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Suorineni F.T.,Laurentian University | Suorineni F.T.,University of New South Wales | Mgumbwa J.J.,Laurentian University | Kaiser P.K.,Laurentian University | And 2 more authors.
Transactions of the Institutions of Mining and Metallurgy, Section A: Mining Technology | Year: 2014

Part 1 of the paper defined shear loaded orebodies and showed through case histories that both pillars and excavations are at elevated risks of failure when mining these orebodies. Part 2 of the paper presents new knowledge on the behaviour of pillars and excavations when mining such orebodies. Numerical modelling is used to understand the behaviours of these structures in the orebodies. It is established that pillars in shear suffer confinement loss compared to their equivalents under pure compression. The confinement loss increases with increasing shear loading in pillars with width : height (W : H)§1. For pillars with W : H §1, the Lunder and Pakalnis (1997) empirical pillar design chart should be used with caution. For excavations in eccentrically loaded orebodies, passive and active high stress envelopes are created in the excavation process. The combined effect of the active high stress and tension zones often results in excavation surface sloughing. © 2014 Institute of Materials, Minerals and Mining and The AusIMM. Source


Xu M.,Vale Base Metals Technology Development
Separation Technologies for Minerals, Coal, and Earth Resources | Year: 2012

Over the years, a comprehensive procedure has been established for ore evaluation and flowsheet development at Vale Base Metals Technology Development. When an ore sample arrives from a mine with an existing concentrator, the ore is subject to a set of standardized tests following a known flowsheet. This is termed ore evaluation. When an ore sample comes from an exploration project, the ore is subject to testwork that starts from simple batch tests to complex flowsheet tests. This is termed flowsheet development, which consists of nine steps that generally proceed in sequence: sample selection/ore preparation, grinding time determination, mineralogy analysis using Mineral Liberation Analyzer, incremental rougher flotation, staged rougher and scavenger flotation, batch full circuit simulation test, spreadsheet calculations, miniplant testing (20-50 kg/h), and pilot plant testing (>100 kg/h). This paper describes these steps and discusses the best practices for reliable and accurate assessment of ore separability. Source


Bobicki E.R.,University of Alberta | Liu Q.,University of Alberta | Xu Z.,University of Alberta | Manchak N.,University of Alberta | Xu M.,Vale Base Metals Technology Development
Materials Science and Technology Conference and Exhibition 2013, MS and T 2013 | Year: 2013

Grinding required for mineral liberation represents the largest energy consumption in mineral processing. Great effort has been made to reduce the energy intensity of grinding. A process involving the treatment of ultramafic nickel ores by microwave irradiation prior to grinding has been developed. Two different ultramafic nickel ores were studied: one from a deposit near Thompson, Manitoba, Canada (Pipe ore), and the other from the Okanogan region of Washington State, USA (OK ore). Ore grindability and pentlandite liberation were studied as a function of microwave pre-treatment time. The costs and benefits of microwave pre-treatment are discussed specifically with reference to energy usage. Copyright © 2013 MS&T'13®. Source


Moula M.G.,University of Guelph | Szymanski G.,University of Guelph | Shobeir B.,Vale Base Metals Technology Development | Huang H.,Vale Base Metals Technology Development | And 3 more authors.
Electrochimica Acta | Year: 2015

The anodic dissolution of two laboratory-made Ni samples obtained using the carbonyl method was investigated to understand the origin of residue formation in the anode basket in an electroplating tank. The first sample was obtained with 3 ppm addition of carbonyl sulfide to introduce a small amount of sulfur (CN-S sample). The second was obtained without sulfur impurities (CN sample). Linear sweep voltammetry and chronopotentiometry were applied to characterize the dissolution of these samples. The dissolution of the CN-S sample took place in the active region at low overpotentials. This behavior is determined by the presence of sulfur impurities that break down the passive layer and facilitate Ni dissolution. The CN sample without sulfur was dissolved at high overpotentials. The overpotential-time plots displayed regular large amplitude oscillations in which the overvoltage periodically moved between the transpassive and passive regimes. The anodic dissolution of this sample was controlled by two competing processes: breakdown and formation of the passive layer. Scanning electron microscopy and white light interference microscopy were applied to monitor the morphological changes of the two samples as a function of the dissolution time. The results of these studies showed that the CN-S sample dissolved uniformly across the surface. However, the roughness and the aspect ratio of the protruding features on the surface increased with time. This sample produced a fine residue due to detachment of small protruding crystallites. In contrast, the dissolution of the CN sample involved pit formation and took place predominantly from the bulk of the pits. The dissolution of this sample left a porous skeleton of more passivated Ni. The residue in this case consisted of large, porous chunks of the skeleton. © 2014 Elsevier Ltd. All rights reserved. Source


Dong J.,Vale Base Metals Technology Development | Xu M.,Vale Base Metals Technology Development
Water in Mineral Processing - Proceedings of the 1st International Symposium | Year: 2012

Diethylenetriamine (DETA) has been used as an effective pyrrhotite depressant at Vale's Clarabelle Mill for more than a decade. In the fall of 2004, DETA started showing up as copper-DETA complexes in the effluent of the waste water treatment plant. Sporadic monthly copper exceedances have been observed since. DETA is a strong chelating agent and forms stable complexes with heavy metal ions (Cu 2+ and Ni 2+), leading to an ineffective removal of the DETA-metal complexes by conventional lime precipitation method. In the future, more challenging ores will be processed and will require more DETA to be added in order to achieve the grade/recovery target. To avoid the exceedances of heavy metals in effluent due to DETAmetal complexation, effective mitigation strategies are being developed to reduce DETA level in the tailings water. These strategies include: (1) maximizing adsorption of DETA onto pyrrhotite and rock tailings while minimizing desorption during processing and disposal of tailings, (2) adding natural zeolite as extra sorbents to capture additional free or complexed DETA in the tailings water if necessary, and (3) finding DETA replacements as pyrrhotite depressants. In this paper, DETA adsorption and desorption properties are studied on pyrrhotite and rock tailings, natural zeolite and the mixture. Source

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