JPS6221594B2 - - Google Patents
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- Publication number
- JPS6221594B2 JPS6221594B2 JP54098820A JP9882079A JPS6221594B2 JP S6221594 B2 JPS6221594 B2 JP S6221594B2 JP 54098820 A JP54098820 A JP 54098820A JP 9882079 A JP9882079 A JP 9882079A JP S6221594 B2 JPS6221594 B2 JP S6221594B2
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- Prior art keywords
- water
- steelmaking dust
- soluble sulfide
- dust
- added
- 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
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Description
本発明は製鋼ダストに含まれる有害物質の無害
化処理方法に関するものであり、特に処理物の取
扱いやその廃棄の極めて容易な、且つ処理効率が
著しく高められた製鋼ダストの無害化処理法を提
供するものである。
従来より、アーク炉などの製鋼炉から発生する
製鋼ダストは、該ダスト中に含有されている有価
金属の回収およびその他原料として再利用する場
合を除き、保管されているが、かかる製鋼ダスト
には有害金属が含まれる場合があり、そのうち産
業廃棄物の処理に関する法令で定められている溶
出試験を行なうと、6価クロム、カドミウム、鉛
などが溶出することがあるため、産業廃棄物とし
ての規制の対象となつている。そして、近年、こ
のような製鋼ダストの無害化処理の要請に応える
ために、各種の手法が提案され、検討されてきて
いるが、いずれも処理技術、経済性、作業性等の
面において一長一短があり、実用的に未だ充分に
満足し得るものではないのである。
そこで、かかる事情に鑑みて種々検討した結
果、製鋼ダストにアルカリ性で還元機能を有する
可溶性硫化物を添加混練することにより、該ダス
ト中の水溶性有害物質の溶出を極めて効果的に且
つ容易に抑制し得ることを見い出した。
而して、かかる可溶性硫化物による有害成分の
無害化機構は、次式(可溶性硫化物としてCaS4
を使用する場合);
CaS4+O2+H2O→CaS2O3+H2S+S
に従つて発生するH2Sにより、製鋼ダスト中に含
まれる場合がある金属(M;Cd,Pb,Hg等)が
次式;
H2S+M2+→MS↓+2H+
の如く金属硫化物となつて安定化せしめられた
り、また6価クロムが次式;
CrO4 2-+4H2S→Cr3++4H2O+4S
CrO4 2-+4CaS2O3 →Cr3++4CaSO4+4S
に従つて3価のクロムに還元されると共に、系の
アルカリ性によつてかかる生成した3価のクロム
が水酸化物に変換されることにより安定化される
ことによるものと考えられるところから、反応系
には水(H2O)の存在が必須とされている。
しかし、製鋼ダストに対して水を約30%以上添
加した場合、この混和物は、一般にスラリー状或
は泥状を呈するようになり反応後の生成物(無害
化物)の取扱い、廃棄処理などを著しく困難なも
のにすることとなる。そこで粉末状で得られる製
鋼ダストに、それの取扱いが容易な泥状とならな
い程度の水のみを加えて、上記した反応に従つて
無害化することを試みたが、該反応の進行が遅い
ことがわかつた。しかも、この問題は、可溶性硫
化物の添加量を増大させても、迅速化できなかつ
た。
ここにおいて、本発明者らは、上述の問題を解
消すべく更に鋭意研究を進めた結果、反応混合物
が固形状態の下でも前記無害化反応を迅速に進行
せしめ得る有効な手法を見い出し、本発明を完成
するに至つたのである。
すなわち、かかる本発明の要旨とするところ
は、粉末状の製鋼ダストに、アルカリ性で還元機
能を有する可溶性硫化物と共に、泥状とならない
程度の水分を加えて混練し、その混練物を、必要
に応じて所望の形状に成形した後、400℃を越え
ない温度下で加熱養生せしめるようにしたことに
あり、これによつて製鋼ダストと可溶性硫化物と
水との間の反応は極めて迅速に進行せしめられ得
ることとなつたことは勿論、該製鋼ダストの最終
的な廃棄形態を考えて、所望の形状物に成形し、
無害化せしめ得るという利点も生じるに至つたの
である。
また、かくの如き本発明に従つて得られる混練
物を、ペレツト、ブリケツト、団子状、塊状など
の所望の形状に成形せしめれば、かかる成形物は
それに更にはある程度の水が加えられてもその形
状を崩壊することがなく、従つてかかる再度の水
分の添加が可能となり、ひいては前記無害化反応
を更に良好に進行せしめ得ることが出来るのであ
り、またかかる水分の再度の添加に代えて蒸気に
よる加熱養生手法を採用しても同様な効果が得ら
れるのである。
さらに、本発明に従う所定温度下での加熱養生
に、CO2を含む排ガス、例えば加熱炉、燃焼炉な
どから排出される燃焼排ガス、製鋼の集塵機から
排出される排ガス等を使用すれば、これら排ガス
の熱エネルギーの有効利用と共に、CO2に基づく
CaS4+CO2+H2O→CaCO3+H2S+3Sの如き反応
によつて、その処理時間を著しく短縮せしめ得る
利点が生ずるのである。
なお、かくの如き本発明手法は、アーク炉など
の製鋼炉において通常粉末状態で発生する、クロ
ム(6価)、カドミウム、鉛などの有害金属成分
を含む製鋼ダストの全べてに適用され得るもので
あり、かかる製鋼ダストに対して、アルカリ性で
還元機能を有する可溶性硫化物、好ましくは可溶
性多硫化物、例えば多硫化アルカリ金属塩類、多
硫化アルカリ土類金属塩類、多硫化アンモニウム
塩などを、本発明に従う所定量の水分と共に添加
して混練せしめるものである。かかる(水)可溶
性硫化物の配合量は製鋼ダストの種類、性状など
によつて種々異なり、目的とする無害化の度合に
応じて適宜決定されることとなるが、一般に製鋼
ダスト100重量部に対して硫化物態硫黄(S2-)
0.01〜10重量部程度の割合で用いられることとな
る。また、これら製鋼ダスト及び可溶性硫化物に
加えられる水分量としては、混練して得られる混
練物が泥状を呈しない程度の割合、具体的には製
鋼ダストに対して一般に約30%以下の割合におい
て目的とする迅速な無害化処理が行なわれるよう
に適宜決定されることとなる。
また、かくして得られる製鋼ダストと可溶性硫
化物と水分との所定割合の混練物は、泥状とはな
つていないため、その後の処理においてその取扱
が極めて容易であるのであり、そしてまたそれは
所望の形状に容易に成形し得るため、製鋼ダスト
の運搬形態やその最終的な廃棄状態などを考慮し
てペレツト状、ブリケツト状、団子(豆炭)状、
塊状などの形状の成形物に必要に応じて成形され
ることとなるのである。そして、このような成形
物には、前述の如く、更に或程度の水分、換言す
れば成形形状を崩壊させない程度、一般に成形物
の約10%以下の水分が散布などの手段によつて加
えられ、以て有効な反応の促進が図られるのであ
る。
さらに、かくの如き工程を経た固形状態の混練
物若しくはその成形物は、本発明に従つて、400
℃を越えない温度下において種々加熱養生せしめ
られることによつて、水分量の不充分な状態下に
あつても前記無害化反応を有利に且つ迅速に進行
せしめて、可溶性硫化物による水溶性有害物質の
溶出の抑制効果を最大限に発揮せしめるのであ
る。なお、この加熱養生処理に際して、加熱温度
は400℃を越えないようにすることが必要であ
り、それより高い加熱温度を採用した場合には、
抑制されるべき有害金属成分(特に6価クロム)
の溶出量が増大するようになり、本来の目的を達
成することが困難となる。また、加熱方法として
は、適当な炉を用いて単純に加熱するのみの方式
の他、加熱空気の吹付け、過熱蒸気による処理、
更には本発明にとつて好ましいCO2を含む排ガス
を用いて加熱し、排熱利用並びに反応の促進を狙
う方式など、あらゆる加熱手段、方法が採用され
得る。
そして、このようにして得られた製鋼ダスト処
理物は、アルカリ性で還元機能を有する可溶性硫
化物による有効な無害化作用(反応)によつて、
そこに含まれる有害金属成分の溶出量が効果的に
抑制される一方、泥状形態とはなつていないた
め、そのまま埋立処分に供することが出来るので
あり、またその運搬など、取扱上においても著し
く有利となつたのである。
以下に実施例を示し、本発明を更に具体的に明
らかにするが、本発明がかかる実施例の記載によ
つて何等の制限をも受けるものでないことは言う
までもない。なお、実施例並びに参考例における
部及び百分率は特に断わりのない限り全て重量基
準である。
参考例
製鋼ダストの成分は溶解原料および鋼種によつ
て大きく変動するが、ここでは第1表に示される
如き溶出量を有する2種のダストAおよびBにつ
いて検討した。
The present invention relates to a method for detoxifying harmful substances contained in steelmaking dust, and in particular provides a method for detoxifying steelmaking dust that makes it extremely easy to handle and dispose of treated materials, and has significantly improved processing efficiency. It is something to do. Traditionally, steelmaking dust generated from steelmaking furnaces such as arc furnaces has been stored unless the valuable metals contained in the dust are recovered or reused as other raw materials. It may contain hazardous metals, including hexavalent chromium, cadmium, lead, etc., which may be leached out during elution tests stipulated by laws and regulations regarding industrial waste treatment, so they are not regulated as industrial waste. is subject to. In recent years, various methods have been proposed and studied in order to meet the demand for detoxifying steelmaking dust, but all of them have advantages and disadvantages in terms of processing technology, economic efficiency, workability, etc. However, it is still not fully satisfactory in practical terms. Therefore, as a result of various studies in view of the above circumstances, we found that by adding and kneading soluble sulfide, which is alkaline and has a reducing function, to steelmaking dust, the elution of water-soluble harmful substances in the dust can be extremely effectively and easily suppressed. I found out what I can do. The mechanism by which such soluble sulfides detoxify harmful components is expressed by the following formula (CaS 4 as soluble sulfide).
); CaS 4 +O 2 +H 2 O→CaS 2 O 3 +H 2 S+S The H 2 S generated as a result of this process causes metals (M; Cd, Pb, Hg, etc.) that may be contained in steelmaking dust to ) is stabilized by becoming a metal sulfide as shown in the following formula ; O+4S CrO 4 2- +4CaS 2 O 3 →Cr 3+ +4CaSO 4 +4S It is reduced to trivalent chromium according to O+4S CrO 4 2- +4CaS 2 O 3 , and the generated trivalent chromium is converted to hydroxide depending on the alkalinity of the system. The presence of water (H 2 O) is essential in the reaction system, as it is thought that this is due to the stabilization caused by the reaction. However, when approximately 30% or more of water is added to steelmaking dust, this mixture generally becomes slurry-like or mud-like, making it difficult to handle and dispose of the reaction product (detoxified material). This will make things extremely difficult. Therefore, an attempt was made to make the steel dust obtained in powder form harmless by adding just enough water to make it easy to handle and not turn it into a muddy form, and to make it harmless according to the reaction described above, but the reaction proceeded slowly. I understood. Moreover, this problem could not be solved quickly even by increasing the amount of soluble sulfide added. Here, as a result of further intensive research in order to solve the above-mentioned problems, the present inventors have discovered an effective method that allows the detoxification reaction to proceed rapidly even when the reaction mixture is in a solid state. This led to the completion of the . That is, the gist of the present invention is to knead powdered steelmaking dust together with soluble sulfide that is alkaline and has a reducing function and add water to an extent that does not become muddy, and to mix the kneaded product as necessary. After forming it into the desired shape, it is heated and cured at a temperature not exceeding 400℃, which allows the reaction between steelmaking dust, soluble sulfide, and water to proceed extremely quickly. Of course, considering the final disposal form of the steelmaking dust, it is possible to form it into a desired shape,
This also led to the advantage that it could be rendered harmless. Furthermore, if the kneaded product obtained according to the present invention is molded into a desired shape such as pellets, briquettes, dumplings, or lumps, such molded products can be formed even if a certain amount of water is added thereto. The shape does not collapse, and therefore water can be added again, and the detoxification reaction can proceed even better, and steam can be used instead of adding water again. A similar effect can be obtained by using the heating curing method. Furthermore, if exhaust gas containing CO2 , such as combustion exhaust gas discharged from a heating furnace, combustion furnace, etc., exhaust gas discharged from a steelmaking dust collector, etc., is used for heat curing at a predetermined temperature according to the present invention, these exhaust gases can be used. based on CO 2 as well as effective use of thermal energy.
Reactions such as CaS 4 +CO 2 +H 2 O→CaCO 3 +H 2 S+3S offer the advantage of significantly shortening the processing time. The method of the present invention as described above can be applied to all steelmaking dust containing harmful metal components such as chromium (hexavalent), cadmium, and lead, which is normally generated in powder form in steelmaking furnaces such as arc furnaces. For such steelmaking dust, a soluble sulfide that is alkaline and has a reducing function, preferably a soluble polysulfide, such as polysulfide alkali metal salts, polysulfide alkaline earth metal salts, polysulfide ammonium salts, etc. According to the present invention, it is added and kneaded together with a predetermined amount of water. The amount of (water) soluble sulfide blended varies depending on the type and properties of the steelmaking dust, and is determined as appropriate depending on the desired degree of detoxification, but generally it is added to 100 parts by weight of steelmaking dust. On the other hand, sulfide sulfur (S 2- )
It will be used in a proportion of about 0.01 to 10 parts by weight. In addition, the amount of water added to these steelmaking dust and soluble sulfides should be such that the kneaded material obtained by kneading does not appear muddy, specifically, the amount of water added to the steelmaking dust is generally about 30% or less. The decision will be made as appropriate so that the intended rapid detoxification process can be carried out. In addition, the thus obtained kneaded product of steelmaking dust, soluble sulfide, and water in a predetermined ratio is not slurry-like, so it is extremely easy to handle in subsequent processing, and it can also be used in the desired manner. Since it can be easily formed into shapes, it can be shaped into pellets, briquettes, dumplings (pulverized charcoal),
It is then molded into a block-like molded product as needed. As mentioned above, a certain amount of moisture is added to such a molded product, in other words, an amount of water that does not disintegrate the molded shape, generally about 10% or less of the molded product, is added by means such as spraying. , thereby promoting effective reaction. Further, according to the present invention, the solid kneaded product or the molded product obtained through such a process can be used for 400
By being heat-cured in various ways at temperatures not exceeding ℃, the detoxification reaction can proceed advantageously and quickly even under conditions of insufficient moisture content, and the water-soluble harmful substances caused by soluble sulfides can be effectively and rapidly cured. This maximizes the effect of suppressing the elution of substances. In addition, during this heat curing treatment, it is necessary to ensure that the heating temperature does not exceed 400℃, and if a higher heating temperature is used,
Hazardous metal components that should be suppressed (especially hexavalent chromium)
The amount of elution increases, making it difficult to achieve the original purpose. In addition, heating methods include simple heating using an appropriate furnace, blowing heated air, treatment with superheated steam,
Furthermore, any heating means or methods may be employed, such as a method that uses waste gas containing CO 2 and aims to utilize waste heat and promote the reaction, which is preferable for the present invention. The steelmaking dust treated product obtained in this way is treated by the effective detoxifying action (reaction) of soluble sulfide which is alkaline and has a reducing function.
While the elution amount of harmful metal components contained in it is effectively suppressed, it is not in a muddy form, so it can be sent to landfill as is, and it is also extremely difficult to transport and handle. It turned out to be an advantage. Examples will be shown below to clarify the present invention more specifically, but it goes without saying that the present invention is not limited in any way by the description of these Examples. Note that all parts and percentages in Examples and Reference Examples are based on weight unless otherwise specified. Reference Example Although the components of steelmaking dust vary greatly depending on the melted raw material and the type of steel, two types of dust A and B having the elution amounts shown in Table 1 were studied here.
【表】
*〓それぞれの金属成分の溶出量は、環境庁告
示第13号(最終改正環境庁告示第4号)に従
う溶出試験によつて求めたものである。
かかる2種のダストのそれぞれの100部に、
27.5%濃度の多硫化カルシウム水溶液と水とを第
2表に示す割合にて加えて混和せしめ、常温下に
一昼夜放置した後、それぞれの溶出試験を行な
い、その結果を第2表に示した。[Table] * The elution amount of each metal component was determined by an elution test in accordance with Environment Agency Notification No. 13 (Final revised Environment Agency Notification No. 4).
100 parts of each of these two types of dust,
A 27.5% calcium polysulfide aqueous solution and water were added and mixed in the proportions shown in Table 2, and after being left at room temperature for a day and night, each elution test was conducted, and the results are shown in Table 2.
【表】【table】
【表】
第2表の結果より明らかな如く、有害金属成分
のうち6価クロムについては反応系に多量の水分
(約30%)を存在させなければ一昼夜放置では完
全な無害化は困難であるのであり、またそれは多
硫化カルシウムの添加量を増加せしめても解決が
困難である。なお、アルカリ性である可溶性硫化
物である多硫化カルシウムの配合によつて、形成
される配合物のPHはより高いアルカリ性を示すよ
うになることが認められる。
実施例 1
参考例に示す製鋼ダスト(B)100部に、27.5
%濃度の多硫化カルシウム水溶液3.6部及び水15
部を添加せしめ、充分混練した後、豆炭状に成形
せしめ、次いでこれをマツフル炉内に載置して第
3表に示す如き種々なる温度条件下に種々なる時
間で加熱養生処理した。
得られたそれぞれの試料について、Cr6+の溶
出量(mg/)を求め、その結果を第3表に示し
た。
第3表より明らかなように、加熱温度が著しく
高くなるとCr6+の溶出量が増加する結果が出て
おり、それ故400℃を越える温度は避けることが
望ましいのである。また、望ましい温度範囲とし
ては、100〜300℃程度、特に150〜250℃程度であ
ることが理解される。[Table] As is clear from the results in Table 2, it is difficult to completely render hexavalent chromium, one of the harmful metal components, harmless by leaving it for a day and night unless a large amount of water (approximately 30%) is present in the reaction system. This problem is difficult to solve even if the amount of calcium polysulfide added is increased. It is recognized that by adding calcium polysulfide, which is an alkaline soluble sulfide, the PH of the resulting mixture becomes more alkaline. Example 1 To 100 parts of steelmaking dust (B) shown in the reference example, 27.5
% concentration calcium polysulfide aqueous solution 3.6 parts and water 15
After thoroughly kneading the mixture, it was formed into a charcoal shape, which was then placed in a Matsufuru furnace and heat-cured for various times under various temperature conditions as shown in Table 3. The elution amount (mg/) of Cr 6+ was determined for each sample obtained, and the results are shown in Table 3. As is clear from Table 3, when the heating temperature becomes significantly higher, the amount of Cr 6+ eluted increases, and therefore it is desirable to avoid temperatures exceeding 400°C. Further, it is understood that the desirable temperature range is about 100 to 300°C, particularly about 150 to 250°C.
【表】
実施例 2
実施例1に示す製鋼ダスト100部に、27.5%濃
度の多硫化カルシウム水溶液3.6部及び水15部を
添加し、混練せしめた後、ブリケツト状に成形せ
しめ、この成形物に更に散水によつて成形物の約
5%の水分を添加した。
この散水した成形物と、散水しない成形物とに
ついて、200℃の温度下にてそれぞれ処理時間を
種々変えた加熱養生処理を行ない、得られた処理
物のCr6+溶出量を求めた。その結果を第4表に
示す。[Table] Example 2 To 100 parts of the steelmaking dust shown in Example 1, 3.6 parts of a 27.5% calcium polysulfide aqueous solution and 15 parts of water were added, kneaded, and then formed into a briquette. Furthermore, approximately 5% moisture of the molded article was added by water sprinkling. The molded products that were sprinkled with water and the molded products that were not sprinkled with water were subjected to heat curing treatment at a temperature of 200° C. with various treatment times, and the amount of Cr 6+ eluted from the resulting treated products was determined. The results are shown in Table 4.
【表】
第4表より明らかなように、散水によつて、多
硫化カルシウムによるCr6+の無害化が著しく保
進されていることが理解される。
実施例 3
実施例2で得られた混練物のブリケツトに対し
て、第5表に示される如き加熱養生処理を施し
た。
第5表に示された結果より、蒸気加熱による養
生処理によつても無害化処理反応が促進されてい
ることが理解される。[Table] As is clear from Table 4, it is understood that the detoxification of Cr 6+ by calcium polysulfide is significantly promoted by water sprinkling. Example 3 The briquettes of the kneaded product obtained in Example 2 were subjected to heat curing treatment as shown in Table 5. From the results shown in Table 5, it is understood that the detoxification reaction is also promoted by the curing treatment by steam heating.
【表】
実施例 4
実施例2で得られた混練物(成形されていない
もの)に対して、200℃の温度の単純加熱または
排ガス加熱を各種処理時間で行ない、得られた処
理物のCr6+溶出量を求めた。なお、用いた排ガ
スはCO2を約10%(容積)含むボイラー排ガスで
あつた。
結果を第6表に示す。
第6表より明らかな如く、排ガス加熱の採用に
よつて製鋼ダスト中のCr6+が極めて短時間にて
無害化され得るのである。[Table] Example 4 The kneaded product (not shaped) obtained in Example 2 was subjected to simple heating at 200°C or exhaust gas heating for various treatment times, and the Cr The amount of 6+ elution was determined. The exhaust gas used was boiler exhaust gas containing about 10% (by volume) of CO2 . The results are shown in Table 6. As is clear from Table 6, by employing exhaust gas heating, Cr 6+ in steelmaking dust can be rendered harmless in an extremely short period of time.
【表】
実施例 5
実施例1に示すダスト100部に対して、多硫化
ナトリウム1部を水20部に溶解したものを添加混
練した後、ブリケツト状に成形せしめ、ついでこ
の混練物を種々の条件下で加熱養生処理を行な
い、得られた処理物のCr6+溶出量を求めた。そ
の結果を第7表に示す。[Table] Example 5 To 100 parts of the dust shown in Example 1, 1 part of sodium polysulfide dissolved in 20 parts of water was added and kneaded, and then formed into a briquette. Heat curing treatment was performed under these conditions, and the amount of Cr 6+ eluted from the resulting treated product was determined. The results are shown in Table 7.
Claims (1)
能を有する可溶性硫化物と共に、泥状とならない
程度の水分を加えて混練し、必要に応じて所望の
形状に成形した後、400℃を越えない温度下で加
熱養生せしめることにより、それら製鋼ダストと
可溶性硫化物と水との間の反応を進行せしめるよ
うにしたことを特徴とする製鋼ダストの無害化処
理方法。 2 前記製鋼ダストと可溶性硫化物と水分との混
練物を所望の形状に成形した後、かかる成形物に
更にその形状を崩壊させない程度の水分を加えて
加熱養生するようにした特許請求の範囲第1項記
載の処理方法。 3 前記製鋼ダストと可溶性硫化物と水分との混
練物を所望の形状に成形した後、蒸気加熱養生す
るようにした特許請求の範囲第1項記載の処理方
法。 4 前記製鋼ダストと可溶性硫化物と水分との混
練物を、必要に応じて所望の形状に成形した後、
CO2を含む排ガス中にて加熱養生するようにした
特許請求の範囲第1項記載の処理方法。[Scope of Claims] 1. Powdered steelmaking dust is kneaded together with soluble sulfide that is alkaline and has a reducing function, and water is added to an extent that it does not become muddy, and if necessary, after molding into a desired shape, A method for detoxifying steelmaking dust, comprising heating and curing it at a temperature not exceeding 400°C to promote a reaction between the steelmaking dust, soluble sulfide, and water. 2. After the kneaded product of the steelmaking dust, soluble sulfide, and moisture is formed into a desired shape, the formed product is further added with moisture to an extent that does not collapse the shape, and then heated and cured. The treatment method described in Section 1. 3. The treatment method according to claim 1, wherein the kneaded product of the steelmaking dust, soluble sulfide, and water is formed into a desired shape and then cured by steam heating. 4 After forming the kneaded product of the steelmaking dust, soluble sulfide, and water into a desired shape as necessary,
The treatment method according to claim 1, wherein the treatment method is heated and cured in exhaust gas containing CO 2 .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9882079A JPS5624083A (en) | 1979-08-02 | 1979-08-02 | Antipollution treatment of steel making dust |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9882079A JPS5624083A (en) | 1979-08-02 | 1979-08-02 | Antipollution treatment of steel making dust |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5624083A JPS5624083A (en) | 1981-03-07 |
| JPS6221594B2 true JPS6221594B2 (en) | 1987-05-13 |
Family
ID=14229940
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9882079A Granted JPS5624083A (en) | 1979-08-02 | 1979-08-02 | Antipollution treatment of steel making dust |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5624083A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0508697A1 (en) * | 1991-04-09 | 1992-10-14 | Qi-Jiang Situ | A re-calcination and extraction process for the detoxification and comprehensive utilization of chromic residues |
| JP3986397B2 (en) * | 2002-09-03 | 2007-10-03 | 株式会社クボタ | Method for insolubilizing ash containing heavy metals |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52107120A (en) * | 1976-03-04 | 1977-09-08 | Maeda Seikan Kk | Building material that use casting wasted sand dust |
| JPS5312165A (en) * | 1976-07-20 | 1978-02-03 | Nec Corp | Process for treating incinerator fly ash |
-
1979
- 1979-08-02 JP JP9882079A patent/JPS5624083A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5624083A (en) | 1981-03-07 |
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