JPS595033B2 - flotation separation device - Google Patents
flotation separation deviceInfo
- Publication number
- JPS595033B2 JPS595033B2 JP55029601A JP2960180A JPS595033B2 JP S595033 B2 JPS595033 B2 JP S595033B2 JP 55029601 A JP55029601 A JP 55029601A JP 2960180 A JP2960180 A JP 2960180A JP S595033 B2 JPS595033 B2 JP S595033B2
- Authority
- JP
- Japan
- Prior art keywords
- flotation separation
- treated
- sludge
- water
- screw
- 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.)
- Expired
Links
Landscapes
- Physical Water Treatments (AREA)
Description
【発明の詳細な説明】
本発明は、被処理水中の汚泥を気泡により凝集させて浮
上分離させる装置に関し、可及的に設備費高騰を抑制し
た状態で、浮上分離を効率良く行えるように改造する事
を目的とする。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device that aggregates sludge in water to be treated using air bubbles and floats it to separate it, and has been modified so that it can efficiently float and separate it while suppressing the rise in equipment costs as much as possible. The purpose is to do.
次に、例示図により本発明の実施態様を説明する。Next, embodiments of the present invention will be described with reference to illustrative figures.
水処理設備1から供給される汚泥含有被処理水と、凝集
剤供給装置2からの凝集剤を、攪拌装置3によって混合
して、汚泥を薬液により凝集すべく構成した凝集混和槽
4を設け、凝集混和槽4からオーバフローしてくる被処
理水を下降流動させると共にノズル5からの空気により
曝気処理すべく構成した曝気槽6を設け、曝気槽6から
の被処理水を泥槽部分7aで上昇流動させながら、汚泥
を気泡によって凝集させて浮上分離させるべく構成した
浮上分離槽7を設けである。The sludge-containing treated water supplied from the water treatment equipment 1 and the flocculant from the flocculant supply device 2 are mixed by a stirring device 3, and a flocculation mixing tank 4 is provided to flocculate the sludge with a chemical solution, An aeration tank 6 configured to cause the water to be treated that overflows from the coagulation mixing tank 4 to flow downward and to be aerated with air from the nozzle 5 is provided, and the water to be treated from the aeration tank 6 is raised in the mud tank portion 7a. A flotation separation tank 7 is provided which is configured to aggregate the sludge with air bubbles and float and separate it while flowing.
前記曝気槽6の深い位置に、凝集助剤を供給するパイプ
8を設けて、汚泥凝集を助長すべく構成すると共に、前
記泥槽部分7aの底部近くに、螺旋状上昇流路を形成す
るためのスクリュー9を内装して、上昇流路延長により
、汚泥と気泡との接触確率の増大、及び、曝気槽から流
入する気泡の溶解促進を図ると共に、気泡のスクリュー
9との接触により細分化を図り、全体として効率良く浮
上分離が行われるべく構成しである。A pipe 8 for supplying a flocculation aid is provided deep in the aeration tank 6 to promote sludge flocculation, and a spiral upward flow path is formed near the bottom of the mud tank portion 7a. By installing a screw 9 inside the sludge and extending the ascending flow path, the probability of contact between the sludge and air bubbles is increased, and the dissolution of air bubbles flowing from the aeration tank is promoted. The structure is designed so that flotation and separation can be carried out efficiently as a whole.
前記浮上分離槽7の上部に、浮上汚泥を汚泥トラフ10
に送り込む掻寄せ装置11、及び、清水を取出す処理水
トラフ12を設けである。The floated sludge is transferred to the upper part of the flotation separation tank 7 in a sludge trough 10.
A raking device 11 for feeding fresh water into the tank, and a treated water trough 12 for taking out fresh water are provided.
尚、前記浮上分離槽7の最深け、10m程度が一般的で
あるが、必要に応じて適宜変更自在であり、また、前記
泥槽部分7aに被処理水を供給する手段も各種変更自在
であり、そのための構成を被処理水供給流路6と総称す
る。The maximum depth of the flotation separation tank 7 is generally about 10 m, but it can be changed as necessary, and the means for supplying the water to be treated to the mud tank section 7a can also be changed in various ways. There is a configuration for this purpose, which is collectively referred to as a treated water supply channel 6.
また、前記スクリュー9を、前述のように底部近くに配
置したり、あるいは、前記泥槽部分7aの全長あるいは
ほぼ全長にわたって配置すると、気泡溶解を促進できて
有利であるが、泥槽部分7aの上部あるいは上部寄りに
スクリュー9を配置してもよく、そして、スクリュー9
の長さ、形状、ピッチ等は、必要に応じて適宜変更自在
である。Further, it is advantageous to dispose the screw 9 near the bottom as described above, or over the entire length or almost the entire length of the mud tank portion 7a, as this can promote bubble dissolution. The screw 9 may be placed at the top or near the top;
The length, shape, pitch, etc. can be changed as necessary.
以上型するに、本発明は、冒記浮上分離装置において、
浮上分離槽7の少なくとも一部?aを比較的深く構成し
、その泥槽部分7aに対し、その底部近くに被処理水供
給流路6を接続すると共に、螺旋状上昇流路を形成する
ためのスクリュー9を内装しである事を特徴とする特
すなわち、探検部分7aの底部近くに供給される被処理
水に溶解させたガスを、被処理水上昇に伴って気泡化で
きるから、極めて微細な気泡が均等にかつ大量に被処理
水中に存在する状況を現出できて、汚泥と気泡との接触
効率が高くなり、その上、スクリュー9の作用によって
、気泡の細分化、及び、汚泥と気泡の接触のための時間
の延長を図れ、その事によっても汚泥と気泡との接触効
率が高くなり、全体として汚泥の浮上分離効率を顕著に
向′上できた。In summary, the present invention provides the flotation separation device described above.
At least part of flotation tank 7? a is relatively deep, and a water supply flow path 6 to be treated is connected to the mud tank portion 7a near the bottom thereof, and a screw 9 for forming a spiral ascending flow path is installed inside. Specifically, the gas dissolved in the water to be treated, which is supplied near the bottom of the exploration portion 7a, can be turned into bubbles as the water to be treated rises, so extremely fine bubbles can be uniformly and in large quantities. The situation existing in the treated water can be expressed, and the contact efficiency between sludge and air bubbles can be increased. Furthermore, the action of the screw 9 can fragment the air bubbles and extend the time for contact between sludge and air bubbles. This also increased the contact efficiency between the sludge and air bubbles, and significantly improved the sludge flotation separation efficiency as a whole.
そして、上述のごとく浮上分離効率を向上する手段とし
て、例えば、探検部分7aを単純な直管状にして極めて
深くするもの、あるいは、探検部分7aそのものをジグ
ザグ状にするものが考えられるが、前者は、地上高や地
中埋設深さが極めて犬になって、多大な設備費を要し、
また、後者は、探検部分Ia自体のコストが大巾に増大
すると共に、地中埋設タイプにすると掘削孔径が大きく
なって掘削工事に大きな経費を必要とする等、いずれも
設備費の大巾増大を伴う欠点がある。As mentioned above, as a means to improve flotation separation efficiency, for example, the exploration section 7a can be made into a simple straight pipe shape and made extremely deep, or the exploration section 7a itself can be made into a zigzag shape. , the height above ground and the depth of underground burial are extremely high, requiring a large amount of equipment cost,
In addition, the latter greatly increases the cost of the exploration part Ia itself, and if the underground type is used, the diameter of the borehole becomes large and the excavation work requires a large expense, both of which greatly increase the equipment cost. There are disadvantages associated with this.
他方、本発明によれば、単にスクリュー9を内装して探
検部分7aをできる限り短くするのであるから、設備費
高騰を効果的に抑制できる。On the other hand, according to the present invention, the exploration portion 7a is made as short as possible by simply incorporating the screw 9, so that it is possible to effectively suppress the increase in equipment costs.
図面は本発明に係る浮上分離装置の実施の態様を例示し
、第1図は概略縦断面図、第2図は第1図の■−■縦断
面図である。
6・・・・・・被処理水供給流路、7・・・・・・浮上
分離槽、7a・・・・・・探検部分、9・・・・・・ス
クリュー。The drawings illustrate an embodiment of the flotation and separation apparatus according to the present invention, and FIG. 1 is a schematic longitudinal sectional view, and FIG. 2 is a longitudinal sectional view taken along the line 1--2 of FIG. 1. 6...Water supply channel to be treated, 7...Flotation separation tank, 7a...Exploration section, 9...Screw.
Claims (1)
させる装置であって、浮上分離槽7の少なくとも一部7
aを比較的深く構成し、その泥槽部分7aに対し、その
底部近くに被処理水供給流路6を接続すると共に、螺旋
状上昇流路を形成するためのスクリュー9を内装しであ
る事を特徴とする浮上分離装置。 2 前記スクリュー9の下端を前記泥槽部分7aの底部
近くに配置しである事を特徴とする特許請求の範囲第1
項に記載の装置。[Scope of Claims] 1. A device for flotation separation by agglomerating sludge in water to be treated using air bubbles, which comprises at least a portion 7 of a flotation separation tank 7.
a is relatively deep, and a water supply flow path 6 to be treated is connected to the mud tank portion 7a near the bottom thereof, and a screw 9 for forming a spiral ascending flow path is installed inside. A flotation separation device featuring: 2. Claim 1, characterized in that the lower end of the screw 9 is disposed near the bottom of the mud tank portion 7a.
The equipment described in section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55029601A JPS595033B2 (en) | 1980-03-07 | 1980-03-07 | flotation separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55029601A JPS595033B2 (en) | 1980-03-07 | 1980-03-07 | flotation separation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56126478A JPS56126478A (en) | 1981-10-03 |
| JPS595033B2 true JPS595033B2 (en) | 1984-02-02 |
Family
ID=12280584
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55029601A Expired JPS595033B2 (en) | 1980-03-07 | 1980-03-07 | flotation separation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS595033B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6064100U (en) * | 1983-10-06 | 1985-05-07 | 日立造船株式会社 | Continuous alcohol fermentation tank |
| JPS6447489A (en) * | 1987-08-17 | 1989-02-21 | Toshin Technical Kk | Liquid activating device |
| JPH0676728U (en) * | 1994-02-18 | 1994-10-28 | タツタ電線株式会社 | Disc spring |
-
1980
- 1980-03-07 JP JP55029601A patent/JPS595033B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56126478A (en) | 1981-10-03 |
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