JPH0768271A - Water purifying method - Google Patents
Water purifying methodInfo
- Publication number
- JPH0768271A JPH0768271A JP16053592A JP16053592A JPH0768271A JP H0768271 A JPH0768271 A JP H0768271A JP 16053592 A JP16053592 A JP 16053592A JP 16053592 A JP16053592 A JP 16053592A JP H0768271 A JPH0768271 A JP H0768271A
- Authority
- JP
- Japan
- Prior art keywords
- water
- air bubbles
- basin
- polymeric flocculant
- muddiness
- 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.)
- Granted
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、水浄化方法に関する。FIELD OF THE INVENTION The present invention relates to a water purification method.
【0002】[0002]
【従来技術とその課題】従来、閉鎖系の汚濁した水を浄
化する方法としては、例えば該汚濁水に無機凝集剤及び
合成系の高分子凝集剤を添加して汚濁及び汚染原因物質
を沈殿槽に沈殿させ、これを除去する方法が知られてい
る。しかしながら、斯かる方法では、沈殿槽を別個に設
ける必要があり、そのために広いスペースを確保しなけ
ればならず、しかも汚濁及び汚染原因物質の沈殿に数日
程度の日数を要し、作業能率が極めて悪いという欠点を
有している。更に該方法によれば、上記凝集剤により、
有用な微生物までもが強制的に沈殿せしめられることに
なり、その結果自然生態系が破壊される虞れがある。2. Description of the Related Art Conventionally, as a method for purifying contaminated water in a closed system, for example, an inorganic coagulant and a synthetic polymer coagulant are added to the contaminated water to settle a pollutant and a pollutant in a sedimentation tank. There is known a method of precipitating and removing this. However, in such a method, it is necessary to separately provide a settling tank, a large space must be secured for that purpose, and moreover, several days are required for the precipitation of pollutants and pollutants, and the work efficiency is high. It has the drawback of being extremely bad. Furthermore, according to the method, by the coagulant,
Even useful microorganisms will be forced to settle, which may result in the destruction of natural ecosystems.
【0003】[0003]
【課題を解決するための手段】本発明の目的は、上記問
題点を解消した新しい水浄化方法を提供することにあ
る。SUMMARY OF THE INVENTION An object of the present invention is to provide a new water purification method which solves the above problems.
【0004】即ち、本発明は、閉鎖系の汚濁した水に、
高圧、高速下に微細気泡を多量に含有する水を循環させ
ると共に、高分子凝集剤を添加して、水に含有されてい
る汚濁及び汚染原因物質を低比重の浮上性凝集体として
浮遊せしめ、次いでこれを捕集して除去することを特徴
とする水の浄化方法に係る。That is, the present invention relates to polluted water in a closed system,
While circulating water containing a large amount of fine bubbles under high pressure and high speed, by adding a polymer flocculant, the contaminants and pollutants contained in the water are suspended as low-specific-gravity floating flocs, Then, it relates to a method for purifying water, which is characterized by collecting and removing this.
【0005】本発明において処理対象とされる水として
は、水の流れのない閉鎖された系の汚濁水である限り特
に限定されるものではなく、例えばゴルフ場の池の水、
溜め池の水、プールの水、小規模の工場排水等を挙げる
ことができる。The water to be treated in the present invention is not particularly limited as long as it is a contaminated water of a closed system in which water does not flow, and for example, water of a golf course pond,
Examples include water from reservoirs, pool water, and small-scale industrial wastewater.
【0006】高圧、高速下に微細気泡を多量に含有する
水を循環させるに当って用いられる装置としては、従来
公知の微細気泡発生装置を広く用いることができる。高
圧及び高速の程度としては、特に限定がなく、適用すべ
き閉鎖水系の広さ、水の汚濁程度等により適宜決定すれ
ばよい。As a device used for circulating water containing a large amount of fine bubbles under high pressure and high speed, conventionally known fine bubble generators can be widely used. The degree of high pressure and high speed is not particularly limited and may be appropriately determined depending on the size of the closed water system to be applied, the degree of water pollution, and the like.
【0007】本発明では、閉鎖系の汚濁した水に、高
圧、高速下に微細気泡を多量に含有する水を循環させつ
つ、これに高分子凝集剤を添加、配合することが必須で
ある。用いられる高分子凝集剤としては、水溶性である
限り従来公知のものを広く利用でき、例えばキチンキト
サン等の天然高分子化合物、ポリアクリル酸ソーダ、ポ
リアクリル酸アミド、ポリアクリル酸イミド等の合成高
分子化合物等を挙げることができる。これら高分子凝集
剤は、1種又は2種以上混合して使用され得る。本発明
では、特にキチンキトサンとポリアクリル酸ソーダ又は
ポリアクリル酸アミドとを組合わせて使用するのが望ま
しく、斯くして本発明の所期の効果が顕著に発現され得
る。高分子凝集剤の添加量としても、特に制限されるも
のではなく、適用すべき閉鎖水系の広さ、水の汚濁程度
等により適宜決定すればよい。In the present invention, it is essential to add and blend a polymer flocculant into closed polluted water while circulating water containing a large amount of fine bubbles under high pressure and high speed. As the polymer flocculant used, conventionally known ones can be widely used as long as they are water-soluble. For example, natural polymer compounds such as chitin chitosan, polyacrylic acid soda, polyacrylic acid amide, polyacrylic acid imide and the like are synthesized. Polymer compounds and the like can be mentioned. These polymer flocculants may be used alone or in combination of two or more. In the present invention, it is particularly desirable to use chitin chitosan in combination with polyacrylic acid soda or polyacrylic acid amide, and thus the intended effect of the present invention can be remarkably exhibited. The amount of the polymer flocculant added is not particularly limited and may be appropriately determined depending on the size of the closed water system to be applied, the degree of water contamination, and the like.
【0008】上記処理により、水に含有されている汚濁
及び汚染原因物質が低比重の凝集体になって、水上に浮
遊してくるので、これを従来公知の捕集手段、例えばス
クリュー式捕集機を用いる方法、オリーバ式(ドラム回
転式)捕集機を用いる方法、ベルトコンベア式捕集機を
用いる方法等により、除去すればよい。[0008] By the above treatment, the pollutants and pollutants contained in water become agglomerates of low specific gravity and float on the water, and these are collected by conventionally known collecting means, for example, screw type collecting. It may be removed by a method using a machine, a method using an oliver type (drum rotation type) collector, a method using a belt conveyor type collector, or the like.
【0009】本発明の方法の一実施態様を図1に基づい
て以下に説明する。One embodiment of the method of the present invention will be described below with reference to FIG.
【0010】池(1)にある閉鎖された水の一部が水取
入口(2)からポンプによりベンチュリー(5)に送水
される。一方、コンプレッサー(4)により空気がベン
チュリー(5)に送気され、ここで微細な気泡(3μm
以下)が水中に発生せしめられ、引続く気液混合装置
(6)で微細な気泡が水中に均一に分散された状態とさ
れる。気液混合装置としては、従来公知のものを広く使
用でき、例えばスタティックミキサー、スケアーミキサ
ー、ハニカムミキサー等を挙げることができる。これら
気液混合装置は、水質の汚濁度、粘性等に応じて適宜選
択して使用すればよいし、斯かる気液混合装置を用いな
い場合でも本発明の目的をある程度達成できる。上記で
得られる微細気泡が多量に含有された水は、次に気液分
離タンク(7)に送られ、ここで大径の気泡を除去した
後、高分子凝集剤注入ホッパー(8)を経由して、水噴
射口(9)を通じて池(1)に吐き出される。高分子凝
集剤注入ホッパー(8)では高分子凝集剤が微細気泡含
有水に添加、配合される。高分子凝集剤は、解離した状
態で水に溶解しているが、水噴射口(9)を通じて池
(1)に吐き出された後には、各々の高分子物質が有す
る官能基(イオン基)が汚濁及び汚染原因物質である無
機乃至有機のコロイド状懸濁物質や電解物質等と架橋反
応して吸着し、凝結し、更に凝集し、汚濁及び汚染原因
物質を含有、包接した凝集体になる。この際に、多量の
微細気泡をも同時に包接しながら多孔性凝集体(スカ
ム)になる。この凝集体は、低比重の浮上性のものであ
るために、短時間に水上に浮遊するのである。一方、微
細気泡を多量に含有し、高分子凝集剤が添加された水
は、水噴射口(9)からかなりの勢いで吐き出されるの
で、処理すべき水を水圧にて攪拌することになり、上記
の高分子凝集剤による凝集作用等を広範囲で促進させる
役割を果たす。上記水噴射口(9)は、逃し弁と同じ構
造を有しているものでよい。本発明では、次に水上に浮
遊してくるスカムをオリーバ式捕集機を用いて、池
(1)から取り出せばよい。A part of the closed water in the pond (1) is pumped from the water intake (2) to the venturi (5). On the other hand, air is sent to the venturi (5) by the compressor (4), where fine air bubbles (3 μm)
The following) is generated in water, and fine gas bubbles are made to be uniformly dispersed in water in the subsequent gas-liquid mixing device (6). As the gas-liquid mixing device, conventionally known ones can be widely used, and examples thereof include a static mixer, a scare mixer, and a honeycomb mixer. These gas-liquid mixing devices may be appropriately selected and used according to the degree of pollution of water quality, viscosity, and the like, and the object of the present invention can be achieved to some extent even when such a gas-liquid mixing device is not used. The water containing a large amount of fine air bubbles obtained above is then sent to the gas-liquid separation tank (7), where large-sized air bubbles are removed, and then the water passes through the polymer coagulant injection hopper (8). Then, it is discharged to the pond (1) through the water injection port (9). In the polymer coagulant injection hopper (8), the polymer coagulant is added to and mixed with water containing fine bubbles. The polymer flocculant is dissolved in water in a dissociated state, but after being discharged into the pond (1) through the water injection port (9), the functional group (ionic group) possessed by each polymer substance is changed. Cross-linking reaction with inorganic or organic colloidal suspension substances or electrolytes that are pollutants and pollutants, adsorbs, coagulates, and agglomerates to form a clathrate containing inclusions of pollutants and pollutants. . At this time, a large amount of fine bubbles are simultaneously included to form a porous aggregate (scum). Since this aggregate has a low specific gravity and floatability, it floats on water in a short time. On the other hand, water containing a large amount of fine bubbles and added with the polymer coagulant is discharged from the water injection port (9) with considerable force, so that the water to be treated is agitated by water pressure, It plays a role of promoting the aggregating action and the like of the above-mentioned polymer aggregating agent in a wide range. The water injection port (9) may have the same structure as the relief valve. In the present invention, the scum floating next on the water may be taken out from the pond (1) using an oliver type collector.
【0011】[0011]
【発明の効果】本発明によれば、汚濁及び汚染原因物質
がスカムとなって水上に浮遊してくるので、これを取り
除くだけでよく、従来のように沈殿槽を別個に設ける必
要もなく、狭い用地での水の浄化が可能になった。しか
も、本発明によれば、スカムとなって水上に浮遊してく
るのに要する時間も数時間程度という極めて短時間であ
り、作業能率の点でも優れたものである。また本発明の
方法を実施することにより、自然生態系がなんら阻害さ
れることはない。EFFECTS OF THE INVENTION According to the present invention, since pollutants and pollutants cause scum to float on the water, it suffices to remove them, and it is not necessary to separately provide a sedimentation tank as in the conventional case. It has become possible to purify water on a small site. Moreover, according to the present invention, the time required for the scum to float on the water is a very short time of about several hours, which is excellent in work efficiency. In addition, by carrying out the method of the present invention, the natural ecosystem is not disturbed at all.
【図1】本発明の方法の一実施態様を示す概略図であ
る。FIG. 1 is a schematic diagram showing an embodiment of the method of the present invention.
(1)…池、(2)…水取入口、(3)…ポンプ、
(4)…エアーコンプレッサー、(5)…ベンチュリ
ー、(6)…気液混合装置、(7)…気液分離タンク、
(8)高分子凝集剤注入ホッパー、(9)…水噴出口、
(10)…気泡、(11)…スカム、(12)…オリー
バ式捕集機(1) ... Pond, (2) ... water intake, (3) ... pump,
(4) ... Air compressor, (5) ... Venturi, (6) ... Gas-liquid mixing device, (7) ... Gas-liquid separation tank,
(8) Polymer coagulant injection hopper, (9) ... Water jet port,
(10) ... Air bubbles, (11) ... Scum, (12) ... Oliva type collector
───────────────────────────────────────────────────── フロントページの続き (72)発明者 八木 一三 大阪府堺市中三国ヶ丘町6丁2−19 (72)発明者 藤田 美代子 大阪府堺市新金岡町4丁6−14−106 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Ichizo Yagi 6-chome Nakamikunigaoka-cho, Sakai-shi, Osaka 2-19 (72) Inventor Miyoko Fujita 4-6-14 Shin-kanaoka-cho, Sakai-shi, Osaka
Claims (1)
微細気泡を多量に含有する水を循環させると共に、高分
子凝集剤を添加して、水に含有されている汚濁及び汚染
原因物質を低比重の浮上性凝集体として浮遊せしめ、次
いでこれを捕集して除去することを特徴とする水の浄化
方法。1. A closed system of polluted water, in which water containing a large amount of fine bubbles is circulated under high pressure and high speed, and a polymer flocculant is added to the polluted water and the cause of contamination. A method for purifying water, which comprises suspending a substance as a floating aggregate having a low specific gravity, and then collecting and removing this.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4160535A JPH0775705B2 (en) | 1992-06-19 | 1992-06-19 | Water purification method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4160535A JPH0775705B2 (en) | 1992-06-19 | 1992-06-19 | Water purification method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0768271A true JPH0768271A (en) | 1995-03-14 |
| JPH0775705B2 JPH0775705B2 (en) | 1995-08-16 |
Family
ID=15717082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4160535A Expired - Lifetime JPH0775705B2 (en) | 1992-06-19 | 1992-06-19 | Water purification method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0775705B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003100520A1 (en) * | 2002-05-24 | 2003-12-04 | Kabushiki Kaisha Aqua-Enterprise | Projection screen forming method and device therefor, and image displaying method and device therefor |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105329969A (en) * | 2015-11-27 | 2016-02-17 | 无锡工源机械有限公司 | Jet flow air dissolving device |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6051591A (en) * | 1983-08-31 | 1985-03-23 | Kurita Water Ind Ltd | Pressure flotation separation apparatus |
| JPH0398688A (en) * | 1989-09-12 | 1991-04-24 | Kubota George Fischer Kk | Water treatment method |
-
1992
- 1992-06-19 JP JP4160535A patent/JPH0775705B2/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6051591A (en) * | 1983-08-31 | 1985-03-23 | Kurita Water Ind Ltd | Pressure flotation separation apparatus |
| JPH0398688A (en) * | 1989-09-12 | 1991-04-24 | Kubota George Fischer Kk | Water treatment method |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003100520A1 (en) * | 2002-05-24 | 2003-12-04 | Kabushiki Kaisha Aqua-Enterprise | Projection screen forming method and device therefor, and image displaying method and device therefor |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0775705B2 (en) | 1995-08-16 |
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