JPS61127000A - Slit roller type dehydrating device - Google Patents
Slit roller type dehydrating deviceInfo
- Publication number
- JPS61127000A JPS61127000A JP59248495A JP24849584A JPS61127000A JP S61127000 A JPS61127000 A JP S61127000A JP 59248495 A JP59248495 A JP 59248495A JP 24849584 A JP24849584 A JP 24849584A JP S61127000 A JPS61127000 A JP S61127000A
- Authority
- JP
- Japan
- Prior art keywords
- slit
- rollers
- rows
- roller
- slit roller
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/20—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using rotary pressing members, other than worms or screws, e.g. rollers, rings, discs
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は産業廃水や下水中の汚泥の脱水、パルプの脱水
等に用いられるスリットローラ式脱水装置に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a slit roller dewatering device used for dewatering sludge in industrial wastewater or sewage, dewatering pulp, and the like.
(従来の技術)
産業廃水や下水中の汚泥の脱水、パルプの脱水等には従
来から真空脱水機、フィルタープレス、ベルトプレス等
の各種の脱水機が使用されているが、これらの脱水機は
いずれも装置が大きく構造が複雑であるうえ、濾布を使
用しているのでその目詰りによる濾過速度の低下を避け
るために頻繁に濾布を取替えなければならない欠点があ
り、従ってイニシャルコスト及びランニングコストが高
いものとなる通弊があった。一方、濾布を使用しない脱
水機としてtよ、特公昭53−34346号公報に示さ
れるように多数の円板状の濾板とスペーサとを交互に積
層した渡体を隣接する渡体の濾板の先端が互いに突入す
る状態で噛み合わせて渡体列となし、各減俸を同一方向
に回転させつつ被処理物の濾過を行わせるようにしたも
のが知られている。しかしこの脱水機は薄い濾板を多数
枚積層した渡体を用いるものであるから部品数が膨大で
組立や分解に多くの時間を要し、イニシャルコストが高
価であるうえメンテナンスが困難である欠点をもつもの
であった。(Conventional technology) Various dehydrators such as vacuum dehydrators, filter presses, and belt presses have been used to dehydrate sludge in industrial wastewater and sewage, dehydrate pulp, etc. In both cases, the device is large and has a complicated structure, and since it uses a filter cloth, it has the disadvantage that the filter cloth must be replaced frequently to avoid a decrease in filtration speed due to clogging, which reduces the initial cost and running time. There was a drawback that the cost was high. On the other hand, as a dehydrator that does not use a filter cloth, as shown in Japanese Patent Publication No. 53-34346, a cross body consisting of a large number of disk-shaped filter plates and spacers stacked alternately is used to filter the filter between adjacent cross bodies. It is known that the tips of the plates are interlocked with each other so as to protrude into each other to form a transfer body row, and each plate is rotated in the same direction to filter the material to be processed. However, since this dehydrator uses a body made of a large number of laminated thin filter plates, it has a large number of parts, requires a lot of time to assemble and disassemble, has high initial costs, and is difficult to maintain. It had a
(発明が解決しようとする問題点)
本発明は上記のような従来の問題点を解消し、構造簡単
にして目詰りがなく、組立、分解が容易で安価に製作す
ることができ、しかも故障の虞れがほとんどない脱水機
を目的として完成されたものである。(Problems to be Solved by the Invention) The present invention solves the above-mentioned conventional problems, has a simple structure, is free from clogging, is easy to assemble and disassemble, can be manufactured at low cost, and is free from failures. It was completed with the aim of creating a dehydrator with almost no risk of damage.
(問題点を解決するための手段)
本発明は表面に濾液が通過する微細なスリットを多数透
設した複数本の中空のスリットローラを相互間に微細な
間隙を設けて上下2列に並設するとともに、各スリット
ローラを同一送り方向へ回転させるようにしたことを特
徴とするものである(実施例)
以下に本発明を図示の実施例について詳細に説明すると
、(1)は濾過室、(2)は該濾過室(1)の内部に上
下2列に並設された複数本の中空のスリットローラであ
り、各スリットローラ(2)は薄肉鋼板からなるもので
、第2図に・示されるように表面に濾液が通過する微細
なスリット(3)を多数透設したものである。本実施例
のスリットローラ(2)は長孔のパンチングメタルを長
孔の長手方向が軸方向となるように巻いて製作したもの
であるが、スリット(3)の形状は丸孔であってもよく
、またワイヤーを巻いてスリットローラとしたものや円
板の周面に多数のバーを並べてスリットローラとしたも
のを用いてもよい、。各スリットローラ(2)は相互間
に汚泥等が落下しない程度の微細な間隙を設けて濾過室
(1)の入口(4)から出口(5)に向ってやや上り勾
配に並設されており、上下の各スリットローラ(2)を
千鳥配列とするとともに上下の間隔を出口(5)に向か
うにつれて次第に狭くなるようにすることが好ましい。(Means for Solving the Problems) The present invention provides a plurality of hollow slit rollers each having a large number of fine slits on the surface through which the filtrate passes, which are arranged in two rows, one above the other, with minute gaps between them. At the same time, each slit roller is rotated in the same feeding direction (Embodiment) The present invention will be described in detail below with reference to the illustrated embodiment. (1) is a filtration chamber; (2) is a plurality of hollow slit rollers arranged in two rows vertically inside the filtration chamber (1), and each slit roller (2) is made of a thin steel plate. As shown, the surface has many fine slits (3) through which the filtrate passes. The slit roller (2) of this example is made by winding a punched metal with long holes so that the longitudinal direction of the holes is in the axial direction, but the shape of the slits (3) may be round holes. Alternatively, a slit roller made by winding a wire or a slit roller made by arranging a large number of bars around the circumference of a disk may also be used. Each slit roller (2) is arranged in parallel with a slight upward slope from the entrance (4) to the exit (5) of the filtration chamber (1), with a fine gap between them to prevent sludge from falling. It is preferable that the upper and lower slit rollers (2) are arranged in a staggered manner, and that the interval between the upper and lower parts becomes gradually narrower toward the exit (5).
第2図に示されるように、各スリットローラ(2)は濾
過室(1)の側壁に軸受(6)、(7)をもって軸支さ
れており、軸受(6)の外側のスプロケット(814q
チエーン(9)を掛は回したうえで人口(4)側のスリ
ットローラ(2)を駆動モータ(10)に接続して時計
方向に回転させることにより、各スリットローラ(2)
は同一送り方向、即ち上側のスリットローラ(2)は時
計方向に下側のスリットローラ(2)は反時計方向に等
速度で回転されるようになっている。各スリットローラ
(2)はその片側の端面(11)に多数の透孔(12)
を備え、濾過室(1)の対応する側壁にも同様の透孔(
13)が透設されているので、スリット(3)からスリ
ットローラ(2)の内部へ入った濾液は透孔(12)、
透孔(13)を経て濾液排出管(14)から外部へ排出
されることとなる。なお、(15)は濾過室(1)の入
口(4)に先端がスリットローラ(2)に達するように
設けられた投入シュート、(16)は濾過室(11の出
口(5)に同様に設けられた排出シュートである。As shown in Fig. 2, each slit roller (2) is supported by bearings (6) and (7) on the side wall of the filtration chamber (1), and the sprocket (814q) on the outside of the bearing (6)
After rotating the chain (9), connect the slit roller (2) on the population (4) side to the drive motor (10) and rotate it clockwise, each slit roller (2)
are rotated in the same feeding direction, that is, the upper slit roller (2) is rotated clockwise and the lower slit roller (2) is rotated counterclockwise at a constant speed. Each slit roller (2) has a large number of through holes (12) in its one end surface (11).
, and a similar through hole (
13), the filtrate entering the slit roller (2) from the slit (3) passes through the through hole (12).
The filtrate is discharged to the outside from the filtrate discharge pipe (14) through the through hole (13). In addition, (15) is a feeding chute provided at the entrance (4) of the filtration chamber (1) so that its tip reaches the slit roller (2), and (16) is a chute provided similarly at the outlet (5) of the filtration chamber (11). A discharge chute is provided.
(作用)
このように構成されたものは、各スリットローラ(2)
を駆動モータ(10)により同一送り方向に回転させつ
つ濾過室(1)の入口(4)の投入シュート(15)か
ら下水汚泥等の被処理物を投入すれば、被処理物は中空
のスリットローラ(2)の表面に多数透設された微細な
スリット(3)上で重力濾過されたうえ上下のスリット
ローラ(2)、(2)間を加圧されつつジグザグ状に進
行し、徐々に脱水される。このとき、スリットローラ(
2)、(2)の相互間の間隙は微細であるので濾液のみ
が流出し、汚泥等の被処理物は流出することなく次のス
リ・ノドローラ(2)によって移送方向を上向きに変え
られるとともに大きい剪断効果を受けて脱水が促進され
ることとなる。また図示のように上下のスリットローラ
(2)の間隔を送り方向に向って徐々に狭くなるように
配置したものは、出口(5)に向って徐々に圧力が高ま
るためにより優れた脱水効果が得られ、またスリットロ
ーラ(2)を出口(5)に向って上り勾配に配置したも
のは脱水されたケーキに濾液が再吸収されることがない
利点がある。このように被処理物はスリットローラ(2
)、(2)間の間隔が小さい部分で圧力を受け、その中
間部では低圧となって水分の均一化が進行するので、全
体が均一に脱水されたうえ、脱水ケーキとして出口(5
)の排出シュート(16)から排出されることとなる。(Function) In this configuration, each slit roller (2)
If the material to be treated, such as sewage sludge, is input through the input chute (15) at the entrance (4) of the filtration chamber (1) while rotating in the same feeding direction by the drive motor (10), the material to be treated will flow through the hollow slit. It is filtered by gravity on the fine slits (3) made in large numbers on the surface of the roller (2), and then progresses in a zigzag pattern while being pressurized between the upper and lower slit rollers (2), and gradually Dehydrated. At this time, the slit roller (
2) Since the gap between 2) and (2) is minute, only the filtrate flows out, and the material to be treated such as sludge does not flow out, and the transfer direction can be changed upward by the next pickpocket roller (2). Dehydration is accelerated by the large shearing effect. In addition, as shown in the figure, if the distance between the upper and lower slit rollers (2) is arranged so that it gradually narrows in the feeding direction, the pressure gradually increases toward the outlet (5), resulting in a better dewatering effect. The slit roller (2) arranged upwardly toward the outlet (5) has the advantage that the filtrate is not reabsorbed into the dewatered cake. In this way, the object to be processed is transferred to the slit roller (2
) and (2), the pressure is applied to the part with a small gap between them, and the pressure is low in the middle part, and the water becomes uniform, so that the entire area is uniformly dehydrated, and a dehydrated cake is delivered to the outlet (5).
) will be discharged from the discharge chute (16).
濾過水はスリット(3)からスリットローラ(2)の内
部に入り、透孔(12)、透孔(13)、濾液排出管(
14)から外部へ排出されるが、下面のスリフト(3)
から下方へ排出させるようにしてもよい(発明の効果)
本発明は以上の説明からも明らかなように、中空のスリ
ットローラを相互間に微細な間隙を設けて2列に並設し
たものであり一1従来の多数の濾板を積層させたものと
は異なり構造簡単にして分解、組立が容易であるうえ、
濾布を使用しないので目詰りの虞れがな(、安価にして
故障の處れもないものである。よって本発明は従来の問
題点を解消したものとして産業の発展に寄与するところ
極めて大である。The filtered water enters the slit roller (2) through the slit (3), passes through the through hole (12), through hole (13), and through the filtrate discharge pipe (
14) to the outside, but the lower thrift (3)
(Effects of the Invention) As is clear from the above description, the present invention is a system in which hollow slit rollers are arranged in two rows with a fine gap between them. 1. Unlike the conventional filter plates that stack many filter plates, it has a simple structure and is easy to disassemble and assemble.
Since it does not use a filter cloth, there is no risk of clogging (and it is inexpensive and has no risk of failure. Therefore, the present invention contributes to the development of industry to a great extent as it solves the conventional problems. It is.
第1図は本発明の実施例を示す一部切欠正面図第2図は
同じく一部切欠側面図である。
(2)ニスリットローラ、(3)ニスリット、(10)
:駆動モータ。
しく二2ノFIG. 1 is a partially cutaway front view showing an embodiment of the present invention, and FIG. 2 is a partially cutaway side view. (2) Nislit roller, (3) Nislit, (10)
: Drive motor. Shikaku22no
Claims (1)
透設した複数本の中空のスリットローラ(2)を相互間
に微細な間隙を設けて上下2列に並設するとともに、各
スリットローラ(2)を同一送り方向へ回転させるよう
にしたことを特徴とするスリットローラ式脱水装置。 2、スリットローラ(2)が被処理物の送り方向に向っ
て上り勾配に並設されたものである特許請求の範囲第1
項記載のスリットローラ式脱水装置。 3、上下2列に並設されたスリットローラ(2)の上下
の間隔が送り方向に向って次第に狭くなるよう配置され
たものである特許請求の範囲第1項または第2項記載の
スリットローラ式脱水装置。[Claims] 1. A plurality of hollow slit rollers (2) each having a large number of fine slits (3) on the surface through which the filtrate passes are arranged in two rows, one above the other, with minute gaps between them. A slit roller type dewatering device characterized in that the slit rollers (2) are rotated in the same feeding direction. 2. Claim 1, wherein the slit rollers (2) are arranged in parallel on an upward slope in the feeding direction of the processed material.
The slit roller dewatering device described in Section 1. 3. The slit roller according to claim 1 or 2, wherein the slit rollers (2) are arranged in two rows, one above the other, and the distance between the top and bottom becomes gradually narrower in the feeding direction. Type dehydration equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59248495A JPS61127000A (en) | 1984-11-24 | 1984-11-24 | Slit roller type dehydrating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59248495A JPS61127000A (en) | 1984-11-24 | 1984-11-24 | Slit roller type dehydrating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61127000A true JPS61127000A (en) | 1986-06-14 |
Family
ID=17179015
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59248495A Pending JPS61127000A (en) | 1984-11-24 | 1984-11-24 | Slit roller type dehydrating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61127000A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0490810A (en) * | 1990-08-02 | 1992-03-24 | Teera Bunri:Kk | Method and apparatus for filtering suspension |
JPH06121907A (en) * | 1992-10-12 | 1994-05-06 | Yanagawa Giken:Kk | Filter and filter device |
JPH07217833A (en) * | 1994-02-04 | 1995-08-18 | Kinsei Gan | Refuse incineration treating device |
FR2727647A1 (en) * | 1994-12-06 | 1996-06-07 | Chazelle Hubert | Continuous wine press assembly |
JP2014076418A (en) * | 2012-10-10 | 2014-05-01 | Tsurumi Mfg Co Ltd | Solid-liquid separation device |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS559277A (en) * | 1978-07-05 | 1980-01-23 | Fujitsu Ltd | Information processor |
JPS5627358A (en) * | 1979-08-14 | 1981-03-17 | Nippon Telegr & Teleph Corp <Ntt> | Printer |
-
1984
- 1984-11-24 JP JP59248495A patent/JPS61127000A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS559277A (en) * | 1978-07-05 | 1980-01-23 | Fujitsu Ltd | Information processor |
JPS5627358A (en) * | 1979-08-14 | 1981-03-17 | Nippon Telegr & Teleph Corp <Ntt> | Printer |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0490810A (en) * | 1990-08-02 | 1992-03-24 | Teera Bunri:Kk | Method and apparatus for filtering suspension |
JPH06121907A (en) * | 1992-10-12 | 1994-05-06 | Yanagawa Giken:Kk | Filter and filter device |
JPH07217833A (en) * | 1994-02-04 | 1995-08-18 | Kinsei Gan | Refuse incineration treating device |
FR2727647A1 (en) * | 1994-12-06 | 1996-06-07 | Chazelle Hubert | Continuous wine press assembly |
JP2014076418A (en) * | 2012-10-10 | 2014-05-01 | Tsurumi Mfg Co Ltd | Solid-liquid separation device |
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