JPS5898200A - Dehydration of sludge - Google Patents

Dehydration of sludge

Info

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
Application number
JP56195009A
Other languages
Japanese (ja)
Inventor
Hiroichi Sakano
坂野 博一
Kazunori Matsumoto
松本 和典
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP56195009A priority Critical patent/JPS5898200A/en
Publication of JPS5898200A publication Critical patent/JPS5898200A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To remarkably enhance the dehydrating power of a dehydrator, in dehydrating excess sludge formed in the purification of filthy water, by adding an inorganic salt to the sludge, reserving the sludge for a specified period, and then dehydrating the sludge. CONSTITUTION:Slurry 1 of biocells or SS contg. biocells, e.g. active sludge or sludge formed in the treatment of night soil, is let flow into a mixing cell 2. At this time, an inexpensive innoxious inorganic salt such as NaCl or its solution 3 is concurrently added to the slurry, and the slurry is agitated by an agitator 4 and reserved as such for a specified period. During the reserving period, water in cells is permeated through biomembranes and exude outside the cells by osmotic pressure. The slurry rendered into said state is fed to a dehydrator 6 by a pump 5 and dehydrated. An effluent 7 is desalinated by a reverse osmosis device 8. Desalinated water 9 is drained as purified water, while water 10 having high concentration of the salt is returned to the mixing cell 2 and reused. The water-retaining ratio of dehydrated cake discharged from the dehydrator 6 is remarkably lowered so that the costs of incineration, disposal, etc. in the next step can be lowered.

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.

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

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)

【特許請求の範囲】[Claims] (1)  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・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.
(2)  汚泥を脱水処理するに際し、その前処理どし
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.
JP56195009A 1981-12-03 1981-12-03 Dehydration of sludge Pending JPS5898200A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (4)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
Sharma Industrial chemistry
JP3467492B2 (en) How to purify sewage
US5885461A (en) Process and system for treatment of pig and swine manure for environmental enhancement
JPH09510651A (en) Method for purifying medium containing organic waste
ES2404140T3 (en) Procedure and device for the regeneration of contaminated washing solutions
CN105777217A (en) Resourceful treatment utilization method and device for livestock excrement
US3963637A (en) Compositions for treating domestic and industrial liquid wastes
CN206266392U (en) A kind of papermaking wastewater zero-discharge treatment system
Cornwell et al. Characteristics of Acid‐Treated Alum Sludges
CN207210182U (en) A kind of percolate embrane method concentrate decrement treatment equipment
JPS5898200A (en) Dehydration of sludge
CN106517661B (en) A kind of papermaking wastewater treatment system
CN111733781A (en) Device and method for in-situ collection, treatment and disposal of river and lake algae
JPH0214794A (en) Treatment of waste liquid after regeneraton of ion exchange apparatus
CN108975565A (en) A kind of steel and iron industry strong brine processing unit and method
US3812032A (en) Process for treating domestic and industrial liquid wastes
US2296523A (en) Process for the biological and simultaneous purification of waste liquors and their slimes
GB1587205A (en) Process for the treatment disinfection neutralisation and/or detoxification of heavily polluted waste waters
JPS5624089A (en) Coagulation and sedimentation treatment of waste water of pulp mill
CN209338314U (en) A kind of chemical wastewater treatment system
JPS59186696A (en) Treatment of waste water
JP4405286B2 (en) Fishery processing wastewater scum treatment method
SU912670A1 (en) Apparatus for purifying effluents from dyening and finishing processes
JP2767314B2 (en) Method for treating sludge polluted water and sludge dewatering device
JPH0515879A (en) Device for processing circulating water