1 / 28

Optimising Parameters and Measuring Improved Gold Recovery in a Copper-Zinc Flotation Circuit Myra Falls Operation Trev

Optimising Parameters and Measuring Improved Gold Recovery in a Copper-Zinc Flotation Circuit Myra Falls Operation Trevor Yeomans NVI Mining. 4000 mtpd copper/zinc flotation mill with gold/silver. Historical Gold Recovery Gravity circuit – 2-5% Copper concentrate – 20-30%

channer
Download Presentation

Optimising Parameters and Measuring Improved Gold Recovery in a Copper-Zinc Flotation Circuit Myra Falls Operation Trev

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript


  1. Optimising Parameters and Measuring Improved Gold Recovery in a Copper-Zinc Flotation Circuit Myra Falls OperationTrevor YeomansNVI Mining

  2. 4000 mtpd copper/zinc flotation mill with gold/silver • Historical Gold Recovery • Gravity circuit – 2-5% • Copper concentrate – 20-30% • Zinc concentrate – 13-23% • Overall – 35-58%

  3. Gravity Circuit • Installed in 1992, two Knelson CD-30 • CD-30 on “A” Circuit • CD-30 on “B” Circuit • Gravity concentrate shipped offshore • One of the first sites in the world using automated Knelsons • Unusual upgrading step • Cleaning of rougher conc, using CD-30

  4. GOLD RECOVERY STEPS

  5. Myra Falls Upgrading Step-Historical • Primary Knelsons operated on 6 hour concentrating cycles • Concentrate stored in two concentrate hoppers, one for each grinding circuit • Upgrading step: • Once per week, the “A” circuit Knelson was taken off line • The concentrate stored in each concentrate hopper was individually pumped to the A circuit Knelson • This “cleaned” product was decanted, dried, and shipped • The goal was to reduce the mass and increase the grade • No data on efficiency of this process

  6. Typical ‘cleaned’ concentrate, note flakes

  7. Initial Changes • Myra Falls staff thought that shorter cycles and more frequent cleaning would improve results • Change made • Start decreasing primary cycle time from 6 to 1 hour • Start increasing frequency of cleaning step, to once every 12 hours • Result • Significant increase in gravity recovery • Positive influence on overall gold recovery

  8. Question? • Why such an increase? • Was this due to….. • Ore change? • Short cycles? • Frequent cleaning? • How can we measure?

  9. Knelson Gravity Circuit Audit - Goals • What is the effect of Knelson concentrating cycle time on gravity recovery • What are the losses associated with the unusual upgrade step • What alternatives for upgrading are feasible • Tabling • Intensive Leaching • How to maximize primary gravity recovery with the existing Knelson Concentrators • What is the upper limit of gravity recovery, and what additional equipment might be needed Once results of sampling completed, circuit can be modeled

  10. Gravity Circuit Audit - Sampling • Grinding Cyclones • Characterize for GRG recovery to underflow • Characterize GRG in COF before and after upgrading • Primary Knelson recovery – characterize for unit GRG recovery • KC con • KC tails • Upgrade system – recovery characterization • KC feed grade during upgrade • KC tails grade during upgrade

  11. Audit Results – Grinding Cyclones • GRG partition curve typical for finer grind circuits • Some coarser GRG exiting the circuit

  12. Audit Results– Cyclone Overflow • Significant increase in GRG exiting during upgrading

  13. Audit Results- Upgrading • Significant increase in grade of tails in only a few minutes • This was with the already reduced cycle time and more frequent cleaning

  14. Old vs New Upgrade Frequency Previous Current • Primary cycles: 6 hours 1 hour • Cleaning: Weekly 12 hours • Gravity recovery 2-5% 15-20%

  15. RESULT OFCHANGES GRAVITY Recovery increase ~12%

  16. MORE OVERALL RECOVERY??

  17. MORE OVERALL RECOVERY??

  18. MORE OVERALL RECOVERY??

  19. Base Case predicted 14.6% recovery, similar to plant actual Gravity Circuit Audit – Model Calibration

  20. Acacia pilot study carried out Excellent recovery No copper solubility issues Sensitive site for cyanide use (BC Park) Table selected as being a reliable upgrade option Table purchased and installed, Operational April 2006 Modelling - Outcomes

  21. NEW CLEANER CIRCUIT

  22. TABLING UPGRADE CIRCUIT • NEW ‘FLAKE’ CONC @ 65% GOLD TO DORE • TABLE ‘MIDDLINGS’, WITH NO ‘FLAKE’ SOLD AS HISTORIC GRAVITY CONC. @ 10000 G/T • TABLE TAILINGS SENT DIRECTLY TO COPPER CONCENTRATE • NOTE 100% UPGRADING RECOVERY

  23. RESULT OF TABLING

  24. Gravity + Gold to Copper vs Overall Recovery

  25. Overall Gold Recovery vs Tails Loss

  26. OverallOutcomes and Conclusions KNELSON OPERATING CHANGES: • Gravity recovery was increased to 15%, from 2-5%. • Overall Recovery Increase maybe? • Very simple operating changes made to gravity circuit. • Inexpensive test program, confirmed gain, and modelling predicted further possible gains.

  27. OverallOutcomes and Conclusions TABLING UPGRADING CHANGES: 100% stage recovery Gravity recovery decrease ~ -5% Copper conc increase ~ + 12% Overall Recovery Increase YES, ~ + 10% Mill tailings Decrease 0.3 g/t.

More Related