JPH0113887B2 - - Google Patents

Info

Publication number
JPH0113887B2
JPH0113887B2 JP56094141A JP9414181A JPH0113887B2 JP H0113887 B2 JPH0113887 B2 JP H0113887B2 JP 56094141 A JP56094141 A JP 56094141A JP 9414181 A JP9414181 A JP 9414181A JP H0113887 B2 JPH0113887 B2 JP H0113887B2
Authority
JP
Japan
Prior art keywords
roller
sludge
cloths
pressure
diaphragm
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
JP56094141A
Other languages
Japanese (ja)
Other versions
JPS57207516A (en
Inventor
Minoru Morita
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.)
Tsukishima Kikai Co Ltd
Original Assignee
Tsukishima Kikai 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 Tsukishima Kikai Co Ltd filed Critical Tsukishima Kikai Co Ltd
Priority to JP56094141A priority Critical patent/JPS57207516A/en
Publication of JPS57207516A publication Critical patent/JPS57207516A/en
Publication of JPH0113887B2 publication Critical patent/JPH0113887B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明はベルトプレス型脱水機に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a belt press type dehydrator.

例えば含水率の高いスラツジをそのまま廃棄処
理することは河川、海等を汚染することとなり、
公害発生防止の観点から下水スラツジの効果的な
処理が望まれている。
For example, if sludge with a high moisture content is disposed of as is, it will pollute rivers, oceans, etc.
Effective treatment of sewage sludge is desired from the viewpoint of preventing pollution.

通常はスラツジを加圧脱水し、焼却処理或は直
接廃棄するようにしているが、従来脱水機構とし
ては複数本のロールにより張力を与えられた二枚
の布の間に下水スラツジのような汚泥を挿入
し、布を同方向へ回転させることにより二枚の
布の圧縮圧力で汚泥を順次脱水する脱水機が広
く利用されている。このような脱水機の型式に
は、前記のように二枚の布の張力のみによるも
のと、ロールとロールを直接相対して接触させる
もの等がある。前者は比較的軟質な汚泥に対して
二枚の布の両側よりの汚泥のはみ出しを考慮し
ながら最大の張力を布にかけできるだけ最大の
圧力を汚泥に加えようとするもので、この際の操
業の限界は布に一定以上の張力を加えた場合に
布が破断する点にある。この限度は30Kg程度で
あり、この張力より得られるロール上の布への
圧力はロール直径にもよるがロール径100〜300mm
の場合2〜3Kg/cm2である。このような圧力に対
応して各種汚泥の脱水される限界が存在し、これ
がベルトプレス型脱水機の限界とされていた。
Normally, sludge is dehydrated under pressure and then incinerated or directly disposed of.However, conventional dewatering mechanisms have been to remove sludge, such as sewage sludge, between two pieces of cloth that are tensioned by multiple rolls. A dehydrator is widely used in which sludge is sequentially dewatered by the compression pressure of two cloths by inserting a cloth into the cloth and rotating the cloths in the same direction. There are two types of dehydrators: one that uses only the tension between two cloths as described above, and one that uses rolls directly facing each other and in contact with each other. In the former method, the maximum tension is applied to relatively soft sludge, taking into account the protrusion of the sludge from both sides of the cloth, and the maximum pressure possible is applied to the sludge. The limit lies in the fact that the fabric will break if a certain amount of tension is applied to it. This limit is about 30 kg, and the pressure on the fabric on the roll obtained from this tension is 100 to 300 mm depending on the roll diameter.
In this case, it is 2 to 3 Kg/cm 2 . There is a limit to how many types of sludge can be dehydrated in response to such pressure, and this has been considered the limit of belt press type dewatering machines.

上記の改良案として二枚の布が周回するロー
ルに対し、Vベルトのような張力の大きいベルト
を三本のロールを介して外部から圧着される機構
が開発されている。この方法は布よりも張力の
高いベルトを使用するので布自体よりも圧縮圧
力が高くなるが、これにも限度があり実測した圧
力は4〜5Kg/cm2である。従つて、次に続く操作
が乾燥あるいは焼却のような熱的操作であるため
極力汚泥中の水分を除去して省エネルギーを図ろ
うとする場合には更に強力な圧縮圧力が要求され
る。
As an improvement to the above, a mechanism has been developed in which a high-tension belt, such as a V-belt, is externally pressed onto two rolls of cloth through three rolls. This method uses a belt with higher tension than the cloth, so the compression pressure is higher than that of the cloth itself, but there is a limit to this, and the actual pressure measured is 4 to 5 kg/cm 2 . Therefore, since the subsequent operation is a thermal operation such as drying or incineration, even stronger compression pressure is required in order to save energy by removing as much moisture from the sludge as possible.

本発明は上記のような従来技術の欠点を解消
し、かつ上記の如き要求に対応する脱水機を提供
することを目的とするものである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a dehydrator that overcomes the drawbacks of the prior art as described above and meets the requirements as described above.

以下図面に従つて本発明を詳細に説明する。 The present invention will be described in detail below with reference to the drawings.

第1図は本発明脱水機の一実施例を示す全体図
であり、上下二枚の無端状布1,2は、複数個
の張設ローラとは離隔して存在する脱水ローラ3
において積層周回するように、張設ローラ間に張
設してある。ローラ3は、第2図、第3図に示す
ように、両端に突出する軸4が架台5の軸受6に
回転可能に軸支してあり、ローラ3を電気的或い
は機械的操作により回転させることにより、二枚
の布1,2を同方向へ連続的に循環移動可能と
し、その回転にともない狭圧する汚泥を脱水する
ようになつている。
FIG. 1 is an overall view showing one embodiment of the dewatering machine of the present invention, in which two upper and lower endless cloths 1 and 2 are connected to a dewatering roller 3 that is located apart from a plurality of tension rollers.
The sheets are stretched between tension rollers so that they can be laminated and rotated at. As shown in FIGS. 2 and 3, the roller 3 has a shaft 4 protruding from both ends rotatably supported by a bearing 6 of a pedestal 5, and the roller 3 is rotated by electrical or mechanical operation. This allows the two cloths 1 and 2 to be continuously circulated in the same direction, and the sludge compressed as they rotate is dehydrated.

脱水ローラ3の直径は、複数個の張設ローラ群
の内、ローラ3に近接する二個のローラ、即ち、
ローラ3へ布1,2を送るローラ3aと、ロー
ラ3から布1,2を受けるローラ3b間よりも
大となつている。
The diameter of the dewatering roller 3 is the same as that of the two rollers close to the roller 3 among the plural tension roller groups, that is,
It is larger than the space between the roller 3a that sends the cloths 1 and 2 to the roller 3 and the roller 3b that receives the cloths 1 and 2 from the roller 3.

脱水ローラ3に近接して加圧機構7が設置して
ある。この加圧機構7は、第2図、第3図に示す
ように、ローラ3と同一円弧状に形成し、ローラ
3とほぼ同じ長さを有する長尺なダイヤフラム板
8の内面に、外表面に凹凸溝を形成したゴムのよ
うな可撓製材質からなるダイヤフラム9の周辺を
密接したものである。この加圧機構7は、両端を
ローラ3の軸4に揺動可能に吊設してあるととも
にシリンダー10と直結している。そして、常態
において、ローラ3の周面とダイヤフラム9間に
は〓間が形成されている。
A pressure mechanism 7 is installed adjacent to the dewatering roller 3. As shown in FIGS. 2 and 3, this pressure mechanism 7 is formed in the same arc shape as the roller 3, and has an elongated diaphragm plate 8 having approximately the same length as the roller 3. The periphery of a diaphragm 9 made of a flexible material such as rubber and having grooves formed therein is closely placed. The pressure mechanism 7 has both ends swingably suspended from the shaft 4 of the roller 3 and is directly connected to the cylinder 10 . In a normal state, a gap is formed between the circumferential surface of the roller 3 and the diaphragm 9.

本発明は上記のように構成しており、脱水ロー
ラ3を全体工程的にほぼ連続状態で回転させた状
態で二枚の布1,2間に下水スラツジのような
汚泥11を連続して供給すれば、ローラ3までの
中間にある複数の張設ローラ間で汚泥はある程度
脱水され、汚泥は粘性体となる。
The present invention is constructed as described above, and the sludge 11 such as sewage sludge is continuously supplied between the two cloths 1 and 2 while the dewatering roller 3 is rotated almost continuously throughout the entire process. Then, the sludge is dehydrated to some extent between the plurality of tension rollers located in the middle up to the roller 3, and the sludge becomes a viscous body.

このようにして粘性化した汚泥がローラ3に移
動した時、ダイヤフラム板8とダイヤフラム9間
に圧力水を注入すれば、ダイヤフラム9は膨張し
てローラ3に対し二枚の布1,2を同時に圧接
させる。加圧機構7全体は、布1,2とダイヤ
フラム9との圧接摩擦でローラ3と同方向へ回動
し、その間において粘性汚泥の最終脱水を行う。
When the sludge that has become viscous in this way moves to the roller 3, if pressure water is injected between the diaphragm plate 8 and the diaphragm 9, the diaphragm 9 expands and simultaneously pushes the two cloths 1 and 2 against the roller 3. Apply pressure. The entire pressure mechanism 7 rotates in the same direction as the roller 3 due to the pressure friction between the cloths 1 and 2 and the diaphragm 9, and final dewatering of the viscous sludge is performed during this period.

加圧機構7が所定の位置まで回動した時に、例
えば、切換バルブ12により加圧水を放出してダ
イヤフラム9の表面を減少させる。これにより、
布1,2からダイヤフラム9を離間して、ロー
ラ3に対する布1,2の圧接を開放し、同時に
シリンダー10によつて加圧機構7を定位置まで
急激に逆回転させる。
When the pressurizing mechanism 7 is rotated to a predetermined position, pressurized water is released by, for example, the switching valve 12 to reduce the surface of the diaphragm 9. This results in
The diaphragm 9 is separated from the cloths 1 and 2 to release the cloths 1 and 2 from being pressed against the roller 3, and at the same time the pressure mechanism 7 is rapidly reversely rotated by the cylinder 10 to a home position.

前記の如く、脱水ローラ3の直径は、これに近
接する二個の張設ローラ3a,3b間よりも大き
くなつているので、布1,2に接する周面積は
大きなものとなり、かつローラ3の周面外方に自
由空間を大きく取ることができる。従つて、加圧
機構7のローラ3の周面に対する操作範囲が広く
得られ、加圧機構7の使用効率が高くなる。
As mentioned above, the diameter of the dewatering roller 3 is larger than that between the two tension rollers 3a and 3b adjacent to it, so the circumferential area in contact with the fabrics 1 and 2 is large, and the diameter of the roller 3 is A large amount of free space can be secured outside the circumferential surface. Therefore, the operating range of the pressure mechanism 7 with respect to the circumferential surface of the roller 3 is wide, and the usage efficiency of the pressure mechanism 7 is increased.

加圧機構7を所定の位置まで逆回転させた後、
更にダイヤフラム板8とダイヤフラム9間に加圧
水を圧入すれば、前記と同じ操作により粘性汚泥
の脱水作業を行うことになる。
After rotating the pressure mechanism 7 in the opposite direction to a predetermined position,
Furthermore, if pressurized water is injected between the diaphragm plate 8 and the diaphragm 9, the viscous sludge can be dehydrated by the same operation as described above.

以上のようにして脱水された汚泥は、二枚の
布1,2が分離した時点で外部に取り出される。
The sludge dehydrated as described above is taken out to the outside when the two cloths 1 and 2 are separated.

第4図、第5図は本発明の他の実施例を示すも
のであつて、前記と同一部分は同符号を使用して
いる。
FIGS. 4 and 5 show other embodiments of the present invention, and the same parts as described above are given the same reference numerals.

本実施例においては回転可能に軸支したローラ
3周面に複数個の孔13を穿設するとともにこの
ローラ3内に、ローラ3内面と摺接するシール部
材14を設置し、このシール部材14の排出管1
5をローラ3外において例えば図示しない真空ポ
ンプに直結固定したことを特徴とする。
In this embodiment, a plurality of holes 13 are bored in the circumferential surface of a rotatably supported roller 3, and a sealing member 14 is installed inside the roller 3 to make sliding contact with the inner surface of the roller 3. Discharge pipe 1
5 is directly connected and fixed to, for example, a vacuum pump (not shown) outside the roller 3.

従つて、加圧機構7によつて圧縮された汚泥か
ら出る水分はローラ3内に吸収され、シール部材
14内を通つて外部へ吸収排出されることにな
り、ローラ3と加圧機構7間から圧縮水分が流出
することがなくなる。
Therefore, the water coming out of the sludge compressed by the pressure mechanism 7 is absorbed into the roller 3, passes through the seal member 14, and is absorbed and discharged to the outside. This prevents compressed water from flowing out.

上記する本発明によれば、張設ローラ群より脱
水ローラ3を離隔して布1,2を張設してある
ので、脱水ローラの回動を、全体工程からみれ
ば、その回動停止が僅かか或いは全く停止するこ
となく、その回動に追従して加圧機構7による加
圧脱水を、繰り返し、全体工程的にほぼ連続状態
で行うことができる。従つて、布1,2の張力
とは無関係に汚泥に圧力を加えることができ、脱
水効率はきわめて良好であり、しかもダイヤフラ
ム9は可撓性部材であるから圧縮汚泥面に凹凸面
があつても、加圧機構7に注入する加圧水圧に対
応して全面を均等に圧縮することができる。
According to the present invention described above, since the cloths 1 and 2 are stretched with the dewatering roller 3 separated from the tensioning roller group, the rotation of the dewatering roller can be stopped from the perspective of the overall process. Pressurized dehydration by the pressurizing mechanism 7 can be repeated and performed almost continuously in the entire process by following the rotation with little or no stopping. Therefore, pressure can be applied to the sludge regardless of the tension of the cloths 1 and 2, and the dewatering efficiency is extremely good.Moreover, since the diaphragm 9 is a flexible member, the compressed sludge surface has an uneven surface. Also, the entire surface can be compressed uniformly in response to the pressurized water pressure injected into the pressurizing mechanism 7.

尚、加圧機構7はローラ3に対し一台に限らず
複数台圧接可能に設置してもよい。これは第一段
より徐々に圧縮圧力を上げることが効果的である
場合に使用して最適である。
Note that the pressure mechanism 7 is not limited to one unit, but may be installed in a plurality of units so as to be able to press against the roller 3. This is best used when it is effective to gradually increase the compression pressure from the first stage.

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

第1図は本発明脱水機の一実施例を示す全体の
正面図、第2図はローラと加圧機構を示す一部破
断正面図、第3図は同側面図、第4図は本発明の
他の実施例を示す一部断面図、第5図は同側面図
である。 1,2は布、3はローラ、7は加圧機構、8
はダイヤフラム板、9はダイヤフラムである。
Fig. 1 is an overall front view showing an embodiment of the dehydrator of the present invention, Fig. 2 is a partially cutaway front view showing the rollers and pressure mechanism, Fig. 3 is a side view of the same, and Fig. 4 is the present invention. FIG. 5 is a partial sectional view showing another embodiment, and FIG. 5 is a side view of the same. 1 and 2 are cloth, 3 is a roller, 7 is a pressure mechanism, 8
is a diaphragm plate, and 9 is a diaphragm.

Claims (1)

【特許請求の範囲】 1 連続的に循環可能に張設した二枚の無端状
布1,2間に汚泥を供給し、張設ローラ群にて狭
圧し、ローラ群の要部の脱水ローラの外側より加
圧可能なベルトプレス型脱水機において、 張設ローラ群より離隔して配設した脱水ローラ
3に布1,2を積層周回させ、脱水ローラ3の
回転にともない汚泥を脱水するとともに膨張可能
なダイヤフラム9を有するダイヤフラム板8から
なる加圧機構7を脱水ローラ3に近接して設置
し、加圧機構7は脱水ローラ3に圧接して同方向
へ回転可能であるとともに脱水ローラ3から離間
して逆回転可能として成ることを特徴とするベル
トプレス型脱水機。
[Claims] 1. Sludge is supplied between two endless cloths 1 and 2 stretched so that it can be continuously circulated, and is compressed by a group of stretching rollers, and the sludge is applied to the dewatering roller of the main part of the roller group. In a belt press type dehydrator that can be pressurized from the outside, cloths 1 and 2 are laminated and circulated around a dewatering roller 3 that is placed apart from a group of stretched rollers, and as the dewatering roller 3 rotates, the sludge is dehydrated and expanded. A pressure mechanism 7 consisting of a diaphragm plate 8 having a diaphragm 9 is installed close to the dewatering roller 3. A belt press type dehydrator characterized by being able to separate and rotate in reverse.
JP56094141A 1981-06-16 1981-06-16 Belt-press type dehydrator Granted JPS57207516A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56094141A JPS57207516A (en) 1981-06-16 1981-06-16 Belt-press type dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56094141A JPS57207516A (en) 1981-06-16 1981-06-16 Belt-press type dehydrator

Publications (2)

Publication Number Publication Date
JPS57207516A JPS57207516A (en) 1982-12-20
JPH0113887B2 true JPH0113887B2 (en) 1989-03-08

Family

ID=14102100

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56094141A Granted JPS57207516A (en) 1981-06-16 1981-06-16 Belt-press type dehydrator

Country Status (1)

Country Link
JP (1) JPS57207516A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105251261A (en) * 2015-11-20 2016-01-20 无锡山川环保机械有限公司 Sludge treatment and sludge carding mechanism

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6041354Y2 (en) * 1980-04-21 1985-12-16 荏原インフイルコ株式会社 Sludge dewatering equipment

Also Published As

Publication number Publication date
JPS57207516A (en) 1982-12-20

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