JP2007313478A - Method for adsorbing/recovering phosphorous, phosphorous adsorbing/recovering device, and method for reutilizing recovered phosphorous - Google Patents

Method for adsorbing/recovering phosphorous, phosphorous adsorbing/recovering device, and method for reutilizing recovered phosphorous Download PDF

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JP2007313478A
JP2007313478A JP2006148179A JP2006148179A JP2007313478A JP 2007313478 A JP2007313478 A JP 2007313478A JP 2006148179 A JP2006148179 A JP 2006148179A JP 2006148179 A JP2006148179 A JP 2006148179A JP 2007313478 A JP2007313478 A JP 2007313478A
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purification
phosphorus
water
hollow particles
coal ash
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JP4904474B2 (en
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Isao Kawabata
功 河端
Hiroshi Saiki
博 齊木
Masao Karube
征夫 輕部
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Hokuriku Electric Power Co
National Institute of Advanced Industrial Science and Technology AIST
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National Institute of Advanced Industrial Science and Technology AIST
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Abstract

<P>PROBLEM TO BE SOLVED: To inexpensively perform purification of eutrophicated water by efficiently recovering phosphorous comprised in the eutrophicated water, and further, to effectively reutilize the recovered phosphorous. <P>SOLUTION: Eutrophicated water in a water region 12 as the object for purification is passed through the inside of a purifying/recovering device 10 installed in the outside of the system of the water region 12 as the object for purification and charged with coal ash 2 comprising hollow particles 1, thus phosphorous comprised in the eutrophicated water is adsorbed into the hollow particles 1 and is recovered to efficiently purify the eutrophicated water. In the case the hollow particles 1 reach an adsorption volume, what is necessary is to exchange only the coal ash 2 comprising the hollow particles 1 to the purifying/recovering device 10 installed in the outside of the system of the water region 12 as the object for purification. In this way, a dredging treatment is not required, thus waste sludge caused by dredging is not produced, and the treatment can be performed at a low cost. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、富栄養化水中に含まれるリンの浄化回収方法、リンの浄化回収装置および回収リンの再利用方法に関するものである。   The present invention relates to a method for purifying and recovering phosphorus contained in eutrophication water, a device for purifying and recovering phosphorus, and a method for reusing recovered phosphorus.

従来、湖沼・河川その他の閉鎖性水域における水質汚染要因の一つに、富栄養化水中に含まれるリンの溶出がある。このようなリンを確実に吸着させて富栄養化水を浄化する方法の一つとして、富栄養化水中にゼオライトなどの吸着材を投入し、富栄養化成分を吸着させた後、浚渫して水域系外に排出させる方法がある(例えば、特許文献1参照)。また、石炭灰の造粒物を湖沼などの浄化対象水域中の底部に敷設させリンを吸着させる方法がある(例えば、特許文献2参照)。   Conventionally, elution of phosphorus contained in eutrophic water is one of the water pollution factors in lakes, rivers and other closed water areas. As one of the methods for purifying eutrophication water by reliably adsorbing such phosphorus, an adsorbent such as zeolite is introduced into the eutrophication water, adsorbed the eutrophication component, and then stirred. There is a method of discharging outside the water system (for example, see Patent Document 1). In addition, there is a method in which a coal ash granulated material is laid on the bottom of a purification target water area such as a lake to adsorb phosphorus (for example, see Patent Document 2).

特開平9−310373号公報JP-A-9-310373 特開2004−113885号公報JP 2004-113985 A

しかしながら、特許文献1,2に示されるように、ゼオライトの投入や石炭灰造粒物の底部への敷設によるものは、リンの吸着容量に達した時点で吸着効果がなくなるため、ゼオライトや石炭灰造粒物などの吸着剤自体を浚渫して除去する必要があり、人件費等のコストがかかるという欠点がある。また、富栄養化水に対するリンの浄化のみを考慮したものであって、効率のよいリンの回収並びに回収したリンの有効な再利用については何ら言及されていない。   However, as shown in Patent Documents 1 and 2, when the zeolite is introduced or the bottom of the coal ash granule is laid, the adsorption effect disappears when the phosphorus adsorption capacity is reached. It is necessary to remove the adsorbent itself such as a granulated material, and there is a drawback that it costs labor costs. Moreover, it considers only the purification | cleaning of phosphorus with respect to eutrophication water, Comprising: Efficient collection | recovery of phosphorus and effective reuse of the collect | recovered phosphorus are not mentioned at all.

本発明は、上記に鑑みてなされたものであって、富栄養化水中に含まれるリンを効率よく回収して安価に富栄養化水の浄化を行うことができるとともに、回収したリンを有効に再利用することができるリンの浄化回収方法、リンの浄化回収装置および回収リンの再利用方法を提供することを目的とする。   The present invention has been made in view of the above, and is capable of efficiently recovering phosphorus contained in eutrophication water and purifying eutrophication water at low cost, and effectively recovering the recovered phosphorus. It is an object of the present invention to provide a phosphorus purification and recovery method that can be reused, a phosphorus purification and recovery device, and a method of recycling recovered phosphorus.

上述した課題を解決し、目的を達成するために、本発明に係るリンの浄化回収方法は、中空粒子を含む石炭灰が充填された浄化回収装置を浄化対象水域の系外に設置し、前記浄化対象水域の富栄養化水を前記浄化回収装置中に通水させて該富栄養化水中に含まれるリンを前記中空粒子の内部に吸着させるようにしたことを特徴とする。   In order to solve the above-described problems and achieve the object, a method for purifying and recovering phosphorus according to the present invention includes installing a purification and recovery device filled with coal ash containing hollow particles outside the system to be purified, It is characterized in that the eutrophication water in the water area to be purified is passed through the purification and recovery device so that phosphorus contained in the eutrophication water is adsorbed inside the hollow particles.

また、本発明に係る回収リンの再利用方法は、浄化対象水域の系外に設置された浄化回収装置内に充填された石炭灰中に含まれ、前記浄化対象水域の富栄養化水の通水を受けて該富栄養化水中に含まれるリンを吸着容量に達するまで内部に吸着した使用済みの中空粒子を農業用のリン肥料とすることを特徴とする。   The method for reusing recovered phosphorus according to the present invention is contained in coal ash filled in a purification and recovery device installed outside the purification target water area, and passes eutrophication water in the purification target water area. It is characterized in that used hollow particles that have received water and adsorbed phosphorus contained in the eutrophic water until the adsorption capacity is reached are used as agricultural fertilizers.

また、本発明に係るリンの浄化回収装置は、中空粒子を含む石炭灰が充填されて浄化対象水域の系外に設置される筐体を備え、該筐体内に前記浄化対象水域の富栄養化水が通水されることを特徴とする。   The phosphorus purification and recovery apparatus according to the present invention includes a casing that is filled with coal ash containing hollow particles and is installed outside the purification target water area, and the eutrophication of the purification target water area within the casing. Water is passed through.

本発明に係るリンの浄化回収方法、リンの浄化回収装置および回収リンの再利用方法によれば、石炭灰に含まれる中空粒子をリン酸液中に浸漬させた場合、リン酸イオンが中空粒子の外殻の間隙を通過して内部のカルシウムと結合することにより、リンが中空粒子の内部に吸着するという吸着メカニズムを見出し、浄化対象水域の系外に設置されて中空粒子を含む石炭灰を充填した浄化回収装置内に浄化対象水域の富栄養化水を通水させることにより、富栄養化水中に含まれるリンを中空粒子の内部に吸着させて回収することにより富栄養化水を効率よく浄化させることができ、中空粒子が吸着容量に達した場合には浄化対象水域の系外に設置された浄化回収装置に対する中空粒子を含む石炭灰のみを交換すればよく、浚渫処理が不要で浚渫による余剰汚泥が生ずることもなく、安価に処理することができるという効果を奏する。また、吸着容量に達して交換される石炭灰に含まれる中空粒子は、汚泥等を含んでおらず、リンの回収効率が高く、農業用のリン肥料として有効に再利用することができるという効果を奏する。   According to the method for purifying and recovering phosphorus according to the present invention, the device for purifying and recovering phosphorus and the method for reusing recovered phosphorus, when hollow particles contained in coal ash are immersed in a phosphoric acid solution, phosphate ions are hollow particles. The adsorption mechanism of phosphorus adsorbing inside the hollow particles is found by passing through the outer shell gap and binding with the calcium inside, and coal ash containing hollow particles is installed outside the system to be purified. By allowing eutrophication water in the water to be purified to pass through the clarified purification / collection device, phosphorus contained in the eutrophication water is adsorbed inside the hollow particles and recovered to efficiently recover the eutrophication water. When the hollow particles reach the adsorption capacity, only the coal ash containing the hollow particles for the purification and recovery device installed outside the system to be purified needs to be replaced, and no soot treatment is required. It without the excess sludge by occurs, an effect that can be processed at low cost. In addition, the hollow particles contained in the coal ash that reaches the adsorption capacity and is exchanged does not contain sludge, has high phosphorus recovery efficiency, and can be effectively reused as an agricultural phosphorus fertilizer. Play.

以下に、本発明に係るリンの浄化回収方法、リンの浄化回収装置および回収リンの再利用方法の実施の形態を図面に基づいて説明する。なお、本発明は、本実施の形態に限らず、本発明の趣旨を逸脱しない範囲であれば、種々の変形が可能である。   Embodiments of a phosphorus purification and recovery method, a phosphorus purification and recovery apparatus, and a method of reusing recovered phosphorus according to the present invention will be described below with reference to the drawings. The present invention is not limited to this embodiment, and various modifications can be made without departing from the spirit of the present invention.

本実施の形態のリンの浄化回収方法および浄化回収装置は、富栄養化水中に含まれるリンを浄化回収するための吸着剤に石炭灰を用いることを基本とする。ここで、石炭灰を用いる場合の石炭灰へのリンの吸着メカニズムについて説明する。   The phosphorus purification and recovery method and purification recovery apparatus of the present embodiment are based on using coal ash as an adsorbent for purifying and recovering phosphorus contained in eutrophication water. Here, the adsorption mechanism of phosphorus to coal ash when using coal ash will be described.

まず、図3は、従来のリン吸着のメカニズムを示す模式図である。従来のリン吸着のメカニズムは、石炭灰中に含まれるカルシウムCaがカルシウムイオンCa2+として溶解し、液中のリン酸イオンPO4 2-と結合し、液中でリン酸カルシウムCaPO4として不溶化するという認識である。このようなリン吸着のメカニズムを、富栄養化水に対するリンの浄化に利用しているものである。これは、石炭灰と接触させた水にリン酸を加えると、リン酸カルシウムが析出することにより確認できるが、このようなリン吸着のメカニズムを利用する場合、効率のよいリンの回収は困難である。 First, FIG. 3 is a schematic diagram showing a conventional mechanism of phosphorus adsorption. The conventional mechanism of phosphorus adsorption is that calcium Ca contained in coal ash dissolves as calcium ions Ca 2+ , binds to phosphate ions PO 4 2− in the liquid, and becomes insoluble in the liquid as calcium phosphate CaPO 4. It is recognition. This mechanism of phosphorus adsorption is used for purifying phosphorus with respect to eutrophication water. This can be confirmed by adding calcium phosphate to the water brought into contact with the coal ash, whereby calcium phosphate is precipitated. However, when such a phosphorus adsorption mechanism is used, efficient phosphorus recovery is difficult.

一方、図1は、本発明者らが新たに見出した石炭灰へのリン吸着のメカニズムを示す模式図である。すなわち、石炭灰、特にフライアッシュ中には図1に示すような中空粒子1が存在し、中空粒子1をリン酸液中に浸漬させた場合、液中のリン酸イオンPO4 2-が中空粒子1の外殻の間隙を通過し、中空粒子1の内部のカルシウムイオンCa2+と結合することで、リンが中空粒子1の内部に吸着するというメカニズムを見出したものである。 On the other hand, FIG. 1 is a schematic diagram showing a mechanism of phosphorus adsorption to coal ash newly found by the present inventors. That is, coal ash, in particular there is a hollow particle 1 as shown in FIG. 1 in the fly ash, when immersed hollow particles 1 in a phosphate solution, phosphate ions PO 4 2-hollow in the liquid The inventors have found a mechanism in which phosphorus is adsorbed inside the hollow particles 1 by passing through the gaps in the outer shell of the particles 1 and binding to calcium ions Ca 2+ inside the hollow particles 1.

このようなリン吸着のメカニズムは、以下の手順により確認できたものである。まず、石炭灰(フライアッシュ)を十分に洗浄し、リン酸液中に浸漬させたところ、リン酸濃度が低下した。そこで、石炭灰の表面を電子顕微鏡で確認したところ、表面にリンの存在(リンの吸着)は認められなかった。一方、石炭灰中から粒径が比較的大きい粒子を篩い分けにより分取し、電子顕微鏡で観察したところ、中空粒子が多く存在していることが確認された。そこで、中空粒子をすり潰して内部の元素分布を電子顕微鏡等で観察したところ、リン酸カルシウムの存在が確認できたものである。   Such a phosphorus adsorption mechanism has been confirmed by the following procedure. First, when the coal ash (fly ash) was thoroughly washed and immersed in a phosphoric acid solution, the phosphoric acid concentration decreased. Then, when the surface of coal ash was confirmed with an electron microscope, the presence of phosphorus (phosphorus adsorption) was not observed on the surface. On the other hand, when particles having a relatively large particle diameter were separated from the coal ash by sieving and observed with an electron microscope, it was confirmed that many hollow particles were present. Thus, when hollow particles were ground and the internal element distribution was observed with an electron microscope or the like, the presence of calcium phosphate could be confirmed.

そこで、本実施の形態のリンの浄化回収方法および浄化回収装置は、富栄養化水中に含まれるリンを浄化回収するための吸着剤として、石炭灰、特に中空粒子を含むフライアッシュを用いることを基本とする。ここで、フライアッシュは、例えば石炭火力発電所において燃焼により溶融状態となって高温燃焼ガス中を浮遊する灰の粒子が、ボイラ出口での温度低下に伴い球形微細粒子となった石炭灰の一種であり、シリカ、アルミナ等を主成分とし、電気集塵器によって捕集される。   Therefore, the purification and recovery method and the recovery device for phosphorus according to the present embodiment uses coal ash, particularly fly ash containing hollow particles, as an adsorbent for purifying and recovering phosphorus contained in eutrophication water. Basic. Here, fly ash is a kind of coal ash in which, for example, ash particles that are in a molten state by combustion in a coal-fired power plant and float in high-temperature combustion gas become spherical fine particles as the temperature decreases at the boiler outlet. It is mainly collected from silica, alumina, etc., and is collected by an electrostatic precipitator.

図2は、上記リン吸着のメカニズムを利用した本実施の形態のリンの浄化回収方法を実現するためのシステム構成例を示す模式図である。まず、石炭灰2を充填する浄化回収装置10を用意しておく。浄化回収装置10は、多数の石炭灰2を適宜充填した筐体11からなる。ここで、石炭灰2は、少なくとも中空粒子1を含むものであり、本実施の形態では、粒径が比較的大きくて大半が中空粒子1を占めるように予め篩い分けされたものが用いられる。このような浄化回収装置10を、浄化対象となる湖沼、お堀等の富栄養化水を有する閉鎖性の浄化対象水域12の系外の適宜場所に設置し、浄化対象水域12の富栄養化水をポンプ13で汲み上げて浄化回収装置10内に注水し、浄化回収装置10内に充填された中空粒子1を含む石炭灰2中を通水させ、下部側から浄化された水を排水して浄化対象水域12に還流させる。   FIG. 2 is a schematic diagram showing a system configuration example for realizing the phosphorus purification and recovery method of the present embodiment using the phosphorus adsorption mechanism. First, a purification and recovery device 10 for filling the coal ash 2 is prepared. The purification and recovery device 10 includes a housing 11 that is appropriately filled with a large number of coal ash 2. Here, the coal ash 2 includes at least the hollow particles 1. In the present embodiment, the coal ash 2 is used that has been sieved so that the particle size is relatively large and most of the hollow particles 1 are occupied. Such a purification and recovery device 10 is installed at an appropriate location outside the system of the closed purification target water area 12 having eutrophication water such as lakes and moats to be purified, and the eutrophication of the purification target water area 12 is performed. Water is pumped up by the pump 13 and poured into the purification and recovery device 10, water is passed through the coal ash 2 including the hollow particles 1 filled in the purification and recovery device 10, and the purified water is drained from the lower side. Reflux to the water area 12 to be purified.

このように浄化回収装置10中に浄化対象水域12の富栄養化水を通水させることにより、富栄養化水中に含まれるリンは、リン酸イオンとして、石炭灰2中に含まれる中空粒子1の外殻の間隙を通過し、中空粒子1の内部のカルシウムイオンと結合し、リン酸カルシウムとなって内部に吸着固定されることにより回収され、富栄養化水はリンが浄化された状態で浄化対象水域12に還流されることとなる。   As described above, the eutrophication water of the purification target water area 12 is allowed to flow through the purification / recovery device 10, so that phosphorus contained in the eutrophication water is phosphate particles and the hollow particles 1 contained in the coal ash 2. Passes through the outer shell, and binds to calcium ions inside the hollow particles 1 and is recovered by adsorbing and fixing calcium phosphate inside. The eutrophication water is purified in a state where the phosphorus is purified. It will be refluxed to the water area 12.

このように、本実施の形態のリンの浄化回収方法によれば、浄化対象水域12の系外に設置されて中空粒子1を含む石炭灰2を充填した浄化回収装置10内に浄化対象水域12の富栄養化水を通水させ、富栄養化水中に含まれるリンを中空粒子1の内部に吸着させて回収することにより富栄養化水を効率よく浄化させることができる。そして、石炭灰2中の中空粒子1が吸着容量に達した場合には浄化対象水域12の系外に設置された浄化回収装置10に対する中空粒子1を含む石炭灰2のみを交換すればよく、浚渫処理が不要で浚渫による余剰汚泥が生ずることもなく、リンの浄化回収方法を安価に実現することができる。   As described above, according to the method for purifying and recovering phosphorus according to the present embodiment, the purification target water area 12 is installed in the purification and recovery apparatus 10 that is installed outside the system to be purified 12 and is filled with the coal ash 2 including the hollow particles 1. The eutrophication water can be efficiently purified by allowing the eutrophication water to pass through and adsorbing and recovering phosphorus contained in the eutrophication water inside the hollow particles 1. And when the hollow particles 1 in the coal ash 2 reach the adsorption capacity, only the coal ash 2 containing the hollow particles 1 for the purification recovery device 10 installed outside the system 12 to be purified needs to be replaced, No soot treatment is required and no excess sludge is produced by soot, and a phosphorus purification and recovery method can be realized at low cost.

また、吸着容量に達して交換される使用済みの中空粒子1を含む石炭灰2は、汚泥等を含んでおらず、リンの回収効率が高いことから、浄化回収装置10から取り出された使用済みの中空粒子1をそのまま農業用のリン肥料として有効に再利用することが可能となる。すなわち、見た目には、表面にリンが吸着しておらず、従来の石炭灰のリン吸着のメカニズムの認識によれば廃棄処分の対象となってしまう中空粒子1をそのまま有効に再利用できるものである。   Moreover, since the coal ash 2 including the used hollow particles 1 to be exchanged after reaching the adsorption capacity does not contain sludge or the like and has a high phosphorus recovery efficiency, the used coal ash 2 that has been taken out from the purification and recovery device 10 is used. This hollow particle 1 can be effectively reused as it is as an agricultural phosphorus fertilizer. That is, it is apparent that phosphorus is not adsorbed on the surface, and the hollow particles 1 that are subject to disposal can be effectively reused as they are according to the conventional mechanism of phosphorus adsorption of coal ash. is there.

なお、本実施の形態では、予め篩い分けして中空粒子1が大半を占める石炭灰2を用いるようにしたが、事前に篩い分けせず少なくとも中空粒子1を含む石炭灰2を利用し、リン回収時に石炭灰2を篩い分けして使用済みの中空粒子1を分別してリン肥料として再利用するようにしてもよい。   In this embodiment, the coal ash 2 in which the hollow particles 1 occupy the majority is sieved in advance, but the coal ash 2 containing at least the hollow particles 1 is used without sieving in advance. The coal ash 2 may be sieved during collection to separate the used hollow particles 1 and reused as phosphorus fertilizer.

本実施の形態で利用する中空粒子へのリン吸着のメカニズムを示す模式図である。It is a schematic diagram which shows the mechanism of the phosphorus adsorption | suction to the hollow particle utilized in this Embodiment. 本実施の形態のリンの浄化回収方法を実現するためのシステム構成例を示す模式図である。It is a schematic diagram which shows the system structural example for implement | achieving the purification and collection | recovery method of phosphorus of this Embodiment. 従来認識されている石炭灰へのリン吸着のメカニズムを示す模式図である。It is a schematic diagram which shows the mechanism of the phosphorus adsorption | suction to the coal ash recognized conventionally.

符号の説明Explanation of symbols

1 中空粒子
2 石炭灰
10 浄化回収装置
11 筐体
12 浄化対象水域
DESCRIPTION OF SYMBOLS 1 Hollow particle 2 Coal ash 10 Purification | purification collection apparatus 11 Case 12 Water purifying object water area

Claims (3)

中空粒子を含む石炭灰が充填された浄化回収装置を浄化対象水域の系外に設置し、
前記浄化対象水域の富栄養化水を前記浄化回収装置中に通水させて該富栄養化水中に含まれるリンを前記中空粒子の内部に吸着させるようにしたことを特徴とするリンの浄化回収方法。
A purification and recovery device filled with coal ash containing hollow particles is installed outside the system to be purified,
Purifying and recovering phosphorus, wherein eutrophication water in the water area to be purified is passed through the purification and recovery device so that phosphorus contained in the eutrophication water is adsorbed inside the hollow particles. Method.
浄化対象水域の系外に設置された浄化回収装置内に充填された石炭灰中に含まれ、前記浄化対象水域の富栄養化水の通水を受けて該富栄養化水中に含まれるリンを吸着容量に達するまで内部に吸着した使用済みの中空粒子を農業用のリン肥料とすることを特徴とする回収リンの再利用方法。   Phosphorus contained in the coal ash filled in the purification and recovery device installed outside the system of the purification target water area, receiving eutrophication water from the purification target water area, and phosphorus contained in the eutrophication water A method for reusing recovered phosphorus, characterized in that spent hollow particles adsorbed inside until reaching the adsorption capacity are used as an agricultural phosphorus fertilizer. 中空粒子を含む石炭灰が充填されて浄化対象水域の系外に設置される筐体を備え、該筐体内に前記浄化対象水域の富栄養化水が通水されることを特徴とするリンの浄化回収装置。   It is provided with a casing that is filled with coal ash containing hollow particles and installed outside the purification target water area, and the eutrophication water of the purification target water area is passed through the casing. Purification recovery device.
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JP2009119451A (en) * 2007-11-09 2009-06-04 Hokuriku Electric Power Co Inc:The Method and apparatus for recovering phosphoric acid and method for reusing recovered phosphorus
JP2010234280A (en) * 2009-03-31 2010-10-21 Hokuriku Electric Power Co Inc:The Phosphorus adsorbent and method for manufacturing fertilizer using the same

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JPH07101717A (en) * 1993-10-06 1995-04-18 Chugoku Electric Power Co Inc:The Production of kaolin-based clay
JPH07124523A (en) * 1993-10-29 1995-05-16 Sadao Ito Classifier
JP2000176447A (en) * 1998-12-18 2000-06-27 Taiheiyo Cement Corp Water purifying tank and water purifying system using the same
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JPS61281093A (en) * 1985-06-04 1986-12-11 三菱重工業株式会社 Adsorbent treatment
JPH07101717A (en) * 1993-10-06 1995-04-18 Chugoku Electric Power Co Inc:The Production of kaolin-based clay
JPH07124523A (en) * 1993-10-29 1995-05-16 Sadao Ito Classifier
JP2000176447A (en) * 1998-12-18 2000-06-27 Taiheiyo Cement Corp Water purifying tank and water purifying system using the same
JP2001129562A (en) * 1999-11-08 2001-05-15 Natl Inst Of Advanced Industrial Science & Technology Meti Phosphorus removing method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009119451A (en) * 2007-11-09 2009-06-04 Hokuriku Electric Power Co Inc:The Method and apparatus for recovering phosphoric acid and method for reusing recovered phosphorus
JP2010234280A (en) * 2009-03-31 2010-10-21 Hokuriku Electric Power Co Inc:The Phosphorus adsorbent and method for manufacturing fertilizer using the same

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