JPH031076B2 - - Google Patents
Info
- Publication number
- JPH031076B2 JPH031076B2 JP16051986A JP16051986A JPH031076B2 JP H031076 B2 JPH031076 B2 JP H031076B2 JP 16051986 A JP16051986 A JP 16051986A JP 16051986 A JP16051986 A JP 16051986A JP H031076 B2 JPH031076 B2 JP H031076B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- water
- magnetic field
- ion exchange
- raw water
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 64
- 238000005342 ion exchange Methods 0.000 claims description 23
- 238000001914 filtration Methods 0.000 claims description 18
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 15
- 239000000460 chlorine Substances 0.000 claims description 15
- 229910052801 chlorine Inorganic materials 0.000 claims description 15
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 230000004907 flux Effects 0.000 claims description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 35
- 229910052742 iron Inorganic materials 0.000 description 18
- 239000012535 impurity Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 9
- 238000005192 partition Methods 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000008234 soft water Substances 0.000 description 4
- 239000008399 tap water Substances 0.000 description 4
- 235000020679 tap water Nutrition 0.000 description 4
- VNWKTOKETHGBQD-AKLPVKDBSA-N carbane Chemical class [15CH4] VNWKTOKETHGBQD-AKLPVKDBSA-N 0.000 description 3
- 230000005389 magnetism Effects 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 230000027455 binding Effects 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000005415 magnetization Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 230000009149 molecular binding Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Water Treatment By Sorption (AREA)
Description
「技術分野」
本発明は、例えば水道水、ボイラーのリターン
水等、塩素分や鉄分その他の不純物などを多く含
んだ原水を軟水化する活水製造装置に関する。
「従来技術およびその問題点」
いわゆる水道水等の原水には、塩素分、鉄分、
カルシウム分や、その他の不純物が多く含まれて
いる。このような原水は、飲料に供されることは
勿論、工業用にも用いられる。例えば、原水をボ
イラーのリターン水に使用する場合、時間的経過
とともに、ボイラーの供給パイプ内面に水あかと
して付着し、ボイラーの性能の劣化を招くことか
ら、原水を軟水化してから使用している。
この軟水化の方法として、従来では、原水を活
性炭により濾過したり、あるいはイオン交換材に
通すことで行なつている。
しかしながら、原水中にはかなりの割合の鉄分
が含まれており、その他の不純物成分の結合状態
が強固なために、上記従来方法では、鉄分の除
去、他の成分の分解等が充分には行なえず、所望
の軟水を得るには至つていないのが現状である。
「発明の目的」
本発明は、原水中に含まれる鉄分をほぼ完全に
除去し、原水中のその他の不純物成分をも分解し
て軟水化することのできる活水製造装置を提供す
ることを目的とする。
「発明の概要」
上記目的を達成するため、本発明では、原水を
取り入れこの原水中の塩素分を取り除く濾過槽
と、この濾過槽に連通させ該濾過槽からの塩素分
の除かれた水を永久磁石によつて磁化させる磁場
槽と、この磁場槽に連通させ該磁場槽からの磁化
水をイオン交換により軟水化するイオン交換槽と
を備えてなることを特徴とする。
原水は濾過槽で塩素分が除去され、磁場槽へと
送られる。磁場槽では、槽内で強力な磁界が働い
ており、塩素分の除去された水はこの強力な磁界
に接する。この磁界による磁気エネルギーで該水
は磁化され、成分中の鉄分は永久磁石に吸着され
る。また、他の成分は磁気エネルギーによつてそ
の分子結合力がなくなる。そして、このような水
はイオン交換槽に送られ、同槽にてイオン交換さ
れ軟水化される。したがつて、得られた軟水は、
鉄分が含まれておらず、その他の不要成分は除去
されている。
本発明の好ましい態様によれば、磁場槽は複数
槽に分割され、各槽が連通したものが用いられ
る。このように磁場槽を複数にすれば、濾過槽か
らの水は複数槽を順次通過するので、該水の磁化
促進が図られ、成分中の鉄分の吸着も容易とな
る。
本発明のさらに好ましい態様によれば、磁場槽
内の永久磁石は、一方面がＮ極、他方面がＳ極を
呈する多数で構成され、各極面が相互に反発する
関係で配置されている。永久磁石を反発関係で配
列することで、水中の鉄分以外の成分は反発磁場
に接することとなり、その分子が撹乱分散させら
れ、結合力がなくなる。
本発明のさらに別の好ましい態様によれば、永
久磁石の磁束密度は4000G以上となつている。磁
束密度が高ければ、水の磁化効率が向上するの
で、鉄分の吸着力も増し、さらに反発磁場が大き
くなり、上記分子の撹乱分散効果も向上する。
「発明の実施例」
以下に、本発明の一実施例を図面に基いて説明
する。
濾過槽１１は、下部に原水の入口１２を有し、
内部には底部と平行に仕切壁１３，１４が形成さ
れている。仕切壁１３，１４は一部が反対位置で
開放され、濾過槽１１内で蛇行流路を構成してい
る。この仕切壁１３，１４はこの実施例では２枚
配置されているが、３枚以上を互い違いに配置し
てもよいことは勿論である。このような濾過槽１
１中には活性炭１５が充填されている。この活性
炭１５は、原水に含まれる塩素分を取り去る作用
を有する。したがつて、濾過槽１１は、入口１２
から取り入れられた原水が蛇行状に上部に導かれ
る過程で、原水を濾過し、原水中の塩素分を取り
除く。
濾過槽１１は、連結管１６を介して磁場槽２０
と上部で連結されており、この連結管１６により
濾過槽１１と磁場槽２０は連通している。連結管
１６には濾過槽１１側にフイルタ１７が装着され
ている。磁場槽２０は、第１の磁場槽２１と第２
の磁場槽２２が仕切壁２３によつて分割されてな
つており、仕切壁２３の下部の開放部で第１の磁
場槽２１と第２の磁場槽２２が連通している。本
実施例では、磁場槽２０が第１の磁場槽２１と第
２の磁場槽２２に二分割されているが、これは例
示であつて、三分割以上であつてもよいことは勿
論である。第１の磁場槽２１およ第２の磁場槽２
２には、磁気発生装置２４が配置されている。こ
の磁気発生装置２４は、濾過槽１１から流れてく
る塩素分の除かれた水を磁化させ、鉄分を吸着す
るもので、多数の永久磁石２５により構成されて
いる。永久磁石２５は、中央に挿通された銅管２
６によつて保持され、永久磁石２５の各々は銅管
２６に嵌められたスペーサ２７によつて所定間隔
が保たれている。これらの永久磁石２５は、それ
ぞれの極面を相互に反発する関係で、すなわち、
第４図に示すように、（Ｎ、Ｓ）（Ｓ、Ｎ）（Ｎ、
Ｓ）（Ｓ、Ｎ）…の関係で、対向させてある。し
たがつて、各永久磁石２５の対向面からは磁力線
の反発力が生じることになる。この反発力は、水
の不純物成分の構成分子を撹乱分散させる作用を
有する。反発力の強弱は、各永久磁石２５間の間
隔Ｗを調整することによつて行なうことができ
る。この間隔Ｗの調整はスペーサ２７の長さ調整
によつて行なう。このような永久磁石２５の磁束
密度は、強力な反発力を得るためには高い方が良
く、4000G以上のものが好ましい。
上記磁場槽２０は、上部の連結管２８を介して
イオン交換槽３０と連通している。連結管２８の
磁場槽２０側にはフイルタ２９が設けられてい
る。このフイルタ２９は、磁場槽２０からの撹乱
された不純物を濾過するものである。イオン交換
槽３０は、下部に出口３１を有しており、内部に
はイオン交換材３２が充填されている。イオン交
換槽３０は、磁場槽２０からの鉄分が除かれ不純
物成分の分子結合のなくされた水中の分子とイオ
ン交換するものである。イオン交換材３２として
は、例えばスチレン−ビジビニルベンゼン共重合
体からなるダイアイオンSK−1B（商品名、三菱
化成株式会社製造）が用いられる。
上記構成の本発明によると、水あかや不純物を
含んだ原水は、濾過槽１１の入口１２から導入さ
れ、仕切壁１３，１４で構成される蛇行状の流路
を通りながら活性炭１５によりその成分中の塩素
分が除かれ、フイルタ１７で濾過された後、連結
管１６から磁場槽２０に流れ込む。塩素分の除去
された水は、まず第１の磁場槽２１に入り、第１
の磁場槽２１内の磁気発生装置２４による永久磁
石２５の4000G以上の強力な磁界に触れて磁化さ
れ、さらに第２の磁場槽２２に入つて同じく磁気
発生装置２４による磁界に触れて磁化率が高くな
る。この過程で、濾過槽１１からの水の成分中の
鉄分は永久磁石２５で吸着されてなくなり、他の
成分の分子は永久磁石２５による反発磁力によつ
て撹乱され、分子結合力を弱められる。このよう
な磁化水は、磁気エネルギーの影響を受け、活水
自律運動を起こすため、溶存酸素を取り出す。磁
化水が連結管２８を通過する際にフイルタ２９に
よつて濾過され、その後イオン交換槽３０内に入
る。イオン交換槽３０では、イオン交換材３２
が、磁場槽２０からの鉄分および不純物が除か
れ、かつ分子結合の撹乱された水とイオン交換す
る。イオン交換材３２は鉄分に弱いが、この鉄分
は磁場槽２０の永久磁石２５ですでに捕捉され、
成分中には存在しないため、イオン交換運動は活
発に行なわれ、イオン交換材３２の持続性が保証
される。そして、こうしてイオン交換された水
は、出口３１から流出される。
実施例
原水に水道水を用い、この水道水１（水温25
℃）を、従来のイオン交換材と本発明装置に通
し、得られたそれぞれの軟水を分析計量して原水
と比較したところ、第一表のような結果を得た。
この表で明らかなように、従来のイオン交換材
による軟水化と比べ、原水１当り、カルシウム
分0.2mg、マグネシウム分0.05mg、溶存酵素0.6mg
それぞれ減少しており、本発明装置による原水の
軟水化度が高まつたことが分かる。
TECHNICAL FIELD The present invention relates to an activated water production device for softening raw water containing a large amount of chlorine, iron, and other impurities, such as tap water or return water from a boiler. "Prior art and its problems" Raw water such as so-called tap water contains chlorine, iron,
It contains a lot of calcium and other impurities. Such raw water is of course used for drinking purposes, but also for industrial purposes. For example, when raw water is used as return water for a boiler, water scales can accumulate on the inner surface of the boiler's supply pipe over time, degrading the boiler's performance, so the raw water must be softened before use. Conventionally, water softening has been carried out by filtering raw water through activated carbon or passing it through an ion exchange material. However, since raw water contains a considerable proportion of iron and other impurity components are strongly bound, the above conventional methods cannot sufficiently remove iron and decompose other components. However, at present, it has not been possible to obtain the desired soft water. ``Object of the Invention'' The purpose of the present invention is to provide an activated water production device that can almost completely remove iron contained in raw water and decompose other impurity components in raw water to soften the water. do. "Summary of the Invention" In order to achieve the above object, the present invention includes a filtration tank that takes in raw water and removes chlorine from the raw water, and a filtration tank that communicates with the filtration tank to remove the chlorine from the filtration tank. It is characterized by comprising a magnetic field tank that is magnetized by a permanent magnet, and an ion exchange tank that is communicated with the magnetic field tank and softens the magnetized water from the magnetic field tank by ion exchange. The raw water is filtered to remove chlorine and sent to the magnetic field tank. In a magnetic tank, a strong magnetic field operates inside the tank, and the water from which chlorine has been removed comes into contact with this strong magnetic field. The water is magnetized by the magnetic energy generated by this magnetic field, and the iron component in the water is attracted to the permanent magnet. In addition, other components lose their molecular binding strength due to magnetic energy. Then, such water is sent to an ion exchange tank, where it is ion-exchanged and softened. Therefore, the obtained soft water is
It does not contain iron and other unnecessary components have been removed. According to a preferred embodiment of the present invention, the magnetic field tank is divided into a plurality of tanks, each of which communicates with each other. By providing a plurality of magnetic fields in this way, the water from the filtration tank passes through the plurality of tanks in sequence, which promotes magnetization of the water and facilitates adsorption of iron in the components. According to a further preferred embodiment of the present invention, the permanent magnets in the magnetic field tank are composed of a large number of permanent magnets each having a north pole on one side and a south pole on the other side, and are arranged in such a manner that the respective pole faces repel each other. . By arranging permanent magnets in a repulsive relationship, components other than iron in the water come into contact with the repulsive magnetic field, causing their molecules to be disturbed and dispersed, and their binding force is eliminated. According to yet another preferred embodiment of the present invention, the magnetic flux density of the permanent magnet is 4000G or more. If the magnetic flux density is high, the magnetization efficiency of water is improved, so the adsorption power for iron is also increased, and the repulsion magnetic field is also increased, which improves the effect of disturbing and dispersing the molecules. "Embodiment of the Invention" An embodiment of the present invention will be described below with reference to the drawings. The filtration tank 11 has a raw water inlet 12 at the bottom,
Partition walls 13 and 14 are formed inside parallel to the bottom. Parts of the partition walls 13 and 14 are open at opposite positions, forming a meandering flow path within the filtration tank 11. Although two partition walls 13 and 14 are arranged in this embodiment, it goes without saying that three or more partition walls 13 and 14 may be arranged alternately. Such a filter tank 1
1 is filled with activated carbon 15. This activated carbon 15 has the effect of removing chlorine contained in raw water. Therefore, the filtration tank 11 has an inlet 12
During the process in which the raw water taken in is led to the top in a meandering manner, the raw water is filtered and the chlorine content in the raw water is removed. The filtration tank 11 is connected to a magnetic field tank 20 via a connecting pipe 16.
The filtration tank 11 and the magnetic field tank 20 communicate with each other through the connecting pipe 16. A filter 17 is attached to the connecting pipe 16 on the filtration tank 11 side. The magnetic field tank 20 has a first magnetic field tank 21 and a second magnetic field tank 21.
The magnetic field tank 22 is divided by a partition wall 23, and the first magnetic field tank 21 and the second magnetic field tank 22 communicate with each other through an open portion at the bottom of the partition wall 23. In this embodiment, the magnetic field tank 20 is divided into two parts, a first magnetic field tank 21 and a second magnetic field tank 22, but this is just an example, and it goes without saying that it may be divided into three or more parts. . First magnetic field tank 21 and second magnetic field tank 2
2, a magnetism generating device 24 is arranged. This magnetism generating device 24 magnetizes the water from which chlorine is removed, which flows from the filter tank 11, and adsorbs iron, and is composed of a large number of permanent magnets 25. The permanent magnet 25 is a copper tube 2 inserted through the center.
6, and each of the permanent magnets 25 is maintained at a predetermined distance by a spacer 27 fitted into a copper tube 26. These permanent magnets 25 are arranged in such a manner that their respective pole faces repel each other, that is,
As shown in Figure 4, (N, S) (S, N) (N,
S) (S, N)... are placed facing each other. Therefore, a repulsive force of magnetic lines of force is generated from the facing surfaces of each permanent magnet 25. This repulsive force has the effect of disturbing and dispersing the constituent molecules of the impurity components of water. The strength of the repulsive force can be adjusted by adjusting the distance W between the permanent magnets 25. This distance W is adjusted by adjusting the length of the spacer 27. The higher the magnetic flux density of the permanent magnet 25, the better, in order to obtain a strong repulsive force, and preferably 4000G or more. The magnetic field tank 20 communicates with an ion exchange tank 30 via an upper connecting pipe 28. A filter 29 is provided on the magnetic field tank 20 side of the connecting pipe 28 . This filter 29 filters out disturbed impurities from the magnetic field tank 20. The ion exchange tank 30 has an outlet 31 at the bottom, and the inside thereof is filled with an ion exchange material 32. The ion exchange tank 30 performs ion exchange with molecules in water from which iron from the magnetic field tank 20 has been removed and molecular bonds of impurity components have been eliminated. As the ion exchange material 32, Diaion SK-1B (trade name, manufactured by Mitsubishi Kasei Corporation), which is made of a styrene-bidivinylbenzene copolymer, is used, for example. According to the present invention having the above configuration, raw water containing limescale and impurities is introduced from the inlet 12 of the filtration tank 11, and as it passes through the meandering flow path constituted by the partition walls 13 and 14, the activated carbon 15 removes its components. After removing the chlorine content and filtering through the filter 17, the water flows into the magnetic field tank 20 from the connecting pipe 16. The water from which chlorine content has been removed first enters the first magnetic field tank 21, and then enters the first magnetic field tank 21.
It is magnetized by contact with the strong magnetic field of 4000 G or more of the permanent magnet 25 generated by the magnetic generator 24 in the magnetic field tank 21, and further enters the second magnetic field tank 22 and is exposed to the magnetic field generated by the magnetic generator 24, so that the magnetic susceptibility decreases. It gets expensive. In this process, the iron in the water components from the filter tank 11 is absorbed by the permanent magnet 25 and disappears, and the molecules of other components are disturbed by the repulsive magnetic force of the permanent magnet 25, weakening the molecular bonding force. Such magnetized water is affected by magnetic energy and causes autonomous movement of active water, which extracts dissolved oxygen. When the magnetized water passes through the connecting pipe 28, it is filtered by the filter 29, and then enters the ion exchange tank 30. In the ion exchange tank 30, the ion exchange material 32
is ion-exchanged with water from which iron and impurities have been removed from the magnetic field tank 20 and whose molecular bonds have been disturbed. The ion exchange material 32 is sensitive to iron, but this iron has already been captured by the permanent magnet 25 of the magnetic field tank 20.
Since it is not present in the components, ion exchange movement takes place actively, ensuring the sustainability of the ion exchange material 32. The ion-exchanged water is then discharged from the outlet 31. Example Using tap water as raw water, this tap water 1 (water temperature 25
℃) was passed through a conventional ion exchange material and the apparatus of the present invention, and the obtained soft water was analyzed and weighed and compared with raw water, and the results shown in Table 1 were obtained. As is clear from this table, compared to water softening using conventional ion exchange materials, calcium content is 0.2 mg, magnesium content is 0.05 mg, and dissolved enzyme is 0.6 mg per raw water.
It can be seen that the degree of softening of raw water by the apparatus of the present invention has increased.
【表】
「発明の効果」
以上説明したように、本発明によれば、原水
は、濾過槽で塩素分を除去され、磁場槽でその鉄
分を吸着されるとともに磁気の反発力によつて分
子結合力が撹乱された後、イオン交換槽によりイ
オン交換されるので、原水中に含まれる鉄分はほ
ぼ完全に除去され、原水中のその他の不純物成分
をも分解された軟水を得ることができる。[Table] "Effects of the Invention" As explained above, according to the present invention, raw water has its chlorine content removed in a filtration tank, its iron content adsorbed in a magnetic field tank, and the molecules of raw water are absorbed by magnetic repulsion. After the binding force is disrupted, ions are exchanged in an ion exchange tank, so that the iron contained in the raw water is almost completely removed, and soft water can be obtained in which other impurity components in the raw water are also decomposed.
第１図は本発明による活水製造装置の一実施例
を示す断面図、第２図は第１図における磁場槽内
に設置される磁気発生装置の正面図、第３図は第
２図の−線に沿う拡大断面図である。
１１……濾過槽、１２……入口、１５……活性
炭、１６，２８……連結管、１７，２９……フイ
ルタ、２０……磁場槽、２１……第１の磁場槽、
２２……第２の磁場槽、２３……仕切壁、２４…
…磁気発生装置、２５……永久磁石、３０……イ
オン交換槽、３１……出口、３２……イオン交換
材。
FIG. 1 is a sectional view showing an embodiment of the active water production apparatus according to the present invention, FIG. 2 is a front view of the magnetic field generating device installed in the magnetic field tank in FIG. 1, and FIG. 3 is a - FIG. 3 is an enlarged cross-sectional view taken along the line. 11... Filter tank, 12... Inlet, 15... Activated carbon, 16, 28... Connecting pipe, 17, 29... Filter, 20... Magnetic field tank, 21... First magnetic field tank,
22... Second magnetic field tank, 23... Partition wall, 24...
... Magnetism generator, 25 ... Permanent magnet, 30 ... Ion exchange tank, 31 ... Outlet, 32 ... Ion exchange material.
Claims (1)
く濾過槽と、この濾過槽に連通させ該濾過槽から
の塩素分の除かれた水を永久磁石により磁化させ
る磁場槽と、この磁場槽に連通させ該磁場槽から
の磁化水をイオン交換により軟水化するイオン交
換槽とを備えてなることを特徴とする活水製造装
置。 ２ 前記磁場槽は複数槽に分割連通され、前記塩
素分の取り除かれた水が上記複数槽を順次通過す
る特許請求の範囲第１項に記載の活水製造装置。 ３ 前記永久磁石は、一方面がＮ極、他方面がＳ
極を呈する多数で構成され、各極面が相互に反発
する関係で配置されている特許請求の範囲第２項
または第３項に記載の活水製造装置。 ４ 前記永久磁石は、磁束密度が4000G以上であ
る特許請求の範囲第１項ないし第３項のいずれか
一に記載の活水製造装置。[Scope of Claims] 1. A filtration tank that takes in raw water and removes chlorine from the raw water, and a magnetic field tank that communicates with the filtration tank and magnetizes the water from the filtration tank from which chlorine has been removed using a permanent magnet. An ion exchange tank that communicates with the magnetic field tank and softens magnetized water from the magnetic field tank by ion exchange. 2. The activated water production apparatus according to claim 1, wherein the magnetic field tank is divided into a plurality of tanks and communicated with each other, and the water from which the chlorine content has been removed sequentially passes through the plurality of tanks. 3 The permanent magnet has an N pole on one side and an S pole on the other side.
The active water production device according to claim 2 or 3, which is composed of a large number of poles, and each pole surface is arranged in a mutually repulsive relationship. 4. The active water production apparatus according to any one of claims 1 to 3, wherein the permanent magnet has a magnetic flux density of 4000G or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16051986A JPS6316091A (en) | 1986-07-08 | 1986-07-08 | Manufacturing facility for activated water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16051986A JPS6316091A (en) | 1986-07-08 | 1986-07-08 | Manufacturing facility for activated water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6316091A JPS6316091A (en) | 1988-01-23 |
| JPH031076B2 true JPH031076B2 (en) | 1991-01-09 |
Family
ID=15716711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16051986A Granted JPS6316091A (en) | 1986-07-08 | 1986-07-08 | Manufacturing facility for activated water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6316091A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3223450B2 (en) * | 1999-06-07 | 2001-10-29 | モリオキ産業株式会社 | Ultra high magnetic fluid processing equipment |
| KR100461903B1 (en) * | 2002-12-13 | 2004-12-17 | 한국수자원공사 | Meandering flow powered activated charcoal contactor with paneled barriers |
| CN111706556B (en) * | 2020-06-05 | 2021-09-03 | 浙江优绣家居用品有限公司 | Prevent blockking up water intaking fire control water pump |
-
1986
- 1986-07-08 JP JP16051986A patent/JPS6316091A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6316091A (en) | 1988-01-23 |
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