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By Qiu Rongqing, Huang Kongxuan

This paper summarizes the results of treating arsenic­bearing refractory gold concentrates from six gold Mines of Chi­na by using bioleaching method and discusses the conditions of bioleaching processes. Results indicate that Thiobacillus fer­rooxidans T-3 Strain can intensely oxidize arsenopyrite, how­ever oxidation rate and degree differe considerably for different. During initial inoculation of 5 X 106 cell/ml. FeH contration generaly 4 -8 g/1. Sample size > 80 % - 3 20 mesh and pulp density 10 % ( w /v) and leaching time ,1 -- G clays, arsenic re­moval rate reached more than 80 % , Fe extraction ,10 - GO% desulfurization rate 30-45% after bacterial oxidation of 4-G days.

Jan 1, 1992

By Peng Yu-mei, Cao Zhi-yun, Fan Qing-en

In China, an enormous amount of Au-Ag bering calcines, residues and tailings are produced each year from various sources in mining, metallurgical and chemical industries. For a long time, these materials have been either stored up in dumps or disposed of into rivers, resulting in not only waste of resources but also severe environmental pollution. It is therefore of great significance, both from economical and public welfare points of view, to recover efficiently and make full use of the metallic values from these miscellaneous materials. In this paper the physical and chemical properties of these Au-Ag bearing calcines, leached residues and tailings are described and the current status of their utilization are briefly outlined, followed by a more detailed description of some innovative processes now in practice. Lastly, the potential prospects of gold and silver recovery from these materials in China, particularly in the Hunan province, are envisaged.

Jan 1, 1998

By P. Richardson, B. Sceresini

The carbon-in-pulp and the carbon-in leach process for the recovery of gold and silver from cyanide leaching of ores is now widespread in the precious metals mining industry. However the presence of various base metals can have a detrimental effect on the efficiency and the economics of the process due to high cyani,:••? consumption and a reduction in leaching and adsorption rates resulting in poor recovery of the precious metals. Furthermore the presence of fast leaching and adsorbing metals such as copper can significantly reduce carbon loading capacity for the precious metais thereby necessitating a higher carbon inventory, more frequent stripping and poor bullion quality resulting in higher production costs. This paper describes the development and application of a process for the recovery of copper and and the recovery and re-use of the associated cyanide from the leach circuit at the Mt. Gibson Gold Project in the Murchison Goldfield in Western Australia. The process provides a means to counter-act the detrimental effects of the copper which occurs in the ore as various oxide and sulphide minerals including an extremely fine chalcopyrite powder. It has the added benefit of recovering the base metals in this instance copper, in a saleable form. The process is subject to a patent application by Reynolds Australia Metals, Forsayth N.L. and the author.

Jan 1, 1991

By D. K. Gibson, A. I. M. Ritchie

The phenomenon of acid drainage is likely to occur whenever pyritic rock is broken up, permitting access of air and water. The basic chemistry of the oxidation process is described by the equations below:- FeS 2 +1120 + 7 02 ➔FeS04 +112S04 +1440k.J This reaction proceeds rather slowly, although believed to be bacterially catalysed to some extent. Once sufficient ferrous ions and acidity have been established the following two reactions take over, yielding the same net result but at a much greater rate. First, ferrous ions are oxidised to ferric; this is an extremely slow reaction unless bacterially catalysed.

Jan 1, 1991

By Kenneth B. DeGraaf

The development of precious metal recovery processes using chloride systems has mostly evolved from the development of chloride based treatments for base metal concentrates or ores. The recovery of silver from chloride solutions within a process designed for the treatment of base metals usually is part of a solution purification stage. This paper discusses the development of the silver recovery stage used in the GCM HydroCopper process.

Jan 1, 1990

By LeRoy D. Poindexter

TWO-INCH TO MINUS #100 MESH IN ONE GO The need to reduce mineral ore to a very fine mesh economically has been a timeless problem in the mining industry. With this as the specific and we.l.l focused objective, the Cyclone Crusher has been designed and is being manufactured. Utilizing space age technology from such military projects as piercing steel plate with plastic particles, the Cyclone uses the physical principles of centrifugal force. Through a combination of very high G-forces and asymmetrical loadings between a cone and anvil, particles are pulverized to very fine mesh gradation. Just how fine the final product will be, of course, is dependant on a number of factors. The machine setting, the feed rate, the gradation of the in feed material, the molecular structure of the material, and the original fracture planes of the material all affect the end result.

Jan 1, 1992

By Dan Slyter

This paper prov ides comparisons be­tween Merrill-Crowe and Carbon Adsorption pl Rnts 11sed for Pree ious Metal Heap Leach Operations. During the first stage of mine devel­opement, the question arises as to type of gold recovery circuit to be employed, Car­bon or Zinc. Several important factors to consider in answering this question are: Au/Ag ratio Solution grades Daily plant production Plant throughput required Plant gold inventories

Jan 1, 1992

By John E. Litz, Charles W. Kenney, Wayne Carter

Refractory gold ore pretreatment processes continue to receive much attention. This paper compares the relative economics of treating ores by oxygen pressure oxidation, roasting and bacterial oxidation with or without preconcentration by froth flotation. Capital and operating cost estimates for each method of pretreatment were prepared and these estimated costs and ore sulfide grades then are used to compare the process economics. The study indicates that the most significant item affecting the economics is the amenability of the ore to flotation. The cost benefits of flotation are $10-13 per tonne ore processed (2%-4% s=, 10:1 ratio of concentration). In most cases bacterial oxidation has the lowest overall cost, especially if less than complete oxidation of the sulfides will give acceptable recovery, however bacterial oxidation has yet to be practiced on a large scale. In all situations pressure oxidation shows the highest cost. However, the cost differences between the treatments are small, less than $7 per tonne.

Jan 1, 1990

By Mike Irish, Deb Mukhapodhyay

It has been demonstrated by Arrowhead Industrial Water that a proprietary reverse osmosis technology can be used efficiently, effectively, and economically to reduce the levels of cyanide species, heavy metals, and other ions as shown in Figure 1 to allow safe discharge of a permeate solution to the environment. A simultaneous benefit of this process was the cost savings of reduction in quantities of cyanide requiring destruction by hydrogen peroxide and recovery of a concentrated gold and silver value in the concentrate solution.

Jan 1, 1992

By Thomas J. DeMull

Heap leaching was introduced to the precious metals mining industry approximately two decades ago as a simple, low cost method for recovering gold and silver from ores. Since that time, operational experience has contributed to knowledge and understanding of the process, making it a reliable alternative to conventional milling processes for low grade ores. At time of this writing, dozens of heap leach operations are active producing hundreds of thousands of ounces of gold and millions of ounces of silver annually. These successes have caused the popular press to acclaim heap leaching "high-tech" gold mining, but, despite the hype, the process remains a simple one. An example of simplicity in heap leaching is the operation established in 1986 at Amax Gold's Sleeper Mine. Starting with a simple goal, namely to produce gold from sub-mill grade ore at low cost, heap leaching was rapidly implemented at Sleeper; only five months after testwork started, leaching commenced on the first commercial scale, 50,000 ton heap of low grade ore. Sized at 600,000 tons per year to produce 10,500 oz gold per year, the low grade heap operation has performed beyond expectations. During the first year of production, 881,800 tons have been leached producing 15,665 oz of gold and 35,528 oz of silver. Operating ·costs for the first year have averaged $112 per oz gold produced ( or $95 per oz if silver credit is included). Successful implementation of heap leaching at Sleeper has had a dramatic impact on ore reserves and future operations.

Jan 1, 1998

By Leslie C. Thompson

The heap leach process used for recovering gold from oxide and sulfide ores is operated as a closed circuit system in which the cyanide process solutions are continuously recy­cled. In a well-designed operation there is little or no dis­charge of cyanide to the environment. Spent leached ore residues are water washed to remove most of the trace cyan­ides and precious metals remaining after completion of cyan­ide leaching. After the washing step, small amounts of cyanide, metal-cyanide complexes and nitrates remain in the residue. Most of the cyanide and nitrate residue constituents exist in the pore water of the spent ore rather than in the solid mineral fraction. More than 90% of the complexed cyanides in a freshly washed ore residue are present as free cyanide or weakly complexed metal-cyanides. Natural volatilization and decom­position rapidly remove most of these easily dissociable cyanides from the spent ore. Only the stable, strongly com­plexed metal-cyanides, such as gold, cobalt or the ferrocyan­ides and other constituents such as nitrates have a long term persistence in the spent ore residue (Towill et al). Despite washing and natural removal mechanisms, spent ore has the potential to act as a point source of com­plexed cyanides and nitrates for soil and groundwater con­tamination if inadequately contained (Huiatt et al). The groundwater contamination is caused by the leaching of the soluble cyanide compounds and nitrates from the pore water of the residue.

Jan 1, 1990

By J. M. Carter, Rodney H. Sergent, L. E. Kun, J. T. Pressly

Underground mine service water in South Africa is used for dust suppression and cooling the environment as well as the pneumatic rock drills. Although the chilled water is not intended for potable use, it is often used as drinking water by mining personnel. Furthermore, droplets sprayed are liable to be inhaled. The water is recirculated on a continuous basis and is a potential source of infection by intestinal microorganisms or water-borne diseases such as cholera or typhoid. In order to protect the health of the underground workforce it is customary to disinfect the chilled service water, The bacteriological quality of the water is monitored by enumerating total aerobic bacteria (TAB), total coliforms (C C) and Escherichia coli (E Coli). E coli is an indicator of human faeca_l __ - -- contamination, The bacteriological standard specified by the Anglo American Corporation for mine service water is less than 3000 TA B per 100ml, less than 2 CC per ml and the total absence of E Coli. There are several disinfecting agents available for use. Among these are UV irradiation, ozone, chlorine dioxide and compounds that produce hypobromous and hypochlorous acids. Historically, the methods of treatment have been chlorine based and include the use of gaseous chlorine (surface installations only), calcium hypochlorite granules or tablets, chlorinated cyanurate tablets, sodium hypochlorite solutions and hypochlorite produced by electrolysis.

Jan 1, 1991

By Trent Temple, Curtis Johnson, John Mudge

Newmont Gold Company uses centralized carbon handling facilities to strip loaded carbon from five mills and four leach facilities located along a 38 mile stretch of the Carlin Trend in Nevada. Both Zadra and AARL elution processes are employed at this centralized facility which is located near the company's Gold Quarry operations. The Zadra elution circuit was commissioned in 1985 and later expanded in 1987. This circuit can strip carbon at a rate of 24 tons per day. The AARL elution circuit, commissioned in 1988, also has the capacity to strip 24 tons of carbon per day. Two horizontal, rotating, regeneration kilns are used to reactivate approximately 60% of the stripped carbon before it is returned to the mills or leach facilities. One kiln is located in the Zadra plant, while the other is located in the AARL plant.

Jan 1, 1990

By E. Haug, Quamrul Ahsan, R. Norcross

Cyanide leaching is the most common process employed in the majority of the gold extraction plants. These gold extraction plants naturally generate tailings and/or effluents that contain highly toxic cyanides, In geographic locations with excess precipitation and therefore net positive water balance, a portion of these tailings must be discharged. Before these highly toxic cyanide-containing effluents can be discharged to the waterways, cyanide and any other toxic substance must be destroyed. Geographic locations with high evaporation and low precipitation, as in the western USA, result in net negative water balance and therefore these plants can operate with a zero discharge option. However, with the current stringent environ­mental regulations and concerns for bird and wildlife mortality, even these operations may be required to partially treat their tailings to preclude potential harm to wildlife. Furthermore, heap leach opera­tions are now generally required to detoxify the heaps before abandonment. It is, there­fore, apparent that all gold extraction plants may be required to install some form of effluent treatment in order to achieve the above objectives,.

Jan 1, 1990

By J. L. Waldron

This paper presents a theoretical tool used to analyze gold recovery problems at Dee Gold Mining Co. The first step in addressing the problem was realizing that lower gold extraction was linked to high silver grades, and could not be correlated to either the carbonaceous or sulfidic content of the ore. Analyses of metallurgical testwork, blasthole, and mill recovery data demonstrated that decreases in gold extraction correlatP� well to increases in silver extraction. Figure 1 illustrates this for 1991 mill operations. This was the starting point for the work described in this paper.

Jan 1, 1992

By Len H. Steele

To date VMD have designed, built and supplied nine autoclaves to various mining companies in Canada, the US, and Papua New Guinea. Initially, completely fabricated and lead lined units were shipped. The logistics of Placer Dome's Porgera PNG Project necessitated fabricating and lead lining each autoclave in five sections for transportation to site, each piece weighing approximately 30.5 tonnes. Support equipment such as turning rolls, automatic and manual welding machines had to be set up on site to facilitate assembly of these units which was a challenge in planning. This on site erection programme was completed in three months.

Jan 1, 1992

By P. G. Semple, K. W. Major, P. Eng.

The recent increase in development of refractory gold deposits has resulted in changes to the traditional treatment processes. The selection of the preferred refractory treatment process is dependent on the mineralogy of the ore. One process, which has recently gained increasing attention, utilizes dry grinding and roasting of the whole ore. This paper will discuss some of the considerations to be addressed during the design of the process fl owsheet and what the effects of the various alternatives will be on the plant capital and operating costs. The paper will be based, in part, on current experiences with dry grinding, roasting plant design and start-up.

Jan 1, 1990

By Rick T. Richins

Despite what may be overwhelming evidence that natural degradation of cyanide and cyanide attenuation in hydrogeochemical processes are capable of reducing or eliminating potential water quality problems associated with heap leach facilities, the recent sharp increase in the price of gold and wide interest in the cyanidation process has focused all regulatory eyes on cyanide leaching. Regulations continue to increase, design criteria are more strict, and detoxification requirements approach or exceed the level of detectability. Current governmental regulation of mining and milling operations using cyanide varies considerably from state to state. The lack of regulatory consistency at this level is largely attributable to the current Bevill Amendment exclusion of mine wastes as potentially hazardous wastes, the undefined status of the Environmental Protection Agency's ongoing mine wast study effort, and the mining industry's reluctance to develop a consistent policy regarding state versus federal mine waste regulation.

Jan 1, 1998

By David Martin Menne

Introduction

Jan 1, 1991

By Deepak Malhotra, Sean Armstrong, Linda Baltich

The economic profitability of any mineral company is dependent upon maximizing mineral recoveries while minimizing costs. The effectiveness of any strategy to meet this objective is dependent upon firstly obtaining quantitative information concerning the steady-state metallurgical balance of the plant, and secondly, how efficiently this information is used to improve/optimize plant performance. This two-step approach can be designated as a "plant audit." Plant audits on a routine basis can be very expensive and time-consuming. Most plants have reduced staffs to cut costs. The remaining staff has to spend time to solve production/operation problems, thereby leaving limited resources (i.e., people, time, and money), for plant auditing. This paper briefly reviews plant auditing categories, and a systematic approach to auditing which has been successfully used at several operations. An example illustrating the use of this approach in gold operations is discussed in this paper.

Jan 1, 1992