JPH0239957B2 - - Google Patents
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- Publication number
- JPH0239957B2 JPH0239957B2 JP13439187A JP13439187A JPH0239957B2 JP H0239957 B2 JPH0239957 B2 JP H0239957B2 JP 13439187 A JP13439187 A JP 13439187A JP 13439187 A JP13439187 A JP 13439187A JP H0239957 B2 JPH0239957 B2 JP H0239957B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- air
- dissolved oxygen
- mineral
- magnetic field
- 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 - Lifetime
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Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Farming Of Fish And Shellfish (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Description
産業上の利用分野
本発明は、空気を水中に曝気して水中溶存酸素
を富化させる方法、より詳しくは水中に曝気させ
る空気を磁化活性化することにより水中溶存酸素
を富化させる方法に関する。
従来の技術
水は一般に放置しておくとその溶存酸素量の減
少が起こり、これに伴つて水の腐敗や水棲生物の
死滅が起こる。このような腐敗や死滅を防止する
ためには水中溶存酸素の富化が必要であり、従来
より種々の方法による水中溶存酸素の富化が行な
われてきている。該水中の溶存酸素量を増加させ
る方法としては、代表的には空気を水中に曝気さ
せる方法、例えばエアーホースを水中に導入して
送気し、多数の気泡を水と接触させる方法や曝気
機で水面や水中を攪拌する方法等が知られてい
る。しかしながら、かかる曝気法による溶存酸素
の富化は、量的にも、時間的にも限界があり、飽
和溶解度以上に高めることはできず、しかも富化
された溶存酸素状態を永く保つことも困難であ
る。
一方、従来より、水の浄化方法として磁界を利
用することにより、スケールの発生及び付着の防
止や滅菌等を行ない得ることが知られている。か
かる磁界を利用した水処理法を応用することによ
つて、酸素を励起させ、水中溶存酸素の富化を行
なうことは可能であるが、その効果は磁界の強さ
(磁束密度の強度)に依存し、通常水中溶存酸素
の富化に充分な磁界強度を生じさせることは困難
である。即ち、上記方法では、水と磁石とを直接
接触させることなく、通常上記被処理水を適当な
配管に流し、該配管の外部に磁石を設置して磁界
を生じさせる手段が取られているが、この手段で
は必然的に磁極間の距離は配管の外径以上とな
り、充分な磁界強度を得ることが困難となる。特
に配管の径が大きい場合、上記方法は採用できな
い。また磁石表面を何らかの手段により被覆して
水中に配置する手段も考えられるか、かかる手段
では管内配置が複雑となり実用的でない。しかも
上記いずれの手段を採用する場合も、磁界を利用
するのみでは、富化された水中溶存酸素は安定性
に乏しく、この富化状態を永く保つことはできな
い。
発明が解決しようとする問題点
本発明者らは、上記従来技術の欠点を解消し、
より簡単に、効率よく水中溶存酸素量を急速に向
上させ得、しかも向上させた溶存酸素状態を長期
間保持できる、新しい水中溶存酸素の富化方法を
提供することを目的として鋭意研究を重ねた。そ
の結果、水中に曝気させるべき空気を特定の自然
残留磁化を有する鉱物と接触させて磁化活性化す
る時には、上記目的に合致する水中溶存酸素の富
化方法が提供できることを見出し、ここに本発明
を完成するに至つた。
問題点を解決するための手段
本発明は、空気を水中に爆気して水中溶存酸素
を富化するに当たり、水中に曝気させる空気を、
自然残留磁化を有する鉱物と接触させて磁化活性
化するか又はこれと共に上記空気に磁界を作用さ
せて空気中の酸素を励起させることを特徴とする
水中溶存酸素の富化方法に係わる。
本発明方法によれば、簡単に、効率よく水中溶
存酸素量を急速に且つ顕著に向上させることがで
き、しかも向上された溶存酸素状態を長期間保持
させることができる。
本発明方法によつて、かかる優れた効果が奏さ
れる理由はなお明確ではないが、本発明に利用す
る自然残留磁化を有する鉱物は、それに固有の磁
化作用を有しており、これを空気と接触させる時
には、該鉱物より無方向に発生される電磁波によ
つて、空気乃至その中の酸素が磁化活性化され、
また上記空気に磁界を作用させる時には、酸素が
励起され、上記鉱物との接触による磁化活性化も
一層顕著となるためと考えられる。即ち、酸素は
常磁性体であり励起し易く、これを上記の如く特
定の鉱物と接触させ、また磁場を与えるときに
は、酸素分子の価電子の運動軌道が一つに互いに
近づこうとし、エネルギー準位が上がり励起状態
となり、活性酸素状態を呈する。この際のエネル
ギーは、勿論紫外線やコロナ放電のような強いも
のではないので、酸素分子の解離によるオゾン発
生等は起きないが、イオン化は進むと考えられ、
これにより該酸素の水分子に対する親和性が高ま
り、分子会合が起こり、かくして水中の溶存酸素
が急速に高められ、またこの向上された溶存酸素
状態が上記鉱物の磁化作用により安定するものと
考えられる。いずれにせよ、従来、水中溶存酸素
の富化、安定化に、自然残留磁化を有する鉱物の
利用及び該鉱物と磁界作用との併用が行なわれた
例はなく、勿論かかる利用乃至併用によつて、本
発明の目的とする水中溶存酸素の富化、安定化が
行ない得るとの知見も皆無である。
本発明方法においては、水中に曝気させる空気
を自然残留磁化を有する鉱物と接触させて磁化活
性化することを必須とする。
ここで自然残留磁化を有する鉱物としては、自
然残留磁化10-4〜10-13T(Sl慣用磁化強度、以下
同じ)を有する各種のものを使用できる。その代
表例としては、上記範囲の自然残留磁化を有する
粘土類及び鉱石類を例示できる。この粘土類は、
通常石英、長石、緑泥石、角閃石及び雲母をその
構成鉱物とし、SiO2及びAl2O3を主成分とする赤
褐色のものであり、本発明では粒度約2μm以下
の粉末形態で用いられるが好ましい。また上記鉱
石類とは、花崗岩、石英斑岩、安山岩、流紋岩等
やそれらの周辺の堆積岩、例えば泥岩、砂岩等が
熱による変成作用を受けて硬くなつた所謂ホルン
エルスを指称し、これは、SiO2及びAl2O3を主成
分とする灰色鉱石であり、通常適当な大きさに粉
砕して利用され、特に粒度5μm以下の粉末形態
で用いられるのが有利である。
上記自然残留磁化を有する鉱物の具体例として
は、宮崎県東臼杵郡北方町や同西臼杵郡日之影町
付近に産生される粘度及び鉱石を例示できる。之
等の特徴及び分析値は、下記第1表に示す通りで
ある。
INDUSTRIAL APPLICATION FIELD The present invention relates to a method of enriching dissolved oxygen in water by aerating air into water, and more particularly to a method of enriching dissolved oxygen in water by magnetizing and activating the air aerated into water. BACKGROUND ART Generally, when water is left undisturbed, the amount of dissolved oxygen in the water decreases, which causes the water to rot and aquatic organisms to die. In order to prevent such rotting and death, it is necessary to enrich dissolved oxygen in water, and various methods have been used to enrich dissolved oxygen in water. Typical methods for increasing the amount of dissolved oxygen in the water include a method of aerating air into the water, such as a method of introducing an air hose into the water and supplying air to bring a large number of bubbles into contact with the water, and an aeration machine. A method of stirring the water surface or water with a stirrer is known. However, the enrichment of dissolved oxygen by such aeration method is limited both in quantity and time, and it is not possible to increase the solubility beyond the saturated solubility, and furthermore, it is difficult to maintain the enriched dissolved oxygen state for a long time. It is. On the other hand, it has been conventionally known that by utilizing a magnetic field as a water purification method, it is possible to prevent scale formation and adhesion, and to sterilize water. By applying water treatment methods using such magnetic fields, it is possible to excite oxygen and enrich dissolved oxygen in water, but the effect depends on the strength of the magnetic field (intensity of magnetic flux density). It is usually difficult to generate a magnetic field strength sufficient to enrich dissolved oxygen in water. That is, in the above method, the water to be treated is usually passed through a suitable pipe, and a magnet is installed outside the pipe to generate a magnetic field, without direct contact between the water and the magnet. In this method, the distance between the magnetic poles is inevitably greater than the outer diameter of the pipe, making it difficult to obtain sufficient magnetic field strength. In particular, when the diameter of the pipe is large, the above method cannot be adopted. It is also conceivable to cover the surface of the magnet with some kind of means and place it in water; however, such a method would complicate the arrangement within the tube and would be impractical. Moreover, in any case where any of the above-mentioned means is adopted, the enriched dissolved oxygen in water has poor stability and cannot maintain this enriched state for a long time only by using a magnetic field. Problems to be Solved by the Invention The present inventors have solved the drawbacks of the above-mentioned prior art,
We have conducted extensive research with the aim of providing a new method for enriching dissolved oxygen in water that can more easily and efficiently increase the amount of dissolved oxygen in water and maintain the improved dissolved oxygen state for a long period of time. . As a result, it was discovered that when the air to be aerated into water is brought into contact with a mineral having a specific natural residual magnetization to activate magnetization, a method for enriching dissolved oxygen in water that meets the above objective can be provided, and the present invention is hereby made. I was able to complete it. Means for Solving the Problems The present invention provides that when air is aerated into water to enrich dissolved oxygen in water, the air to be aerated into water is
The present invention relates to a method for enriching dissolved oxygen in water, which comprises bringing the air into contact with a mineral having natural residual magnetization to activate its magnetization, or simultaneously applying a magnetic field to the air to excite oxygen in the air. According to the method of the present invention, the amount of dissolved oxygen in water can be rapidly and significantly increased simply and efficiently, and the improved dissolved oxygen state can be maintained for a long period of time. The reason why the method of the present invention achieves such excellent effects is still not clear, but the minerals with natural residual magnetization used in the present invention have an inherent magnetizing effect, and this When brought into contact with the mineral, the air or the oxygen in it is magnetized and activated by the electromagnetic waves generated non-directionally by the mineral.
It is also believed that this is because when a magnetic field is applied to the air, oxygen is excited and the magnetization activation due to contact with the mineral becomes even more significant. In other words, oxygen is a paramagnetic substance and is easily excited. When oxygen is brought into contact with a specific mineral as described above and a magnetic field is applied, the orbits of the valence electrons of oxygen molecules tend to approach each other, causing the energy level to change. increases and becomes an excited state, exhibiting an active oxygen state. Of course, the energy at this time is not as strong as ultraviolet rays or corona discharge, so ozone generation due to the dissociation of oxygen molecules does not occur, but ionization is thought to proceed.
This increases the affinity of the oxygen for water molecules, causing molecular association, thus rapidly increasing the dissolved oxygen in the water, and it is thought that this improved dissolved oxygen state is stabilized by the magnetization of the mineral. . In any case, there has been no example of the use of minerals with natural residual magnetization or the combination of such minerals and magnetic field action to enrich and stabilize dissolved oxygen in water, and of course, such use or combination has never been done. There is also no knowledge that enrichment and stabilization of dissolved oxygen in water, which is the objective of the present invention, can be achieved. In the method of the present invention, it is essential to bring the air aerated into the water into contact with minerals having natural residual magnetization to activate magnetization. As the mineral having natural residual magnetization, various minerals having a natural residual magnetization of 10 -4 to 10 -13 T (commonly used Sl magnetization strength, hereinafter the same) can be used. Typical examples include clays and ores having natural residual magnetization within the above range. This clay is
Usually, its constituent minerals are quartz, feldspar, chlorite, amphibole, and mica, and it is a reddish-brown substance whose main components are SiO 2 and Al 2 O 3. In the present invention, it is used in the form of a powder with a particle size of about 2 μm or less. preferable. In addition, the above-mentioned ores refer to so-called hornels, which are made of granite, quartz porphyry, andesite, rhyolite, etc., and sedimentary rocks around them, such as mudstone and sandstone, which have become hard due to thermal metamorphism. , SiO 2 and Al 2 O 3 as main components, and is usually used after being crushed to an appropriate size, and it is particularly advantageous to use it in the form of a powder with a particle size of 5 μm or less. Specific examples of minerals having natural residual magnetization include viscosity and ores produced near Kitagata-cho, Higashiusuki-gun, Miyazaki Prefecture, and Hinokage-cho, Nishiusuki-gun, Miyazaki Prefecture. The characteristics and analysis values are as shown in Table 1 below.
【表】
上記例示の鉱物(粘土及び鉱石)は、また上記
成分以外に、チタン、マンガン、銅、鉛、アンチ
モン、バリウム、ジルコニウム、ルビジウム、ス
トロンチウム等の微量金属が含有されている。
また、本発明では上記自然残留磁化を有する鉱
物は、上記粉末形態で利用される他、適宜焼成等
を行なつて任意の形状に加工した焼結体の形態で
用いることができ、かかる焼成等によつても上記
特定の自然残留磁化強度は損われることなく、従
つて、これに基づく本発明所期の効果を奏し得
る。
本発明方法の好ましい一つの実施態様によれ
ば、上記自然残留磁化を有する鉱物は、これを適
当な容器に充填され、水中に曝気される空気の配
管経路内に設置され、該配管内で空気と接触され
実用される。この際容器への充填の容易性も考慮
すれば、上記鉱物は例えば球状セラミツク等の形
態とするのが好ましく、かかる形態は粉末形態よ
りも優れた磁化活性化効果を奏し得る利点があ
る。また上記容器への充填は、該容器中に被処理
空気を通過させることを考慮すれば、該空気の流
動性、圧力損失等の面より、適度に疎な状態とす
るのが望ましい。通常、その充填率(体積比)は
約5〜30%程度とするのがよい。
また、上記鉱物と空気との接触条件は、特に制
限されるものではないが、通常上記配管経路内に
設置された自然残留磁化を有する鉱物の充填容器
中に、空気を約0.5m/秒以上、好ましくは約0.5
〜5.0m/秒の速度で通過させるものとするのが
よい。
本発明の他の実施態様によれば、上記自然残留
磁化を有する鉱物は、その粉末を常法に従い適当
な基材に塗布、焼成等を行なつて上記容器や送気
管(パイプ)等を作成し、之等を、水中に曝気さ
れる空気の配管等として利用することもでき、更
には空気を曝気させる水槽中に浸漬等により配置
しておくこともできる。かかる態様による本発明
方法の実施の際の条件も上記と同様のものとする
ことができる。
また、本発明方法は上記自然残留磁化を有する
鉱物と接触させる手段と共に、磁界を作用させる
手段を併用することができ、これによれば一層優
れた水中溶存酸素の豊富化、安定化をはかること
ができる。
この磁界の作用は、永久磁石を用いるか又は電
磁石を用いることにより実施できる。かかる磁界
を作用させる手段を採用した本発明の好ましい実
施態様によれば、水中に曝気される空気の配管の
外部に、上記永久磁石又は電磁石を設置して、管
内を流れる空気に磁界を作用させて、該空気を励
起させる。ここで用いられる磁石の形状、寸法等
は何ら限定されるものではなく、中板型、ドーナ
ツ型、直方体型等の任意のものでよいが、残留磁
束密度が約800ガウス以上、好ましくは約1000〜
4000ガウスの範囲となる磁界強度を有するもので
あるのがよい。該残留磁束密度が約800ガウス未
満では、その利用の効果は殆んど認められず、ま
た約4000ガウスを越えると、微生物等の水棲生物
に対する抑制効果等が認められることとなり、処
理水の用途に制限を受けることとなり、いずれも
好ましくない。
本発明方法の実施に好ましい被処理水は、特に
限定されるものではなく、通常の水道水、地下水
等の各種の家庭用、工業用、養魚用水等でよく、
本発明は、かかる水及び空気が約6〜45℃の条件
で容易に実施でき、所期の効果を奏し得る。
以下、本発明方法の好ましい一つの実施態様を
添附図面を用いて説明する。
第1図は本発明方法の実施に当たり、特に好ま
しい一つの装置の概略断面図を示すものである。
該図に示された装置を利用した本発明方法は、空
気圧縮機1と水槽2とを、例えば硬質塩化ビニル
製の連結管3で連結し、水槽2の底部に固定した
散水管4より、磁化した空気の水中に噴出させて
曝気し、水中溶存酸素の富化を行ない得る。上記
空気圧縮機1としては、例えば株式会社萩原製作
所製造OGA−15(風量17/m)を利用すること
ができ、水槽2としては60×30×高さ30cm(50
)のものを、また連結管3としては内径13mmの
ものを利用しているが、特にこれらに限定される
ものではない。
上記連結管3中を流れる空気の磁化は、該管3
に接続され、磁界を発生させる磁石を固定した空
気通気管5及び自然残留磁化を有する鉱物を充填
した容器6によりなされる。上記空気通気管5の
具体的一例は第2図及び第3図に示されており、
容器6の具体例は第4図に示されている。また、
上記連結管3中を流れる空気量の調節は、該管3
に設置されたコツク7及びコツク8によりな
される。また水槽2中の溶存酸素量の測定は、該
水槽2内に設置されたセンサー9及びこれに接続
された溶存酸素測定器10を用いて行なわれる。
その測定点として後記実施例では第1図に示す以
下の4点(P1〜P4)を選択している。
P1…水槽底部より35mm、右短側壁より100mm離れ
た長側壁中央部
P2…水槽底部より35mm、左短側壁より100mm離れ
た長側壁中央部
P3…水槽底部より200mm、左短側壁より100mm離
れた長側壁中央部
P4…水槽底部より200mm、右短側壁より100離れ
た長側壁中央部
第2図(斜視図)及び第3図(中央断面図)に
示す空気通気管5につき詳述すれば、これは永久
磁石(直方体)5aの2枚を管(管径:0.5mm)
5bの外部に、磁石間隔3〜5mmとなるように配
置したものであるが、磁石は永久磁石である必要
はなく、電磁石であつてもよく、その形状も直方
体に限定されるものではない。上記磁石を固定さ
れる管5bの材質は金属、合成樹脂、陶磁器等の
いかなるものであつてもよく、またその断面形状
は、図示されるように扁平状四角形であるのが管
内を通過する空気の磁化強さを均一にでき好まし
いが、他の任意の形状、例えば円形、楕円形、三
角形、四角形、多角形等であつてもよい。上記空
気通気管の肉厚は、管路抵抗を少なくするためで
きるだけ薄い方が好ましい。また、磁化効果を得
るために、磁石を固定した先端より通気方向に10
cm以上の間隔をおいて、管の絞り込みを行なうこ
とによつて、空気及び酸素の分子会合が乱されず
になされて良好な結晶を得られることが経験的に
見出されている。
第4図に示された鉱物充填容器6につき詳述す
れば、これは硬質塩化ビニル製連結管3にフラン
ジ6aを用いて連結されており、該容器6の材質
は金属、合成樹脂、陶磁器等のいかなるものであ
つてもよい。また該容器内には粒状セラミツク形
態の自然残留磁化を有する鉱物6bが充填されて
いる。該鉱物については前述した通りであり、そ
の形状、大きさ、充填量等は後記実施例に詳述す
る。また上記鉱物6bのフランジ6aに接する部
分には、該鉱物の流出を防止するために金網6c
が設置されている。金網はまた鉱物の充填を疎と
するため、容器6内に空気の流れと平行に介在さ
せることもできる。
かくして本発明方法によれば、簡単に、効率よ
く水中溶存酸素量を急速に向上させることがで
き、しかも向上された溶存酸素状態を長期間保持
させることができる。また本発明に利用できる装
置は配管経路の任意の位置に上記磁石を利用した
空気通気管5と鉱物充填容器6とを設置するだけ
の非常に簡単な構造のものとすることができ、こ
れにより、該配管を通過する空気を磁化、活性化
し、水中での溶存酸素濃度を顕著に向上できるも
のであり、かくして処理された水は、殊に水棲生
物への酸素供給に好適である。更に本発明方法で
は、上記以外に何らのエネルギーを要することな
く、しかも処理時間も短く、その利用は省エネル
ギー面からも有効なものである。
実施例
以下、本発明を更に詳しく説明するため、実施
例を挙げる。
実施例 1
第1図に示す装置(詳細は次に示す)を用い
て、以下の条件下に空気圧縮機1より空気を連結
管3中に流し、これを空気通気管5及び鉱物充填
容器6にて磁化させ、水槽2の水中に曝気させ、
水中溶存酸素の富化を行ない、その測定を溶存酸
素測定器(セントラル科学株式会社製、UC−11
型)を用いて実施した。なお、上記測定は散水管
から放出される気泡が直接センサー9に当たらな
いようにして行なつた。また水温の調節は、日本
水槽工業株式会社製α−オートヒーター(150W)
を用いて行ない、供給空気の風速、風量は、コツ
ク7及びコツク8を用いて調節し、ピトー管
及び風量計を用いて測定した。
<使用装置>
空気通気管5
下記第2表に示す4種の残留磁束密度を有す
る異方性フエライト磁石(いずれもTDK株式
会社製)の各2枚を、磁石間隔3mmで、長手方
向に平行に、上下を異極対面にて挟んで使用し
た。[Table] In addition to the above-mentioned components, the minerals (clays and ores) exemplified above also contain trace metals such as titanium, manganese, copper, lead, antimony, barium, zirconium, rubidium, and strontium. In addition, in the present invention, the mineral having natural residual magnetization can be used in the powder form as described above, or in the form of a sintered body processed into an arbitrary shape by appropriately firing, etc. The above-mentioned specific natural residual magnetization strength is not impaired even when the magnetic field is turned on, and therefore, the desired effect of the present invention based on this can be achieved. According to a preferred embodiment of the method of the present invention, the above-mentioned mineral having natural residual magnetization is filled in a suitable container and placed in a piping route for air to be aerated into the water, and the mineral having natural residual magnetization is It is brought into contact with and put into practical use. In this case, considering the ease of filling the mineral into a container, it is preferable that the mineral be in the form of, for example, spherical ceramic, and such a form has the advantage that it can exhibit a better magnetization activation effect than a powder form. Furthermore, in consideration of passing the air to be treated through the container, it is desirable to fill the container in an appropriately sparse state in view of fluidity of the air, pressure loss, etc. Usually, the filling rate (volume ratio) is preferably about 5 to 30%. The contact conditions between the mineral and air are not particularly limited, but usually air is introduced at a rate of about 0.5 m/sec or more into a container filled with a mineral with natural residual magnetization installed in the piping route. , preferably about 0.5
It is preferable to allow the passage to pass at a speed of ~5.0 m/sec. According to another embodiment of the present invention, the above-mentioned mineral having natural residual magnetization is used to create the above-mentioned containers, air pipes, etc. by coating the powder on a suitable base material according to a conventional method and firing the powder. However, these can also be used as piping for air to be aerated into water, and furthermore, they can be placed by immersion in a water tank for aerating air. The conditions for carrying out the method of the present invention according to this embodiment can also be the same as those described above. Furthermore, in the method of the present invention, a means for applying a magnetic field can be used in combination with the above-mentioned means for contacting with minerals having natural residual magnetization, thereby achieving even better enrichment and stabilization of dissolved oxygen in water. Can be done. This magnetic field action can be carried out using permanent magnets or by using electromagnets. According to a preferred embodiment of the present invention that employs means for applying such a magnetic field, the above-mentioned permanent magnet or electromagnet is installed outside a pipe for air that is aerated into water, and a magnetic field is applied to the air flowing inside the pipe. to excite the air. The shape and dimensions of the magnet used here are not limited in any way, and may be any shape such as a medium plate shape, donut shape, rectangular parallelepiped shape, etc., but the residual magnetic flux density is about 800 Gauss or more, preferably about 1000 Gauss or more. ~
It is preferable to have a magnetic field strength in the range of 4000 Gauss. If the residual magnetic flux density is less than about 800 Gauss, there is almost no effect of its use, and if it exceeds about 4000 Gauss, it will have a suppressive effect on aquatic organisms such as microorganisms, and the use of treated water will be limited. Both of these are undesirable. The water to be treated that is preferable for carrying out the method of the present invention is not particularly limited, and may be any type of water for household use, industry, fish farming, etc., such as ordinary tap water or underground water.
The present invention can be easily carried out under conditions where the water and air are about 6 to 45°C, and the desired effects can be achieved. Hereinafter, one preferred embodiment of the method of the present invention will be described using the accompanying drawings. FIG. 1 shows a schematic cross-sectional view of one particularly preferred apparatus for carrying out the method of the present invention.
The method of the present invention using the apparatus shown in the figure connects an air compressor 1 and a water tank 2 with a connecting pipe 3 made of, for example, hard vinyl chloride, and connects an air compressor 1 and a water tank 2 with a connecting pipe 3 made of, for example, hard vinyl chloride. Magnetized air can be ejected into the water to aerate it and enrich dissolved oxygen in the water. As the air compressor 1, for example, OGA-15 manufactured by Hagiwara Seisakusho Co., Ltd. (air volume 17/m) can be used, and as the water tank 2, 60 x 30 x height 30 cm (50 cm) can be used.
), and as the connecting pipe 3, one with an inner diameter of 13 mm is used, but it is not particularly limited to these. The magnetization of the air flowing through the connecting pipe 3
This is accomplished by an air ventilation pipe 5 connected to a magnet and fixed with a magnet for generating a magnetic field, and a container 6 filled with minerals having natural residual magnetization. A specific example of the air ventilation pipe 5 is shown in FIGS. 2 and 3,
A specific example of the container 6 is shown in FIG. Also,
The amount of air flowing through the connecting pipe 3 can be adjusted by
This is done by Kotoku 7 and Kotoku 8 installed at Further, the amount of dissolved oxygen in the water tank 2 is measured using a sensor 9 installed in the water tank 2 and a dissolved oxygen measuring device 10 connected thereto.
In the example described later, the following four points (P1 to P4) shown in FIG. 1 are selected as the measurement points. P1...Central part of the long side wall 35mm from the bottom of the aquarium and 100mm from the short right wall P2...Central part of the long side wall 35mm from the bottom of the tank and 100mm from the short left wall P3...200mm from the bottom of the tank and 100mm from the short left wall Long side wall central part P4...Long side wall central part 200 mm from the bottom of the aquarium and 100 mm away from the right short side wall The air ventilation pipe 5 shown in Fig. 2 (perspective view) and Fig. 3 (center sectional view) will be described in detail. This is a tube (tube diameter: 0.5 mm) made of two permanent magnets (rectangular parallelepiped) 5a.
5b, the magnets are arranged at a spacing of 3 to 5 mm, but the magnets do not have to be permanent magnets and may be electromagnets, and their shape is not limited to a rectangular parallelepiped. The material of the tube 5b to which the magnet is fixed may be any material such as metal, synthetic resin, ceramics, etc., and its cross-sectional shape is a flat rectangle as shown in the figure. Although it is preferable because it can make the magnetization strength uniform, it may have any other shape, such as a circle, an ellipse, a triangle, a square, or a polygon. The wall thickness of the air ventilation pipe is preferably as thin as possible in order to reduce pipe resistance. In addition, in order to obtain a magnetization effect, we placed a
It has been empirically found that by narrowing the tubes at intervals of cm or more, the molecular association of air and oxygen is not disturbed and good crystals can be obtained. In detail, the mineral filling container 6 shown in FIG. 4 is connected to a hard vinyl chloride connecting pipe 3 using a flange 6a, and the container 6 is made of metal, synthetic resin, ceramics, etc. It can be any of the following. The container is also filled with a mineral 6b having natural residual magnetization in the form of granular ceramic. The mineral is as described above, and its shape, size, filling amount, etc. will be described in detail in Examples below. In addition, a wire mesh 6c is placed on the portion of the mineral 6b in contact with the flange 6a to prevent the mineral from flowing out.
is installed. A wire mesh can also be interposed in the container 6 parallel to the air flow to make the mineral filling loose. Thus, according to the method of the present invention, the amount of dissolved oxygen in water can be rapidly increased easily and efficiently, and the improved dissolved oxygen state can be maintained for a long period of time. Furthermore, the device that can be used in the present invention can have a very simple structure in which the air ventilation pipe 5 using the magnet and the mineral filling container 6 are installed at any position on the piping route. It magnetizes and activates the air passing through the piping, and can significantly improve the dissolved oxygen concentration in water, and the water treated in this way is particularly suitable for supplying oxygen to aquatic organisms. Furthermore, the method of the present invention does not require any energy other than the above, and the processing time is short, so its use is effective from an energy saving perspective. Examples Examples will be given below to explain the present invention in more detail. Example 1 Using the apparatus shown in FIG. 1 (details are shown below), air was flowed from the air compressor 1 into the connecting pipe 3 under the following conditions, and the air was passed through the air ventilation pipe 5 and the mineral filling container 6. to magnetize it and aerate it into the water in tank 2,
We enrich dissolved oxygen in water and measure it using a dissolved oxygen measuring device (manufactured by Central Kagaku Co., Ltd., UC-11).
It was carried out using a mold). Note that the above measurements were carried out in such a way that the bubbles released from the water sprinkler tube did not directly hit the sensor 9. In addition, the water temperature can be adjusted using an α-auto heater (150W) manufactured by Nippon Suisan Kogyo Co., Ltd.
The wind speed and air volume of the supplied air were adjusted using Kotoku 7 and Kotoku 8, and measured using a pitot tube and an airflow meter. <Equipment used> Air ventilation pipe 5 Two anisotropic ferrite magnets (both manufactured by TDK Corporation) having the four types of residual magnetic flux densities shown in Table 2 below were placed parallel to each other in the longitudinal direction with a magnet spacing of 3 mm. It was used by sandwiching the top and bottom with opposite polarity surfaces.
【表】
鉱物充填容器6
前記第1表に示す自然残留磁化を有する鉱物
の破砕物(平均粒度5mm)500gを充填率30%
となるように充填して使用した。
<実施条件>
通気速度:
0.5、1.0、1.5、2.0及び5.0m/秒のそれぞれ
につき、同一試験を繰返した。
空気温度及び水温:
いずれも17℃とした。
<結果>
上記試験開始(送気開始)より5分後の水中の
溶存酸素量(mgO/:P1〜P4の4点での測定
値の平均値)を測定した結果を下記第3表に示
す。
また、第3表には、上記において空気通気管5
を使用せず、鉱物充填容器6のみを用いて、空気
を磁化活性化した場合の本発明実施例に従い得ら
れた結果を併記する。
更に、第3表には、対照として上記空気通気管
5及び鉱物充填容器6を使用することなく、水中
への曝気のみを行なつた場合、並びに比較のため
鉱物充填容器6を用いることなく磁石のみを用い
た場合の各結果をも併記する。[Table] Mineral Filling Container 6 500 g of crushed minerals (average particle size 5 mm) having natural residual magnetization shown in Table 1 above were packed at a filling rate of 30%.
It was filled and used. <Implementation Conditions> The same test was repeated at ventilation speeds of 0.5, 1.0, 1.5, 2.0, and 5.0 m/sec. Air temperature and water temperature: Both were 17°C. <Results> Table 3 below shows the results of measuring the amount of dissolved oxygen in the water (mgO/: average value of the measured values at 4 points P1 to P4) 5 minutes after the start of the above test (start of air supply). . Table 3 also shows the air vent pipe 5 in the above.
The results obtained according to the embodiment of the present invention in the case where the air was magnetized and activated using only the mineral-filled container 6 without using the mineral-filled container 6 are also described. Furthermore, Table 3 shows a case where only aeration into water was performed without using the air vent pipe 5 and mineral filling container 6 as a control, and a case where a magnet was used without using the mineral filling container 6 for comparison. The results obtained when using only the same method are also shown.
【表】【table】
【表】
上記第3表より、以下のことが伴る。
(1) 磁石の形状・寸法は溶存酸素量の増加には関
与しない。
(2) 曝気のみではその水温における飽和溶解酸素
量を上回ることはない。
(3) 自然残留磁化を有する鉱物を利用した本発明
方法の実施によれば、曝気のみに比し、ほぼ11
〜18%の溶存酸素量の増加が認められる。
(4) 自然残留磁化を有する鉱物の利用と800〜
4000ガウスの残留磁束密度を有する磁石の利用
とを組合せた本発明方法の実施によれば、曝気
のみに比し、実に20%以上の溶存酸素量の増加
が認められる。
(5) 磁石の単独利用でも、曝気のみに比して溶存
酸素量の増加は認められる場合があるが、その
程度は4000ガウスの残留磁束密度を有する磁石
を利用した最大の場合でも約8%程度である。
(6) 供給空気速度は0.5m/秒以上で、本発明方
法により充分な溶存酸素量の増加が認められ
る。
実施例 2
実施例1において、以下の装置及び実施条件を
組合せ利用し、同様にして本発明方法を実施し
た。
<使用装置>
空気通気管5
残留磁束密度4000ガウスを有する異方性フエ
ライト磁石(直方体型、45mm×20mm×8mm径、
TDK株式会社製)の各2枚を、磁石間隔4mm
で、長手方向に平行に、上下を異極対面にて挟
んで使用した。
鉱物充填容器6
前記第1表に示す自然残留磁化を有する鉱物
の焼成品(径5mm球状体)500gを充填率30%
となるように充填して使用した。
<実施条件>
通気速度:1.5m/秒
空気温度:20℃(室内温度調節)
水温:20℃
送気量:15/分
<結果>
上記試験に従い、送気開始より経時的に水中の
溶存酸素量(mgO/)を測定した。
また送気開始より13分後に送気を停止させ、以
後水槽中の水を静置し、この静置水につき、同様
にして経時的に溶存酸素量を測定し、該溶存酸素
量の安定性を調べた。
結果を第5図に曲線1として示す。該図におい
て、横軸は送気開始後時間(分)を、縦軸は溶存
酸素量(mg/)を示す。
第5図には、上記において空気通気管5を使用
せず、鉱物充填容器6のみを用いた本発明実施例
に従う結果[曲線2として示す]、鉱物充填容器
6を用いることなく磁石のみを用いた比較例の結
果[曲線3として示す]、並びに上記空気通気管
5及び鉱物充填容器6のいずれも使用することな
く、水中への曝気のみを行なつた対照例の結果
[曲線4として示す]を併記する。
上記第5図より、本発明方法の実施によれば、
曲線1及び2に示される通り、非常に短時間で、
水中溶存酸素が活性化され、水温における飽和溶
解酸素濃度を顕著に上回る水中溶存酸素濃度が得
られ、しかもこの向上された水中溶存酸素濃度
は、曝気を停止した後も非常に長時間に亘つて持
続され、上記活性化の安定性が高いことが明らか
である。殊にこの効果は空気通気管5と鉱物充填
容器6との組合せ利用の場合に顕著である。
これに対し、磁石のみの使用によれば、曲線3
として示されるように、水中溶存酸素の活性化及
びこれによる水中溶存酸素濃度の向上効果は、な
お不充分であるのみならず、曝気停止後の上記濃
度の低下が比較的速やかであり、その安定性も本
発明に比しなお向上され難いことが判る。
実施例 3
実施例1において、以下の装置及び実施条件を
組合せ利用し、同様にして本発明方法を実施し
た。
<使用装置>
空気通気管5
残留磁束密度4000ガウスを有する異方性フエ
ライト磁石(直方体型、45mm×20mm×8mm径、
TDK株式会社製)の各2枚を、磁石間隔4mm
で、長手方向に平行に、上下を異極対面にて挟
んで使用した。
鉱物充填容器6
前記第1表に示す自然残留磁化を有する鉱物
の焼成品(径10mm球状体)500gを充填率30%
となるように充填して使用した。
<実施条件>
通気速度:1.5m/秒
空気温度:20℃(室内温度調節)
水温:6〜50℃
送気量:15/分
<結果>
上記試験に従い、送気開始より5分後の、所定
水温下における水中の溶存酸素(mgO/)を測
定し、その平均値を、該水温下における飽和溶解
酸素濃度で除した値の百分率(%)を算出した。
結果を第6図に曲線1として示す。図において
横軸は水温(℃)を、縦軸は(溶存酸素量測定
体/飽和酸素値)×100(%)をそれぞれ示す。
第6図には、上記において空気通気管5を使用
せず、鉱物充填容器6のみを用いた本発明実施例
に従う結果[曲線2として示す]、鉱物充填容器
6を用いることなく磁石のみを用いた比較例の結
果[曲線3として示す]、並びに上記空気通気管
5及び鉱物充填容器6のいずれも使用することな
く、水中への曝気のみを行なつた対照例の結果
[曲線4として示す]を併記する。
更に第6図には、鉱物充填容器6を第1図に示
す連結管3の水槽内の水中に浸漬した装置を用い
て、同一試験を繰返した結果を曲線5として併記
する。
上記第6図より、本発明方法の実施によれば、
曲線1,2及び5として示される通り、広範な水
温範囲で、水中溶存酸素の活性化、富化が行ない
得、殊にこの効果は、空気通気管5と鉱物充填容
器6との組合せ利用の場合に顕著であることが明
らかである。[Table] From Table 3 above, the following follows. (1) The shape and dimensions of the magnet do not affect the increase in the amount of dissolved oxygen. (2) Aeration alone will not exceed the saturated dissolved oxygen content at that water temperature. (3) According to the implementation of the method of the present invention using minerals with natural residual magnetization, compared to only aeration, the
An increase in dissolved oxygen content of ~18% is observed. (4) Utilization of minerals with natural residual magnetization and 800~
By implementing the method of the present invention in combination with the use of a magnet having a residual magnetic flux density of 4000 Gauss, an increase in the amount of dissolved oxygen of more than 20% is observed compared to aeration alone. (5) Even when a magnet is used alone, an increase in the amount of dissolved oxygen may be observed compared to aeration alone, but the degree of increase is approximately 8% even in the maximum case using a magnet with a residual magnetic flux density of 4000 Gauss. That's about it. (6) When the supplied air velocity is 0.5 m/sec or more, a sufficient increase in the amount of dissolved oxygen is observed by the method of the present invention. Example 2 The method of the present invention was carried out in the same manner as in Example 1 using a combination of the following apparatus and conditions. <Equipment used> Air ventilation pipe 5 Anisotropic ferrite magnet with a residual magnetic flux density of 4000 Gauss (cuboid shape, 45 mm x 20 mm x 8 mm diameter,
(manufactured by TDK Corporation), with a magnet spacing of 4 mm.
It was used by sandwiching the upper and lower sides with opposite polarity surfaces parallel to the longitudinal direction. Mineral Filling Container 6 500 g of fired minerals (5 mm diameter spherical bodies) having the natural residual magnetization shown in Table 1 above were filled at a filling rate of 30%.
It was filled and used. <Implementation conditions> Ventilation speed: 1.5 m/sec Air temperature: 20°C (indoor temperature control) Water temperature: 20°C Air supply rate: 15/min <Results> According to the above test, dissolved oxygen in water increased over time from the start of air supply. The amount (mgO/) was measured. In addition, the air supply was stopped 13 minutes after the start of air supply, and the water in the aquarium was then allowed to stand still.The amount of dissolved oxygen in this still water was measured over time in the same manner, and the stability of the amount of dissolved oxygen was determined. I looked into it. The results are shown as curve 1 in FIG. In this figure, the horizontal axis shows the time (minutes) after the start of air supply, and the vertical axis shows the amount of dissolved oxygen (mg/). FIG. 5 shows the result according to the embodiment of the present invention in which the air ventilation pipe 5 was not used in the above and only the mineral-filled container 6 was used [shown as curve 2], and the result in which only the magnet was used without using the mineral-filled container 6. The results of a comparative example [shown as curve 3], and the results of a control example in which only aeration into the water was performed without using either the air vent pipe 5 or the mineral filling container 6 [shown as curve 4] Also listed. From FIG. 5 above, according to the implementation of the method of the present invention,
As shown in curves 1 and 2, in a very short time,
Dissolved oxygen in the water is activated, and a dissolved oxygen concentration in the water that significantly exceeds the saturated dissolved oxygen concentration at the water temperature is obtained, and this improved dissolved oxygen concentration in the water remains for a very long time even after the aeration is stopped. It is clear that the activation is sustained and the stability of the activation is high. This effect is particularly noticeable when the air vent pipe 5 and the mineral filling container 6 are used in combination. On the other hand, if only magnets are used, curve 3
As shown in Figure 1, the activation of dissolved oxygen in water and the effect of improving the dissolved oxygen concentration in water are not only insufficient, but also that the concentration decreases relatively quickly after the aeration is stopped, and its stability is poor. It can be seen that the properties are also difficult to improve compared to the present invention. Example 3 The method of the present invention was carried out in the same manner as in Example 1 using a combination of the following apparatus and conditions. <Equipment used> Air ventilation pipe 5 Anisotropic ferrite magnet with a residual magnetic flux density of 4000 Gauss (cuboid shape, 45 mm x 20 mm x 8 mm diameter,
(manufactured by TDK Corporation), with a magnet spacing of 4 mm.
It was used by sandwiching the upper and lower sides with opposite polarity surfaces parallel to the longitudinal direction. Mineral Filling Container 6 500 g of fired minerals (spherical bodies with a diameter of 10 mm) having the natural residual magnetization shown in Table 1 above are filled at a filling rate of 30%.
It was filled and used. <Implementation conditions> Ventilation speed: 1.5 m/sec Air temperature: 20°C (indoor temperature control) Water temperature: 6 to 50°C Air supply rate: 15/min <Results> According to the above test, 5 minutes after the start of air supply, Dissolved oxygen (mgO/) in water at a predetermined water temperature was measured, and the percentage (%) of the average value divided by the saturated dissolved oxygen concentration at the water temperature was calculated. The results are shown as curve 1 in FIG. In the figure, the horizontal axis represents water temperature (°C), and the vertical axis represents (dissolved oxygen amount measurement unit/saturated oxygen value)×100 (%). FIG. 6 shows the result according to the embodiment of the present invention in which the air vent pipe 5 was not used in the above and only the mineral-filled container 6 was used [shown as curve 2], and the result in which only the magnet was used without using the mineral-filled container 6. The results of a comparative example [shown as curve 3], and the results of a control example in which only aeration into the water was performed without using either the air vent pipe 5 or the mineral filling container 6 [shown as curve 4] Also listed. Further, in FIG. 6, the results of repeating the same test using an apparatus in which the mineral-filled container 6 was immersed in water in the water tank of the connecting pipe 3 shown in FIG. 1 are also shown as a curve 5. From FIG. 6 above, according to the implementation of the method of the present invention,
As shown by curves 1, 2 and 5, the activation and enrichment of dissolved oxygen in water can be achieved over a wide range of water temperatures, and this effect is especially evident when using the combination of air vent pipe 5 and mineral-filled container 6. It is clear that this is noticeable in some cases.
第1図は本発明方法の実施に当たり、特に好ま
しい一つの装置の概略断面図を示す。第2図及び
第3図はそれぞれ第1図に示す装置に利用される
磁石を用いた空気通気管5の斜視図及び中央断面
図を示す。第4図は、第1図に示す装置に利用さ
れる鉱物充填容器6の縦断面図である。第5図は
本発明実施例2に従う方法の実施による水中溶存
酸素量の経時変化を示すグラフである。第6図は
本発明実施例3に従う方法の実施による水温と水
中溶存酸素量との関連を調べたグラフである。
FIG. 1 shows a schematic cross-sectional view of one particularly preferred apparatus for carrying out the method of the present invention. 2 and 3 show a perspective view and a central cross-sectional view, respectively, of a magnetic air vent tube 5 utilized in the apparatus shown in FIG. FIG. 4 is a longitudinal sectional view of the mineral filling container 6 used in the apparatus shown in FIG. FIG. 5 is a graph showing changes over time in the amount of dissolved oxygen in water by implementing the method according to Example 2 of the present invention. FIG. 6 is a graph showing the relationship between water temperature and the amount of oxygen dissolved in water by implementing the method according to Example 3 of the present invention.
Claims (1)
るに当たり、水中に曝気させる空気を、自然残留
磁化を有する鉱物と接触させて磁化活性化するか
又はこれと共に上記空気に磁界を作用させて空気
中の酸素を励起させることを特徴とする水中溶存
酸素の富化方法。 2 自然残留磁化を有する鉱物が10-4〜10-13Tを
有する鉱物の粉砕物又は焼結体である特許請求の
範囲第1項に記載の方法。 3 処理水の温度が6〜45℃である特許請求の範
囲第1項に記載の方法。 4 磁界の作用が永久磁石により行なわれる特許
請求の範囲第1項に記載の方法。 5 磁界の作用が電磁石により行なわれる特許請
求の範囲第1項に記載の方法。 6 磁界の作用が空気を0.5m/秒以上の速度で
1000〜4000ガウスの磁束密度を有する磁場に暴露
させて行なわれる特許請求の範囲第1項に記載の
方法。[Claims] 1. When aerating air into water to enrich dissolved oxygen in water, the air to be aerated into water is brought into contact with minerals having natural residual magnetization to activate magnetization, or together with the above-mentioned minerals. A method for enriching dissolved oxygen in water, characterized by applying a magnetic field to the air to excite oxygen in the air. 2. The method according to claim 1, wherein the mineral having natural residual magnetization is a crushed product or a sintered body of a mineral having 10 -4 to 10 -13 T. 3. The method according to claim 1, wherein the temperature of the treated water is 6 to 45°C. 4. A method according to claim 1, in which the action of the magnetic field is carried out by a permanent magnet. 5. The method according to claim 1, wherein the action of the magnetic field is carried out by an electromagnet. 6 The action of a magnetic field moves air at a speed of 0.5 m/s or more.
A method according to claim 1, which is carried out by exposure to a magnetic field having a magnetic flux density of 1000 to 4000 Gauss.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62134391A JPS63296896A (en) | 1987-05-28 | 1987-05-28 | Method for enriching dissolved oxygen in water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62134391A JPS63296896A (en) | 1987-05-28 | 1987-05-28 | Method for enriching dissolved oxygen in water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63296896A JPS63296896A (en) | 1988-12-02 |
| JPH0239957B2 true JPH0239957B2 (en) | 1990-09-07 |
Family
ID=15127305
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62134391A Granted JPS63296896A (en) | 1987-05-28 | 1987-05-28 | Method for enriching dissolved oxygen in water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63296896A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04114796A (en) * | 1990-09-05 | 1992-04-15 | S K Eng Kk | Wastewater treatment |
| KR20000012682A (en) * | 1999-12-14 | 2000-03-06 | 김경미 | Active air generator |
| JP2002346588A (en) * | 2001-05-23 | 2002-12-03 | Hukko:Kk | Water purification method and purification device |
| EP1749799A1 (en) * | 2005-08-03 | 2007-02-07 | Norbert Stadler | Water treatment apparatus |
-
1987
- 1987-05-28 JP JP62134391A patent/JPS63296896A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63296896A (en) | 1988-12-02 |
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