• 제목/요약/키워드: Recovery of metal

검색결과 547건 처리시간 0.031초

The Pad Recovery as a function of Diamond Shape on Diamond Disk for Metal CMP (Metal CMP 용 컨디셔너 디스크 표면에 존재하는 다이아몬드의 형상이 미치는 패드 회복력 변화)

  • Kim, Kyu-Chae;Kang, Young-Jae;Yu, Young-Sam;Park, Jin-Goo;Won, Young-Man;Oh, Kwang-Ho
    • Journal of the Microelectronics and Packaging Society
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    • 제13권3호
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    • pp.47-51
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    • 2006
  • Recently, CMP (Chemical Mechanical Polishing) is one of very important processing in semiconductor technology because of large integration and application of design role. CMP is a planarization process of wafer surface using the chemical and mechanical reactions. One of the most important components of the CMP system is the polishing pad. During the CMP process, the pad itself becomes smoother and glazing. Therefore it is necessary to have a pad conditioning process to refresh the pad surface, to remove slurry debris and to supply the fresh slurry on the surface. A conditioning disk is used during the pad conditioning. There are diamonds on the surface of diamond disk to remove slurry debris and to polish pad surface slightly, so density, shape and size of diamond are very important factors. In this study, we characterized diamond disk with 9 kinds of sample.

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Recovery of Nitric acid and Copper from Plating Waste of Automobile Wheel (자동차 휠 도금박리폐액으로부터 질산 및 구리의 회수)

  • Ha, Yonghwang;Gang, Ryun-Ji;Son, Seong-Ho;Lee, Wonsik;Ahn, Jong-Gwan
    • Journal of the Korea Academia-Industrial cooperation Society
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    • 제14권11호
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    • pp.6015-6022
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    • 2013
  • It has been known that there are large amount of nitric acid and valuable metals, copper in the plating waste solution of automobile wheel. As nitric acid and valuable metals are high price and toxic, they should be recovered for economics and environment. Plating waste was extracted with TBP diluted with kerosene. The concentration of nitric acid in aqueous phase was analyzed by titration method by NaOH solution (0.1~1.0N) and the amount of metals by ICP-MS and ICP-AES. The concentration of copper in plating waste were 76,850 mg/L. The concentration of nitric acid in plating waste was 1.02 M. After three step extraction was performed with 50% TBP, each organic phase was stripped three times with distilled water to obtain 48.1% of nitric acid. Purity of final nitric acid was over 99.9% by ICP analysis. After recovery of nitric acid, copper was extracted with various solvent extractors like PC 88A, D2EPHA, LIX 84 and ISE 106. Among these extractors, 92% of copper was recovered by ISE 106 after 1st extraction and 30% $H_2SO_4$ stripping. Copper ion was reduced with $N_2H_4$ to make metal powders, respectively.

Lithium Recovery from NCM Lithium-ion Battery by Carbonation Roasting with Graphite Followed by Water Leaching (NCM계 리튬이온 배터리 양극재의 그라파이트 첨가 탄산화 배소와 수침출에 의한 Li 회수)

  • Lee, So-Yeon;Lee, Dae-Hyeon;Lee, So-Yeong;Sohn, Ho-Sang
    • Resources Recycling
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    • 제31권4호
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    • pp.26-33
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    • 2022
  • Owing to the demand for lithium-ion batteries, the recovery of valuable metals from waste lithium-ion batteries is required in future. A pyrometallurgical treatment is appropriate for recycling a large number of waste lithium-ion batteries, but Li loss to slag and dust present a significant challenge. This research investigated carbonation roasting and water leaching behaviors in Li-ion batteries by graphite addition to recover Li from the NCM-based cathode materials of waste Li-ion batteries. When 10 wt% of graphite was added, CO and CO2 gases were emitted with a rapid weight reduction at apporoximately 850 K, when heated in Ar and CO2 atmosphere. After the rapid weight reduction, NCM was decomposed and reduced to metal oxides and pure metals. In the carbonation roasting of black powder (NCM+graphite), O2 is generated via the decomposition of NCM, and an oxides, such as Li2O and NiO were were also generated. Subsequently, Li2O reacts with CO2 to generate Li2CO3, and a part of NiO was reduced by graphite to produce metal Ni. In addition, up to 94.5 % Li2CO3 with ~99.95 % purity was recovered via water leaching after carbonation roasting.

Study on Recovery of Precious Metal (Ag, Au) from Anode Slime Produced by Electro-refining Process of Anode Copper (양극동의 전해정련시 발생된 양극슬라임으로부터 귀금속(Ag, Au) 회수에 대한 연구)

  • Kim, Young-Am;Park, Bo-Gun;Park, Jae-Hun;Hwang, Su-Hyun
    • Resources Recycling
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    • 제27권6호
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    • pp.23-29
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    • 2018
  • Recently rapid economic growth and technological development have led to an increase in the generation of waste electrical and electronic equipment (WEEE). As the amount of electric and electronic waste generated increases, the importance of processing waste printed circuit boards (PCB) is also increasing. Various studies have been conducted to recycle various valuable metals contained in a waste PCB in an environmentally friendly and economical manner. To get anode slime containing Ag and Au, Anode copper prepared from PCB scraps was used by means of electro-refining. Ag and Au recovery was conducted by leaching, direct reduction, and ion exchange method. In the case of silver, the anode slime was leached at 3 M $HNO_3$, 100 g/L, $70^{\circ}C$, and Ag was recovered by precipitation, alkali dissolution, and reduction method. In the case of gold, the nitrate leaching residues of the anode slime was leached at 25% aqua regia, 200 g/L, $70^{\circ}C$, and Au was recovered by pH adjustment, ion exchange resin adsorption, desorption and reduction method. The purity of the obtained Au and Ag were confirmed to be 99.99%.

Recovery of the Vanadium and Tungsten from Spent SCR Catalyst Leach Solutions by Hydrometallurgical Methods (SCR 폐촉매 침출액으로부터 습식제련법에 의한 바나듐, 텅스텐의 회수)

  • Choi, In-Hyeok;Moon, Gyeonghye;Jeon, Jong-Hyuk;Lee, Jin-Young;Jyothi, Rajesh Kumar
    • Resources Recycling
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    • 제29권2호
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    • pp.62-68
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    • 2020
  • In new millennium, wide-reaching demands for selective catalytic reduction (SCR) catalyst have been increased gradually in new millennium. SCR catalyst can prevent the NOx emission to protect the environment. In SCR catalyst the main composition of the catalyst is typically TiO2 (70~80%), WO3 (7~10%), V2O5 (~1%) and others. When the SCR catalysts are used up and disposed to landfills, it is problematic that those should exist in the landfill site permanently due to their extremely low degradability. A new advanced technology needs to be developed primarily to protect environment and then recover the valuable metals. Hydrometallurgical techniques such as leaching and liquid-liquid extraction was designed and developed for the spent SCR catalyst processing. In a first stage, V and W selectively leached from spent SCR catalyst, then both the metals were processed by liquid-liquid extraction process. Various commercial extractants such as D2EHPA, PC 88A, TBP, Cyanex 272, Aliquat 336 were tested for selective extraction of title metals. Scrubbing and stripping studies were tested and optimized for vanadium and tungsten extraction and possible separation. 3rd phase studies were optimized by using iso-decanol reagent.

Mechanism of Tungsten Recovery from Spent Cemented Carbide by Molten Salt Electrodeposition

  • Hongxuan Xing;Zhen Li;Enrui Feng;Xiaomin Wang;Hongguang Kang;Yiyong Wang;Hui Jin;Jidong Li
    • Journal of Electrochemical Science and Technology
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    • 제14권1호
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    • pp.75-84
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    • 2023
  • The accumulation of spent carbide (YG8), not only pollutes the environment but also causes waste of tungsten, cobalt and other rare metal resources. To better address this issue, we proposed a combined electrochemical separation process of low-temperature aqueous solution and high-temperature molten salt for tungsten and cobalt. H2WO4 was obtained from spent carbide in an aqueous solution, and we calcined it to obtain WO3, which was used as a raw material to obtain tungsten by using molten salt electrodeposition. The influence of the current efficiency and the electrochemical behavior of the discharge precipitation of W(VI) were also studied. The calcination results showed that the morphology of WO3 was regular and there were no other impurities. The maximum current efficiency of 82.91% was achieved in a series of electrodeposition experiments. According to XRD and SEM analysis, the recovered product was high purity tungsten, which belongs to the simple cubic crystal system. In the W(VI) reduction mechanism experiments, the electrochemical process of W(VI) in NaCl-Na2WO4-WO3 molten salt was investigated using linear scanning voltammetry (LSV) and chronoamperometry in a three-electrode system. The LSV showed that W(VI) was reduced at the cathode in two steps and the electrode reaction was controlled by diffusion. The fitting results of chronoamperometry showed that the nucleation mechanism of W(VI) was an instantaneous nucleation mode, and the diffusion coefficient was 7.379×10-10 cm2·s-1.

Recovery of Zirconium and Removal of Uranium from Alloy Waste by Chloride Volatilization Method

  • Sato, Nobuaki;Minami, Ryosuke;Fujino, Takeo;Matsuda, Kenji
    • Proceedings of the IEEK Conference
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    • 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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    • pp.179-182
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    • 2001
  • The chloride volatilization method for the recovery of zirconium and removal of uranium from zirconium containing metallic wastes formed in spent fuel reprocessing was studied using the simulated alloy waste, i.e. the mixture of Zr foil and UO$_2$/U$_3$O$_{8}$ powder. When the simulated waste was heated to react with chlorine gas at 350- l00$0^{\circ}C$, the zirconium metal changed to volatile ZrCl$_4$showing high volatility ratio (Vzr) of 99%. The amount of volatilized uranium increases at higher temperatures causing lowering of decontamination factor (DF) of uranium. This is thought to be caused by the chlorination of UO$_2$ with ZrCl$_4$vapor. The highest DF value of 12.5 was obtained when the reaction temperature was 35$0^{\circ}C$. Addition of 10 vol.% oxygen gas into chlorine gas was effective for suppressing the volatilization of uranium, while the volatilization ratio of zirconium was decreased to 68% with the addition of 20 vol.% oxygen. In the case of the mixture of Zr foil and U$_3$O$_{8}$, the V value of uranium showed minimum (44%) at 40$0^{\circ}C$ with chlorine gas giving the highest DF value 24.3. When the 10 vol.% oxygen was added to chlorine gas, the V value of zirconium decreased to 82% at $600^{\circ}C$, but almost all the uranium volatilized (Vu=99%), which may be caused by the formation of volatile uranium chlorides under oxidative atmosphere.ere.

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Recovery of manganese compounds from electric arc furnace dust by Aluminothermy Process (테르밋 반응을 이용한 페로망간 전기로 분진의 재활용에 관한 연구)

  • Ha, Tae-Young;Jo, Young-Min;Park, Young-Koo;Kim, Youn-Che
    • Journal of the Korean Applied Science and Technology
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    • 제32권1호
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    • pp.23-30
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    • 2015
  • The properties of dust collected from electric arc furnace of ferro manganese production units was investigated, and also the metallic manganese was recovered from the dust by aluminothermy process. The ferromanganese dust collected from electric arc furnace contained about 15% of manganese oxide ($Mn_3O_4$) and 9% of carbon as the contaminant, and have a 5um of 50% median diameter and irregular particle shape. The carbon contaminant in the dust could be reduced until about 0.1~0.5% level by roasting in the air at a temperature of 600~900C for 60minutes. The recovery of manganese could not be carried out using only ferromanganese dust from electric arc furnace by aluminothermy process, but the ferromanganese which contained manganese of about 92% and iron of about 5% could be obtained from the mixture of ferromanganese dusts from electric arc furnace and converter. The best mixing condition of dust fixed at electric arc furnace dust / converter dust ratio of 1:9 and 2:8, and the mixing rato of 3:7 or more could not separated the metal and slag from the reactant after aluminothermy reaction.

A Study on the Optimal Design and Performance Analysis of the Solid-Gas Chemical Heat Transformer (고-기 화학열변환기의 최적설계 및 성능해석에 관한 연구)

  • Choi, S.H.;Lee, S.I.;Baek, I.H.;Choi, I.S.
    • Applied Chemistry for Engineering
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    • 제8권5호
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    • pp.729-736
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    • 1997
  • For the recovery of industrial waste heat, a chemical heat transformer based on the reversible reaction between metal chlorides and ammonia gas was designed and a pilot scale unit of 1 kW-1hr was developed. A static calculation, which determined the amount of reacting materials and operating condition of system, and dynamic simulations were performed for the optimal design. The temperature and output power of generator in the system were varying with the amount of salt and heat exchange area. Optimum conditions such as the amount of salt-graphite, apparent density and size of mechanical unit were determined by the dynamic simulation for the system. According to the operating cycle of 4 stages, experimental results of temperature and output power were well agreed with the simulation values. This chemical heat transformer is turned out to be a very promising system for recovery of industrial waste heat because of its effective feature of lifting temperature.

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Identification and Characterization of a Novel Thermostable GDSL-Type Lipase from Geobacillus thermocatenulatus

  • Jo, Eunhye;Kim, Jihye;Lee, Areum;Moon, Keumok;Cha, Jaeho
    • Journal of Microbiology and Biotechnology
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    • 제31권3호
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    • pp.483-491
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    • 2021
  • Two putative genes, lip29 and est29, encoding lipolytic enzymes from the thermophilic bacterium Geobacillus thermocatenulatus KCTC 3921 were cloned and overexpressed in Escherichia coli. The recombinant Lip29 and Est29 were purified 67.3-fold to homogeneity with specific activity of 2.27 U/mg and recovery of 5.8% and 14.4-fold with specific activity of 0.92 U/mg and recovery of 1.3%, respectively. The molecular mass of each purified enzyme was estimated to be 29 kDa by SDS-PAGE. The alignment analysis of amino acid sequences revealed that both enzymes belonged to GDSL lipase/esterase family including conserved blocks with SGNH catalytic residues which was mainly identified in plants before. While Est29 showed high specificity toward short-chain fatty acids (C4-C8), Lip29 showed strong lipolytic activity to long-chain fatty acids (C12-C16). The optimal activity of Lip29 toward p-nitrophenyl palmitate as a substrate was observed at 50℃ and pH 9.5, respectively, and its activity was maintained more than 24 h at optimal temperatures, indicating that Lip29 was thermostable. Lip29 exhibited high tolerance against detergents and metal ions. The homology modeling and substrate docking revealed that the long-chain substrates showed the greatest binding affinity toward enzyme. Based on the biochemical and insilico analyses, we present for the first time a GDSL-type lipase in the thermophilic bacteria group.