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Annual Meeting Preliminary Program - Full Brochure (PDF) - SME

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TECHNICAL PROGRAM<br />

were obtained from second-stage flotation with conventional sulfide collectors.<br />

Static and bio-kinetic ARD potential tests confirmed that these low-sulfur tailings<br />

were non-acid forming.<br />

3:05 PM<br />

An Investigation on the Surface Chemistry of Some Rare Earth<br />

Minerals During Flotation by TOF-SIMS<br />

S. Chelgani 1 , B. Hart 2 and L. Xia 3 ; 1 Earth Science, Surface Science,<br />

University of Western, London, ON, Canada; 2 Surface Science,<br />

University of Western, London, ON, Canada and 3 Surface Science,<br />

University of Western, London, ON, Canada<br />

The Thor lake deposit is a world class resource of REE in Canada. Development<br />

work to optimize a REE recovery process flow sheet is under way, however, given<br />

the ore mineralogy; the developed reagent scheme is relatively complex. Micro<br />

flotation tests were conducted on a feed sample in order to examine factors affecting<br />

stream partitioning. SEM-EDX was performed to evaluate variability in grain<br />

composition between streams and TOF-SIMS analysis was used to determine statistically<br />

differences in surface species particularly related to potential activation of<br />

the examined mineral phases. SEM-EDX analyses reveal that the concentrate has<br />

a significantly higher proportion of REE bearing grains relative to the tail. Spectral<br />

fingerprinting by TOF-SIMS has allowed for the identification of all reagent<br />

species investigated. Reagent signal intensity discrimination on test stream mineral<br />

surfaces was observed by the TOF-SIMS analysis using reagents at plant concentration<br />

levels. TOF-SIMS analysis confirmed that REE bearing grains reporting<br />

to the concentrate are doing so in response to collector attachment. The<br />

surface analyses of gangues reveal similar reagent discrimination as well.<br />

3:25 PM<br />

Analysis of Collector Adsorption in Kaolinite Flotation Systems<br />

J. Liu, X. Wang and J. Miller; Metallurgical Engineering,<br />

University of Utah, Salt Lake City, UT<br />

Investigation of the surface chemistry of collector adsorption by kaolinite is important<br />

to many flotation processes, including, for example, bauxite flotation,<br />

iron ore flotation, and oil sand processing. The structure of kaolinite consists of<br />

one tetrahedral silica sheet and one octahedral alumina sheet. In our study, two<br />

model surfaces—talc and gibbsite are used to simulate the silica face and alumina<br />

face of kaolinite respectively. The hydrophobicity of the kaolinite surfaces at different<br />

collector concentrations and solution pH values is estimated by measuring<br />

contact angles at the model surfaces. In the case of dodecylamine, the results<br />

show that the hydrophobicity of the gibbsite surface increases with increasing<br />

pH, which implies adsorption of the cationic collector from alkaline solution.<br />

However, the gibbsite surface becomes hydrophilic at higher concentrations of<br />

collector apparently due to the formation of surface micelles. Experimental results<br />

are examined with respect to results from molecular dynamic simulations.<br />

3:45 PM<br />

Design and Development of Mineral Specific Collectors in<br />

Flotation: Selectivity in Apatite-calcite Flotation System<br />

T. Karlkvist 1 , A. Patra 1 , H. Kota 1 , R. Bordea 2 and K. Holmberg 2 ;<br />

1<br />

Minerals and Metals Research Laboratory, Lulea University of<br />

Technology, Lulea, Sweden and 2 Dept. of Chemical and Biological<br />

Engineering, Chalmers Univ. of Technology, Gothenburg, Sweden<br />

The present investigation aims to develop and distinguish mineral specific<br />

reagents with two functional groups to use in flotation for calcium containing<br />

minerals. A reference mono-carboxylate and 3 di-carboxylate surfactants with a<br />

fixed alkyl chain length but having two carboxyl groups with varying geometrical<br />

distances (separated by a spacer of 1, 2 and 3 carbon atoms) between them have<br />

been synthesized. Adsorption behaviors of these reagents on pure apatite and calcite<br />

surfaces were studied using Hallimond flotation, FTIR and ∂ potential measurements.<br />

Relation between adsorption behavior of a given surfactant on a specific<br />

mineral surface and its molecular structure over a range of concentration<br />

and pH values, and region of maximum recovery were established. The results<br />

show that only one of the reagents with a specified geometric distance between<br />

the anchoring groups is more selective for either calcite or apatite surface than<br />

other homologues synthesized. Selective adsorption of a given surfactant to a<br />

particular mineral surface relative to other mineral surfaces as evidenced in flotation<br />

studies is substantiated by ∂ potential and spectroscopy data.<br />

4:05 PM<br />

Water Chemistry Effects on Zeta Potential of Concentrated<br />

Hematite Ore<br />

H. Haselhuhn; Chemical Engineering, Michigan Technological<br />

University, Houghton, MI<br />

The effectiveness of selective flocculation and dispersion processes for the concentration<br />

of hematite ore are strongly dependent on the ionic content of the<br />

process water. It has been noticed that magnesium ions are more detrimental to<br />

iron recoveries during gravity separation and flotation processes than calcium.<br />

This phenomenon was studied by measuring the zeta potential of hematite ore at<br />

various concentrations of sodium, magnesium, calcium, strontium and barium at<br />

a pH of 11. Results showed that zeta potential inverts from negative to positive at<br />

very low concentrations of magnesium ions in the solution. It takes a significantly<br />

higher concentration of calcium, ions to achieve the same effect. This difference<br />

was attributed to the ability of magnesium ions to adsorb to all surface<br />

hydroxyl groups, whereas calcium, due to their larger size, can only adsorb to<br />

every other hydroxyl group. This hypothesis was confirmed by results similar to<br />

those seen with calcium when this test was repeated with strontium and barium<br />

ions. This adsorption theory explains how higher concentrations of calcium ions<br />

are less detrimental to hematite concentration processes than magnesium.<br />

chair:<br />

2:00 PM<br />

Introductions<br />

Mineral & Metallurgical Processing:<br />

Plant design and optimization II<br />

2:00 PM • Tuesday, February 26<br />

H. Haselhuhn, Michigan Technological University,<br />

Houghton, MI<br />

2:05 PM<br />

Haile Gold Mine Metallurgy and Flowsheet Review<br />

J. Wickens and M. Deal; Haile Gold Mine, Kershaw, SC<br />

Haile Gold Mine is located near Kershaw, South Carolina, approximately 50<br />

miles south of Charlotte, North Carolina. Gold was first discovered at the site in<br />

1827, and the property has been through several operating periods since. The relatively<br />

low grade and refractory nature of the deposit has been a challenge for efficient<br />

processing since the start of mining on the property. Early processing techniques<br />

included gravity separation and barrel chlorination. The last operation<br />

employed heap leaching in 1985 through 1991. After being closed and reclaimed<br />

for over 20 years, the property is poised to re-open and produce once again. In<br />

this chapter of the Mines legacy, flotation and ultra-fine grinding will be employed<br />

to achieve economic extraction of gold and silver from the pyrite. This<br />

paper briefly reviews some of the historic processing methods, reviews the current<br />

metallurgical testing and results used to develop the new process flow sheet,<br />

presents the flow sheet and equipment selection, and highlights a few of the specific<br />

project nuances experienced to date.<br />

2:25 PM<br />

Larger Flotation Cells in the Copper Processing Industry Recent<br />

Experiences and Future Considerations for 2012 Onwards<br />

D. Meadows 1 , F. Traczyk 2 and C. Letelier 3 ; 1 FLSmidth Minerals,<br />

Salt Lake City, UT; 2 FLSmidth Minerals, Salt Lake City, UT and<br />

3<br />

FLSmidth Minerals, Salt Lake City, UT<br />

During the last few years the economies of scale have continued to drive copper<br />

projects to larger throughputs to offset the depleting lower grade resources. A<br />

decade ago there were only a small number of projects that stretched beyond<br />

100,000 mtpd throughput rates. Nowadays and moving forward virtually all the<br />

major copper projects are sized beyond this, with throughput rates up to 250,000<br />

mtpd now under evaluation for a number of key projects in Chile and Peru. This<br />

paper explores the development from the 160 m3 flotation cells, through to the<br />

257 m3 cells and nowadays to the 300 m3 cells. A number of specific installations<br />

are reviewed in this growth phase including Kennecott, Minera Los Pelambres,<br />

Mineral Park and Esperanza. Metallurgical results as well as layout, maintenance<br />

and operational aspects are highlighted. Finally some discussion is made on the<br />

new 600 m3 cell and its role and potential in the new flowsheets.<br />

This is the Technical <strong>Program</strong> as of September 1, 2012. IT IS SUBJECT TO CHANGE.<br />

86<br />

Please see the Onsite <strong>Program</strong> for final details.

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