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JPH0771680B2 - Sludge dewatering method - Google Patents
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JPH0771680B2 - Sludge dewatering method - Google Patents

Sludge dewatering method

Info

Publication number
JPH0771680B2
JPH0771680B2 JP62257783A JP25778387A JPH0771680B2 JP H0771680 B2 JPH0771680 B2 JP H0771680B2 JP 62257783 A JP62257783 A JP 62257783A JP 25778387 A JP25778387 A JP 25778387A JP H0771680 B2 JPH0771680 B2 JP H0771680B2
Authority
JP
Japan
Prior art keywords
sludge
dehydrated
slaked lime
dehydration
added
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 - Fee Related
Application number
JP62257783A
Other languages
Japanese (ja)
Other versions
JPH0199700A (en
Inventor
秀典 岡橋
清彦 徳永
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP62257783A priority Critical patent/JPH0771680B2/en
Publication of JPH0199700A publication Critical patent/JPH0199700A/en
Publication of JPH0771680B2 publication Critical patent/JPH0771680B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、汚泥をカチオン系の高分子凝集剤の添加によ
り凝集させた後重力脱水し、重力脱水した脱水汚泥を更
に強制脱水する汚泥脱水処理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to sludge dehydration in which sludge is coagulated by adding a cationic polymer coagulant and then gravity dehydrated, and gravity dehydrated dehydrated sludge is further forcedly dehydrated. Regarding processing method.

〔従来の技術〕[Conventional technology]

従来の上記汚泥脱水処理方法では、汚泥及び脱水汚泥か
ら臭気が発生しやすく、汚泥の貯留及び移送並びに焼却
時に環境を悪化するために、汚泥を消臭する消石灰を、
前記高分子凝集剤の添加前或いは添加と同時に汚泥に添
加することが考えられていた。
In the conventional sludge dewatering method, odor is easily generated from sludge and dewatered sludge, to deteriorate the environment during storage and transfer of sludge and incineration, slaked lime to deodorize sludge,
It has been considered to add to the sludge before or simultaneously with the addition of the polymer flocculant.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかし、カチオン系の高分子凝集剤が汚泥に対して有効
に働くのはpH5〜9であるのに対し、消石灰を汚泥の消
臭に必要な最低量を添加するだけでも、汚泥は、ほぼpH
11になり、このため小さなフロックしか形成できず、そ
のために脱水効率が低下するばかりか、水分中に消石灰
が溶解しているために、汚泥を重力脱水する時には汚泥
中に添加した消石灰がろ液中に溶けて流出しやすく、充
分な汚泥消臭効果を維持するためには、消石灰の添加量
を増やさなければならないという問題があった。
However, while the cationic polymer flocculant works effectively on sludge at pH 5-9, even if the minimum amount of slaked lime required for deodorizing sludge is added, the sludge will be almost at pH.
Therefore, only small flocs can be formed, which not only lowers the dehydration efficiency, but also dissolves slaked lime in the water, so when sludge is gravity dehydrated, the slaked lime added to the sludge is filtered. There is a problem that it is necessary to increase the amount of slaked lime added in order to maintain a sufficient sludge deodorizing effect by dissolving in it and flowing out.

本発明の目的は、カチオン系の高分子凝集剤による凝集
機能を低下させることなく、汚泥を消臭する点にある。
An object of the present invention is to deodorize sludge without deteriorating the aggregating function of the cationic polymer aggregating agent.

〔問題点を解決するための手段〕 本発明の汚泥脱水処理方法の特徴手段は、脱水汚泥に対
し、消石灰を添加して消臭した後に前記強制脱水するこ
とにあり、その作用効果は、次の通りである。
[Means for Solving Problems] The characteristic means of the sludge dewatering treatment method of the present invention is to dehydrate sludge, to deodorize by adding slaked lime, and then to perform forced dehydration. Is the street.

〔作 用〕[Work]

つまり、消石灰添加前の汚泥がカチオン系の高分子凝集
剤の添加により凝集されて大きなフロックを形成した
後、重力脱水により大きなフロック間に遊離した水が効
率良く充分に脱水され、水分の少くなった脱水汚泥に消
石灰を添加することにより、消石灰がろ液中に溶け出す
ことが少く、しかも脱水汚泥は消臭には充分な水分を保
っているので、十分に脱水汚泥を消臭することができ
る。
In other words, the sludge before addition of slaked lime is aggregated by the addition of the cationic polymer flocculant to form large flocs, and the water liberated between the large flocs by gravity dehydration is efficiently and sufficiently dehydrated to reduce the water content. By adding slaked lime to the dehydrated sludge, slaked lime rarely dissolves in the filtrate, and since the dehydrated sludge retains sufficient water for deodorization, it is possible to sufficiently deodorize the dehydrated sludge. it can.

〔発明の効果〕〔The invention's effect〕

従って、フロック形成後に消石灰を添加するので、カチ
オン系の高分子凝集剤による汚泥に対する凝集機能を低
下させずに汚泥を消臭でき、汚泥処理環境を悪化させず
に効率良く脱水作業が行えるようになった。
Therefore, since slaked lime is added after the formation of flocs, the sludge can be deodorized without deteriorating the coagulation function of sludge by the cationic polymer coagulant, and the dehydration work can be performed efficiently without deteriorating the sludge treatment environment. became.

しかも、ろ液中に溶出する消石灰の量が少いために、汚
泥消臭のために使用する消石灰の量を少なくできて、経
済性を向上するとともに、水分の少くなった脱水汚泥中
へ添加された消石灰は、汚泥より粒子径が大きいため
に、脱水助剤として強制脱水の脱水効率を更に上げるこ
とができるようになった。
Moreover, since the amount of slaked lime that elutes in the filtrate is small, the amount of slaked lime used for deodorizing sludge can be reduced, which improves economic efficiency and is added to dehydrated sludge with low water content. Moreover, since slaked lime has a larger particle size than sludge, it has become possible to further improve the dehydration efficiency of forced dehydration as a dehydration aid.

〔実施例〕〔Example〕

次に、本発明の実施例を、図面に基づいて説明する。 Next, an embodiment of the present invention will be described with reference to the drawings.

第2図に示すように、第1貯留層(1)から供給される
被処理物と、第2貯留層(2)から供給されるカチオン
系の高分子凝集剤を凝集混和する混和機(3)を設け、
無端帯状の第1回動ろ布(4)と、ケース側壁(5)並
びに仕切壁(6)との間に、前記混和機(3)からの凝
集処理物を供給して水分を自重ろ過させる重力脱水部
(7)を形成すると共に、その重力脱水部(7)のろ布
(4)回動方向下手側に、第1回動ろ布(4)に載って
送り出されてくる汚泥ケーキの厚みを調整する調厚ロー
ル(8)を設け、そして、その下手側に、前記第1回動
ろ布(4)との間に、厚みを調整されたケーキを挟圧す
る第2回動ろ布(9)を設けて、直線状経路の輾厚脱水
ゾーン(A)、大径円弧状経路の圧縮脱水ゾーン(B)
及び、蛇行状経路(C)からなる強制脱水部(10)を形
成し、もって、第1ろ布(4)の重力脱水部(7)から
強制脱水部(10)にわたっての回動に伴い、し尿や都市
下水あるいは産業廃水等、各種の水処理に伴って発生す
る汚泥等の被処理物を連続的に脱水処理するようにベル
トプレス型脱水機を構成してあり、上記ベルトプレス型
脱水機からの汚泥を消臭するために、調厚ロール(8)
の手前に、重力脱水した脱水汚泥に消石灰を添加する添
加装置(12)を配置してある。
As shown in FIG. 2, a mixer (3) for aggregating and mixing the object to be treated supplied from the first reservoir (1) and the cationic polymer flocculant supplied from the second reservoir (2). ),
Between the endless belt-shaped first rotating filter cloth (4) and the case side wall (5) and the partition wall (6), the coagulation-treated product from the kneading machine (3) is supplied to perform self-weight filtration of water. While forming the gravity dehydration section (7), the sludge cake sent out on the first rotation filter cloth (4) is sent to the gravity dehydration section (7) on the lower side in the rotating direction of the filter cloth (4). A thickness adjusting roll (8) for adjusting the thickness is provided, and on the lower side thereof, a second rotating filter cloth for pressing the thickness-adjusted cake between the first rotating filter cloth (4). (9) is provided, and the thickness dewatering zone (A) of a straight path and the compression dewatering zone (B) of a large-diameter circular arc path are provided.
And, the forced dehydration part (10) formed of the meandering path (C) is formed, and accordingly, with the rotation of the first filter cloth (4) from the gravity dehydration part (7) to the forced dehydration part (10), The belt press type dehydrator is configured to continuously dehydrate the object to be treated such as sludge generated by various water treatments such as human waste, municipal sewage or industrial wastewater. Rolls (8) for deodorizing sludge from
An addition device (12) for adding slaked lime to gravity-dehydrated dehydrated sludge is arranged in front of the.

つまり、汚泥を脱処理する時に、汚泥に対する消臭方法
を、第1図のブロック図で順を追って説明すると、汚泥
をカチオン系の高分子凝集剤の添加により凝集させた後
重力脱水し、重力脱水した脱水汚泥に対し、消石灰を添
加して汚泥を消臭し、そして更にその脱水汚泥を強制脱
水する。
That is, when dewatering sludge, the deodorizing method for sludge will be explained step by step with the block diagram of FIG. 1. Sludge is flocculated by adding a cationic polymer flocculant, and then gravity dehydration is performed. Slaked lime is added to the dehydrated dehydrated sludge to deodorize the sludge, and the dehydrated sludge is further forcedly dehydrated.

尚、前記高分子凝集剤は、0.5〜1.5wt%で、1mm〜5mmの
フロックが形成され、また、汚泥消臭のために消石灰
を、最低3〜5%添加され、消石灰の吸着作用によって
臭気性分が脱臭される。
The above-mentioned polymer flocculant is 0.5 to 1.5 wt% and forms flocs of 1 mm to 5 mm, and at least 3 to 5% of slaked lime is added for deodorizing sludge. The deodorizing nature.

〔別実施例〕[Another embodiment]

前記脱水汚泥に添加する消石灰は、粉末のままでも、溶
液の状態でも良く、また、添加する位置は、調厚ロール
(8)のすぐ後でも良い。
The slaked lime added to the dehydrated sludge may be in the form of powder or in the form of a solution, and may be added immediately after the thickness adjusting roll (8).

前記強制脱水を行うには、ベルトプレス型脱水機による
以外に、遠心脱水機等による方法でも良い。
In order to perform the forced dehydration, a centrifugal dehydrator or the like may be used instead of the belt press type dehydrator.

前記調厚ロール(8)の手前の消石灰添加箇所には、脱
水汚泥と消石灰の混和を良くするために、撹拌装置を設
けても良い。
A stirrer may be provided at a location where slaked lime is added before the thickness adjusting roll (8) in order to improve mixing of the dehydrated sludge and slaked lime.

尚、特許請求の範囲の項に図面との対照を便利にする為
に符号を記すが、該記入により本発明は添付図面の構造
に限定されるものではない。
It should be noted that reference numerals are added to the claims for convenience of comparison with the drawings, but the present invention is not limited to the structures of the accompanying drawings by the entry.

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

図面は本発明に係る汚泥脱水処理方法の実施例を示し、
第1図は全体の処理方法を示すブロック図、第2図はベ
ルトプレス型脱水機の概略側面図である。
Drawing shows an example of a sludge dewatering method according to the present invention,
FIG. 1 is a block diagram showing the entire processing method, and FIG. 2 is a schematic side view of a belt press type dehydrator.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】汚泥をカチオン系の高分子凝集剤の添加に
より凝集させた後重力脱水し、重力脱水した脱水汚泥を
更に強制脱水する汚泥脱水処理方法であって、 前記脱水汚泥に対し、消石灰を添加して消臭した後に前
記強制脱水する汚泥脱水処理方法。
1. A sludge dewatering method for coagulating sludge by the addition of a cationic polymer coagulant, followed by gravity dehydration, and forced dehydration of gravity dehydrated dehydrated sludge. A sludge dewatering treatment method in which the above is added to deodorize and then the above-mentioned forced dewatering is performed.
JP62257783A 1987-10-13 1987-10-13 Sludge dewatering method Expired - Fee Related JPH0771680B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62257783A JPH0771680B2 (en) 1987-10-13 1987-10-13 Sludge dewatering method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62257783A JPH0771680B2 (en) 1987-10-13 1987-10-13 Sludge dewatering method

Publications (2)

Publication Number Publication Date
JPH0199700A JPH0199700A (en) 1989-04-18
JPH0771680B2 true JPH0771680B2 (en) 1995-08-02

Family

ID=17311041

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62257783A Expired - Fee Related JPH0771680B2 (en) 1987-10-13 1987-10-13 Sludge dewatering method

Country Status (1)

Country Link
JP (1) JPH0771680B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6013205B2 (en) * 2013-01-18 2016-10-25 メタウォーター株式会社 Concentrator
JP6121247B2 (en) * 2013-06-04 2017-04-26 水ing株式会社 Deodorizing cake deodorizing method and apparatus

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59154200A (en) * 1983-02-24 1984-09-03 Ichikawa Keori Kk Treatment of sludge

Also Published As

Publication number Publication date
JPH0199700A (en) 1989-04-18

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