JPH09174045A - Agent for removing phosphate - Google Patents

Agent for removing phosphate

Info

Publication number
JPH09174045A
JPH09174045A JP7341204A JP34120495A JPH09174045A JP H09174045 A JPH09174045 A JP H09174045A JP 7341204 A JP7341204 A JP 7341204A JP 34120495 A JP34120495 A JP 34120495A JP H09174045 A JPH09174045 A JP H09174045A
Authority
JP
Japan
Prior art keywords
magnesium
containing mineral
porous material
dephosphorizing agent
sulfuric acid
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
JP7341204A
Other languages
Japanese (ja)
Inventor
Shinichi Kariya
信一 苅谷
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.)
Toyo Denka Kogyo Co Ltd
Original Assignee
Toyo Denka Kogyo 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 Toyo Denka Kogyo Co Ltd filed Critical Toyo Denka Kogyo Co Ltd
Priority to JP7341204A priority Critical patent/JPH09174045A/en
Publication of JPH09174045A publication Critical patent/JPH09174045A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain an agent for removing phosphates with a higher adsorption coefficient by kneading calcium carbonate, a magnesium-containing mineral immersed in a diluted sulfuric acid, a porous material for increasing the specific surface area, and a binder and forming the resultant mixture into granular bodies. SOLUTION: Calcium carbonate, a magnesium-containing mineral, a porous material for increasing the specific surface area, and a binder, which are respectively formed into powder granules are prepared and at first the powder granules of the magnesium- containing mineral are immersed in a diluted sulfuric acid to give a slurry and the other components are added to the resultant slurry and kneaded for a proper time, and then the resultant mixture is granulated into a proper size, for example about 2-3cm, using a granulating apparatus. Consequently, calcium derived from calcium carbonate is gradually dissolved as calcium sulfate due to the diluted sulfuric acid used for the treatment of the magnesiumcontaining mineral and also magnesium derived from the magnesium-containing mineral is gradually dissolved as magnesium sulfate and the calcium and the magnesium are reacted with pyrophosphoric acid and metaphosphoric acid, so that phosphates in water are made insoluble and phosphates are removed and consequently high efficiency of the removal of the phosphates can be achieved.

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、水質浄化における
脱リン用として用いる脱リン剤に関する。
TECHNICAL FIELD The present invention relates to a dephosphorizing agent used for dephosphorization in water purification.

【0002】[0002]

【従来の技術】水質浄化における脱リンについては、例
えば凝集剤を用いる方法や生物処理による方法、あるい
は吸着的に脱リン剤を用いる方法などが知られている。
この内の脱リン剤法にあっては、それに用いる脱リン剤
のリンに対する吸収係数が大きい程その効率を高めるこ
とができることは言うまでもない。換言すれば、如何に
吸収係数の大きい脱リン剤を得られるかにより、当該法
における脱リン処理の効率が決まるということである。
2. Description of the Related Art For dephosphorization in water purification, for example, a method using a flocculant, a method by biological treatment, or a method using a dephosphorizing agent by adsorption is known.
It goes without saying that the efficiency of the dephosphorizing method among these can be increased as the absorption coefficient of phosphorus of the dephosphorizing agent used therein increases. In other words, the efficiency of the dephosphorization treatment in this method is determined by how the dephosphorizing agent having a large absorption coefficient can be obtained.

【0003】[0003]

【発明が解決しようとする課題】本発明は、このような
観点からなされた研究により得られたものであり、より
吸収係数の大きい脱リン剤の提供を目的としている。
SUMMARY OF THE INVENTION The present invention is obtained by the research conducted from such a viewpoint, and an object thereof is to provide a dephosphorizing agent having a larger absorption coefficient.

【0004】[0004]

【課題を解決するための手段】本発明による脱リン剤
は、炭酸カルシウム、希硫酸に漬けたマグネシウム含有
鉱物、比表面積増加用の多孔性材、及び結合材を混練り
して粒体状に形成してなる。
The dephosphorizing agent according to the present invention is made into a granular form by kneading calcium carbonate, a magnesium-containing mineral immersed in dilute sulfuric acid, a porous material for increasing the specific surface area, and a binder. Formed.

【0005】この脱リン剤は、従来一般に用いられてい
る脱リンに比べ高い吸収係数を持つが、その主な理由と
しては以下のことが考えれる。すなわち、マグネシウム
含有鉱物の処理に用いた希硫酸により、炭酸カルシウム
からのカルシウムが硫酸カルシウムとして、またマグネ
シウム含有鉱物からのマグネシウムが硫酸マグネシウム
として徐々に溶出し、これらが水中のパラリン酸やメタ
リン酸と反応してリン酸カルシウムやリン酸水素カルシ
ウム又はリン酸マグネシウムやリン酸水素マグネシウム
などとなって水中のリン分を不溶化させることで脱リン
をなし、このような脱リン作用により、高い脱リン効率
を実現できる。
This dephosphorizing agent has a higher absorption coefficient than conventionally used dephosphorizing agents, and the main reasons are considered as follows. That is, with the dilute sulfuric acid used for the treatment of the magnesium-containing mineral, calcium from calcium carbonate is gradually eluted as calcium sulfate, and magnesium from the magnesium-containing mineral is gradually eluted as magnesium sulfate. By reacting to form calcium phosphate, calcium hydrogen phosphate, magnesium phosphate, magnesium hydrogen phosphate, etc., to insolubilize the phosphorus content in the water to achieve dephosphorization, and by such dephosphorization action, high dephosphorization efficiency is realized. it can.

【0006】このような脱リン剤については、さらに微
生物の資化として適性を持つ有機物及び微生物の繁殖に
適する細孔を有する多孔性材を加えるようにすると、上
記のような化学的脱リン作用に併せて生物的な脱リン作
用も利用することができ、さらに脱リン効率を高めるこ
とができる。
With respect to such a dephosphorizing agent, if a porous material having pores suitable for organic substances and microorganisms suitable for assimilation of microorganisms is further added, the above chemical dephosphorizing action is obtained. In addition to this, a biological dephosphorization effect can be utilized, and the dephosphorization efficiency can be further enhanced.

【0007】[0007]

【実施の形態】本発明の第1の実施形態では、それぞれ
粉粒体にした炭酸カルシウム、マグネシウム含有鉱物、
比表面積増加用の多孔性材、及び結合材を用意し、先ず
マグネシウム含有鉱物の粉粒体を希硫酸に漬けてスラリ
ー状にし、これにその他の上記成分を加えて適当な時間
混練りし、それから造粒機などを用いて例えば2〜3c
m程度の大きさの粒体状とする。このままで最終品とす
ることもできるが、必要に応じて自然乾燥なり適宜な乾
燥機で乾燥するようにしてもよい。
BEST MODE FOR CARRYING OUT THE INVENTION In the first embodiment of the present invention, calcium carbonate and magnesium-containing minerals, which are each made into powder and granules,
Prepare a porous material for increasing the specific surface area, and a binder, first dip magnesium-containing mineral powder in dilute sulfuric acid to form a slurry, and add the above-mentioned other components to this and knead for a suitable time, Then, using a granulator or the like, for example, 2-3 c
The particle size is about m. Although the final product can be used as it is, it may be naturally dried if necessary and dried by an appropriate dryer.

【0008】マグネシウム含有鉱物としては、種々のも
のを利用できるが、蛇紋岩を用いるのが特に好ましい。
また比表面積増加用の多孔性材としては、バーミキュラ
イトやゼオライトを用いるのが好ましく、通常はこれら
を併用する。また結合材としては、セメント(ポルトラ
ンドセメント)を用いるのが好ましい。
As the magnesium-containing mineral, various minerals can be used, but it is particularly preferable to use serpentine.
Vermiculite or zeolite is preferably used as the porous material for increasing the specific surface area, and these are usually used in combination. Further, it is preferable to use cement (Portland cement) as the binder.

【0009】本発明の第2の実施形態では、第1の実施
形態における成分構成に、さらに微生物の資化として適
性を持つ有機物及び微生物の繁殖に適する細孔を有する
多孔性材を加える。微生物の資化として適性を持つ有機
物としては、多糖類を多く含むもの、例えば寒天とパル
プなどの木質繊維を併せて用いるのが好ましく、この場
合、多糖類を上記したカルシウム分やマグネシウム分の
溶出速度の調整にも働かせることができ、脱リン能の長
期的安定性を高めることができる。また微生物の繁殖に
適する細孔を有する多孔性材としては、モミ殻や木炭を
用いるのが好ましく、通常はこれらを併用する。
In the second embodiment of the present invention, an organic material suitable for assimilation of microorganisms and a porous material having pores suitable for breeding of microorganisms are further added to the component constitution of the first embodiment. As an organic matter suitable for assimilation of microorganisms, those containing a large amount of polysaccharides, for example, it is preferable to use wood fibers such as agar and pulp together, in this case, the polysaccharides elute calcium and magnesium components described above. It can also be used to regulate the rate and increase the long-term stability of the dephosphorization capacity. As the porous material having pores suitable for the propagation of microorganisms, it is preferable to use fir shell or charcoal, and these are usually used together.

【0010】[0010]

【実施例】第1の実施例は、上記第1の実施形態に対応
する例で、本実施例における各成分の配合比は、炭酸カ
ルシウム;63.89 重量%、硫酸処理の蛇紋岩;3.84重量
%、バーミキュライト;0.32重量%、セメント;31.95
重量%である。硫酸処理の蛇紋岩は、規定度15の希硫
酸に1リットルにつき1.2 kgのパウダー状の蛇紋岩を
溶かして作成した。そしてこれらを混ぜ合わせて適当に
水を加えつつ適度な時間練り、それから造粒機で平均3
cm程度の径を持つ球状に造粒した。
EXAMPLES The first example is an example corresponding to the above-mentioned first embodiment, and the compounding ratio of each component in this example is as follows: calcium carbonate; 63.89% by weight; sulfuric acid-treated serpentine; 3.84% by weight. , Vermiculite; 0.32% by weight, cement; 31.95
% By weight. The sulfuric acid-treated serpentine was prepared by dissolving 1.2 kg of powdery serpentine per liter in dilute sulfuric acid having a normality of 15. Then mix these and add water appropriately and knead for a suitable time, then average 3 on a granulator.
It was granulated into a spherical shape having a diameter of about cm.

【0011】第2の実施例は、上記第2の実施形態に対
応する例で、本実施例における各成分の配合比は、炭酸
カルシウム;63.54 重量%、硫酸処理の蛇紋岩;3.82重
量%、バーミキュライト;0.31重量%、寒天;0.04重量
%、バージンパルプ;0.23重量%、モミ殻0.29重量%、
セメント;31.77 重量%である。硫酸処理の蛇紋岩は第
1の実施例と同じである。寒天とバージンパルプは、そ
れぞれ水に溶かして用いた。この場合には、寒天とバー
ジンパルプの溶解水と希硫酸を練り用の水分として適度
な時間練り、それから造粒機で第1の実施例と同様に造
粒した。
The second embodiment is an example corresponding to the above-mentioned second embodiment, and the mixing ratio of each component in this embodiment is as follows: calcium carbonate; 63.54% by weight; sulfuric acid-treated serpentine; 3.82% by weight; Vermiculite: 0.31% by weight, agar: 0.04% by weight, virgin pulp: 0.23% by weight, fir shell 0.29% by weight,
Cement; 31.77% by weight. The sulfuric acid-treated serpentine is the same as in the first embodiment. Agar and virgin pulp were each dissolved in water before use. In this case, dissolved water of agar and virgin pulp and diluted sulfuric acid were used as water for kneading for an appropriate time, and then granulated with a granulator in the same manner as in Example 1.

【0012】第3の実施例は、上記第2の実施形態に対
応する他の例で、本実施例における各成分の配合比は、
炭酸カルシウム;62.12 重量%、硫酸処理の蛇紋岩;3.
74重量%、バーミキュライト;0.31重量%、寒天;0.04
重量%、バージンパルプ;0.22重量%、木炭2.52重量
%、セメント;31.06 重量%である。この場合の造粒条
件は第2の実施例と同じである。
The third example is another example corresponding to the above second embodiment, and the compounding ratio of each component in this example is as follows.
Calcium carbonate; 62.12% by weight, sulfuric acid treated serpentine; 3.
74% by weight, vermiculite; 0.31% by weight, agar; 0.04
% By weight, virgin pulp: 0.22% by weight, charcoal: 2.52% by weight, cement: 31.06% by weight. The granulation conditions in this case are the same as those in the second embodiment.

【0013】これら各実施例で得られた脱リン剤の吸収
係数は、第1の実施例による脱リン剤が概略7000ミ
リグラム当量程度であり、第2の実施例による脱リン剤
が概略10000ミリグラム当量程度であり、第3の実
施例による脱リン剤が概略12000ミリグラム当量程
度であった。これらの吸収係数は、従来の脱リン剤が大
きくても5000ミリグラム当量程度にあるのに比べ大
幅な脱リン能の向上を示している。
The absorption coefficient of the dephosphorizing agent obtained in each of these examples is about 7,000 milligram equivalent for the dephosphorizing agent according to the first example, and about 10000 mg for the dephosphorizing agent according to the second example. The dephosphorizing agent according to the third example was about 12000 mg equivalent. These absorption coefficients show a significant improvement in the dephosphorization ability as compared with the conventional dephosphorizing agent having a large amount of about 5000 mg.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 炭酸カルシウム、希硫酸に漬けたマグネ
シウム含有鉱物、比表面積増加用の多孔性材、及び結合
材を混練りして粒体状に形成してなる脱リン剤。
1. A dephosphorizing agent formed by kneading calcium carbonate, a magnesium-containing mineral immersed in dilute sulfuric acid, a porous material for increasing the specific surface area, and a binder to form a granular form.
【請求項2】 微生物のための資化適性を持つ有機物、
及び微生物の繁殖に適する細孔を有する多孔性材をさら
に加えるようにした請求項1に記載の脱リン剤。
2. An organic substance having an assimilation suitability for microorganisms,
The dephosphorizing agent according to claim 1, further comprising a porous material having pores suitable for propagation of microorganisms.
【請求項3】 マグネシウム含有鉱物として蛇紋岩を用
いた請求項1に記載の脱リン剤。
3. The dephosphorizing agent according to claim 1, wherein serpentine is used as the magnesium-containing mineral.
【請求項4】 比表面積増加用の多孔性材としてバーミ
キュライト又はゼオライト、又はバーミキュライトとゼ
オライトを用いた請求項1に記載の脱リン剤。
4. The dephosphorizing agent according to claim 1, wherein vermiculite or zeolite, or vermiculite and zeolite are used as the porous material for increasing the specific surface area.
【請求項5】 結合材としてセメントを用い請求項1に
記載の脱リン剤。
5. The dephosphorizing agent according to claim 1, wherein cement is used as a binder.
【請求項6】 微生物のための資化適性を持つ有機物と
して寒天と木質繊維を用いた請求項2に記載の脱リン
剤。
6. The dephosphorizing agent according to claim 2, wherein agar and wood fiber are used as the organic substances having an assimilation suitability for microorganisms.
【請求項7】 微生物の繁殖に適する細孔を有する多孔
性材としてモミ殻又は木炭、又はモミ殻と木炭を用いた
請求項2に記載の脱リン剤。
7. The dephosphorizing agent according to claim 2, wherein fir shell or charcoal or fir shell and charcoal is used as the porous material having pores suitable for propagation of microorganisms.
JP7341204A 1995-12-27 1995-12-27 Agent for removing phosphate Pending JPH09174045A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7341204A JPH09174045A (en) 1995-12-27 1995-12-27 Agent for removing phosphate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7341204A JPH09174045A (en) 1995-12-27 1995-12-27 Agent for removing phosphate

Publications (1)

Publication Number Publication Date
JPH09174045A true JPH09174045A (en) 1997-07-08

Family

ID=18344187

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7341204A Pending JPH09174045A (en) 1995-12-27 1995-12-27 Agent for removing phosphate

Country Status (1)

Country Link
JP (1) JPH09174045A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005193078A (en) * 2003-12-26 2005-07-21 Mitsubishi Shoji Construction Materials Corp Phosphorus removing agent
JP2010179213A (en) * 2009-02-04 2010-08-19 Eco Earth Engineering Kk Method and facility for purifying pollutant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005193078A (en) * 2003-12-26 2005-07-21 Mitsubishi Shoji Construction Materials Corp Phosphorus removing agent
JP4565836B2 (en) * 2003-12-26 2010-10-20 三菱商事建材株式会社 Phosphorus remover
JP2010179213A (en) * 2009-02-04 2010-08-19 Eco Earth Engineering Kk Method and facility for purifying pollutant

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