JPH0199700A - Sludge dewatering treatment method - Google Patents
Sludge dewatering treatment methodInfo
- Publication number
- JPH0199700A JPH0199700A JP62257783A JP25778387A JPH0199700A JP H0199700 A JPH0199700 A JP H0199700A JP 62257783 A JP62257783 A JP 62257783A JP 25778387 A JP25778387 A JP 25778387A JP H0199700 A JPH0199700 A JP H0199700A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- slaked lime
- gravity
- dehydration
- 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.)
- Granted
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
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 Application Field] The present invention provides a sludge dewatering treatment in which sludge is flocculated by adding a cationic polymer flocculant and then subjected to gravity dewatering, and the gravity dehydrated sludge is further forcibly dehydrated. Regarding the method.
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 treatment method, sludge and dehydrated sludge tend to emit odors, and the environment is degraded when storing, transporting, and incinerating the sludge, so slaked lime to deodorize the sludge is not used.
It has been considered to add it to the sludge simultaneously with the addition of the polymer flocculant.
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、汚泥の消臭のた
めに、消石灰を最低量添加すると、汚泥は、はぼpHl
lになり、結局小さなフロックしか形成できず、脱水効
率が低下するばかりか、汚泥を重力脱水する時に汚泥中
に添加した消石灰がろ液中に溶けて流出しやすく、汚泥
消臭効果を高(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欠点があった。However, while cationic polymer flocculants work effectively on sludge at a pH of 5 to 9, when the minimum amount of slaked lime is added to deodorize sludge, the sludge has a pH of 5 to 9.
In the end, only small flocs are formed, which not only reduces the dewatering efficiency, but also makes it difficult for the sludge deodorizing effect to increase ( In order to maintain this condition, the amount of slaked lime added must be increased.
本発明の目的は、カチオン系の高分子凝集剤による凝集
機能を低下させずに、汚泥を消臭する点にある。An object of the present invention is to deodorize sludge without reducing the flocculating function of a cationic polymer flocculant.
〔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、重力脱水した
汚泥に対し、強制脱水する前に消石灰を添加して汚泥を
消臭することにあり、その作用効果は、次の通りである
。[Means for Solving the Problems] The characteristic means of the sludge dewatering method of the present invention is that slaked lime is added to deodorize the sludge after gravity dewatering before forced dewatering. The effects are as follows.
つまり、汚泥は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に形成した後、重力脱水によ
りフロック間に遊離した水が効率良く大量に脱水され、
水分の少くなった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は出すことが少く、効率良く消臭作
用をする。In other words, the sludge is flocculated by adding a cationic polymer flocculant to form large flocs, and then the water released between the flocs is efficiently dehydrated in large quantities by gravity dewatering.
By adding slaked lime to sludge with reduced water content,
Slaked lime rarely dissolves into the filtrate and has an efficient deodorizing effect.
従って、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、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, sludge can be deodorized without reducing the sludge flocculating function of the cationic polymer flocculant, and dewatering work can now be carried out efficiently without deteriorating the environment.
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撥を少くできて、経済
性を向上させられ、その上、水分の少くなった汚泥中へ
添加された消石灰は、汚泥より粒子径が大きいために、
脱水助剤として脱水効率を更に上げることができる。Moreover, since the amount of slaked lime eluted into the filtrate is small, the amount of slaked lime used for sludge deodorization can be reduced, improving economic efficiency. The added slaked lime has a larger particle size than the sludge, so
As a dehydration aid, dehydration efficiency can be further increased.
、〔実施例〕 次に、本発明の実施例を、図面に基づいて説明する。,〔Example〕 Next, embodiments of the present invention will be described based on the drawings.
第2図に示すように、第1貯rg1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凹
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、直線状経路の幅圧脱
水ゾーン(^)、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、重力脱水した汚泥に消石灰を添加す
る添加装置(12)を配置しである。As shown in FIG. 2, a mixer ( 3), an endless strip-shaped first rotating filter cloth (4), and a case side wall (5).
) and the partition wall (6), a gravity dehydration section (7) is formed between which the agglomerated product from the mixer (3) is supplied and water is filtered by gravity, and the gravity dehydration section (7) A thickness adjustment roll (8) for adjusting the thickness of the sludge cake carried on the first rotary filter cloth (4) is provided on the lower side in the rotating direction of the filter cloth (4), and the lower side thereof. A second rotary filter cloth (9) is provided between the first concave filter cloth (4) to pinch the cake whose thickness has been adjusted, and a width pressure dewatering zone (^) of a linear path is provided. , compression dewatering zone (B
), and a forced dehydration section (10
), thereby forming a gravity dewatering section (7) of the first filter cloth (4).
) to the forced dewatering section (10), the belt press continuously dewaters materials to be treated such as sludge generated in various water treatments such as human waste, urban sewage, and industrial wastewater. In order to deodorize the sludge from the belt press type dehydrator, an addition device (12) for adding slaked lime to the gravity-dehydrated sludge is installed before the thickness adjusting roll (8). It is arranged.
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、そして更にその汚泥を強制脱水する。In other words, when deprocessing sludge, the deodorizing method for sludge is explained step by step using the block diagram in Figure 1. After sludge is flocculated by adding a cationic polymer flocculant, it is dehydrated by gravity. Slaked lime is added to the dehydrated sludge to deodorize the sludge, and then the sludge is forcibly dehydrated.
尚、前記高分子凝集剤は、0.5〜1.5wt%で、1
m〜5ml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。In addition, the polymer flocculant is 0.5 to 1.5 wt%, and 1
A floc of m to 5 ml is formed, and at least 3 to 5% of slaked lime is added to deodorize the sludge, and odor components are deodorized by the adsorption action of the slaked lime.
前記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 sludge may be in the form of a powder or a solution.
) may be immediately after.
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 method such as a centrifugal dehydrator may be used instead of using a 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、汚
泥と消石灰の混和を良くするために、攪拌装置を設けて
も良い。A stirring device may be provided at the slaked lime addition point before the thickness adjusting roll (8) in order to improve the mixing of the 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。Incidentally, although reference numerals are written in the claims section for convenient comparison with the drawings, the present invention is not limited to the structure shown in the accompanying 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。The drawings show an example of the sludge dewatering treatment method according to the present invention,
FIG. 1 is a block diagram showing the overall processing method, and FIG. 2 is a schematic side view of the belt press type dehydrator.
Claims (1)
た後重力脱水し、重力脱水した汚泥を更に強制脱水する
汚泥脱水処理方法であって、重力脱水した汚泥に対し、
強制脱水する前に消石灰を添加して汚泥を消臭する汚泥
脱水処理方法。This is a sludge dewatering treatment method in which sludge is flocculated by adding a cationic polymer flocculant and then subjected to gravity dewatering, and the gravity dehydrated sludge is further forcibly dehydrated.
A sludge dewatering method that deodorizes sludge by adding slaked lime before forced dewatering.
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 true JPH0199700A (en) | 1989-04-18 |
| JPH0771680B2 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) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014136201A (en) * | 2013-01-18 | 2014-07-28 | Metawater Co Ltd | Concentrator |
| JP2014233693A (en) * | 2013-06-04 | 2014-12-15 | 水ing株式会社 | Deodorizing method and device of dehydrated cake |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59154200A (en) * | 1983-02-24 | 1984-09-03 | Ichikawa Keori Kk | Treatment of sludge |
-
1987
- 1987-10-13 JP JP62257783A patent/JPH0771680B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59154200A (en) * | 1983-02-24 | 1984-09-03 | Ichikawa Keori Kk | Treatment of sludge |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014136201A (en) * | 2013-01-18 | 2014-07-28 | Metawater Co Ltd | Concentrator |
| JP2014233693A (en) * | 2013-06-04 | 2014-12-15 | 水ing株式会社 | Deodorizing method and device of dehydrated cake |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0771680B2 (en) | 1995-08-02 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |