Annual Meeting Preliminary Program - Full Brochure (PDF) - SME
Annual Meeting Preliminary Program - Full Brochure (PDF) - SME
Annual Meeting Preliminary Program - Full Brochure (PDF) - SME
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TECHNICAL PROGRAM<br />
2:45 PM<br />
Testwork <strong>Program</strong>s Too Little, Too Late<br />
C. Jeltema, W. Baum, P. Thompson and D. Meadows; FLSmidth,<br />
Midvale, UT<br />
Testwork programs for greenfield projects and expansions are essential for effective<br />
process design, accurate equipment sizing, and timely startups. Adequate<br />
testwork is even more imperative as mined ore bodies are becoming deeper,<br />
harder, more finely grained, and lower grade with higher impurity elements.<br />
Further, these future ores do not always fit within the framework of currently<br />
available testwork databases and installations. The effects of inadequate testwork<br />
are evident in some of the mill sizing errors made in recent years, together with<br />
slow plant ramp ups. It is recognized that achieving adequate testwork is challenging.<br />
The ramifications of inadequate testwork and lack of mineralogical ore<br />
characterization on equipment sizing and process design will be discussed to emphasize<br />
testwork importance. Explanations, examples, interpretation, and cost<br />
estimates of testwork programs will be presented. Finally, recommendations will<br />
be made for the planning, execution, utilization, and follow-through of a minerals<br />
processing testwork program.<br />
3:05 PM<br />
A Sound Strategy: Using Sonic Horns to Prevents Buildups and<br />
Improve the Efficiency of Baghouses and Fans<br />
J. Shelton and S. Griffith; Martin Engineering, Neponset, IL<br />
This presentation will look at how the application of sonic horns can prevent<br />
material buildups and improve the efficiency of bag houses and fans. Sonic<br />
horns use a high-intensity/low-frequency pulse of sound to prevent and/or<br />
break up the accumulations of dry materials. These accumulations can interfere<br />
with the operating efficiency of large industrial fans and impair the efficiency of<br />
fabric dust collectors. In this presentation the authors will discuss the principles<br />
of the application of sound energy to improve industrial operations. He will<br />
then look at specific examples of application of sonic horns on various types of<br />
baghouses and fans.<br />
3:25 PM<br />
Iron Plant Mill Optimization through the Optimization of a<br />
Single Parameter<br />
E. Tuzcu; DAMA Engineering, Ankara, Turkey<br />
Evaluation of the efficiency of the closed grinding mill-classifier circuit is complicated<br />
due to direct and interaction effects of the process variables. Identifying<br />
the effects of design and operating variables in an isolated environment or in a<br />
controlled experiment is easier than to do the same in an industrial plant.<br />
Functional performance efficiency (FPE) coefficient is defined as the function of<br />
classifier and ball mill efficiency and calculated for a particular set of operating<br />
variables to evaluate circuit efficiency. The configuration that gives the best circuit<br />
output and FPE coefficient is announced as the optimal operating conditions. In<br />
order to find out which configuration is better, different mill surveys are carried<br />
out. This is certainly the exact way to verify an engineers solution. However it is<br />
labor and time intensive. In this work, a combined FPE and simulation method is<br />
applied to optimize FPE coefficient. Different mill surveys are carried out in the<br />
simulation environment to find optimum conditions by tracking FPE coefficient<br />
as a function of everything. Finally, based on the best FPE coefficient, the optimum<br />
process variables are proposed.<br />
Mineral & Metallurgical Processing:<br />
Problematic non-sulfide Gangue Minerals<br />
and their detrimental effects<br />
in Flotation Performance<br />
2:00 PM • Tuesday, February 26<br />
chairs: T. Bhambhani, Cytec Industries, Inc., Stamford, CT<br />
M. Vasudevan, Cytec Industries, Inc., Stamford, CT<br />
2:00 PM<br />
Introductions<br />
2:05 PM<br />
Effect of Clay Minerals on Rheology of Flotation Slurries<br />
N. Cruz; The University of Queensland, Brisbane, QLD, Australia<br />
Clay minerals such as kaolinite and smectite, which are often associated with<br />
copper, gold and other valuable minerals, place a widespread problem in mineral<br />
flotation. There have been numerous observations of these clay minerals having<br />
a deleterious effect on mineral flotation grade and recovery, with simultaneous<br />
observations of high flotation pulp viscosity, over-stable froth or the absence of<br />
froth. Rigorous explanations on how clay minerals affect flotation are not available.<br />
There are extensive studies on the formation of network structures of clay<br />
minerals and the development of viscosity, but they do not address the complex<br />
chemical and physical environment of mineral flotation. The aim of this research<br />
is to identify how clay minerals affect the rheological properties of flotation slurries.<br />
Steady and dynamic rheology measurements are conducted for pure clays<br />
(sodium bentonite and kaolinite) and for mixtures of clays with other minerals<br />
and clean ores in the absence and presence of flotation reagents. The size and<br />
structure of mineral aggregates are monitored in conjunction with rheological<br />
measurement and correlated with mineral flotation behaviour.<br />
2:25 PM<br />
Examining the Different Behaviour of Non-ionic Dispersants in<br />
Fresh and Saline Water<br />
D. Liu and Y. Peng; School of Chemical Engineering, The University<br />
of Queensland, Brisbane, QLD, Australia<br />
Clay minerals, which often coat the surface of valuable minerals and bubble surfaces,<br />
have an adverse effect on the coal flotation process, leading to the decrease<br />
of both coal recovery and grade. These problems are exacerbated by saline water<br />
which is used in coal flotation in Australia. The industry has been fully aware of<br />
the difficulties in treating clayey ores in saline water. To improve the coal flotation,<br />
cationic dispersants are normally used to remove the slime coating.<br />
However in the presence of high ionic strength process water, these traditional<br />
dispersants are invalid due to the ionic effect. In this study, two types of non-ionic<br />
dispersants was introduced and developed with the aim to reduce the viscosity in<br />
both pulp and froth phases and remove slime coating from particles and bubbles<br />
in saline water. For a comparison, coal flotation was also conducted in deionized<br />
water using the same dispersants. It is interesting to find that non-ionic dispersants<br />
behaved differently in fresh and saline water as well.<br />
2:45 PM<br />
Atypical Grade-recovery Curves as Diagnostic Tools in Sulfide<br />
Mineral Processing<br />
M. Vasudevan, T. Bhambhani and D. Nagaraj; Mineral Processing<br />
R&D, Cytec Industries, Stamford, CT<br />
In sulfide mineral flotation, grade recovery curves are used to glean the flotation<br />
response/ kinetics of a given mineral to changes in certain flotation parameters.<br />
One usually finds that their day-to-day usage is largely limited to comparing the<br />
flotation response to different reagents, e.g. collectors. Given the large variability<br />
in the complex mineralogy of ores, several ore types routinely processed exhibit<br />
atypical grade recovery characteristics. This paper is an effort to highlight the hidden<br />
and often neglected aspects of these atypical curves which can help gain insights<br />
of the underlying flotation mechanisms and challenges, and thus help in<br />
designing better processes/solutions. Specifically, we present the flotation response<br />
of problematic sulfide ores with very different gangue mineralogy, which<br />
show unusual but similar grade-recovery characteristics. We present hypotheses<br />
and experiments to understand and explain this behavior and the underlying<br />
mechanism. Finally, we propose chemical modifiers as solutions to the problem<br />
and to improve the efficiency of flotation performance.<br />
This is the Technical <strong>Program</strong> as of September 1, 2012. IT IS SUBJECT TO CHANGE.<br />
87<br />
Please see the Onsite <strong>Program</strong> for final details.