JPS6345603B2 - - Google Patents
Info
- Publication number
- JPS6345603B2 JPS6345603B2 JP8556485A JP8556485A JPS6345603B2 JP S6345603 B2 JPS6345603 B2 JP S6345603B2 JP 8556485 A JP8556485 A JP 8556485A JP 8556485 A JP8556485 A JP 8556485A JP S6345603 B2 JPS6345603 B2 JP S6345603B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- iron
- inner cylinder
- permanent magnet
- lid
- 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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 98
- 229910052742 iron Inorganic materials 0.000 claims description 47
- 239000007788 liquid Substances 0.000 claims description 41
- 238000005192 partition Methods 0.000 claims description 21
- 230000005415 magnetization Effects 0.000 claims description 6
- 230000002093 peripheral effect Effects 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 27
- 238000000034 method Methods 0.000 description 15
- 238000001914 filtration Methods 0.000 description 10
- 239000011550 stock solution Substances 0.000 description 8
- 230000005389 magnetism Effects 0.000 description 5
- 210000000078 claw Anatomy 0.000 description 4
- 238000004891 communication Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 230000004931 aggregating effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 235000014413 iron hydroxide Nutrition 0.000 description 1
- 229910021506 iron(II) hydroxide Inorganic materials 0.000 description 1
- 239000011553 magnetic fluid Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Description
本発明は液体中に含まれている鉄分に磁気を与
える磁化装置に係り、特に醸造用水等の液体中に
イオン状で混在している鉄分に磁気を与えて共有
結合させ、粒子を粗大化して次段の濾過系により
容易且つほぼ完全に除鉄できるようになした液体
中の鉄分の磁化装置に関する。
以下、醸造用水を例にして説明すれば、醸造は
醸造用水の水質如何によつて醗酵状態の良し悪し
が決定される。醸造用水として備えるべき条件
は、水道水の水質基準に準じることは勿論である
が、醸造製品の品質を著しく劣化させる鉄やマン
ガン等の金属含量と、清冽な水の条件を満足させ
るため有機物量等を特に低く抑えなければならな
い。酵母の生育に必要な鉄の量は使用する原料穀
物から充分に供給されるので、用水中に鉄を全く
含有しない水が醸造好適水とされている。すなわ
ち、好適水といわれる用水中の鉄の含有は
0.02ppm以下が望ましく、0.05ppm以上の鉄が含
まれている場合は鉄分とバクテリヤが結合して、
醗酵にとつて有害な雑菌が繁殖したりして製品が
劣化し易いので醸造界では完全な除鉄に腐心して
いるのが現状である。
用水中の鉄分は水酸化鉄のように微粒子で浮遊
状態にあるもの、イオン状の低分子量のもの、腐
植質等の有機物と結合して錯化合物の形態をした
高分子量のもの等、その形態はさまざまで、除鉄
法としては、現在水酸化第一鉄の除去を目的とし
た気曝法、砂濾過法、接触酸化法、水中の第一鉄
を塩素によつて酸化して水酸化第二鉄として除去
する塩素酸化法、薬剤を用いる凝集法、活性炭や
造粒炭を用いた濾過法、イオン交換樹脂処理法等
があるが、これらの単独の濾過法では充分なる除
鉄は望めないのが現状である。特に、低分子量の
イオン化した鉄の除去は極めて困難とされてい
る。近時、電磁石や永久磁石による除鉄法が開発
されているが、本発明は永久磁石によるイオン状
の低分子量の鉄の除去をより効率的に行えるよう
になした液体中の鉄分の磁化装置に関するもので
ある。これまでの永久磁石による液体中の鉄分の
磁化法は、単独の永久磁石に液体を流速を落とし
て通し磁気を与える方法が多く、液体中の鉄に充
分な磁化を与えることができなかつた。
本発明は、処理すべき液体を、所定の間隙を保
持して多数並列せしめた永久磁石体間を複数回に
わたつて反復通過させることにより極めて効率よ
く、液体中の鉄分に充分に磁化を与えることがで
きるようになした液体中の鉄分の磁化装置を提供
することを目的とするものである。
本発明を詳述すれば、一端開口部に液体の流入
口を穿設した蓋体を固定すると共に、他端開口部
に液体の流出口を穿設した蓋体を固定してなる外
筒と、この外筒内のほぼ中心に位置し、一端開口
部を前記蓋体に穿設した液体の流入口に接続させ
ると共に、周面に液体の通流孔を多数穿設してな
る内筒と、この内筒の外周部に間隙保持体を介し
て多数配列させた環状の永久磁石体と、前記内筒
内の液体の通流路を仕切る内仕切板と、前記外筒
と内筒の間に形成される液体の通流路を仕切る外
仕切板とからなり、流入口より内筒内に入つた液
体を前記環状の永久磁石体間を複数回にわたつて
通過させ液体中に含まれている鉄分の磁化を促進
するようにしたことを特徴とする液体中の鉄分の
磁化装置、である。
本発明によれば、永久磁石体相互の間に間隙保
持体が設けられることによつて液体の流速を常に
円滑に保つことができると共に、間隙保持体によ
つて設けられた永久磁石体間の間隙の最も磁場の
強いところを液体が均一にしかも磁場と直交する
ような状態で通流するので磁化効率が大である特
徴を有する。
本発明装置にて処理した磁化液は24〜48時間程
度経過すると磁場通過前の液体と比較して白濁し
てくる。この現象は液体中のイオン化している鉄
が磁気を帯びて粒子が大きくなつたことによるも
ので、この磁化液を次段階の濾過系により精密濾
過することによつて白濁した鉄の粗大粒子が除去
され、用水中の鉄の含有量を醸造好適水の
0.02ppm以下にまで除去することが可能となる。
以下、本発明の具体的構成を図示の実施例に基
づき詳細に説明する。
第1図は本発明装置の一実施例を示す縦断面図
であり、図中1は外筒を示す。2は当該外筒1の
一端開口部に固定した蓋体であり、当該蓋体2の
ほぼ中央部には液体の流入口3を穿設してある。
4は外筒1の他端開口部に固定した蓋体を示し、
当該蓋体4のほぼ中央部には液体の流出口5を穿
設してある。6は前記蓋体2と蓋体4を連結して
外筒1と蓋体2及び蓋体4をそれぞれ水密状に固
定する長尺状の固定棒、7は環状のOリング、8
は蓋体2の流入口3に螺着した接続部材、9は蓋
体4の流出口5に螺着した接続部材をそれぞれ示
すものである。
10は前記外筒1内のほぼ中心に位置する内筒
であり、その周面には液体の通流孔11を多数穿
設してある。内筒10の両端部外周にはそれぞれ
雄螺子を刻設してあり、一方の端部を蓋体2の流
入口3に刻設してある雌螺子に螺着すると共に、
他端部を抑え体12に刻設してある雌螺子に螺着
する。
13は内筒10の外周部に間隙保持体14を介
して多数配列させた環状の永久磁石体であり、そ
れぞれの永久磁石体13はS極とN極とが相対す
るように配設してある。間隙保持体14は、第2
図及び第3図に示す実施例の場合、永久磁石体1
3とほぼ同じ外径形状をもつており、その平坦面
にはくつかの突起15を両側に向け突設すると共
に、中心部に穿設した通孔16の内周縁にはいく
つかの爪17を折曲形成してなる。永久磁石体1
3相互の間に間隙保持体14が介在することによ
り、永久磁石体13同志の間には僅かな隙間18
が得られると共に、爪17が内筒10の外周面に
当接することにより永久磁石体13の内周面と内
筒10との間にも僅かな隙間19が生ずることと
なる。なお、間隙保持体14の構造は、第2図及
び第3図に示す実施例に限られるものではなく、
要するに相隣れる永久磁石体13同志の間並びに
永久磁石体13の内周面と内筒10の外周面との
間に僅かな隙間が生ずるようになしたものであれ
ば、たとえば網目状や波板状となしたものでもよ
いものである。
20は前記内筒10内にある液体の通流路21
を仕切る内仕切板であり、22は外筒1と内筒1
0の間に形成される液体の通流路23を仕切る外
仕切板である。
図示の実施例では、多数配列した永久磁石体1
3をほぼ二分する位置に外仕切板22を水密状に
固定すると共に、流出口5側にも外仕切板22を
水密状に固定して、通流路23を二つのブロツク
に区分するようになし、各ブロツクのほぼ中間位
置にあたる内筒10内にそれぞれ内仕切板20,
20を水密状に固定した構造となつているが、内
仕初板20及び外仕切板22の数や各ブロツクの
長さは適宜変更することができるものである。
なお、流出口5側に配置する外仕切板22は、
抑え体12の螺着により後端の永久磁石体13と
の間に挟まれ固定される。また、一方の端部を蓋
体2の流入口3に螺着した内筒10は外仕切板2
2,22によつて外筒1内のほぼ中心部に保持さ
れる。
本発明装置の使用にあたつては、先づ接続部材
8に原液管をつなぎ該原液管より内筒10内に処
理前の原液を供給する。原液は通流路21を通つ
て、第一の内仕切板20に向け流れるが、内筒1
0の周面には通流孔11が多数穿設してあるの
で、原液はこの通流孔11を通つて外筒1と内筒
10間にある通流路23内に入る。その際、原液
は永久磁石体13同志の間の隙間18を通り、永
久磁石体13の最大磁場(本実施例では、外径80
mm、内径40mm、厚さ10mmで360K/Gの永久磁石
体を使用)を扇状にしかも磁場に対し直交するよ
うに通過するので最も強く磁気を受けることにな
る。なお、間隙保持体14には前記したとおり爪
17が折曲形成してあるので、永久磁石体13と
内筒10の間にも僅かな隙間19が得られ、内筒
10の外周部の原液の円滑なる循環が図れるもの
である。
通流路23内に入つた原液は、外仕切板22に
よつて直進を阻まれ、再び永久磁石体13の間の
最大磁場を通つて、内筒10内の通流路21内に
戻る。そして、原液は外仕切板22を境にした第
二ブロツク内に入り、内筒10内の通流孔11を
通つて外筒1内の通流路23内を進み、後端の外
仕切板22により再度永久磁石体13間の隙間1
8を通つて内筒10内の最終の通流路21内に入
り、蓋体4に穿設した流出口5より磁化液となつ
て装置外に排出されるものである。
本発明によれば、原液は複数の最大磁場を扇状
にしかも磁場に対し直交するように円滑に通流す
ることができ、複数回の磁場の通過により短時間
に且つ確実に大量の磁気液が、塩素酸化法や薬剤
による凝集法等の除鉄のように水質を変えること
なく得られ、原液中のイオン状の低分子量の鉄を
高分子状の粒子となし、次段階の精密濾過にて容
易に除鉄することができるようになるものであ
る。以下に示す表1は、鉄分の含量がそれぞれ異
なる三種類の処理前の原水を対象として、セラミ
ツク濾過処理に直接かけた場合と、本発明装置に
より処理した後セラミツク濾過にかけて処理した
場合の鉄分の含量をそれぞれ比較したものであ
る。
なお、本実施例では外径80mm、内径40mm、厚さ
10mmで360K/Gの永久磁石体を用いた。表1に
示されるとおり、種別3の0.25ppm程度の原水中
の鉄分なら、本発明の永久磁石体間の磁場を二回
程度通過させた後セラミツク濾過一回の処理だけ
でも鉄分不検出の状態にまで鉄分を除去すること
ができる。
この鉄分の除去理論を考察すると、原水中に存
在するイオン型の鉄分が永久磁石の磁場の影響を
受け共有給合することによるものであり、共有給
合した場合の形態は表2のようになる。
共有結合済みの鉄分が永久磁石体間の磁場を通
過するときに受ける磁気によつて、その分子が更
に二個以上の形態を形成すると、少なくとも0.4μ
フイルター(直径4.0×10-7mm)の濾過能力より
も大となるので0.4μフイルターで除去される。こ
こでもし0.2μフイルター(直径2.0×10-7mm)を使
用して濾過を行なえば、共有結合済みの鉄分は全
て除去され、イオン型のみの鉄分だけが水中には
残留することになる。
次の表3は、原水を本発明の永久磁石体間を一
回通過させた後、0.2μフイルターで濾過を行なつ
た場合のFe2+の含有率を示したものである。
表3に示されるとおり、Fe2+の含有率は時間
が経過するほどその値は減少していることが分か
る。従つて、永久磁石体間の磁場を通過させた用
水はできるだけ時間の経過後に濾過を行なうこと
が望ましいことが分かる。
以上の試験結果を総合して考察すると、本発明
の永久磁石体間の磁場を用水が通過するとき、用
水中の鉄分の受ける影響は、Feイオンを共有
結合させる作用、共有結合済みのFeを集合さ
せる作用、上記及び以外の方法でFe2+を
集合体化させその径を巨大化させる作用、等が考
えられる。従つて、表1に示されるとおり、本発
明の永久磁石体間の磁場を用水を通流させた後、
0.2〜0.4μフイルターにより濾過することによつ
て、たとえば醸造用水中の鉄分をその好適水とし
ての鉄分0.02ppm以下にまで濾過することができ
るものである。
The present invention relates to a magnetization device that applies magnetism to iron contained in a liquid, and in particular, applies magnetism to iron contained in ionic form in liquids such as brewing water, covalently bonds it, and coarsens the particles. This invention relates to a device for magnetizing iron in a liquid, which allows iron to be easily and almost completely removed by a subsequent filtration system. In the following explanation, using brewing water as an example, the quality of the fermentation state in brewing is determined by the quality of the brewing water. The conditions that should be provided for brewing water are, of course, that it complies with the water quality standards for tap water, but also the content of metals such as iron and manganese, which can significantly deteriorate the quality of brewed products, and the amount of organic matter to satisfy the requirements for clear water. etc. must be kept particularly low. Since the amount of iron necessary for the growth of yeast is sufficiently supplied from the raw material grains used, water that does not contain any iron is considered suitable water for brewing. In other words, the iron content in the water called suitable water is
0.02ppm or less is desirable, and if it contains more than 0.05ppm, iron and bacteria will combine,
Currently, the brewing industry is working hard to completely remove iron, since bacteria that are harmful to fermentation can grow and the product tends to deteriorate. Iron in water comes in many forms, including suspended fine particles such as iron hydroxide, low-molecular-weight ionic materials, and high-molecular-weight materials combined with organic matter such as humic substances in the form of complex compounds. There are various iron removal methods, and the current iron removal methods include aeration method, sand filtration method, contact oxidation method, and ferrous hydroxide method in which ferrous iron in water is oxidized with chlorine. There are chlorine oxidation methods that remove iron as di-iron, flocculation methods that use chemicals, filtration methods that use activated carbon or granulated carbon, ion exchange resin treatment methods, etc., but these filtration methods alone cannot be expected to remove iron sufficiently. is the current situation. In particular, it is considered extremely difficult to remove low molecular weight ionized iron. Recently, iron removal methods using electromagnets or permanent magnets have been developed, and the present invention provides a device for magnetizing iron in liquid that allows more efficient removal of ionic low molecular weight iron using permanent magnets. It is related to. Conventional methods of magnetizing iron in liquid using permanent magnets have mostly involved passing the liquid through a single permanent magnet at a slow speed to impart magnetism, and it has not been possible to provide sufficient magnetization to the iron in liquid. The present invention allows the liquid to be treated to pass repeatedly between multiple permanent magnet bodies arranged in parallel with a predetermined gap, thereby highly efficiently magnetizing the iron in the liquid. It is an object of the present invention to provide a device for magnetizing iron in a liquid, which is capable of magnetizing iron in a liquid. More specifically, the present invention includes an outer cylinder in which a lid body having a liquid inflow port formed in an opening at one end is fixed, and a lid body having a liquid outflow port formed in the other end opening is fixed. , an inner cylinder located approximately at the center of the outer cylinder, having an opening at one end connected to a liquid inlet formed in the lid, and having a number of liquid passage holes perforated on the circumferential surface; , a large number of annular permanent magnets arranged on the outer periphery of the inner cylinder via gap retainers, an inner partition plate that partitions a liquid flow path in the inner cylinder, and a space between the outer cylinder and the inner cylinder. The liquid flowing into the inner cylinder from the inlet is made to pass between the annular permanent magnet bodies multiple times to remove the liquid contained in the liquid. 1. A device for magnetizing iron in a liquid, characterized in that it promotes magnetization of iron in a liquid. According to the present invention, by providing the gap holder between the permanent magnet bodies, the flow rate of the liquid can always be kept smooth, and the gap holder provides the space between the permanent magnet bodies. Since the liquid flows uniformly through the gap where the magnetic field is strongest and in a state perpendicular to the magnetic field, it is characterized by high magnetization efficiency. After about 24 to 48 hours, the magnetized liquid treated with the apparatus of the present invention becomes cloudy compared to the liquid before passing through the magnetic field. This phenomenon is caused by the ionized iron in the liquid becoming magnetic and becoming larger particles.By passing this magnetized liquid through a precision filtration system in the next step, the coarse particles of iron that become cloudy are removed. Removes the iron content in the water and makes it suitable for brewing water
It becomes possible to remove it down to 0.02ppm or less. Hereinafter, a specific configuration of the present invention will be explained in detail based on illustrated embodiments. FIG. 1 is a longitudinal sectional view showing an embodiment of the device of the present invention, and 1 in the figure indicates an outer cylinder. Reference numeral 2 denotes a lid fixed to an opening at one end of the outer cylinder 1, and a liquid inlet 3 is bored approximately in the center of the lid 2.
4 indicates a lid fixed to the opening at the other end of the outer cylinder 1;
A liquid outlet 5 is provided approximately in the center of the lid 4 . 6 is a long fixing rod that connects the lid 2 and the lid 4 and fixes the outer cylinder 1, the lid 2, and the lid 4 in a watertight manner, 7 is an annular O-ring, and 8
9 indicates a connecting member screwed onto the inlet 3 of the lid 2, and 9 represents a connecting member screwed onto the outlet 5 of the lid 4. Reference numeral 10 denotes an inner cylinder located approximately at the center of the outer cylinder 1, and a large number of liquid passage holes 11 are bored in the circumferential surface of the inner cylinder. A male screw is formed on the outer periphery of both ends of the inner cylinder 10, and one end is screwed into a female screw formed on the inlet 3 of the lid body 2.
The other end is screwed into a female screw cut into the holding body 12. Reference numeral 13 denotes a large number of annular permanent magnet bodies arranged on the outer periphery of the inner cylinder 10 with gap holders 14 in between, and each permanent magnet body 13 is arranged so that the S pole and the N pole face each other. be. The gap holder 14 is a second
In the case of the embodiment shown in Figures and Figure 3, the permanent magnet body 1
It has approximately the same outer diameter shape as 3, and has several protrusions 15 protruding from both sides on its flat surface, and several claws 17 on the inner periphery of a through hole 16 bored in the center. It is formed by bending it. Permanent magnet 1
By interposing the gap holder 14 between the three permanent magnet bodies 13, there is a slight gap 18 between the permanent magnet bodies 13.
At the same time, a slight gap 19 is created between the inner circumferential surface of the permanent magnet body 13 and the inner tube 10 due to the claws 17 coming into contact with the outer circumferential surface of the inner tube 10. Note that the structure of the gap holder 14 is not limited to the embodiment shown in FIGS. 2 and 3;
In short, as long as there is a slight gap between adjacent permanent magnet bodies 13 and between the inner circumferential surface of the permanent magnet bodies 13 and the outer circumferential surface of the inner cylinder 10, it is possible to A plate-shaped one may also be used. Reference numeral 20 denotes a liquid passage 21 in the inner cylinder 10.
22 is an inner partition plate that separates the outer cylinder 1 and the inner cylinder 1.
This is an outer partition plate that partitions a liquid flow path 23 formed between the two. In the illustrated embodiment, a large number of permanent magnet bodies 1 are arranged.
The outer partition plate 22 is fixed in a watertight manner at a position that substantially divides the flow path 23 into two blocks, and the outer partition plate 22 is also fixed in a watertight manner on the side of the outlet 5 to divide the flow path 23 into two blocks. None, internal partition plates 20,
20 are fixed in a water-tight manner, but the number of inner first plates 20 and outer partition plates 22 and the length of each block can be changed as appropriate. Note that the outer partition plate 22 placed on the outlet 5 side is
By screwing the suppressing body 12, it is sandwiched and fixed between it and the permanent magnet body 13 at the rear end. In addition, the inner cylinder 10 whose one end is screwed to the inlet 3 of the lid body 2 is connected to the outer partition plate 2.
2 and 22, it is held approximately at the center inside the outer cylinder 1. In using the apparatus of the present invention, first, a stock solution tube is connected to the connecting member 8, and the stock solution before treatment is supplied into the inner cylinder 10 from the stock solution tube. The stock solution flows through the flow path 21 toward the first inner partition plate 20, but the inner tube 1
Since a large number of communication holes 11 are formed on the circumferential surface of the tube 0, the stock solution passes through the communication holes 11 and enters the communication path 23 located between the outer cylinder 1 and the inner cylinder 10. At that time, the stock solution passes through the gap 18 between the permanent magnets 13, and the maximum magnetic field of the permanent magnets 13 (in this example, the outer diameter is 80
mm, inner diameter 40mm, thickness 10mm, using a 360K/G permanent magnet) in a fan shape and perpendicular to the magnetic field, so it receives the strongest magnetism. In addition, since the gap holder 14 has the claws 17 bent as described above, a slight gap 19 is also obtained between the permanent magnet body 13 and the inner cylinder 10, and the undiluted solution on the outer periphery of the inner cylinder 10 is This will help ensure a smooth circulation. The undiluted solution that has entered the flow path 23 is prevented from going straight by the outer partition plate 22 and returns to the flow path 21 in the inner cylinder 10 through the maximum magnetic field between the permanent magnets 13 again. Then, the stock solution enters the second block bordered by the outer partition plate 22, passes through the flow hole 11 in the inner cylinder 10, moves through the flow path 23 in the outer cylinder 1, and passes through the outer partition plate at the rear end. 22, the gap 1 between the permanent magnet bodies 13 is again
8 and enters the final flow path 21 in the inner cylinder 10, and is discharged outside the apparatus as a magnetized liquid through an outlet 5 formed in the lid 4. According to the present invention, the undiluted solution can smoothly flow through multiple maximum magnetic fields in a fan shape and perpendicularly to the magnetic fields, and by passing through the magnetic fields multiple times, a large amount of magnetic fluid can be reliably passed through in a short period of time. , which can be obtained without changing the water quality like iron removal using chlorine oxidation method or chemical flocculation method, converts the ionic low molecular weight iron in the stock solution into polymeric particles, and then processes it in the next stage of precision filtration. This makes it possible to easily remove iron. Table 1 below shows the iron content of three types of raw water before treatment, each with a different iron content, when it is directly subjected to ceramic filtration treatment, and when it is treated with the device of the present invention and then subjected to ceramic filtration treatment. This is a comparison of their respective contents. In this example, the outer diameter is 80 mm, the inner diameter is 40 mm, and the thickness is 80 mm.
A 10mm, 360K/G permanent magnet was used. As shown in Table 1, if the iron content in the raw water of type 3 is about 0.25 ppm, the iron content will not be detected even after passing through the magnetic field between the permanent magnets of the present invention twice, followed by ceramic filtration once. It is possible to remove iron up to Considering this iron removal theory, it is due to covalent addition of ionic iron present in raw water under the influence of the magnetic field of a permanent magnet, and the form of covalent addition is as shown in Table 2. Become. If the covalently bonded iron molecules form two or more molecules due to the magnetism they receive when they pass through the magnetic field between the permanent magnets, the magnetic field will be at least 0.4μ.
This is greater than the filtration capacity of a filter (diameter 4.0 x 10 -7 mm), so it is removed with a 0.4μ filter. If the water is filtered using a 0.2μ filter (diameter 2.0 x 10 -7 mm), all covalently bound iron will be removed and only ionic iron will remain in the water. Table 3 below shows the content of Fe 2+ when raw water is passed once between the permanent magnet bodies of the present invention and then filtered through a 0.2μ filter. As shown in Table 3, it can be seen that the Fe 2+ content decreases as time passes. Therefore, it can be seen that it is desirable to filter the water that has passed through the magnetic field between the permanent magnet bodies as long as possible. Considering the above test results as a whole, when water passes through the magnetic field between the permanent magnets of the present invention, the influence of iron in the water is due to the effect of covalently bonding Fe ions, and the effect of covalently bonding Fe. Possible actions include an action of aggregating Fe 2+ , and an action of aggregating Fe 2+ using methods described above and other methods to increase its diameter. Therefore, as shown in Table 1, after the magnetic field between the permanent magnet bodies of the present invention is passed through water,
By filtering with a 0.2 to 0.4μ filter, the iron content in brewing water, for example, can be filtered down to 0.02 ppm or less, which is the preferred water.
【表】
析による。
[Table] Based on analysis.
【表】【table】
第1図は本発明装置の一実施例を示す縦断面
図、第2図は間隙保持体の一実施例を示す平面
図、第3図は第2図のA−A断面図、第4図は永
久磁石体と間隙保持体の関係を示す断面図であ
る。
1:外筒、2:蓋体、3:流入口、4:蓋体、
5:流出口、6:固定棒、7:Oリング、8:接
続部材、9:接続部材、10:内筒、11:通流
孔、12:抑え体、13:永久磁石体、14:間
隙保持体、15:突起、16:通孔、17:爪、
18:隙間、19:隙間、20:内仕切板、2
1:通流路、22:外仕切板、23:通流路。
Fig. 1 is a longitudinal sectional view showing an embodiment of the device of the present invention, Fig. 2 is a plan view showing an embodiment of the gap holder, Fig. 3 is a sectional view taken along line AA in Fig. 2, and Fig. 4. FIG. 2 is a cross-sectional view showing the relationship between a permanent magnet and a gap holder. 1: Outer cylinder, 2: Lid body, 3: Inflow port, 4: Lid body,
5: Outlet, 6: Fixed rod, 7: O-ring, 8: Connection member, 9: Connection member, 10: Inner cylinder, 11: Communication hole, 12: Suppressor, 13: Permanent magnet, 14: Gap Holding body, 15: protrusion, 16: through hole, 17: claw,
18: Gap, 19: Gap, 20: Internal partition plate, 2
1: Flow path, 22: External partition plate, 23: Flow path.
Claims (1)
固定すると共に、他端開口部に液体の流出口を穿
設した蓋体を固定してなる外筒と、この外筒内の
ほぼ中心に位置し、一端開口部を前記蓋体に穿設
した液体の流入口に接続させると共に、周面に液
体の通流孔を多数穿設してなる内筒と、この内筒
の外周部に間隙保持体を介して多数配列させた環
状の永久磁石体と、前記内筒内の液体の通流路を
仕切る内仕切板と、前記外筒と内筒の間に形成さ
れる液体の通流路を仕切る外仕切板とからなり、
流入口より内筒内に入つた液体を前記環状の永久
磁石体間を複数回にわたつて通過させ液体中に含
まれている鉄分の磁化を促進するようにしたこと
を特徴とする液体中の鉄分の磁化装置。1. An outer cylinder to which a lid having a liquid inlet in an opening at one end is fixed, and a lid having a liquid outlet in an opening at the other end to which a lid body is fixed; an inner cylinder located at the center and having an opening at one end connected to a liquid inlet formed in the lid body and having a number of liquid passage holes formed on the circumferential surface; and an outer peripheral part of the inner cylinder. a plurality of annular permanent magnets arranged through gap retainers, an inner partition plate that partitions a liquid passage in the inner cylinder, and a liquid passage formed between the outer cylinder and the inner cylinder. It consists of an outer partition plate that partitions the flow path.
The liquid that has entered the inner cylinder from the inlet is passed between the annular permanent magnet bodies multiple times to promote magnetization of iron contained in the liquid. Iron magnetization device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8556485A JPS61245815A (en) | 1985-04-23 | 1985-04-23 | Apparatus for magnetizing iron component in liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8556485A JPS61245815A (en) | 1985-04-23 | 1985-04-23 | Apparatus for magnetizing iron component in liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61245815A JPS61245815A (en) | 1986-11-01 |
| JPS6345603B2 true JPS6345603B2 (en) | 1988-09-09 |
Family
ID=13862305
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8556485A Granted JPS61245815A (en) | 1985-04-23 | 1985-04-23 | Apparatus for magnetizing iron component in liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61245815A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01189389A (en) * | 1988-01-21 | 1989-07-28 | Hitachi Elevator Eng & Service Co Ltd | Magnetic treatment device |
| JPS63270593A (en) * | 1987-04-30 | 1988-11-08 | Hitachi Elevator Eng & Serv Co Ltd | Water treating device |
| JPS63296886A (en) * | 1987-05-29 | 1988-12-02 | Hitachi Elevator Eng & Serv Co Ltd | Magnet strainer of magnetic treatment apparatus |
| KR102692729B1 (en) * | 2023-03-21 | 2024-08-06 | 김수현 | Mineral-purification water supply apparatus for Agricultural and Livestock |
-
1985
- 1985-04-23 JP JP8556485A patent/JPS61245815A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61245815A (en) | 1986-11-01 |
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