JPH09271757A - Water treating device and treating method thereof - Google Patents

Water treating device and treating method thereof

Info

Publication number
JPH09271757A
JPH09271757A JP8495196A JP8495196A JPH09271757A JP H09271757 A JPH09271757 A JP H09271757A JP 8495196 A JP8495196 A JP 8495196A JP 8495196 A JP8495196 A JP 8495196A JP H09271757 A JPH09271757 A JP H09271757A
Authority
JP
Japan
Prior art keywords
water
layer
arsenic
directions
water treatment
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.)
Pending
Application number
JP8495196A
Other languages
Japanese (ja)
Inventor
Masao Yokoyama
昌夫 横山
Hidenari Tsunemi
常深  秀成
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP8495196A priority Critical patent/JPH09271757A/en
Publication of JPH09271757A publication Critical patent/JPH09271757A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To effectively reduce and remove harmful metals such as As an Pb, from raw water containing these harmful metals. SOLUTION: In a water treating device provided with a filter layer having at least one layer of granular ceramics deposited in a cylindrical housing 10 having a water inflow port 12a and an outflow port 13a respectively at an end and the other end and being arranged respectively at least one piece of magnet 41 at the upper and lower positions of the granular ceramic layer 26 such that the directions of the magnetic lines mutually coincide and the directions of the magnetic lines are along the flow of the water, the harmful metals in raw water are reduced and removed by allowing the water to pass through the device.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、特に地下水を利用
した飲料水中に含まれる有害金属を除去するための装置
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for removing harmful metals contained in drinking water, especially groundwater.

【0002】[0002]

【従来の技術】近年、水質悪化が叫ばれているが、特に
地下水を飲料水にしている地域では、有害金属が含まれ
ているために、飲料用に適さない地域が出ている。平成
6年に水質基準が厳しくなったため、砒素、鉛について
は、より一層不適合地域は拡がり、大きな問題になって
いる。しかし、適切な処理能力を有した有害金属除去装
置はこれまで開発されていないのが現状である。
2. Description of the Related Art In recent years, there has been a call for deterioration in water quality. Especially in areas where groundwater is used as drinking water, some areas are not suitable for drinking because they contain harmful metals. Since the water quality standards became stricter in 1994, the areas of non-conformity for arsenic and lead have spread and become a big problem. However, at present, no harmful metal removal device having an appropriate treatment capacity has been developed.

【0003】[0003]

【発明が解決しようとする課題】以上の状況に鑑み、本
発明が解決しようとするところは、砒素、鉛等の有害金
属が含まれている原水から、これら有害金属を効果的に
低減除去することができる水処理装置及びその処理方法
を提供する点にある。
In view of the above situation, what the present invention intends to solve is to effectively reduce and remove harmful metals from raw water containing harmful metals such as arsenic and lead. Another object is to provide a water treatment device and a treatment method therefor.

【0004】[0004]

【課題を解決するための手段】本発明は、前述の課題を
解決するために、一端及び他端にそれぞれ水の流入口及
び流出口を有する筒状のハウジング内に、少なくとも一
層の粒状セラミックスを堆積し、その粒状セラミックス
層の上下に少なくとも1個の磁石をその磁力線の向きが
互いに一致し、かつ磁力線の方向が水の流れに沿うよう
に配置してなるろ過層を備えた水処理装置において、通
水処理することにより、原水中の有害金属を低減除去す
ることを特徴とする水処理装置を提供する。
In order to solve the above problems, the present invention provides at least one layer of granular ceramics in a cylindrical housing having a water inlet and a water outlet at one end and the other end, respectively. In a water treatment device comprising a filtration layer formed by stacking and arranging at least one magnet above and below the granular ceramic layer so that the directions of the magnetic lines of force coincide with each other and the directions of the lines of magnetic force follow the flow of water. The present invention provides a water treatment device characterized by reducing and removing harmful metals in raw water by conducting water treatment.

【0005】また、本発明は、前述の水処理装置を用い
て、砒素が含まれる原水に酸化剤を添加した後、当該水
処理装置で通水処理して、砒素を低減除去してなること
を特徴とする水処理方法を提供する。
Further, according to the present invention, an oxidizer is added to raw water containing arsenic using the above-mentioned water treatment device, and then water is passed through the water treatment device to reduce and remove arsenic. A water treatment method is provided.

【0006】本発明によれば、有害金属が含まれている
原水を通水処理した場合、処理水中の有害金属濃度を低
減させることができる。従って、本発明の水処理装置
は、飲料水を得る目的で使われる地下水あるいは簡易水
道等において、有害金属濃度が水道水質基準をオーバー
している場合などの処理装置として用いられる。また、
産業用廃水設備として有害金属が含まれている場合など
にも適用可能である。
According to the present invention, when raw water containing harmful metals is passed through, the concentration of harmful metals in the treated water can be reduced. Therefore, the water treatment device of the present invention is used as a treatment device for the groundwater or simple waterworks used for the purpose of obtaining drinking water when the harmful metal concentration exceeds the tap water quality standard. Also,
It can also be applied to industrial wastewater equipment containing harmful metals.

【0007】本発明で除去可能な有害金属は色々ある
が、具体的には水道水質基準、水質環境基準(要監視項
目も含む)等の規制項目に挙げられている鉛、カドミウ
ム、砒素、水銀、クロム、マンガン、鉄、銅、亜鉛、モ
リブデン、ニッケル、アンチモン等が該当する。これら
の有害金属の中でも、特に昨今問題にされている鉛、砒
素の除去効果が顕著である。
There are various kinds of harmful metals that can be removed by the present invention. Specifically, lead, cadmium, arsenic, and mercury listed in regulatory items such as tap water quality standards and water quality environmental standards (including monitoring required items). , Chromium, manganese, iron, copper, zinc, molybdenum, nickel, antimony, etc. Among these harmful metals, the effect of removing lead and arsenic, which has become a problem in recent years, is remarkable.

【0008】また、砒素については、水中に酸化剤を添
加し、5価イオンにすることで、より除去性能は向上す
る。この場合に用いられる酸化剤には、各種酸化剤が可
能であるが、次亜塩素酸ナトリウム、過酸化水素等が特
に好ましい。
As for arsenic, the removal performance is further improved by adding an oxidizing agent to water to form pentavalent ions. Various oxidizing agents can be used as the oxidizing agent in this case, but sodium hypochlorite, hydrogen peroxide and the like are particularly preferable.

【0009】原水中の有害金属濃度が高い場合には、処
理速度すなわち空筒速度を下げること、あるいは繰り返
し通水処理することで対応できるが、具体的には、鉛の
場合で5ppm以下、砒素の場合で1ppm以下が、1
回の通水処理で除去可能な濃度である。これらの有害金
属濃度の原水では、通水処理後の濃度は、鉛の場合で5
0ppd以下、砒素の場合で10ppd以下に低減する
ことが可能である。
When the concentration of harmful metals in the raw water is high, it can be dealt with by lowering the treatment speed, that is, the empty cylinder velocity, or by repeating the water passage treatment. 1ppm or less is 1
It is a concentration that can be removed by one pass of water. In raw water with these harmful metal concentrations, the concentration after lead-through treatment is 5 for lead.
It can be reduced to 0 ppd or less and 10 ppd or less in the case of arsenic.

【0010】処理速度すなわち空筒速度は、速すぎると
除去が不十分であり、また遅すぎると装置のサイズに比
較して処理能力が低くなり好ましくない。具体的には、
30〜5000hr-1が好ましく、特に50〜3000
hr-1がより好ましい。
If the processing speed, that is, the empty cylinder speed, is too fast, the removal is insufficient, and if it is too slow, the processing capacity becomes lower than the size of the apparatus, which is not preferable. In particular,
30 to 5000 hr −1 is preferable, and particularly 50 to 3000
hr −1 is more preferable.

【0011】[0011]

【発明の実施の形態】図1は、本発明の水処理装置の一
実施例の要部、すなわちろ過層を示すもので、図中の1
0はハウジング、21は第一の砂層、22は活性炭層、
23は第2の砂層、24は泰澄石層、25は第一の磁鉄
鉱石層、26はセラミックス層、27は第二の磁鉄鉱石
層、28は麦飯石層、31は穴開きフィルター、32は
不織布フィルター、33は仕切網、41は磁石、40−
1、40−2、40−3はマグネットプレートである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows the essential part of one embodiment of a water treatment apparatus of the present invention, that is, a filtration layer.
0 is a housing, 21 is a first sand layer, 22 is an activated carbon layer,
23 is the second sand layer, 24 is the Taiseki stone layer, 25 is the first magnetite layer, 26 is the ceramic layer, 27 is the second magnetite layer, 28 is the barite layer, 31 is a perforated filter, 32 is Nonwoven fabric filter, 33 is a partition net, 41 is a magnet, 40-
1, 40-2 and 40-3 are magnet plates.

【0012】ハウジング10は、円筒状の本体11、水
の流入口12aを有するキャップ12及び水の流出口1
3aを有するキャップ13からなり、本体11の一端及
び他端にそれぞれキャップ12及びキャップ13が取り
付けられてなっている。
The housing 10 has a cylindrical body 11, a cap 12 having a water inlet 12a and a water outlet 1.
It is composed of a cap 13 having 3a, and a cap 12 and a cap 13 are attached to one end and the other end of the main body 11, respectively.

【0013】第一の砂層21及び第二の砂層23は火成
岩シラスを特殊処理した白砂を層状に堆積してなってお
り、また、活性炭層22は粒状活性炭を層状に堆積して
なっており、これらによって主として残留塩素、有機物
質、有害物質(例えばトリハロメタン)、赤錆、不純
物、カビ臭等を除去する。また、泰澄石層24及び麦飯
石層28はそれぞれ泰澄石及び麦飯石の細片を層状に堆
積してなっており、主として水質(pH等)を調整する
とともにミネラルを補給する。尚、活性炭層22は粒状
活性炭に限らず繊維状活性炭を適宜用いることができ
る。
The first sand layer 21 and the second sand layer 23 are layers of white sand obtained by specially treating igneous rock Shirasu, and the activated carbon layer 22 is a layer of granular activated carbon. By these, residual chlorine, organic substances, harmful substances (eg trihalomethane), red rust, impurities, musty odor, etc. are mainly removed. Further, the Taiseki stone layer 24 and the barley stone layer 28 are formed by depositing fine pieces of the Taiseki stone and the barley stone respectively in layers, and mainly adjust water quality (pH and the like) and supply minerals. The activated carbon layer 22 is not limited to granular activated carbon, and fibrous activated carbon can be used as appropriate.

【0014】第一の磁鉄鉱石層25及び第二の磁鉄鉱石
層27は磁鉄鉱石の細片を層状に堆積してなっており、
後述するマグネットの磁場によって磁化され、有害金属
類を除去するとともに水分子を磁化処理して活性化す
る。また、セラミック層26は火成岩シラスを特殊処理
した白砂をさらに高温(例えば1100℃)で特殊処理
した粒状セラミックを層状に堆積してなっており、遠赤
外線照射によって水分子を活性化するとともに水質劣化
を防止する。
The first magnetite ore layer 25 and the second magnetite ore layer 27 are formed by depositing pieces of magnetite ore in layers.
It is magnetized by the magnetic field of a magnet, which will be described later, and removes harmful metals and magnetizes water molecules to activate them. The ceramic layer 26 is formed by layering granular ceramics obtained by specially treating white sand obtained by specially treating igneous rock shirasu at a higher temperature (for example, 1100 ° C.), activating water molecules by far-infrared irradiation and deteriorating water quality. Prevent.

【0015】穴明きフィルター31はほぼ全面に細かい
穴が多数設けられたプラスチックプレートからなってお
り、周知の不織布フィルター32及び仕切網33ととも
に前述した各層を分離・保持する。
The perforated filter 31 is made of a plastic plate having a large number of fine holes formed on almost the entire surface thereof, and separates and holds the above-mentioned layers together with a well-known nonwoven fabric filter 32 and a partition net 33.

【0016】マグネットプレート40−1〜40−3は
全て同一構成で、3個のコイン状の磁石41を固定する
とともに、略全面に細かい穴(図示せず)が多数設けら
れたプラスチックプレート等からなるる。全ての磁石4
1は、それぞれがハウジング10の中心軸を中心とする
同一円上の中心角を等分した位置(ここでは中心角12
0°で3等分した位置)に保持されている。また、前記
磁石61は表面がプラスチック等によりコーティングさ
れた強力な磁石(例えば残留磁束密度12000ガウ
ス)であり、軸方向に磁化されている。
All of the magnet plates 40-1 to 40-3 have the same structure, and fix three coin-shaped magnets 41, and from a plastic plate or the like provided with a large number of fine holes (not shown) on substantially the entire surface. Become All magnets 4
1 is a position obtained by equally dividing the central angle on the same circle about the central axis of the housing 10 (here, the central angle 12
It is held at 0 ° in three equal parts). The magnet 61 is a strong magnet (for example, residual magnetic flux density 12000 gauss) whose surface is coated with plastic or the like, and is magnetized in the axial direction.

【0017】而して、ハウジング10の本体11内にそ
の上部より下方に向かって、前述した各層、フィルター
及びプレートが、符号31、32、21、32、33、
22、32、40−1、32、23、32、33、2
4、33、32、25、32、40−2、26、33、
32、27、32、40−3、28、32、31の順に
積層配置され、ろ過槽が構成される。この際、マグネッ
トプレート40−1〜40−3はマグネットプレート4
0−1及び40−2の間隔とマグネットプレート40−
2及び40−3の間隔とがほぼ同一になり且つそれぞれ
の磁石41の位置が上下方向で一致するように位置決め
され、また、各マグネットプレート40−1〜40−3
の全ての磁石41はその磁力線の向きが互いに一致、特
に水の流れに対して逆向きとなるように一致し且つ磁力
線の方向が水の流れに沿うように配置されている。
Thus, in the main body 11 of the housing 10, the layers, filters and plates described above are denoted by reference numerals 31, 32, 21, 32, 33, from the top to the bottom.
22, 32, 40-1, 32, 23, 32, 33, 2
4, 33, 32, 25, 32, 40-2, 26, 33,
32, 27, 32, 40-3, 28, 32, 31 are stacked in this order to form a filtration tank. At this time, the magnet plates 40-1 to 40-3 are attached to the magnet plate 4
0-1 and 40-2 spacing and magnet plate 40-
2 and 40-3 are substantially equal to each other, and the positions of the magnets 41 are aligned in the vertical direction, and the magnet plates 40-1 to 40-3 are positioned.
All of the magnets 41 are arranged such that their magnetic lines of force coincide with each other, in particular, so that they are opposite to the flow of water, and the directions of the lines of magnetic force are along the flow of water.

【0018】このろ過槽によれば、マグネットプレート
40−1〜40−3のそれぞれの磁石41の磁力線は互
いに結合して増強し合い、特に上向き、即ち水の流れに
沿い且つそれとは逆向きの均一で強力な磁場42を形成
し、また、該磁場42は第一の磁鉄鉱石層25及び第二
の磁鉄鉱石層27全体を強力に磁化するため、水分子は
マグネットプレート40−1とマグネットプレート40
−3との間、特に第一の磁鉄鉱石層25及び第二の磁鉄
鉱石層27を通過する際、効果的に磁化処理されること
になる。また、前記磁場42並びにこれにより磁化され
た第一の磁鉄鉱石層25及び第二の磁鉄鉱石層27によ
る磁場がセラミック層26を通過するため、原水中に含
まれる有害金属が除去される。
According to this filtration tank, the magnetic lines of force of the magnets 41 of the magnet plates 40-1 to 40-3 are combined with each other to reinforce each other, particularly upward, that is, along the flow of water and in the opposite direction. Since a uniform and strong magnetic field 42 is formed and the magnetic field 42 strongly magnetizes the entire first magnetite ore layer 25 and the second magnetite ore layer 27, water molecules are generated in the magnet plate 40-1 and the magnet plate 40-1. 40
-3, particularly when passing through the first magnetite ore layer 25 and the second magnetite ore layer 27, the magnetizing treatment is effectively performed. Further, since the magnetic field generated by the magnetic field 42 and the first magnetite ore layer 25 and the second magnetite ore layer 27 magnetized by the magnetic field 42 passes through the ceramic layer 26, harmful metals contained in the raw water are removed.

【0019】[0019]

【実施例】【Example】

(実施例1)上述の水処理装置に、蒸留水に約60%ヒ
酸溶液(和光純薬製試薬1級)を、0.01mg/L、
及び0.02mg/Lの砒素濃度になるように調整した
水を原水として、ポンプにより4.2L/min(空筒
速度240hr-1)で通水し、処理後の砒素濃度を分析
した。その結果、双方の濃度において、処理水の砒素濃
度は0.001mg/Lであった。
(Example 1) About 60% arsenic acid solution (Wako Pure Chemical Industries reagent grade 1) was added to distilled water in an amount of 0.01 mg / L in the above water treatment device.
And water adjusted to have an arsenic concentration of 0.02 mg / L as raw water were passed by a pump at 4.2 L / min (empty speed 240 hr −1 ) to analyze the arsenic concentration after the treatment. As a result, the arsenic concentration of the treated water was 0.001 mg / L at both concentrations.

【0020】(実施例2)実施例1と同様に、蒸留水に
砒素水溶液として1000mg/LのICP用標準液
(硝酸性:アルドリッチ製)を砒素濃度0.011mg
/Lになるように調整し、さらに次亜塩素酸ナトリウム
約5%溶液(関東化学製)を1.0mg/Lの濃度にな
るように添加し原水とした。この原水をポンプにより
4.2L/min(空筒速度240hr-1)で通水し、
処理後の砒素濃度を分析した。その結果、処理水の砒素
濃度は0.001mg/L未満であった。
(Example 2) As in Example 1, 1000 mg / L of an ICP standard solution (nitric acid: manufactured by Aldrich) was added to distilled water as an arsenic aqueous solution to obtain an arsenic concentration of 0.011 mg.
/ L, and a solution of about 5% sodium hypochlorite (manufactured by Kanto Kagaku) was added to give a concentration of 1.0 mg / L to prepare raw water. This raw water was passed by a pump at 4.2 L / min (empty cylinder speed 240 hr -1 ),
The arsenic concentration after the treatment was analyzed. As a result, the arsenic concentration of the treated water was less than 0.001 mg / L.

【0021】(実施例3)実施例1と同様に、蒸留水に
鉛水溶液として1000mg/LののICP用標準液
(硝酸性:アルドリッチ製)を鉛濃度0.031mg/
L、及び0.068mg/Lになるように調整し、ポン
プにより4.2L/min(空筒速度240hr-1)で
通水し、処理後の鉛濃度を分析した。その結果、処理水
の鉛濃度は0.005mg/L未満であった。
(Example 3) In the same manner as in Example 1, 1000 mg / L of a standard solution for ICP (nitric acid: manufactured by Aldrich) as a lead aqueous solution was added to distilled water to obtain a lead concentration of 0.031 mg / L.
L and 0.068 mg / L were adjusted, and water was passed by a pump at 4.2 L / min (empty cylinder speed 240 hr −1 ) to analyze the lead concentration after the treatment. As a result, the lead concentration of the treated water was less than 0.005 mg / L.

【0022】[0022]

【発明の効果】以上にしてなる本発明の水処理装置及び
その処理方法によれば、砒素、鉛等の有害金属が含まれ
ている原水から、これら有害金属を効果的に低減除去す
ることができ、地下水を飲料水として利用する場合には
特に有効である。
According to the water treatment apparatus and the treatment method thereof of the present invention as described above, it is possible to effectively reduce and remove these harmful metals from raw water containing harmful metals such as arsenic and lead. This is especially effective when groundwater is used as drinking water.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の水処理装置の一態様を示す断面図であ
る。
FIG. 1 is a cross-sectional view showing one embodiment of a water treatment device of the present invention.

【符号の説明】[Explanation of symbols]

10 ハウジング 11 本体 12 キャップ 12a 流入口 13 キャップ 13a 流出口 21 第一の砂層 22 活性炭層 23 第二の砂層 24 泰澄石層 25 第一の磁鉄鉱石層 26 セラミック層 27 第二の磁鉄鉱石層 28 麦飯石層 31 穴明きフィルター 32 不織布フィルター 33 仕切網 40−1,40−2,40−3 マグネットプレート 41 磁石 42 磁場 10 Housing 11 Main Body 12 Cap 12a Inlet 13 Cap 13a Outlet 21 First Sand Layer 22 Activated Carbon Layer 23 Second Sand Layer 24 Taisekiseki Layer 25 First Magnetite Ore Layer 26 Ceramic Layer 27 Second Magnetite Ore Layer 28 Barley Stone layer 31 Perforated filter 32 Nonwoven fabric filter 33 Partition net 40-1, 40-2, 40-3 Magnet plate 41 Magnet 42 Magnetic field

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/62 C02F 1/62 Z 1/68 510 1/68 510B 520 520P 530 530B 540 540A 540B 540F 540H 1/72 1/72 Z ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Internal reference number FI Technical display location C02F 1/62 C02F 1/62 Z 1/68 510 1/68 510B 520 520P 530 530B 540 540A 540B 540F 540F 540H 1/72 1/72 Z

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 一端及び他端にそれぞれ水の流入口及び
流出口を有する筒状のハウジング内に、少なくとも一層
の粒状セラミックスを堆積し、その粒状セラミックス層
の上下に少なくとも1個の磁石をその磁力線の向きが互
いに一致し、かつ磁力線の方向が水の流れに沿うように
配置してなるろ過層を備えた水処理装置において、 通水処理することにより、原水中の有害金属を低減除去
することを特徴とする水処理装置。
1. At least one layer of granular ceramics is deposited in a cylindrical housing having a water inlet and a water outlet at one end and the other end, respectively, and at least one magnet is provided above and below the granular ceramics layer. In a water treatment device equipped with a filtration layer in which the directions of magnetic lines of force match each other and the directions of the lines of magnetic force are arranged along the flow of water, water is treated to reduce harmful metals in raw water. A water treatment device characterized by the above.
【請求項2】 粒状セラミックスを堆積した層の上下の
少なくとも一方に磁鉄鉱石を堆積した層を介在させたこ
とを特徴とする請求項1記載の水処理装置。
2. The water treatment apparatus according to claim 1, wherein a layer of magnetite ore is interposed on at least one of the upper and lower sides of the layer of granular ceramics.
【請求項3】 有害金属が鉛であり、通水処理後の水の
鉛含有量を50ppb以下に低減することを特徴とする
請求項1又は2記載の水処理装置。
3. The water treatment apparatus according to claim 1, wherein the harmful metal is lead, and the lead content of the water after the water passage treatment is reduced to 50 ppb or less.
【請求項4】 有害金属が砒素であり、通水処理後の水
の砒素の含有量が10ppb以下に低減することを特徴
とする請求項1又は2記載の水処理装置。
4. The water treatment apparatus according to claim 1, wherein the harmful metal is arsenic, and the content of arsenic in the water after the water passage treatment is reduced to 10 ppb or less.
【請求項5】 通水処理を50hr-1から3000hr
-1の範囲の空筒速度(SV)で行うことを特徴とする請
求項1、2、3又は4記載の処理方法。
5. Water passing treatment is performed for 50 hr -1 to 3000 hr.
The processing method according to claim 1, 2, 3 or 4, wherein the processing is performed at an empty cylinder speed (SV) in the range of -1 .
【請求項6】 一端及び他端にそれぞれ水の流入口及び
流出口を有する筒状のハウジング内に、少なくとも一層
の粒状セラミックスを堆積し、その粒状セラミックス層
の上下に少なくとも1個の磁石をその磁力線の向きが互
いに一致し、かつ磁力線の方向が水の流れに沿うように
配置してなるろ過層を備えた水処理装置を用いて、 砒素が含まれる原水に酸化剤を添加した後、当該水処理
装置で通水処理して、砒素を低減除去してなることを特
徴とする水処理方法。
6. At least one layer of granular ceramics is deposited in a cylindrical housing having a water inlet and a water outlet at one end and the other end, respectively, and at least one magnet is provided above and below the granular ceramics layer. After adding an oxidizer to raw water containing arsenic using a water treatment device equipped with a filter layer in which the directions of the magnetic lines of force coincide with each other and the directions of the lines of magnetic force are arranged along the flow of water, A water treatment method characterized in that arsenic is reduced and removed by passing water through a water treatment device.
JP8495196A 1996-04-08 1996-04-08 Water treating device and treating method thereof Pending JPH09271757A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8495196A JPH09271757A (en) 1996-04-08 1996-04-08 Water treating device and treating method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8495196A JPH09271757A (en) 1996-04-08 1996-04-08 Water treating device and treating method thereof

Publications (1)

Publication Number Publication Date
JPH09271757A true JPH09271757A (en) 1997-10-21

Family

ID=13844951

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8495196A Pending JPH09271757A (en) 1996-04-08 1996-04-08 Water treating device and treating method thereof

Country Status (1)

Country Link
JP (1) JPH09271757A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000000434A1 (en) * 1998-06-26 2000-01-06 Mimi Georgieva Koleva Method and apparatus for purification and disinfection of liquids
WO2006004329A1 (en) * 2004-07-06 2006-01-12 Byung Kul Lee Water purifier
JP2006116477A (en) * 2004-10-22 2006-05-11 Miura Co Ltd Arsenic removing agent and arsenic removing method
CN1328184C (en) * 2005-04-22 2007-07-25 天津大学 Magnetictaxis bacteria separating apparatus of heavy metal ion waste water

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000000434A1 (en) * 1998-06-26 2000-01-06 Mimi Georgieva Koleva Method and apparatus for purification and disinfection of liquids
WO2006004329A1 (en) * 2004-07-06 2006-01-12 Byung Kul Lee Water purifier
US7658845B2 (en) 2004-07-06 2010-02-09 Byung Kul Lee Functional water purifier
JP2006116477A (en) * 2004-10-22 2006-05-11 Miura Co Ltd Arsenic removing agent and arsenic removing method
CN1328184C (en) * 2005-04-22 2007-07-25 天津大学 Magnetictaxis bacteria separating apparatus of heavy metal ion waste water

Similar Documents

Publication Publication Date Title
AjayKumar et al. Study of various parameters in the biosorption of heavy metals on activated sludge
Wasay et al. Adsorption of fluoride, phosphate, and arsenate ions on lanthanum‐impregnated silica gel
US7445718B2 (en) Removal of arsenic from drinking and process water
US7153435B2 (en) Magnetic process for removing heavy metals from water employing magnetites
CN109516629B (en) Electroplating wastewater zero-discharge treatment process
CA2380843A1 (en) An iron powder and sand filtration process for treatment of water contaminated with heavy metals and organic compounds
US6800204B2 (en) Composition and process for removing arsenic and selenium from aqueous solution
CN105565553A (en) Zero-emission purifying and recycling system of cyanide-containing heavy metal wastewater
US20120138530A1 (en) Method and apparatus for removing arsenic from a solution
Rao et al. Simultaneous removal of lead (II) and nitrate from water at low voltage
Peters et al. Separation of heavy metals: removal from industrial wastewaters and contaminated soil
CN103570160A (en) Device for treating high-concentration ammonia nitrogen in urine by using surfactant
WO2009121093A1 (en) Waste water treatment
JPH09271757A (en) Water treating device and treating method thereof
Kuhlmeier et al. Treatability of inorganic arsenic and organoarsenicals in groundwater
CN207468386U (en) A kind of zero-discharge treatment system of mixed electroplating wastewater
US20050016928A1 (en) Apparatus and method for water treatment by a direct co-precipitation/filtration process
CN105905952A (en) Water treatment agent and application thereof
CN106745917A (en) The process for purifying water of physics and chemistry water purifier at a kind of pickling waste waters
El‐Shoubary et al. A pilot plant to treat chromium‐contaminated groundwater
JPH04193387A (en) Method for purifying sewage
JP2005186047A (en) Method for cleaning arsenic-containing raw water
Newcombe Arsenic removal from drinking water
Lin et al. Decontamination of nitrates and nitrites in wastewater by zero-valent iron nanoparticles
Aulenbach et al. Heavy metals removal in a rapid infiltration sand column