JPS5951880B2 - Micro bubble generator in flotation separation equipment - Google Patents

Micro bubble generator in flotation separation equipment

Info

Publication number
JPS5951880B2
JPS5951880B2 JP55063409A JP6340980A JPS5951880B2 JP S5951880 B2 JPS5951880 B2 JP S5951880B2 JP 55063409 A JP55063409 A JP 55063409A JP 6340980 A JP6340980 A JP 6340980A JP S5951880 B2 JPS5951880 B2 JP S5951880B2
Authority
JP
Japan
Prior art keywords
water
propeller
pipe
flotation
box
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
Application number
JP55063409A
Other languages
Japanese (ja)
Other versions
JPS56161884A (en
Inventor
宜二 井村
勝信 三宅
行夫 森瀬
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.)
Kurimoto Iron Works Ltd
Original Assignee
Kurimoto Iron Works 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 Kurimoto Iron Works Ltd filed Critical Kurimoto Iron Works Ltd
Priority to JP55063409A priority Critical patent/JPS5951880B2/en
Publication of JPS56161884A publication Critical patent/JPS56161884A/en
Publication of JPS5951880B2 publication Critical patent/JPS5951880B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/50Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Water Treatments (AREA)

Description

【発明の詳細な説明】 この発明は汚水辱中の微粒子を浮上分離する装置におけ
る微細気泡発生装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a microbubble generating device used in a device for flotation separation of fine particles in sewage water.

従来より懸濁微粒子を含む汚水あるいは凝集剤を添加し
て懸濁微粒子を凝集(フロック)させた汚水中に該微粒
子の分離を行うため空気(No、O2ガスでも良い)を
水に加圧溶解させた空気加圧溶解液を、汚水を容れた分
離水槽に導き、上記。
Conventionally, air (No, O2 gas may be used) is dissolved in water to separate the particles in wastewater that contains suspended particles or in wastewater that has been flocculated by adding a coagulant. The air-pressurized dissolved solution was introduced into a separation tank containing waste water, and the above-mentioned procedure was carried out.

溶解液の減圧によつて発生する微細気泡を汚水中の微粒
子に付着させて浮上分離させる加圧浮上分離装置は種々
提案されているが、従来のこの種の空気加圧溶解装置は
、コンプレッサー、高圧ポンプ、加圧混合タンクを必要
とするため、装置が複雑且つ大型化すると共に多大な動
力を必要とするものであつた。この発明は上記した各種
機器を使用することなしに極めて微細化された気泡を発
生させるようにした微細気泡発生装置を提供しようとす
るものである。
Various pressurized flotation devices have been proposed in which microbubbles generated by reducing the pressure of the solution are attached to fine particles in wastewater for flotation separation, but conventional air pressurized dissolution devices of this type are Since a high-pressure pump and a pressurized mixing tank are required, the device becomes complicated and large, and requires a large amount of power. The present invention aims to provide a micro-bubble generator capable of generating extremely micro-bubble without using any of the above-mentioned devices.

′ この発明の具体的実施例が添付図面を参照にしなが
ら以下に説明される。
' Specific embodiments of the invention will be described below with reference to the accompanying drawings.

図面中の符号1は浮上箱で上端をスカムの上面SLより
突出した状態で分離水槽6内に保持されている。
Reference numeral 1 in the drawings denotes a flotation box, which is held in the separation water tank 6 with its upper end protruding from the upper surface SL of the scum.

2は混合箱で浮上箱1内に開口端4を位置し、他端は気
泡水管5’となつて分離水槽外に設けた右目16に外筒
18を介して連通している。
Reference numeral 2 denotes a mixing box with an open end 4 located inside the flotation box 1, and the other end serving as a bubble water pipe 5' communicating with a right eye 16 provided outside the separation water tank via an outer tube 18.

またこの混合箱2の開口端4に近接した位置に開口部を
維持するように汚水送入管3が設けられている。また前
記浮上箱1の上端には架台19上に設けた駆動源20を
介して回転するスクレパー7が設けられている。更にこ
の浮上箱1の小区画側壁にスカムレベルSL面に開口端
面を位置するようにしたスカムボツクス8が設けられ、
このスカムボツクス8には分離水槽外に延出する排出管
8’が連接されている。分離水槽6には、上端縁をV型
に切欠した溢流堰21と、この溢流堰21を囲むように
集水管10に連通する集水箱9が設けられており、しか
も下端にはドレーンコック11が設置されている。
Further, a waste water inlet pipe 3 is provided so as to maintain the opening at a position close to the open end 4 of the mixing box 2. Further, at the upper end of the floating box 1, a scraper 7 is provided which rotates via a drive source 20 provided on a pedestal 19. Furthermore, a scum box 8 is provided on the side wall of the subdivision of this flotation box 1, and the opening end surface is located on the scum level SL surface.
A discharge pipe 8' extending outside the separation tank is connected to the scum box 8. The separation water tank 6 is provided with an overflow weir 21 having a V-shaped notch at its upper edge, and a water collection box 9 that surrounds this overflow weir 21 and communicates with the water collection pipe 10, and a drain cock at the lower end. 11 are installed.

右目16は円錐形に形成され導管6’を介して分離水槽
6の清澄水部と連通しており、しかもこの右目16中に
は後述する気泡発生装置の構成部材の1つである空気導
入管13が設けられている。5は気泡発生装置で、前記
右目16と上述の気泡水管5’との中間に連接する外筒
18内に設けられており、この気泡発生装置5はプロペ
ラ型(羽根車型)軸流ポンプ12を内蔵する案内筒12
’と、この案内筒12′と外筒18間に設けた複数枚の
整流板15と、プロペラ14および前記した空気導入管
13の開口端13′を前記プロペラの吸込側の近傍に位
置させるようにして構成されている。
The right eye 16 is formed into a conical shape and communicates with the clear water part of the separation water tank 6 via a conduit 6', and inside this right eye 16 is an air introduction pipe which is one of the components of the bubble generator described later. 13 are provided. Reference numeral 5 denotes a bubble generator, which is provided in an outer cylinder 18 that is connected between the right eye 16 and the bubble water pipe 5'. Built-in guide tube 12
', the plurality of baffle plates 15 provided between the guide cylinder 12' and the outer cylinder 18, the propeller 14, and the open end 13' of the air introduction pipe 13 are positioned near the suction side of the propeller. It consists of:

符号22は空気導入管13に設けた抵抗装置(空気の流
人調整装置)で2個の調整弁22’および22”で構成
されている。なお、上述の整流板15は案内筒12′と
外筒18間のみに限定されず、数段、直列状に設置でき
るものであり、また空気導入管13の開口端の形状は図
示実施例の傘形に限定されることなく例えば放射状のノ
ズル形式等の他の形式のものを任意に選択できるもので
ある。
Reference numeral 22 denotes a resistance device (air flow regulating device) provided in the air introduction pipe 13, and is composed of two regulating valves 22' and 22''. The shape of the open end of the air introduction pipe 13 is not limited to the umbrella shape of the illustrated embodiment, but may be a radial nozzle shape, for example. You can arbitrarily select other formats such as .

この発明は前記構成により以下の作用を生ずるものであ
る。
The present invention has the following effects due to the above configuration.

プロペラ型軸流ポンプ12を作動すると水槽6内の清澄
水が導管6’より呑口16に流れ込むと共に、空気導入
管13より空気が吸入され、プロペラの回転力及び整流
板15の先端部で強烈に混合、剪断され微細化された気
泡水が作られ、この気泡水は気泡水管5’を通じて混合
箱2の下方より送入される。一方汚水は汚水送入管3よ
り混合箱2に図示しない送入装置によつて送り込まれる
When the propeller-type axial flow pump 12 is activated, the clear water in the water tank 6 flows into the spout 16 from the conduit 6', and air is sucked in from the air introduction pipe 13, and the propeller's rotational force and the tip of the baffle plate 15 cause the water to flow into the spout 16. Mixed and sheared to produce fine bubble water, this bubble water is fed from below the mixing box 2 through the bubble water pipe 5'. On the other hand, sewage is sent from the sewage inlet pipe 3 to the mixing box 2 by a feeding device (not shown).

この結果混合箱2内の汚水中の気泡に吸着する物質は、
気泡とともに浮上箱1の内部で水面上に浮き上りスカム
Sとなつて停滞する。 (浮上分離構造)このスカムS
はスクレパー7の回転によりスカムボツクス8に送り込
まれた排出管8’を経て水槽6外に取り出される。微粒
子を除去された清澄水は浮上箱1の下部開口17をくぐ
り抜けて水槽6と浮上箱1の間を通り、一部は循環水と
して導管6’を通じて呑口16に流入する。また、流入
汚水量に相当する清澄水(処理水)は溢流堰21を越え
て集水箱9を介して集水管10に集められ次工程に送ら
れる。なお前記実施例では水槽6内の清澄水を呑口16
に導管6を介して連通せしめたが、これに限定するもの
ではなく、該管を省略し、別源からの清澄水を供給管3
0を介して、呑口16に供給してもよく、さらにまた導
管6汚水管3を省略し、汚水を直接、供給管30を介し
て、呑口16に供給してもよいことは言う迄もない。
As a result, the substances adsorbed to the air bubbles in the wastewater in the mixing box 2 are:
The scum rises to the surface of the water inside the flotation box 1 along with air bubbles and becomes scum S, where it stagnates. (Floating separation structure) This scum S
is taken out of the water tank 6 through the discharge pipe 8' fed into the scum box 8 by the rotation of the scraper 7. The clear water from which fine particles have been removed passes through the lower opening 17 of the flotation box 1, passes between the water tank 6 and the flotation box 1, and a portion flows into the spout 16 through the conduit 6' as circulating water. Further, clear water (treated water) corresponding to the amount of inflowing sewage passes over the overflow weir 21, is collected in the water collection pipe 10 via the water collection box 9, and is sent to the next process. In the above embodiment, the clear water in the water tank 6 is poured into the spout 16.
However, the present invention is not limited to this, and this pipe is omitted, and clear water from another source is connected to the supply pipe 3.
Needless to say, the waste water may be supplied to the spout 16 through the supply pipe 30, or the conduit 6 and the waste water pipe 3 may be omitted and the waste water may be directly supplied to the spout 16 via the supply pipe 30. .

しかも前記の浮上分離構造はこれに限定されるものでな
く、他の異なる形式の浮上分離機構にも容易に適用でき
ることは勿論である。
Moreover, the above-mentioned flotation separation structure is not limited to this, and it goes without saying that it can be easily applied to other different types of flotation and separation mechanisms.

また、汚水の濃度が濃い汚泥の場合はSS(懸濁固形物
)に着目してSSを濃縮する汚泥濃縮装置にも適用する
ことができる。この発明は前記構成により以下の効果を
生ずるものである。
In addition, in the case of sludge with a high concentration of sewage, it can be applied to a sludge concentrator that focuses on SS (suspended solids) and concentrates the SS. The present invention has the following effects due to the above configuration.

(1)気泡を多量に含むことができ且つ極めて微細化す
ることができ、これにより汚水中の微粒子除去、分離を
効率的に行なうことができる。
(1) It can contain a large amount of air bubbles and can be made extremely fine, thereby making it possible to efficiently remove and separate fine particles from wastewater.

(2)従来の加圧水発生装置に比して動力が数十分の一
となり運転費を著しく低減することができる。(3)構
造が簡単でコンパクトとなり設備費が格安となる。
(2) The power required is several tenths of that of conventional pressurized water generators, and operating costs can be significantly reduced. (3) The structure is simple and compact, and equipment costs are low.

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

第1図はこの発明の微細気泡発生装置の要部を示す断面
説明図。 1 ・・・・・・浮上箱、2 ・・・・・・混合箱、3
・・・・・・汚水送水管、4 ・・・・・・開口端部
、5’ ・・・・・・気泡管、5 ・・・・・・気泡発
生装置、6 ・・・・・・分離水槽、6’ ・・・・・
・導管、12・・・・・・プロペラ型軸流ポンプ、13
・・・・・・空気導入管、14・・・・・・プロペラ、
15・・・・・・整流板、18・・・・・・外筒。
FIG. 1 is an explanatory cross-sectional view showing the main parts of the microbubble generator of the present invention. 1 ... Levitation box, 2 ...Mixing box, 3
...Sewage water pipe, 4 ...Open end, 5' ...Bubble pipe, 5 ...Bubble generator, 6 ...... Separation tank, 6'...
・Conduit, 12... Propeller type axial flow pump, 13
... Air introduction pipe, 14 ... Propeller,
15... Rectifier plate, 18... Outer cylinder.

Claims (1)

【特許請求の範囲】[Claims] 1 清澄水または汚水が供給される呑口と、この呑口と
外筒および気泡水管を介して、水槽内に設けた浮上箱内
に開口を位置させた混合箱とを連通し、前記外筒内にプ
ロペラ型軸流ポンプを設け、このプロペラ型軸流ポンプ
のプロペラの負圧部側に空気導入管の出口を位置させ、
プロペラの吸込側に整流板を設けたことを特徴とする浮
上分離装置における微細気泡発生装置。
1. A drinking spout to which clear water or sewage is supplied is communicated with a mixing box whose opening is located in a flotation box provided in a water tank through an outer cylinder and a bubble water pipe, and A propeller type axial flow pump is provided, the outlet of the air introduction pipe is located on the negative pressure side of the propeller of the propeller type axial flow pump,
A micro bubble generator in a flotation separation device, characterized in that a current plate is provided on the suction side of a propeller.
JP55063409A 1980-05-15 1980-05-15 Micro bubble generator in flotation separation equipment Expired JPS5951880B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55063409A JPS5951880B2 (en) 1980-05-15 1980-05-15 Micro bubble generator in flotation separation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55063409A JPS5951880B2 (en) 1980-05-15 1980-05-15 Micro bubble generator in flotation separation equipment

Publications (2)

Publication Number Publication Date
JPS56161884A JPS56161884A (en) 1981-12-12
JPS5951880B2 true JPS5951880B2 (en) 1984-12-17

Family

ID=13228464

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55063409A Expired JPS5951880B2 (en) 1980-05-15 1980-05-15 Micro bubble generator in flotation separation equipment

Country Status (1)

Country Link
JP (1) JPS5951880B2 (en)

Also Published As

Publication number Publication date
JPS56161884A (en) 1981-12-12

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