JPS60261695A - Sludge dehydrator - Google Patents

Sludge dehydrator

Info

Publication number
JPS60261695A
JPS60261695A JP59119522A JP11952284A JPS60261695A JP S60261695 A JPS60261695 A JP S60261695A JP 59119522 A JP59119522 A JP 59119522A JP 11952284 A JP11952284 A JP 11952284A JP S60261695 A JPS60261695 A JP S60261695A
Authority
JP
Japan
Prior art keywords
sludge
section
pressure
dewatering
dehydrating
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.)
Granted
Application number
JP59119522A
Other languages
Japanese (ja)
Other versions
JPH0380600B2 (en
Inventor
Kiyoshi Uyama
清 宇山
Yasuhiko Kihara
泰彦 木原
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP59119522A priority Critical patent/JPS60261695A/en
Priority to US06/674,543 priority patent/US4657682A/en
Priority to KR1019840007408A priority patent/KR870001736B1/en
Priority to EP84114586A priority patent/EP0144090B1/en
Priority to DE8484114586T priority patent/DE3481288D1/en
Priority to AT84114586T priority patent/ATE50196T1/en
Publication of JPS60261695A publication Critical patent/JPS60261695A/en
Priority to US07/003,225 priority patent/US4986910A/en
Publication of JPH0380600B2 publication Critical patent/JPH0380600B2/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

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To decrease considerably the moisture content of dehydrated cake and to increase treating capacity by constituting a titled device of a preliminary dehydrating section, forming section and dehydrating section having a pair of endless filter cloths circulating through a low-pressure dehydrating section, middle-pressure dehydrating section and high-pressure dehydrating section. CONSTITUTION:Sludge is efficiently and preliminarily thickened in the preliminary dehydrating section 10 by which the volume of the sludge is decreased prior to pressure dehydration. The preliminarily thickened sludge is divided and ground in the sludge forming section 20 and is formed to a mince shape, etc. The sludge divided to small lump is introduced into the dehydrating section 30 in succession thereto and dehydrated cake is formed. The dehydrating mechanism of the belt press type consisting of the upper filter cloth 1 and the lower filter cloth 2 is adopted for the section 30 and the high-pressure dehydrating section consisting of a high-pressure belt 3 is provided to the rear stage thereof. The sludge is dehydrated by the gradually increased pressurizing force in the low- and middle-pressure dehydrating sections.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は下水混合生汚泥やヘドロ等のような含水汚泥を
脱水し、廃棄焼却し易くするための汚泥脱水装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a sludge dewatering device for dewatering water-containing sludge such as sewage mixed raw sludge or sludge to facilitate disposal and incineration.

〔発明の技術的背景およびその問題点〕この種の汚泥脱
水装置としては、第2図、第3図に示すものが従来知ら
れている。
[Technical background of the invention and its problems] As this type of sludge dewatering apparatus, those shown in FIGS. 2 and 3 are conventionally known.

第2図の脱水装置は、上部濾布lおよび下部濾布2を夫
々図示のように複数のロール間に掛は亘し、この2枚の
濾布間に含水汚泥を供給して圧搾脱水するもので、従来
使用されているベルトプレス型の汚泥脱水装置は殆どが
このタイプのものである。このタイプの汚泥脱水装置に
は次のような問題がある。
In the dewatering device shown in Fig. 2, an upper filter cloth 1 and a lower filter cloth 2 are each stretched between a plurality of rolls as shown in the figure, and water-containing sludge is supplied between these two filter cloths and compressed and dehydrated. Most of the conventionally used belt press type sludge dewatering devices are of this type. This type of sludge dewatering equipment has the following problems.

第1の問題は、一種類の濾布で汚泥の重力脱水および加
圧脱水の両方を行なうため脱水効率が低いことである。
The first problem is that the dewatering efficiency is low because one type of filter cloth performs both gravity dewatering and pressure dewatering of sludge.

即ち、重力脱水には濾過面積が広く目の粗い濾布が適し
、他方の加圧脱水には目の細かい濾布が適するという相
反する面があり、これを一種類の濾布で賄えば当然に効
率が犠牲にならざるを得ない。
In other words, there are contradictory aspects in that a coarse filter cloth with a wide filtration area is suitable for gravity dehydration, while a fine filter cloth is suitable for pressure dehydration, and it is natural that one type of filter cloth can handle these problems. efficiency has to be sacrificed.

第2の問題は、重力脱水の効率が悪いことから処理能力
が小さいことである。
The second problem is that the efficiency of gravity dewatering is low, resulting in low processing capacity.

第3の問題としては、ロールに濾布を巻き付けただけの
構造であるため、圧搾圧力は最大でも2kg/cm2程
度で、ケーキ含水率が充分には低下しないことが挙げら
れる。
The third problem is that since the structure is simply a filter cloth wrapped around a roll, the compression pressure is about 2 kg/cm2 at maximum, and the moisture content of the cake does not decrease sufficiently.

次に第3図の汚泥脱水装置について説明すると、この装
置も基本的には第2図の装置と同様に2枚のm布1.2
によるベルトプレスタイプであるが、ケーキの脱水率を
高めるため、後段に高圧ベルト3による高圧搾脱水機構
が取り付けられている。この第3図の脱水装置でも第2
図の装置で説明した第1および第2の問題は依然として
解消されずに残り、また次のような別の問題が含まれて
いる。
Next, the sludge dewatering device shown in Fig. 3 will be explained. This device basically uses two sheets of m cloth 1.2 mm, similar to the device shown in Fig. 2.
Although it is a belt press type, a high pressure dehydration mechanism using a high pressure belt 3 is attached at the rear stage to increase the dehydration rate of the cake. In this dehydration equipment shown in Fig. 3, the second
The first and second problems described with respect to the device in the figure still remain unresolved, and the following other problems are included.

即ち、高圧搾機構を後段に設けているが、前工程で含水
率が充分に低下していない場合には後段で高い圧力を加
えることができない。無理に高圧を加えると、ケーキの
はみ出しや濾布からの目洩れといった問題を生じること
になる。
That is, although a high compression mechanism is provided in the latter stage, high pressure cannot be applied in the latter stage if the water content has not been sufficiently reduced in the previous stage. Forcibly applying high pressure may cause problems such as cake sticking out or leaking from the filter cloth.

〔発明の目的〕[Purpose of the invention]

本発明は」二記事情に鑑みてなされたもので、従来の脱
水装置に比較して脱水ケーキの含水率を大幅に低下する
ことができ、汗つ処理能力も増大することができる汚泥
脱水装置を提供するものである。
The present invention was made in view of the following two circumstances, and is a sludge dewatering device that can significantly reduce the water content of dehydrated cake and increase sweat treatment capacity compared to conventional dewatering devices. It provides:

1i〔発明の概要〕 本発明による汚泥脱水装置は、含水汚泥を受け入れる予
備脱水部と、予備脱水された汚泥を小塊に分割する形成
部と、低圧脱水部、中圧脱水部および高圧脱水部を連続
して循環する一対の無端状濾布を有する脱水部とからな
ることを特徴とするものである。
1i [Summary of the Invention] The sludge dewatering apparatus according to the present invention comprises a preliminary dewatering section that receives water-containing sludge, a forming section that divides the predehydrated sludge into small lumps, a low pressure dewatering section, a medium pressure dewatering section, and a high pressure dewatering section. and a dewatering section having a pair of endless filter cloths that continuously circulate water.

上記本発明の脱水装置における各部の作用を概略的に説
明すると、予備脱水部では効率良く汚泥を予備濃縮する
ことにより、加圧脱水する前の汚泥の容量を小さくして
実質的な処理能力を増大することが可能となり、また原
汚泥の濃度が変動した場合にも安定した運転が可能とな
る。
To roughly explain the function of each part in the dewatering apparatus of the present invention, the pre-dewatering section efficiently pre-concentrates sludge to reduce the volume of sludge before pressurized dewatering and increase the actual processing capacity. Moreover, stable operation is possible even when the concentration of raw sludge fluctuates.

次に、こうして予備濃縮された汚泥は形成部で分割破砕
され、ミンチ状等に形成される。これによって汚泥内部
の水分を効率良く排出することが可能になると共に、引
続いて行なわれる加圧脱水時の濾液排出速度を速くする
ことができる。また、汚泥形成部を採用したことで濾布
の幅方向および長さ方向でのケーキの厚みが均一になり
、濾布の皺寄りや蛇行の防止が可能になる。
Next, the sludge pre-concentrated in this way is divided and crushed in a forming section to form minced pieces or the like. This makes it possible to efficiently discharge water inside the sludge, and also to increase the rate of filtrate discharge during the subsequent pressurized dehydration. Furthermore, by employing the sludge forming section, the thickness of the cake in the width direction and length direction of the filter cloth becomes uniform, making it possible to prevent wrinkles and meandering of the filter cloth.

続いて、この小塊に分割された汚泥は脱水部に導入され
て脱水ケーキが形成される。この場合、低圧脱水部、中
圧脱水部では徐々に圧力を高くして脱水し、高圧脱水部
での処理が可能な程度にケーキ含水率を充分に低下させ
る。また、高圧脱水部では低圧および中圧脱水部で脱水
されなかった水分の圧搾親木が行なわれる。そして、本
発明では前記予備脱水部および形成部を設けたことによ
って、この高圧脱水部における脱水が効果的に作用し、
全体として低含水率の脱水ケーキを効率良く形成するこ
とが可能となったものである。
Subsequently, the sludge divided into small lumps is introduced into a dewatering section to form a dewatering cake. In this case, the pressure is gradually increased in the low-pressure dehydration section and the medium-pressure dehydration section to perform dehydration, and the moisture content of the cake is sufficiently reduced to the extent that it can be treated in the high-pressure dehydration section. In addition, in the high-pressure dewatering section, water that has not been dehydrated in the low-pressure and medium-pressure dehydrating sections is squeezed from parent wood. Further, in the present invention, by providing the preliminary dehydration section and the forming section, dehydration in this high pressure dehydration section acts effectively,
This makes it possible to efficiently form a dehydrated cake with an overall low moisture content.

〔発明の実施例〕[Embodiments of the invention]

以下に本発明の詳細な説明する。 The present invention will be explained in detail below.

第1図は本発明の一実施例になる汚泥脱水装置を示す説
明図である。同図において、1Jは予備脱水部、A」は
汚泥形成部、1」は脱水部である。
FIG. 1 is an explanatory diagram showing a sludge dewatering apparatus according to an embodiment of the present invention. In the figure, 1J is a preliminary dewatering section, A'' is a sludge forming section, and 1'' is a dewatering section.

この実施例において、予備脱水部↓Jは図示のようにポ
ケット型重力脱水機構として構成されている。しかし、
これ以外にも例えば第4図(A)のようなフラットな濾
布11を用いた重力脱水機構、或いは第4図(B)に示
すドラムシックナーを使用してもよい。なお、第4図(
A)中の12は洗浄スプレーであり、第4図(B)中の
13は汚泥供給管、14は汚泥シュート、15はシャフ
ト、16はスクリーン、17はスクリーン洗浄管、18
は移送用螺線羽根である。
In this embodiment, the preliminary dehydration section ↓J is configured as a pocket-type gravity dehydration mechanism as shown in the figure. but,
In addition to this, for example, a gravity dewatering mechanism using a flat filter cloth 11 as shown in FIG. 4(A) or a drum thickener as shown in FIG. 4(B) may be used. In addition, Figure 4 (
12 in A) is a cleaning spray, 13 in FIG. 4(B) is a sludge supply pipe, 14 is a sludge chute, 15 is a shaft, 16 is a screen, 17 is a screen cleaning pipe, 18
is a spiral vane for transportation.

次に、第1図の実施例における汚泥形成部20について
説明すると、この実施例では第5図(A)に示す構成の
ロール式形成機が採用されている。即ち、予備脱水され
た汚泥をホッパー21に受け、この汚泥をロール対22
..222の噛合部に通すことによって連続的な汚泥を
ミンチ状の小塊に分割するようになっている。なお、汚
泥形成部20としては、このようなロール式形成機以外
にも、例えば第5図(B)〜(D)に示す形成機を用い
ることができる。第5図(B)は押出し式の形成機で、
油圧等の力を利用したシリンダ23で汚泥を押出してミ
ンチ状に形成するものである。第5図(C)は振動脱水
による形成機で、傾斜の付いたパンチングメタルまたは
網24の上に汚泥を落下させ、装置を振動させることに
よって汚泥をペレット状に形成するものである。また第
5図CD)は押し付は脱水による形成機で、パンチング
メタル製の半円筒25の中に汚泥を供給し、スクレーパ
26や押えローラ27で押し付けることによって汚泥を
うどん状に形成するものである。
Next, the sludge forming section 20 in the embodiment shown in FIG. 1 will be explained. In this embodiment, a roll-type forming machine having the configuration shown in FIG. 5(A) is employed. That is, pre-dehydrated sludge is received in a hopper 21, and this sludge is transferred to a pair of rolls 22.
.. .. The continuous sludge is divided into minced small lumps by passing it through the meshing part of 222. In addition, as the sludge forming section 20, in addition to such a roll-type forming machine, for example, forming machines shown in FIGS. 5(B) to 5(D) can be used. Figure 5(B) shows an extrusion type forming machine.
The sludge is pushed out using a cylinder 23 using hydraulic power or the like to form minced sludge. FIG. 5(C) shows a forming machine using vibration dewatering, in which sludge is dropped onto an inclined punching metal or screen 24, and the sludge is formed into pellets by vibrating the apparatus. In addition, Fig. 5 CD) is a pressing and dewatering forming machine, which supplies sludge into a semi-cylinder 25 made of punched metal and forms the sludge into a noodle shape by pressing with a scraper 26 and a presser roller 27. be.

第1図の実施例における脱水部30は、基本的には第3
図で説明した従来の汚泥脱水装置と同じである。即ち、
上部濾布lおよび下部濾布2によるベルトプレスタイプ
の脱水機構が全体に採用され、後段には高圧ベルト3に
よる高圧搾脱水部が設けられている。高圧搾水部以外の
部分は低・中圧脱氷部で、徐々に加圧力を上げて脱水を
行なうようになっている。なお、高圧脱水部の構成とし
ては、第1図の実施例以外にも、例えば第6図(A)に
示すように加圧濾布31.32及び加圧板33で構成し
てもよく、また第6図(B)に示;) すように加圧ロ
ーラ34を用いて構成してもよい。
The dewatering section 30 in the embodiment of FIG.
This is the same as the conventional sludge dewatering device explained in the figure. That is,
A belt press type dewatering mechanism using an upper filter cloth 1 and a lower filter cloth 2 is adopted throughout, and a high pressure dewatering section using a high pressure belt 3 is provided at the rear stage. The area other than the high-pressure water extraction section is the low- and medium-pressure deicing section, which dehydrates by gradually increasing the pressure. In addition to the embodiment shown in FIG. 1, the high-pressure dewatering section may be constructed of a pressure filter cloth 31, 32 and a pressure plate 33, as shown in FIG. 6(A), for example. The pressure roller 34 may be used as shown in FIG. 6(B).

上記第1図の実施例になる汚泥脱水装置を用いて下水処
理混合生汚泥の脱水を行ない、そのときのケーキ含水率
が低下する様子を調べたところ第7図に示す結果が得ら
れた。図から明らかなように、予備脱水部1辺において
含水率は約90%まで低下したところで略横ばいとなる
。汚泥はこの詩点で汚泥形成部乳」に移送されて分割さ
れ、その際に含水率は更に3〜4%低下する。次いで汚
泥は脱水部−影」に導入され、底・中圧脱氷部で65%
程度の含水率まで脱水された後、更に高圧脱水部では約
60%の含水率が達成されることが分った。
When sewage treatment mixed raw sludge was dehydrated using the sludge dewatering apparatus according to the embodiment shown in FIG. 1, and the manner in which the moisture content of the cake decreased at that time was investigated, the results shown in FIG. 7 were obtained. As is clear from the figure, the water content on one side of the preliminary dewatering section becomes approximately flat when it drops to about 90%. At this point, the sludge is transferred to the sludge-forming part where it is divided, and the water content is further reduced by 3-4%. Next, the sludge is introduced into the dewatering section - shadow, and the sludge is reduced to 65% in the bottom/medium pressure deicing section.
It was found that after the water content has been dehydrated to a certain level, a water content of about 60% is further achieved in the high-pressure dehydration section.

〔発明の効果〕〔Effect of the invention〕

以上詳述したように、本発明の汚泥脱水装置によれば従
来の装置では到達し得なかった低含水率の脱水ケーキを
形成することができ、また処理能力についても従来の装
置と同等、或いはそれ以上とすることが可能である等、
顕著な効果が得られるものである。
As detailed above, the sludge dewatering device of the present invention can form a dehydrated cake with a low water content that could not be achieved with conventional devices, and the processing capacity is also equivalent to or equal to that of conventional devices. It is possible to make it more than that, etc.
It is possible to obtain a remarkable effect.

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

第1図は本発明による汚泥脱水装置の一実施例を示す説
明図、第2図および第3図は夫々従来の汚泥脱水装置の
説明図、第4図(A)および同図(B)は本発明の汚泥
脱水装置に用いる予l!脱水機の他の例を示す説明図、
第5図(A)は第1図の実施例における汚泥形成部20
の説明図であり、同図(B)〜(D)は汚泥形成機の他
の例を示す説明図、第6図(A)および同図(B)は本
発明の脱水装置に用いる高圧脱水部の他の例を示す説明
図、第7図は第1図の実施例になる汚泥脱水装置を用い
て下水処理混合生汚泥の脱水を行ない、そのときのケー
キ含水率が低下する様子を調べた結果を示す線図である
。 ■・・・上部濾布、2・・・下部濾布、3・・・高圧ベ
ルト、上J・・・予備脱水部、11・・・濾布、12・
・・洗浄スレー、13・・・汚泥供給管、14・・・汚
泥シュート、15・・・シャフト、16・・・スクリー
ン、17・・・スクリーン洗浄管、18・・・移送用螺
線羽根、20・・・汚泥形成部、21・・・ホー2パー
、22..222・・・ロール対、23・・・シリンダ
ー、24・・・パンチングメタル(または網)、25・
・・パンチングメタル製の半円筒容器、26・・・スク
レーパ、27・・・押えローラ、30−・・脱水部、3
1.32・・・濾布、33・・・加圧ローラ
FIG. 1 is an explanatory diagram showing one embodiment of the sludge dewatering device according to the present invention, FIGS. 2 and 3 are explanatory diagrams of a conventional sludge dewatering device, respectively, and FIG. 4 (A) and FIG. The preparation used in the sludge dewatering apparatus of the present invention! An explanatory diagram showing another example of a dehydrator,
FIG. 5(A) shows the sludge forming part 20 in the embodiment of FIG.
Fig. 6(B) to (D) are explanatory drawings showing other examples of the sludge forming machine, and Fig. 6(A) and Fig. 6(B) are explanatory drawings showing other examples of the sludge forming machine. Fig. 7 is an explanatory diagram showing another example of the sewage treatment mixed raw sludge using the sludge dewatering apparatus according to the embodiment shown in Fig. 1, and the decrease in cake moisture content was investigated. FIG. ■... Upper filter cloth, 2... Lower filter cloth, 3... High pressure belt, Upper J... Preliminary dewatering section, 11... Filter cloth, 12...
...Cleaning sled, 13...Sludge supply pipe, 14...Sludge chute, 15...Shaft, 16...Screen, 17...Screen cleaning pipe, 18...Transfer spiral vane, 20...Sludge forming part, 21...Hoe 2 par, 22. .. 222...Roll pair, 23...Cylinder, 24...Punching metal (or net), 25...
... Semi-cylindrical container made of punched metal, 26... Scraper, 27... Press roller, 30-... Dewatering section, 3
1.32... Filter cloth, 33... Pressure roller

Claims (1)

【特許請求の範囲】[Claims] 含水汚泥を受け入れる予備脱水部と、予備脱水された汚
泥を小塊に分割する形成部と、低圧脱水部、中圧脱水部
および高圧説木部を連続して循環する一対の無端状濾布
を有する脱水部とからなることを特徴とする汚泥脱水装
置。
A pre-dewatering section that receives water-containing sludge, a forming section that divides the pre-dehydrated sludge into small lumps, and a pair of endless filter cloths that continuously circulate through a low-pressure dewatering section, a medium-pressure dewatering section, and a high-pressure drying section. 1. A sludge dewatering device comprising: a dewatering section.
JP59119522A 1983-12-01 1984-06-11 Sludge dehydrator Granted JPS60261695A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP59119522A JPS60261695A (en) 1984-06-11 1984-06-11 Sludge dehydrator
US06/674,543 US4657682A (en) 1984-06-11 1984-11-26 Method for dehydrating sludge
KR1019840007408A KR870001736B1 (en) 1983-12-01 1984-11-26 Dehydration method of sludge
EP84114586A EP0144090B1 (en) 1983-12-01 1984-11-30 Method and apparatus for dehydrating sludge
DE8484114586T DE3481288D1 (en) 1983-12-01 1984-11-30 METHOD AND DEVICE FOR DRAINING SLUDGE.
AT84114586T ATE50196T1 (en) 1983-12-01 1984-11-30 METHOD AND APPARATUS FOR DEWATERING MUD.
US07/003,225 US4986910A (en) 1984-06-11 1987-01-14 Apparatus for dehydrating sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59119522A JPS60261695A (en) 1984-06-11 1984-06-11 Sludge dehydrator

Publications (2)

Publication Number Publication Date
JPS60261695A true JPS60261695A (en) 1985-12-24
JPH0380600B2 JPH0380600B2 (en) 1991-12-25

Family

ID=14763356

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59119522A Granted JPS60261695A (en) 1983-12-01 1984-06-11 Sludge dehydrator

Country Status (1)

Country Link
JP (1) JPS60261695A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5318869A (en) * 1976-08-05 1978-02-21 Baehr Albert Extractor for sludge or the like
JPS5949494U (en) * 1982-09-21 1984-04-02 市川毛織株式会社 Sludge concentration and dehydration equipment

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5949494B2 (en) * 1978-05-15 1984-12-03 株式会社東芝 Steam heating cooker

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5318869A (en) * 1976-08-05 1978-02-21 Baehr Albert Extractor for sludge or the like
JPS5949494U (en) * 1982-09-21 1984-04-02 市川毛織株式会社 Sludge concentration and dehydration equipment

Also Published As

Publication number Publication date
JPH0380600B2 (en) 1991-12-25

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