JPH04358509A - Drum filter type filter device - Google Patents

Drum filter type filter device

Info

Publication number
JPH04358509A
JPH04358509A JP15984291A JP15984291A JPH04358509A JP H04358509 A JPH04358509 A JP H04358509A JP 15984291 A JP15984291 A JP 15984291A JP 15984291 A JP15984291 A JP 15984291A JP H04358509 A JPH04358509 A JP H04358509A
Authority
JP
Japan
Prior art keywords
filter
stock solution
drum
drum filter
flow path
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP15984291A
Other languages
Japanese (ja)
Inventor
Yoshimi Shinohara
好美 篠原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shinohara Seiki KK
Original Assignee
Shinohara Seiki KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shinohara Seiki KK filed Critical Shinohara Seiki KK
Priority to JP15984291A priority Critical patent/JPH04358509A/en
Publication of JPH04358509A publication Critical patent/JPH04358509A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a device of simple structure with good filtering power by attaching a nozzle means for generating the stock solution flow reverse to the rotating direction of a stream along a curved flow path starting from a filter terminal point at an inflow inlet of stock solution. CONSTITUTION:A curved flow path 22 is formed along the peripheral face of a drum filter 28 at the bottom face of a treatment tank 21. An inflow inlet 15 of stock solution is formed in communication with the curved flow path 22 in the vicinity of a filter terminal point A. A nozzle means 23 for generating the flow of stock solution reverse to the rotating direction of a drum 28 along the curved flow path 22 starting the filter terminal point A is attached under a stock solution inflow inlet 25. A solid floatation material in the stock solution can be easily caught when passing through the opening of the filter 28 by said arrangement, and in addition the stock solution flowed in from the nozzle means 23 is guided first to an area below the filtrate level where adhesion force (suction force) is highest. A secondary flow along the curved flow path 22 starting from the point A is generated by the flow from the nozzle means 23 and fine solid floatation materials not adhering in the vicinity of point A and remaining as they are can be carried along the flow path 22.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、例えばパルプ繊維を含
む固形浮遊物のヘドロ、スラッジ、パルプ原液等を、駆
動回転するドラム状のフィルターで濾過する濾過処理装
置に関し、簡略な構造で良好な処理能を有し、特に従来
より問題となっていたドラムフィルターが原液表面から
液面上方へ脱離する濾過終了点でのパルプ短繊維を含む
微細浮遊物の溜りを解消するドラムフィルター式濾過処
理装置に関するものである。
[Industrial Field of Application] The present invention relates to a filtration treatment device for filtering solid suspended matter such as sludge, sludge, pulp stock solution, etc. containing pulp fibers using a drum-shaped filter that rotates. Drum filter type filtration processing that has processing ability and eliminates the accumulation of fine suspended matter including short pulp fibers at the filtration end point where the drum filter desorbs from the surface of the raw solution to above the liquid surface, which has been a problem in the past. It is related to the device.

【0002】0002

【従来の技術】図4は従来のドラムフィルター式濾過処
理装置の構成を示す説明図である。図に示す通り、処理
槽1は堰板2で区画された原水流入室3及び導管で接続
された液面検出室4及び液面検出器16を有する。堰板
2は処理槽1内よりも高い液面を保つように高さが調整
してあり、流入口5より送られた原水は堰板2の頂部を
越えて分離フィルター6へと供給され、先ずここで粗と
密に液中の固形浮遊物は分離される。パルプ短繊維を含
む微細浮遊物は該分離フィルタ6を通過し、邪魔板7に
ぶつかり、処理槽1内に送り込まれることになり、粗い
繊維を含む粗大浮遊物は分離フィルター6を越えて直接
ドラムフィルター8上に送られる。
2. Description of the Related Art FIG. 4 is an explanatory diagram showing the structure of a conventional drum filter type filtration processing apparatus. As shown in the figure, the processing tank 1 has a raw water inflow chamber 3 divided by a weir plate 2, a liquid level detection chamber 4 and a liquid level detector 16 connected to each other by a conduit. The height of the weir plate 2 is adjusted to maintain a higher liquid level than in the processing tank 1, and the raw water sent from the inlet 5 is supplied to the separation filter 6 over the top of the weir plate 2. First, solid suspended matter in the liquid is separated into coarse and fine particles. Fine suspended matter containing short pulp fibers passes through the separation filter 6, collides with the baffle plate 7, and is sent into the processing tank 1, while coarse suspended matter containing coarse fibers passes through the separation filter 6 and is sent directly to the drum. It is sent onto filter 8.

【0003】このドラムフィルター8は周面にメッシュ
度が大なる金網が形成されていて、モーター10で駆動
回転されるものである。従って前記の粗い繊維等の粗大
浮遊物はこのドラムフィルター8で濾過され、濾出され
た処理水11は取出パイプの開口12より外部へと取出
され再使用または放流させられることになる。尚、分離
フィルター6の内部にはシャワー9が設けられており、
該フィルター6の目詰まりを防止する。
[0003] This drum filter 8 has a wire mesh with a large mesh formed on its circumferential surface, and is driven and rotated by a motor 10. Therefore, the above-mentioned coarse suspended matter such as coarse fibers is filtered by the drum filter 8, and the filtered treated water 11 is taken out from the opening 12 of the take-out pipe and is reused or discharged. Note that a shower 9 is provided inside the separation filter 6.
This prevents the filter 6 from clogging.

【0004】分離フィルター6で取出し得なかったパル
プ短繊維を含む微細浮遊物等は処理槽1内を仕切り板1
3に沿って移動し、仕切り板13の端部で浮上しながら
ドラムフィルター8の金属面に付着してゆく、仕切り板
13はドラムフィルター8の周面に沿って湾曲して設け
られ、処理槽1内の原水の濃度を平均化し、濾過効率を
上昇するに役立つ。そして、原水中の油等は液面付近で
ドラムフィルター8に付着してゆく。
[0004] Fine suspended matter containing pulp short fibers that could not be removed by the separation filter 6 is removed from the treatment tank 1 by a partition plate 1.
The partition plate 13 is curved along the circumferential surface of the drum filter 8, and is attached to the metal surface of the drum filter 8 while floating at the end of the partition plate 13. It helps to average the concentration of raw water within 1 and increase the filtration efficiency. Then, oil and the like in the raw water adhere to the drum filter 8 near the liquid surface.

【0005】該ドラムフィルター8の金網は前述したよ
うに、メッシュ大なので初め付着度が大であり、予め分
離フィルター6で分離された粗いパルプ、粗大粒子等が
、次いでこの上に分離できなかったパルプ短繊維や微細
粒子等が、そして最後に油等が付着し、フィルター8の
表面に3段の層が形成される。
As mentioned above, since the wire mesh of the drum filter 8 has a large mesh size, the degree of adhesion is high at first, and the coarse pulp, coarse particles, etc. that were previously separated by the separation filter 6 could not be separated thereon. Short pulp fibers, fine particles, etc., and finally oil, etc. adhere, forming three layers on the surface of the filter 8.

【0006】ドラムフィルター8の外周面に付着したパ
ルプ等は、水面上においてドラムフィルターと接触して
いる剥離ロール14に乗り移り、該フィルター3から除
去される。そして剥離ローラ14に付着したパルプ等は
ロールの先端に設けられた掻取ナイフ15によって最終
的に除去されて回収される。剥離ロール14との接触に
よって、パルプ繊維や粒子等の付着物が除去されたドラ
ムフィルター8のその部分は、その回転につれ再び原液
内へと入ってゆく。
Pulp and the like adhering to the outer peripheral surface of the drum filter 8 are transferred to the peeling roll 14 which is in contact with the drum filter above the water surface and removed from the filter 3. Pulp and the like adhering to the peeling roller 14 are finally removed and recovered by a scraping knife 15 provided at the tip of the roll. As the drum filter 8 rotates, that part of the drum filter 8 from which deposits such as pulp fibers and particles have been removed by contact with the peeling roll 14 enters the raw solution again.

【0007】[0007]

【発明が解決しようとする課題】回転につれ原液中に入
ったドラムフィルター8の周面には、上述の如く粗いパ
ルプ繊維や粗大粒子が付着し、次に予め分離できなかっ
たパルプ短繊維や微細粒子が付着し、最後に油等の浮遊
物が付着されたパルプ繊維を含む固形浮遊物に吸着され
ることになる。
[Problems to be Solved by the Invention] As described above, coarse pulp fibers and coarse particles adhere to the peripheral surface of the drum filter 8 that enters the raw solution as it rotates, and then short pulp fibers and fine particles that cannot be separated in advance Particles are attached, and finally suspended matter such as oil is adsorbed to the solid suspended matter containing attached pulp fibers.

【0008】しかしながら、ドラムフィルター周面での
原液中のパルプ繊維等の浮遊物の付着は、ドラムフィル
ター周面での水圧によって付着されるために、付着力が
最も高い領域は処理水の水面以下の領域であり、ドラム
フィルターが原液より脱離する濾過終了点に近付くにつ
れて水圧が下がるために付着力(吸引力)が低下し、パ
ルプ短繊維や微細浮遊物が付着されずに残ったり、また
一旦付着したパルプ短繊維や微細浮遊物が脱離したりし
て、ドラムの濾過終了点でパルプ短繊維や微細浮遊物の
溜りが形成されていた。
However, since floating substances such as pulp fibers in the raw solution adhere to the drum filter circumferential surface due to the water pressure on the drum filter circumferential surface, the area with the highest adhesion force is below the water surface of the treated water. As the drum filter approaches the filtration end point where it separates from the raw solution, the water pressure decreases and the adhesion force (suction force) decreases, causing short pulp fibers and fine suspended matter to remain unattached, or The short pulp fibers and fine suspended matter that had once attached were detached, and a pool of short pulp fibers and fine suspended matter was formed at the end of filtration of the drum.

【0009】また、分離フィルター6で粗と密に原液中
の固形浮遊物が分離されるのであるが、装置の構成が複
雑になっていた。また、前述のように、原液中のパルプ
や浮遊粒子物質の付着は、ドラムフィルター周面での水
圧によって付着(吸引)されるために、分離フィルター
6で分離した物質をドラムフィルター8に送っても、原
液中で一旦脱離してまた付着しており、問題となってい
た。更に、処理槽の下方で仕切り板13と処理槽1底面
とが二重になっており、洗浄が困難であるという問題も
あった。
[0009] Furthermore, solid suspended matter in the stock solution is separated by the separation filter 6 into coarse and fine particles, but the structure of the device is complicated. In addition, as mentioned above, pulp and suspended particulate matter in the stock solution are attached (suctioned) by the water pressure around the drum filter, so the substances separated by the separation filter 6 are sent to the drum filter 8. However, it was once desorbed in the stock solution and then adhered again, which was a problem. Furthermore, there was a problem in that the partition plate 13 and the bottom surface of the processing tank 1 were doubled at the bottom of the processing tank, making cleaning difficult.

【0010】本発明は、簡略な構造で良好な処理能を有
し、特にドラムの濾過終了点でパルプ短繊維や微細浮遊
物の溜りを解消することのできるドラムフィルター式濾
過処理装置を得ることを目的とする。
[0010] The present invention provides a drum filter type filtration device which has a simple structure, has good processing performance, and is particularly capable of eliminating accumulations of short pulp fibers and fine suspended matter at the end of filtration of the drum. With the goal.

【0011】[0011]

【課題を解決するための手段】本請求項1に記載の発明
に係るドラムフィルター式濾過処理装置では、原液流入
口から流入される原液を収容する処理槽内に周面フィル
ターの一部が原液表面から露出するように浸漬された回
転駆動式のドラムフィルターと、該ドラムフィルター内
部の濾液を外部へ排出する濾液排出手段とを備え、前記
処理槽中の原液が回動するドラムフィルターの周面フィ
ルターを通過する際に前記周面フィルター表面に付着し
た濾過残渣をドラムフィルターの回転方向下流の水面上
位置で連続的に掻き取るように構成したドラムフィルタ
ー式濾過処理装置において、前記処理槽の底面が、前記
ドラムフィルターの周面に沿った湾曲流路を形成し、前
記原液流入口が、前記ドラムフィルターが前記原液表面
から液面上方へ脱離する濾過終了点近傍位置で前記湾曲
流路に連通して設けられ、前記原液流入口には、前記濾
過終了点から前記湾曲流路に沿ってドラムの回転方向と
逆向きに原液の流れを発生させるノズル手段が付設され
ているものである。
[Means for Solving the Problems] In the drum filter type filtration processing apparatus according to the invention as set forth in claim 1, a part of the peripheral filter is disposed in a processing tank that accommodates the stock solution flowing in from the stock solution inlet. A peripheral surface of the drum filter on which the raw solution in the processing tank rotates, comprising a rotationally driven drum filter immersed so as to be exposed from the surface, and a filtrate discharge means for discharging the filtrate inside the drum filter to the outside. In a drum filter type filtration treatment device configured to continuously scrape off filtration residue adhering to the surface of the peripheral filter when passing through the filter at a position above the water surface downstream in the rotational direction of the drum filter, the bottom surface of the treatment tank forms a curved flow path along the circumferential surface of the drum filter, and the stock solution inlet enters the curved flow path at a position near the filtration end point where the drum filter is detached from the surface of the stock solution above the liquid surface. The undiluted solution inlet is provided with a nozzle means for generating a flow of the undiluted solution from the filtration end point along the curved flow path in a direction opposite to the rotational direction of the drum.

【0012】更に好ましくは、前記ノズル手段が水頭に
応じてノズル開口断面積を変化させる可変ノズルを含む
ものを開示する。
More preferably, the nozzle means includes a variable nozzle that changes the cross-sectional area of the nozzle opening depending on the water head.

【0013】[0013]

【作用】本発明においては、従来のドラムフィルター式
濾過処理装置の形状、配置、ドラムの回転方向等の構成
を種々に変えて、簡略な構造で良好な処理能を有し、特
にドラムの濾過終了点でパルプ短繊維や微細浮遊物の溜
りを解消する構成を求めたところ、処理槽の底面がドラ
ムフィルターの周面に沿った湾曲流路を形成し;原液流
入口が、前記ドラムフィルターが前記原液表面から液面
上方へ脱離する濾過終了点近傍位置で前記湾曲流路に連
通して設けられ;前記原液流入口には、前記濾過終了点
から前記湾曲流路に沿ってドラムの回転方向と逆向きに
原液の流れを発生させるノズル手段が付設されているも
のが、最もよい結果を得た。
[Function] In the present invention, the shape, arrangement, rotation direction of the drum, etc. of the conventional drum filter type filtration processing device are changed in various ways to achieve good processing performance with a simple structure. When we sought a configuration to eliminate the accumulation of short pulp fibers and fine suspended matter at the end point, we found that the bottom of the treatment tank forms a curved flow path along the circumference of the drum filter; Provided in communication with the curved channel at a position near the filtration end point where the undiluted solution is desorbed from the surface of the undiluted solution above the liquid surface; The best results were obtained with a nozzle means that produced a flow of the stock solution in the opposite direction.

【0014】即ち、原液流路には濾過終了点からドラム
の回転方向と逆向きの流れが発生する。一方、ドラムは
原液流路の流れと対向する方向に回転されている。この
ため、原液中のパルプ繊維や浮遊物等がフィルターの孔
を通過する際にフィルター孔に引っ掛かり易くなり、加
えて、原液中のパルプ繊維や浮遊物の付着力(吸引力)
が最も高い領域である処理水の水面以下の領域に、ノズ
ル手段から流入される原液が導かれるため、効率のよい
付着を行うことができ、簡略な構造で良好な処理能が得
られる。
That is, a flow occurs in the raw solution flow path in the opposite direction to the rotational direction of the drum from the filtration end point. On the other hand, the drum is rotated in a direction opposite to the flow of the stock solution channel. For this reason, pulp fibers and suspended matter in the stock solution are likely to get caught in the filter pores when passing through them, and in addition, the adhesion (suction power) of pulp fibers and suspended matter in the stock solution increases.
Since the raw solution flowing from the nozzle means is guided to the region below the surface of the treated water where the .

【0015】また、濾過終了点からドラムの回転方向と
逆向きの流れにより同方向に沿った副流が発生し、濾過
終了点近傍で付着されずに残ったパルプ短繊維や微細浮
遊物をドラムフィルターが原液液面上方から原液表面へ
浸漬し始める濾過開始点方向に湾曲流路に沿って運び、
改めて粗いパルプ繊維や粗大浮遊物が付着したフィルタ
ーによって濾過することができ、濾過終了点でのパルプ
短繊維や微細浮遊物の溜りを解消することができる。
[0015] Also, from the filtration end point, a side stream is generated in the same direction as the rotational direction of the drum, and pulp short fibers and fine suspended matter remaining without being attached near the filtration end point are removed from the drum. The filter is carried along a curved flow path in the direction of the filtration start point where the filter begins to be immersed from above the surface of the stock solution to the surface of the stock solution,
Filtration can be performed again using a filter to which coarse pulp fibers and coarse suspended matter have adhered, and accumulation of short pulp fibers and fine suspended matter at the end of filtration can be eliminated.

【0016】更に好ましくは、前記ノズル手段が水頭に
応じてノズル開口断面積を変化させる可変ノズルを含む
ものでは、原液の流入圧力や原液水面の変化によって生
じる水頭に応じて可変ノズルの開口断面積が変化するの
で、流入量及び流入速度が変更でき、最適な運転条件で
運転でき、広範囲の原液の組成にも対応できる。尚、後
述する実施例中では、この可変ノズルは金属製の板バネ
機構を有した板ノズルであるが、その他の機構として、
任意の開口断面積を設定できるように、板ノズルに開閉
手段を備えた機構としてもよい。
More preferably, when the nozzle means includes a variable nozzle that changes the nozzle opening cross-sectional area according to the water head, the opening cross-sectional area of the variable nozzle can be adjusted according to the water head caused by the inflow pressure of the stock solution or the change in the water level of the stock solution. Since the flow rate changes, the inflow amount and inflow speed can be changed, operation can be performed under optimal operating conditions, and a wide range of stock solution compositions can be accommodated. In the examples described later, the variable nozzle is a plate nozzle having a metal plate spring mechanism, but other mechanisms include:
A mechanism may be used in which the plate nozzle is provided with an opening/closing means so that an arbitrary opening cross-sectional area can be set.

【0017】[0017]

【実施例】図1は本発明の一実施例の構成を示す説明図
である。図2は本発明の別の実施例の構成を示した説明
図である。図3は処理槽の内部の構成を示す説明図であ
る。図1、図2及び図3において、同一符号は同一また
は相当部分を示す。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an explanatory diagram showing the structure of an embodiment of the present invention. FIG. 2 is an explanatory diagram showing the configuration of another embodiment of the present invention. FIG. 3 is an explanatory diagram showing the internal configuration of the processing tank. In FIG. 1, FIG. 2, and FIG. 3, the same reference numerals indicate the same or corresponding parts.

【0018】各々の図に示す通り、原液流入口25から
流入された原液20を保持した処理槽21には、周面に
メッシュ度が大なる金網製フィルターの一部を浸漬した
ドラムフィルター28がモーター30によって矢印方向
に回転するように設置されている。ドラムフィルター2
8内部には、濾液排出口32が設けられており、フィル
ターを通過した処理水31が暫時移送され、原液20の
液面よりも低位の処理水液面を保持するようになってい
る。
As shown in each figure, a drum filter 28 in which a part of a wire mesh filter with a large mesh degree is immersed on the circumferential surface is installed in the processing tank 21 that holds the stock solution 20 that has flowed in from the stock solution inlet 25. It is installed so as to be rotated in the direction of the arrow by a motor 30. drum filter 2
A filtrate discharge port 32 is provided inside the filter 8, and the treated water 31 that has passed through the filter is temporarily transferred to maintain the treated water level lower than the liquid level of the stock solution 20.

【0019】処理槽21の底面及び内側面は、ドラムフ
ィルター28の周面に沿って湾曲し、処理槽21の湾曲
面26とドラムフィルター28の周面とで構成された湾
曲流路22を形成する。また、処理槽21には導管27
で接続された液面検出管24を有する。
The bottom and inner surfaces of the processing tank 21 are curved along the circumferential surface of the drum filter 28 to form a curved flow path 22 composed of the curved surface 26 of the processing tank 21 and the circumferential surface of the drum filter 28. do. In addition, a conduit 27 is connected to the processing tank 21.
It has a liquid level detection tube 24 connected with.

【0020】原液流入口25は、ドラムフィルター28
が原液表面から液面上方へ脱離する地点である濾過終了
点Aの近傍の処理槽21壁面に形成され、この原液流入
口25の上部を覆い下方に延びた金属製の板ノズル23
が処理槽21のほぼ長手方向に全長に渡って着脱可能に
設けられている。この板ノズル23は、原液の流入圧力
や原液水面の変化によって生じる水頭に応じて板ノズル
23の開口断面積が変化する板バネ状に構成されている
。尚、板ノズル23の上部には幾つかのエアー抜き37
が設けられており、板ノズル23内部にエアが溜った場
合にここで抜くようになっている。板ノズル23は処理
槽21の長手方向のほぼ全長に渡って形成されているた
め、ドラムフィルター28に均一に原液を供給すること
ができ、ドラムフィルター28に付着する固形浮遊物が
均一になり、後述する剥離ロール34への剥離が良好に
行なうことができる。
The raw solution inlet 25 is connected to a drum filter 28.
A metal plate nozzle 23 is formed on the wall surface of the processing tank 21 in the vicinity of the filtration end point A, which is the point at which the undiluted solution is desorbed from the undiluted solution surface above the liquid surface, and covers the upper part of this undiluted solution inlet 25 and extends downward.
is removably provided along almost the entire length of the processing tank 21 in the longitudinal direction. This plate nozzle 23 is configured in the shape of a plate spring whose opening cross-sectional area changes according to the water head generated by the inflow pressure of the stock solution or the change in the water level of the stock solution. In addition, there are several air vents 37 at the top of the plate nozzle 23.
is provided so that if air accumulates inside the plate nozzle 23, it can be removed here. Since the plate nozzle 23 is formed over almost the entire length in the longitudinal direction of the processing tank 21, it is possible to uniformly supply the stock solution to the drum filter 28, and the solid suspended matter adhering to the drum filter 28 becomes uniform. Peeling onto a peeling roll 34, which will be described later, can be performed satisfactorily.

【0021】ところで、ドラムフィルター28において
、付着物の付着力(吸引力)はドラム内外の圧力差によ
るものであるため、最も付着力(吸引力)が高い領域は
、ドラム内部の処理水の液面以下の領域である。本装置
では流入口25より送られた原水20は板ノズル23に
よって下方に導かれる。下方に導かれた原液は処理槽2
1の湾曲状の湾曲流路22に沿って流動し、ドラムフィ
ルター28が原液の上方から原液面20に浸漬し始める
地点である濾過開始地点B方向に導かれる。即ち、板ノ
ズル23から排出された原液は、前述の通り付着力(吸
引力)が最も高い領域を最初に通るため、原液中の粗い
繊維のパルプや粗大浮遊物及びパルプ短繊維や微細浮遊
物等の固形浮遊物が効率よく付着する。
By the way, in the drum filter 28, since the adhesion force (suction force) of deposits is due to the pressure difference between the inside and outside of the drum, the region with the highest adhesion force (suction force) is the liquid of the treated water inside the drum. The area is below the surface. In this device, raw water 20 sent from an inlet 25 is guided downward by a plate nozzle 23. The undiluted solution led downward is processed into treatment tank 2.
The liquid flows along one curved curved channel 22 and is guided toward a filtration start point B, which is the point where the drum filter 28 starts to be immersed in the raw liquid surface 20 from above the raw liquid. That is, since the stock solution discharged from the plate nozzle 23 first passes through the area where the adhesion force (suction force) is highest as described above, the pulp of coarse fibers, coarse suspended matter, pulp short fibers, and fine suspended matter in the stock solution are removed. etc., solid suspended matter adheres efficiently.

【0022】固形浮遊物の多くが付着して取り除かれた
原液は、濾過開始地点B近傍に到達し、ここで先ず粗い
繊維のパルプや粗大浮遊物がドラムフィルタ28のメッ
シュ度が大なる網に付着して、フィルターのメッシュ度
を小さくする。この後に、パルプ短繊維や微細浮遊物が
フィルターに付着する。前述の付着力(吸引力)が最も
高い領域を過ぎたドラムフィルター28は濾過終了点A
を過ぎて、原液水面上に至る。
The raw solution with most of the solid suspended matter attached and removed reaches the vicinity of the filtration start point B, where the coarse fiber pulp and coarse suspended matter are first filtered through the mesh of the drum filter 28 with a large mesh degree. It adheres to the filter and reduces the mesh size of the filter. After this, short pulp fibers and fine suspended matter adhere to the filter. The drum filter 28 that has passed the region where the adhesion force (suction force) is the highest is the filtration end point A.
The undiluted solution reaches the surface of the water.

【0023】ドラムフィルター28の外周面に付着した
パルプ等の固形浮遊物は、水面上においてドラムフィル
ターと接触している剥離ロール34に乗り移り、ドラム
フィルター28から除去される。そして剥離ロール34
に付着したパルプ等の固形浮遊物はロールの先端に設け
られた掻取ナイフ35によって除去されて、受けドクタ
ー33から排出される。剥離ロール34との接触によっ
て、パルプ繊維や粒子等の付着物が除去されたドラムフ
ィルター28のその部分は、その回転につれ再び原液内
へと入ってゆく。尚、ドラムフィルター28の上部には
シャワー29が設けられており、ドラムフィルター28
の目詰まりを防止する。
Solid suspended matter such as pulp adhering to the outer peripheral surface of the drum filter 28 is transferred to the peeling roll 34 that is in contact with the drum filter on the water surface and is removed from the drum filter 28. and peeling roll 34
Solid floating matter such as pulp adhering to the roll is removed by a scraping knife 35 provided at the tip of the roll and discharged from the receiving doctor 33. As the drum filter 28 rotates, that portion of the drum filter 28 from which deposits such as pulp fibers and particles have been removed by contact with the stripping roll 34 enters the raw solution again. A shower 29 is provided above the drum filter 28, and the drum filter 28
prevent clogging.

【0024】ところで、前述のように、ドラムフィルタ
ー28周面での原液中のパルプ繊維や浮遊物の付着力は
、ドラム内外の圧力差によるものであるため、付着力が
最も高い領域は処理水の水面以下の領域であり、ドラム
フィルターが原液より脱離する濾過終了点Aに近付くに
つれて水圧が下がるために付着力(吸引力)が低下し、
パルプ短繊維や微細浮遊物が付着されずに残ったり、ま
た一旦付着したパルプ短繊維や微細浮遊物が脱離したり
して、ドラムフィルター28の濾過終了点Aでパルプ短
繊維や微細浮遊物の溜りが形成されるが、板ノズル23
によって下方に導かれた水流により、同方向に沿った副
流が発生し、濾過終了点A近傍で付着されずに残ったパ
ルプ短繊維や微細浮遊物をドラムフィルターが原液液面
上方から原液表面へ浸漬し始める濾過開始点方向に湾曲
流路に沿って運び、改めて粗いパルプ繊維や粗大浮遊物
が付着したフィルターによって濾過することができ、濾
過終了点でのパルプ短繊維や微細浮遊物の溜りを解消す
ることができる。
By the way, as mentioned above, the adhesion force of pulp fibers and suspended matter in the raw solution on the peripheral surface of the drum filter 28 is due to the pressure difference between the inside and outside of the drum, so the area with the highest adhesion force is the treated water. As the drum filter approaches the filtration end point A where it separates from the stock solution, the water pressure decreases and the adhesion (suction force) decreases.
Pulp short fibers and fine suspended matter may remain unattached, or pulp short fibers and fine suspended matter once attached may be detached, and pulp short fibers and fine suspended matter may be removed at the filtration end point A of the drum filter 28. Although a pool is formed, the plate nozzle 23
The water flow guided downward by the drum filter generates a side flow along the same direction, and the drum filter removes pulp short fibers and fine suspended matter that remain unattached near the filtration end point A from above the undiluted liquid surface to the undiluted solution surface. It can be carried along a curved flow path in the direction of the filtration start point where it begins to be immersed, and then filtered again through a filter to which coarse pulp fibers and coarse suspended matter are attached. can be resolved.

【0025】更に、板ノズル23が着脱自在であり、処
理槽21内部には特別な突設や二重の被覆がないため、
処理槽21の洗浄が容易となった。原液のロット毎に固
形浮遊物の回収を変更する場合には、容易に先行の原液
を廃棄して洗浄し、新たなロットの原液を流入して処理
しても、先行の原液の固形浮遊物が混入しない特徴も有
している。また、付着量が増えてドラムフィルター28
の濾過能力が下がると処理槽11内の液面は上昇するの
で、この液面を液面検出室14及び検出器36で調べ、
この結果をモーター20へ送り、ドラムフィルター28
の回転速度を調整する。だけでなく、板バネ機構の板ノ
ズルによって、原液の流入圧力や原液水面の変化によっ
て生じる水頭に応じて可変ノズルの開口断面積が変化す
るので、流入量及び流入速度が変更でき、最適な運転条
件で運転でき、広範囲の原液の組成にも対応できる。
Furthermore, since the plate nozzle 23 is removable and there is no special protrusion or double coating inside the processing tank 21,
Cleaning of the processing tank 21 has become easier. When changing the collection of solid suspended solids for each lot of stock solution, it is easy to dispose of the previous stock solution and wash it, and even if the stock solution of a new lot is introduced and processed, the solid suspended solids of the previous stock solution can be removed. It also has the feature of not being contaminated. In addition, the amount of adhesion increases and the drum filter 28
When the filtration capacity of the processing tank 11 decreases, the liquid level in the processing tank 11 rises, so this liquid level is checked by the liquid level detection chamber 14 and the detector 36,
This result is sent to the motor 20 and the drum filter 28
Adjust the rotation speed. In addition, the plate nozzle with a plate spring mechanism changes the opening cross-sectional area of the variable nozzle in accordance with the inflow pressure of the undiluted solution and the water head caused by changes in the undiluted solution water level, so the inflow volume and speed can be changed to achieve optimal operation. It can be operated under various conditions and can handle a wide range of stock solution compositions.

【0026】[0026]

【発明の効果】本発明は以上説明したとおり、処理槽の
底面がドラムフィルターの周面に沿った湾曲流路を形成
し;原液流入口が、前記ドラムフィルターが前記原液表
面から液面上方へ脱離する濾過終了点近傍位置で前記湾
曲流路に連通して設けられ;前記原液流入口には、前記
濾過終了点から前記湾曲流路に沿ってドラムの回転方向
と逆向きに原液の流れを発生させるノズル手段が付設さ
れているものであるため、原液中のパルプ繊維や浮遊物
等がフィルターの孔を通過する際にフィルター孔に引っ
掛かり易くなり、加えて、原液中のパルプ繊維や浮遊物
の付着力(吸引力)が最も高い領域である処理水の水面
以下の領域に、ノズル手段から流入される原液が導かれ
るため、効率のよい付着を行うことができ、簡略な構造
で良好な処理能が得られる。
[Effects of the Invention] As explained above, in the present invention, the bottom surface of the processing tank forms a curved flow path along the circumferential surface of the drum filter; Provided in communication with the curved flow path at a position near the filtration end point where desorption occurs; the stock solution inlet is provided with a flow of the stock solution from the filtration end point along the curved flow path in a direction opposite to the rotational direction of the drum. Since the filter is equipped with a nozzle means that generates Since the raw solution flowing from the nozzle means is guided to the area below the surface of the treated water, where the adhesion force (suction force) of objects is highest, efficient adhesion can be achieved, and the simple structure makes it easy to use. processing performance can be obtained.

【0027】また、濾過終了点からドラムの回転方向と
逆向きの流れにより同方向に沿った副流が発生し、濾過
終了点近傍で付着されずに残ったパルプ短繊維や微細浮
遊物をドラムフィルターが原液液面上方から原液表面へ
浸漬し始める濾過開始点方向に湾曲流路に沿って運び、
改めて粗いパルプ繊維や粗大浮遊物が付着したフィルタ
ーによって濾過することができ、濾過終了点でのパルプ
短繊維や微細浮遊物の溜りを解消することができるとい
う効果がある。
[0027] Further, from the filtration end point, a side stream is generated in the same direction as the rotation direction of the drum, and pulp short fibers and fine suspended matter remaining without being attached near the filtration end point are removed from the drum. The filter is carried along a curved flow path in the direction of the filtration start point where the filter begins to be immersed from above the surface of the stock solution to the surface of the stock solution,
It is possible to perform filtration again using a filter to which coarse pulp fibers and coarse suspended matter have adhered, and there is an effect that accumulation of short pulp fibers and fine suspended matter at the end of filtration can be eliminated.

【図面の簡単な説明】[Brief explanation of drawings]

【図1】本発明の一実施例の構成を示す説明図である。FIG. 1 is an explanatory diagram showing the configuration of an embodiment of the present invention.

【図2】本発明の別の実施例の構成を示した説明図であ
る。
FIG. 2 is an explanatory diagram showing the configuration of another embodiment of the present invention.

【図3】図1又は図2の処理槽の内部の構成を示す説明
図である。
FIG. 3 is an explanatory diagram showing the internal configuration of the processing tank shown in FIG. 1 or 2. FIG.

【図4】従来のドラムフィルター式濾過処理装置の構成
を示す説明図である。
FIG. 4 is an explanatory diagram showing the configuration of a conventional drum filter type filtration processing device.

【符号の説明】[Explanation of symbols]

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】  原液流入口から流入される原液を収容
する処理槽内に周面フィルターの一部が原液表面から露
出するように浸漬された回転駆動式のドラムフィルター
と、該ドラムフィルター内部の濾液を外部へ排出する濾
液排出手段とを備え、前記処理槽中の原液が回動するド
ラムフィルターの周面フィルターを通過する際に前記周
面フィルター表面に付着した濾過残渣をドラムフィルタ
ーの回転方向下流の水面上位置で連続的に掻き取るよう
に構成したドラムフィルター式濾過処理装置において、
前記処理槽の底面が、前記ドラムフィルターの周面に沿
った湾曲流路を形成し、前記原液流入口が、前記ドラム
フィルターが前記原液表面から液面上方へ脱離する濾過
終了点近傍位置で前記湾曲流路に連通して設けられ、前
記原液流入口には、前記濾過終了点から前記湾曲流路に
沿ってドラムの回転方向と逆向きに原液の流れを発生さ
せるノズル手段が付設されていることを特徴とするドラ
ムフィルター式濾過処理装置。
1. A rotatably driven drum filter immersed in a processing tank containing a raw solution flowing in from a raw solution inlet so that a part of the peripheral filter is exposed from the surface of the raw solution, and and a filtrate discharge means for discharging the filtrate to the outside, when the raw solution in the treatment tank passes through the peripheral filter of the rotating drum filter, the filter residue attached to the surface of the peripheral filter is removed in the rotation direction of the drum filter. In a drum filter type filtration treatment device configured to continuously scrape water at a downstream position above the water surface,
The bottom surface of the processing tank forms a curved flow path along the circumferential surface of the drum filter, and the stock solution inlet is located at a position near the filtration end point where the drum filter is detached from the surface of the stock solution above the liquid surface. A nozzle means is provided in communication with the curved channel, and the stock solution inlet is provided with a nozzle means for generating a flow of the stock solution from the filtration end point along the curved channel in a direction opposite to the rotational direction of the drum. A drum filter type filtration device characterized by:
【請求項2】  前記請求項1に記載のドラムフィルタ
ー式濾過処理装置において、前記ノズル手段が水頭に応
じてノズル開口断面積を変化させる可変ノズルを含むこ
とを特徴とするドラムフィルター式濾過処理装置。
2. The drum filter type filtration treatment apparatus according to claim 1, wherein the nozzle means includes a variable nozzle that changes a nozzle opening cross-sectional area according to the water head. .
JP15984291A 1991-06-05 1991-06-05 Drum filter type filter device Pending JPH04358509A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15984291A JPH04358509A (en) 1991-06-05 1991-06-05 Drum filter type filter device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15984291A JPH04358509A (en) 1991-06-05 1991-06-05 Drum filter type filter device

Publications (1)

Publication Number Publication Date
JPH04358509A true JPH04358509A (en) 1992-12-11

Family

ID=15702431

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15984291A Pending JPH04358509A (en) 1991-06-05 1991-06-05 Drum filter type filter device

Country Status (1)

Country Link
JP (1) JPH04358509A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011041923A (en) * 2009-08-24 2011-03-03 Fujita Corp Solid-liquid separator and solid-liquid separation method by precoat rotary drum
JP2011167871A (en) * 2010-02-17 2011-09-01 Fujita Corp Method of manufacturing wood-based fine fiber material and method of forming woody formed article using this material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011041923A (en) * 2009-08-24 2011-03-03 Fujita Corp Solid-liquid separator and solid-liquid separation method by precoat rotary drum
JP2011167871A (en) * 2010-02-17 2011-09-01 Fujita Corp Method of manufacturing wood-based fine fiber material and method of forming woody formed article using this material

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