JPH05192567A - Filter medium and production thereof - Google Patents

Filter medium and production thereof

Info

Publication number
JPH05192567A
JPH05192567A JP35821891A JP35821891A JPH05192567A JP H05192567 A JPH05192567 A JP H05192567A JP 35821891 A JP35821891 A JP 35821891A JP 35821891 A JP35821891 A JP 35821891A JP H05192567 A JPH05192567 A JP H05192567A
Authority
JP
Japan
Prior art keywords
oil
filter medium
waste material
water
mixed
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
JP35821891A
Other languages
Japanese (ja)
Inventor
Hiroshi Imai
弘 今井
Hiroshi Nishio
広志 西尾
Fumihiro Azeta
文博 畦田
Kazuo Tanaka
一男 田中
Tatsuo Ono
龍生 尾野
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.)
ANDO TEKKOSHO KK
KUNNETSUPU SEKKAI KOGYO KK
Original Assignee
ANDO TEKKOSHO KK
KUNNETSUPU SEKKAI KOGYO KK
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 ANDO TEKKOSHO KK, KUNNETSUPU SEKKAI KOGYO KK filed Critical ANDO TEKKOSHO KK
Priority to JP35821891A priority Critical patent/JPH05192567A/en
Publication of JPH05192567A publication Critical patent/JPH05192567A/en
Pending legal-status Critical Current

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  • Water Treatment By Sorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To make it possible to perform filtration at a high rate and to reuse it when used as a filter medium by forming a porous granules with a mixture of magnesium oxide and powdering org. waste material. CONSTITUTION:Magnesium, a powdering org. waste material, (e.g. a plastic waste material) and a granulating agent (e.g. bentonite) are mixed, granulated and fired to make it porous. As the result, it is used as a filter medium for removing inclusions, oils etc., in a liq. to make it possible to perform filtration at a high rate and to use it again.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、液体中に含まれる異物
としての油等(以下「油等」という)の濾過を行うため
の濾過材及びその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 a filter material for filtering oil or the like (hereinafter referred to as "oil or the like") as foreign matter contained in a liquid and a method for producing the same.

【0002】[0002]

【従来の技術】養殖漁場、水産加工場の排水には有機性
の不純物や脂肪が多く含まれているが、これを放置する
と微生物が発生し悪臭を放つ。
2. Description of the Related Art Wastewater from aquaculture fisheries and fisheries processing plants contains a large amount of organic impurities and fats. If left untreated, microorganisms will be generated and give off a foul odor.

【0003】さらに、機械工作メーカー及び各種工場や
ガソリンスタンド、洗車場の排水に含まれる油類は、そ
れぞれ河川への流入に対する防止策を講じてはいるもの
の、完全に除去されるには至っていない。
Further, although the oils contained in the drains of machine tool manufacturers, various factories, gas stations, and car washes have taken preventive measures against their inflow into rivers, they have not been completely removed. ..

【0004】これらは河川より海へ流出し、将来、海の
環境汚染の原因となることが予測される。
It is expected that these will flow out of the river into the sea and cause environmental pollution of the sea in the future.

【0005】また、機械工作メーカーで切削加工時に使
用されている切削油(クーラント)は、金属の切削加工
の過程で、被加工金属部材(ワーク)の表面に付着した
潤滑油や金属粉が混入した状態でリサイクル槽に集めら
れる。これを長時間放置すると、潤滑油の脂肪酸にバク
テリアが繁殖し、悪臭を放ち再利用出来ないため、切削
油として再利用するためには、潤滑油の除去が必要とな
るとともに、切削加工の障害となる金属粉の除去も必要
である。
Further, the cutting oil (coolant) used in the cutting process by the machine tool manufacturer is mixed with the lubricating oil and the metal powder adhered to the surface of the metal member (workpiece) to be processed in the process of cutting the metal. It is collected in the recycling tank in the state of being. If this is left for a long time, bacteria will grow in the fatty acid of the lubricating oil, and it will give off a bad odor and cannot be reused.Therefore, in order to reuse it as cutting oil, it is necessary to remove the lubricating oil as well as damage to the cutting process. It is also necessary to remove the metal powder that becomes

【0006】一方、プラスチック製品、発泡スチロール
製品等の有機廃棄物は、年々増加の一途を辿りごみ処理
場ではその処理に苦慮している。
On the other hand, the amount of organic wastes such as plastic products and styrofoam products has been increasing year by year, and it is difficult to dispose of them at the waste treatment plant.

【0007】最近、これらの廃棄物を回収して粉砕、溶
融、そして成形し、再利用を目的として、外国への輸出
や再製品化が試みられているが、廃棄される量が多すぎ
るために再生原料の供給過剰となり、用途の開発が求め
られている。
Recently, it has been attempted to export or remanufacture these wastes to foreign countries for the purpose of recovering, crushing, melting, shaping, and reusing them, but the amount of waste is too large. Due to the excessive supply of recycled raw materials, development of applications is required.

【0008】また、石炭の需要は、石油の輸入量の増加
に伴い減少の一途を辿り、今では少数の炭鉱が需要の開
発を模索しながら採炭を続けている。しかし、選炭工場
行程で排出される、不純物の混じったカロリーの少ない
微粉炭は、全く用途がなく産業廃棄物として捨てられて
いるのが現状である。
[0008] Further, the demand for coal has been declining steadily with the increase in the import amount of oil, and now a small number of coal mines are continuing to collect coal while seeking to develop the demand. However, the current situation is that pulverized coal containing impurities and low in calories discharged in the process of a coal preparation plant has no use and is discarded as industrial waste.

【0009】[0009]

【発明が解決しようとする課題】従来、液体中に混入し
た油を除去するための吸着材には、樹皮を粉砕しこれに
吸油加工を施したもの、珪石と粘土を混合焼成後、粉砕
し疎水加工したもの(特開昭55−7549)等が知ら
れているが、前者は微粉末であり取扱づらく、濾過材と
して用いるより、水の表面や地表の表面に拡散した油の
吸着を目的としており、吸油後はごみとして捨てるか、
もしくは焼却しなければならず、吸着材自体は再利用で
きない。
Conventionally, an adsorbent for removing oil mixed in a liquid has been obtained by crushing bark and subjecting it to oil absorption processing. After mixing and burning silica stone and clay, crushing is performed. Hydrophobized ones (Japanese Patent Laid-Open No. 55-7549) and the like are known, but the former is a fine powder and is difficult to handle, and the purpose is to adsorb oil diffused on the surface of water or the surface of the ground rather than being used as a filter medium. After oil absorption, do you throw it as garbage,
Or it must be incinerated and the adsorbent itself cannot be reused.

【0010】後者は焼成後粉砕しているため製品の取扱
中に粉分が多く発生し、切削油を濾過した場合、濾過材
の粉が混ざり機械工作の障害となり、切削油として再利
用ができない。この濾過材は、吸油後は前者の場合と同
じくごみとなり、放置すると潤滑油に発生したバクテリ
アにより悪臭を放つ。その結果、廃棄物処理業者に処理
を委託しなければならず、使用した後にも処理費用を要
するため、結果的にコストの高い濾過材となってしま
う。
Since the latter is crushed after firing, a large amount of powder is generated during the handling of the product, and when the cutting oil is filtered, the powder of the filter material is mixed and it interferes with the machine work and cannot be reused as the cutting oil. .. After the oil is absorbed, this filter material becomes dust like the former case, and when left unattended, it gives off a bad odor due to the bacteria generated in the lubricating oil. As a result, it is necessary to outsource the treatment to a waste treatment company, and treatment costs are required even after use, resulting in a high-cost filter material.

【0011】本発明はかかる問題を解決し、廃棄物を有
効に活用して、あらゆる不純物を含んだ液体を濾過する
ことができ、使用後は不純物を焼却することにより再使
用可能な濾過材を提供することを目的としている。
The present invention solves such a problem, and by effectively utilizing waste, it is possible to filter a liquid containing all impurities, and a filter material that can be reused by incinerating the impurities after use is provided. It is intended to be provided.

【0012】[0012]

【課題を解決するための手段】本発明によれば、上記目
的は、濾過材に関しては、酸化マグネシウムと粉状の有
機廃材の混合物で、多孔質の粒状体を成していることに
より達成される。
According to the present invention, the above-mentioned object is achieved by forming a porous granular material with a mixture of magnesium oxide and powdery organic waste material as to the filtering material. It

【0013】また、上記濾過材の製造方法に関しては、
酸化マグネシウムに粉粒状の有機廃材を造粒剤を共に混
合し、造粒して粒状化した後に焼成して多孔質化するこ
とにより達成される。
Further, regarding the method for producing the above-mentioned filter material,
This is accomplished by mixing magnesium oxide with a granular organic waste material together with a granulating agent, granulating and granulating, and then firing to make it porous.

【0014】[0014]

【作用】本発明の濾過材は、製造過程において、造粒後
に焼成される際に、有機廃材が燃焼あるいは揮撥してし
まうために、多孔質状となる。
The filter material of the present invention is porous because the organic waste material burns or volatilizes when it is fired after granulation in the manufacturing process.

【0015】したがって、これを濾過材として使用した
場合、多孔質であるが故に、液体中の油等のための吸着
空間そして接触面積を大きく確保でき、濾過時に油を付
着せしめる。
Therefore, when this is used as a filtering material, it is possible to secure a large adsorption space and a contact area for oil and the like in the liquid because it is porous, so that the oil adheres during filtration.

【0016】濾過材の再利用のためには、油等を燃焼さ
せて除去し、濾過材として繰り返し使用可能となる。
In order to reuse the filter medium, oil or the like is burned to be removed, and the filter medium can be repeatedly used.

【0017】なお、本発明の濾過材に撥水加工を施せ
ば、濾過の際に水分を吸収・付着しないので油等の濾過
効果が向上する。この撥水加工はシリコン等をコーティ
ングすることにより成される。
When the filter material of the present invention is subjected to a water repellent treatment, it does not absorb or attach water during filtration, so that the effect of filtering oil or the like is improved. This water repellent treatment is performed by coating silicon or the like.

【0018】本発明において、粒状体の形には特に限定
がなく、破壊強度を重視する分野には球状、吸着性を重
視する分野には顆粒状等とすることができる。また、造
粒剤も特に限がなく、製紙排水濃縮液、アルコール発酵
排水濃縮液、さらにはベントナイト等も使用可能であ
る。
In the present invention, the shape of the granular material is not particularly limited, and may be spherical in the field where the breaking strength is important, and granular in the field where the adsorptive property is important. Also, the granulating agent is not particularly limited, and papermaking wastewater concentrate, alcoholic fermentation wastewater concentrate, and bentonite can also be used.

【0019】[0019]

【実施例】以下、本発明の実施例について説明する。EXAMPLES Examples of the present invention will be described below.

【0020】<実施例1>酸化マグネシウム4kgに、
平均粒径が0.6mm以下となるように粉砕したプラス
チック廃材を1kg混合し、これに造粒剤として水で希
釈した製紙廃水濃縮液を1,300cc添加し十分に混
合した。
<Example 1> With 4 kg of magnesium oxide,
1 kg of a plastic waste material pulverized to have an average particle diameter of 0.6 mm or less was mixed, and 1,300 cc of a papermaking waste water concentrate diluted with water as a granulating agent was added thereto and sufficiently mixed.

【0021】この、混合した混合物を転動造粒機に投入
し造粒した。造粒された混合物を乾燥機で水分が無くな
るまで乾燥し、これを1,300°Cの雰囲気で1時間
焼成した。ここで得られた試作品を「試作品1」とし
た。
This mixed mixture was put into a rolling granulator and granulated. The granulated mixture was dried in a drier until the water content disappeared, and the mixture was calcined in an atmosphere of 1,300 ° C for 1 hour. The prototype obtained here was designated as "Prototype 1".

【0022】<実施例2>酸化マグネシウム4kgに、
平均粒径が0.6mm以下となるように粉砕したプラス
チック廃材を1kg混合し、これに造粒剤として水で希
釈した製紙廃水濃縮液を1,300cc添加し十分に混
合した。
<Example 2> With 4 kg of magnesium oxide,
1 kg of a plastic waste material pulverized to have an average particle diameter of 0.6 mm or less was mixed, and 1,300 cc of a papermaking waste water concentrate diluted with water as a granulating agent was added thereto and sufficiently mixed.

【0023】さらに混合した混合物を押し出し造粒機に
入れ、円柱状の不定形な造粒品を得た。得られた造粒品
を乾燥機で水分がなくなるまで乾燥し、これを1,30
0°Cの雰囲気で1時間焼成した。ここで得られた試作
品を「試作品2」とした。
Further, the mixed mixture was extruded and put into a granulator to obtain a columnar and irregularly shaped granulated product. The obtained granulated product is dried in a dryer until the water content disappears,
It was fired in an atmosphere of 0 ° C for 1 hour. The prototype obtained here is referred to as "Prototype 2".

【0024】<実施例3>酸化マグネシウム2.5kg
に、平均粒径が0.6mm以下となるように粉砕した石
炭粉を2.5kg混合し、これに造粒剤として水で希釈
した製紙廃水濃縮液を1,300cc添加し十分に混合
した。
<Example 3> 2.5 kg of magnesium oxide
Then, 2.5 kg of coal powder pulverized to have an average particle size of 0.6 mm or less was mixed, and 1,300 cc of a papermaking wastewater concentrate diluted with water as a granulating agent was added thereto and sufficiently mixed.

【0025】さらに混合した混合物を転動造粒機に入れ
造粒した。造粒された混合物を乾燥機で水分が無くなる
まで乾燥し、これを1,300°Cの雰囲気で1時間焼
成した。ここで得られた試作品を「試作品3」とした。
The further mixed mixture was put into a rolling granulator and granulated. The granulated mixture was dried in a drier until the water content disappeared, and the mixture was calcined in an atmosphere of 1,300 ° C for 1 hour. The prototype obtained here is referred to as "Prototype 3".

【0026】<実施例4>酸化マグネシウム2.5kg
に、平均粒径が0.6mm以下となるように粉砕した石
炭粉を2.5kg混合し、これに造粒剤として水で希釈
した製紙廃水濃縮液を1,300cc添加し十分に混合
した。
<Example 4> 2.5 kg of magnesium oxide
2.5 kg of coal powder pulverized to have an average particle size of 0.6 mm or less was mixed, and 1,300 cc of a papermaking waste water concentrate diluted with water as a granulating agent was added thereto and sufficiently mixed.

【0027】さらに混合した混合物を押し出し造粒機に
入れ、円柱状の不定形な造粒品を得た。造粒された混合
物を乾燥機で水分がなくなるまで乾燥し、これを1,3
00°Cの雰囲気で1時間焼成した。ここで得られた試
作品を「試作品4」とした。
Further, the mixed mixture was extruded and put into a granulator to obtain a columnar and irregularly shaped granulated product. The granulated mixture is dried in a dryer until the water content disappears, and this is mixed with 1,3
It was fired in an atmosphere of 00 ° C for 1 hour. The prototype obtained here was designated as "Prototype 4".

【0028】次に、かくして得られた試作品を各種試験
に供したので、その結果について説明する。
Next, the prototypes thus obtained were subjected to various tests, and the results will be described.

【0029】表1は、得られた各試作品の物性試験を行
ったもので、軽量で十分な硬度を有し開孔率が大きいた
め、吸水率、吸油率に優れていることが分かる。なお、
表1において、主な特性についての定義は次の通りであ
る。
Table 1 shows a physical property test of each of the obtained prototypes. It can be seen that the sample has excellent water absorption and oil absorption because it is lightweight, has sufficient hardness, and has a large open area ratio. In addition,
In Table 1, the definitions of the main characteristics are as follows.

【0030】真比重:1つの粒体について、多孔質開孔
を含まない濾過材そのものについての比重 嵩比重:1つの粒体の多孔質開孔を含む比重の、複数の
粒体についての平均値 充填密度:一定容量の容器に複数の粒体を充填した際の
密度 硬度:粒体に外圧を加えて破壊するときのその外圧の圧
力 開孔率:開孔を含めた濾過材の体積に対する開孔の容積
の比
True Specific Gravity: Specific Gravity of Filter Material itself without Porous Openings for One Granule Bulk Specific Gravity: Average Value of Specific Gravity of One Granule with Porous Openings for Multiple Granules Packing density: Density when a plurality of granules are packed in a container with a fixed volume Hardness: Pressure of the external pressure when the granules are broken by applying external pressure Porosity: Opening with respect to the volume of the filter medium including pores Pore volume ratio

【0031】[0031]

【表1】 表2は撥水加工を施していない試作品1と、撥水加工を
施した試作品1から4までの濾過材を漏斗に入れ、試験
溶液を上から注ぎ一度通過させた濾過試験の結果を示
し、油の分析にはn−ヘキサン抽出物質で判定した。な
お、表2において濾過率とは、混合水中の油等の量と濾
過材により除去された油等の量の比を示すものである。
[Table 1] Table 2 shows the results of the filtration test in which the water-repellent treated prototype 1 and the water-repellent treated prototypes 1 to 4 were placed in the funnel and the test solution was poured from above and passed once. The oil analysis was determined by n-hexane extract material. In Table 2, the filtration rate indicates the ratio of the amount of oil or the like in the mixed water to the amount of oil or the like removed by the filtering material.

【0032】撥水加工を施していない試作品1でも一度
の溶液通過で70%前後の潤滑油あるいは廃油の濾過が
可能で、繰り返し濾過することで完全に除去が可能であ
る。例えば、二回行えば、約90%の濾過率となる。
Even with the prototype 1 which has not been subjected to the water-repellent treatment, it is possible to filter about 70% of the lubricating oil or the waste oil by passing the solution once, and it is possible to completely remove it by repeatedly filtering. For example, if it is performed twice, the filtration rate will be about 90%.

【0033】撥水加工を施した各試作品においては、潤
滑油、廃油の除去には著しい効果を確認できた。
It was confirmed that each of the water-repellent prototypes had a remarkable effect on the removal of lubricating oil and waste oil.

【0034】[0034]

【表2】 [Table 2]

【0035】[0035]

【発明の効果】以上のように、本発明によると撥水加工
を施さない場合であっても、油等を高い率で濾過する効
果をもたらし、鉱物油のほか動物の脂肪も除去できるよ
うになった。さらに、融点の高い酸化マグネシアを用い
るので、使用済の濾過材に付着した濾過物を焼却するこ
とで、再び濾過材として繰り返し使用することが可能と
なった。
Industrial Applicability As described above, according to the present invention, even when water-repellent treatment is not applied, the effect of filtering oil and the like at a high rate can be obtained, and mineral fat as well as animal fat can be removed. became. Furthermore, since magnesia oxide having a high melting point is used, it is possible to repeatedly use it as a filter medium by incinerating the filtered material attached to the used filter medium.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 田中 一男 北海道北見市錦町173番地の60 (72)発明者 尾野 龍生 北海道北見市三輪439−1 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kazuo Tanaka 60, 173 Nishiki-cho, Kitami-shi, Hokkaido (72) Inventor Tatsuo Ono 439-1, Miwa, Kitami-shi, Hokkaido

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 酸化マグネシウムと粉状の有機廃材の混
合物で、多孔質の粒状体を成していることとする濾過
材。
1. A filter medium comprising a mixture of magnesium oxide and a powdery organic waste material, and forming a porous granular material.
【請求項2】 有機廃材はプラスチック廃材であること
とする請求項1に記載の濾過材。
2. The filtering material according to claim 1, wherein the organic waste material is a plastic waste material.
【請求項3】 有機廃材は微粉炭であることとする請求
項1に記載の濾過材。
3. The filtering material according to claim 1, wherein the organic waste material is pulverized coal.
【請求項4】 酸化マグネシウムに粉状の有機廃材を造
粒剤と共に混合し、造粒して粒状化した後に焼成して多
孔質化することとする濾過材の製造方法。
4. A method for producing a filter medium, which comprises mixing magnesium oxide with a powdery organic waste material together with a granulating agent, granulating and granulating, and then firing to make the material porous.
JP35821891A 1991-12-27 1991-12-27 Filter medium and production thereof Pending JPH05192567A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35821891A JPH05192567A (en) 1991-12-27 1991-12-27 Filter medium and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35821891A JPH05192567A (en) 1991-12-27 1991-12-27 Filter medium and production thereof

Publications (1)

Publication Number Publication Date
JPH05192567A true JPH05192567A (en) 1993-08-03

Family

ID=18458150

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35821891A Pending JPH05192567A (en) 1991-12-27 1991-12-27 Filter medium and production thereof

Country Status (1)

Country Link
JP (1) JPH05192567A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012060036A1 (en) * 2010-11-05 2012-05-10 パナソニック株式会社 Method for desalinizing salt water using desalination apparatus

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS48100391A (en) * 1972-03-31 1973-12-18
JPS5320656A (en) * 1976-08-09 1978-02-25 Mitsubishi Rayon Co Ltd Method of decoloring colored waste water
JPS53117687A (en) * 1977-03-24 1978-10-14 Toyo Soda Mfg Co Ltd Adsorbent
JPS5440291A (en) * 1977-09-06 1979-03-29 Toyo Soda Mfg Co Ltd Adsorbend composition
JPS5710793A (en) * 1980-06-25 1982-01-20 Aisin Warner Ltd Coil spring type variable capacity pump
JPS61200853A (en) * 1985-03-04 1986-09-05 Toyota Central Res & Dev Lab Inc Preparation of highly adsorbable substance
JPS6245690A (en) * 1985-08-23 1987-02-27 Agency Of Ind Science & Technol Production of gas containing hydrogen and carbon monoxide
JPH04122490A (en) * 1990-09-14 1992-04-22 Akio Onda Synthetic treatment and utilization of environmental pollutant

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS48100391A (en) * 1972-03-31 1973-12-18
JPS5320656A (en) * 1976-08-09 1978-02-25 Mitsubishi Rayon Co Ltd Method of decoloring colored waste water
JPS53117687A (en) * 1977-03-24 1978-10-14 Toyo Soda Mfg Co Ltd Adsorbent
JPS5440291A (en) * 1977-09-06 1979-03-29 Toyo Soda Mfg Co Ltd Adsorbend composition
JPS5710793A (en) * 1980-06-25 1982-01-20 Aisin Warner Ltd Coil spring type variable capacity pump
JPS61200853A (en) * 1985-03-04 1986-09-05 Toyota Central Res & Dev Lab Inc Preparation of highly adsorbable substance
JPS6245690A (en) * 1985-08-23 1987-02-27 Agency Of Ind Science & Technol Production of gas containing hydrogen and carbon monoxide
JPH04122490A (en) * 1990-09-14 1992-04-22 Akio Onda Synthetic treatment and utilization of environmental pollutant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012060036A1 (en) * 2010-11-05 2012-05-10 パナソニック株式会社 Method for desalinizing salt water using desalination apparatus
JP5045863B2 (en) * 2010-11-05 2012-10-10 パナソニック株式会社 Method of desalinating salt water using a desalination device
US8652303B2 (en) 2010-11-05 2014-02-18 Panasonic Corporation Method for desalinating saltwater with desalination device

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