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 />
the pulp interface in the tank to rise as air accumulates in the pulp. A uniform<br />
bubble diameter of 0.7 mm is assumed. Air volume fraction contours, velocity<br />
vectors and profiles are presented and discussed.<br />
chair:<br />
9:00 AM<br />
Introductions<br />
Mineral & Metallurgical Processing:<br />
Plant design and optimization I<br />
9:00 AM • Tuesday, February 26<br />
J. Lommen, Consultant, Socorro, NM<br />
9:05 AM<br />
When Laboratory Work and Operating Plant Don’t Agree:<br />
Commercializing the Caron Ammonia-ammonia Carbonate<br />
Ni Process<br />
L. Southwick; L.M. Southwick & Assoc., Cincinnati, OH<br />
In the early 1940s, the Caron ammonia-ammonia carbonate leach process was<br />
used to produce nickel from Mayari ores at the Nicaro plant in Oriente Province,<br />
Cuba. While plant operation was generally successful, it was not broadly economical<br />
and was shut down. The plant was later restarted in the 1950s and a<br />
number of investigations initiated to resolve the more serious operational and<br />
performance issues. Troublesome processing steps studied included iron reduction<br />
(chemistry nickel and iron, reductant, equipment), ore variability (homogeneity<br />
and consistency of mineral concentrations, serpentine vs. laterite), leach<br />
solution strength, nickel recovery (temperature reduction and leaching, reoxidation)<br />
and a variety of other topics. These studies and their findings will be discussed.<br />
Caron himself obtained good results on these ores in the laboratory. They<br />
could not be duplicated in the field, the reasons for which will be reviewed.<br />
9:25 AM<br />
Electrowinning Precious Metals from Cyanide Solution Using<br />
EMEW Technology<br />
M. Mooiman 1 , I. Ewart 2 and J. Robinson 2 ; 1 College of Graduate and<br />
Professional Studies, Franklin Pierce University, Concord, NH and<br />
2<br />
Electrometals Technologies Ltd, O’ Fallon, MO<br />
The recovery of gold and silver from cyanide bearing solutions using electrowinning<br />
technology designed by Electrometals Corporation is reviewed. The technology<br />
can be considered as a complete or partial replacement for Merrill Crowe<br />
technology and offers several advantages in high grade solutions. It has been successfully<br />
implemented in copper electrowinning applications, silver refining and<br />
in mining operations for recovery of gold and silver. The advantages of the<br />
EMEW approach and actual plant applications and practices are evaluated<br />
and discussed.<br />
9:45 AM<br />
Best Practices in Material Selection and Design for<br />
Hydrometallurgical Equipment<br />
D. Kelley and T. Johnson; Ashland Inc, Dublin, OH<br />
Hydrometallurgical processes can be exceptionally corrosive. Operating conditions<br />
associated with metal extraction and refining require materials of construction<br />
that can withstand process acids and acid chlorides at temperatures up to<br />
90∞C. Process vessels, piping, scrubbers and ducting can be rapidly compromised<br />
in these aggressive environments if not designed with great care. Design engineers<br />
are frequently challenged to find materials of construction that can stand<br />
up to hydrometallurgical processes especially for copper, zinc, nickel, cobalt and<br />
uranium. This paper will evaluate a variety of material solutions to determine<br />
which provide attractive economics for initial procurement as well as high durability<br />
for reasonable life cycle costs. The comparative cost and durability information<br />
presented is intended to enable design engineers and material specialists to<br />
choose materials of construction that will be the most beneficial for their projects.<br />
10:05 AM<br />
25 Years of FRP Performance at a Copper Smelting<br />
Sulfuric Acid Plant<br />
R. Moubarac 1 , G. Landry 2 , G. Clarkson 3 and K. Townsend 4 ; 1 Experco<br />
Composites Inc., Pierrefonds, QC, Canada; 2 Fabricated Plastics,<br />
Maple, ON, Canada; 3 UTComp, Cambridge, ON, Canada and 4 RPS<br />
Composites, Mahon Bay, NS, Canada<br />
The sulfuric acid plant at a copper smelting operation in Northern Quebec will<br />
celebrate its silver jubilee in 2013, with 25 years in service. The performance of<br />
FRP (Fiberglass Reinforced Plastics) equipment will be reviewed. Case histories<br />
will be presented by the FRP equipment manufacturers, with a video, and pictures<br />
of the FRP tanks, absorption towers, piping, ducting, electrostatic precipitators,<br />
and grating, in service since 1988. A report of the yearly inspections of that<br />
equipment will be given by the inspection company.<br />
10:25 AM<br />
Molybdenum Flotation Practice – Cell Selection Types and<br />
Design Considerations<br />
D. Meadows, D. Jensen, A. Weber, F. Traczyk and S. Yu; FLSmidth,<br />
Salt Lake City, UT<br />
Several of the larger copper projects built in recent times have included a<br />
Molybdenum byproduct circuit as part of the overall project due to the favorable<br />
molybdenum market conditions and overall economic contribution to the project.<br />
This paper provides a summary of moly plant flotation practices across a<br />
number of both recent projects and historical ones. Modern Moly flotation flowsheets<br />
predominantly incorporate either Inert gas cells or forced air machines<br />
with nitrogen addition and as a final cleaner column flotation . The paper provides<br />
an insight into the process considerations, capital and operating costs associated<br />
with both of the cell types. It also reviews metallurgical aspects and important<br />
safety aspects. Other aspects including instrumentation and degree of<br />
automation are also discussed along with overall plant design aspects.<br />
Mineral & Metallurgical Processing:<br />
research and characterization<br />
9:00 AM • Tuesday, February 26<br />
chairs: T. Bhambhani, Cytec Industries, Inc., Stamford, CT<br />
M. Vasudevan, Cytec Industries, Inc., Stamford, CT<br />
9:00 AM<br />
Introductions<br />
9:05 AM<br />
The Simulation of Solvent Extraction Plants: Application to the<br />
Separation of Rare Earth Elements<br />
C. Bazin and V. Ouellet; Mining and metallurgy, Laval University,<br />
Quebec, QC, Canada<br />
The separation of rare earth elements is a complicated process that is currently<br />
carried out using liquid/liquid separation. Detailed flow sheets of solvent extraction<br />
plants for the separation of rare earth elements are rarely available in the literature<br />
which limits the opportunity to teach and test the applicability of modern<br />
methods of data reconciliation and process control to these processes. A simulator<br />
for solvent extraction for the separation of rare earth elements is described in this<br />
paper. A module is used to simulate the operation of a mixer settler. Mixer settlers<br />
are then combined into batteries of units for extraction, scrubbing and stripping.<br />
Finally batteries are combined to simulate circuits for the separation of heavy rare<br />
earth elements from light rare earth elements, and to simulate the separation of individual<br />
rare earths. The program simulates the steady state process separation of<br />
several rare earth elements and provides data for testing the application of data<br />
reconciliation techniques for material balancing of the plant operation.<br />
9:25 AM<br />
Estimating the Residual Inventory of a Large Gold Heap Leach<br />
J. Winterton; AngloGold Ashanti, Denver, CO<br />
Estimating the residual metal inventory of large heap leaching operations is desirable<br />
for many reasons. Several methods have been tried with limited success.<br />
Drilling data from the Valley Leach Facility at AngloGold Ashanti’s Cripple<br />
This is the Technical <strong>Program</strong> as of September 1, 2012. IT IS SUBJECT TO CHANGE.<br />
70<br />
Please see the Onsite <strong>Program</strong> for final details.