• Title/Summary/Keyword: 습식 제련

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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.

Hydrometallurgical Processes for the Recovery of Tungsten from Ores and Secondary Resources (원광석 및 2차 자원으로부터 텅스텐 습식 제련 기술)

  • Ahn, Hyeong Hun;Lee, Man Seung
    • Resources Recycling
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    • v.27 no.6
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    • pp.3-10
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    • 2018
  • Tungsten is a metal with high melting point and used as a raw material for the production of super alloys. Tungsten exists as $WO{_4}^{2-}$ in alkaline solution. As solution pH decreases, polymerization reaction of $WO{_4}^{2-}$ occurs to result in the precipitation of tungstic acid. The hydrometallurgical process for the recovery of tungsten from ores or secondary resources can be classified as acid and alkaline leaching. In selecting a process for the recovery of pure tungsten from secondary resources, the nature and concentration of impurities in the secondary resources and the manufactured tungsten materials should be considered.

A Study on Classification of Limonite and Saprolite from Nickel Laterite Ores (뉴칼레도니아산 니켈라테라이트광의 분급 연구)

  • Seo, Joobeom;Kim, Kee-seok;Bae, In-kook;Lee, Jae-young;Kim, Hyung-seok
    • Resources Recycling
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    • v.25 no.1
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    • pp.40-47
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    • 2016
  • Nickel laterite ore is classified into two principal ore types: saprolite (silicate ore) and limonite (oxide ore). Saprolite-type ore characterized by high magnesia and silica contents is treated by pyrometallurgy process. On the other hand, limonite-type ore is subjected to hydrometallurgy process to produce nickel products. Hydrometallurgy process requires that a raw material to meet the demands that Si+Mg contents lower than 10% and Fe content over than 40%. It is therefore required that separation of saprilite-type ore to use nickel laterite ore as a raw material for hydrometallurgy process. In this study, separation of sparolite-type ore and limonite-type ore from nickel laterite ore from New Caledonia has been tried by dry classification. The results show that -5 mm size fraction and +5 mm size fraction of the nickel laterite ore contains mainly limonite-type ore and saprolite-type ore, respectively. To understand the moisture content of the raw ore on the dry classification, nickel laterite ore with different moisture contents of 23.0% and 9.1% were subjected to the dry classification. The results show that drying of the ore makes the separation more efficient as the amount of the fine product, that can be subjected to hydrometallurgy process without further separation or drying operations, was increased.

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.

Current Status of Zinc Smelting and Recycling (아연의 제련 및 리사이클링 현황)

  • Sohn, Ho-Sang
    • Resources Recycling
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    • v.28 no.5
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    • pp.30-41
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    • 2019
  • Global production of zinc is about 13 million tons and zinc is the fourth-most widely used primary metal in the world following iron, aluminum and copper. When zinc is recycled to produce secondary zinc, it can save about 75 % of the total energy that is needed to produce the primary zinc from ore, and in therms of $CO_2$ emissions reduced by about 40 %. However, since zinc is mainly used for galvanizing of steel, the recycling rate of zinc is about 25 %, which is lower than other metals. The raw materials for recycling of zinc include dusts generated in the production of steel and brass, sludge in the production process of non-ferrous metals, dross in the melting of zinc ingots or hot dip galvanizing, waste batteries, and metallic scrap. Among them, steelmaking dust and waste batteries are most actively recycled up to now. Most of the recycling process uses pyrometallurgical methods. Recently, however, much attention has been given to a combined process of pyrometallurgical and hydrometallurgical processes.

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.

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 %.

Current Status of Nickel Smelting Technology (니켈 제련기술의 현황)

  • Sohn, Ho-Sang
    • Resources Recycling
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    • v.30 no.2
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    • pp.3-13
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    • 2021
  • Nickel is widely used due to its excellent toughness, malleability and enhanced corrosion resistance. Therefore, nickel is indispensable in our daily lives, and it is widely used in basic to advanced applications such as stainless steel, super alloys and electronic devices. Recently, nickel has been widely used as the major material in secondary batteries and capacitors. The use of nickel continues to rise and has increased from 800 thousand tonnes per year worldwide in the 1970s to about 2 million tonnes in the 2010s. However, nickel is a representative rare metal and ranks 23rd among the abundant elements in the earth's crust. This study reviews the current status of the nickel smelting processes as well as the trend in production amount and use. Nickel is extracted by a wide variety of smelting methods depending on the type of ore. These smelting methods are essential for the development of new recycling processes that can extract nickel from secondary nickel resources.