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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.

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