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By A. Goulsbra, S. McAllister, R. Dunne

Since 1992, a tailings gravity re-treatment plant has been in operation at the New Celebration Gold Mine to recover aurifer­ous pyrite (Martins, Dunne and Gelfi 1991; Martins, Dunne and Delahey 1993). The gravity pyrite concentrate is ground in a Tower mill to liberate gold (average particle size around 25µm) prior to cyanide leaching. Although the re-treatment plant has met the predicted gold recovery, based on original laborat01y testwork, there is still room for improved gold recovery. This requires enhanced pyrite recovery, especially in the finer size ranges. The application of centrifugal gravity separators would seem to be an ideal means to achieve this criterion. In particular, the Falcon continuous centrifugal separator (Series C machines) would appear to be ideal for this particular duty. A testwork program to evaluate the application of the contin­uous Falcon to recover pyrite from New Celebration ores was unde1iaken over a six month period during the later part of 1997. The work involved laboratory batch testwork, followed by con­tinuous testing of the Falcon Cl0 (2tph to 3tph) and Falcon C40 (l00tph) units. A summary of the results from this evaluation program are provided in this paper.

Jan 1, 1998

By Rein Buisman, Michael Fullam

This paper outlines the general operating principles, benefits and applications for the Pansep Screen. The Pansep is a continuous fine screen developed in 1997 capable of processing high volumes of fine mineral f actions continuously, and at small apertures.

Jan 1, 2000

By P. M. May, J. S. Solis, G. T. Hefter

Chemical speciation plays a critical role in many areas of gold processing. These include the formation of HCN in plant liquors, interference by copper in the extraction efficiency of gold, the recovery of adsorbed gold, and the behaviour of plant effluents in the environment. Thermodynamic modelling provides a cost-efficient method of rationalizing and even predicting of chemical behaviour. Unfortunately, because thermodynamic data for cyanide complexes are of poor quality and few are known under hydrometallurgical conditions. Such models are currently of limited use. This paper describes recent work on the thermodynamics of cyanide complexes of a range of metal ions. Data will be presented on the stabilities and enthal­pies (heats) and entropies of formation of a variety of metal ion species determined by potentiometry and calorimetry. Particular emphasis will be placed on the Cu(I)/CN- system.

Jan 1, 1995

By Shawn Orser, Jennifer Waddell, Mike Sierakowski, Tom Barrett

Production evaluations were conducted at Daisy Gold Mine (Glamis Gold, formerly Rayrock), between August, 1997 and August, 1998 to quantify the effect of 3M fluorochemical surfactants (fluorosurfactants) on extraction kinetics and gold recovery in gold heap leach mining operations. Ore was treated at a level of 7-10 grams surfactant per ton of ore using 3M Pluorad TM Leach Mining Additive PC-GOLD. Kinetics and gold recovery were determined by solution assay for each of the tests. Both tests indicated improved kinetics, and data from Test 2 was used for determination of a quantitative increase in gold recovery resulting from PC-GOLD addition. A discussion of test results including methods used to determine gold recovery is provided.

Jan 1, 2000

By Mohamed Younis, Keith Ward

INTRO PAGE

Jun 13, 2021

By Mark W. Johns

The design or optimization of a carbon-in-pulp (CIP) plant requires the determination and setting of a number of parameters to ensure optimum economic performance. A number of these parameters are either fixed, a function of the pulp, interdepen­dent, affect other parameters or outputs, so only a limited number of degrees of freedom exist from a metallurgical point of view. The traditional CIP contactor employs a low carbon concen­tration, a low agitation intensity and a reasonably long pulp residence time. The pump cell contactor employs a high carbon concentration, a high agitation intensity and a reasonably short pulp residence time. The two philosophies are dipolar in nature and the question arises as to which configuration is the optimum configuration for a CIP plant. The carbon particle size is shown to have a small effect on the capital cost of a CIP plant. A decrease in the pulp residence time, an increase in the pulp density, an increase in the carbon residence time, an increase in the agitation intensity and an increase in the number of stages are shown to have a positive effect on the capital cost of a CIP plant. The pulp residence time, the pulp density and carbon particle size are shown to have a small effect on the operating cost of a CIP plant. An increase in the carbon residence time, a decrease in the agitation intensity and an increase in the number of stages are shown to have a positive effect on the operating cost of a CIP plant. The optimum CIP plant, therefore, employs a short pulp residence time, the traditional pulp density, a long carbon residence time, the traditional carbon particle size, the traditional agitation intensity, and the traditional number of stages. Neither the pump cell configuration nor the traditional CIP configurations match the optimum configuration.

Jan 1, 1995

By Gregory Owen Lewis

The use of gravity concentration as a means of recovering the 'free' gold component from alluvial and milled ore products is widely used and is receiving increasing attention, particularly with the introduction of the centrifugal-type concentrating units. Because of ever-increasing mining and processing costs and a decline in the gold price, it has become important that the recov­ery efficiency from concentrates is improved so as to increase the yield of bankable gold from this primary recovery step. This paper outlines an alternative hydrometallurgical approach aimed at achieving overall gold recoveries in excess of 98%, together with the elimination of any secondary residue streams which, in the case of conventional treatment methods, require re-processing. An adaptation to the Minataur™ Process technology is being applied with the proposed method, incorpo­rating the pre-treatment of the concentrate, oxidative leaching of the pre-treatment residue, followed by precipitation of a high­purity gold. This route is seen to have application in all scales of operation. Selected results from laboratory-scale testwork are presented to highlight the discussion.

Jan 1, 1998

By Brendan Parker, Joseph Skrypniuk

Boddington Gold Mine1 (BGM) commenced production in 1987 and is currently ranked as the second largest gold producer in Australia. In a strategy to improve plant efficiency, constraints to plant performance were identified and prioritised with a view to maximising benefit for minimal expenditure. After identifying that leach kinetics and circuit residence time were major constraints, the introduction of oxygen was identified as having the greatest potential for the delivery of sig­nificant cost benefits. The application of oxygen, initially by conventional tech­niques, and subsequently by installation of Atomaer's Filblast gas shear reactor, improved gold recovery, reduced the resi­dence time constraint and enabled higher mill throughput to be achieved. Additional benefits included operation at lower pulp densities and a reduction in reagent usage. A significant reduc­tion in unit operating cost resulted from these benefits. This paper quantifies the above benefits in a format accept­able to both metallurgists and accountants by integrating the findings in a techno-economic perspective.

Jan 1, 1996

By W lethlean, Laurie Smith

When coarse gold is present in an ore, there are advantages in physically recovering this gold in the grinding section of the ore processing plant. This reduces the risk of the coarse gold being locked up in the grinding section equipment, reduces the quantity of activated carbon to be eluted and reduces the risk of gold passing out of the cyanide leaching circuit only partially dissolved. The free gold may be recovered by various mechanical means utilising the significant difference between the specific gravity of the gold and waste minerals. Frequently, sulphide minerals and ball mill attrition steel in the form of fines and chips are present in the ground ore and behave in a similar manner to the gold in the concentrating process. These materials must be removed to produce a concentrate suitable for direct smelting and several stages of cleaning, sometimes utilising different physical principles, may be required. The removal of these materials invariably results in a loss of gold from the final concentrate. The rejected materials containing significant quantities of gold are returned to the grinding section, consequently the opportunity for a high and early recovery has been lost. The quantity of gold returned to the grinding section will vary according to the number and type of cleaning stages and the physical characteristics of the materials and the gold but surveys of the gravity concentration processes suggest that it may be as high as 50%. To maximise the recovery of gold from the primary gravity concentrate, some operations batch cyanide leach this concentrate with or without additional reagents. The method of agitation and solution recovery vary. The most common method of agitation is by a high-speed propeller mixer and the least expensive but time-consuming method of solution recovery is by decantation after settling and by repeated decant washing. The pregnant gold solution is either introduced into the main ore leaching circuit or the gold is recovered by direct electrowinning. After commissioning in 1994, Union Reefs Gold Mine (URGM) experienced below expected recovery of gold from the gravity concentrate generated from the Knelson Concentrators. It was shown that the recovery into the Knelson Concentrate was high but that the subsequent mechanical concentrating techniques of tabling and magnetic separation resulted in significant gold being returned to the grinding circuit.

Jan 1, 2000

By G. S. Walker, W. van Bronswijk

The accurate determination of free cyanide and metal cyanide complexes is of increasing interest to Carbon-in-Pulp (CIP) gold extraction operations as cyanide consumption is an important economic factor in the processing of complex ores. Characteristically complex ores are high cyanide consumers and these ores usually contain a range of sulfide minerals e.g. covellite (CuS), digenite (Cu1,S), chalcocite (Cu, S), Pyrrhotite (Feci-x)S), marcasite (FeS2), arsenic and antimony sulfides and zinc sulfide. These minerals can consume significant quantities of cyanide, e.g. various copper(!) cyanide complexes such as CuCN, Cu(CN)2·, Cu(CN)/ and Cu(CN)/ can form, depending on the cyanide to copper ratio in solution. Measurement of free and complexed cyanide is thus a prerequisite for efficient cyanide dosage control. Free cyanide can be determined potentiometrically or amperometrically but the methods are prone to error and are laborious [1]. Metal cyanide complexes can be determined by reverse phase HPLC, however, the species ofa single cation (e.g. Cu(CN)i-, Cu(CN);2 and Cu(CN)/) elute as one species [2]. Additionally the high amount of suspended matter in CIP leach solutions tends to introduce errors. Raman spectroscopy has the potential to be used as an in­line or on-line method of analysis. Free cyanide and the cyanides of gold, silver, copper and iron have been studied in aqueous alkaline solutions with a view to developing such a method. Spectra were obtained with a Bruker RFSl00 FT-Raman spectrometer using a 1064 nm laser delivering 800 mW of power at the sample. Depending on the solution, 250, 1000 or 4000 scans at 4 cm-1 resolution were accumulated. The cyanide stretches observed were relatively narrow (10 15 cm-1 full width at half height) and well resolved (Figure 1 ).

Jan 1, 1995

By Peter J. Stewart

My first experience with carbon reactivation in the gold industry was at Whim Creek, Meekatharra some 15 years ago. Very little was known, in fact, carbon reactivation kilns in the gold room were a complete mystery. Ten years ago at conferences such as this the mystery was more as to why field kilns would not reproduce activities achieved in the laboratory. A carbon reactivation kiln manufac­turer was thought to be brave or stupid to speak at a venue such as this. Reactivation kiln design has improved dramatically in the past 10 years and with a few exceptions, most kilns operate well. May I suggest that now, the focus is on plant practice rather than kiln design, and that the basics of plant practice as it relates to carbon activity needs revisiting. As metallurgists like to talk on engineering, accountants on the Economy and vice versa, my presentation on Carbon Reactivation will focus on plant design and operation as it effects carbon reactivation. There have been some excellent papers published over the past 15 years on the basics of carbon reactivation in relation to gold processingl,2,}. Taken that kilns operate and are effective to a greater or lesser degree, plant design and operating practise have an enormous bearing on carbon activity, solution tail, carbon loss and other cost items. This presentation will not argue the merits of equipment used for the thermal reactivation of organically fouled carbon, questions on this subject are welcome over a drink after this session.

Jan 1, 1995

By William M. Clark

In 1988, the Chemical Manufacturers Association (CMA) launched Responsible Care®, a program of guiding principles created to address the publics' concern about the manufacture and use of chemicals. The Product Stewardship Management Practice code is a key component of the program. Along with the other five comple­mentary codes - Community Awareness and Emergency Response (CAER), Pollution Prevention, Employee Health and Safety, Process Safety, and Distribution - it has been initiated to protect the health and safety of member companies employees, neighbors, customers, the public and the environment. Possibly no other Management Code requires greater collec­tive effort or comprehensive commitment to implement than Product Stewardship. With its mandated cradle-to-grave control, every employee is required to consider all of the potential cir­cumstances involving product and processes, from raw material supply to customers final use or consumption of product. Degussa Corporation, a long time CMA member, fully endors­es the Responsible Care initiative and is most active in imple­menting the various codes. In fact, the guiding principles of the program are an integral part of the company's business strategy. Degussa recognizes that its long-term success and the health of each of its products, the company and the chemical industry itself, is contingent on the successful implementation of the program. Furthermore, the company believes its role in society and the economy can only be justified and sustained if it improves the overall quality of peoples' lives. Consequently, it is a dictum that Degussa products must provide a net benefit over their entire life cycle - from inception to final disposal - both in terms of their utility and their impact on health, safety and the environment.

Jan 1, 1998

By John C. Schneider

During the past decade, operators and researchers have worked toward a better understanding of the mechanisms operating in flotation. As reported by W. J. Trahar in 1981, this work commenced with the operators determining a relationship between recovery and particle size. They defined three particle size ranges, that being fine, intermediate and coarse. It was noted that the fine and the coarse ranges had slower flotation rates than the intermediate range as demonstrated by their lower recoveries.

Jan 1, 1998

By Paul Chamberlin

Although performing a heap leach test is inherently simple, a lot of information beyond extraction, leach time, and reagent consumption can be obtained from a well designed test program. The following is a list of information to look for and acquire when performing column tests and field heap leach tests.

Jan 1, 1998

By Wade N. Ellett, K. Marc Le Vier, Timothy A. Fitzpatrick, Kenneth A. Brunk

As the gold mining industry matured through the 1980' s, and into the 1990's, the development of refractory gold orebodies has become more prevalent. Newmont Mining Corporation developed and commercialized flash chlorination for the treatment of carbonaceous preg robbing ores; Homestake Mining Company developed and commercialized the industry's first application of autoclaves. Barrick installed the world's largest autoclaves on whole ore treatment a few years later. Dry grinding and roasting followed at Placer Dome's Cortez, Freeport -Independence and Newmont's Carlin operations. Today, numerous papers are presented on research efforts worldwide which address treatment of refractory gold ores by bioxidation, roasting, autoclaving, alternative lixiviant treat­ment and other novel process ideas. The overall objectives are to develop economic processes for difficult refractory ores where no process exists or conventional practice is cost prohibitive. Successful research can lead to lower operating costs, increased profits, and increased ore reserves. One such research effort directed by E I DuPont de Nemours and Company, Advanced Mining Technologies, was focused on gold ores which were refractory in nature due to the cyanide soluble copper content. Approximately five years of research effort culminated in a patented process (U.S. Patent 5,411,575)1 and the formation of a new joint venture company, AuGMENT Technologies, in 1995 with Newmont Mining Corporation. Today significant progress has been made in moving the laboratory scale tests to commercialization.

Jan 1, 1997

By M. S. Hunter, Al Bishop

In 1994, Lone Tree Mine invited Hunter Hawk to participate in a problem-solving arena at their mine located in Valmy, Nevada. Lone Tree was experiencing consistency problems with autoclave valve component quality and delivery. Based upon a prior working relationship at Homestake Mining Company's McLauglin Mine, located in Lake County, California, both customer and vendor enjoyed a measure of rap­po1i and trust - the keys to problem solving communication. This paper is an overview of the problem solving process that has contributed to Lone Tree's excellent record of 95 per cent autoclave availability since 1995.

Jan 1, 1998

By Corale L. Brierley

This paper lists commercial bioheap and stirred tank bioleach operations and explains the status of these operations. A total of 17 commercial-scale bioleaching plants have been commissioned. Bioleaching plants are divided into two technology applications: bioheaps and aerated stirred­tanks. In bioheap leaching, secondary copper ores or sulfidic refractory precious metal ores are crushed and bioleached on pads. Stirred-tank technology is used to bioleach base and precious metal concentrates.

Jan 1, 1999

By DIONISSIOS T. HRISTOPULOS, JUAN DIAZ, Kray Luxbacher, Steven Schafrik, Zach Agioutantis

Explosions in underground mining due to methane gas have been the leading cause of incidents and fatalities in the mining industry. The main objective of this research is to develop a forecasting methodology for methane gas emissions based on time series analysis. Methane time series data were retrieved from atmospheric monitoring systems (AMS) of three underground coal mines in the United States. The AMS data were preprocessed and statistically evaluated to explore the potential autocorrelation of methane gas. It was concluded that the autoregressive integrated moving average (ARIMA) time series model used in the one-step-ahead forecasting mode provides accurate estimates that match the increase or decrease of the methane gas emission data.

Feb 1, 2023

By Kimberlie Staheli

A new sanitary sewer was installed in Pleasant Hill, California using microtunnelling methods. The project consisted of 693 meters of 1372 mm and 1981 mm concrete pipe. A Herrenknecht AVN 1200 was used to install the nominal 1372 mm pipe in three drives. The machine was then fitted with an oversized shield used to install the large diameter pipeline. This articulated shield allowed the excavation of a 2362 mm diameter hole with a 1524 mm machine-- a technique new to North America. This paper reviews the design considerations for the articulated shield and reports on the project challenges and solutions to overcome these challenges.

Jan 1, 1995

By W. J. Garmoe

The Carr Fork mine is located approximately 50 kilometers southwest of Salt Lake City, Utah, in the Bingham or West Mountain District, adjacent to the Bingham open pit copper mine. Applied geology at Carr Fork, by Anaconda Minerals Company personnel, includes detailed geologic mapping and sampling of underground workings, logging and sampling of drill core and cuttings, and the preparation and posting of geologic maps and cross sections for geologic interpretation, ore reserve calculation, mine operations, and long range planning. Accurate and easily understood graphic recording of Carr Fork geology is essential for optimum use by operating and engineering personnel. The design and implementation of exploration, development and definition drilling programs, research into geological spatial relationships, and analysis of structural complexities of the Carr Fork deposit are also integral parts of the applied geology program.

Jan 1, 1992