• 자원리싸이클링
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• 제18권2호
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• pp.56-61
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• 2009

알루미늄 화합물을 합성하기 위한 전단계 연구로써, 국산 99.7% 순도의 수산화알루미늄을 대상으로 무기산 및 유기산을 이용한 용해실험을 수행하였다. 본 실험에서 사용한 수산화알루미늄의 평균입도는 각각 $14.4{\mu}m$, $22.9{\mu}m$ 및 $62.3{\mu}m$이었으며, 반응온도, 산농도, 반응시간에 따른 수산화알루미늄 용해율을 조사하였다. 실험결과 염산에 의한 용해시 염산농도가 증가할수록 용해율은 증가하였으며, $70^{\circ}C$에서 4시간 용해시 염산농도 5 mole/l의 경우 70% 이상의 용해율을 보였다. 또한, 황산을 사용하여 수산화알루미늄을 용해하고자 하는 경우 적정 황산농도는 6 mole/l 부근으로 유지하는 것이 바람직하였다. 옥살산을 사용하는 경우 반응온도는 $90^{\circ}C$가 적절하며, 옥살산농도 1.0 mole/l, 고체농도 20 g/l의 조건에서 16시간 용해하였을 때 거의 100%에 근접하는 용해율을 얻을 수 있었다.

• 자원리싸이클링
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• 제12권4호
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• pp.30-37
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• 2003

황산 용액에서 Zinc-ferrite의 용해에 대한 반응속도론을 황산 용액의 반응온도와 농도 변화에 대해 조사하였다. 반응율(R)과 겉보기 반응 속도상수(K)는 황산 용액의 온도와 농도가 클수록 증가한다. Zinc-ferrite의 반응속도는 반응초기에서 $1-(1-K)^{1/3}=Kt$와 같은 속도식을 적용할 수 있다. 용해에 대한 활성화 에너지는 황산 용액의 농도에 관계없이 약 16.3kcal/mole 이다. Zinc-ferrite가 황산 용액에서 용해할 때는 Zinc-ferrite의 화학 양론적 조성으로 용해되며, Fe 또는 Zn의 단독으로는 용해되지 않는다.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.472-477
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• 2001

Spent catalysts containing platinum were generated in petroleum refinery and other chemical industries. The reclamation of precious metals from such wastes has long been attempted in view of their rare, expensive and indispensable nature. In this study, the recovery of platinum from petroleum catalysts was attempted by a method consisting mainly of dissolving alumina substrate with sulfuric acid thereby concentrating insoluble platinum. Also, platinum dissolved partially in sulfuric acid was recovered by a cementation method using aluminum metal as a reductive agent. The effect of temperature, time, concentration of sulfuric acid. and pulp density on the dissolution of substrate was investigated. When the substrate of platinum catalyst was ${\gamma}$-AI$_2$O$_3$ about 95% alumina was dissolved in 6.0M sulfuric acid at 10$0^{\circ}C$ for 2 hours. When the substrate was the mixture of ${\gamma}$-A1$_2$O$_3$and $\alpha$-A1$_2$O$_3$about 92% was dissolved after 4 hours. As a result, more than 99% of platinum could be recovered by this method and aluminum sulfate was obtained as byproduct.

• 자원리싸이클링
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• 제30권3호
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• pp.41-46
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• 2021

메탄술폰산은 우수한 물리화학적 특성을 지니고 있어 금속의 침출에 효과적이다. 분자구조 및 코발트와 니켈 금속의 침출자료를 이용하여 메탄술폰산과 황산의 화학적 반응성을 비교하였다. 유발과 공명효과는 두 산의 반응성에 큰 영향을 미쳤다. 동일한 침출조건에서 코발트와 니켈의 침출률은 메탄술폰산보다 황산에서 높았다. 메탄술폰산의 강한 산도와 금속염의 높은 용해도를 고려하면 메탄술폰산을 금속회수시 침출제로 이용하는 것이 가능하다.

• 환경위생공학
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• 제16권4호
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• pp.62-68
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• 2001

The advantages of hydrogen peroxide dissolution method were no discharge of noxious matter when dissolution of iron wire which used as the center supporter, reactions occur in room temperature and easy to recover dissolved iron. This study was aimed at gathering the basic data of iron wire dissolution- recovery process and proposes the reaction condition of iron wire dissolution- recovery process rind the factors influencing those reactions. The results were as follows : 1 . Hydrogen peroxide dissolution method used hydrochloric acid as the catalyst. 1. In the dissolution of iron wire(1.668 g), the condition of reaction was E1702(30 ml), HCI(20 ml) and $H_2O$(200 ml) ; time of the reaction was 18 min. P.W.(Piece weight) was 7.75 mg, and C.R. was $2.34{\;}{\Omega}$ 2. In the dissolution of iron wire(1.529 g), the condition of reaction was H7O2(30 ml), HCI(20 ml) and $H_2O$(200 ml), time of the reaction was 21 min., P.W.(Piece weight) was 7.73 mg, and C.R. was $2.35{\;}{\Omega}$. Hydrogen peroxide dissolution method used sulfuric acid as the catalyst. 1. In the dissolution of iron wire(0.834 g), the condition of reaction was $H_2O$(65 ml), $H_2SO_4$(5 ml) and 1702(5 ml) ; time of the reaction was 5 min.30 sec, P.W.(Piece weight) was 7.74 mg, and C.R. was $2.33{\;}{\Omega}$ 2. In the dissolution of iron wire(1.112 g), the condition of reaction was $H_2O$(65 ml), $H_2SO_4$(5 ml) and $H_2O_2$(5 ml) ; time of the reaction was 4 min.30 sec, P.W.(Piece weight) was 7.75 mg, and C.R. was $2.33{\;}{\Omega}$. Hydrogen peroxide dissolution method used hydrochloric acid and sulfuric acid as the catalyst confirmed a clean technology, because there were not occurred a pollutant discharged in the existing method.

• 자원리싸이클링
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• 제13권1호
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• pp.14-21
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• 2004

백금을 함유하고 있는 폐촉매가 정유공장과 화학공장에서 발생하고 있다. 백금은 고가일 뿐만 아니라 희귀하고 뛰어난 물성으로 인하여 오래 전부터 회수대상이 되어 왔다. 본 연구에서는 알루미나로 구성된 폐촉매의 담체를 황산으로 용해하여 불용성 백금을 농축하는 방법으로 석유 폐촉매로부터 백금을 회수하고자 하였다. 황산에 일부 용해된 백금은 알루미늄을 환원제로 사용하는 세멘테 이션법으로 회수되었다. 온도, 시간, 황산농도, 광액농도 등이 담체의 용해에 미치는 영향을 조사하였다. 담체가 $\Upsilon-Al_2$$O_3$로 구성된 폐 촉매를 6.0 M $H_2$$SO_4$ 용액으로 $100^{\circ}C$에서 2시간 동안 용해하였을 때 알루미나의 용해율은 약 95% 정도이었다. 담체가 $\Upsilon-Al_2$O$_3$와 $\alpha$-$Al_2$O$_3$의 혼합물로 구성되어 있는 경우, 4시간 용해하였을 때 약 92%의 알루미나가 용해하였다. 담체를 황산으로 용해한 다음 백금을 회수하는 방법을 이용하여 석유 폐촉매로부터 99% 이상의 백금을 회수할 수 있었으며 동시에 황산알루미늄을 부산물로 얻었다.

• 한국응용과학기술학회지
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• 제6권2호
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• pp.21-28
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• 1989

1-naphthol-2-sulfonic acid and 1-naphthol-4-sulfonic acid were synthesized under the dissolution of 1-naphthol in 2-nitrotoluene with stirring 98.08-90％ sulfuric acid at $5-95^{\circ}C$ for 1-5 hours. As the reaction temperatures and the reaction time were raised, the yield of 2-sulfonate was decreased, while that of 4-sulfonate was increased. But we could not observe the tendency to the various reaction concentrations of sulfuric acids. The mixtures of two isomeric 1-naphtholulfonic acids in excess concentrated sulfuric acids was quantitatively determinded by using multicomponent spectrophotomeric analysis method on the basis of the ultraviolet absorption peak of the sulfonic acids. The standard deviation in this method was ${\pm}\;2.6$, and the above method seem to be rapid and accurate.

• 한국지반공학회:학술대회논문집
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• 한국지반공학회 2003년도 봄 학술발표회 논문집
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• pp.189-196
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• 2003

Soil-cement column is often used as a contaminant barrier. This study presents the results of experimental study performed to investigate the changes of properties of soil-cement column under the attack of acids. Sulfuric nitric, and ascetic acid were used as contaminants. Specimen were made of clayey and sandy soils with addition of cement and water Permeability of soil-cement decreased with time during permeability test. When significant amount of acid percolated the specimen, permeability increased and compressive strength decreased due to the dissolution and leaching of cement and its chemical reaction compounds. Sulfuric and nitric acid were more effective than ascetic acid in deteriorating soil-cement column. Amount of acid required to lower the pH of soil cement below 12 was calculated from the results of permeability tests. This leads to a conclusion that, under the conditions employed in this study, the chemical stability of soil-cement column could be maintained against acid attack for longer than generally accepted lifetime of contaminant barriers.

• 분석과학
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• 제37권1호
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• pp.63-78
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• 2024

The continuous increasing of the global demand of copper and nickel metals raises the interest in developing alternative technologies to produce them from copper sulfide ore. Also, in line with Egypt's vision 2030 for achieving the sustainable socioeconomic development which aims at developing alternative and eco-friendly technologies for processing the Egyptian ores to produce these strategic products instead of its importing. These metals enhance the advanced electrical and electronic industries. The current work aims at investigating the recovery of copper and nickel from Abu Swayeil copper ore using pug leaching technique by sulfuric acid. The factors affecting the pug leaching process including the sulfuric acid concentration, leaching time and temperature have been investigated. The copper ore sample was characterized chemically using X-ray fluorescence (XRF) and scanning electron microscope (SEM-EDX). A response surface methodology develops a quadratic model that expects the nickel and copper leaching effectiveness as a function of three controlling factors involved in the procedure of leaching was also investigated. The obtained results showed that the maximum dissolution efficiency of Ni and Cu are 99.06 % and 95.30%, respectively which was obtained at the following conditions: 15 % H₂SO₄ acid concentration for 6 hr. at 250 ℃. The dissolution kinetics of nickel and copper that were examined according to heterogeneous model, indicated that the dissolution rates were controlled by surface chemical process during the pug leaching. The activation energy of copper and nickel dissolution were 26.79 kJ.mol^-1 and 38.078 kJ.mol^-1 respectively; and the surface chemical was proposed as the leaching rate-controlling step.

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 2005년도 추계학술대회 논문집
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• pp.585-588
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• 2005

The dissolution characteristic of metal shows the different tendency according to the applied electrical potential, the kind of electrolyte and pH value, etc. In the micro electrochemical machining (ECM), unfavorable oxide/passive layer formation and overall corrosion of electrodes must be prevented. The anodic polarization curve of nickel has distinct three dissolution regions, i.e. two active regions and the transpassive dissolution region. In this paper, the stable electrode potentials of workpiece and tool were determined in sulfuric acid and hydrochloric acid solution, respectively. In each solution, different machining property was shown and possible electrochemical reactions were discussed. On the basis of this experiment, the methodology to obtain the proper electrode potential was suggested.