JPS5898200A - Dehydration of sludge - Google Patents
Dehydration of sludgeInfo
- Publication number
- JPS5898200A JPS5898200A JP56195009A JP19500981A JPS5898200A JP S5898200 A JPS5898200 A JP S5898200A JP 56195009 A JP56195009 A JP 56195009A JP 19500981 A JP19500981 A JP 19500981A JP S5898200 A JPS5898200 A JP S5898200A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- water
- slurry
- dehydrating
- dehydrator
- 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
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は汚泥脱水方法の改良に関する。[Detailed description of the invention] The present invention relates to improvements in sludge dewatering methods.
現在下水処理場、し尿処理場寺の余剰汚泥はデカ−73
−、遠心分離機、ペルドブしス、フィルタープレス等で
脱水処理後、焼却、尚洋投棄晋を行っているが、脱水機
の機構的な改良がひとわたり進み性能が頭打ちとなって
いる。Excess sludge from the sewage treatment plant and human waste treatment plant is currently 73
- After dewatering using centrifuges, peridots, filter presses, etc., the waste is incinerated and then dumped in the ocean, but as mechanical improvements have been made to dehydrators, their performance has reached a plateau.
従来の脱水機は一般にスラリー中の88分とSSを聡濁
させている液(SS外部の液)とを分離する事を目的と
していた。Conventional dehydrators were generally intended to separate the 88 minutes in the slurry from the liquid that clouded the SS (liquid outside the SS).
そこで1本発明は、SSか生物、′用胞である場合にそ
のjln IIFJ 膜内部の水分(生体内水分)をも
同時に除去する拳によって脱水機による脱水性能を飛躍
的Vc1i%め、ひいては焼却8投東等のコストを下げ
ることを目的として提案されたもので、汚泥を脱水処理
するに除し、その前処理として汚泥に無機塩類を混合し
一定時曲滞留させ汚泥に含有される生体細胞内の水分を
浸透圧作用によりR411Its外に浸出させた仮、脱
水処理することを特長とする汚泥脱水方法、及び汚泥を
脱水処理するに際し、その前処理として汚泥に無機塩類
を混合し一定時間滞笛させ汚dQに含有される生体fl
ll胞円の水分を浸透圧作用により細胞外に浸出させた
後、脱水処理し、その脱離水を脱塩装置により濃厚塩水
と淡水とに分離し、そのうち濃厚塩水を前処理に再オロ
用することを特長とするとり記脱水方広を提供する。Therefore, the present invention dramatically increases the dehydration performance of the dehydrator by Vc1i% by simultaneously removing the moisture inside the membrane (biological moisture) in the case of SS or living organisms, and further incinerates it. This method was proposed for the purpose of lowering the cost of sludge, and as a pretreatment, inorganic salts are mixed with the sludge and allowed to stagnate for a certain period of time to remove the living cells contained in the sludge. A sludge dewatering method is characterized by temporarily dehydrating the water inside R411Its by leaching it out to the outside by osmotic pressure, and when dewatering sludge, as a pretreatment, inorganic salts are mixed with the sludge and left for a certain period of time. Living body fl contained in whistle dQ
After the water in the cells is leached out of the cell by osmotic pressure, it is dehydrated, and the dehydrated water is separated into concentrated salt water and fresh water using a desalting device, of which the concentrated salt water is used for pretreatment. We provide a dehydration method that is characterized by:
本発明方法においては、j脱水処理の前処理として、汚
泥に無磯塩緬を混合し汚泥に含有される生体細胞内の水
分な凝透圧作用により予め細胞外に浸出させることによ
り、その後の脱水工程において、細胞外の水分のみなら
ず細胞内の水分をも同時に除去し得るようにしたもので
ある。In the method of the present invention, as a pretreatment for the dehydration process, sludge is mixed with salt-free salt, and water contained in the sludge is leached out of the cells by the coagulant pressure action of the living cells. In the dehydration process, not only extracellular water but also intracellular water can be removed at the same time.
さらに脱水工程で生じた脱離水を脱塩装置により濃厚塩
水と淡水とに分離し、そのうち濃厚塩水を前処理に再利
用させるため、脱水グー十に同伴するわずかな無磯塩緬
に相当する菫を補給してやるだけで連続的な脱水処理を
円滑に行なうことができ、極めて経η的であQとともに
。Furthermore, the dehydrated water generated in the dehydration process is separated into concentrated salt water and fresh water using a desalination device, and in order to reuse the concentrated salt water for pretreatment, the violet equivalent to a small amount of unsalted seaweed that accompanies the dehydrated goo is removed. Continuous dehydration processing can be carried out smoothly simply by replenishing the water.
無機塩類を系外に、 jJF出てることがないため環境
汚染等の問題を発生しない。Since no inorganic salts or jJF are released outside the system, there are no problems such as environmental pollution.
次に本発明方法の一冥施例を図面に基づいて説明1−る
。Next, one embodiment of the method of the present invention will be explained based on the drawings.
第1図で、活性汚泥、し尿処理汚泥等の生物1tlI+
胞あるいは、生物細胞を含O8sのスラリー1を楕2に
流入させる。ここでNaC11等の安f+ltiで無害
な無イ幾塩又汀その訂液3ン同時に混合槽2添加し、撹
拌装置4で撹拌して一定時間浦笛さ一1!′る。すると
この間に削11#内の水分は浸透圧で生体膜を通過して
細1@外へ浸出する。このような状態になったスラリー
をボクブ5によって脱水機6に移送してノ況水する。In Figure 1, living organisms such as activated sludge, human waste sludge, etc.
A slurry 1 containing O8s containing cells or biological cells is made to flow into the ellipse 2. At this point, a harmless non-toxic salt such as NaC11 is added to the mixing tank 2 at the same time, stirred by the stirring device 4, and stirred for a certain period of time. 'ru. During this time, the water inside the cut 11# passes through the biological membrane due to osmotic pressure and leaks out of the cut 11@. The slurry in such a state is transferred to the dehydrator 6 by the bokubu 5 and is dehydrated.
なお、脱離水7は逆浸透(reverse oamoa
ia)装置8で脱塩を行ない、塩分を除去した水9は処
理水として糸外へ1ノ1出するかあるいは再利用する。Note that the desorbed water 7 is generated by reverse osmosis (reverse osmosis).
ia) The water 9 from which salt is removed by desalination in the device 8 is discharged to the outside of the yarn as treated water or reused.
また塩分濃度の11Gい水1o(ま混合槽2へもどして
書ひ細側日水分を反量さぜり為に利用すの0なお逆浸透
装置は従来がら周知の千面彊型。In addition, the water with a salinity of 11G (100 g) is returned to the mixing tank 2 and used to mix up the water content.
前型、スバイラIL巻き型、中空糸状模型等があり2
これらの型式のものを使用1〜ればよい。There are two types: front model, Svaira IL winding model, hollow fiber model, etc.
It is sufficient to use one of these types.
このような系によって運転する場合脱水グー十11に同
伴するわずがな塩分に相当する鎗を塩供給ライン6から
添加してやる事によって円滑に運転を継dすることがで
きる。When such a system is operated, the operation can be continued smoothly by adding from the salt supply line 6 a spoon equivalent to the slight salt accompanying the dehydrated goo 11.
なお本発明で使用される無機塩類は一般的な;tlfi
成塩類でよく、安価で堆り扱いやすく1m解じやすく、
また無害なものであればなお望ましい。Note that the inorganic salts used in the present invention are common; tlfi
Compound salts are suitable, inexpensive, easy to handle, and easy to unravel for 1 m.
It is even more desirable if it is harmless.
次に本発明方法の作用、効果をR認する為に行った試懺
結果を記す。Next, the results of a trial conducted to confirm the action and effect of the method of the present invention will be described.
第2図のような攪拌槽21に生体fill I掴を含む
スラリー(下水処理場で生じた余剰どり泥)を投入し、
これに一定量のNtrClを添加して攪P1機22で一
定時間攪拌後、このスラリーなへリドプレス型脱水機に
よって脱水したところ、第1辰の結果が、′Xjもれた
口
第1表
比較1クリとしてNaCeを添加しないで直接ベルトプ
レス型呪水磯て上記仮処理物を脱水したところ、脱水グ
ー十含水率は79重量%であり1本発明方法による脱水
効果のほうが格段VC優れていることが判明した。A slurry (excess sludge generated at a sewage treatment plant) containing biological fill I is poured into a stirring tank 21 as shown in Fig. 2,
A certain amount of NtrCl was added to this, and after stirring for a certain period of time using the stirring P1 machine 22, this slurry was dehydrated using a helido press type dehydrator. When the above temporarily treated product was directly dehydrated using a belt press-type jusuiiso without adding NaCe, the water content of the dehydrated product was 79% by weight, and the dehydration effect obtained by the method of the present invention was significantly superior in VC. It has been found.
以上のよ5 VC,不発明方、去によれば、活性汚泥、
し尿処理汚泥、その他の生吻細制を含む汚泥、あるいは
生9IJ細胞を含むSSのスラリー等を脱水丁0に際し
、従来の脱水力法に比べて格段の脱水効果が得られ、か
つ経% I’l’Jであって公害問題を生起させない寺
優れた長所をもつ。According to the above 5 VC, non-inventor, activated sludge,
When dehydrating sludge treated with human waste, other sludge containing sludge, or SS slurry containing live 9IJ cells, a marked dehydration effect can be obtained compared to the conventional dehydration method, and the dehydration rate can be reduced by %I. It has the great advantage of being 'l'J and does not cause pollution problems.
第1図は本発明方法の一実施例を示す概要図。
第2図は試験装置を示す説明図である。
i −s sスラリ、2 混合槽、6・・・添m勲磯塩
、4 ・攪拌装置、6・脱水機、7・・脱離水。
8 逆浸透装置、9 淡水、10・羨jψ塩水。
11 脱水グー十。
・ :1.、二
(力
覇I関
麓2図FIG. 1 is a schematic diagram showing an embodiment of the method of the present invention. FIG. 2 is an explanatory diagram showing the test device. i-ss slurry, 2. Mixing tank, 6. Added salt, 4. Stirring device, 6. Dehydrator, 7. Desorbed water. 8 reverse osmosis equipment, 9 fresh water, 10 salt water. 11 Dehydration goo ten.・ :1. , 2 (Rikiha I Sekiroku 2)
Claims (2)
て汚泥に無機塩・項を混合し一定時間浦留させ汚泥に含
有される生体細胞内の水分を浸透圧作用により細胞外に
浸出させた後、脱水処理することを特長とする汚泥脱水
方法。(1) When dehydrating sludge, as a pretreatment, inorganic salts are mixed with the sludge and left to linger for a certain period of time to leach out the water inside living cells contained in the sludge to the outside of the cells by osmotic pressure. , a sludge dewatering method characterized by dewatering.
て汚泥に無機塩類を混合し一定時間面笛させ汚泥に含有
される生体τ用胞内の水分?浸透圧作用により細胞外に
浸出させた後、ノ況水処理し、その脱離ボを脱塩装置に
より一厚塩水と淡水とに分離し、そのうち刺17塩水を
前処理に再利用することを特長とする汚泥脱水方法。(2) When dehydrating sludge, as a pretreatment, inorganic salts are mixed with the sludge and the sludge is allowed to float for a certain period of time. After being leached out of the cells by osmotic pressure, it is treated with fresh water, and the desorbed water is separated into thick salt water and fresh water using a desalination device, of which 17 brine is reused for pretreatment. Features of sludge dewatering method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56195009A JPS5898200A (en) | 1981-12-03 | 1981-12-03 | Dehydration of sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56195009A JPS5898200A (en) | 1981-12-03 | 1981-12-03 | Dehydration of sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5898200A true JPS5898200A (en) | 1983-06-10 |
Family
ID=16334010
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56195009A Pending JPS5898200A (en) | 1981-12-03 | 1981-12-03 | Dehydration of sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5898200A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104671623A (en) * | 2015-02-04 | 2015-06-03 | 福建省洋屿化工工贸有限公司 | Osmotic treatment process of municipal sewage sludge |
CN108503188A (en) * | 2018-04-27 | 2018-09-07 | 江苏大学 | A kind of processing of deeply dehydrating sludge and its additive recovery method |
CN109336352A (en) * | 2018-11-05 | 2019-02-15 | 李舒馨 | A kind of method for sludge treatment |
JP2020049452A (en) * | 2018-09-28 | 2020-04-02 | 株式会社石垣 | Osmotic pressure dewatering method of filter press and osmotic pressure dewatering system |
-
1981
- 1981-12-03 JP JP56195009A patent/JPS5898200A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104671623A (en) * | 2015-02-04 | 2015-06-03 | 福建省洋屿化工工贸有限公司 | Osmotic treatment process of municipal sewage sludge |
CN108503188A (en) * | 2018-04-27 | 2018-09-07 | 江苏大学 | A kind of processing of deeply dehydrating sludge and its additive recovery method |
JP2020049452A (en) * | 2018-09-28 | 2020-04-02 | 株式会社石垣 | Osmotic pressure dewatering method of filter press and osmotic pressure dewatering system |
CN109336352A (en) * | 2018-11-05 | 2019-02-15 | 李舒馨 | A kind of method for sludge treatment |
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