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By Marcel Magnusson, Guozhu Ye, Pekka Vaananen, Yang Tian

The most used technology for recycling of spent alkaline batteries consists of crushing, magnetic separation and processing of the nonmagnetic fraction, black mass, using a rotary kiln. In the process only zinc is recovered and all manganese in the black mass is lost. According to the EU regulation for recycling of batteries, more than 50% of batteries should be recovered. To meet the demand, Swerea MEFOS has together with a major battery recycler IsoLogistics in Finland and Sweden developed technologies for efficient recovery of zinc and manganese aiming for >50% recovery. This paper will focus on a treatment process using a DC furnace to produce a ZnO- and a MnO-product. The process has been demonstrated in pilot scale, 1 ton/h. The major outcomes will be highlighted. Another approach by using thermal vacuum technology for distillation of zinc metal has also been demonstrated in laboratory scale which is also reported in this paper.

Mar 1, 2018

By Pei-xiao Liu, Han-jie Guo, Yan-xiang Li

The thermodynamic analysis on chromium ore pellets in solid reduction chromium process is carried out, and the result is validated by pre-reduction experiment of cold briquetted chromium ore. Polarization Microscope and SEM are employed to observe microstructure and element composition. The thermodynamic and experimental results reveal the reduction mechanisms at different temperatures in the SRC pre-reduction process.

Mar 1, 2017

By HeeDong Lee, Owen Reedy, Lawrence Matson, Naidu Seetala, Thomas Key

Spark Plasma Sintering (SPS) consolidated ZrB2+SiC composites using nano-powders (around 40 nm) showed smaller grains compared to those using micron size powders and segregation of SiC into islands is minimal but with higher oxidation of ZrB2 to form ZrO2 in nano-composites. Argon-gas purging prior to SPS consolidation at around 2000 °C and 40 MPa of ZrB2+20vol.%SiC nano-powders was used to minimize the oxidation and obtain fine granules with high densification. The densification of the Argon-gas purged nano-composites is higher compared to those consolidated without Argon gas purging. The EDX analysis showed a strong reduction in the oxygen peak for the Argon gas purged composites. The XRD spectra also support this observation with less ZrO2 phase composition in Argon gas purged composites. The Vickers micro-hardness showed slightly lower values for Argon gas purged composites though they have higher densification.

Mar 1, 2017

By J. David Chapman

There are a variety of choices of materials for mineral extraction processing. Traditionally, end users have used metallic piping for fluid handling and little is known about the advantages (or limitations) of non-metallic piping systems. This presentation will review custom FRP pipe systems and their use in severe corrosive and erosive process streams. These systems can be designed to various pressure and temperature ratings and different components (such as resin and glass type) can be varied to suit the process conditions

By Huimin Lu, Neale R. Neelameggham, Guangzhi Wu

In China’s Inner Mongolia Tuquan County, 1.4 billion tons of reserves of serpentine deposits were found. Because serpentine belongs to magnesium silicate, there is no good reducing agent to reduce magnesium. In the local there is also a large reserves of high-aluminum bituminous coal for thermal power, power plants each year produce a large number of high-aluminum fly ash. The aluminum-silicon alloys obtained from this high-aluminum fly ash as the raw material by carbothermal reduction method can reduce the magnesium from the serpentine. In this paper, first, the feasibility of producing aluminum-silicon alloys by carbothermal reduction of high-alumina fly ash was studied, the hypereutectic aluminum-silicon alloys were obtained; and then the investigation on aluminum-silicon alloy as a reducing agent to reduce of metal magnesium from serpentine was carried out. According to the previous investigation, the optimized technical process for the extraction of metal magnesium from serpentine was proposed.

Mar 1, 2018

By Shilai Yuan, Huimin Lu, Panpan Wang

A big andalusite ore bed was found in Dingxi District, Gansu, China. In this paper, the feasibility of producing solar grade silicon from aluminum-silicon alloys by carbothermal reduction of andalusite ore was studied. First, the carbothermal reduction experiments were conducted in a 100 kVA DC submerged arc furnace with reducing temperature 2000–2200 °C and reducing time 4 h, the hypereutectic aluminum-silicon alloys containing 50–55 mass% aluminum and 35–45 mass% silicon were obtained; then the investigation on solidification of the hypereutectic Al-Si melts under the temperature gradient as an intensified separation silicon way was carried out. According to previous investigation, the optimized technical process for solar grade silicon and eutectic Al-Si alloy from andalusite ore was proposed.

Mar 1, 2017

By Shengli Wu, Feng Chang, Hua Lu, Jianliang Zhang

Kinetic studies of the blast furnace dust (BFD) reduction process have been carried out under non-isothermal conditions. BFD pellets were made with bentonite as the binder. A Comprehensive Thermal Analyzer (TG-DSC) was used to determine the mass loss of pellets, which were heated at three heating rates of 10, 20, 30 K/min up to 1493 K. Furthermore, the metallization rate and mineral composition of BFD pellets heated to several different temperatures were analyzed by chemical analysis and X-ray diffraction (XRD). It was found that, with its inherent carbon resources as the reducing agent, the metallization rate of BFD pellets could reach 88% at most. The reduction and weight loss process of iron oxides mainly happens above 1273 K. In addition, from application of the Coats-Redfern equation the apparent activation energy of the reduction from wustite to Fe was 443 kJ/mol and the mechanism was interface reaction R..

Mar 1, 2017

By Weizhi Zeng, Michael L. Free, Sayan Sarkar, Prashant K. Sarswat

Black Phosphorus was recently discovered as a 2D material and it exemplified huge prospects for application in electronics, optoelectronics, photonics and catalysis. It is a direct band semiconductor with tunable band gap varying from 0.35 eV (bulk) to 2 eV (single layer). But the layer dependent band gap of black phosphorus restricts it to make use of the full spectra of sunlight for absorption. First principle calculations were performed using ‘Quantum Wise Atomistic Toolkit’ package with Perdew-Burke-Ernzerhof (PBE) exchange-correlation for black phosphorus doped with non-metallic dopants of B, S and Se and metallic dopants of Ti, Mg and In. It has been found that doping with non-metallic impurities result in a small diminution of the band edges (0.96–0.57 eV), whereas doping with metallic impurities decrease the band edge drastically (0.85–0.025 eV). Moreover, it was also observed that dopants with an even number of valence electrons incorporated a metallic nature of black phosphorus, whereas dopants with odd number of valence electrons further attributed to its semiconducting features. Thus in a holistic discernment, black phosphorus with the incorporation of some dopants in appropriate amounts can absorb more visible range of the optical spectra, making it ideal for use in photovoltaics.

Mar 1, 2017

By Batric Pesic

The interactions of mineral-pyrite with T. ferrooxidans were studied by using a cyclic voltametry technique. The interactions with bacteria were carefully examined during the entire growth stage of bacteria (fermentation). Several very important discoveries were made. For example, the pyrite surface invariably drastically changed its properties at the second day of fermentation. Beyond two days of fermentation, the cyclic voltamograms were insensitive to convective diffusion produced by stirring. The SEM study revealed that bacteria populated the pyrite surface at an extremely high density levels. The high density of bacteria, and the solid reaction products formed on the pyrite surface created conditions for pore diffusion which explained why the CVs became insensitive to convective diffusion in solution (stirring).

Jan 1, 1990

By Shengfan Zhou, XUEWEN WANG, Bianfang Chen, Mingyu Wang

Vanadium was leached from roasted stone coal by NaOH solution, and the effect of leaching temperature, leaching time, addition of NaOH, liquid to solid ratio, the grinding fineness of stone coal, and stirring speed on the vanadium leaching rate was studied. The kinetics analysis for the process is presented by the shrinking core model. The results show that the vanadium leaching ratio of roasted stone coal can be beyond 75% at the 6% NaOH addition, leaching temperature of 95°C, leaching time of 7h, liquid to solid ratio of 1.2mL/g, and grinding fineness of 0.111mm. The leaching process is controlled by interfacial reaction kinetics and the apparent activation energy was 59.36kJ/mol.

Jan 1, 2016

By Kathryn C. Sole

A novel solvent-extraction process for the refining of gold was recently commercialised, with the commissioning in May 1997 of a 24 t a-' refinery at Harmony Gold Mine in Virginia, South Africa. The MinataurTM Process (Mintek Alternative Technology for Au Refining) uses solvent-extraction technology to produce gold of 99.99% purity from the cathode sludge arising from a conventional carbon-in-pulp / electrowinning circuit. Implementation of this process introduces significant cost benefits compared with the conventional dore smelting / toll-refining route previously followed. This paper outlines the process, presents selected operating results obtained during the first few months of operation, and provides some details of the associated techno-economic advantages.

Jan 1, 1998

By Patrick M. Eduafo, Brajendra Mishra, Mark L. Strauss

Direct acid leaching of rare earth metals (REMs) from waste lamp phosphors is non-selective, leading to co-dissolution of impurities mainly calcium, phosphorus, silicon, iron and zinc. Calcining the phosphor powder at different temperatures followed by leaching with HCl isn’t efficient for the extraction of all the chief rare earths especially cerium (Ce), lanthanum (La) and terbium (Tb). Therefore, multi-stage leaching operations are required for the separation of the REMs in phosphor dust. This paper will outline a new process for extracting Ce, La, Tb, Eu and Y from waste fluorescent lamps using a three-stage leaching and separation process. A flowsheet has been developed which shows this process is selective and efficient.

Jan 1, 2015

By Yan Wen

For the impurities in the copper smelting waste acid, SO3, Cu, As, Pb, Zn, Re and other elements enter the waste acid and generate a lot of arsenic residue, gypsum and neutralized residue, in which Cu, Zn and Re metals have not been recycled. Cu, Re and As are separated by step-wise vulcanization. The valuable metals of Cu, Zn and Re are recovered by separating zinc through pH adjustment. Calcium injection is conducted for boiler for reducing the amount of SO3. The residues generated in the form of arsenate and hydroxide will be returned together with arsenic filter cake for smelting treatment so as to achieve the purpose of valuable metal recycling and solid waste reduction and harmless treatment.

By Aichun Zhao, Rui Wang, Yihong Li, Yanping Bao, Yafeng Ji, Jiansheng Liu, Xiao Hu, Qingxue Huang

The slag entrapment under different conditions of 80t blowing argon ladle furnace was investigated by physical simulation. The water was used to simulate liquid steel and liquid paraffin was for slag. The processing of slag entrapment under different blowing structures was analyzed and the critical velocity and critical droplets diameter of describing it was obtained. Based on the experiments, the relationship between the interface flow velocity and the critical blowing rate CBR was deduced. In the real process, it is suggested that the bottom blowing rate is from 40 L/min to 180L/min when the interface tension is 0.12~1.2 N/m during the soft argon blowing.

Jan 1, 2016

By Takahiro Furuzono

Saganoseki Smelter and Refinery of Pan Pacific Copper Co., Ltd. started treating copper anode slimes using a unique hydrometallurgical process in chloride media in 1997. The process comprises the following stages, decopperizing, wet chlorination, solvent extraction for gold, silver chloride reduction, and separate reduction stages that treat the gold extraction raffinate with sulfur dioxide gas. Precious metals and rare metals in the copper anode slimes are dissolved in an aqueous solution of hydrochloric acid by oxidative leaching, which is termed wet chlorination. Gold is efficiently extracted from the chlorination liquor by dibutyl carbitol in the solvent extraction stage. Gold is reduced by oxalic acid from goldloaded dibutyl carbitol and recovered as gold powder. The gold powder is cast directly into granules or ingots of more than 99.99% purity without electrorefining. Selenium is recovered as a selenium residue by reduction with sulfur dioxide gas and refined through vacuum distillation. The plant was designed to process 132 tonnes of copper anode slimes per month and has a current capacity of 206 tonnes per month due to several enhancements. Compared with the conventional process, the hydrometallurgical process described here provides some advantages, in particular, a higher product quality, shorter gold-retention time, and reduction in environmental load.

By Jianhua Xin, Min Chen, Lei Xu, Haohua Deng, Nan Wang

A mathematical model of converter slagging and steelmaking process by replacing part of lime with limestone is established. The rate equations of oxidation reactions and lime dissolution in converter under the limestone substitution proportion increasing from 25 to 50% can be obtained and the effects of limestone substitution proportion on the variations of the composition of hot metal, slag and converter gas during the steelmaking process are investigated. In the process of converter slagging and steelmaking by replacing part of lime with limestone, increasing the hot metal temperature and the lance height could be favor to increase the content of FeO in the slag and accelerate the limestone decomposition and dissolution. With the limestone substitution proportion increasing from 25 to 50%, the maximum of oxygen supply ratio increases from 10.7 to 19.7% and the temperature drop of converter bath is 8–60 °C.

Mar 1, 2018

By Naixiang Feng, Kun Zhao

This work presents a two-stage aluminothermic reduction process for preparing Ti and Ti-Al alloys using Na2TiF6. Al-Ti master alloy and pure cryolite as co-products could be obtained. After the first stage reduction, the oxygen content of the metal product is reduced, and the second stage produces high-purity titanium or Ti-Al alloys with cryolite and Al-Ti master alloy as recyclable co-products.

Mar 1, 2017

By Shengli Wu, Yuandong Pei, Shaoguo Chen, Zhixing Zhao, Haijun Kang, Jiangshan Shi, Wen Pan, Zhengming Cheng, Yaosheng Luo

Grate bar is the key component of the sinter machine used for loading sinter and raw materials. Bar channels are sometimes bonded into blocks, which affects the service life of bar, and more importantly reduces the effective ventilation area of the sintering, affecting the normal production of sintering, resulting in unstable negative pressure, higher electricity consumption, and lower production and quality of sinter. In order to solve this problem, the systematic study was done on bonding materials of bars, based on which bonding mechanism of sinter grate bars was obtained. The KCl is an important characterization of bonding. Control standard of blending ore that prevents bonding is K2O content below 0.06% and Cl content below 0.05%.

Mar 1, 2018

By Wen Liangying, Zou Chong, Tan Xiuqin, Bai Chenguang, Zhang Shengfu

"Eight typical metallurgical byproducts containing iron were selected based on the effect of the chemical composition, particle size, additives on the burnout degree of pulverized coal. Effect of three typical byproducts including fine iron ore, BOF dust and BOF sludge on combustion reactivity and combustion efficiency were investigated using TG-DSC method. The results indicated that the three additives have obvious catalytic effects on pulverized coal. By comparison, the relative active sequence of byproducts to the catalytic combustion can be described as follows: BOF dust>BOF sludge>fine iron ore. Moreover, adding BOF dust as component of additives also shows significant catalytic effects on combustion efficiency during rapid heating process.IntroductionChina is the largest producer in the world with an annual output reaching over 6 billion tons. Solid wastes arising from iron and steel making increases the environment pressure in recently years. For instance, annual output of dust during the production of iron and steel making in China reach up to 5 million tons, which is close to 8%~15% of the amount of steel [1]. Another characteristic of these byproducts is they are finer particle which are just harder to deal with. Since some of solid wastes, including dusts, scales, and sludge, usually contain high iron content, sintering plants have traditionally been used to recycle byproducts in integrated steel plants in China. However these byproducts also have noticeable effects on sinter quality, sinter strength and productivity and, therefore, waste recycling is limited depending on the analysis of the waste materials [2]. Another method which is pre-treatment of byproducts in pelletizing process, increases of energy consumption and production cost. In addition, metallurgical byproducts often contain heavy metals and alkalis. For these reasons, recycling rate of the byproducts in China is very low. Therefore, how to recycle the byproducts in iron and steel making process is an important subject."

Jan 1, 2012

By Xiaolong Lin, Yuanbo Zhang, Guanghui Li, Zhizhong Li, Zhiwei Peng, Tao Jiang, Yan Zhang, Yutian Ma

Pyrometallurgical processes for recovering platinum group metals (PGMs) from spent catalyst have been the focus of current research for many years. They suffer from high energy consumption, large trapping agent consumption and huge slag production. Because of versatility of PGMs-containing spent catalysts, comprehensive recovery of valuable metals from these catalysts from an experimental point of view remains a challenge. In this study, thermodynamic analysis of pyrometallurgical smelting process in the presence of various additives for ef ficient recovery of PGMs was performed. It showed that addition of sodium salts would promote the migration and separation of the precious metals from carrier of the spent catalyst. By replacing calcium oxide with sodium carbonate and sodium borate, the smelting temperature could be reduced by more than 200 °C, which agreed well with the experimental findings.

Mar 1, 2018