JPS60238200A - Treatment of sludge - Google Patents
Treatment of sludgeInfo
- 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
Links
Landscapes
- Physical Water Treatments (AREA)
- Treatment Of Sludge (AREA)
Abstract
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.
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)
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.
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)
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 |
-
1984
- 1984-05-11 JP JP59093046A patent/JPS60238200A/en active Pending
Cited By (3)
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 |
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