Apparatus for continual magnetisation of a slurry
AssigneeAusmetec Pty Ltd.
InventorBarry Lumsden
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AssigneeAusmetec Pty Ltd.
InventorBarry Lumsden
Estimating the term…
An apparatus for inducing magnetism in a flowstream of an at least partially magnetisable particulate feed material suspended in a liquid, in use to condition the flowstream to enhance the subsequent separation process, the apparatus including: a treatment chamber having an inlet and an outlet through which the flowstream respectively enters and exits the chamber; and a magnetic source within the treatment chamber, said magnetic source substantially continuously immersed in and activated with respect to the flowstream.
A preconditioning apparatus for inducing magnetism in a flowstream, the flowstream feeding continuously into a subsequent and separate separation process located downstream of the preconditioning apparatus, the flowstream including an at least partially magnetisable particulate feed material suspended in a liquid, the preconditioning apparatus comprising:
The preconditioning apparatus of 12, wherein the paramagnetic particulates include at least one sulfide mineral.
Dependencies are inferred from the claim text.
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From the US filing history. Foreign family members aren’t listed.
Magnetic plugs and dipsticks: disposed at the inner circumference of a recipient, e.g. magnetic drain bolt
Magnetic separation: pretreatment specially adapted for magnetic separation
Magnetic plugs and dipsticks: with associated cleaning means, e.g. retractable non-magnetic sleeve
Froth-flotation processes: adapted for the flotation of fines
About 6 years of term left · ends 19 Oct 2032 (estimated)
The present invention relates to the field of mineral processing and, more particularly, to methods and apparatus for enhancing the efficiency of magnetising a slurry for the extraction of minerals from a flowstream.
1. Mineral Separation
Many important metal ores are sulfides. Significant examples include; argentite (silver sulfide), galena (lead sulfide), molybdenite (molybdenum sulfide), pentlandite (nickel sulfide]), realgar (arsenic sulfide), and stibnite (antimony), sphalerite (zinc sulfide), and pyrite (iron disulfide), and chalcopyrite and bornite (iron-copper sulfide). Vaughan, D. J. Craig, J. R. 1978
Embodiments of the present invention will now be described with reference to the accompanying drawings wherein:
FIGS. 1A and 1B illustrate the effect of equipment sizing on using wiper magnetising according to a first-preferred embodiment of the present invention.
FIG. 2 illustrates the slurry magnetising equipment according to a preferred embodiment of the invention.
It has been discovered that magnetizing a flotation slurry that contains a number of paramagnetic minerals can result in not only the increase in recovery of some paramagnetic minerals that are actively collected but also the reduction in recovery of other paramagnetic minerals that are recovered by entrainment. This is a surprising result. It was thought that there would be heteroaggregation of all the paramagnetic minerals, but what has been discovered is that there is primarily homoaggregation of the paramagnetic minerals. However, in flotation some fine mineral is recovered not by being actively floated but by being entrained in the froth. This is a well recognized phenomenon. Entrainment is most pronounced for fine minerals and generally increases with the fineness of the minerals. Therefore, if the mineral can be aggregated then its particle size will increase and there will be less entrainment of these mineral in the froth, if the plant is not actively trying to float them.
For example, in a recent investigation in a plant the slurry contained the paramagnetic sulfides chalcopyrite and sphalerite. The process operates to produce a chalcopyrite concentrate first and then subsequently a sphalerite concentrate. When magnetic conditioning was applied to the chalcopyrite slurry the chalcopyrite recovery increased (less copper in the tailings from the process) but the recovery of the sphalerite in the chalcopyrite concentrate actually declined.
% Cu % Cu in % Zn Recovery in % Zn Recovery in Rec Tailings Cu Concentrate Zn Concentrate Magnetic 84.5 0.5 7.41 79.7 Conditioning ON Magnetic 84.0 0.54 7.96 77.9 Conditioning OFF