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By Ryan Marsters, Adam Pring, Robin Dornfest

Raw water supply in the central Rocky Mountains often relies on trans-basin conveyance. Many of these older diversions incorporate high-elevation, miles-long tunnels driven over a century ago in hard rock. Tunnels were excavated using conventional drill-and-blast mining and weak ground was supported by timber sets and other various means. Over time, timbers rot and fail, rock quality deteriorates, and the timbers are gradually replaced by more timber, steel patches and braces, formed concrete, rock bolts, split sets, shotcrete, and other means which are commonly applied over existing support, thereby reducing tunnel cross sections, obscuring previous support systems, and rarely addressing the failing rock itself, leading to further deterioration of both the rock and the existing support. Traditional investigation techniques to assess compromised areas are often unfeasible due to access, depth, rubble and voids behind weight-bearing existing supports, confined space, poor invert conditions, poor ventilation, and flowing water. This presentation will discuss design procedures for assessing obscured ground conditions, assigning support classes which accommodate for unknowns, and implementing contractual means to address inevitable surprises or quantity overruns. Case studies include raw water supply tunnels in the Rocky Mountain region constructed between early to mid-20th century.

Dec 1, 2022

By Harry Asche

Tunnels are frequently specified by owners to be designed to a structural code, often a bridge code. In the USA, AASHTO have created a tunnel code, based on structural principles, the AASHTO LRFD Tunnel Design Specification. The Load Resistance Factor Design method (LRFD) described in the AASHTO title is an approximation to the probabilistic design of structures, based on the independence of load and resistance. This methodology is well known to be problematic in geotechnical design, but it is widely used. The paper considers the difficulties of this approach and describes alternative approaches that would result in more appropriate designs for tunnels.

Jun 13, 2021

By Sam Lo Grasso, Carlos Herranz Calvo, Stuart Warren, Ted Giesing, Charles Marchesano

Mott MacDonald and Project Management Advisors are providing Technical and Project Management services for San Diego County for the Courthouse Commons Project. The Courthouse Commons Project involves the redevelopment of three downtown blocks owned by San Diego County and construction of an Inmate Transfer Tunnel between the County Central Jail and the San Diego Central Court. The tunnel will be 327 feet long, crosses the San Diego Fault and is being constructed using the Sequential Excavation Method (SEM). This paper discusses the history and procure‑ ment strategy for the project, the technical aspects of the transfer tunnel and the con‑ struction progress of the tunnel to date.

Jun 13, 2021

By Thomas Schwind, Elmar Feigl, Gerald Skalla, Angelos Gakis

Cedarvale station was constructed as part of the Eglinton Crosstown Light Rail Line, under the operational Yonge-University Line Subway box of Toronto Transit Commission (TTC). The station was constructed as an open-cut, which necessitated the underpinning of the existing TTC box to minimize the impact on the Subway and allow its unhindered operation. Six mined galleries, 4 m wide by 2.75 m high, were excavated sequentially (SEM) immediately under the existing box, to provide the required space for the installation of the main underpinning beams. This novel solution was executed successfully providing quick access for the main excavation works to commence.

Dec 1, 2022

By Ted DePooter, Mun Wei Leong, Chad Frederick

Downtown Bellevue Tunnel (DBT) is part of Sound Transit’s $3.7 billion, 14-mile light rail transit system from downtown Seattle, across Lake Washington, to the cities of Mercer Island, Bellevue, and Redmond. The tunnel was the first Sound Transit East Link project and posed significant construction risk. This paper discusses implementation of design changes to the soft ground tunneling method, implementation of several technologies such as the use macro-synthetic fiber initial shotcrete lining, use of spray-applied waterproofing, and use of shotcrete for the final tunnel lining. These efforts allowed for significant time and cost savings to the project.

Jun 13, 2021

By Jamal Rostami, Mark Board, Clayr Alexander, Muthu Vinayak Thyagarajan

In the past several decades, many major equipment manufacturers have ventured into developing new technology for underground hard rock excavation. This includes variety of configurations for full and partial face mobile excavation units. Mining industry prefers machines that can excavate noncircular, flat invert profiles and be able to make tight turns in hard rock. The need to use disc cutters for cutting hard rock has impeded the development of such machines due to the need for gripper system or large mass of a machine to support the force requirements of the disc cutters. Most of the prior attempts have been partially successful and the operations have faced some practical limits and challenges. Among the units that have been successfully used, one can name mobile miner, which was used for rock excavation in some projects. A redesigned mobile miner, called the “Remote Vein Miner,” or RVM, has been developed by Epiroc for underground hard rock mining in Hecla’s Lucky Friday Mine. This equipment potentially opens numerous opportunities for innovation in civil tunneling projects, where the operational flexibility and accessibility of a TBM’s limited tunnel path, design of the profile, and cost are limiting factors. This paper explores the application of the RVM in tunneling projects, its advantages and possible areas of innovation in tunnel planning and design.

Jun 13, 2021

By Richard Crowell, James Gillaspie

A concentrate biooxidation process was successfully demon­strated in the field in a remote part of northwestern Mexico. A 275 tonne (300 st) biooxidation heap was constructed using GeoBiotics' proprietary GEOCOAT™ coated concentrate process. The pyrite/chalcopyrite/sphalerite concentrate was bioox­idized in the heap for 60 days. Cyanide leach recovery of the con­centrate increased from 68% gold recovery at a cyanide consump­tion of 1.6 kg NaCN/g Au (llO lbs/oz) in the as-received concen­trate, to 94% gold recovery at a cyanide consumption of 0.37 kg NaCN/g Au (27 lbs/oz) in the biooxidized concentrate. The heap was constructed at a rate of7 tonnes (7.5 st) concentrate per hour, using typical heap leach equipment and easily scalable methods. Heap operations demonstrated that energy dissipation in the humid summer environment was easily controlled by low pressure aeration and management of solution chemistry and application. Observations of the demonstration heap appear to support the presence of reflux of moisture within the biooxidation heap.

Jan 1, 1998

By A. Russell, M. N. Hughes, Jack Barrett

The bacterial oxidation of arsenopyrite has been shown to be an efficient, economic and environmentally acceptable method for the liberation of any gold content . The mechanism of the process is not certain but is usually considered to involve direct and indirect reactions with respect to bacterial involvement. The direct reactions are those in which the bacteria attached to the mineral surface cause its dissolution, with dioxygen being the oxidant. The iron(III) produced in solution is the chemical oxidant in the so-called indirect reactions. Barrett et al 2 showed that a synthetic bio-oxidation solution (with no cells present) could dissolve up to 15% of an arsenopyrite sample, the products of the chemical oxidation being iron(II) and arsenic(III). This paper describes an extension of the investigation of the chemical process and its imp! ication for the mechanism of the bio-oxidation of arsenopyrite.

Jan 1, 1990

By Matthew A. Omofoma, Andrew P. Hampton

The application of the Cyprus Cyanisorb process was investigated using a pilot scale facility at the NERCO DeLamar Silver Mine (DSM) in Owyhee County, Idaho. The purpose of this process is to remove cyanide from the DeLamar mill tailings slurry prior to its introduction to the tailings impoundment. This will maintain the tailings impoundment solution in a detoxified condition and thus prevent migratory bird mortalities. The cyanide removed is to be collected and recycled to the mill. The process successfully recovered approximately 90 percent of the weak acid dissociable cyanide (WAD), reducing the effluent tailings cyanide concentration from about 300 ppm to less than 20 ppm. This was accomplished by stripping the slurry with air in a packed tower and recovering the volatilized HCN in a packed absorption tower. Data were obtained for the design of the full scale facility including the stripping and absorption towers, currently under construction at the DeLamar Mine site. Finally, test results indicated that the final pH of reneutralization can be optimized to provide for minimal gold and silver losses, while selectively precipitating unwanted metal impurities (Zinc, Selenium, Iron, and Copper) from solution

Jan 1, 1992

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