• Title/Summary/Keyword: 황산아연

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Recovery of Zine sulfate from zine sulfate waste water contain organic compound (유기물이 포함된 황산아연폐수로부터 황산아연의 회수)

  • Yoon, Guk-Joung;Lee, Tack-Hyuck
    • The Journal of Natural Sciences
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    • v.14 no.2
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    • pp.33-40
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    • 2004
  • The eliminating of organic compound is essential process of the recovery of zinc sulfate from zinc sulfate waste water contained organic compound. The ozone oxidation and adsorption treatment is good for eliminating of organic compound in waste water. The zinc oxide treated an excess of sulfuric acid for zinc sulfate. We got zinc sulfate 740g from water 1kg.

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Study on the Interaction between Depressants Zinc Sulfate and Xanthate on the Flotation of Sphalerite (섬아연석 억제제인 황산아연과 잔세이트의 상호 작용에 관한 연구)

  • KIM, Minkyu;YOU, Kwangsuk
    • Resources Recycling
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    • v.29 no.6
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    • pp.98-103
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    • 2020
  • In this study, the depression behavior of zinc sulfate on the sphalerite with the addition of potassium butyl xanthate was investigated to clear the relationship between zinc sulfate and xanthate in depression of sphalerite. As a result of the experiment, it was confirmed that the depress effect of zinc sulfate on the sphalerite declined with the increase of its addition amount. From the results of SEM-EDS and FT-IR analysis, it was found out that the amorphous precipitate of metal xanthate (Zn-BX) was formed in sphalerite concentrate, when the solubility product of [Zn+]·[BX] in the pulp solution exceeded 3.71×10-11, which is the solubility of Zn-butyl xanthate. It is considered that the Zn-butyl xanthate had a negative effect on the depression of sphalerite.

Study for Manufacturing of Zinc Sulfate from Electric Arc Furnace Dust by Hydrometallrugical Process (제강분진으로부터 습식제련공정에 의한 황산아연의 제조 연구)

  • Dong Ju Shin;Sung-Ho Joo;Dongseok Lee;Shun Myung Shin
    • Resources Recycling
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    • v.32 no.1
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    • pp.33-41
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    • 2023
  • Herein, we selectively recovered Zn and produced ZnSO4 from electric arc furnace dust using a hydrometallurgical process. The analysis of the properties of the electric arc furnace dust revealed that the Fe content (9.9%) was relatively low while the Mn content (19%) was high as compared to the composition of general dust. Therefore, an appropriate hydrometallurgical process was designed based on the properties of the raw materials. In the leaching process involving the use of 1.6 M sulfuric acid and 20% solid-liquid ratio at 60℃ for 1 h, 85% of the Zn and Mn got dissolved while the Fe was not leached. To selectively recover Zn, a solvent extraction process using D2EHPA as the extractant was chosen, and 99% of the Zn was extracted using 0.8 M D2EHPA with 32% saponification and an O/A ratio of 2 using counter-current 3-stage extraction. Mn was entirely scrubbed with an aqueous sulfuric acid solution of pH 1.5. Finally, Zn was concentrated and stripped using 1.5 M sulfuric acid at an O/A ratio of 4 using counter-current 4-stage stripping. The stripping solution contained 40 g/L of Zn, and 99.9% of ZnSO4∙H2O was obtained by vacuum distillation.

Sulfuric Acid Leaching of Zinc and Manganese from Spent Zinc-Carbon Battery (황산에 의한 폐망간전지로부터 아연과 망간의 침출)

  • Sohn Hyun-Tae;Ahn Jong-Gwan;Sohn Jeong-Soo;Park Kyoung-Ho;Park In-Yong
    • Resources Recycling
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    • v.11 no.4
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    • pp.44-50
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    • 2002
  • Characteristics on the sulfuric acid leaching of zinc and manganese from the spent zinc-carbon battery powders obtained by cushing and magnetic separation, were investigated with the variation of sulfuric acid concentration, reaction temperature, stir-ring speed and solid/liquid ratio. The sample powders were composed of Zn metal, ZnO, $MnO_2$ and $Mn_2$$O_3$. and it was found that the selective leaching of zinc was difficult in this system. At the condition of S/L ratio 1:10, IM H$_2$$SO_4$, $60^{\circ}C$ and 200 rpm, leaching rate of Zn and Mn are 92% and 35% respectively. The concentration of Zn and Mn in the leaching solution are 19.5 g/l, 7.8 g/l and pH of that solution is 0.75. It was confirmed at reducing agent should be added to increase e leaching rate of manganese with sulfuric acid.

Voltammetric Study on the Underpotential Deposition of Zinc

  • Lee, Joong-Bae;Paul F. Duby
    • Journal of the Korean institute of surface engineering
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    • v.26 no.3
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    • pp.135-142
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    • 1993
  • 탄소강 및 Nickel 음극에서 아연의 전착특성에 대하여 조사하였다. 황산아연 및 염화아연용액속에서 회전전극을 사용하여 실험한 결과 아연의 평형전위 이전에서 전착이 일어나는 소위 Underpotential Deposition 현상이 관찰되었다. 또한 이렇게 전착이 일어난 아연층은 평형상태에서 일정한 두께로 제한되는데 전착전압에 따른 전착층의 전하량을 계산한 결과 다층흡착구조과 유사한 경향을 나타내었다.

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Effects of Electricity Supporting Agents on the Characteristics of Electroplated Zinc Layer from Sulfuric Bath (황산욕에서 전기아연 도금 피막 특성에 미치는 전기전도 보조제의 영향)

  • 남궁성;이용진;정연수;전유택
    • Proceedings of the Korean Institute of Surface Engineering Conference
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    • 2000.05a
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    • pp.51-52
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    • 2000
  • 전기아연도금강판은 표면이 미려하고 희생방식력이 뛰어나기 때문에 주로 자동차와 가전, 건자재 등에 많이 사용된다. 현재 냉연 표면처리 제품들은 연속도금공정에 의해 생산되고 있으며 고전류밀도에 의한 고속생산과 도늠액 제조와 조성이 비교적 단순해야 하는 여러 가지 이유로 염산욕과 황산욕을 가장 많이 사용하고 있다. 최근에 신설된 당사의 전기도금공정은 수직형으로 황산욕에서 불용성 양극을 채용하여 아연을 전기도금하고 있다. 일반적으로 황산욕은 염산욕 대비 전기 전도성이 나빠 과전압이 크게 걸리므로 불용성 양극을 사용하여 극간 거리를 최소화할 필요가 있다. 그러나 $Ir0_2$가 코팅된 불용성 양극은 가격이 비싸기 때문에 극간 거리를 너무 짧게 하면 깡대에 의해 손상을 받을 수가 있어 극간 거리를 줄이는데 한제가 있다. 따리서 용액의 전도도들 증가시켜 과전합을 줄이기 위해서는 타사에서 현재 사용하고 있는 황산나트륨, 황산칼륨, 황산암모늄 등에 대한 검토가 필요하다. 전기전도 보조제들은 용액의 전기전도도 뿐만 아니라 도금층의 외관 및 미세구조에도 많은 영향을 주는 것으로 알려져 있다. 따라서 본 연구에서는 황산나트륨, 황산암모늄의 농도를 변화시켜 표면외관, 한계전류밀도, 미세구조, 우선배향성 등을 조사하여 최적의 물성을 갖는 아연 도금층을 얻기 위한 조건을 도출하고자 하였다. 전기아연도금용 소재로는 두께 0.8mm이고 크기가 $100{\times}120mm$인 중저탄소강 (0.02% C)을 사용하였으며 전처리 과정으로 탈지와 산세를 행하고 현장 도금액을 사용하여 다음과 같은 조건 하에서 아연도금을 행하였고 극간전합을 측정하였다. 도금 후 표면의 미세구조는 SEM을 사용하여 관찰하였으며 표면외관 특성을 분석하기 위해 광택도계(Tri- Microgloss-60-85)를 이용하여 입사각 $60^{\circ}$ 에서 광택도를 측정하였고, 색차계(Color Quest II Hunter Lab.)를 사용하여 백색도를 각각 측정하였다. 또한 X선 회절기를 이용하여 도금층의 우선 배향성을 분석하였다.

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Survey on rechargeable battery of MnO2-Zn using aqueous solution (수용성 전해질을 이용한 이산화망간 2차 전지에 대한 고찰)

  • Park, S.J.;Shin, H.S.;Kim, Y.C.;Oh, C.S.
    • Journal of Energy Engineering
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    • v.25 no.4
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    • pp.245-250
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    • 2016
  • Manganese dioxide is the material which has a good characteristic property for a secondary cell. We have surveyed on rechargeable battery of zink-manganese dioxide using aqueous solution and we also surveyed on redox reversibility of zink-manganese dioxide for checking up possibility for a secondary cell. We have found out to be active for charging and discharging of those.

Removal of Copper and Zinc Ions by Neutralization from the Spent Sulfate Solutions of Brass Bulb Base (황동(黃銅) 전구(電球) Base 제조과정(製造過程)에서 발생(發生)한 구리와 아연 함유(含有) 황산폐수(黃酸廢水)의 중화법(中和法)에 의한 제거(除去))

  • Lee, Man-Seung;Ahn, Jae-Woo;Lee, Chang-Hae
    • Resources Recycling
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    • v.16 no.6
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    • pp.39-45
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    • 2007
  • Optimum condition for neutralization has been studied to remove the copper and zinc ions from spent sulfate solutions which resulted from the acid washing of the base of brass bulb. Chemical distribution of copper and zinc species and the variation of solubility of the two ions with solution pH were obtained by considering the complex formation reaction and mass balance. Removal percentage of zinc was more sensitive to solution pH than that of copper. This results from the fact that the solubility of zinc is higher than that of copper. The form of coagulant affected little the removal percentage of zinc, while addition of coagulant as the phase of solution resulted in higher removal percentage of copper than as the phase of solid.

The Optimization of Hydrometallurgical Process for Recovery of Zinc from Electric Arc Furnace Dust (Part I : leaching process) (습식산화법을 이용한 제강분진 내 아연회수를 위한 최적조건 도출에 관한 연구(Part I; 침출공정))

  • Moon, Dea-Hyun;Ahn, Sang-Woo;Kim, Han-lae;Kim, Ji-Tae;Chang, Soon-Woong
    • Resources Recycling
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    • v.24 no.3
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    • pp.27-33
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    • 2015
  • EAFD (Electric Arc Furnace Dust) is considered as pernicious pollutant, assigned hazardous waste. Since this dust is a by-product of industry, it contains valuable metals such as Fe, Zn, Ni, Cu which can be turned into resources by recycling process. In this study, hydrometallurgical process was applied to recover Zn from Electric Arc Furnace Dusts. The result showed 95% Zn recovery at 3M $H_2SO_4$, Solids/Liquid ratio 1:2 and aeration of 1.8L/min for 2hr. However there was 80% Zn recovery at lower $H_2SO_4$ concentration apply for pilot scale plant.

A Study on the Efficiency of Zinc Fertilizers Using Zn-65 (Zn-65를 이용(利用)한 아연비료(亞鉛肥料)의 유효도(有效度)에 관(關)한 연구(硏究))

  • U., Zang-Kual
    • Applied Biological Chemistry
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    • v.20 no.2
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    • pp.255-261
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    • 1977
  • Using tracer technique of Zn-65, a pot experiment has been carried out in order to evaluate the efficiency of zinc fertilization on two paddy soils; an acidic from Kimpo and an alkaline from Yeongweol. The sources of zinc were zinc sulfate, zinc carbonate, zinc chloride and zinc oxide. Two rates of zinc were applied to the soils and control treatment was also included for this study. The methods of zinc application were uniform mixing throughout the soil, applying to the soil surface and irrigation water, and root dipping with zinc oxide at transplanting. In general, Yeongweol soil had higher efficiency of zinc fertilizers than Kimpo soil. The results showed that zinc fertilizer application should be required to improve the rice growing conditions in Yeongweol soil especially at early stage of growth after transplanting. As to the application method of zinc fertilizers, mixing treatment appeared to be most superior to any other methods in both soils. In addition, it is found that root dipping in the zinc oxide suspension would be a rather effective method of zinc application. In aspect of fertilizer efficiency there was no superiority or inferiority among the zinc sources used in this experiment.

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