JPH11104422A - Metallic silicon sintered filter medium and its manufacture - Google Patents
Metallic silicon sintered filter medium and its manufactureInfo
- Publication number
- JPH11104422A JPH11104422A JP27481497A JP27481497A JPH11104422A JP H11104422 A JPH11104422 A JP H11104422A JP 27481497 A JP27481497 A JP 27481497A JP 27481497 A JP27481497 A JP 27481497A JP H11104422 A JPH11104422 A JP H11104422A
- Authority
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- Japan
- Prior art keywords
- metallic silicon
- filter medium
- powder
- sintered filter
- catching
- 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.)
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Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、汚染液体を浄化す
る画期的濾過材、詳しくは、金属珪素を巧みに連続発泡
させて吸着捕捉性能を増大させ、これを汚染された河水
や湖水あるいは生活排水の浄化、更には海水浄化にまで
利用できるようにした高性能のメタリックシリコン焼結
濾過材、およびその経済的な製造方法に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an epoch-making filter material for purifying a contaminated liquid, and more particularly, to a method of continuously adsorbing metallic silicon to increase adsorption and trapping performance and contaminate river water, lake water or the like. The present invention relates to a high-performance metallic silicon sintered filter which can be used for purification of domestic wastewater and even for purification of seawater, and an economical production method thereof.
【0002】[0002]
【従来の技術】周知のとおり、従来においては不純物や
有害物質が混入した液体(特に、水)を浄化する場合に
は、活性炭、ゼオライト、活性アルミナといった多孔質
媒体やイオン交換樹脂、イオン交換膜といったポーラス
型の高分子化合物を濾材として用いて当該液体を通過接
触させ、これら濾材の空隙内に不純物や有害物質を捕捉
して液体の浄化を図っていた。2. Description of the Related Art As is well known, conventionally, when purifying a liquid (especially water) mixed with impurities and harmful substances, a porous medium such as activated carbon, zeolite and activated alumina, an ion exchange resin, and an ion exchange membrane are used. Such a porous polymer compound is used as a filter medium and the liquid is brought into contact therewith, and impurities and harmful substances are trapped in the voids of the filter medium to purify the liquid.
【0003】ところが、上記従来の濾材は、何れも不純
物・有害物質の捕捉吸着性能に偏りがあって、活性炭、
ゼオライト、活性アルミナや、イオン交換性高分子化合
物を単独で使用するだけではオールラウンドに全ての不
純物・有害物質を捕捉することができないため複数種を
組み合わせて使用しなければならず、コスト的に高価に
なるうえに、体積も大きくなって濾過装置が大型化する
という難点があった。そしてまた、イオン交換性の高分
子化合物は不純物・有害物質の捕捉性能は良好ではある
が、陽イオン交換樹脂と陰イオン交換樹脂との双方を逐
次的に使用しなければならないため効率的でなく、しか
も河水や湖水を浄化する場合のように大量の汚染水を処
理するのには不適当であった。[0003] However, all of the above-mentioned conventional filter media have a bias in the performance of capturing and adsorbing impurities and harmful substances.
Simply using zeolite, activated alumina, or an ion-exchange polymer compound alone cannot capture all impurities and harmful substances in all rounds, so multiple types must be used in combination, resulting in cost reduction. In addition to being expensive, the volume is increased and the size of the filtration device is increased. In addition, ion-exchange polymer compounds have good trapping performance of impurities and harmful substances, but they are not efficient because both cation exchange resin and anion exchange resin must be used sequentially. Moreover, it is not suitable for treating a large amount of contaminated water such as when purifying river water or lake water.
【0004】[0004]
【発明が解決しようとする課題】本発明は、従来の濾材
に前述のごとき難点があったのに鑑みて為されたもので
あって、複数種類の濾材を組み合せなくとも、有害物質
や微生物・有機物の混入した液体(例えば、汚染河水や
湖水など)を効率的に浄化できる高性能の濾材、および
その製造方法を提供することを技術的課題とする。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned drawbacks of the conventional filter media. Even if a plurality of types of filter media are not combined, harmful substances, microorganisms, It is a technical object to provide a high-performance filter medium capable of efficiently purifying a liquid (for example, polluted river water or lake water) mixed with an organic substance, and a method for producing the same.
【0005】また、本発明の他の技術的課題は、廃棄半
導体チップや半導体チップ製造工場から副産物として得
られるシリコンウェハー破損物に含まれる金属珪素を巧
みに連続発泡させて吸着性能を増大させて汚染された河
水や湖水、更に海水といった大量の汚染水を高能率に浄
化することを可能にする画期的濾材、およびその工業的
な製造方法を提供することにある。Another technical problem of the present invention is to improve the adsorption performance by skillfully and continuously foaming metallic silicon contained in discarded semiconductor chips and broken silicon wafers obtained as a by-product from a semiconductor chip manufacturing plant. It is an object of the present invention to provide an epoch-making filter medium capable of efficiently purifying a large amount of contaminated water such as polluted river water, lake water, and seawater, and an industrial production method thereof.
【0006】さらに、本発明の他の技術的課題は、不純
物や有害物質に対する吸着捕捉機能を長期に亙って発揮
して、汚染液体を安価に浄化することができる高性能に
して安価なメタリックシリコン焼結濾過材、およびその
焼結濾過材を経済的に量産することができる方法を提供
するにある。Further, another technical object of the present invention is to provide a high-performance and inexpensive metallic material capable of inexpensively purifying a contaminated liquid by exerting a function of adsorbing and trapping impurities and harmful substances over a long period of time. An object of the present invention is to provide a silicon sintered filter medium and a method capable of economically mass-producing the sintered filter medium.
【0007】[0007]
【課題を解決するために採用した手段】本発明は、上記
技術的課題を解決するために、金属珪素が連続気孔状態
に焼結して成る成形体を有害汚染物質の吸着捕捉手段を
採用することによって、汚染液体が接触通過する際に当
該メタリックシリコン気孔に含有汚染物質を強力に吸着
捕捉して除去できるようにした点に特徴がある。In order to solve the above-mentioned technical problems, the present invention employs means for adsorbing and trapping harmful pollutants on a compact formed by sintering metallic silicon into a continuous pore state. This is characterized in that the contaminant contained in the metallic silicon pores can be strongly adsorbed and captured and removed when the contaminated liquid passes through the contact.
【0008】また、本発明は、上記技術的課題を方法的
に解決する手段として、金属珪素粉中に炭粉を混入して
粘土状に捏和する捏和工程と、この捏和して得られた粘
土状物を所要形状に成形する成形工程と、こうして成形
して得られた成形粘土状物を焼成炉中で前記炭粉を燃焼
昇華させつゝ焼成し徐冷する焼成工程を採用することに
よって上記メタリックシリコン焼結濾過材を効率的かつ
経済的に量産することができる画期的方法を実現した点
に存する。[0008] The present invention also provides a means for solving the above technical problem in a method, in which a kneading step of mixing carbon powder into metal silicon powder and kneading the mixture into a clay-like form is provided. A forming step of forming the obtained clay-like material into a required shape, and a firing step of firing and sublimating the charcoal powder in a firing furnace, firing the formed clay-like material in a firing furnace, and gradually cooling. Accordingly, an epoch-making method capable of efficiently and economically mass-producing the metallic silicon sintered filtration material is realized.
【0009】[0009]
【発明の実施の形態】以下、本発明の具体的内容を実施
形態を挙げて説明してゆきたい。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The specific contents of the present invention will be described below with reference to embodiments.
【0010】本発明を具体的に適用して得られた実施形
態品を、福井県工業技術センターにおいて定性分析を行
ったところ、次段に列挙する結果が得られた。なお、同
技術センターでは、JIS Z 8830に準じて、蛍光X線分析
装置(株式会社リガク:3070E)との比例表面積/細孔
分布装置(日本ベル株式会社:BELSORP 28SA)を使用して
測定した。測定条件としては、温度 300℃、圧力 10-1m
mHg以下の減圧下、5時間を掛ける一方、吸着質および
吸着量の測定方法は「窒素、定容量法」で行い、かつ、
試料の採取量は 0.3476gであった。The qualitative analysis of the embodiment product obtained by specifically applying the present invention at the Fukui Industrial Technology Center resulted in the following results. In addition, in the same technical center, in accordance with JIS Z 8830, the measurement was performed using a proportional surface area / pore distribution device (Nippon Bell Co., Ltd .: BELSORP 28SA) with a fluorescent X-ray analyzer (Rigaku Corporation: 3070E). . Measurement conditions are as follows: temperature 300 ° C, pressure 10 -1 m
While applying 5 hours under reduced pressure of mHg or less, the measurement method of the adsorbate and the adsorption amount is performed by "nitrogen, constant volume method", and
The amount of sample collected was 0.3476 g.
【0011】 1.定性分析結果 (1) Si 82.00 wt% (9) Mn 0.078wt% (2) Na 5.4 wt% (10) Mg 0.070wt% (3) Al 4.0 wt% (11) P 0.046wt% (4) Ti 2.5 wt% (12) S 0.026wt% (5) Ag 2.3 wt% (13) Cl 0.022wt% (6) Zn 1.8 wt% (14) Ca 0.021wt% (7) Fe 1.5 wt% (15) Sr トレース (8) K 0.098wt% (16) Zr トレース 2.比表面積0.000 m2/g[0011] 1. Qualitative analysis results (1) Si 82.00 wt% (9) Mn 0.078wt% (2) Na 5.4 wt% (10) Mg 0.070wt% (3) Al 4.0 wt% (11) P 0.046wt% (4) Ti 2.5 wt% (12) S 0.026wt% (5) Ag 2.3 wt% (13) Cl 0.022wt% (6) Zn 1.8 wt% (14) Ca 0.021wt% (7) Fe 1.5 wt% (15) Sr trace ( 8) K 0.098wt% (16) Zr trace 2. Specific surface area 0.000 m 2 / g
【0012】琵琶湖湖水(平成9年6月16日:琵琶湖に
おいて採取)を試験対象とし、本実施形態品とヤシ殻活
性炭(粒状)を用いて、これらの濾材によるCOD削減
度合いの比較試験を「福井県衛生研究所」に委嘱して行
った。なお、当該琵琶湖湖水自体のCODは、6.5mg/l
であった。 a.本実施形態品(79g固形) 3.0mg/l b.ヤシ殻活性炭(約39g) 4.2mg/l (本比較試験では、工場排水試験法<JIS K 0102>に
準拠し、2Lビーカに上記琵琶湖湖水を分取して検体a
およびbを浸漬した後、6時間スターラーで攪拌のう
え、3昼夜放置後のCODを測定したものである。Lake Biwa lake water (June 16, 1997: collected at Lake Biwa) was used as a test object, and a comparative test of the COD reduction degree of these filter media using the product of the present embodiment and coconut shell activated carbon (granular) was conducted. Commissioned to the Fukui Prefectural Institute of Public Health. The COD of the lake water itself is 6.5 mg / l.
Met. a. This embodiment product (79 g solid) 3.0 mg / l b. Coconut shell activated carbon (about 39 g) 4.2 mg / l (In this comparative test, in accordance with the factory drainage test method <JIS K0102>
After the immersion of the samples (a) and (b), the COD was measured after stirring for 6 hours with a stirrer and then left for 3 days and nights.
【0013】上記本実施例品aのCOD削減率は、ヤシ
殻活性炭と比較して 1.2mg/lであるが、この差は従来水
準を大幅に打破するものとして驚異的であるとの講評を
受けた。The COD reduction rate of the product a of the present embodiment is 1.2 mg / l as compared with the coconut shell activated carbon, but it has been commented that this difference is surprising as it greatly breaks the conventional level. Received.
【0014】次に、上記実施例品を製造した工程につい
て説明する。金属珪素(JIS G 2312 MSi2)の一般サ
イズ(粒度:10〜150mm)と竹炭粉とを、前者90重量部
に対し、後者を10重量部を混合し水を加えて粘土状に
なるまで捏和した後、これを直径 10cm 、厚さが 2.5cm
の円盤型に塑形して、これを陶窯に入れ竹炭を燃焼させ
て焼成した。焼成温度は火入れから2時間で720℃上
昇させた後、1時間で720℃にまで上げ、その後、2
4時間を掛けて徐々に火力を弱めて約200℃にまで降
温させ、しかる後、116時間ほど当該陶窯内の炭酸ガ
ス雰囲気中で空冷し、焼成物を取り出した。この焼成物
が上記実施形態品(Si 82.00 wt%、Na 5.4 wt%、Al 4.0
wt%、Ti 2.5 wt%、Ag 2.3 wt%、Zn 1.8wt%、Fe 1.5 wt
%、K 0.098 wt%、Mn 0.078 wt%、Mg 0.070 wt%、 P 0.
046wt%、S 0.026 wt%、Cl 0.022 wt%、Ca 0.021 wt%、
その他 Sr 、Zr) であった。Next, a description will be given of a process of manufacturing the above-mentioned example product. Mix the general size (granularity: 10-150mm) of metallic silicon (JIS G 2312 MSi2) and bamboo charcoal powder with 90 parts by weight of the former and 10 parts by weight of the latter, add water and knead until clay-like. After that, this is 10cm in diameter, 2.5cm in thickness
This was placed in a pottery kiln and fired by burning bamboo charcoal. The firing temperature was increased by 720 ° C. in 2 hours after the burning, and then increased to 720 ° C. in 1 hour.
Over 4 hours, the heating power was gradually reduced to about 200 ° C., and then the air was cooled in a carbon dioxide atmosphere in the ceramic kiln for about 116 hours, and the fired product was taken out. This calcined product is the product of the above embodiment (Si 82.00 wt%, Na 5.4 wt%, Al 4.0
wt%, Ti 2.5 wt%, Ag 2.3 wt%, Zn 1.8 wt%, Fe 1.5 wt
%, K 0.098 wt%, Mn 0.078 wt%, Mg 0.070 wt%, P 0.
046 wt%, S 0.026 wt%, Cl 0.022 wt%, Ca 0.021 wt%,
Others were Sr and Zr).
【0015】本明細書に具体的に例示する実施形態例お
よびその製造工程は概ね上記のとおりであるが、本発明
は前述の実施形態例に限定されるものでは決してなく、
「特許請求の範囲内」において種々の変更が可能であ
る。Although the embodiments specifically illustrated in the present specification and the manufacturing steps thereof are generally as described above, the present invention is by no means limited to the above-described embodiments.
Various changes are possible within the scope of the claims.
【0016】上記した製造工程例にあっては陶窯の加熱
燃料として竹炭を用いたけれども、予め当該陶窯内に稲
藁を炭化させた黒色藁灰を収納し、その上に備長炭を入
れて燃焼させてもよく、さすれば稲藁灰に含まれる珪素
成分が焼成物に転移して良質のメタリックシリコン焼結
濾材が得られる。In the above-described example of the manufacturing process, bamboo charcoal was used as a heating fuel for the pottery kiln. However, black straw ash made by carbonizing rice straw was stored in the pottery kiln in advance, and bincho charcoal was put on top of it. It may be burned, and if it does, the silicon component contained in the rice straw ash is transferred to the fired product, and a good quality metallic silicon sintered filter medium is obtained.
【0017】また、焼成炉(陶窯)内での燃焼降下処置
による降温速度も、上記製造工程例では24時間を掛け
たが、18時間ほどでも支障はないし、炭酸ガス雰囲気
中での緩徐空冷時間も48時間でも十分の満足できる製
品が得られる。Also, in the above-described example of the manufacturing process, the cooling rate in the firing furnace (ceramic kiln) was 24 hours. However, even about 18 hours, there was no problem. A satisfactory product can be obtained even for 48 hours.
【0018】[0018]
【発明の効果】以上、実施形態を挙げて説明したとお
り、本発明のメタリックシリコン焼結濾過材は、金属珪
素が連続気孔状態に焼結して成る成形体を有害汚染物質
の吸着捕捉手段を採用したので、有害物質や微生物・有
機物の混入した液体を非常に効率的に浄化することが可
能であって、しかもそのような汚染物質に対する吸着捕
捉機能は長期に亙って保持する特性を有しているので、
環境浄化のコストダウンにも大いに役立つ。As described above with reference to the embodiments, the metallic silicon sintered filter material of the present invention provides a molded body obtained by sintering metallic silicon in a continuous pore state as a means for adsorbing and trapping harmful pollutants. Adopted, it is possible to purify liquids containing harmful substances, microbes and organic substances very efficiently, and the function of adsorbing and trapping such contaminants is maintained for a long time. So
It is also very useful for cost reduction of environmental purification.
【0019】さらに本発明のメタリックシリコン焼結濾
過材は、廃棄半導体チップや半導体チップ製造工場から
副産物として得られるシリコンウェハー破損物に含まれ
る金属珪素を原料として利用して、恰も陶器を焼成する
ごとく簡単な焼成炉で安価な炭燃料を使用して効率的に
焼成できるので、その製造コストも頗る経済である。Further, the metallic silicon sintered filter material of the present invention utilizes metallic silicon contained in waste semiconductor chips or broken silicon wafers obtained as a by-product from a semiconductor chip manufacturing plant as a raw material, as if firing ceramics. Since it can be fired efficiently using a cheap coal fuel in a simple firing furnace, the production cost is very economical.
【0020】このように本発明は、従来の濾過材におけ
る難点を殆ど完全なまでに解消することができるので、
その産業上の利用価値は非常に大きい。As described above, the present invention can almost completely eliminate the difficulties of the conventional filter media.
Its industrial utility value is very large.
Claims (5)
成形体であって、汚染液体が接触通過する際に含有汚染
物質を強力に吸着捕捉して除去することを特徴としたメ
タリックシリコン焼結濾過材。1. A metallic silicon body formed by sintering metallic silicon in a continuous pore state, wherein a metallic contaminant is strongly adsorbed and trapped to remove contaminants when the contaminant liquid passes through the metallic silicon. Sintered filter media.
%、 Tiが 2.5wt%、Agが2.3wt%、 Znが 1.8wt%、Feが1.5wt
%、および残部が不純物である請求項1記載の、メタリ
ックシリコン焼結濾過材。2. Si is 82.00 wt%, Na is 5.4 wt%, and Al is 4.0 wt%.
%, 2.5 wt% Ti, 2.3 wt% Ag, 1.8 wt% Zn, 1.5 wt% Fe
The metallic silicon sintered filter material according to claim 1, wherein% and the balance are impurities.
捏和して後、この粘土状物を所要形状に成形し、これを
焼成炉中で前記炭粉を燃焼昇華させつゝ焼成し徐冷する
ことを特徴とするメタリックシリコン焼結濾過材の製造
方法。3. Mixing carbon powder into metallic silicon powder and kneading it into a clay-like material, forming the clay-like material into a required shape, and burning and sublimating the coal powder in a firing furnace. (4) A method for producing a sintered metallic silicon filter material, characterized by firing and slow cooling.
で700〜800℃の温度で3〜4時間焼成し、しかる
後、火力を弱めながら18〜24時間で200℃程度まで降
温させ、ついで、火を落として炭酸ガスが充満する当該
炉内において48時間以上空冷して取り出すことを特徴
とする請求項3記載の、メタリックシリコン焼結濾過材
の製造方法。4. A kneaded product of metallic silicon powder and charcoal powder is fired in a firing furnace at a temperature of 700 to 800 ° C. for 3 to 4 hours, and thereafter, while heating power is reduced, about 200 ° C. for 18 to 24 hours. The method for producing a metallic silicon sintered filter material according to claim 3, wherein the temperature is lowered until the temperature falls, and then, the fire is dropped and air-cooled in the furnace filled with carbon dioxide gas for 48 hours or more.
請求項3または4記載の、メタリックシリコン焼結濾過
材の製造方法。5. The method for producing a metallic silicon sintered filter according to claim 3, wherein bamboo charcoal is used as a heating fuel for the firing furnace.
Priority Applications (1)
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JP27481497A JPH11104422A (en) | 1997-10-07 | 1997-10-07 | Metallic silicon sintered filter medium and its manufacture |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP27481497A JPH11104422A (en) | 1997-10-07 | 1997-10-07 | Metallic silicon sintered filter medium and its manufacture |
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JPH11104422A true JPH11104422A (en) | 1999-04-20 |
Family
ID=17546944
Family Applications (1)
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JP27481497A Pending JPH11104422A (en) | 1997-10-07 | 1997-10-07 | Metallic silicon sintered filter medium and its manufacture |
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Cited By (4)
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---|---|---|---|---|
JP2002079068A (en) * | 2000-09-11 | 2002-03-19 | Mikio Kobayashi | Apparatus for dispersing gas-liquid mixed fluid |
JP2002346588A (en) * | 2001-05-23 | 2002-12-03 | Hukko:Kk | Water cleaning method and water cleaning apparatus |
WO2017032713A1 (en) * | 2015-08-24 | 2017-03-02 | Wacker Chemie Ag | Sintered filter made of polycrystalline silicon |
CN118122030A (en) * | 2024-05-07 | 2024-06-04 | 广东友安应急消防科技股份有限公司 | Gas mask filter element material and manufacturing method thereof |
-
1997
- 1997-10-07 JP JP27481497A patent/JPH11104422A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002079068A (en) * | 2000-09-11 | 2002-03-19 | Mikio Kobayashi | Apparatus for dispersing gas-liquid mixed fluid |
JP2002346588A (en) * | 2001-05-23 | 2002-12-03 | Hukko:Kk | Water cleaning method and water cleaning apparatus |
WO2017032713A1 (en) * | 2015-08-24 | 2017-03-02 | Wacker Chemie Ag | Sintered filter made of polycrystalline silicon |
DE102015216144A1 (en) | 2015-08-24 | 2017-03-02 | Wacker Chemie Ag | Sintered polycrystalline silicon filter |
CN118122030A (en) * | 2024-05-07 | 2024-06-04 | 广东友安应急消防科技股份有限公司 | Gas mask filter element material and manufacturing method thereof |
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