• Title/Summary/Keyword: 건식제련

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Current Status on Gold Smelting Technology (금제련(金製鍊) 기술(技術)의 현황(現況))

  • Kim, Byung-Su;Kim, Chi-Kwon;Sohn, Jeong-Soo
    • Resources Recycling
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    • v.16 no.3 s.77
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    • pp.3-11
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    • 2007
  • Presently, most of gold is smelted from gold concentrates and anode slimes. Anode slimes are by-products of nonferrous smelters such as lead and copper. In addition, gold is recovered from waste dental and medical materials, waste gold coating solution, and waste printed circuit boards (waste PCBs). The smelting method of gold from gold concentrates and various wastes containing high concentration of gold is largely divided into chlorination, cyanidation, and amalgamation methods. For the anode slimes, electrolysis method is usually used, which largely consists of roasting, high temperature melting and electrolysis processes. Also, various wastes containing low concentration of gold are mainly treated by pyrometallursical processes. In the paper, current status on gold smelting technology is reviewed, and a novel process for gold smelting which is researched in the recent is briefly introduced.

Overview on Pyrometallurgical Recycling Process of Spent Lithium-ion Battery (건식 공정을 통한 리튬이차전지의 재활용 연구 동향)

  • Park, Eunmi;Han, Chulwoong;Son, Seong Ho;Lee, Man Seung;Kim, Yong Hwan
    • Resources Recycling
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    • v.31 no.3
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    • pp.27-39
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    • 2022
  • The global demand for lithium-ion batteries (LIBs) has been continuously increasing since the 1990s along with the growth of the portable electronic device market. Of late, the rapid growth of the electric vehicle market has further accelerated the demand for LIBs. The demand for the LIBs is expected to surpass the supply of lithium from natural resources in the near future, posing a risk to the global lithium supply chain. Moreover, the continuous accumulation of end-of-life LIBs is expected to cause serious environmental problems. To solve these problems, recycling the spent LIBs must be viewed as a critical technological challenge that must be urgently addressed. In this study, recycling LIBs using pyrometallurgical processes and post-processes for efficient lithium recovery are briefly reviewed along with the major accomplishments in the field and current challenges.

A Study on Separation of Limonite and Saprolite from Nickel Laterite Ores (니켈라테라이트광으로부터 리모나이트 및 사프로라이트의 분리선별 연구)

  • Kim, Kee-Seok;Seo, Joo-Beom;Bea, In-Kook;Bae, Kwang-Hyun;Yoo, Kwang-Suk;Lee, Jae-Young;Kim, Hyung-Seok
    • Resources Recycling
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    • v.23 no.6
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    • pp.12-21
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    • 2014
  • Nickel oxide ores are composed of two kinds of minerals; one is saprolite that is processed by smelting to obtain nickel products, and the other is limonite that is used in hydrometallugical processes. It is not efficient economically to process the mixture of limonite and saprolite, so the processes to saparate the ore mixture should be developed. In the present study, the mixture was separated by dry-classification after liberationg using grindability difference between limonite and saprolite. Consequently, it is possible to obtain the limonite with less than 10% of Mg+Si contents, which could be treated by hydrometallurgical processes, when the limonite contain less than 30% of saprolite.

The Enhancement of Recycling Processes Efficiency of Lithium Ion Batteries; A Review (리튬이온전지 재활용공정 효율 향상을 위한 공정개선 연구동향)

  • Kyoungkeun Yoo;Wonhwa Heo;Bumchoong Kim
    • Resources Recycling
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    • v.33 no.2
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    • pp.24-36
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    • 2024
  • The lithium-ion battery recycling process has been classified into direct recycling, hydrometallurgical process, and pyrometallurgical process. The commercial process based on the hydrometallurgical process produces black mass through pretreatment processes consisting of dismantling, crushing and grinding, heat treatment, and beneficiation, and then each metal is recovered by hydrometallurgical processes. Since all lithium-ion battery recycling processes under development conducts hydrometallurgical processes such as leaching, after the pretreatment process, to produce precursor raw materials, this article suggests a classification method according to the pretreatment method of the recycling process. The processes contain sulfation roasting, carbothermic reduction roasting, and alloy manufacturing, and the economic feasibility of the lithium-ion battery recycling process can be enhanced using unused by-products in the pretreatment process.

Separation Technology of Pure Zirconia from Zirconsand by the Ar-H2 Arc Plasma Fusion and Sulfuric Acid Leaching with Microwave Irradiation (Ar-H2플라즈마 건식제련과 마이크로웨이브침출을 통한 지르콘샌드로부터 고순도 지르코니아 분리)

  • Lee, Jeong-Han;Hong, Sung-Kil
    • Resources Recycling
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    • v.25 no.3
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    • pp.49-54
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    • 2016
  • In this study, zircon sand is separated into zirconia and silica by using the Ar-$H_2$ arc plasma refining. And then silica is removed from it by the microwave leaching method to produce a high pure zirconia. Plasma melting consist of two sequential processes; reduction process with Ar gas only followed by refining process with Ar-$H_2$ gas. After cooling in chamber. The solid phase obtained at $240^{\circ}C$ were found to be composed of 20% sulfuric acid solution. The solution was used as a leaching solution with microwave irradiation to obtain a high purity zirconia.

Extractive Metallurgy and Separation Technology of Rare Earth Ores (교토류광석(橋土類鑛石)의 제련(製鍊) 및 분리(分離) 기술(技術))

  • Lee, Man-Seung;Jeon, Ho-Seok
    • Resources Recycling
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    • v.19 no.6
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    • pp.27-35
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    • 2010
  • Rare earth alloys and compounds are the raw materials for the manufacture of advanced materials. Although domestic monazite ores have been found, there are some difficulties in recovering rare earth from these ores. Rare earth ores are found in few countries and these countries put an embargo on the export of rare earth ores for the protection of their industry. We gathered some information on the hydrometallurgical and pyrometallurgical processes to recover rare earths from bastnasite, monazite, and xenotime which consist of 95% of the total rare earth ores. Since rare earth with the purity more than 6N is needed for use in advanced materials, some separation methods such as fractional crystallization, precipitation, ion exchange, and solvent extraction were introduced.

Recovery of Uranium in $LiF-BeF_2$ Molten Salt System by Electrowinning ($LiF-BeF_2$ 용융염계에서 전해제련에 의한 우라늄 회수)

  • 우문식;김응호;유재형
    • Proceedings of the Korean Radioactive Waste Society Conference
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    • 2003.11a
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    • pp.426-430
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    • 2003
  • Fissionable uranium will be separated from long-lived nuclear materials in pyroprocess for transmutation. This study was measured decomposition voltage and deposition rate on cathode of uranium in $LiF-BeF_2$ molten salt by electrowinning. The result of experimental is that decomposition voltage of $UF_4$ and $LiF-BeF_2$ molten salt is -1.4 and -1.5 volt at $500^{\circ}C$ Deposition rate of uranium on cathode increases with increase of uranium concentration in molten salt.

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Status of Pyrometallurgical Treatment Technology of EAF Dust (제강분진의 건식 처리기술 현황)

  • Sohn, Ho-Sang
    • Resources Recycling
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    • v.27 no.2
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    • pp.68-76
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    • 2018
  • EAF (Electric arc furnace) dust is an important secondary resource such as zinc, lead, and iron. Recycling of EAF dust is benefit to solving disposal and environmental problems caused by the heavy metals entrained in the dust. In this study, pyrometallurgical treatment technology of EAF dust reviewed for the improvement of conventional process and development of new process. The existing technologies categorized into four groups: those by rotary kiln process, rotary hearth furnace (RHF) process, shaft type process, and reduction smelting process. The product of these processes are ZnO and Fe or slag as a waste. Their mechanisms for the production of ZnO from EAF dust were carbothermic reduction and oxidation of zinc gas with air.

A Study on the Recycling Process of Nickel Recovery from Inconel 713C Scrap based on Hydrometallurgy (인코넬 713C 스크랩으로부터 니켈 자원 회수를 위한 습식제련 기반 재활용공정 연구)

  • Min-seuk Kim;Rina Kim;Kyeong-woo Chung;Jong-Gwan Ahn
    • Resources Recycling
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    • v.33 no.4
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    • pp.36-46
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    • 2024
  • We investigated a hydrometallurgical process of nickel recovery from Inconel 713C scrap. The process proceeded with a series of i) comminution of pyrometallurgical treated scrap, ii) sulfuric acid leaching, iii) solvent extraction of unreacted acid, molybdenum, aluminum, and precipitation of chromium, iv) crystallization of nickel sulfate by vacuum evaporation, and v) nickel electrowinning. The nickel-aluminum intermetallic compound, Ni2Al3, was formed by the pyrometallurgical pretreatment readily grounded under 75 ㎛. Sulfuric acid leaching was done for 2 hours in 2 mol/L, 20 g/L solid/liquid ratio, and 80 ℃. It revealed that over 98 % of nickel and aluminum was dissolved, whereas 28 % of molybdenum was. A nickel sulfate solution with 2.34 g/L for the crystallization of nickel sulfate hydrate was prepared via solvent extraction and precipitation. Over 99 % of molybdenum and aluminum and 93 % of chromium was removed. Nickel metal with 99.9 % purity was obtained by electrowinning with the nickel sulfate monohydrate in the cell equipped with anion exchange membranes for catholyte pH control. The membrane did not work well, resulting in a low current efficiency of 73.3 %.

Recycling of Copper Scrap (동스크랩의 리사이클링)

  • Sohn, Ho-Sang
    • Resources Recycling
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    • v.28 no.3
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    • pp.3-14
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    • 2019
  • Copper is one of the first metals utilized by humankind about 11,500 years ago. But copper is not plentiful metallic element in the earth's crust. Copper has a high thermal and electric conductivity and is relatively corrosion resistant. In principle copper is virtually 100 % recyclable as an element without loss of quality. The recycling of copper scrap reduces the energy consumption and environmental burden, comparing to the primary metal production. Currently, approximately 30% of the global copper supply provides by recycling. Copper scrap is smelted in primary and secondary smelter. Type of furnace and process steps depend on the quality and grade of scrap. Depending on copper content of the secondary raw material, refining is required, which is usually done through electrorefining. This work provides an overview of the primary copper production and recycling process.