JPH0626663B2 - Phosphorus removing material and manufacturing method thereof - Google Patents
Phosphorus removing material and manufacturing method thereofInfo
- Publication number
- JPH0626663B2 JPH0626663B2 JP20385989A JP20385989A JPH0626663B2 JP H0626663 B2 JPH0626663 B2 JP H0626663B2 JP 20385989 A JP20385989 A JP 20385989A JP 20385989 A JP20385989 A JP 20385989A JP H0626663 B2 JPH0626663 B2 JP H0626663B2
- Authority
- JP
- Japan
- Prior art keywords
- phosphorus
- water
- removing material
- phosphorus removing
- main component
- 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 - Lifetime
Links
Landscapes
- Water Treatment By Sorption (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、水中に低濃度に含まれるリンを除去するリン
除去材、特にダム,湖沼等の富栄養化の防止のために好
適なリン除去材及びその製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a phosphorus removing material for removing phosphorus contained in water at a low concentration, particularly, a phosphorus suitable for preventing eutrophication of dams, lakes and the like. The present invention relates to a removing material and a manufacturing method thereof.
近年、湖沼,海域,河川などの停滞性水域における富栄
養化が重大な社会問題となってきている。富栄養化の主
原因物質は、栄養塩あるいは有機物とみられているが、
そのうち、リンが富栄養化の制限因子の一つと言われて
いる。従って、富栄養化防止対策としては、河川に流入
する排水中のリンを除去するか、あるいは底部に蓄積す
る汚泥中のリン溶出防止策をとることなどが考えられ
る。In recent years, eutrophication in stagnant waters such as lakes, seas and rivers has become a serious social problem. The main causative agent of eutrophication is considered to be nutrient salts or organic matter,
Among them, phosphorus is said to be one of the limiting factors for eutrophication. Therefore, as measures for preventing eutrophication, it is conceivable to remove phosphorus in wastewater flowing into rivers or take measures to prevent phosphorus elution from sludge accumulated in the bottom.
水中のリンを除去する手段としては、凝集沈殿法,吸着
法,晶析脱リン法,生物脱リン法があり、また、汚泥中
のリン溶出防止手段としては、覆砂や浚渫などの方法が
ある。As means for removing phosphorus in water, there are coagulation sedimentation method, adsorption method, crystallization dephosphorization method, biological dephosphorization method, and as a means for preventing phosphorus elution in sludge, methods such as sand cover and dredging are available. is there.
しかしながら、ダム,湖沼等の富栄養化の場合のよう
に、流入する河川水のリン濃度は一般的には約0.07
mg/以下と低い濃度であるが、藻類増殖のリン濃度限
界値0.03mg/より高い値であると、貯留中に富栄
養化を生じ、放流先の水道水や養魚場等への被害や環境
への悪影響を生じている。このような場合、リン排出源
は農地,生活排水など多岐にわたっており、それぞれの
排出源に対する対策を立てにくく、河川水を直接脱リン
することが効果的であるが、このような大水量で低濃度
にリンを含有した水を脱リンすることはむずかしいと考
えられていた。However, as in the case of eutrophication in dams and lakes, the phosphorus concentration in the inflowing river water is generally about 0.07.
When the concentration is as low as mg / or less, but higher than the phosphorus concentration limit value of algae growth of 0.03 mg /, eutrophication occurs during storage, causing damage to tap water or fish farms at the discharge destination. Has a negative impact on the environment. In such a case, phosphorus sources are wide-ranging, such as farmland and domestic wastewater, and it is difficult to devise countermeasures for each source, and it is effective to directly dephosphorize river water. It has been considered difficult to dephosphorize water containing phosphorus at a concentration.
一方、汚泥中のリン溶出防止対策としての覆砂や浚渫な
どの手段は、一時的なものであり、さらに浚渫は底部汚
泥の除去に多大な費用を要すると共に、除去した汚泥の
処理,処分が厄介な問題となっていた。On the other hand, measures such as sand cover and dredging as a measure to prevent phosphorus elution in sludge are temporary, and dredging requires a great deal of cost to remove bottom sludge, and the treatment and disposal of removed sludge is also required. It was a troublesome problem.
本発明は、上記従来の問題点を解決し、特に河川水等の
大量の水中に低濃度に含まれるリンを効率的に除去し、
ダム,湖沼等の富栄養化を容易に防止することができ、
しかも、充填層形成のための強度も満足できるリン除去
材及びその製造方法を提供することを目的とするもので
ある。The present invention solves the above-mentioned conventional problems, particularly efficiently removes phosphorus contained in a low concentration in a large amount of water such as river water,
It is possible to easily prevent eutrophication of dams and lakes,
Moreover, it is an object of the present invention to provide a phosphorus removing material and a method for producing the same, which can satisfy the strength required for forming a packed bed.
本発明は、アロフェンを主成分とする物質を成形してか
ら300〜600℃で焼成してなるリン除去材であり、またア
ロフェンを主成分とする物質でリン除去材とするに際し
てアロフェンを主成分とする物質を粉砕後成形してか
ら、300〜600℃で焼成して固化することを特徴とするリ
ン除去材の製造方法でもある。The present invention is a phosphorus removing material obtained by molding a substance containing allophane as a main component and baking it at 300 to 600 ° C. It is also a method for producing a phosphorus-removing material, which comprises crushing and shaping a substance to be mentioned, and then firing and solidifying at 300 to 600 ° C.
本発明のリン除去材の原料は、アロフェンを主成分とす
る物質で、このアロフェンを主成分とする物質は、アル
ミニウムのケイ酸塩〔nSio2・Al2O3・nH2O(n=1〜2)〕
を主成分とする物質であって、火山灰源の表土中に広く
産する(関東火山灰層等)もので、天然に大量に産出さ
れ、安価で入手容易である。例えば、栃木県真岡市寺内
産出土,鹿沼産出土,大沢産出土があげられ,それらの
組成は次表の通りである。Raw materials for phosphorus removal material of the present invention, a material composed mainly of allophane, material mainly composed of this allophane, silicates aluminum [nSio 2 · Al 2 O 3 · nH 2 O (n = 1 ~ 2))
It is a substance containing as a main component and widely produced in the surface soil of the source of volcanic ash (Kanto volcanic ash layer, etc.). For example, excavations from Terauchi, Kanuma, and Osawa from Moka City, Tochigi Prefecture are listed, and their composition is as shown in the following table.
このようなアロフェンを主成分とする物質は、そのAl−
OH基がリン酸イオンの除去に寄与するものと考えられ、
ケイ素,アルミニウムの含有率が高く、かつSi/Al比の
小さなものが好適である。そして、この物質を成形して
から焼成するものであるが、多くの実験を重ねた結果、
300〜600℃で焼成すれば極めて優れたリン除去性能を示
すことと、焼成品の強度も上がり充填層の形成が安全に
行えることが確認された。 Such a substance containing allophane as a main component is
It is considered that the OH group contributes to the removal of phosphate ions,
It is preferable that the content of silicon and aluminum is high and the ratio of Si / Al is small. And, this material is molded and fired, but after many experiments,
It was confirmed that baking at 300 to 600 ° C shows extremely excellent phosphorus removal performance, and that the strength of the baked product is increased and the filling layer can be safely formed.
第1図は、それぞれリンを0.05mg/,0.1mg/
含有する液に、各種温度で焼成した鹿沼土を添加し、
30秒反応させたのちの液中のリン濃度を測定した結果
を示し、この第1図に示すように、200〜600℃で焼成し
たものが、藻類増殖のリン濃度限界値0.03mg/以
下にまでリンを除去することができ、特に300〜600℃で
焼成したものが表−1に示すように著しくリン除去能力
が向上することを確認したのである。Fig. 1 shows that phosphorus is 0.05 mg / and 0.1 mg /, respectively.
Kanuma soil that has been baked at various temperatures is added to the contained liquid,
The result of measuring the phosphorus concentration in the liquid after reacting for 30 seconds is shown, and as shown in FIG. 1, the one burned at 200 to 600 ° C. has a phosphorus concentration limit value of 0.03 mg / or less for algal growth. It was confirmed that the phosphorus can be removed up to the above, and that especially the one fired at 300 to 600 ° C. has a significantly improved phosphorus removing ability as shown in Table 1.
なお、第1表は鹿沼土を直径2cmの球状に造粒成形し 1
00〜700 ℃にて焼成した脱リン材を微粉砕し吸着テスト
した結果である。 In Table 1, Kanuma soil was granulated into a spherical shape with a diameter of 2 cm.
The results are obtained by finely pulverizing the dephosphorized material fired at 00 to 700 ° C and performing an adsorption test.
アロフェンを主成分とする物質によるリン除去の機構
は、表面に存在する官能基による吸着と考えられ、 300
〜600 ℃で焼成したものが特にリン除去能力が向上する
のは、表面の官能基が変化したためと推定される。The mechanism of phosphorus removal by substances containing allophane as the main component is thought to be adsorption by functional groups present on the surface.
It is presumed that the reason why the phosphorus removal ability is particularly improved in the one baked at ~ 600 ° C is that the functional group on the surface is changed.
このようにして、アロフェンを主成分とする物質を成形
焼成して得られたリン除去材は、例えば第2図に示すよ
うに、リン吸着塔1内に充填して充填層2を形成させる
が、この充填層2が形成できる強度がリン除去材には必
要であり、表−2に示すように前記条件とすることが肝
要である。In this way, the phosphorus removing material obtained by molding and firing the substance containing allophane as the main component is filled in the phosphorus adsorption tower 1 to form the packed layer 2 as shown in FIG. 2, for example. The phosphorus removing material must have sufficient strength to form the filling layer 2, and it is important to satisfy the above conditions as shown in Table 2.
表2より空気中,水中どちらにおいても 300〜600 ℃に
おいては他に比べて強度は極めて高い。このように実用
上、例えばダム流入水リン除去においては、ダム湖に流
入する河川に脱リン材を充填し処理するため、ハンドリ
ング面において充填材の強度が要求されても造粒成形後
300〜600 ℃にて焼成することで、リン吸着量と強度と
の向上ができることは実用面での価値が高い。 From Table 2, the strength is extremely higher in both air and water at 300 to 600 ° C than that of the others. Thus, practically, for example, when removing phosphorus in the inflow water of a dam, since the river that flows into the dam lake is filled with dephosphorization material for processing, even if the strength of the packing material is required on the handling surface, after granulation molding
It is of great practical value that the amount of phosphorus adsorbed and the strength can be improved by firing at 300 to 600 ° C.
また、このリン除去材は、多孔質であり、当初は空気を
内部に含んでいるので、浮上を防止するために透水性の
抑え部材3を設けることが好ましい。このリン吸着塔1
にリンを含有する原水を下向流で通水すると、水が充填
層2を通過する間にリンが吸着され、同時に水中の濁質
の一部も除去されながら、リンが除去された処理水が系
外へ流出する。Further, since the phosphorus removing material is porous and initially contains air therein, it is preferable to provide the water permeability suppressing member 3 in order to prevent floating. This phosphorus adsorption tower 1
When raw water containing phosphorus is passed in a downward flow, the phosphorus is adsorbed while the water passes through the packed bed 2 and, at the same time, a part of suspended matter in the water is also removed, and the treated water from which the phosphorus is removed Flows out of the system.
しかして、このような脱リン処理を継続するうちに、リ
ン除去材はリンを吸着して飽和状態になるから、吸着飽
和したリン除去材をリン吸着塔1から取り出し、アルカ
リ溶液等に浸漬することにより容易に再生される。その
場合、リン除去材を第3図に示すように、網体4内に適
当な量を充填しておけば、取り出しその他の取り扱いが
容易になる。Then, while such a dephosphorization process is continued, the phosphorus removing material adsorbs phosphorus and becomes saturated, so that the adsorption-saturated phosphorus removing material is taken out from the phosphorus adsorption tower 1 and immersed in an alkaline solution or the like. It is easily reproduced. In that case, if the phosphorus removing material is filled in the net body 4 in an appropriate amount as shown in FIG.
また、脱リンすべき原水中に多量の濁質が含まれている
時は、前記充填層2は濁質による目詰まりが生ずる。こ
れを避けるために、原料を粉砕後成形してから 300〜60
0 ℃で焼成して焼成成形品とすることが好ましい。即
ち、原料を粉砕したのち、例えば、第4図のように透水
孔5を多数有する直方体に成形して焼成したものや、第
5,6図のように透水孔5を単数又は複数有する円柱
状、あるいは第7図のように透水孔5を複数有する球形
状に成形して焼成したものが目詰まりがなく、強度的に
取扱いも便利である。When the raw water to be dephosphorized contains a large amount of suspended matter, the packed bed 2 is clogged with suspended matter. To avoid this, the raw material should be
It is preferable to calcine at 0 ° C. to obtain a calcined molded product. That is, after crushing the raw material, for example, it is molded into a rectangular parallelepiped having a large number of water permeation holes 5 as shown in FIG. 4 and fired, or a columnar shape having a single or a plurality of water permeation holes 5 as shown in FIGS. Alternatively, as shown in FIG. 7, the one formed into a spherical shape having a plurality of water permeation holes 5 and fired has no clogging and is easy to handle in terms of strength.
内径50mm,高さ1000mmのカラムに、表−3に示す
各種リン除去材を収容し、これらのカラムにそれぞれリ
ン0.07mg/,濁度50度を含有する河川水をLV
90m/日で通水した時の処理結果は表−3に示すとお
りで、本発明で得られたリン除去材は、比較例に較べて
リン除去性能が著しく良好であることを示した。A column with an inner diameter of 50 mm and a height of 1000 mm was filled with various phosphorus removal materials shown in Table-3, and the river water containing phosphorus of 0.07 mg / and turbidity of 50 degrees was LV.
The treatment results when water was passed at 90 m / day are as shown in Table 3, and it was shown that the phosphorus removing material obtained by the present invention had remarkably good phosphorus removing performance as compared with the comparative example.
〔発明の効果〕 以上述べたように本発明は、大量に入手容易なアロフェ
ンを主成分とする物質を成形してから300 〜600 ℃で焼
成して、リン除去能力の優れた成形されたリン除去材を
得ることができ、充填層の形成にも取扱いにも支障のな
い強度の脱リン材として用いられ、大量の河川水中に低
濃度に含まれるリンを効率的かつ経済的に除去すること
ができ、ダム,湖沼等の富栄養化防止に極めて有利とな
るものである。 [Effects of the Invention] As described above, according to the present invention, a large amount of an easily available substance containing allophane as a main component is molded and then fired at 300 to 600 ° C. to obtain a molded phosphorus excellent in phosphorus removing ability. It can be used as a dephosphorization material that can be used as a dephosphorization material that does not hinder the formation and handling of packed beds, and can efficiently and economically remove phosphorus contained in a large amount of river water at low concentrations. This is extremely advantageous for preventing eutrophication of dams, lakes and marshes.
第1図はアロフェンを主成分とする物質の焼成温度とリ
ン除去能力との関係を示す線図で、第2図は脱リン処理
の一例を示すリン吸着塔の説明図、第3〜7図は本発明
のリン除去材の使用形態を示す説明図である。 1……リン吸着塔、2……充填層、3……抑え部材、 4……網体、5……透水孔。FIG. 1 is a diagram showing the relationship between the burning temperature and the phosphorus removing ability of a substance containing allophane as a main component, and FIG. 2 is an explanatory diagram of a phosphorus adsorption tower showing an example of dephosphorization treatment, and FIGS. FIG. 3 is an explanatory diagram showing a usage pattern of the phosphorus removing material of the present invention. 1 ... Phosphorus adsorption tower, 2 ... Packed bed, 3 ... Suppression member, 4 ... Net, 5 ... Water permeation hole.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 平沢 泉 東京都港区港南1丁目6番27号 荏原イン フィルコ株式会社内 (72)発明者 中村 峯也 東京都港区港南1丁目6番27号 荏原イン フィルコ株式会社内 (56)参考文献 特開 昭57−24635(JP,A) 特開 昭58−177195(JP,A) 特公 昭49−9311(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Izumi Hirasawa 1-6-27 Konan Minato-ku, Tokyo Ebara In Filco Co., Ltd. (72) Minya Nakamura 1-6-27 Konan Minato-ku, Tokyo (56) References JP-A-57-24635 (JP, A) JP-A-58-177195 (JP, A) JP-B-49-9311 (JP, B2)
Claims (2)
から、300〜600℃で焼成してなるリン除去材。1. A phosphorus-removing material obtained by molding a material containing allophane as a main component and then calcining the material at 300 to 600 ° C.
材とするに際し、該物質を粉砕後成形してから、 300〜
600 ℃で焼成して固化することを特徴とするリン除去材
の製造方法。2. A material containing allophane as a main component, which is used as a phosphorus-removing material, is crushed after molding the material,
A method for producing a phosphorus removing material, which comprises baking at 600 ° C to solidify.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20385989A JPH0626663B2 (en) | 1989-08-08 | 1989-08-08 | Phosphorus removing material and manufacturing method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20385989A JPH0626663B2 (en) | 1989-08-08 | 1989-08-08 | Phosphorus removing material and manufacturing method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0368445A JPH0368445A (en) | 1991-03-25 |
| JPH0626663B2 true JPH0626663B2 (en) | 1994-04-13 |
Family
ID=16480879
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20385989A Expired - Lifetime JPH0626663B2 (en) | 1989-08-08 | 1989-08-08 | Phosphorus removing material and manufacturing method thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0626663B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1991010536A1 (en) * | 1990-01-16 | 1991-07-25 | Fanuc Ltd | Copying-speed control method |
| JP2007014923A (en) * | 2005-07-11 | 2007-01-25 | Dowa Construction Co Ltd | Phosphorus removal material |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0612692B1 (en) * | 1993-02-26 | 1999-01-20 | Createrra Inc. | Method for production of water purifying substances |
| WO2005080274A1 (en) * | 2004-02-19 | 2005-09-01 | Environment Technology Research Institute Corporation | Water purification material |
| CN114557160B (en) * | 2022-02-17 | 2023-09-05 | 江西省农业科学院土壤肥料与资源环境研究所 | South paddy field nitrogen and phosphorus loss prevention and control equipment |
-
1989
- 1989-08-08 JP JP20385989A patent/JPH0626663B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1991010536A1 (en) * | 1990-01-16 | 1991-07-25 | Fanuc Ltd | Copying-speed control method |
| JP2007014923A (en) * | 2005-07-11 | 2007-01-25 | Dowa Construction Co Ltd | Phosphorus removal material |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0368445A (en) | 1991-03-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104528868A (en) | Application of magnetic particles in in-situ treatment of eutrophic water and sedimentary phosphate | |
| WO2021054116A1 (en) | Phosphorus adsorbent | |
| CN109206148A (en) | A kind of preparation method and applications of haydite | |
| US6627083B2 (en) | Light expanded clay aggregates for phosphorous removal | |
| ES2209335T3 (en) | SOIL TREATMENT METHOD TO CONTROL THE DUST AND TO ACHIEVE THE STABILIZATION OF THE SOIL THROUGH THE APPLICATION OF WASTEWATER. | |
| CN109225126A (en) | A kind of porous phosphorus removing filtrate and preparation method thereof based on diatomite and tripoli | |
| JPH0626663B2 (en) | Phosphorus removing material and manufacturing method thereof | |
| JP5713735B2 (en) | Phosphorus adsorbent and soil conditioner or fertilizer using the same | |
| JP2009142783A (en) | Bottom mud reforming method in closed water area or tidal flat, and material for bottom mud reforming | |
| EP0938377B1 (en) | Light expanded clay aggregates for phosphorus removal | |
| JP3040097B2 (en) | Contact purification material and method for producing the same | |
| JP2001029951A (en) | Purification method of sea area with artificial coal ash zeolite | |
| JPS6322876B2 (en) | ||
| JP3103473B2 (en) | Water purification material and its production method | |
| CN100999372A (en) | Substrate formulating method for aquatic vegetation repairing | |
| JP2012091076A (en) | Functional porous body | |
| JPS63264192A (en) | Method and device for purifying sewage | |
| JP2003112044A (en) | Underwater dephosphorization material, dephosphorization method using the same, and method for producing fertilizer | |
| JP2006150172A (en) | Method for removing phosphorous and method for regenerating phosphorous adsorbent material | |
| JP2005030074A (en) | Covering sand material and covering sand method of water bottom | |
| JPH0368489A (en) | Device for removing phosphorus in water | |
| KR20020010532A (en) | Filter material for water-treating and water-treating apparatus | |
| CN115650540B (en) | A method and its application for resource treatment of eutrophic water body sludge | |
| JP3137326B2 (en) | Water purification method | |
| JP2005145771A (en) | Permeability block |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 15 Free format text: PAYMENT UNTIL: 20090413 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090413 Year of fee payment: 15 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100413 Year of fee payment: 16 |
|
| EXPY | Cancellation because of completion of term | ||
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Year of fee payment: 16 Free format text: PAYMENT UNTIL: 20100413 |