Observation of Wash Water Effect on Particle Motion in a Spiral Concentrator by Positron Emission Particle Tracking

Canadian Institute of Mining, Metallurgy and Petroleum
Darryel Boucher Joshua Sovechles Zhoutong Deng Raymond Langlois Thomas W. Leadbeater McGill University
Organization:
Canadian Institute of Mining, Metallurgy and Petroleum
Pages:
12
File Size:
5757 KB
Publication Date:
Jan 1, 2016

Abstract

"Spiral concentrators are used to upgrade ore based on the density difference between their component minerals. This simple flowing film gravity separator is of interest for the processing of large amounts of material, as found in the iron ore industry. Addition of wash water at different points on the trough of the spiral affects the grade and recovery of the valuable concentrate by affecting the flow of particles within the thin slurry film. This paper shows how radiolabelled hematite (-355+300 µm) and quartz (–1,180+1,000 µm) tracers were used to determine the particles’ behaviour within the slurry film with and without the addition of wash water. The results presented provide a detailed particle flow pattern around a wash water addition point and its effect on the trajectory and velocity of the particles. This information is of interest in building knowledge about spiral wash water injection parameters such as injection location, direction, flow rate and nozzle orifice type (affecting jet shape and velocity).INTRODUCTIONSpiral concentrators are density based separation devices. They are extensively used in the upgrading of iron ore, fine coal and minerals sands (sources of ilmenite, rutile, zircon and monazite) (Wills & Finch, 2016). A spiral unit is composed of a channel of specific profile formed as a helix of 3 to 7 turns around a central structural post. The feed pulp is composed of 15 to 45% solids with particle size from 75 µm to 3000 µm (Wills & Finch, 2016). Throughput of a single spiraling trough can be up to 8 ton per hour and multiple trough unit (up to four trough) can process up to 30 ton per hour for a footprint of around 0.7 m2 (Palmers & Vadeikis, 2010). They are low cost concentrators considering manufacturing of their trough via polymer reverse molding. The energy intensity of a spiral plan is notably small considering the throughput and is mostly related to pulp pumping and final concentrate dewatering."
Citation

APA: Darryel Boucher Joshua Sovechles Zhoutong Deng Raymond Langlois Thomas W. Leadbeater McGill University  (2016)  Observation of Wash Water Effect on Particle Motion in a Spiral Concentrator by Positron Emission Particle Tracking

MLA: Darryel Boucher Joshua Sovechles Zhoutong Deng Raymond Langlois Thomas W. Leadbeater McGill University Observation of Wash Water Effect on Particle Motion in a Spiral Concentrator by Positron Emission Particle Tracking. Canadian Institute of Mining, Metallurgy and Petroleum, 2016.

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