake outlet 9 of the filtration chamber 13, and the opening / closing valve 24 is connected to a rotating shaft 25 that is pivotally supported at one end of the outlet 9. It comprises a damper 26, a rotating lever 27 connected to the rotating shaft 25 of the damper 26, and a cylinder 28 pivotally attached to the rotating lever 27. The piston 29 of the cylinder 28 is expanded and contracted to take out the cake. 9 is opened and closed, the piston 29 is extended, the damper 26 is rotated, the outlet 9 is closed, and the back pressure is applied to the squeezing zone C. First, the outlet 9 is closed, and while the stock solution is continuously supplied from the supply port 8 of the filtration chamber 13, the sludge is concentrated and squeezed and dehydrated, and then the supply of the stock solution is stopped and the outlet of the filtration chamber 13 is removed. 9 is released, and the cake is taken out while the filtration chamber 13 is continuously rotated.
[0012]
As shown in FIGS. 6 and 7, the filter plate 11 includes a donut-shaped metal screen 30 composed of a wedge wire 30a and a support rod 30b attached to the back surface, and a lattice-shaped rib 31a joined and integrated. The outer ring support frame 31 is fitted so that the filter medium can be easily exchanged. In addition, if the metal screen 32 is stretched also to the inner ring support body 10 to which the inner peripheral edge of the filtration chamber 13 is fixed, the filtration area is increased and the dewaterability of sludge is improved. A plurality of drainage channels 33 are formed so that the filtrate separated from the filtration chamber 13 can be drained into the filtrate chamber 15. The continuous squeezing and dehydrating apparatus shown in FIG. 8 is another embodiment in which a plurality of the above-mentioned filter presses are arranged in parallel, and the filtration plate 11 forming each filtration chamber 13 is connected to the drive shaft 5a to form a multi-chamber configuration. is there. Further, the front and rear filtration chambers 13 are connected by a support cylinder 34, the support cylinders 34a and 34a at the front end and the rear end are supported by the frames 2a and 2a, and a pulley 35 fitted to the drive shaft 5a is attached to the drive machine 6a. A plurality of filter plates are rotated in conjunction with each other. Reference numeral 15a denotes a filtrate chamber for separating the filtrate from the filter plate 11. As described above, the parallel multi-chamber configuration enables large-capacity treatment of sludge and reduces the occupied space.
[0013]
【The invention's effect】
As is clear from the above description, the filter press according to the present invention performs double-sided filtration on the sludge press-fitted into the filtration chamber while slowly feeding the two sludge plates and sludge together. Between the cake and the relatively soft sludge at the center of the cake laminated on the filtration surface, and the sludge is concentrated and dehydrated. That is, the conventional filter press requires a complicated filter plate opening / closing device and a wide installation space. In the rotary filter press, colloidal sludge is generated from the filter plate in order to rotate the stirring plate at a high speed. In this invention, the filter plate and sludge generate frictional resistance and dehydrated cake, and the filter chamber is continuously rotated while the filter chamber is rotated. Since high-pressure water and compressed air are supplied, the components contained in the cake are separated, and the water in the washed cake can be separated. And since the washing water piping of the filter plate was provided in the check plate and the sludge supply side of the filter chamber, the filter plate can be regenerated.
[Brief description of the drawings]
FIG. 1 is a schematic front view of a filter press according to the present invention.
FIG. 2 is a schematic longitudinal sectional front view showing the structure of a filtration chamber according to the present invention.
3 is a longitudinal side view of the filtration chamber according to the present invention cut along the line AA in FIG. 1. FIG.
FIG. 4 is a conceptual diagram showing piping for supplying pressure water and compressed air to the filtration chamber according to the present invention.
FIG. 5 is a front view of the check plate as viewed from the squeezing zone of the filtration chamber.
FIG. 6 is a plan view of a wedge wire screen.
FIG. 7 is a front view of a filter plate in which a wedge wire screen is fitted into a support frame.
FIG. 8 is a longitudinal side view of a filter press having a filtration chamber according to the present invention in a parallel multi-chamber configuration.
[Explanation of symbols]
2a Frame 5, 5a Drive shaft 6, 6a Drive 7 Sludge supply pipe 8 Supply port 9 Outlet 10 Inner ring support 11 Filter plate 12 Outer ring 13 Filtration chamber 17 Check plate 17a Side edge 17b Tip 18 Washing water pipe 19 Compressed air pipe 20 Washing water supply pipe 21 Injection port 22 Washing water supply pipe 21 Injection port 24 Opening and closing valve 25 Rotating shaft 26 Damper 27 Rotating lever 28 Cylinders 30 and 32 Metal screen 31 Outer ring support frame 31a Rib

Claims (11)

回転自在な駆動軸(5)に配設した2枚の円盤状のろ過板(11、11)と、ろ過板(11)の外周部に摺接させた外周環(12)とでろ過室(13)を形成し、ろ過室(13)の下方部の外周環(12)に逆止板(17)を止着して、この逆止板(17)の側縁部(17a)をろ過板(11)に近接させ、その先端部(17b)を駆動軸(5)に摺設させると共に、逆止板(17)で規制するろ過室(13)の始端側に汚泥の供給口(8)と、その終端側にケーキの取出口(9)を外周環(12)に開口し、この取出口(9)に開閉弁(24)を設けたことを特徴とするフイルタープレス。A filtration chamber (12) having two disc-shaped filter plates (11, 11) disposed on a rotatable drive shaft (5) and an outer ring (12) slidably contacted with the outer periphery of the filter plate (11). 13), a check plate (17) is fastened to the outer peripheral ring (12) at the lower part of the filtration chamber (13), and the side edge (17a) of the check plate (17) is attached to the filter plate. (11), the tip (17b) is slid on the drive shaft (5), and the sludge supply port (8) on the start end side of the filtration chamber (13) regulated by the check plate (17) The filter press is characterized in that a cake outlet (9) is opened to the outer ring (12) on the end side, and an open / close valve (24) is provided at the outlet (9). 上記ろ過室(13)の汚泥の供給口(8)に連結した汚泥供給管(7)に切替自在に洗浄水管(18)を連結したことを特徴とする請求項1記載のフイルタープレス。2. The filter press according to claim 1, wherein a washing water pipe (18) is connected to a sludge supply pipe (7) connected to a sludge supply port (8) of the filtration chamber (13). 上記ろ過室(13)の汚泥の供給口(8)に連結した汚泥供給管(7)に切替自在に圧縮空気管(19)を連結したことを特徴とする請求項1または2記載のフイルタープレス。The filter press according to claim 1 or 2, wherein a compressed air pipe (19) is connected to a sludge supply pipe (7) connected to a sludge supply port (8) of the filtration chamber (13). . 上記逆止板(17)に配設した洗浄水供給管(20…)の噴射口(21…)をろ過板(11)に対設したことを特徴とする請求項1または3記載のフイルタープレス。The filter press according to claim 1 or 3, wherein an injection port (21 ...) of a washing water supply pipe (20 ...) disposed on the check plate (17) is provided on the filter plate (11). . 上記取出口(9)側の逆止板(17)は、ろ過板(11)に近接させた側縁部(17a)と、駆動軸(5)に摺設させた先端部(17b)が切刃状に突出させてあることを特徴とする請求項1乃至4記載のフイルタープレス。The check plate (17) on the outlet (9) side has a side edge (17a) close to the filter plate (11) and a tip (17b) slid on the drive shaft (5). 5. The filter press according to claim 1, wherein the filter press is projected in a blade shape. 上記取出口(9)側の逆止板(17)の壁面を放物線状に湾曲させたことを特徴とする請求項1乃至5記載のフイルタープレス。6. The filter press according to claim 1, wherein a wall surface of the check plate (17) on the outlet (9) side is curved in a parabolic shape. 上記供給口(8)を設けたろ過室(13)の始端部に、ろ過板(11)の外周面に対向して洗浄水供給管(22)を配設したことを特徴とする請求項1乃至6記載のフイルタープレス。The washing water supply pipe (22) is arranged at the starting end of the filtration chamber (13) provided with the supply port (8) so as to face the outer peripheral surface of the filter plate (11). The filter press of thru | or 6. 上記ろ過板(11)は、多数の微細孔を有する円盤状のメタルスクリーン(30)と、このメタルスクリーン(30)を嵌入した格子状のリブ(31a)を接合一体化した外環支持枠(31)とからなり、2枚の円盤状のろ過板(11)がボス状の内環支持体(10)に連結され、この内環支持体(10)が回転自在な駆動軸(5)に嵌着されていることを特徴とする請求項1乃至7記載のフイルタープレス。The filter plate (11) includes a disc-shaped metal screen (30) having a large number of fine holes and an outer ring support frame in which lattice-shaped ribs (31a) fitted with the metal screen (30) are joined and integrated. 31) and two disk-shaped filter plates (11) are connected to a boss-shaped inner ring support (10), and the inner ring support (10) is connected to a rotatable drive shaft (5). 8. The filter press according to claim 1, wherein the filter press is fitted. 上記ろ過板(11)の内環支持体(10)にメタルスクリーン(32)を張設したことを特徴とする請求項1乃至8記載のフイルタープレス。9. The filter press according to claim 1, wherein a metal screen (32) is stretched on the inner ring support (10) of the filter plate (11). 上記開閉弁(24)は、ケーキの取出口(9)の回動軸(25)に止着したダンパー(26)と、ダンパー(26)の回動軸(25)に連結した回動レバー(27)と、回動レバー(27)に枢着したシリンダー(28)とからなることを特徴とする請求項1乃至9記載のフイルタープレス。The on-off valve (24) includes a damper (26) fixed to the rotating shaft (25) of the cake outlet (9) and a rotating lever (25) connected to the rotating shaft (25) of the damper (26). The filter press according to any one of claims 1 to 9, wherein the filter press comprises a cylinder (28) pivotally attached to the rotation lever (27). 上記ろ過室(13)を駆動軸(5a)に複数並列し、このろ過室(13…)を軸支した駆動軸(5a)の両端部をフレーム(2a、2a)に支架させて、駆動軸(5a)を駆動機(6a)に連動連結したことを特徴とする請求項1乃至10記載のフイルタープレス。A plurality of the filtration chambers (13) are arranged in parallel to the drive shaft (5a), and both ends of the drive shaft (5a) that pivotally supports the filtration chamber (13 ...) are supported on the frame (2a, 2a). 11. The filter press according to claim 1, wherein (5a) is interlocked and connected to a driving machine (6a).
JP21844699A 1999-06-17 1999-08-02 Filter press Expired - Fee Related JP3772598B2 (en)

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CN1933886A (en) * 2004-04-22 2007-03-21 巴工业株式会社 Rotary compression filter with slit blow scraper
WO2005105263A1 (en) * 2004-04-28 2005-11-10 Tomoe Engineering Co., Ltd. High dehydration type rotation pressurization dehydrator
BRPI0514226A (en) 2004-08-09 2008-06-03 Prime Solution Inc liquid extractor assembly for extracting liquid from a mass, method of washing a liquid extractor assembly for extracting liquid from a mass, and, system for extracting liquid from a mass
CN101296739B (en) 2005-10-28 2011-12-14 普莱姆解决方案公司 Rotating fan compressor
JP4820784B2 (en) * 2007-07-18 2011-11-24 株式会社神鋼環境ソリューション Rotating pressure dehydrator and sludge dewatering method using rotating pressure dehydrator
JP5507908B2 (en) * 2009-07-07 2014-05-28 三菱化工機株式会社 Rotating filter type filter
ITVI20120190A1 (en) * 2012-07-30 2014-01-31 Nuove En S R L MACHINE FOR CONTINUOUS MICROFILTRATION OF PROCESS AND DISCHARGE WATERS REUSABLE IN AGRICULTURE AND INDUSTRY
JP6557254B2 (en) 2014-04-08 2019-08-07 プライム ソリューション インク. Rotating fan press machine with auger
CN107321035A (en) * 2017-07-07 2017-11-07 象山德曼机械有限公司 A kind of solid-liquid separating equipment
JP7255073B2 (en) * 2020-04-13 2023-04-11 株式会社石垣 How to wash the dehydrated cake
KR102371210B1 (en) * 2021-01-25 2022-03-08 주식회사 대승엔지니어링 Rotary Type Compressive Filtering Machine
CN115974358B (en) * 2023-03-16 2023-06-06 甘肃祥农兆丰农业科技发展有限公司 Automatic dehydration treatment equipment for livestock manure

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