IM 2017 August 17 | Page 42

GOLD EXTRACTION many factors including slurry temperature, solution and slurry chemistry, slurry viscosity, agitator type, dimensions and power, oxygen bubble residence time, oxygen purity, tank geometry and oxygen injection technique. Oxygen generation represents an important operating cost for the Albion Process. Pivotal to the process operating economically at atmospheric pressure is the capability to efficiently transfer oxygen while using as much oxygen injected to the process as possible. To respond to this Glencore Technology developed the HyperSparge™ supersonic gas injector. The paper Oxygen mass transfer in the Albion Process: from the laboratory to the plant by Glencore Technology’s Paul Voigt, Daniel Mallah and Mike Hourn, (Proceedings of EMC 2017) compares the HyperSparge against other sparging techniques to quantify the benefits of oxygen injection via a supersonic gas jet on scale up of the oxygen mass transfer system. It then examines plant survey data from the GPM project to demonstrate the very high oxygen utilisation that can be achieved with a correctly designed oxygen mass transfer system. Its specific purpose is to float coarse particles containing only small amounts of exposed hydrophobic minerals. Over the last decade, this technology has been successfully applied to industrial minerals with several full-scale units installed to recover particles up to and exceeding 3,000 μm in diameter. More recently, sulphide-based test work has shown that this novel device is also capable of recovering metalliferous values at a grind size that is much coarser than currently used in industrial concentrators, according to J D Miller et al in the IMPC paper Significance of Exposed Grain Surface Area in Coarse Particle Flotation of Low-Grade Gold Ore with the HydroFloat™ Technology, Quebec City, September 2016. Mike Mankosa, Eriez Executive Vice President of Global Technology, was a co-author. “In the current study, high resolution X-ray microtomography (HRXMT) was used to experimentally compare the degree of exposed grain surface area necessary to recover coarse particles using the HydroFloat technology to that attainable using a traditional mechanical flotation cell. The data indicate that exposed GPM gold Albion Process plant design criteria Parameter Throughput S 2- concentration S 2- oxidation Oxygen Utilisation Required k L a CIL Gold recovery Units t/h Design 13.1 Actual 14.5 % % % m.s -1 % 17.6 76 80 0.12 90 10.0 - 20.0 70 - 82 90 0.14 95 The authors conclude that: “Oxygen injection using convergent-divergent nozzles generate superior thrust and oxygen mass transfer compared to other gas injection techniques. Power delivered to the system is more efficient through gas injection rather than mechanical agitation. The HyperSparge is a development of the convergent-divergent nozzle and offers additional advantages over other sparging technologies contributing to a safer work environment, maximising process run-time and optimising energy input through the agitator. GT successfully scaled up the oxygen mass transfer system from the laboratory to the industrial scale at the GPM Albion Process plant which achieves greater than design performance in terms of oxygen mass transfer and oxygen utilisation.” And optimising flotation Conventional flotation machines are typically limited to a particle top size of 150-200 μm due to inherent constraints created by the pulp and froth phases. To overcome these limitations, a novel fluidised-bed flotation system has been developed by Eriez – the HydroFloat™ Separator. 40 International Mining | AUGUST 2017 grain surface area is a critical factor for coarse particle flotation. For the gold-bearing sulphide ore examined in this study, the HRXMT data suggest that near complete recoveries of coarse (850×500 nanometre) multiphase particles containing as little as 1% exposed grain surface area were realistically attainable using HydroFloat. As such, this new technology may offer a unique opportunity for increasing concentrator capacity by increasing the primary grind size needed for rougher/scavenger separations.” The HydroFloat Separator is an aerated fluidised-bed (or teeter-bed) separator. The synergistic effect of combining flotation with gravity concentration results in an outcome that cannot be achieved by either approach alone, says Eriez. “Air bubbles are dispersed by the fluidisation system, percolate through the hindered-setting zone and attach to the hydrophobic component altering its density and rendering it sufficiently buoyant to float and be recovered. The use of the dense phase, fluidised bed eliminates axial mixing, increases coarse particle residence time How the Eriez HydroFloat technology works and improves the flotation rate through enhanced bubble-particle interactions.” As a result, the rate of recovery is high for both fully-liberated and semi-liberated particles. “HydroFloat separators improve coarse particle recovery through: n Increased bubble/particle collision rates n Increased bubble/particle sliding time n Increased residence time n Decreased mixing n Decreased turbulence and detachment n Decreased buoyancy restrictions. As we know, froth flotation selectively separates hydrophobic materials from hydrophilic materials. Air bubbles can only stick to the desired mineral particles if they can displace water from the mineral surface, and can only continue to support the mineral particles at the surface if they can form a stable froth achieved by using flotation reagents.” “As the characteristics of froth can vary from day to day, a thorough understanding of froth transfer applications is critical when designing and selecting froth pumps. Insufficient froth volume factor (FVF) knowledge can often contribute to incorrect froth pump selections and hopper designs,” states Warren Taylor, Product Specialist at Weir Minerals. Pumping mineral froths using standard slurry pumps often leads to problems for operators, especially when treating mixed ores. Furthermore, froths can easily vary from brittle froth – generally large bubbles that are easily broken down, to very tenacious froth – generally fine, tightly bound air bubbles that remain in a froth state for many hours. In high FVF conditions such as medium to tenacious froths, air separation from the liquid contributes to air-binding within the eye of the impeller. This may create the expectation of cavitation, but rather than the collapse of vapour pockets, the entrained air bubbles rapidly expand in areas of low pressure w ithin the pump impeller