JPS59278B2 - flotation separation device - Google Patents
flotation separation deviceInfo
- Publication number
- JPS59278B2 JPS59278B2 JP52025908A JP2590877A JPS59278B2 JP S59278 B2 JPS59278 B2 JP S59278B2 JP 52025908 A JP52025908 A JP 52025908A JP 2590877 A JP2590877 A JP 2590877A JP S59278 B2 JPS59278 B2 JP S59278B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- tank
- raw water
- pipe
- scum
- 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、懸濁性または沈降性の物質を含有する廃水等
の水液から、該特定物質を分離処理する浮上分離装置に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a flotation separation device for separating a specific substance from an aqueous liquid such as wastewater containing suspended or sedimentary substances.
廃水の処理などに利用される浮上分離方法には、(1)
、気泡接触型、(2)、気泡析出型の2型式が知られて
おり、さらに、前者の型式には、攪拌式、空気吹込式、
および電解式などの方式があり、また、後者の型式には
、減圧式、および加圧式などの方式がある。Flotation separation methods used for wastewater treatment include (1)
Two types are known: , bubble contact type, and (2) bubble precipitation type.Furthermore, the former type includes stirring type, air blowing type,
The latter type includes a reduced pressure type and a pressurized type.
しかして、これら倒れの方式を採る場合においても、特
定物質を浮上し易い凝集フランクに形成することが最も
重要なことであるが、(1)、従来の気泡接触型では、
作動時における浮上速度が遅いばかりでなく、処理装置
の設置に広いスペースを必要とし、また、(2)、従来
の気泡析出型では、処理装置の構造が複雑化して、設備
費が高価になるなど、何れの型式においても多くの欠点
を持っていた。However, even when adopting these collapse methods, the most important thing is to form the specific substance into an aggregation flank that is easy to float. (1) In the conventional bubble contact type,
Not only is the floating speed during operation slow, but a large space is required to install the processing equipment, and (2) with the conventional bubble deposition type, the structure of the processing equipment is complicated, resulting in high equipment costs. Both types had many drawbacks.
本発明は、上記欠点を解消するためになされたものであ
って、すなわち本発明の目的は、たとえばコロイド状水
酸化鉄や、水酸化アルミニウムのように、沈降性の極め
て悪い各種の特定物質を含有する廃水に対しても、有効
に分離作動を行い、かつ構造が簡単かつ安価な浮上分離
装置を提供することにある。The present invention has been made to eliminate the above-mentioned drawbacks, and the purpose of the present invention is to eliminate various specific substances that have extremely poor sedimentation properties, such as colloidal iron hydroxide and aluminum hydroxide. It is an object of the present invention to provide a flotation separation device which effectively performs a separation operation even on contained wastewater and which has a simple structure and is inexpensive.
以下、図示の一実施例に基づいて本発明を説明する。The present invention will be described below based on an illustrated embodiment.
廃水処理系の上流端には、処理原水の貯水タンク1が設
置されていて、このタンク1内には、界面活性剤のよう
な起泡剤を既に含有しているか、または、処理前にあら
かじめ同起泡剤が添加されるかして、起泡剤を含んだ原
水が貯水されている。A storage tank 1 for raw water to be treated is installed at the upstream end of the wastewater treatment system, and this tank 1 already contains a foaming agent such as a surfactant, or contains a foaming agent such as a surfactant beforehand. The foaming agent is added and raw water containing the foaming agent is stored.
このタンク1の上方には、小型のフィードタンク2が取
付られていて、ポンプ3による原水の汲上げと、戻し管
4によるオーバフローの循環作用で、フィードタンク2
内には、常に定ヘッドHの原水が貯えられる。A small feed tank 2 is attached above this tank 1, and the pump 3 pumps up raw water and the return pipe 4 circulates the overflow.
A constant head H of raw water is always stored inside.
また、処理系の下流端には、流入側が仕切板5aで仕切
られた箱型の分離タンク5が設置されており、このタン
ク5の下流側の上部には、水液の表層をオーバフローさ
せるためのリップ5bが形成3
されると共に、同下流側の床部には、排水管5Cが取付
られている。Furthermore, a box-shaped separation tank 5 whose inflow side is partitioned by a partition plate 5a is installed at the downstream end of the treatment system. A lip 5b is formed, and a drain pipe 5C is attached to the floor on the downstream side.
しかして、分離タンク5の流入側の床部には、一連の送
水管6,7,8.9を介してフィードタンク2から原水
が送り込まれているが、その給送作動は、送水管7,8
間に介設されたポンプ10によって行われている。Raw water is fed from the feed tank 2 to the floor on the inflow side of the separation tank 5 via a series of water pipes 6, 7, 8. ,8
This is done by a pump 10 interposed between them.
ところで、送水管6,7間と、送水管8,9間には、夫
々T管より成る前後部吸気管11.12が弁蓋されてい
て、各吸気管の上向通孔11a。Incidentally, between the water pipes 6 and 7 and between the water pipes 8 and 9, front and rear intake pipes 11 and 12 each made of a T-tube are covered with valve lids, and the upward passage holes 11a of each intake pipe.
12aは、調節弁13.14を介し、ポンプ10よりも
高位置における定ヘッドH付近の高さにおいて外気に開
口している。12a opens to the outside air at a height near the fixed head H at a higher position than the pump 10 via a regulating valve 13.14.
そのほか、各吸気管11.12には、低濃度に希釈され
た高分子凝集剤が供給される添加孔11b。In addition, each intake pipe 11.12 has an addition hole 11b through which a polymer flocculant diluted to a low concentration is supplied.
12bが付設されており、また、送水管6には給水流量
を調整するための制御弁15が介設されている。12b is attached, and a control valve 15 for adjusting the water supply flow rate is interposed in the water pipe 6.
なお、ポンプ10よりも下流側における送水管9の管径
は、流速を下げることによって特定物質の凝集効果を図
る目的から、他管6,7.8の径より大きい径に設定さ
れている。Note that the diameter of the water supply pipe 9 on the downstream side of the pump 10 is set to be larger than the diameter of the other pipes 6, 7.8 for the purpose of reducing the flow rate and thereby achieving a flocculating effect of the specific substance.
つぎに、以上のように構成された実施例分離装置の作動
につき述べる。Next, the operation of the embodiment separator constructed as above will be described.
まず、装置の稼動に際して、制御弁15の開度と、調節
弁13.14の夫々の開度を連係的に調整することによ
り、吸気管の調節弁13,14部において適量の空気が
外部より原水中に混入するように操作する。First, when operating the device, by adjusting the opening degree of the control valve 15 and the opening degree of each of the regulating valves 13 and 14 in conjunction with each other, an appropriate amount of air is supplied from the outside to the regulating valves 13 and 14 of the intake pipe. Operate so that it is mixed into raw water.
なお、このような操作は、給水ヘッドが一定Hしており
、且つ吸気管はポンプ10よりも高位置にあるために極
めて容易であり、かつ、外気の吸入流量は正確に維持さ
れる。Note that such an operation is extremely easy because the water supply head is at a constant H level and the intake pipe is located at a higher position than the pump 10, and the intake flow rate of outside air is maintained accurately.
このような吸気作動により、給送される原水中には、適
量の気泡と凝集剤が混入し、あわせて送水管9における
流速低下に援けられて、特定物質は送水管9において有
効に泡沫スカムに生成され**る。Due to this suction operation, an appropriate amount of air bubbles and flocculant are mixed into the supplied raw water, and with the help of a decrease in the flow velocity in the water pipe 9, the specific substance is effectively turned into foam in the water pipe 9. Generated by scum**.
従って、原水が分離タンク5に流入した時点において、
凝集スカムは殆んど瞬間的に浮上し、事後、スカムは、
タンク5内の表層上を押し流されながら圧縮、過密化し
、さらに、リップ5bを越えて外部に排水され、これに
より、特定物質は、迅速かつ有効に原水から分離され、
系外に排出される。Therefore, at the time the raw water flows into the separation tank 5,
Agglomerated scum surfaces almost instantaneously, and after the fact, scum is
The specific substances are compressed and overcrowded as they are swept over the surface layer in the tank 5, and are further drained to the outside beyond the lip 5b, whereby the specific substances are quickly and effectively separated from the raw water.
Exhausted from the system.
なお、図示鎖線のように、処理水の一部を戻し管16を
介してポンプ10の吸込側に流し込むようにすれば、原
水中に添加すべき起泡剤の節減に資する有利性がある。In addition, if a part of the treated water is allowed to flow into the suction side of the pump 10 via the return pipe 16, as shown by the chain line in the figure, there is an advantage in contributing to saving on the foaming agent to be added to the raw water.
ここで本願発明者が行った実施例分離装置の試験成績を
説明する。Here, the test results of the example separation apparatus conducted by the inventor of the present application will be explained.
(試験例、その−)
供試原水・・・水酸化鉄30011+)[11含有水(
硫酸第1鉄の水溶液に、苛性ソーダ水溶
液を加えて、pH6、8としたもの)
添加起泡剤・・・ライポン(商品名)201)声添加凝
集剤・・・バイモロツクM−366(商品名)100p
陣
給水流量・・・1.2rrl’/H
(試験例、その二)
供試原水・・・稼動工場のバレル研摩廃水に硫酸を添加
したpH3,3の第1液と、硫
酸アルミニウム水溶液700pPの
第2液とを混合した水液、(pH6,8)そ の 他・
・・第1例に同じ
成 績
以上の成績により、実施例分離装置における有効性が確
認された。(Test example, part-) Test raw water...Iron hydroxide 30011+) [11-containing water (
A caustic soda aqueous solution was added to an aqueous solution of ferrous sulfate to adjust the pH to 6 or 8) Added foaming agent: Ripon (trade name) 201) Added flocculant: Bimorok M-366 (trade name) 100p
Water supply flow rate: 1.2rrl'/H (Test example, part 2) Test raw water: First solution with pH 3.3, which is made by adding sulfuric acid to barrel polishing waste water from an operating factory, and aluminum sulfate aqueous solution of 700 pP. Aqueous liquid mixed with second liquid, (pH 6, 8), etc.
...Same results as in Example 1. The effectiveness of the separation device of the example was confirmed by the above results.
以上のように、本発明に係る浮上分離装置によれば、処
理原水タンクと、浮上分離タンクを連設すると共に、両
タンク間の送水管中に、空気と凝集剤を混入させるよう
に構成したので、比較的簡単かつ安価な構造の装置によ
り、迅速かつ有効に特定物質をスカム生成して、これを
有効に浮上分離させることが可能となり、これにより、
装置の実用性、経済性を向上させる効果が大きい。As described above, according to the flotation separation device according to the present invention, the treated raw water tank and the flotation separation tank are arranged in series, and the air and flocculant are mixed into the water pipe between the two tanks. Therefore, using a device with a relatively simple and inexpensive structure, it is possible to quickly and effectively generate scum of a specific substance and effectively float and separate it.
This has a great effect on improving the practicality and economic efficiency of the device.
図は、本発明の一実施例を示す浮上分離装置の概要図で
ある。
1・・・・・・処理原水タンク、H・・・・・・定ヘッ
ド、2・・・・・・フィードタンク、4・・・・・・分
離タンク、6,7゜8.9・・・・・・送水管、10・
・・・・・ポンプ、11.12・・・・・・吸気管、I
la、12a・・・・・・通孔、11b。
12b・・・・・・添加孔。The figure is a schematic diagram of a flotation separation device showing an embodiment of the present invention. 1...Treatment raw water tank, H...Constant head, 2...Feed tank, 4...Separation tank, 6,7゜8.9...・・・・Water pipe, 10・
...Pump, 11.12...Intake pipe, I
la, 12a...through hole, 11b. 12b... Addition hole.
Claims (1)
水液から、該特定物質を分離処理する浮上分離装置にお
いて、処理原水タンクと、表層を浮遊するスカムをオー
バフローさせる分離タンクとを、上記水液の流過経路の
途中に設置し、かつ、ポンプが介設された送水管により
、上記原水タンクから分離タンクへ水液を給送させると
共に、同ポンプの少なくとも前部位置における送水管の
途中に吸気管を発着し、さらに、この吸気管の一通孔を
空気中に開口させると共に、高分子凝集剤が供給される
添力pJLを、吸気管に付設し、これにより、給送中の
水液に気泡と凝集剤を混入させて、上記特定物質のスカ
ム化を促進し、上記分離タンクにおけるスカム浮上を容
易にしたことを特徴とする浮上分離装置。1. In a flotation separator that separates specific substances from water such as wastewater containing suspended or sedimentary specific substances, a treated raw water tank and a separation tank that overflows the scum floating on the surface layer, A water pipe installed in the middle of the flow path of the water liquid and equipped with a pump is used to feed the water liquid from the raw water tank to the separation tank, and the water pipe is installed at least in front of the pump. An intake pipe is placed in the middle of the air, and a hole in this intake pipe is opened to the air, and an additive pJL to which a polymer flocculant is supplied is attached to the intake pipe. A flotation separation device characterized in that air bubbles and a flocculant are mixed into the aqueous liquid to promote scum formation of the specific substance, thereby facilitating the floating of the scum in the separation tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52025908A JPS59278B2 (en) | 1977-03-11 | 1977-03-11 | flotation separation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52025908A JPS59278B2 (en) | 1977-03-11 | 1977-03-11 | flotation separation device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS53111570A JPS53111570A (en) | 1978-09-29 |
JPS59278B2 true JPS59278B2 (en) | 1984-01-06 |
Family
ID=12178869
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP52025908A Expired JPS59278B2 (en) | 1977-03-11 | 1977-03-11 | flotation separation device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59278B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01307492A (en) * | 1988-06-07 | 1989-12-12 | Iseki Tory Tech Inc | Treatment of mud water |
-
1977
- 1977-03-11 JP JP52025908A patent/JPS59278B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS53111570A (en) | 1978-09-29 |
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