JPH08281261A - Method for removing phosphorus in river water - Google Patents
Method for removing phosphorus in river waterInfo
- Publication number
- JPH08281261A JPH08281261A JP11029095A JP11029095A JPH08281261A JP H08281261 A JPH08281261 A JP H08281261A JP 11029095 A JP11029095 A JP 11029095A JP 11029095 A JP11029095 A JP 11029095A JP H08281261 A JPH08281261 A JP H08281261A
- Authority
- JP
- Japan
- Prior art keywords
- phosphorus
- river water
- iron oxide
- river
- fine particles
- 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
Links
Landscapes
- Removal Of Specific Substances (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、シルト等の懸濁粒子を
含んだ河川水中に含まれる微量のリン酸イオンを極めて
合理的に選択除去することができる新技術に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a new technique capable of extremely reasonably selective removal of a trace amount of phosphate ions contained in river water containing suspended particles such as silt.
【0002】[0002]
【従来の技術】河川及び河川が流入する湖沼、ダム湖、
海等の富栄養化を防止するために、河川水中に含まれる
リンを除去する試みが近年始められている。従来の河川
水中のリン除去方法は、凝集沈殿装置を陸上に設置し、
河川水をポンプアップし硫酸アルミニウムなどの凝集剤
を添加してリンを凝集させた後、生成フロックを沈殿分
離する方法が知られている。しかし、この方法は化学プ
ラント的な凝集沈殿装置、ポンプ、配管、大きなポンプ
動力等が必要であり設備費、動力費が高価であるほか、
装置を設置する広いスペースが陸上に必要であるという
欠点があった。また観光地の河川からリン除去を行なお
うとする場合、このような装置を設置すると自然の景観
を損なうという欠点があった。また凝集沈殿処理にとも
なって発生する難脱水性汚泥の処理処分が必要であると
いう欠点もあった。2. Description of the Related Art Rivers and lakes, dam lakes, where rivers flow in,
In recent years, attempts have been made to remove phosphorus contained in river water in order to prevent eutrophication of the sea and the like. The conventional method for removing phosphorus in river water is to install a coagulating sedimentation device on land,
A method is known in which river water is pumped up, a flocculant such as aluminum sulfate is added to flocculate phosphorus, and then the produced flocs are separated by precipitation. However, this method requires a coagulation-sedimentation device like a chemical plant, a pump, piping, large pump power, etc., and the equipment cost and power cost are high,
There is a drawback that a large space for installing the device is required on land. In addition, when trying to remove phosphorus from a river in a tourist area, the installation of such a device has a drawback that the natural landscape is damaged. There is also a drawback that it is necessary to dispose of the hardly dehydratable sludge generated by the coagulation sedimentation treatment.
【0003】他の方法として、粒状の脱リン材(鹿沼
土、アロフェンなどを粒径数cmの粒状に成型したもの
など)を河川中に充填し河川水をこの充填部に流通させ
河川水中のリンを除去しようとの試みも行われている。
しかし豪雨時等に河川水の濁質量が急増し、この濁質に
よって脱リン材の充填部が速やかに閉塞してしまうとう
欠点があった。また脱リン材が豪雨時の河川水流量増加
時に流出してしまわないようにするために脱リン材を粒
径数センチの粒状物にしているので表面積が小さく、し
たがってリン吸着速度も小さいという欠点があった。こ
のため、大量の脱リン材を河川中に充填しなければ効果
的なリン除去が行えないという問題があった。そのため
の大量の脱リン材を製作する設備、製造コストが多額で
あるほか、大量の脱リン材を現場に輸送し、河川中に充
填する工事が煩雑であり、そのコストも多額であるとい
う欠点もあった。さらにリン除去能力が飽和に達した廃
脱リン材の処分が困難であり、廃脱リン材を新しい脱リ
ン材に交換する工事も面倒であった。As another method, a granular dephosphorization material (such as Kanuma soil or allophane molded into a granular shape having a particle size of several cm) is filled into a river, and the river water is circulated in the filled portion to collect the river water. Attempts have also been made to remove phosphorus.
However, there was a drawback that the turbid mass of the river water increased rapidly during heavy rain, and the suspended matter quickly blocked the filling part of the dephosphorizing material. In addition, since the dephosphorization material is a granular material with a particle size of several centimeters in order to prevent it from flowing out when the river water flow rate increases during heavy rainfall, the surface area is small and therefore the phosphorus adsorption rate is also low. was there. Therefore, there is a problem that effective phosphorus removal cannot be performed unless a large amount of dephosphorization material is filled into the river. In addition to the large amount of equipment and manufacturing cost for producing dephosphorization material for that purpose, the drawback is that the construction of transporting a large amount of dephosphorization material to the site and filling it into the river is complicated, and its cost is also large. There was also. Furthermore, it is difficult to dispose of the waste dephosphorization material whose phosphorus removal capacity has reached saturation, and the construction of replacing the waste dephosphorization material with a new dephosphorization material was troublesome.
【0004】[0004]
【発明が解決しようとする課題】本発明は、上記のよう
な従来技術の諸欠点を根本的に解決可能な新技術を提供
することを課題としており、凝集沈殿装置、揚水ポン
プ、配管などの全てが不要であり、さらに粒状の脱リン
材による河川水中のリン除去方法における前記の多数の
欠点が無い新技術を提供するものである。SUMMARY OF THE INVENTION An object of the present invention is to provide a new technique capable of fundamentally solving the above-mentioned drawbacks of the prior art, such as a coagulating sedimentation device, a pumping pump, and piping. The present invention provides a new technology that does not require all of the above and does not have the above-mentioned many drawbacks in the method of removing phosphorus in river water by using granular dephosphorization material.
【0005】[0005]
【課題を解決するための手段】本発明の上記課題は、本
発明の河川水中のリン除去方法によって解決される。す
なわち、リンと懸濁粒子を含有する河川水に、リン吸着
性を持つ磁性酸化鉄微粒子を添加し、該酸化鉄微粒子を
河川水と接触させた後、磁気分離すると共に河川水中の
懸濁粒子はそのまま河川の下流側に流出させることを特
徴とする河川水中のリン除去方法である。The above object of the present invention is solved by the method for removing phosphorus in river water according to the present invention. That is, magnetic iron oxide fine particles having a phosphorus adsorption property are added to river water containing phosphorus and suspended particles, and the iron oxide fine particles are brought into contact with river water, then magnetically separated and suspended particles in river water Is a method for removing phosphorus in river water, which is characterized by discharging it to the downstream side of the river as it is.
【0006】本発明の技術思想の骨子は、本発明者らが
行った実験結果から得られた新知見に基づいており、ま
た以下に述べるように河川という自然環境それ自体の現
象を利用して効果的に河川水中のリンを除去し、従来技
術の多くの欠点を完全に解決することにある。すなわ
ち、川には流れがあり、流れがあるところには攪拌、混
合、及び輸送作用がある。本発明者らはこの自然現象に
着目し、後記するような方法で作成した粒径がミクロン
オーダーの微粒子状の磁性を持つ酸化鉄系のリン吸着材
を微量河川水中に添加共存させ、微粒子状脱リン材を河
川の流れに乗って懸濁させながら数分間流下させた後、
河川の流れ自体によって磁気分離装置に流入させ、磁性
を持つ酸化鉄を磁気分離し、河川水中の懸濁粒子(土砂
に由来するシルト等)は分離せずにそのまま流出させる
ことによって、リンのみを効果的に吸着除去できること
を見出した。The essence of the technical idea of the present invention is based on the new findings obtained from the results of the experiments conducted by the present inventors. Further, as described below, the phenomenon of the natural environment itself of rivers is used. It is to effectively remove phosphorus in river water and completely solve many drawbacks of the prior art. That is, there is a flow in the river, and where there is a flow, there are stirring, mixing, and transport functions. Focusing on this natural phenomenon, the present inventors have added a trace amount of iron oxide-based phosphorus adsorbent having magnetic properties in the form of fine particles with a particle size of the order of micron, which was created by the method described below, to coexist in a small amount of river water, After dephosphorizing material is suspended in the flow of the river and flowed down for several minutes,
By flowing into the magnetic separation device by the flow of the river itself, magnetic iron oxide is magnetically separated, and suspended particles (silt etc. derived from sediment) in the river water are not separated but flowed out as it is, so that only phosphorus is contained. It was found that it can be effectively removed by adsorption.
【0007】以上の原理を図1によって説明する。図1
において5は磁気分離装置を設置して、リンを吸着した
酸化鉄系のリン吸着材を磁気的に分離する磁気分離部で
あり、通常は懸濁粒子を含有している河川の磁気分離部
5を設置した位置の上流A点において磁性酸化鉄微粒子
1を適量、含リン河川水3中に投入し、A点より磁気分
離部5に至る作用領域Bの間において含リン河川水3中
のリンのみを磁性酸化鉄微粒子1によって吸着除去す
る。実験の結果、リンを除去するに十分な微粒子状リン
除去材(磁性酸化鉄微粒子1)の添加量は極めて微量で
あり、含リン河川水3中のリン濃度が0.1mg/リッ
トル程度の場合、1〜5mg/リットル(リン除去材微
粒子1の乾燥重量として)という微量の添加で良い。微
粒子状リン除去材をA点で添加し、河川の水流に乗せて
数分間流下させた後、磁気分離装置(回転円盤型永久磁
石が好適)を備えた磁気分離部5を通過させると、含リ
ン河川水3からリンを吸着除去した含リン磁性酸化鉄微
粒子2が速やかに磁気分離される。しかして、磁気分離
部5を通過した脱リン河川水4に含まれる土砂に由来す
るシルト等の懸濁粒子はそのままで、その河川水4のリ
ン濃度が確実に0.02mg/リットル以下にまで除去
できることを見出した。磁気分離された含リン磁性酸化
鉄微粒子2は、リンを吸着しているのでこれをそのまま
山林等に散布するこによってリン肥料として有効利用で
きることもわかった。従って汚泥脱水等の汚泥処理設備
が不要であった。The above principle will be described with reference to FIG. FIG.
5 is a magnetic separation unit for magnetically separating an iron oxide-based phosphorus adsorbent that adsorbs phosphorus by installing a magnetic separation device, and is usually a magnetic separation unit for rivers containing suspended particles. An appropriate amount of magnetic iron oxide fine particles 1 is introduced into the phosphorus-containing river water 3 at the point A upstream of the position where the is installed, and phosphorus in the phosphorus-containing river water 3 is added between the action area B from the point A to the magnetic separation unit 5. Only the magnetic iron oxide fine particles 1 are adsorbed and removed. As a result of the experiment, the addition amount of the particulate phosphorus removing material (magnetic iron oxide fine particles 1) sufficient to remove phosphorus is extremely small, and the phosphorus concentration in the phosphorus-containing river water 3 is about 0.1 mg / liter. 1 to 5 mg / liter (as the dry weight of the phosphorus removing material fine particles 1) may be added in a very small amount. The particulate phosphorus removing material was added at point A, and the particulate phosphorus removing material was placed on the water flow of the river and allowed to flow down for several minutes, and then passed through the magnetic separation unit 5 equipped with a magnetic separation device (a rotary disk type permanent magnet is preferable). The phosphorus-containing magnetic iron oxide fine particles 2 from which phosphorus is adsorbed and removed from the phosphorus river water 3 are rapidly magnetically separated. Therefore, suspended particles such as silt derived from the sediment contained in the dephosphorized river water 4 that has passed through the magnetic separation unit 5 remain as they are, and the phosphorus concentration of the river water 4 is reliably reduced to 0.02 mg / liter or less. It was found that it can be removed. It was also found that the magnetically separated phosphorus-containing magnetic iron oxide fine particles 2 adsorbed phosphorus, so that the phosphorus-containing magnetic iron oxide fine particles 2 can be effectively used as a phosphorus fertilizer by spraying the phosphorus as it is on a forest or the like. Therefore, no sludge treatment equipment such as sludge dewatering was required.
【0008】本発明の微粒子状でリン吸着性の大きな磁
性酸化鉄を作成する方法を種々検討した結果、硫酸第1
鉄水溶液と硫酸第2鉄を後記特定の混合比率で混合した
溶液を水酸化ナトリウム、消石灰等でpH9〜11程度
に中和し、加温しながら攪拌すると、粒径数十ミクロン
以下のリン吸着能力が著しく大きい磁性酸化鉄が生成
し、これが河川水中のリンを除去する微粒子状リン除去
材として好適であることが判明した。As a result of various studies on the method of producing the magnetic iron oxide of the present invention in the form of fine particles and having a high phosphorus adsorption property, it was found that
A solution obtained by mixing an aqueous iron solution and ferric sulfate at a specific mixing ratio described below is neutralized with sodium hydroxide, slaked lime, etc. to a pH of about 9 to 11, and stirred while heating to adsorb phosphorus with a particle size of several tens of microns or less. It has been found that magnetic iron oxide having a remarkably large capacity is produced, which is suitable as a particulate phosphorus removing material for removing phosphorus in river water.
【0009】下記第1表に示すように、リン吸着能力の
大きな磁性酸化鉄を作成するために種々検討した結果、
従来知られている単なる磁性酸化鉄(マグネタイト)製
造法、すなわち硫酸第1鉄と硫酸第2鉄の等モル混合液
を水酸化ナトリウムによってpH10に中和する方法
は、生成した磁性酸化鉄のリン吸着性が小さく好適な条
件とはいえず、リン吸着性の大きい磁性酸化鉄を作成す
るには硫酸第1鉄よりも硫酸第2鉄を過剰に(モル比で
1以上)混合した混合液を中和することが重要であるこ
とを見出した。すなわち、リン吸着性の大きい磁性酸化
鉄の製造法を具体的に例示すると、第1表の通りであ
る。As shown in Table 1 below, as a result of various studies for preparing magnetic iron oxide having a large phosphorus adsorption capacity,
A known method for producing magnetic iron oxide (magnetite), that is, a method for neutralizing an equimolar mixture of ferrous sulfate and ferric sulfate to pH 10 with sodium hydroxide is a known method for producing phosphorus of magnetic iron oxide. In order to produce a magnetic iron oxide having a low adsorptivity and not a suitable condition and having a high phosphorus adsorptivity, a mixed solution containing ferric sulfate in excess (more than 1 in molar ratio) than ferrous sulfate is used. We have found that neutralization is important. That is, Table 1 shows a specific example of the method for producing magnetic iron oxide having a large phosphorus adsorption property.
【0010】[0010]
【表1】 [Table 1]
【0011】第1表より、リン吸着性の大きい磁性酸化
鉄を作成するには、硫酸第1鉄と硫酸第2鉄のモル比を
1:1.4〜1:2に設定するのが良いことが認められ
た。従って、磁性とリン吸着性のバランスを良くし、本
発明を有効に実施するには前記したように硫酸第1鉄よ
りも硫酸第2鉄をモル比で過剰に混合した混合液を中和
することが重要であることがわかる。From Table 1, in order to prepare a magnetic iron oxide having a large phosphorus adsorption property, it is preferable to set the molar ratio of ferrous sulfate to ferric sulfate to 1: 1.4 to 1: 2. Was confirmed. Therefore, in order to improve the balance between magnetism and phosphorus adsorptivity, and to effectively carry out the present invention, as described above, the mixture liquid in which ferric sulfate is excessively mixed in a molar ratio rather than ferrous sulfate is neutralized. It turns out that is important.
【0012】なお、河川の流れを利用して、数分間リン
除去材微粒子を川底に沈殿させずに流下させるには、酸
化鉄粒子の粒径が重要であり、粒径が数百ミクロン以上
であると、河川の流速がかなり速くない限りリン除去材
が磁気分離装置に流入する前に川底に沈殿してしまう恐
れがある。この場合には曝気を行い流動を増大させるよ
うにすると良い。なお、河川の流速が小さい場所(河口
など)では、粒径が数十ミクロンの微粒子であっても沈
殿してしまう恐れがあるのでやはり曝気等を行い攪拌す
ることが好ましい。It is to be noted that the particle size of the iron oxide particles is important in order to allow the phosphorus removal material particles to flow down for several minutes without settling on the river bottom using the flow of the river. If so, the phosphorus removal material may settle to the bottom of the river before it enters the magnetic separation device unless the flow velocity of the river is fairly high. In this case, aeration may be performed to increase the flow. In a place where the flow velocity of the river is small (such as a river mouth), even fine particles having a particle size of several tens of microns may be precipitated, so it is preferable to perform aeration and stirring.
【0013】[0013]
【実施例】以下に本発明のリン吸着性磁性酸化鉄微粒子
の製造方法及びそれを使用した水処理についての実施例
を示す。ただし、本発明の実施態様はこの説明によって
限定されるものではない。 (実施例1)自然の河川を模擬して人工水路(水深30
cm、長さ4m、幅10cm)に0.05mg/リット
ルのリンを添加した水道水を流速50cm/minで流
しながら、後述する方法で作成した磁性酸化鉄微粒子
(平均粒径10ミクロン)を5mg/リットル添加し、
水路を7分間流下させた。水路の末端に断面が5mm×
5mmの棒板状の永久磁石を5mm間隔で9本設置し
た。リン含有の磁性酸化鉄微粒子は磁気分離部に容易に
付着して除去された。磁気分離部から流出する水を採取
し、リンを分析した結果0.012mg/リットルであ
った。リン吸着能力の大きい磁性酸化鉄微粒子の作成
は、硫酸第1鉄の10%水溶液に硫酸第2鉄の20%水
溶液を等容量混合したものに水酸化ナトリウムを添加し
てpH10に中和し、80℃に加温して2時間攪拌して
作成した。EXAMPLES Examples of the method for producing the phosphorus-adsorptive magnetic iron oxide fine particles of the present invention and the water treatment using the same will be shown below. However, the embodiment of the present invention is not limited to this description. (Example 1) An artificial waterway (water depth: 30) simulating a natural river
cm, length 4 m, width 10 cm) 5 mg of magnetic iron oxide fine particles (average particle size 10 micron) prepared by the method described later while flowing tap water containing 0.05 mg / liter of phosphorus added at a flow rate of 50 cm / min. / Liter,
The water channel was allowed to flow down for 7 minutes. 5mm cross section at the end of the channel
Nine 5 mm rod-shaped permanent magnets were installed at 5 mm intervals. The phosphorus-containing magnetic iron oxide fine particles were easily attached to the magnetic separation portion and removed. Water flowing out from the magnetic separation part was collected and analyzed for phosphorus. As a result, it was 0.012 mg / liter. The preparation of magnetic iron oxide fine particles having a large phosphorus adsorption capacity was carried out by adding sodium hydroxide to a mixture of 10% aqueous solution of ferrous sulfate and 20% aqueous solution of ferric sulfate to neutralize the pH to 10, It was prepared by heating to 80 ° C. and stirring for 2 hours.
【0014】(実施例2)さらに別の実施態様として、
ダム湖に流入する河川からリンを除去する例について説
明する。図2に示すように河川に堰6を設け、堰の越流
部に回転円盤型等の磁気分離装置7を設置する。この堰
6の上流側において含リン河川水3(シルト等の懸濁粒
子を含んでいる。)中に磁性酸化鉄微粒子1を添加し、
河川の流れに乗せて数分間流下・接触させ、リンを吸着
除去する。リンを吸着した磁性酸化鉄微粒子1は、前記
の磁気分離装置7において分離され、リンが除去された
河川水(脱リン河川水4でシルト等の懸濁粒子を含んで
いる。)が堰6から下流に流出する。(Embodiment 2) As yet another embodiment,
An example of removing phosphorus from a river flowing into a dam lake will be described. As shown in FIG. 2, a weir 6 is provided in the river, and a rotating disk type magnetic separator 7 is installed in the overflow portion of the weir. On the upstream side of the weir 6, the magnetic iron oxide fine particles 1 were added to the phosphorus-containing river water 3 (containing suspended particles such as silt),
Put on the flow of a river and let it flow down and contact for several minutes to adsorb and remove phosphorus. The magnetic iron oxide fine particles 1 having adsorbed phosphorus are separated by the magnetic separation device 7 and river water from which phosphorus has been removed (the dephosphorized river water 4 contains suspended particles such as silt) is a weir 6. To the downstream.
【0015】この結果、揚水ポンプ、配管が不要にな
り、簡単な磁気分離装置を設けるだけで河川からリンを
選択的に除去できる。As a result, no pumping pump or piping is required, and phosphorus can be selectively removed from the river simply by providing a simple magnetic separator.
【0016】[0016]
【発明の効果】本発明のリン酸イオン吸着材は次の効果
がある。 河川に本発明の磁性を持つリン除去材微粒子を微量添
加し、河川自体の流れを利用して磁気分離装置を通過さ
せるという簡単な方法で、河川水中の懸濁粒子は除去せ
ずにリンだけを効果的に除去でき、従って従来技術のよ
うな凝集沈殿装置、揚水ポンプ、配管、汚泥処理施設の
全て及び大量の河川水を揚水する膨大なポンプ動力コス
トが不要になる。The phosphate ion adsorbent of the present invention has the following effects. A simple method of adding a minute amount of the magnetic phosphorus removing material fine particles of the present invention to a river and using the flow of the river itself to pass through a magnetic separation device. Therefore, all of the coagulation-sedimentation device, pumping pump, piping, sludge treatment facility and huge pump power cost for pumping a large amount of river water as in the prior art becomes unnecessary.
【0017】粒径数センチメートルもの粒状脱リン材
を河川に充填し、リンを除去する従来技術において、必
要であった粒状脱リン材の製造、製造設備、現地への輸
送、河川への充填、廃脱リン材の交換の全てが不要にな
るので著しい合理化が可能である。 河川水中の懸濁粒子は除去されないので、懸濁粒子に
よるリン除去部の閉塞トラブルが起きない。雨量が多い
場合河川水中の懸濁質量がかなり増加するが、このよう
な場合にも本発明の技術ではなんら問題ない。Granular dephosphorizing material having a particle size of several centimeters is filled in a river to remove phosphorus, which is required in the conventional technology for producing granular dephosphorizing material, manufacturing equipment, transportation to the site, and filling in a river. Since it is not necessary to replace all the waste dephosphorization material, it is possible to significantly rationalize. Since the suspended particles in the river water are not removed, the trouble of blocking the phosphorus removal part due to the suspended particles does not occur. When the amount of rainfall is large, the suspended mass in river water increases considerably, but even in such a case, the technique of the present invention causes no problem.
【0018】汚泥処理が不要であり、磁気分離された
リンを吸着した酸化鉄微粒子をスラリー状で林地に散布
して容易に処分できる。酸化鉄に吸着されたリンは植物
の肥料に利用される。No sludge treatment is required, and the iron oxide fine particles adsorbing the magnetically separated phosphorus are sprayed in the form of slurry on the forest land for easy disposal. Phosphorus adsorbed on iron oxide is used as a fertilizer for plants.
【図1】本発明の河川水中のリン除去方法の1例の原理
を示すフローダイヤグラムである。FIG. 1 is a flow diagram showing the principle of an example of a method for removing phosphorus in river water according to the present invention.
【図2】本発明の河川水中のリン除去方法を、ダム湖へ
流入河川に適用する例を示す側面説明図である。FIG. 2 is a side view showing an example in which the phosphorus removal method in river water of the present invention is applied to a river flowing into a dam lake.
1 磁性酸化鉄微粒子 2 含リン磁性酸化鉄微粒子 3 含リン河川水 4 脱リン河川水 5 磁気分離部 6 堰 7 磁気分離装置 A 微粒子投入点 B 作用領域 1 Magnetic Iron Oxide Fine Particles 2 Phosphorus-containing Magnetic Iron Oxide Fine Particles 3 Phosphorus-containing River Water 4 Dephosphorized River Water 5 Magnetic Separation Part 6 Weir 7 Magnetic Separation Device A Particle Input Point B Action Area
───────────────────────────────────────────────────── フロントページの続き (72)発明者 高田 正英 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 (72)発明者 浅井 良紀 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Masahide Takada 11-1 Haneda Asahicho, Ota-ku, Tokyo Ebara Corporation (72) Inventor Yoshinori Asai 11-11 Haneda-Asahicho, Ota-ku, Tokyo Inside the EBARA CORPORATION
Claims (1)
ン吸着性を持つ磁性酸化鉄微粒子を添加し、該酸化鉄微
粒子を河川水と接触させた後、磁気分離すると共に河川
水中の懸濁粒子はそのまま河川の下流側に流出させるこ
とを特徴とする河川水中のリン除去方法。1. A river water containing phosphorus and suspended particles is added with magnetic iron oxide fine particles having a phosphorus adsorbing property, and the iron oxide fine particles are brought into contact with river water, and then magnetic separation is carried out, and A method for removing phosphorus in river water, characterized in that suspended particles are directly discharged to the downstream side of the river.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11029095A JPH08281261A (en) | 1995-04-12 | 1995-04-12 | Method for removing phosphorus in river water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11029095A JPH08281261A (en) | 1995-04-12 | 1995-04-12 | Method for removing phosphorus in river water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08281261A true JPH08281261A (en) | 1996-10-29 |
Family
ID=14531951
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11029095A Pending JPH08281261A (en) | 1995-04-12 | 1995-04-12 | Method for removing phosphorus in river water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08281261A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003053860A1 (en) * | 2001-12-11 | 2003-07-03 | Henkel Kommanditgesellschaft Auf Aktien | Method for purifying waste water and magnetic adsorbents suited therefor |
JP2004509750A (en) * | 2000-09-26 | 2004-04-02 | バイエル アクチェンゲゼルシャフト | Contact and adsorbent particulates |
WO2008019982A1 (en) * | 2006-08-16 | 2008-02-21 | Siemens Aktiengesellschaft | Method and device for eliminating foreign matters present in dissolved form from waste water |
-
1995
- 1995-04-12 JP JP11029095A patent/JPH08281261A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004509750A (en) * | 2000-09-26 | 2004-04-02 | バイエル アクチェンゲゼルシャフト | Contact and adsorbent particulates |
WO2003053860A1 (en) * | 2001-12-11 | 2003-07-03 | Henkel Kommanditgesellschaft Auf Aktien | Method for purifying waste water and magnetic adsorbents suited therefor |
WO2008019982A1 (en) * | 2006-08-16 | 2008-02-21 | Siemens Aktiengesellschaft | Method and device for eliminating foreign matters present in dissolved form from waste water |
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