JPS6117599B2 - - Google Patents

Info

Publication number
JPS6117599B2
JPS6117599B2 JP53080314A JP8031478A JPS6117599B2 JP S6117599 B2 JPS6117599 B2 JP S6117599B2 JP 53080314 A JP53080314 A JP 53080314A JP 8031478 A JP8031478 A JP 8031478A JP S6117599 B2 JPS6117599 B2 JP S6117599B2
Authority
JP
Japan
Prior art keywords
rotating drum
belt
cloth belt
pressure
section
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.)
Expired
Application number
JP53080314A
Other languages
Japanese (ja)
Other versions
JPS558812A (en
Inventor
Shoji Ito
Shiro Kondo
Kazuo Pponjo
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.)
Shinko Pfaudler Co Ltd
Original Assignee
Shinko Pfaudler Co Ltd
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 Shinko Pfaudler Co Ltd filed Critical Shinko Pfaudler Co Ltd
Priority to JP8031478A priority Critical patent/JPS558812A/en
Priority to US06/052,351 priority patent/US4260492A/en
Priority to DE19792926146 priority patent/DE2926146A1/en
Publication of JPS558812A publication Critical patent/JPS558812A/en
Publication of JPS6117599B2 publication Critical patent/JPS6117599B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/24Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band
    • B30B9/246The material being conveyed around a drum between pressing bands
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/22Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using a flexible member, e.g. diaphragm, urged by fluid pressure
    • B30B9/225Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using a flexible member, e.g. diaphragm, urged by fluid pressure the diaphragm being tubular

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明は主として産業廃水処理、下水処理等の
設備から排出される汚泥の連続脱水を目的とした
回転ドラム型の圧搾脱水装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a rotating drum-type press dewatering apparatus mainly intended for continuous dehydration of sludge discharged from equipment such as industrial wastewater treatment and sewage treatment.

前記の汚泥はその主成分が水酸化アルミニウム
あるいは生物処理工程から発生する余剰汚泥等で
ある場合が多く、脱水ケーキは通常その大部分が
水分であり、遠隔地に運搬して投棄する場合にお
ける取扱および輸送費の点、あるいは脱水ケーキ
をさらに乾燥、焼却する場合における燃料消費の
点でも問題があるため、脱水ケーキの含水率は脱
水工程において可能な限り低下させておくことが
望ましい。
The main component of the sludge mentioned above is often aluminum hydroxide or surplus sludge generated from biological treatment processes, and the dehydrated cake is usually mostly water, making it difficult to handle when transporting and dumping it to a remote location. There are also problems in terms of transportation costs and fuel consumption when the dehydrated cake is further dried and incinerated, so it is desirable to reduce the moisture content of the dehydrated cake as much as possible during the dehydration process.

これらの汚泥を対象とした脱水工程には各種の
方式が採用されており、中でもケーキ含水率低下
の点で最もすぐれているのはフイルタープレスで
代表される加圧圧搾方式であるが、この方式は操
作が回分的であることから処理量を確保するため
に、またケーキの剥離性を良くするためにケーキ
の厚みを大きくする必要があるため長い圧搾時間
を要する点と、回分操作に関係する多くの附属設
備を要し脱水工程が連続化しにくい点に弱点があ
る。
Various methods are used for the dehydration process for these sludges, and among them, the pressure-pressing method represented by the filter press is the most excellent in terms of reducing the moisture content of the cake. Since the operation is batchwise, it is necessary to increase the thickness of the cake in order to ensure the throughput and to improve the peelability of the cake, so it requires a long pressing time. The weak point is that it requires a lot of auxiliary equipment and it is difficult to make the dewatering process continuous.

一方、連続式脱水装置として真空脱水あるいは
遠心脱水方式によるものがあり現在最も広く使わ
れているが、前記汚泥を対象とした場合にはこれ
らの方式は到達含水率の点で限度がある。
On the other hand, as continuous dewatering devices, vacuum dewatering or centrifugal dewatering methods are currently most widely used, but these methods have a limit in terms of the moisture content that can be achieved when the target is the sludge.

また、装置の構成が最も単純で強力な圧搾圧力
が得られるものとした実公昭45−25717の如きベ
ルト式加圧脱水機があるが、ケーキの含水率低下
が主として圧搾圧力と圧搾時間とに起因すること
を考慮すると、圧搾圧力が圧搾部全域にわたつて
通過中のケーキに持続して作用せずローラーの当
り部に限定されるため有効圧搾時間が短かくなり
ケーキの含水率低下が不充分とる。そこでローラ
ーによる圧搾圧力を高くしてケーキの含水率を低
下させようとすると、特に汚泥の予備濃縮が不充
分な場合には最初のローラー部において汚泥が強
い圧搾圧力をうけて薄く広がる等の支障が生じて
有効な脱水ができなくなる問題があつた。
In addition, there is a belt-type pressure dewatering machine such as Utility Model Publication No. 45-25717, which has the simplest device configuration and can obtain powerful squeezing pressure, but the decrease in the moisture content of the cake is mainly due to the squeezing pressure and squeezing time. Considering this, the effective compression time is shortened and the moisture content of the cake does not decrease because the compression pressure does not continuously act on the cake passing through the entire compression area but is limited to the contact area of the rollers. Take enough. Therefore, if you try to lower the moisture content of the cake by increasing the squeezing pressure with the rollers, especially if the pre-concentration of the sludge is insufficient, the sludge will be subject to strong squeezing pressure at the first roller section, causing problems such as spreading thinly. There was a problem that dehydration could not be carried out effectively.

そこで、本発明はローラーによる局部的な圧搾
をなくし圧搾部全域にわたつてほぼ均一な圧搾圧
力が維持できるようにして有効圧搾時間を増加さ
せベルト式加圧脱水機における前記問題点を解消
することを目的としている。すなわち、ゴム等の
可撓性耐圧性材料でできた中空管を外周全面に接
着した回転ドラムに対して、多数の受けローラー
で支持された金網、キヤタピラー等の無伸縮性材
料でできた液の排出が可能なバツクアツプベル
トを外接させて張設し、圧力流体の導入により膨
脹した前記中空管とバツクアツプベルトとの間の
接触部全面にほぼ均一かつ連続した圧搾圧力を作
用させる長い圧搾部を形成させ、両者の間に布
ベルトと押え布ベルトとで挾持された汚泥を通過
させることにより圧搾部全域にわたつて有効な脱
水効果を発揮させるものである。
Therefore, the present invention solves the above-mentioned problems in belt-type pressurized dehydrators by eliminating localized squeezing by rollers and maintaining substantially uniform squeezing pressure over the entire squeezing area to increase the effective squeezing time. It is an object. In other words, a rotating drum made of a hollow tube made of a flexible pressure-resistant material such as rubber is glued to the entire outer periphery, and a liquid made of a non-stretchable material such as a wire mesh or a caterpillar supported by a number of receiving rollers is placed on the drum. A back-up belt capable of discharging water is stretched around the circumference, and a substantially uniform and continuous squeezing pressure is applied to the entire surface of the contact area between the hollow tube expanded by the introduction of pressure fluid and the back-up belt. By forming a pressing section and passing the sludge held between the cloth belt and the pressing cloth belt between the two, an effective dewatering effect can be exerted over the entire pressing section.

以下本発明になる連続式圧搾脱水装置の実施例
に関して図面に従つて説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Examples of the continuous compression dewatering apparatus according to the present invention will be described below with reference to the drawings.

回転ドラム1は円筒形でその中心の主軸2が両
側一対の機枠3,3に設けた軸受4,4により水
平状態に支承され、主軸上に設けたスプロケツト
5に対し原動部6からのチエーン7の巻掛により
回転駆動される。
The rotating drum 1 has a cylindrical shape, and a main shaft 2 at the center is supported horizontally by bearings 4, 4 provided on a pair of machine frames 3, 3 on both sides, and a chain from a driving part 6 is connected to a sprocket 5 provided on the main shaft. Rotationally driven by winding 7.

第1図の実施例において、回転ドラム1の外周
にはリブ8等によつて螺旋状に形成された受溝に
可撓性耐圧性の中空管9が嵌め込まれ、その両端
部が回転ドラムに固定されている。
In the embodiment shown in FIG. 1, a flexible pressure-resistant hollow tube 9 is fitted into a receiving groove spirally formed by ribs 8 etc. on the outer periphery of the rotating drum 1, and both ends of the hollow tube 9 are connected to the rotating drum. is fixed.

可撓性耐圧性の中空管は他の実施例、例えば第
3図に示すように複数の中空管9a,9aを回転
ドラム上に並列させて装着してもよく、また回転
ドラムの幅が狭い場合には第4図に示すように扁
平断面の中空管9bを一本装着しただけでもよ
い。
The flexible pressure-resistant hollow tubes may be arranged in other embodiments, for example, as shown in FIG. If the space is narrow, a single hollow tube 9b with a flat cross section may be installed as shown in FIG.

前記中空管9には圧力流体例えば圧縮空気が供
給源10からロータリージヨイント11、導圧管
2を経て導入され、装置の稼動中は一定圧力に保
持される。
Pressure fluid, such as compressed air, is introduced into the hollow tube 9 from a supply source 10 via a rotary joint 11 and a pressure guiding tube 2, and is maintained at a constant pressure during operation of the device.

中空管9を装着した前記回転ドラム1の下方外
周には第2図に示すように回転ドラム側より無端
の押え布ベルト13、無端の布ベルト14およ
び伸縮性がなく液の排出が可能な無端のバツク
アツプベルト15の順に重なるようにそれぞれ別
個に張設された無端帯群が巻掛されており、その
巻掛区間において無端帯群の外部には前記中空管
からの押圧力を受けるように回転ドラムの主軸に
対して平行な多数の受けローラー16,16…が
小間隔に配設され、各受けローラー16,16…
の両端部は前記機枠3,3に設けた軸受17,1
7により回転自在に支承されている。回転ドラム
1と各受けローラー16,16…との間隔は、第
2図に明らかなごとく、圧力液体の導入により膨
脹した前記中空管9の外周部が前記バツクアツプ
ベルト15に押圧されて変形し幅広でかつ事実上
連続した長弧状の接触面を形成するように配列
し、かくして回転ドラム1とバツクアツプベルト
15、布ベルト14、受けローラー16,16
…との間に前記巻掛区間の全域にわたつて連続的
な圧搾部を形成するのである。
As shown in FIG. 2, on the outer periphery of the lower part of the rotary drum 1 equipped with the hollow tube 9, there is an endless pressing cloth belt 13 and an endless cloth belt 14 from the rotary drum side, which are non-stretchable and allow liquid to be discharged. A group of endless belts stretched separately is wound around the endless back-up belt 15 so as to overlap in this order, and in the winding section, the outside of the group of endless bands receives a pressing force from the hollow tube. A large number of receiving rollers 16, 16... parallel to the main axis of the rotating drum are arranged at small intervals, and each receiving roller 16, 16...
Both ends of the bearings 17, 1 provided on the machine frames 3, 3
It is rotatably supported by 7. As is clear from FIG. 2, the distance between the rotating drum 1 and each of the receiving rollers 16, 16, . are arranged to form a wide and virtually continuous arc-shaped contact surface, thus connecting the rotating drum 1, the back-up belt 15, the cloth belt 14, and the receiving rollers 16, 16.
A continuous compressed portion is formed between the two parts over the entire area of the wrapping section.

送りローラー18,19により張設されたバツ
クアツプベルト15は回転ドラム1の駆動により
前記中空管9からの圧搾圧力をうけながら、それ
ぞれ引張調整用ローラー20,21により張設さ
れた押え布ベルト13と布ベルト14ともに中
空管外周の周速とほぼ等しい速度で前記圧搾部を
通過する。
The backup belt 15 stretched by the feed rollers 18 and 19 is compressed by the presser cloth belt stretched by the tension adjustment rollers 20 and 21, respectively, while receiving compression pressure from the hollow tube 9 by the drive of the rotating drum 1. Both the belt 13 and the cloth belt 14 pass through the pressing section at a speed approximately equal to the circumferential speed of the outer periphery of the hollow tube.

汚泥は供給部22から布ベルト14上に連続
供給され、ローラー23部で布ベルト14と押
え布ベルト13に挾持されて前記圧搾部を通過し
板状のケーキとなつて機外に排出され、押え布ベ
ルト13および布ベルト14上に付着残存した
ケーキはそれぞれ剥離ローラー24,25部にお
いてスクレーパー26,27により除去される。
28,29はそれぞれ押え布ベルト13および
布ベルト14に対する洗浄装置であり、30は洗
浄水受皿である。布ベルト側にはさらに、蛇行
防止ローラー31および布絞りローラー32が
設けられている。
The sludge is continuously supplied onto the cloth belt 14 from the supply section 22, is held between the cloth belt 14 and the pressing cloth belt 13 by the roller 23 section, passes through the pressing section, becomes a plate-shaped cake, and is discharged outside the machine. The cake remaining on the presser cloth belt 13 and cloth belt 14 is removed by scrapers 26 and 27 at peeling rollers 24 and 25, respectively.
28 and 29 are washing devices for the presser cloth belt 13 and the cloth belt 14, respectively, and 30 is a washing water receiver. Further, a meandering prevention roller 31 and a cloth squeezing roller 32 are provided on the cloth belt side.

以上の構成によつて、圧力流体が導入されて膨
脹した前記可撓性耐圧性の中空管9と、多数の受
けローラー16,16…によつて支持された伸縮
性のないバツクアツプベルト15との面接触によ
り、圧搾部全域にわたつてほぼ均一な圧搾圧力が
作用するため布ベルト14と押え布ベルト13
に挾持された汚泥が前記圧搾部を通過する際には
効率の良い脱水が可能となる。
With the above configuration, the flexible pressure-resistant hollow tube 9 expanded by introducing pressure fluid, and the non-stretchable back-up belt 15 supported by a large number of receiving rollers 16, 16... Due to the surface contact between the cloth belt 14 and the presser cloth belt 13, almost uniform pressing pressure is applied over the entire pressing section.
When the sludge held in the sludge passes through the pressing section, efficient dewatering becomes possible.

以上の説明から明らかなように、本発明になる
連続式圧搾脱水装置は圧搾部全域にわたつてほぼ
均一な圧搾効果が得られることから、従来のベル
ト式加圧脱水機と比較すると有効圧搾時間が増加
するため、脱水効率が向上してケーキの含水率を
より低下させることができるとともに、局部的に
強い圧搾力を受けることがないため供給される汚
泥の予備濃縮が最小限で済ますことができる。ま
た、フイルタープレス等の加圧圧搾方式と比較す
ると、本装置は押え布ベルトと布ベルトが剥離
ローラー部において屈曲するためケーキの剥離性
が良好である点と、連続式であるため処理量が確
保しやすい点とからケーキの厚みが小さくてよい
から比較的短時間、低圧力の圧搾でフイルタープ
レスによる場合と同程度のケーキ含水率が得られ
る等の効果があり、さらに本装置における可撓性
耐圧性の中空管は稼動中において常時加圧したま
までよいから圧搾部においてのみ圧力流体を供給
して加圧される区分圧搾ダイヤフラム方式と比較
すると、無端帯群の巻掛区間全域を有効圧搾部と
することができるとともに圧力流体の切換操作が
一切不要となるために処理効率の面、製作費用の
面および維持管理の面からの利点も注目すべきも
のがある。
As is clear from the above explanation, the continuous compression dehydrator according to the present invention can achieve a substantially uniform compression effect over the entire pressing section, so the effective compression time is shorter than that of the conventional belt-type pressure dehydrator. This increases the dewatering efficiency and lowers the moisture content of the cake, while also minimizing the need for pre-concentration of the supplied sludge as it is not subject to locally strong squeezing force. can. In addition, compared to pressure pressing methods such as filter presses, this device has good cake peeling properties because the presser cloth belt and cloth belt are bent at the peeling roller section, and the throughput is reduced because it is a continuous type. It is easy to secure the cake, and since the thickness of the cake is small, it has the advantage of being able to obtain the same moisture content of the cake as with a filter press in a relatively short time and at low pressure. The pressure-resistant hollow tube can be kept pressurized at all times during operation, so compared to the segmented compression diaphragm method in which pressure fluid is supplied and pressurized only in the compression section, the entire wrapped section of the endless band group can be It can be used as an effective compression section, and there is no need to switch the pressure fluid at all, so there are noteworthy advantages in terms of processing efficiency, manufacturing cost, and maintenance management.

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

第1図は本発明による連続式圧搾脱水装置の実
施例の縦断面図、第2図は横断面図、第3図およ
び第4図は回転ドラムの外周に装着する可撓性耐
圧性の中空管9の他の実施例9a,9a…および
9bの装着状態を示す部分断面図である。 図中、1は回転ドラム、2は主軸、3は機枠、
4は主軸用軸受、5はスプロケツト、6は原動
部、7はチエーン、8はリブ、9,9a,9bは
中空管、10は圧力流体供給源、11はロータリ
ージヨイント、12は導圧管、13は押え布ベル
ト、14は布ベルト、15はバツクアツプベル
ト、16は受けローラー、17は受けローラー用
軸受、18,19は送りローラー、20,21は
引張調整用ローラー、22は汚泥供給部、24,
25はケーキ剥離ローラー、26,27はスクレ
ーパー、28,29は洗浄装置、30は洗浄水受
皿、31は布蛇行防止ローラー、32は布絞
りローラーである。
Fig. 1 is a longitudinal sectional view of an embodiment of the continuous compression dewatering device according to the present invention, Fig. 2 is a cross sectional view, and Figs. It is a partial sectional view showing the mounting state of other Examples 9a, 9a... and 9b of the empty tube 9. In the figure, 1 is a rotating drum, 2 is a main shaft, 3 is a machine frame,
4 is a bearing for the main shaft, 5 is a sprocket, 6 is a driving part, 7 is a chain, 8 is a rib, 9, 9a, 9b are hollow tubes, 10 is a pressure fluid supply source, 11 is a rotary joint, 12 is a impulse tube , 13 is a presser cloth belt, 14 is a cloth belt, 15 is a backup belt, 16 is a receiving roller, 17 is a bearing for the receiving roller, 18 and 19 are feed rollers, 20 and 21 are tension adjustment rollers, and 22 is a sludge supply Part, 24,
25 is a cake peeling roller, 26 and 27 are scrapers, 28 and 29 are washing devices, 30 is a washing water tray, 31 is a cloth meandering prevention roller, and 32 is a cloth squeezing roller.

Claims (1)

【特許請求の範囲】[Claims] 1 主軸方向に並列させて外面全周に可撓性耐圧
性の中空管を装着した回転ドラムと、該回転ドラ
ム上の巻掛区間で回転ドラム側より押え布ベル
ト、布ベルトおよび無伸縮性で液の排出が可
能なバツクアツプベルトの順に重ねて外接するよ
うそれぞれ別個に張設してなる無綻帯群と、前記
無端帯群の巻掛区間におい膨脹した中空管の外周
部を前記無端帯群と協働して変形せしめ事実上連
続した長弧状の圧搾部を形成するように配列して
なる一連の受けローラと、によつて構成されたこ
とを特徴とする連続式圧搾装置。
1 A rotating drum equipped with flexible pressure-resistant hollow tubes arranged in parallel in the direction of the main axis and attached to the entire outer circumference, and a presser cloth belt, a cloth belt, and a non-stretchable material attached from the rotating drum side in the winding section on the rotating drum. A group of endless belts formed by back-up belts that are capable of draining liquid in order and stretched separately so as to circumscribe them, and an outer circumferential portion of a hollow tube expanded in the winding section of the endless belt group. 1. A continuous pressing device comprising a series of receiving rollers which are arranged to deform in cooperation with the endless bands and form a substantially continuous long arc-shaped pressing section.
JP8031478A 1978-07-01 1978-07-01 Continuous press dehydrator Granted JPS558812A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP8031478A JPS558812A (en) 1978-07-01 1978-07-01 Continuous press dehydrator
US06/052,351 US4260492A (en) 1978-07-01 1979-06-27 Rotary diaphragm press
DE19792926146 DE2926146A1 (en) 1978-07-01 1979-06-28 ROTATING MEMBRANE FILTER PRESS

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8031478A JPS558812A (en) 1978-07-01 1978-07-01 Continuous press dehydrator

Publications (2)

Publication Number Publication Date
JPS558812A JPS558812A (en) 1980-01-22
JPS6117599B2 true JPS6117599B2 (en) 1986-05-08

Family

ID=13714794

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8031478A Granted JPS558812A (en) 1978-07-01 1978-07-01 Continuous press dehydrator

Country Status (1)

Country Link
JP (1) JPS558812A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5693345A (en) * 1979-12-27 1981-07-28 Fujitsu Ltd Packing method of ceramic sealed-type semiconductor device
NL8003667A (en) * 1980-06-25 1982-01-18 Pannevis Bv Machf METHOD AND APPARATUS FOR REMOVING LIQUID FROM A MIXTURE OF LIQUID AND SOLID
JPH0412592Y2 (en) * 1986-03-24 1992-03-26

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JPS558812A (en) 1980-01-22

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