JPS60238200A - Treatment of sludge - Google Patents

Treatment of sludge

Info

Publication number
JPS60238200A
JPS60238200A JP59093046A JP9304684A JPS60238200A JP S60238200 A JPS60238200 A JP S60238200A JP 59093046 A JP59093046 A JP 59093046A JP 9304684 A JP9304684 A JP 9304684A JP S60238200 A JPS60238200 A JP S60238200A
Authority
JP
Japan
Prior art keywords
sludge
treated
tank
compressed air
supply pipe
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
JP59093046A
Other languages
Japanese (ja)
Inventor
Kiyoji Yamazaki
山崎 喜代治
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.)
Koyo Giken KK
Original Assignee
Koyo Giken KK
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 Koyo Giken KK filed Critical Koyo Giken KK
Priority to JP59093046A priority Critical patent/JPS60238200A/en
Publication of JPS60238200A publication Critical patent/JPS60238200A/en
Pending legal-status Critical Current

Links

Landscapes

  • Physical Water Treatments (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To efficiently treat high concn. sludge by fine air bubbles, by mixing compressed air into a sludge supply pipe and directly breaking said air by an ultrasonic wave to adhere the same to the solid component in treated sludge. CONSTITUTION:Sludge 5 to be treated is guided to a nozzle 6 from a sludge tank 2 and compressed air is guided to and mixed in the downstream side of said nozzle 6. At the same time, said air formed into extremely fine air bubbles by ultrasonic waves from an oscillator 7 while said fine air bubbles are uniformly dispersed throughout the sludge 5 to be treated to be sufficiently adhered to the solid component in the sludge 5. By this method, high concn. sludge can be treated with good efficiency without requiring large amount recirculation.

Description

【発明の詳細な説明】 本発明は水処理等における特に高濃度の汚泥処理に適し
た汚泥処理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sludge treatment method suitable for particularly high concentration sludge treatment in water treatment and the like.

従来この種汚泥処理方法として、汚泥中に微細気泡を供
給して該汚泥中の固形分に付着させ、これを該汚泥の上
方に浮上させて除去するようにしたものが知られている
が、該微細気泡の該汚泥中への供給は、汚泥濃縮槽内の
分離水を加圧タンクを介して循環させると共に該加圧タ
ンク内に圧縮空気を供給し、該タンク内で該圧縮空気を
該循環水中に溶解させ、該加圧循環水を該汚泥濃縮槽に
戻す際に減圧して該溶解された圧縮空気を微細な気泡と
して供給するようにしているため、高濃度の汚泥を処理
するには該加圧タンクの圧力を非常に大きなものとする
か或いは分離水の循環量を増やすことによって該透徹水
中に〆解される圧縮空気量を増さなければならないとい
う不都合を有していた。
Conventionally, as a method for treating this kind of sludge, a method is known in which fine air bubbles are supplied into the sludge to adhere to the solid content in the sludge, and the bubbles are floated above the sludge and removed. The microbubbles are supplied into the sludge by circulating the separated water in the sludge thickening tank through a pressurized tank and supplying compressed air into the pressurized tank. The compressed air is dissolved in circulating water, and when the pressurized circulating water is returned to the sludge thickening tank, the pressure is reduced and the dissolved compressed air is supplied as fine bubbles, making it difficult to treat highly concentrated sludge. This method has the disadvantage that the amount of compressed air dissolved in the clear water must be increased by increasing the pressure in the pressurized tank or by increasing the amount of separated water circulated.

本発明にかジノ上る不都合を解消し、高圧の加圧タンク
の使用や分離水の大量循環を必要とすることなく高濃度
の汚泥を効率よく処理できる汚泥処理方法を提供するこ
とをその目的とするもので、汚泥槽から汚泥濃縮槽へ汚
泥供給管を介して被処理汚泥を連続的に供給すると共に
該供給管に圧縮空気を混入させてこれを直ちに超音波で
破壊して微細気泡に生成せしめ、該供給管中で該被処理
汚泥中の固形分に付着させ、その後膣濃縮槽へ導いて浮
上分離することから成る。
It is an object of the present invention to provide a sludge treatment method capable of efficiently treating highly concentrated sludge without using a high-pressure pressurized tank or circulating a large amount of separated water. The sludge to be treated is continuously supplied from the sludge tank to the sludge thickening tank via the sludge supply pipe, and compressed air is mixed into the supply pipe, which is immediately destroyed by ultrasonic waves and generated into fine bubbles. The solid content in the sludge to be treated is deposited in the supply pipe, and then introduced into a vaginal thickening tank for flotation separation.

以上添付図面に従って本発明の実施例に付き説明する。Embodiments of the present invention will be described above with reference to the accompanying drawings.

第1図は本発明汚泥処理方法を実施するための汚泥処理
@置の一例を示すもので、図中1は汚泥濃縮槽を示し、
汚泥槽2から供給ポンプ3を備えた汚泥供給管4を介し
て被処理汚泥5を連続的に供給される鳴のとした。
FIG. 1 shows an example of a sludge treatment facility for carrying out the sludge treatment method of the present invention. In the figure, 1 indicates a sludge thickening tank;
Sludge 5 to be treated was continuously supplied from a sludge tank 2 through a sludge supply pipe 4 equipped with a supply pump 3.

また該汚泥供給管4のポンプ3の下流側にはノズル6を
介装してその下流近傍を負圧に保ち、かかる汚泥供給管
4の負圧領域に発振器7に連なる振動子8を備えると共
に圧縮空気供給管9を介してニアコンプレッサ10から
圧縮空気を供給するものとした。尚、図中11は濃縮汚
泥排出口、12は分離水排出口を示す。
Further, a nozzle 6 is interposed on the downstream side of the pump 3 of the sludge supply pipe 4 to maintain a negative pressure in the vicinity of the downstream thereof, and a vibrator 8 connected to an oscillator 7 is provided in the negative pressure region of the sludge supply pipe 4. Compressed air was supplied from a near compressor 10 via a compressed air supply pipe 9. In the figure, 11 indicates a concentrated sludge outlet, and 12 indicates a separated water outlet.

ここで当該処理装置による汚泥処理方法の一例を示すと
、まず汚泥槽2から被処理汚泥5なノズル6に導くと共
に該ノズル6の下流に生じる負圧を利用してコンプレッ
サ10から供給される圧縮空気を該ノズル6の下流側へ
と導き、ここで被処理汚泥5に圧縮空気を混入させると
同時に該圧縮空気な発振器7の設定信号に応じて振動子
8によって発生する所望振動数の超音波で例えば40〜
80μmの極めて微細な気泡に破壊形成し、該被処理汚
泥5中に均一に分散させてこれな該被処理汚泥5中の固
形分に十分付着させ、次でかかる被処理汚泥5を大気開
放の汚泥濃縮槽1へと導いて微細気泡を付着された固形
分を該濃縮槽1の上方へと浮上きせる。これを連続的に
行なって該濃縮槽1の上方に集められた固形分な濃縮汚
泥排出口11から順次排出すると共に分離水を分離水排
出口12から順次排出する。
Here, an example of the sludge treatment method using the treatment device is shown. First, the sludge to be treated 5 is introduced from the sludge tank 2 to the nozzle 6, and the compressed sludge is supplied from the compressor 10 using the negative pressure generated downstream of the nozzle 6. The air is guided to the downstream side of the nozzle 6, where compressed air is mixed into the sludge to be treated 5, and at the same time an ultrasonic wave of a desired frequency is generated by the vibrator 8 according to the setting signal of the compressed air oscillator 7. For example, 40~
They are broken into extremely fine bubbles of 80 μm, dispersed uniformly in the sludge 5 to be treated, and sufficiently adhered to the solid content in the sludge 5 to be treated, and then the sludge 5 to be treated is exposed to the atmosphere. The sludge is guided to the sludge thickening tank 1 and the solids with fine bubbles attached thereto are floated above the sludge thickening tank 1. This is done continuously, and the solid concentrated sludge collected above the thickening tank 1 is sequentially discharged from the discharge port 11, and the separated water is sequentially discharged from the separated water discharge port 12.

このように本発明によるときに、汚泥供給管に圧縮空気
を混入させてこれを直ちに超音波で破壊して微細気泡に
生成せしめ、該供給管中で被処理汚泥中の固形分に付着
させるようにしたために、高圧の加圧タンクの使用や分
離水の大量循環を要することなく極めて微細な気泡を該
固形分に良好に付着し得、高濃度の汚泥を効率よく処理
できると共に超音波の振動数を制御するだけで被処理物
の汚泥濃度に合わせた粒径の微細気泡を供給し得、被処
理物に応じた最適の汚泥処理を行なえる効果を有する。
As described above, according to the present invention, compressed air is mixed into the sludge supply pipe, and the air is immediately destroyed by ultrasonic waves to generate fine bubbles, which are then attached to the solids in the sludge to be treated in the supply pipe. As a result, extremely fine air bubbles can be adhered to the solid content without using a high-pressure tank or circulating a large amount of separated water, making it possible to efficiently treat highly concentrated sludge and using ultrasonic vibrations. By simply controlling the number of microbubbles, it is possible to supply microbubbles with a particle size that matches the sludge concentration of the object to be treated, which has the effect of allowing optimal sludge treatment depending on the object to be treated.

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

第1図は本発明汚泥処理方法を実施するための汚泥処理
@置の一実施例の系統図、第2図はその硬面の截断面図
である。 1・・・汚泥濃縮槽 2・・・汚泥槽 4・・・汚泥供給管 5・・・被処理汚泥7・・・発振
器 8・・・振動子 10・・・ニアコンプレッサ 外2名 第1図 第2図
FIG. 1 is a system diagram of an embodiment of a sludge treatment facility for carrying out the sludge treatment method of the present invention, and FIG. 2 is a cutaway sectional view of its hard surface. 1... Sludge thickening tank 2... Sludge tank 4... Sludge supply pipe 5... Sludge to be treated 7... Oscillator 8... Vibrator 10... 2 people outside the near compressor Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 汚泥槽から汚泥濃縮槽へ汚泥供給管を介して被処理汚泥
を連続的に供給すると共に該供給管に圧縮空気を混入さ
せてこれを直ちに超音波で破壊して微細気泡に生成せし
め、該供給管中で該被処理汚泥中の固形分に付着させ、
その後濃縮槽へ導いて浮上分離することから成る汚泥処
理方法。
The sludge to be treated is continuously supplied from the sludge tank to the sludge thickening tank via a sludge supply pipe, and compressed air is mixed into the supply pipe, which is immediately destroyed by ultrasonic waves to generate fine bubbles, and then the sludge is supplied. attached to the solid content in the sludge to be treated in the pipe,
A sludge treatment method that consists of leading the sludge to a thickening tank and flotation separation.
JP59093046A 1984-05-11 1984-05-11 Treatment of sludge Pending JPS60238200A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59093046A JPS60238200A (en) 1984-05-11 1984-05-11 Treatment of sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59093046A JPS60238200A (en) 1984-05-11 1984-05-11 Treatment of sludge

Publications (1)

Publication Number Publication Date
JPS60238200A true JPS60238200A (en) 1985-11-27

Family

ID=14071562

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59093046A Pending JPS60238200A (en) 1984-05-11 1984-05-11 Treatment of sludge

Country Status (1)

Country Link
JP (1) JPS60238200A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004524963A (en) * 2001-03-16 2004-08-19 ソニコ・リミテッド Fluid treatment equipment using ultrasonic waves
KR100477156B1 (en) * 2002-01-30 2005-03-17 사가노노보루 Disposing method and disposing device of organic sludge
JP2006289183A (en) * 2005-04-06 2006-10-26 Nano Bubble Kk Nano-bubble forming method and apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004524963A (en) * 2001-03-16 2004-08-19 ソニコ・リミテッド Fluid treatment equipment using ultrasonic waves
KR100477156B1 (en) * 2002-01-30 2005-03-17 사가노노보루 Disposing method and disposing device of organic sludge
JP2006289183A (en) * 2005-04-06 2006-10-26 Nano Bubble Kk Nano-bubble forming method and apparatus

Similar Documents

Publication Publication Date Title
TWI444232B (en) Floatation device and method and method of making products resulted therefrom
EP1403221A2 (en) Water purifier
KR20030024631A (en) Process and device for aerating a liquid with gas
JPH10226503A (en) Air-ozone mixer and ozone fog generator
GB1423210A (en) Wewage tretment apparatus and method
DE3887711D1 (en) Device and method for treating water saturated with oxygen under high pressure.
CA2312735A1 (en) Water treatment apparatus and water treatment method
US6036584A (en) Blast system
US3809240A (en) Method of injecting fluids into a flotation tank
JPS60238200A (en) Treatment of sludge
JP2006055737A (en) Sludge treatment method and sludge treatment apparatus
CA1055168A (en) Method and apparatus for microflotation by means of pressure liquid
CN116851408A (en) Gas slag treatment device and method
NO971699D0 (en) Flotation method and mixing device for carrying it out
CA1036718A (en) Separation method and device
JP4264089B2 (en) Ultra miniaturization equipment
GB2090240A (en) The treatment of liquid suspensions
JPH02245286A (en) Floatation equipment for suspended matter in water
JPS61201093A (en) Deinking apparatus
JP2606716Y2 (en) Mixing equipment for mud and solidified material
JPS598436B2 (en) Flotation separation method for solids contained in sewage sludge, etc.
RU2038856C1 (en) Method of flotation of mineral resources
RU1787945C (en) Open-flow microflotation method and device
JP4205876B2 (en) Sludge treatment method and ejector
JPS6427692A (en) Apparatus for disposal of garbage