JPH0233915Y2 - - Google Patents

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Publication number
JPH0233915Y2
JPH0233915Y2 JP5746585U JP5746585U JPH0233915Y2 JP H0233915 Y2 JPH0233915 Y2 JP H0233915Y2 JP 5746585 U JP5746585 U JP 5746585U JP 5746585 U JP5746585 U JP 5746585U JP H0233915 Y2 JPH0233915 Y2 JP H0233915Y2
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JP
Japan
Prior art keywords
separated water
cylindrical body
water
take
separated
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
JP5746585U
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Japanese (ja)
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JPS61175291U (en
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 filed Critical
Priority to JP5746585U priority Critical patent/JPH0233915Y2/ja
Publication of JPS61175291U publication Critical patent/JPS61175291U/ja
Application granted granted Critical
Publication of JPH0233915Y2 publication Critical patent/JPH0233915Y2/ja
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 <産業上の利用分野> 本考案は比較的浮上しやすい懸濁物質を含む原
水から懸濁物質を浮上させて除去する浮上分離槽
に関するものである。
[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a flotation separation tank that floats and removes suspended solids from raw water containing suspended solids that are relatively easy to float.

<従来技術> 従来から比較的浮上しやすい懸濁物質、たとえ
ば魚肉蛋白質あるいは油等を含む廃水から当該懸
濁物質を除去する場合、浮上分離槽が用いられて
いる。
<Prior Art> A flotation separation tank has conventionally been used to remove suspended solids that relatively easily float, such as fish protein or oil, from wastewater.

従来から用いられている浮上分離槽は第3図に
示したようなもので、浮上槽1内に内筒2を設け
るとともに、当該内筒2の外側に外筒3を設けた
もので、懸濁物質を含む原水を内筒2の下方内部
に開口させた原水流入管4から流入するととも
に、原水流入管4に連通した加圧水管5から気体
たとえば空気を加圧下で溶解させた加圧水を流入
し、当該加圧水から発生する気泡と懸濁物質とを
合体せしめ、浮上懸濁物質を点線の矢印線で示し
たごとく浮上槽1の上方に浮上させ、また浮上懸
濁物質を除いた分離水を実線の矢印線で示したご
とく外筒3の下端を通して浮上槽1の内周縁部を
上昇させ、浮上槽1の外周部に設けた集水樋6を
介して分離水管7より流出させるものである。ま
た浮上槽1の水面に浮上した浮上懸濁物質8をモ
ータなど(図示せず)で回転させる掻取機9によ
り浮上槽1の水面の一部に設けた導入溝10内に
掻取り、これを外部へ排出するものである。
A conventional flotation separation tank is shown in Fig. 3, in which an inner cylinder 2 is provided inside the flotation tank 1, and an outer cylinder 3 is provided outside the inner cylinder 2. Raw water containing turbid substances flows in from a raw water inflow pipe 4 opened at the lower inside of the inner cylinder 2, and pressurized water in which a gas, such as air, is dissolved under pressure flows in from a pressurized water pipe 5 communicating with the raw water inflow pipe 4. , the air bubbles generated from the pressurized water and the suspended solids are combined, the floating suspended solids are floated above the flotation tank 1 as shown by the dotted arrow line, and the separated water from which the floating suspended solids have been removed is separated by the solid line. As shown by the arrow line, the inner circumferential edge of the flotation tank 1 is raised through the lower end of the outer cylinder 3, and the water flows out from the separation water pipe 7 through the water collection gutter 6 provided on the outer circumference of the flotation tank 1. In addition, the floating suspended solids 8 floating on the water surface of the flotation tank 1 are scraped into an introduction groove 10 provided in a part of the water surface of the flotation tank 1 by a scraper 9 rotated by a motor or the like (not shown). is discharged to the outside.

<解決しようとする問題点> しかしながら従来の浮上分離槽は以下のような
欠点がある。
<Problems to be Solved> However, conventional flotation tanks have the following drawbacks.

第1に内筒2内では発生した気泡と水による撹
拌乱流が生じているため、気泡に付着した懸濁物
質のフロツクが乱流により離反したり、あるいは
フロツクの成長を妨げたりして、かえつてフロツ
クを微細なものとし、効率的な浮上懸濁物質層の
形成を阻害する原因となり、第2に内筒2から上
昇する流体が水面付近で急激な流れの拡がりを生
ずるため、気泡が付着した懸濁物質が破壊され、
浮上分離効果を減退させている。
First, since the bubbles generated and water create stirring turbulence inside the inner cylinder 2, the flocs of suspended matter attached to the bubbles may be separated by the turbulence, or the growth of the flocs may be hindered. On the contrary, this causes the flocs to become finer, which inhibits the formation of an efficient floating suspended solids layer.Secondly, the fluid rising from the inner cylinder 2 causes a rapid flow expansion near the water surface, which causes air bubbles to form. Adhering suspended matter is destroyed,
This reduces the flotation separation effect.

本考案は従来のかかる欠点を除き、効率良く懸
濁物質を浮上分離できる浮上分離槽を提供するこ
とを目的とする。
An object of the present invention is to eliminate such drawbacks of the conventional technology and to provide a flotation tank that can efficiently float and separate suspended solids.

<問題点を解決する手段> 本考案は従来のように内筒内に直接原水を流入
せずに、バツフル板を介して内筒の下部から原水
を流入し、次いで内筒の周囲に原水を導いてここ
で懸濁物質を水面に浮上させ、分離水を内筒の上
端から導いて内筒の内部に設けた分離水取水機構
から取り出すように構成したものである。
<Means for solving the problem> The present invention does not directly flow raw water into the inner cylinder as in the conventional case, but instead flows the raw water from the lower part of the inner cylinder through a buttful plate, and then flows the raw water around the inner cylinder. The separated water is introduced from the upper end of the inner cylinder and taken out from the separated water intake mechanism provided inside the inner cylinder.

以下に本考案を図面を参照して詳細に説明す
る。
The present invention will be explained in detail below with reference to the drawings.

第1図は本考案の実施態様の一例を示す縦断面
説明図であり、浮上槽1内に、上方に向かつて末
広がりの両端が開口した筒状体11を内設し、当
該筒状体11の上端開口部に両端が開口する分離
水取出筒12を挿入することによつて、当該分離
水取出筒12の下端開口部を筒状体11内部に位
置させるとともに、当該分離水取出筒12の上端
を浮上槽1に形成される水面より上方に位置させ
たものである。また分離水取出筒12内に形成さ
れる分離水面に近接して分離水取出樋13を設
け、当該取出樋13に分離水取出筒14の一端を
連通する。なお場合によつては分離水取出樋13
を省略し、分離水面に近接して直接分離水取出管
14の開口部を設けても差し支えない。また筒状
体11の下端開口部の下方にバツフル板15を設
け、当該バツフル板15の下方に原水流入管4の
開口部を設け、さらに原水流入管4に加圧水管5
を連通する。また前記分離水取出筒12の上方周
縁部に浮上懸濁物質8の収集溝16を設け、当該
収集溝16に連通して第2図に示したごとく浮上
槽1の半径に相当する長さの導入溝10を水面に
近接して設け、また浮上懸濁物質8を導入溝10
に掻取るための掻取機9を設置する。なお前述し
たバツフル板15は上部に頂点を有する円錐状あ
るいは角錐状のものを用いることが好ましいが、
場合によつては単なる板状のものを用いても差し
支えない。図中17は収集溝16に連通した浮上
懸濁物質の排出管であり、18は沈澱物質のブロ
ー管である。
FIG. 1 is an explanatory longitudinal cross-sectional view showing an example of an embodiment of the present invention, in which a cylindrical body 11 facing upward and widening at both ends is provided inside a flotation tank 1. By inserting the separated water take-out cylinder 12 with both ends open into the upper end opening, the lower end opening of the separated water take-out cylinder 12 is located inside the cylindrical body 11, and the separated water take-out cylinder 12 is The upper end is located above the water surface formed in the flotation tank 1. Further, a separated water outlet gutter 13 is provided close to the separated water surface formed in the separated water outlet tube 12, and one end of the separated water outlet tube 14 is communicated with the outlet gutter 13. In some cases, separated water outlet gutter 13
may be omitted and the opening of the separated water outlet pipe 14 may be provided directly close to the separated water surface. Further, a baffle plate 15 is provided below the lower end opening of the cylindrical body 11, an opening of the raw water inflow pipe 4 is provided below the buffle plate 15, and a pressurized water pipe 5 is provided in the raw water inflow pipe 4.
communicate. In addition, a collection groove 16 for floating suspended solids 8 is provided at the upper peripheral edge of the separated water take-out tube 12, and the collection groove 16 is connected to the collection groove 16 and has a length corresponding to the radius of the flotation tank 1 as shown in FIG. The introduction groove 10 is provided close to the water surface, and the floating suspended solids 8 are placed in the introduction groove 10.
A scraper 9 is installed for scraping. It is preferable to use the buff-full plate 15 described above in the shape of a cone or pyramid having an apex at the top.
In some cases, a simple plate-like material may be used. In the figure, 17 is a discharge pipe for floating suspended solids that communicates with the collection groove 16, and 18 is a blow pipe for precipitated substances.

<作 用> 次に本考案の浮上分離槽の操作を説明する。<Effect> Next, the operation of the flotation tank of the present invention will be explained.

懸濁物質を含む原水と、気体としてたとえば空
気を溶解させた加圧水をそれぞれ原水流入管4お
よび加圧水管5から流入する。加圧水管5から流
入された加圧水はその加圧状態から開放されるも
ので、原水流入管4内または浮上槽1内で加圧水
内に溶解していた空気が微細な気泡となり、当該
気泡が懸濁物質に付着してより浮上しやすい懸濁
物質となり、当該浮上懸濁物質を含む水がバツフ
ル板15に衝突して筒状体11の周囲に導入され
る。図中の点線の矢印線で示したごとく浮上懸濁
物質8は浮上槽1の水面に浮上し、また実線の矢
印線で示したごとく分離水は筒状体11の上端を
介して筒状体11内に流入し、次いで分離水取出
筒12の下端から流入し、分離水取出樋13を介
して分離水取出管14から外部へ取り出される。
Raw water containing suspended matter and pressurized water in which a gas such as air is dissolved flow in from raw water inlet pipe 4 and pressurized water pipe 5, respectively. The pressurized water flowing in from the pressurized water pipe 5 is released from its pressurized state, and the air dissolved in the pressurized water in the raw water inflow pipe 4 or flotation tank 1 becomes fine bubbles, and the bubbles become suspended. The suspended solids that adhere to the substance become more easily floated, and the water containing the floating suspended solids collides with the baffle plate 15 and is introduced around the cylindrical body 11 . As shown by the dotted arrow line in the figure, the floating suspended solids 8 float to the water surface of the flotation tank 1, and as shown by the solid arrow line, the separated water flows through the upper end of the cylindrical body 11 to the cylindrical body. 11, then from the lower end of the separated water take-out tube 12, and is taken out from the separated water take-out pipe 14 via the separated water take-out gutter 13 to the outside.

また筒状体11内に流入する分離水中に気泡を
充分に付着していないため、沈降しやすい懸濁物
質が含まれている場合は、一点鎖線の矢印線で示
したごとく当該懸濁物質を筒状体11内に沈降さ
せ、筒状体11の下端から流出させて再び気泡と
接触させて浮上しやすい浮上懸濁物質とする。
Furthermore, if the separated water flowing into the cylindrical body 11 contains suspended solids that tend to settle due to insufficient adhesion of air bubbles, the suspended solids will be removed as shown by the dashed-dotted arrow line. The material is allowed to settle in the cylindrical body 11, flowed out from the lower end of the cylindrical body 11, and brought into contact with air bubbles again to form suspended suspended matter that easily floats.

なお図面で示したごとく当該筒状体11を上方
に向かつて末広がりとすると分離水が筒状体11
の上端からより流入しやすくなり、また下方に向
かつて狭くすることにより筒状体11内の沈降す
る前記懸濁物質の沈降流速を早くすることがで
き、さらにバツフル板15の設置面積を小さくで
きるなどの種々の利点を有するが、場合によつて
は当該筒状体11を単なる円筒あるいは角筒とし
ても差し支えない。
Note that if the cylindrical body 11 is directed upward and widened at the end as shown in the drawing, the separated water will flow into the cylindrical body 11.
It becomes easier to flow in from the upper end, and by narrowing it downward, the sedimentation flow rate of the suspended matter that settles inside the cylindrical body 11 can be increased, and the installation area of the buff-full plate 15 can be made smaller. However, in some cases, the cylindrical body 11 may be a simple cylinder or a rectangular cylinder.

一方水面に浮上した浮上懸濁物質8を回転する
掻取機9により導入溝10内に掻取り、次いで収
集溝16内に収集した後、排出管17より外部へ
取り出す。また浮上槽1の底部に沈澱物が堆積し
た場合はこれを時々ブロー管18より外部へ排出
する。
On the other hand, the floating suspended solids 8 floating on the water surface are scraped into the introduction groove 10 by a rotating scraper 9, then collected in the collection groove 16, and then taken out from the discharge pipe 17. Further, if sediment accumulates at the bottom of the flotation tank 1, it is occasionally discharged to the outside through the blow pipe 18.

<効 果> 以上説明したごとく本考案は懸濁物質を含む原
水を筒状体11の下方からバツフル板15を介し
て筒状体11の周囲に導くので、従来のように水
面付近で急激な流れの拡がりを生じないので乱流
とならず、かつ筒状体11の外側で低速度でしか
も安定した上昇流を作りだすことができるので、
気泡を付着した懸濁物質を破壊することなく効果
的に浮上分離することができる。また筒状体11
内を下降する懸濁物質を筒状体11の下端から流
出して筒状体11の下端外側で、上昇する流体と
再度接触させるので、当該懸濁物質に再び気泡を
付着させることができ、よつて従来の装置と比較
して気泡に接触する機会が多いので、より効果的
に懸濁物質を浮上させることができる。
<Effects> As explained above, the present invention guides the raw water containing suspended solids from below the cylindrical body 11 to the periphery of the cylindrical body 11 via the buff-full plate 15, so that it is not possible to cause a sudden drop near the water surface as in the conventional case. Since the flow does not spread, turbulence does not occur, and a low-velocity and stable upward flow can be created outside the cylindrical body 11.
Suspended substances attached to air bubbles can be effectively separated by flotation without being destroyed. Also, the cylindrical body 11
The suspended matter descending inside flows out from the lower end of the cylindrical body 11 and is brought into contact with the rising fluid again on the outside of the lower end of the cylindrical body 11, so that air bubbles can be attached to the suspended matter again. Therefore, compared to conventional devices, there are more opportunities to come into contact with air bubbles, so suspended matter can be floated more effectively.

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

第1図は本考案の浮上分離層の縦断面説明図で
あり、第2図は第1図の上面図であり、第3図は
従来の浮上分離槽の縦断面説明図である。 1……浮上槽、2……内筒、3……外筒、4…
…原水流入管、5……加圧水管、6……集水樋、
7……分離水管、8……浮上懸濁物質、9……掻
取機、10……導入溝、11……筒状体、12…
…分離水取出筒、13……分離水取出樋、14…
…分離水取出管、15……バツフル板、16……
収集溝、17……排出板、18……ブロー管。
FIG. 1 is an explanatory longitudinal cross-sectional view of the flotation layer of the present invention, FIG. 2 is a top view of FIG. 1, and FIG. 3 is an explanatory longitudinal cross-sectional view of a conventional flotation tank. 1...Flotation tank, 2...Inner cylinder, 3...Outer cylinder, 4...
... Raw water inflow pipe, 5 ... Pressurized water pipe, 6 ... Water collection gutter,
7...Separation water pipe, 8...Floating suspended solids, 9...Scraper, 10...Introduction groove, 11...Cylindrical body, 12...
...Separated water take-out tube, 13...Separated water take-out gutter, 14...
...Separated water outlet pipe, 15...Bullet plate, 16...
Collection groove, 17...discharge plate, 18...blow pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 浮上槽内に両端が開口した筒状体を内設し、当
該筒状体の上端開口部に、両端が開口する分離水
取出筒を挿入することによつて、当該分離水取出
筒の下端開口部を筒状体内部に位置させるととも
に、当該分離水取出筒の上端を浮上槽に形成され
る水面より上方に位置させ、かつ分離水取出筒内
に形成される分離水面に近接して分離水取出管の
開口部を設け、また筒状体の下端開口部の下方に
バツフル板を介して原水流入管の開口部を設けた
構造からなり、原水を原水流入管から流入し、筒
状体の外側に導いて原水中の浮上懸濁物質を浮上
槽の水面に浮上させるとともに、分離水を筒状体
の上端開口部次いで分離水取出筒の下端開口部と
導いて、分離水取出管から流出させることを特徴
とする浮上分離槽。
By installing a cylindrical body with both ends open in the flotation tank, and inserting a separated water take-out cylinder with both ends open into the upper end opening of the cylindrical body, the lower end of the separated water take-out cylinder is opened. is located inside the cylindrical body, and the upper end of the separated water take-out tube is located above the water surface formed in the flotation tank, and the separated water is placed close to the separated water surface formed in the separated water take-out tube. It has a structure in which an opening for a take-out pipe is provided, and an opening for a raw water inflow pipe is provided below the opening at the bottom end of the cylindrical body via a baffle plate. The suspended solids in the raw water are guided to the outside to float to the water surface of the flotation tank, and the separated water is led to the upper end opening of the cylindrical body and then to the lower end opening of the separated water take-out tube, and then flows out from the separated water take-out pipe. A flotation separation tank characterized by:
JP5746585U 1985-04-19 1985-04-19 Expired JPH0233915Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5746585U JPH0233915Y2 (en) 1985-04-19 1985-04-19

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5746585U JPH0233915Y2 (en) 1985-04-19 1985-04-19

Publications (2)

Publication Number Publication Date
JPS61175291U JPS61175291U (en) 1986-10-31
JPH0233915Y2 true JPH0233915Y2 (en) 1990-09-11

Family

ID=30582021

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5746585U Expired JPH0233915Y2 (en) 1985-04-19 1985-04-19

Country Status (1)

Country Link
JP (1) JPH0233915Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0710384B2 (en) * 1989-02-06 1995-02-08 孝志 前 Sewage treatment equipment

Also Published As

Publication number Publication date
JPS61175291U (en) 1986-10-31

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