JPS60183100A - Dehydration and coagulation treatment of sludge - Google Patents

Dehydration and coagulation treatment of sludge

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Publication number
JPS60183100A
JPS60183100A JP59039674A JP3967484A JPS60183100A JP S60183100 A JPS60183100 A JP S60183100A JP 59039674 A JP59039674 A JP 59039674A JP 3967484 A JP3967484 A JP 3967484A JP S60183100 A JPS60183100 A JP S60183100A
Authority
JP
Japan
Prior art keywords
sludge
dehydration
filter cloth
vacuum
dewatering
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
JP59039674A
Other languages
Japanese (ja)
Inventor
Nobunao Murakami
信直 村上
Shigetaka Iida
飯田 茂隆
Munehisa Nakagawa
中川 宗久
Tadayoshi Nakai
中井 唯喜
Yasuko Tawara
田原 靖子
Toru Hongo
本郷 徹
Kazuharu Shimada
島田 和治
Hiromi Tajiri
田尻 弘水
Yutaka Sakaguchi
豊 坂口
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.)
Takenaka Komuten Co Ltd
Original Assignee
Takenaka Komuten 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 Takenaka Komuten Co Ltd filed Critical Takenaka Komuten Co Ltd
Priority to JP59039674A priority Critical patent/JPS60183100A/en
Publication of JPS60183100A publication Critical patent/JPS60183100A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To sufficiently lower the water content of dehydrated cake, by performing dehydration treatment in a dehydration part by a vacuum degree retaining member in such a state that air sucking from the outside is prevented as compared with that from the sludge adhered to the outer surface of filter cloth. CONSTITUTION:The filter cloth 3 wound around a vacuum dehydration drum 1 and a roll 2 is revolved and sludge mixture of sludge and a coagulation material is adhered to the outer surface of the revolving filter cloth 3 in a sludge adhering part 5 for immersing said filter cloth 3 in a sludge mixture bath 4 with the revolution thereof. This adhered sludge receives vacuum sucking dehydration treatment by a sheet member in a dehydration part 6 at a position where said filter cloth 3 is revolved above the sludge adhering part 5 in such a state that air sucking from the outside is prevented as compared with that from the sludge adhered to the outer surface of the filter cloth 3. Thereafter, the filter cloth 3 is revolved from the dehydration part 6 to a peeling-off part 8 and a dehydrated cake is peeled off and removed from the outer surface of the filter cloth 3.

Description

【発明の詳細な説明】 本発明は、産業廃棄物としての廃秦物汚配とか、河川・
湖沼・港湾・海域などの底質としての堆積汚泥、あるい
は、下水道終末処理場から排出さ、れる下水汚泥などの
、放置しておけば環境悪化となる各種汚泥〔以下、単に
汚泥と称する〕を処理する方法で、詳しくは、汚泥と固
化材との混合汚泥を汚泥付着部で回動p布の外表面に付
着させ、七の付着汚泥を脱水部で!’2吸引脱水処理し
た後、七の脱水ケーキta記P布から剥離除去する汚泥
の脱水固化処理方法に関する。
[Detailed Description of the Invention] The present invention is applicable to waste pollution as industrial waste, river pollution, etc.
Various types of sludge (hereinafter simply referred to as sludge) that will degrade the environment if left untreated, such as accumulated sludge as bottom sediment in lakes, ports, sea areas, etc., or sewage sludge discharged from sewage treatment plants, etc. In detail, the sludge mixture of sludge and solidifying material is applied to the outer surface of the rotating p-cloth in the sludge adhesion section, and the adhering sludge in step 7 is removed in the dewatering section! 2. A method for dehydrating and solidifying sludge, in which the dehydrated cake is peeled off and removed from the cloth after being subjected to suction dehydration treatment.

上記汚泥の脱水固化処理方法は、同化材を脱水前に添加
することによシ、旧来の、脱水後の汚泥に固化材を添加
して処理する方法に比べ、同化材と汚泥とtIkP、練
かつ一生する夫々の設備が要らなくて投媚費?六幅に低
減できるとともに汚泥の同化処理?迅速に行える利点が
ある。
The dewatering and solidifying treatment method for sludge described above is characterized by adding an assimilating agent before dewatering. Also, you don't need any equipment that will last a lifetime, so it's a cost-effective option? Can it be reduced to six widths and assimilated sludge? It has the advantage of being quick.

ところが、この改良された汚泥の脱水同化処理方法にお
いては、上記利点があるものの、脱水処理において、混
合汚泥の含水率を十分に低下できず、得られる脱水ケー
キの含水率が制いために、固化処理後において目標強度
−を得る上から、固化材r多量に必要として高価になる
欠点があり、また、汚泥中の固形分量の割に同化処理さ
れる脱水ケーキの量が多く、嵩高になり、投棄のための
運搬費がかさみ、より−m高価になるなど、未だ改善の
余地があった。
However, although this improved sludge dehydration and assimilation treatment method has the above-mentioned advantages, the water content of the mixed sludge cannot be sufficiently lowered during the dewatering process, and the water content of the resulting dehydrated cake is limited, resulting in solidification. In order to obtain the target strength after treatment, a large amount of solidifying material is required, which makes it expensive.Also, the amount of dewatered cake to be assimilated is large compared to the solid content in the sludge, resulting in bulk. There was still room for improvement, as transportation costs for dumping increased and the waste became more expensive.

本発明は、汚泥の脱水前に固化付全添加して真空吸引脱
水処理する汚泥の脱水固化処理方法において、汚泥含水
率を十分に低下できない原因に考察を加えて改良し、脱
水ケーキの含水率を十分に低下できる方法ケ提案せんと
するものである。
The present invention improves the sludge dehydration and solidification treatment method in which the sludge is completely added with solidification and vacuum suction dewatered before the sludge is dehydrated. The purpose of this paper is to propose a method that can sufficiently reduce the

本発明は、冒頭に記した汚泥の脱水同化処理方法におい
て、上記目的を達成する次めに、前記脱水部において、
具を度維持用部材により、1′iJ記p布の外表1fl
に付着された汚泥よりも外方からの吸気を防止した状態
で脱水処理することを特徴とする。
The present invention achieves the above object in the sludge dehydration and assimilation treatment method described at the beginning, and next, in the dewatering section,
The outer surface of the cloth 1fl
The sludge is characterized by being dehydrated in a state where air is prevented from being sucked in from the outside of the sludge.

同化材を添加しfC混合汚泥を真空吸引脱水処理する場
合の汚泥性状の経時的変化について考察したところ、同
化材の添加に伴って混合汚泥の粘看性が低下し、脱水部
で十分に脱水さfiないうちに、脱水ケーキにヒビ削れ
ケ生じ、そのヒビ部分から外気が吸引され、真室吸引力
が脱水のために何ら自助に作用しなくなυ、これが汚泥
含水率?十分に低下できない原因になっていることを見
出すに至シ、本発明で社、この点に看目し、ヒビ削れが
生じ又も、七のヒビ部分から外気が吸引されること全真
空度維持用部材によって防止し、真空吸引脱水処理に十
分に作用させられるようになったのである。
When we considered changes in sludge properties over time when vacuum suction dewatering was performed on fC mixed sludge with the addition of an assimilation agent, we found that the viscosity of the mixed sludge decreased with the addition of an assimilation agent, and that the dewatering section did not fully dewater the sludge. Before it can be removed, cracks appear in the dehydrated cake, outside air is sucked in through the cracks, and the vacuum suction force no longer acts to help itself due to dehydration.Is this the water content of the sludge? We discovered that this is the reason why the temperature could not be lowered sufficiently, and in this invention, we focused on this point, and even if cracks occur, outside air is sucked through the cracked part to maintain the full vacuum level. This has enabled the vacuum suction dehydration treatment to work effectively.

したがって、同化材を添加した混合汚泥の脱水処理にお
いて、同化材す加に起因するヒビ割れが原因となっての
真空箋の低下を回避し、汚泥含水率を十分に低下して脱
水ケーキの含水率を十分に低くでき、脱水と同時に同化
処理して得られる脱水グー・キにおいて、同化材の量を
増加させること無く必要強度を良好に得られるとともに
、汚泥中の固形分の含有量が同量とした場合に、得られ
る脱水ケーキの容量を従来より小さくでき、固化材消費
量及び投棄のだめの運搬費のいずれをも大幅に節約でき
、極めて経済性有利に汚泥を処理・処分できるようにな
った。
Therefore, in the dewatering treatment of mixed sludge containing assimilated material, it is possible to avoid a decrease in vacuum paper quality due to cracks caused by the addition of assimilated material, and to sufficiently reduce the water content of the sludge, thereby increasing the moisture content of the dehydrated cake. In the dehydrated goo and ki obtained by assimilation treatment at the same time as dewatering, the required strength can be obtained satisfactorily without increasing the amount of assimilated material, and the solid content in the sludge can be kept at the same level. In terms of volume, the volume of the dehydrated cake obtained can be made smaller than before, and both the consumption of solidifying agent and the transportation cost of the dumping tank can be significantly reduced, making it possible to treat and dispose of sludge in an extremely economically advantageous manner. became.

以下、本発明方法の実施例を図面により説明する。Examples of the method of the present invention will be described below with reference to the drawings.

真空脱水用ドラム(1)とロール(2)・・トニわたっ
て巻回されたP布(3)を回動させ、それに伴い、四合
汚泥浴(4)K浸漬させる汚泥付着部(5)で、回動P
布(3)の外表面に、汚泥と同化材−との混合汚泥を付
着させ、その付着汚泥を、汚泥付着部(5)より上方に
回動された位置の脱水部(6)において、シート部材(
7)により、p布(3)の外表面に付着された汚泥より
も外方からの吸気を防止した状態で真空吸引脱水処理し
、その後、脱水部(6)から剥離部(8)に回動され、
脱水ケーキを戸布t31の外表面から剥離除去する。
Vacuum dewatering drum (1) and roll (2)... Rotate the P cloth (3) wound across the drum, and accordingly, the sludge adhesion part (5) where it is immersed in the four-piece sludge bath (4). So, rotation P
A mixed sludge of sludge and an assimilating agent is attached to the outer surface of the cloth (3), and the attached sludge is removed from the sheet in the dewatering section (6) at a position rotated upward from the sludge adhering section (5). Element(
7), the sludge adhering to the outer surface of the P cloth (3) is dehydrated by vacuum suction in a state where air is prevented from being sucked in from the outside, and then the sludge is transferred from the dewatering section (6) to the stripping section (8). moved,
The dehydrated cake is peeled off and removed from the outer surface of the door cloth t31.

こうして連続的に脱水同化処理された脱水ケーキは回収
一槽(9)に回収され、しかる後に1.トランクなどに
より埋立地などへ固化物上して投棄処分される。
The dehydrated cake that has been continuously dehydrated and assimilated in this way is collected in a recovery tank (9), and then 1. The solidified material is dumped in trunks and other places in landfills.

前記混合汚泥浴(4)に対しては混合汚泥貯留槽(10
)からの混合汚泥が供給貯留され、そして、この混合汚
泥貯留槽(10)には、汚泥貯留槽(II)、凝集剤貯
留槽(12)及び固化材貯餉槽(I3)夫々から汚晶、
凝集剤及び固化材が供給されて混合貯留される。
For the mixed sludge bath (4), there is a mixed sludge storage tank (10
) is supplied and stored, and this mixed sludge storage tank (10) receives sludge from the sludge storage tank (II), flocculant storage tank (12), and solidification agent storage tank (I3), respectively. ,
A flocculant and a solidifying agent are supplied and mixed and stored.

上記凝集剤としては、塩化鉄、消石灰、各種ポリマー、
あるいは、それらの混合物力ど各種のものを用いること
ができる。 なお、汚泥の凝集性が良い場合には、この
凝集剤は添加しなくても良い。
The above flocculants include iron chloride, slaked lime, various polymers,
Alternatively, various kinds of materials such as a mixture thereof can be used. Note that if the sludge has good flocculating properties, it is not necessary to add this flocculant.

上記固化材としては、各種ボルトランドセメント、高炉
セメント、高アルミナ質セメントなどの水硬性セメント
系物質、もしくは、これらの水硬性セメント系物質を主
成分とする固化材が適用でき、殊に、下水汚泥のように
、ポルトランドセメントの水和硬化を阻害する物質(例
えば、糖類、フミン類など)を含有する汚泥に一対して
は、Al2O,/ wt 4以上、50./jwt 4
以上含み、かつ、アクイン(Hauyne ) (8C
aO−8A1hO3・Ca5O,)を主要成分として含
む高アルミナ高硫酸塩質セメントが有効に適用できる。
As the above-mentioned solidification material, hydraulic cement materials such as various boltland cements, blast furnace cements, high alumina cements, etc., or solidification materials mainly composed of these hydraulic cement materials, can be used. For sludge containing substances that inhibit the hydration hardening of Portland cement (for example, sugars, humins, etc.), Al2O,/wt 4 or more, 50. /jwt 4
Including the above, and Hauyne (8C
A high alumina high sulfate cement containing aO-8A1hO3.Ca5O,) as a main component can be effectively applied.

次に、本発明方法に使用される、第1図に示した真空脱
水機の細部について説明する。
Next, details of the vacuum dehydrator shown in FIG. 1 used in the method of the present invention will be explained.

前記真空脱水用ドラム(1)は、図示しないが、その内
部が多数の室に区画されるとともに、それらの室夫々と
7個の真空吸引ポンプ(14Iとが切換弁及び配管を介
して運上接続され、ドラム+11の回転に伴って切換弁
をリノ換え、汚泥付着部(6)に対応する吸着ゾーン囚
、及び、脱水部(6)に対応する脱水ゾーン(B)大々
においてのみ吸引圧を作用させ、それ以外の剥離ゾーン
(C)においては吸引圧を作用させないように構成され
ている。
Although not shown, the inside of the vacuum dehydration drum (1) is divided into a number of chambers, and each of these chambers and seven vacuum suction pumps (14I) are operated via switching valves and piping. The switching valve is changed as the drum +11 rotates, and the suction pressure is increased only in the adsorption zone corresponding to the sludge attachment part (6) and the dewatering zone (B) corresponding to the dewatering part (6). is applied, and suction pressure is not applied in the other peeling zone (C).

前記脱水部(6)K対応する箇所において、ドラート部
材(7)が遊転ロールα5)・・に巻回され、脱水に伴
って汚泥ケーキにヒビ割れが生じても、そのヒビ部分を
シート部材(7)で閉塞しなかもシート部材(7)がP
布(3)と同調して回動され、脱水部(6)で汚泥に作
用する吸引圧の低下を防止し、真空度を高い状態に維持
するように構成されている。
At a location corresponding to the dewatering section (6)K, the drat member (7) is wound around the free rotating roll α5), and even if cracks occur in the sludge cake due to dewatering, the cracks can be removed by the sheet member. Although the sheet member (7) is blocked by (7), the P
It is configured to rotate in synchronization with the cloth (3) to prevent a drop in the suction pressure acting on the sludge in the dewatering section (6) and maintain a high degree of vacuum.

前記剥離部(8)においては、ロール(2)の回11J
径路途中にスタレーパ(I6)が設けられ、p布f31
の表面に付着した脱水ケーキを剥離除去するように構成
されている。
In the peeling section (8), the roll (2) is rotated 11J.
A Starepa (I6) is provided in the middle of the path, and p cloth f31
The device is configured to peel off and remove dehydrated cake attached to the surface of the device.

図中07) 、 (17)は、夫々、脱水ケーキを剥離
除去した後のP布(3)に対して洗浄水を噴出供給し、
残存した汚泥を洗浄除去するための洗浄スプレーを示す
07) and (17) in the figure respectively jet and supply cleaning water to the P cloth (3) after peeling and removing the dehydrated cake;
A cleaning spray for cleaning and removing residual sludge is shown.

上記真空脱水機では、汚泥付着をも真空吸引Kjつで行
っており、シート部材(7)で真空度を高い状態に維持
することにより、汚泥脱水のみならず、汚泥吸着のため
の吸引圧をも高め、戸布(3)の外表面に付着される混
合汚泥の厚みを大に、即ち、付着混合汚泥量を増加でき
、単位時回当りの脱水固化処理量を増加して処理効率を
向上できている。
In the above-mentioned vacuum dehydrator, sludge adhesion is also performed by vacuum suction Kj, and by maintaining the degree of vacuum at a high level with the sheet member (7), it is possible to not only dehydrate sludge but also increase the suction pressure for sludge adsorption. This increases the thickness of the mixed sludge that adheres to the outer surface of the door cloth (3), that is, increases the amount of adhering mixed sludge, increases the amount of dewatering and solidification processed per unit time, and improves treatment efficiency. is made of.

次に、この真を脱水機を用いて実施した本発明方法の場
合(開発方式と表記する)と、上記真空脱水機からシー
ト部材(7)を収り除いて実施した場合(従来方式と表
記する)夫々Vζついて行った比較夫瞼結果を表記する
Next, we will discuss the case of the method of the present invention carried out using a dehydrator (denoted as the developed method) and the case of the method carried out by removing the sheet member (7) from the vacuum dehydrator (denoted as the conventional method). ) Comparison of eyelid results for each Vζ is shown.

なお、この夫験における汚泥としては、標準活性汚T)
F!、法処理の混合汚泥であり、濃縮汚泥拷水率約98
.5%、強熱減波82.5異のものを使用した。
The sludge used in this experiment was standard activated sludge T).
F! It is mixed sludge processed by law, and the thickened sludge water treatment rate is approximately 98.
.. 5% and ignition wave attenuation of 82.5 was used.

まノヒ、固化付添加率としては、ドライベースにかける
汚泥の同形分車菫どの比率で示した。
The solidification addition rate was expressed as the ratio of the same type of sludge added to the dry base.

上記結果から、吸着ゾーン囚及び脱水部(6)のいずれ
においても、本発明方法では高い真空度を容易に設定し
て得られ、それに伴って脱水ケーキの含水率を十分に低
下でき、かつ、十分な強度の脱水ケーキを得られること
が明らかである。
From the above results, the method of the present invention can easily set and obtain a high degree of vacuum in both the adsorption zone prisoner and the dehydration section (6), and accordingly, the water content of the dehydrated cake can be sufficiently reduced, and It is clear that a dehydrated cake of sufficient strength can be obtained.

第2図は、本発明方法を実施するのに用いる真空脱水機
の池の実施例を示し、回動自在に設けられた1布(3)
の上側回妨経w!!に2いて、その回前方向上手側に仕
切臂四が設けられ、その仕切壁す樽と両側壁(図省略)
並びにp布(3)によって混合汚泥の受止め部四が形成
され、p布(3)の回動に伴も、p布(3)の外表面に
混合汚泥を載置付着させていくように汚泥付着部(6)
が構成されている。
Figure 2 shows an embodiment of a vacuum dehydrator pond used to carry out the method of the present invention, in which one cloth (3) is rotatably provided.
The upper sutra sutra lol! ! 2, a partition arm is provided on the upper side in the forward direction, and the partition wall, barrel and both side walls (figure omitted)
In addition, a receiving part 4 for the mixed sludge is formed by the p-cloth (3), and as the p-cloth (3) rotates, the mixed sludge is placed and adhered to the outer surface of the p-cloth (3). Sludge adhesion part (6)
is configured.

また、上記汚泥付着部(5)L95P布(3)の回前方
間下手側におめて、p布(3)の下方に、真空吸引ポン
プ+l荀に連通接−続された気密室−が設けられ、汚泥
を真空吸引脱水処理する脱水部(6)が構成されている
。 この脱水部(6)の上方に、一対の遊転ロール−、
u5)にわたり、P布(3)上の汚泥の外表面金drJ
K接触するLうにシート部材(7)が巻回され、脱水部
(6)での真空度を高い伏急に維持する工うに構成され
ている。
In addition, in the sludge adhesion part (5) on the lower side between the front parts of the L95P cloth (3), there is an airtight chamber connected to the vacuum suction pump +1 below the P cloth (3). A dewatering section (6) is provided for dehydrating the sludge by vacuum suction. Above this dewatering section (6), a pair of idler rolls,
u5) over the outer surface of the sludge on the P cloth (3) gold drJ
A sheet member (7) is wound around the L side that is in contact with the K, and is configured to maintain a high degree of vacuum in the dewatering section (6).

前述の脱水5(6)での真空度を高い状聯に維持するた
めのシート部材(7)としては、p布(3)と同様の通
気性の低いものでも良く、ま几塩ビシニドの工うに非通
気性のシート部材でも良く、更には、脱水部(6)に対
応させて、P布(3)の外表面に付着された汚泥の外方
側に、汚泥とp布(3)の防止するものであれば、各種
の変形が可能であり、それらをして真空度維持用部材(
7)と総称する0
The sheet member (7) for maintaining a high degree of vacuum in the above-mentioned dehydration step 5 (6) may be made of a material with low air permeability similar to the P cloth (3), or may be made of vinyl chloride. A non-porous sheet member may also be used, and furthermore, the sludge and P cloth (3) can be placed on the outer side of the sludge adhered to the outer surface of the P cloth (3) in correspondence with the dewatering section (6). Various modifications can be made as long as they can prevent the vacuum level (
7) collectively referred to as 0

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

第1図は本発明方決に用いる真空脱水機−の全体概略縦
断面図、第8図は本発明方決に用いる真空脱水機の池の
実施例を示す全体概略縦断面図である。 (3)・・・・・・tpJ、(6)・・・・・・汚泥付
着部、(6)・・・・・・脱水部、(7)・・・・・・
真空度維持用部材、シート部材。 代理人 弁理士 北 村 修
FIG. 1 is an overall schematic longitudinal sectional view of a vacuum dehydrator used in the method of the present invention, and FIG. 8 is an overall schematic longitudinal sectional view showing an embodiment of a pond of the vacuum dehydrator used in the method of the present invention. (3)...tpJ, (6)...sludge adhesion section, (6)...dewatering section, (7)...
Vacuum maintenance parts and sheet parts. Agent Patent Attorney Osamu Kitamura

Claims (1)

【特許請求の範囲】 ■ 汚泥と固化材との混合汚泥を汚泥+を着部(6)で
回#Fi131の外表面に付着させ、七の付看汚泥全脱
水部+61で真空吸引脱水処理した後、七の脱水ブーキ
を前記rp * ts+から剥離除去する汚泥の脱水同
化処理方法であって、la記脱水部161 K’おいて
、真空度維持用部材(7)によシ、前記p布131の外
表面に付着された汚泥よシも外方からのflL気を防止
した状態で脱水処理することt特徴とする汚泥の脱水固
化処理方法。 ■ 前記真空度維持用部材として、前記p布t8Jと同
調して回前自社に設けた通気性の−低いシート部材ll
lを用いるものである特IfFm氷の範囲第■項に記載
の汚泥の脱水固化処理方法。 ■ 前記真空度維持用部材として、前記p布13Jと同
調して回前自社に設けた非通気性のシート部材を用いる
ものである特ffF請求の範囲第■項に記載の汚泥の脱
水同化処理方法。 ■ 前記汚泥が下水汚泥であシ、かり、la記固化材と
して高アルミナ高硫酸塩責セメントに用いるものである
特許請求の範囲第■ないし■項のいずれかに記載の汚泥
の脱水固化処理方法。
[Claims] ■ Mixed sludge of sludge and solidifying material was attached to the outer surface of #Fi131 in the sludge attachment section (6), and subjected to vacuum suction dewatering in the sludge total dewatering section +61 in step 7. The dehydration and assimilation treatment method for sludge includes peeling off and removing the dehydration bag No. 7 from the rp*ts+, in which in the dewatering section 161 K', the vacuum degree maintaining member (7) is attached to the p cloth. A method for dewatering and solidifying sludge, characterized in that the sludge adhering to the outer surface of the sludge is dehydrated while preventing flL air from outside. ■ As the member for maintaining the degree of vacuum, a sheet member with low air permeability, which was previously provided in-house in conjunction with the P cloth T8J, was used.
The method for dewatering and solidifying sludge according to item (2) above, which uses ice. (2) The dehydration and assimilation treatment of sludge according to claim (2), wherein a non-breathable sheet member previously provided in-house in conjunction with the P cloth 13J is used as the vacuum degree maintaining member. Method. ■ The sludge dehydration and solidification treatment method according to any one of claims 1 to 3, wherein the sludge is sewage sludge, and is used as a solidification material in high alumina high sulfate cement. .
JP59039674A 1984-02-29 1984-02-29 Dehydration and coagulation treatment of sludge Pending JPS60183100A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59039674A JPS60183100A (en) 1984-02-29 1984-02-29 Dehydration and coagulation treatment of sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59039674A JPS60183100A (en) 1984-02-29 1984-02-29 Dehydration and coagulation treatment of sludge

Publications (1)

Publication Number Publication Date
JPS60183100A true JPS60183100A (en) 1985-09-18

Family

ID=12559641

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59039674A Pending JPS60183100A (en) 1984-02-29 1984-02-29 Dehydration and coagulation treatment of sludge

Country Status (1)

Country Link
JP (1) JPS60183100A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62172179A (en) * 1986-01-25 1987-07-29 株式会社クボタ Spiral carrying type drier

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5520602A (en) * 1978-06-22 1980-02-14 Mitsubishi Electric Corp Dehydrator for sludge
JPS5564815A (en) * 1978-11-10 1980-05-15 Nippon Solid Co Ltd Dehydrator
JPS5811016A (en) * 1981-07-11 1983-01-21 Tsukishima Kikai Co Ltd Belt press type dehydrator

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5520602A (en) * 1978-06-22 1980-02-14 Mitsubishi Electric Corp Dehydrator for sludge
JPS5564815A (en) * 1978-11-10 1980-05-15 Nippon Solid Co Ltd Dehydrator
JPS5811016A (en) * 1981-07-11 1983-01-21 Tsukishima Kikai Co Ltd Belt press type dehydrator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62172179A (en) * 1986-01-25 1987-07-29 株式会社クボタ Spiral carrying type drier
JPH0586552B2 (en) * 1986-01-25 1993-12-13 Kubota Kk

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