JP4589544B2 - Heavy metal elution reducing material - Google Patents
Heavy metal elution reducing material Download PDFInfo
- Publication number
- JP4589544B2 JP4589544B2 JP2001037393A JP2001037393A JP4589544B2 JP 4589544 B2 JP4589544 B2 JP 4589544B2 JP 2001037393 A JP2001037393 A JP 2001037393A JP 2001037393 A JP2001037393 A JP 2001037393A JP 4589544 B2 JP4589544 B2 JP 4589544B2
- Authority
- JP
- Japan
- Prior art keywords
- heavy metal
- reducing
- reducing material
- metal elution
- elution
- 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 - Fee Related
Links
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
【０００１】
【発明の属する技術分野】
本発明は、有害な重金属を含有する廃棄物、汚泥、土壌等からの重金属の溶出を低減することのできる重金属溶出低減材に関する。
【０００２】
【従来の技術】
有害物質を含んだ廃棄物、汚泥、土壌等の処理の際には、何らかの手段による無害化が必要であり、該無害化の方法は、従来より多数提案されている。例えば、重金属を含む廃棄物の処理方法として、特開2000-37676号公報には、「カルシウムアルミネートおよび／またはカルシウムシリケートを含む製綱工程での生成物の粉末を、固定剤として用い、重金属を含む廃棄物の安定化処理を行うことを特徴とする重金属を含む廃棄物の安定化処理法」が開示されている。
【０００３】
【発明が解決しようとする課題】
一般に、有害な重金属を含有する廃棄物には、種々の重金属が含まれていることが多い。例えば、ゴミ焼却灰や下水汚泥焼却灰には、Pb、Cd、Zn、Cr6+等の重金属が含まれている。
このようなCr6+を含む種々の重金属を含有する廃棄物に対しては、前記した特開2000-37676号公報に開示される「カルシウムアルミネートおよび／またはカルシウムシリケートを含む製綱工程での生成物の粉末」では、Cr6+の溶出の低減は困難であった。
【０００４】
本発明は、上記の課題に鑑みなされたものであって、その目的は、
Cr6+を含む種々の重金属を含有する廃棄物等であっても、Cr6+等の重金属の溶出を低減できる重金属溶出低減材を提供することにある。
【０００５】
【課題を解決するための手段】
本発明者等は、上記の課題を解決すべく鋭意研究した結果、特定の条件で製造された特定の化学成分を有する材料であれば、上記課題が解決されることを見いだし、本発明を完成させたものである。
【０００６】
即ち、本発明は、1000℃以上の還元雰囲気下で製造され、化学成分としてCaO、Al 2 O 3 、R 2 O（アルカリ金属酸化物）及び還元性物質を合計で85重量％以上含有する重金属溶出低減材であって、CaO量が30.4〜46.1重量％、Al2O3量が39.4〜50.8重量％、R2O量が6.5〜10.1重量％であり、還元性物質がFeOであることを特徴とする重金属溶出低減材である。
【０００７】
【発明の実施の形態】
以下、本発明について詳しく説明する。本発明の重金属溶出低減材は、1000℃以上の還元雰囲気下で製造され、化学成分としてCaO、Al2O3及びR2O（アルカリ金属酸化物）を主成分とし、かつ、還元性物質を含有するものである。ここで、R2Oはアルカリ金属酸化物であり、具体的には、K2O、Na2O、Li2Oが挙げられる。前記本発明の重金属溶出低減材では、Cr6+を含む種々の重金属を含有する廃棄物等であっても、Cr6+等の重金属の溶出を低減することができる。なお、本発明の重金属溶出低減材は、該重金属溶出低減材の製造の容易さや生産効率等から、化学成分が、CaO量が30.4〜46.1重量％、Al 2 O 3 量が39.4〜50.8重量％、R 2 O量が6.5〜10.1重量％であることが好ましい。
【０００８】
本発明の重金属溶出低減材は、1000℃以上、重金属溶出低減材の製造コストや生産効率等から好ましくは1200〜1800℃の還元雰囲気下で製造されるものである。
製造温度が1000℃未満では、重金属溶出低減材の製造に時間がかかり生産効率が低下するので好ましくない。製造時の雰囲気が酸化雰囲気では、後述する還元性物質を含有することが困難であり、重金属（特に、Cr6+）の溶出低減効果が低下するので好ましくない。
本発明の重金属溶出低減材の製造に使用する製造装置は、1000℃以上での加熱が可能で、かつ、還元雰囲気にすることができる製造装置（加熱装置）であれば、特に限定するものではなく、例えば、キルン、電気炉、反射炉、キュポラ等が挙げられる。還元雰囲気にする方法としては、例えば、コークス等の可燃物を後述する原料とともに製造装置（加熱装置）に投入する、鉄やアルミニウム等の金属成分を後述する原料とともに製造装置（加熱装置）に投入する、COやH2等の還元性のガスを流す等の方法が挙げられる。
【０００９】
本発明の重金属溶出低減材は、還元性物質を含有するものである。該還元性物質としては、例えば、Fe、FeOや硫黄等が挙げられる。重金属溶出低減材中に還元性物質が含まれていないと、重金属（特に、Cr6+）の溶出低減効果が低下するので好ましくない。
【００１０】
重金属溶出低減材中に還元性物質が含まれているかどうかは、例えば、以下に示す方法によって確認することができる。
(1)重金属溶出低減材中の全鉄量に対する還元状態の鉄（Fe、FeO）の割合を求める方法
▲１▼試料1gをビーカーに入れ、少量の蒸留水と10mlのHClと10mlのHClO4を加えて、時計皿をかぶせて加熱し、白煙を生じてから約10分間加熱を続けたあと、室温まだ冷却する。
▲２▼温水50mlと6規定のHClを5mlを加えて再度加熱し可溶性塩類を溶解させた後に濾過して沈殿物を取り除く。濾液を25％酢酸アンモニウム緩衝液とアンモニア水(1+1)によりpH=3に調整した後、2％サリチル酸水溶液を2ml添加し、0.01mol/lのEDTA標準溶液で滴定しFe2O3量を求め、試料中の全鉄量（Ｆ１）を求める。
▲３▼窒素雰囲気中で、試料1gに臭素−メチルアルコール50mlを加えて10分間攪拌した後、濾過し、残さをメチルアルコールで洗浄する。続いて、残さを濾紙ごと三角フラスコに入れ、窒素と置換した状態で6規定のHClを20ml加えて加熱溶解し、室温まで冷却したものに、更に水100mlと、H2SO4:HPO4:水＝3:3:14(重量比)の混酸水溶液30ml、及び、ジフェニルアミンスルホン酸ナトリウム0.5mlを加えて、1/40規定の重クロム酸カリウムで滴定し、FeOの含有量を求め、FeOとして含有されるFe量（Ｆ２）を算出する。また、濾液と洗浄液を300mlのビーカーに入れ、6規定のHClを20ml加えて、約1時間濃縮し、さらに10mlのHClO4を加えて乾固し、6規定のHClを10mlと温水50mlを加えて、濾過し、200mlのメスフラスコで定容し、2.483Åで原子吸光分析で測定し、Fe量（Ｆ３）を求める。
▲４▼前記Ｆ１〜Ｆ３から、全鉄量に対する還元状態の鉄（Fe、FeO）の割合を求める。
【００１１】
(2)重金属溶出低減材中の硫化物イオンの状態を測定する方法
▲１▼蛍光Ｘ線分析又は硫黄分析計により、試料中の全硫黄量（Ｓ１）を測定する。
▲２▼「JIS R 9101(せっこうの化学分析法)」等の公知の方法で、三酸化硫黄及びニ酸化硫黄として含有される硫黄量（Ｓ２）を測定する。
▲３▼（Ｓ１−Ｓ２）より、還元状態の硫黄量を算出する。
【００１２】
次に、本発明の重金属溶出低減材の製造方法について説明する。本発明の重金属溶出低減材の製造方法としては、CaO原料、Al2O3原料、R2O原料等を、CaO量が30.4〜46.1重量％、Al 2 O 3 量が39.4〜50.8重量％、R 2 O量が6.5〜10.1重量％となるように製造装置（加熱装置）に投入し、1000℃以上の還元雰囲気下で加熱（焼成、溶融等）して製造する方法が挙げられる。前記CaO原料としては、生石灰、消石灰、石灰石等の工業原料が、Al2O3原料としては、ボーキサイト、ばん土頁岩、水酸化アルミニウム、アルミナ等の工業原料が、R2O原料としては、ソーダ灰、アルミン酸ソーダ、炭酸カリウム、アルミン酸カリウム、炭酸リチウム等の工業原料が挙げられる。前記各原料は、製造装置（加熱装置）に投入する前に混合しておいても良いし、個別に製造装置（加熱装置）に投入しても良い。また、原料は、粉体状のものを使用しても良いし、粒状／又は塊状のものを使用しても良い。なお、前記した各種原料には、SiO2、Fe2O3、TiO2、MgO等の不純物が含まれている。本発明の重金属溶出低減材は、これらの不純物を合計で15重量％以下含有することは差し支えない。また、本発明の重金属溶出低減材は、結晶質、非晶質のいずれであってもよい。
【００１３】
本発明の重金属溶出低減材は、ブレーン比表面積で、2000cm2/g以上に粉砕して使用することが好ましい。より好ましいブレーン比表面積は3000〜10000cm2/gである。
粉砕は、慣用の粉砕装置で行えば良い。
【００１４】
本発明の重金属溶出低減材の使用にあたっては、有害な重金属を含有する廃棄物、汚泥、土壌等に、本発明の重金属溶出低減材を水とともに加えて混練（混合）すればよい。また、セメント等の水硬性材料を併用することは差し支えない。
本発明の重金属溶出低減材は、有害な重金属を含有する廃棄物、汚泥、土壌等からの重金属の溶出を低減する効果を有するものである。また、本発明の重金属溶出低減材は、水硬性材料からの重金属の溶出を低減する効果も有するものである。
【００１５】
【実施例】
以下、実施例により本発明を説明する。
(1)重金属溶出低減材の調製
CaO原料として生石灰、Al2O3原料としてばん土頁岩、R2O原料としてソーダ灰又は炭酸カリウムを使用し、該原料とコークスを加熱装置に投入し、1600℃の還元雰囲気下で溶融し、重金属溶出低減材（試料１〜３）を調製した。
該重金属溶出低減材は、ボールミルでブレーン比表面積5000cm2/gに粉砕した。
調製した重金属溶出低減材の化学分析値を表１に示す。なお、試料４は、1600℃の酸化雰囲気下で溶融したものである。
【００１６】
【表１】
実施例１〜３、比較例１
(2)溶出試験１；重金属に汚染された土壌（砂質土、特性は表２に示す）に対する 重金属溶出低減効果の測定
表３に示す配合で、表２の重金属に汚染された土壌、重金属溶出低減材、水を混合し、該混合物をφ3cm×6cmに成形し、該成形体を20℃で24時間養生して、供試体を調製した。
前記供試体を粉砕し、環境庁告知13号「産業廃棄物に含まれる金属等の検定方法」に準じて、重金属の溶出量を測定した。
結果を表３に併記する。
【００１８】
【表２】
【表３】
表３から、1000℃以上の還元雰囲気下で製造され、化学成分としてCaO、Al2O3及びR2Oを主成分とし、かつ、還元性物質を含有する本発明の重金属溶出低減材では、重金属の溶出量が少なかった。
一方、酸化雰囲気下で製造された試料４を使用した比較例１では、重金属の溶出量が多かった。
【００２１】
実施例４〜６、比較例２〜４
(3)溶出試験２；Cr6+を含有する水硬性材料に対する重金属溶出低減効果の測定
Cr6+含有量が35ppmである普通ポルトランドセメントクリンカを電気炉にて調製し、該クリンカに石膏を加えて、Cr6+を含有する水硬性材料を試製した。
表４に示す配合で、前記試製水硬性材料及び重金属溶出低減材を混合し、環境庁告知13号「産業廃棄物に含まれる金属等の検定方法」に準じて、重金属の溶出量を測定した。
また、比較として高炉スラグ（新日鐵（株）製「エスメント」）を用いた場合についても測定を行った。
結果を表４に併記する。
【００２２】
【表４】
表４から、1000℃以上の還元雰囲気下で製造され、化学成分としてCaO、Al2O3及びR2Oを主成分とし、かつ、還元性物質を含有する本発明の重金属溶出低減材では、水硬性材料からの重金属（Cr6+）の溶出を低減する効果を有することが分かる。
【００２４】
【発明の効果】
以上詳記したように、本発明の重金属溶出低減材は、有害な重金属を含有する廃棄物、汚泥、土壌等からの重金属の溶出を低減する効果を有するものである。また、本発明の重金属溶出低減材は、水硬性材料からの重金属の溶出を低減する効果も有するものである。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a heavy metal elution reducing material capable of reducing elution of heavy metals from waste, sludge, soil and the like containing harmful heavy metals.
[0002]
[Prior art]
In the treatment of waste, sludge, soil, and the like containing harmful substances, it is necessary to detoxify them by some means, and many detoxification methods have been proposed. For example, as a method for treating waste containing heavy metals, Japanese Patent Application Laid-Open No. 2000-37676 states that “product powder in a steelmaking process containing calcium aluminate and / or calcium silicate is used as a fixing agent. A method for stabilizing a waste containing heavy metal, which is characterized in that the waste containing the metal is stabilized.
[0003]
[Problems to be solved by the invention]
In general, waste containing harmful heavy metals often contains various heavy metals. For example, garbage incineration ash and sewage sludge incineration ash contain heavy metals such as Pb, Cd, Zn, Cr 6+ .
For such waste containing various heavy metals including Cr 6+ , disclosed in the above-mentioned Japanese Patent Application Laid-Open No. 2000-37676 “in a steelmaking process including calcium aluminate and / or calcium silicate” In the “product powder”, it was difficult to reduce the elution of Cr 6+ .
[0004]
The present invention has been made in view of the above problems, and its purpose is as follows.
An object of the present invention is to provide a heavy metal elution reducing material capable of reducing elution of heavy metals such as Cr 6+ even if the waste contains various heavy metals including Cr 6+ .
[0005]
[Means for Solving the Problems]
As a result of earnest research to solve the above problems, the present inventors have found that the above problems can be solved if the material has a specific chemical component manufactured under specific conditions, and the present invention has been completed. It has been made.
[0006]
That is, the present invention is a heavy metal that is produced in a reducing atmosphere at 1000 ° C. or higher and contains 85% by weight or more in total of CaO, Al 2 O 3 , R 2 O (alkali metal oxide) and reducing substances as chemical components. a elution reducing material, CaO amount is 30.4 to 46.1 wt%, Al 2 O 3 amount is 39.4 to 50.8 wt%, R 2 O content is 6.5 to 10.1 wt%, the reducing substance is FeO It is a heavy metal elution reducing material.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
The present invention will be described in detail below. The heavy metal elution reducing material of the present invention is produced in a reducing atmosphere of 1000 ° C. or higher, and contains CaO, Al 2 O 3 and R 2 O (alkali metal oxide) as main components as chemical components, and a reducing substance. It contains. Here, R 2 O is an alkali metal oxide, and specific examples include K 2 O, Na 2 O, and Li 2 O. The heavy metal elution reducing material of the present invention may be a waste containing various heavy metals including Cr 6+, it is possible to reduce the elution of heavy metals such as Cr 6+. Note that heavy metal elution reducing material of the present invention, the ease and productivity in manufacturing of heavy metal elution reducing material, chemical composition, CaO amount is 30.4 to 46.1 wt%, Al 2 O 3 amount is 39.4 to 50.8 wt% The amount of R 2 O is preferably 6.5 to 10.1% by weight .
[0008]
The heavy metal elution reducing material of the present invention is produced in a reducing atmosphere of preferably 1200 to 1800 ° C. in view of the production cost and production efficiency of the heavy metal elution reducing material.
If the production temperature is less than 1000 ° C., it takes time to produce the heavy metal elution reducing material, and the production efficiency is lowered. If the atmosphere during production is an oxidizing atmosphere, it is difficult to contain a reducing substance, which will be described later, and the elution reduction effect of heavy metals (particularly Cr 6+ ) is reduced, which is not preferable.
The manufacturing apparatus used for manufacturing the heavy metal elution reducing material of the present invention is not particularly limited as long as it is a manufacturing apparatus (heating apparatus) that can be heated at 1000 ° C. or higher and can be in a reducing atmosphere. For example, a kiln, an electric furnace, a reflection furnace, a cupola, etc. are mentioned. As a method for making a reducing atmosphere, for example, combustible materials such as coke are introduced into a manufacturing apparatus (heating apparatus) together with raw materials to be described later, and metal components such as iron and aluminum are introduced into a manufacturing apparatus (heating apparatus) together with raw materials to be described later. And a method of flowing a reducing gas such as CO or H 2 .
[0009]
The heavy metal elution reducing material of the present invention contains a reducing substance. Examples of the reducing substance include Fe, FeO, and sulfur. If the reducing material is not contained in the heavy metal elution reducing material, the effect of reducing the elution of heavy metals (particularly Cr 6+ ) is reduced, which is not preferable.
[0010]
Whether or not a reducing substance is contained in the heavy metal elution reducing material can be confirmed by, for example, the following method.
(1) Method for determining the ratio of reduced iron (Fe, FeO) to the total amount of iron in the heavy metal elution reducing material (1) Place 1 g of sample in a beaker, add a small amount of distilled water, 10 ml of HCl and 10 ml of HClO 4 , Cover the watch glass and heat. After producing white smoke, continue heating for about 10 minutes, then cool to room temperature.
(2) Add 50 ml of warm water and 5 ml of 6N HCl and heat again to dissolve soluble salts, and then filter to remove precipitates. The filtrate was adjusted to pH = 3 with 25% ammonium acetate buffer and ammonia water (1 + 1), then 2 ml of 2% aqueous salicylic acid solution was added, and titrated with 0.01 mol / l EDTA standard solution, and the amount of Fe 2 O 3 was added. And the total iron amount (F1) in the sample is obtained.
(3) In a nitrogen atmosphere, add 50 ml of bromine-methyl alcohol to 1 g of the sample, stir for 10 minutes, filter, and wash the residue with methyl alcohol. Subsequently, the residue was put together with the filter paper in an Erlenmeyer flask, and after replacing with nitrogen, 20 ml of 6N HCl was added and dissolved by heating, cooled to room temperature, 100 ml of water, and H 2 SO 4 : HPO 4 : Add 30 ml of mixed acid aqueous solution of water = 3: 3: 14 (weight ratio) and 0.5 ml of sodium diphenylaminesulfonate, and titrate with 1/40 potassium dichromate to determine the content of FeO. The amount of Fe contained (F2) is calculated. Add the filtrate and washing solution to a 300 ml beaker, add 20 ml of 6N HCl, concentrate for about 1 hour, add 10 ml of HClO 4 to dryness, add 10 ml of 6N HCl and 50 ml of warm water. Then, it is filtered, made up to volume in a 200 ml volumetric flask, and measured by atomic absorption analysis at 2.483 to determine the amount of Fe (F3).
(4) From F1 to F3, the ratio of reduced iron (Fe, FeO) to the total iron content is determined.
[0011]
(2) Method of measuring the state of sulfide ions in the heavy metal elution reducing material (1) Measure the total sulfur amount (S1) in the sample by fluorescent X-ray analysis or sulfur analyzer.
(2) The sulfur content (S2) contained as sulfur trioxide and sulfur dioxide is measured by a known method such as “JIS R 9101 (chemical analysis method of gypsum)”.
(3) The sulfur amount in the reduced state is calculated from (S1-S2).
[0012]
Next, the manufacturing method of the heavy metal elution reducing material of this invention is demonstrated. As a method for producing a heavy metal elution reducing material of the present invention, a CaO raw material, an Al 2 O 3 raw material, an R 2 O raw material, etc., the CaO amount is 30.4 to 46.1% by weight, the Al 2 O 3 amount is 39.4 to 50.8% by weight, Examples include a method in which the amount of R 2 O is 6.5 to 10.1% by weight in a production apparatus (heating apparatus) and heated (fired, melted, etc.) in a reducing atmosphere at 1000 ° C. or higher. As the CaO raw material, industrial raw materials such as quick lime, slaked lime, limestone, etc., as Al 2 O 3 raw material, industrial raw materials such as bauxite, porphyry shale, aluminum hydroxide, alumina, etc., as R 2 O raw material, soda Industrial raw materials such as ash, sodium aluminate, potassium carbonate, potassium aluminate, and lithium carbonate are listed. The raw materials may be mixed before being introduced into the production apparatus (heating apparatus), or may be individually introduced into the production apparatus (heating apparatus). In addition, the raw material may be in powder form, or may be in granular / bulk form. The various raw materials described above contain impurities such as SiO 2 , Fe 2 O 3 , TiO 2 , and MgO. The heavy metal elution reducing material of the present invention may contain 15% by weight or less of these impurities in total. Further, the heavy metal elution reducing material of the present invention may be crystalline or amorphous.
[0013]
The heavy metal elution reducing material of the present invention is preferably used after being pulverized to a brain specific surface area of 2000 cm 2 / g or more. A more preferable Blaine specific surface area is 3000 to 10000 cm 2 / g.
The pulverization may be performed with a conventional pulverizer.
[0014]
In using the heavy metal elution reducing material of the present invention, the heavy metal elution reducing material of the present invention may be added together with water to a waste, sludge, soil or the like containing harmful heavy metals and kneaded (mixed). Further, it is possible to use a hydraulic material such as cement in combination.
The heavy metal elution reducing material of the present invention has an effect of reducing elution of heavy metals from waste, sludge, soil and the like containing harmful heavy metals. Moreover, the heavy metal elution reducing material of the present invention also has an effect of reducing elution of heavy metal from the hydraulic material.
[0015]
【Example】
Hereinafter, the present invention will be described by way of examples.
(1) Preparation of heavy metal elution reducing material
Quicklime as CaO raw material, sand shale as Al 2 O 3 raw material, soda ash or potassium carbonate as R 2 O raw material, the raw material and coke are put into a heating device, melted in a reducing atmosphere of 1600 ° C, Heavy metal elution reducing materials (samples 1 to 3) were prepared.
The heavy metal elution reducing material was pulverized by a ball mill to a brain specific surface area of 5000 cm 2 / g.
Table 1 shows the chemical analysis values of the prepared heavy metal elution reducing materials. Sample 4 was melted in an oxidizing atmosphere at 1600 ° C.
[0016]
[Table 1]
Examples 1-3, Comparative Example 1
(2) Dissolution test 1; Measurement of heavy metal dissolution reduction effect on soil contaminated with heavy metals (sandy soil, characteristics are shown in Table 2). Soil and heavy metals contaminated with heavy metals in Table 2 with the formulation shown in Table 3. An elution reducing material and water were mixed, the mixture was molded into φ3 cm × 6 cm, and the molded body was cured at 20 ° C. for 24 hours to prepare a specimen.
The specimen was pulverized, and the elution amount of heavy metal was measured according to Environmental Agency Notification No. 13 “Testing Method for Metals in Industrial Waste”.
The results are also shown in Table 3.
[0018]
[Table 2]
[Table 3]
From Table 3, the heavy metal elution reducing material of the present invention produced in a reducing atmosphere of 1000 ° C. or higher, containing CaO, Al 2 O 3 and R 2 O as chemical components and containing a reducing substance, The amount of elution of heavy metals was small.
On the other hand, in Comparative Example 1 using the sample 4 manufactured in an oxidizing atmosphere, the amount of heavy metal eluted was large.
[0021]
Examples 4-6, Comparative Examples 2-4
(3) Dissolution test 2: Measurement of heavy metal dissolution reduction effect on hydraulic materials containing Cr 6+
A normal Portland cement clinker having a Cr 6+ content of 35 ppm was prepared in an electric furnace, and gypsum was added to the clinker to produce a hydraulic material containing Cr 6+ .
In the formulation shown in Table 4, the trial hydraulic material and the heavy metal elution reducing material were mixed, and the elution amount of heavy metal was measured according to the Environmental Agency Notification No. 13 “Testing Method for Metals in Industrial Waste” .
Further, as a comparison, measurement was also performed when a blast furnace slag (“Esment” manufactured by Nippon Steel Co., Ltd.) was used.
The results are also shown in Table 4.
[0022]
[Table 4]
From Table 4, the heavy metal elution reducing material of the present invention produced in a reducing atmosphere of 1000 ° C. or higher, containing CaO, Al 2 O 3 and R 2 O as chemical components and containing a reducing substance, It can be seen that it has an effect of reducing elution of heavy metal (Cr 6+ ) from the hydraulic material.
[0024]
【The invention's effect】
As described above in detail, the heavy metal elution reducing material of the present invention has an effect of reducing the elution of heavy metals from waste, sludge, soil and the like containing harmful heavy metals. Moreover, the heavy metal elution reducing material of the present invention also has an effect of reducing elution of heavy metal from the hydraulic material.
Claims (1)
CaO量が30.4〜46.1重量％、Al2O3量が39.4〜50.8重量％、R2O量が6.5〜10.1重量％であり、
還元性物質がFeOであることを特徴とする重金属溶出低減材。 A heavy metal elution reducing material manufactured in a reducing atmosphere of 1000 ° C or higher and containing 85% by weight or more in total of CaO, Al 2 O 3 , R 2 O (alkali metal oxide) and reducing substances as chemical components. ,
CaO amount is 30.4 to 46.1 wt%, Al 2 O 3 amount is 39.4 to 50.8 wt%, R 2 O content is 6.5 to 10.1 wt%,
A heavy metal elution reducing material, wherein the reducing substance is FeO.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001037393A JP4589544B2 (en) | 2001-02-14 | 2001-02-14 | Heavy metal elution reducing material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001037393A JP4589544B2 (en) | 2001-02-14 | 2001-02-14 | Heavy metal elution reducing material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002239378A JP2002239378A (en) | 2002-08-27 |
| JP4589544B2 true JP4589544B2 (en) | 2010-12-01 |
Family
ID=18900530
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001037393A Expired - Fee Related JP4589544B2 (en) | 2001-02-14 | 2001-02-14 | Heavy metal elution reducing material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4589544B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6686630B2 (en) * | 2016-03-30 | 2020-04-22 | 住友大阪セメント株式会社 | Heavy metal insolubilizing material and method for producing the same |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5263881A (en) * | 1975-11-21 | 1977-05-26 | Tatsuaki Oomasa | Manufacture of chromium removing agents |
| JPH0625007B2 (en) * | 1990-08-16 | 1994-04-06 | 電気化学工業株式会社 | Cement admixture and cement composition |
| JPH05345658A (en) * | 1992-06-16 | 1993-12-27 | Kuree Baan Ceramics:Kk | Pollution-free sintered ceramics of soluble chromate and its manufacturing method |
| JP3377604B2 (en) * | 1994-07-12 | 2003-02-17 | 電気化学工業株式会社 | Cement quick setting material and cement composition |
| JP3299174B2 (en) * | 1997-03-27 | 2002-07-08 | 川崎製鉄株式会社 | Method for treating chromium oxide-containing material |
| JPH11165147A (en) * | 1997-12-02 | 1999-06-22 | Nippon Kayaku Co Ltd | Treatment agent for heavy metal-containing waste and stabilization method for heavy metal-containing waste |
-
2001
- 2001-02-14 JP JP2001037393A patent/JP4589544B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2002239378A (en) | 2002-08-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Kindness et al. | Immobilization of chromium in cement matrices | |
| Wang et al. | Heavy metals migration during the preparation and hydration of an eco-friendly steel slag-based cementitious material | |
| JP2005040685A (en) | Heavy metal adsorbent material and heavy metal treatment method | |
| JP2002362949A (en) | Manufacturing method of solidified material using oyster shells | |
| RO105948B1 (en) | PROCEDURE FOR CHEMICAL STABILIZATION OF SECONDARY PRODUCTS AND METALURGICAL RESIDUES | |
| JP2001506963A (en) | Method of producing environmentally stable substances by decontamination of contaminated sediments and soil | |
| JP2005254077A (en) | Method for manufacturing heavy metal adsorbent and adsorbent obtained thereby | |
| Bayuseno et al. | Improved understanding of the pozzolanic behaviour of MSWI fly ash with Ca (OH) 2 solution | |
| Wang et al. | Preparation of backfill materials by solidifying municipal solid waste incineration fly ash with slag-based cementitious materials | |
| JP5768293B2 (en) | Method for producing soil-solidifying material using fluorine-containing inorganic waste, obtained soil-solidifying material, and method for solidifying soft soil using the soil-solidifying material | |
| JP5915202B2 (en) | Insolubilization method | |
| JP2002241166A (en) | Hydraulic composition | |
| JP5013005B1 (en) | Insolubilizer and method for producing the same | |
| JP3702385B2 (en) | Exhaust gas treatment agent, method for producing the same, and exhaust gas treatment method | |
| JP3919648B2 (en) | Hazardous heavy metal collector | |
| JP2018158876A (en) | Coal ash cured product | |
| JP4589544B2 (en) | Heavy metal elution reducing material | |
| CN107109185A (en) | The insoluble method of harmful substance insolubilizing agent and harmful substance | |
| JP3844456B2 (en) | Solidification material and method for purification of contaminated soil using the same | |
| JPWO2000004982A1 (en) | Exhaust gas treatment agent, its manufacturing method and exhaust gas treatment method | |
| JP4409102B2 (en) | Heavy metal elution reducing material | |
| JPS63108093A (en) | Solidifying material for waste or soft ground soil | |
| JP2002205032A (en) | Heavy metal elution reducing material | |
| Zhang et al. | Immobilization of Cr in a heavily Cr (VI)-contaminated soil using alkali-activated blast furnace slag and calcium polysulfide: Remediation efficiency and mechanism | |
| JP3897727B2 (en) | Hazardous material collector |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20070329 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20100706 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20100802 |
|
| RD03 | Notification of appointment of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7423 Effective date: 20100813 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20100817 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20100819 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20100907 |
|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20100910 |
|
| R150 | Certificate of patent or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130917 Year of fee payment: 3 |
|
| 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 |
|
| LAPS | Cancellation because of no payment of annual fees |