Search Documents

By Jaime Lomelin

The brines from the sub-surface of the Laguna del Rey dry lake are pumped to Química del Rey, S. A. plant, where they are cooled in adiabatic crystallizers precipitating sodium sulphate decahydrate. This salt is dehydrated in multiple effect evaporators and dried in rotary kilns producing high purity anhydrous sodium sulphate. The spent brines from the sodium sulphate operation are concentrated in solar ponds, precipitating astrakanite and leaving a brine with a higher concentration of magnesium ions. This brine is treated with calcium chloride solution to eliminate the remainder of sulphates, leaving a solution of magnesium chloride ready for the manufacture of refractory grade magnesium oxide or periclase. The magnesium chloride is reacted with dolime to produce magnesium hidroxide which is washed, filtered, and calcined to produce soft burned magnesium oxide, which is briquetted and dead burned to produce the periclase.

Jan 1, 1984

By H. D. Freeman

The Pacific Northwest Laboratory (PNL) is developing cover technology for uranium mill tailings that will inhibit the diffusion of radon to the atmosphere. As part of this cover program, an improved radon flux measurement system has been developed. The radon measurement system is a recirculating, pressure-balanced, flow-through system that uses activated carbon at ambient temperatures to collect the radon. With the system, an area of 0.93 m2 is sampled for periods ranging from 1 to 12 h. The activated carbon is removed from the radon trap and the collected radon is determined by counting the 214Bi daughter product. Development of the system included studies to determine the efficiency of activated carbon, relative calibration measurements and field measurements made during 1980 at the inactive tailings pile in Grand Junction, Colorado. Results of these studies are presented.

Jan 1, 1981

By Michael Ferrell

The primary reason pigments are used in plastics is to impart a desired color to the plastic. Color is one of the more important assign considerations associated with today's market oriented society. Secondary reasons for adding pigments to plastics include: 1. Improved UV stability 2. Enhancement to selected physical properties 3. Changes in optical properties Pigments may be used at loadings as high as 20% or as low as .001%. Generally the loading levels are between 0.2% and 2.0%. Pigments may be added to the plastic either by the manufacturer of the plastic, or by the user of the plastic. If the customer buys material that is already colored, it is referred to as "pre-colored". If the customer buys uncolored plastic and adds colorants, the process is referred to as "in-house" coloring.

Jan 1, 1985

By Yongping Hu, Dianchen Cai, Congya Zhang

China is a rich in stromite mineral resource. Unfortunately, the resource is very difficult to separate by using conventional flotation method because stromite and gangue minerals are very fine disseminated, the average size of them is about 10 µm or below, and the content of clay minerals such as illite is 19% or even more. In this paper, the aggregation floatation behavior of ultrafine (-10 µm) stromite, illite, ablbite and quartz using anion collector were studied. The result show that, Oxidized paraffin (O.P) is a good collector and has better selectivity for stromite particles flotation. The salted sodium silicate depressed illite gangues minerals effectively. The separation of mineral mixtures was carried on successfully at one stage flotation by the technique. The mechanism of O.P. and salted sodium silicate were studied and discussed by using IR and Zeta- potential measurements.

Jan 1, 1995

By D. N. Madge

A survey is given of production scheduling systems currently in use or contemplated for future use in Cominco operations. Emphasis in this presentation is made on the chain of decisions that are made with the help of mathematical programming models. Some attention is devoted to the structural properties of the models.

Jan 1, 1966

By A. M. Laird

Endako Mines' molybdenum operation is located near the geographic center of the province of British Columbia, Canada. The property is six miles south of the Northern Transprovincial Highway and the northern main line of the Canadian National Railway. The area is broken by high hills covered with dense stands of spruce and pine with vast areas of the valley floors covered with aspen and poplar. The climate is moderate with precipitation averaging 22 inches per year. Approximately four feet of snow accumulates in the winter, and temperatures range from 900 F. in summer to -40° F. in winter. The orebody, a lowgrade porphyry type deposit, occurs in a widespread granitic intrusive which has been locally weakened at the intersection of two regional faults. In this vicinity the quartz monzonite has been further shattered to permit the entry of mineralizing solutions and local dykes. Two types of mineralization occur within the orebody. The most prom¬inent is the six inch to four foot wide continuous quartz veins with characteristic ribbons of molybdenite and frequently finely-divided grains of molybdenite within the quartz. The second type occurs as fine fractures filled with quartz molybdenite in the form of a stockwork halo radiating out from 20 to 200 feet from the quartz veins. Minor hematite, magnetite and chalcopyrite are also present. Mineralization is roughly proportional to the extent of kaolinization in the quartz monzonite, kaolinization being one of three distinct forms of hydrothermal alteration. Pyrite is commonly associated with molybdenum mineralization within the orebody and a pyrite halo is recognized on the south side of the orebody.

Jan 1, 1968

By F. W. Brackebusch

Paste backfill is a pumpable, flowable, non-Newtonian fluid consisting generally of mine tailings and cement. Paste is prepared from dilute slurries of tailings. This is done by dewatering the slurries with conventional thickening or filtering. Backfill with a paste consistency is prepared by mixing dewatered tailings with cement and water to obtain the desired consistency of medium slump concrete. The paste is pumped with concrete pumps over relatively long (1 km or 0.6 mile) horizontal distances. More commonly, though, it flows by gravity down a mine shaft and then horizontally to the void being filled. Alternatively, cement can be added near the end of the pipeline. A certain proportion of fine particles <20 µm (<625 mesh) must be present in pastes but particles of aggregate can be added without significantly affecting the flow characteristics. Detailed testwork is necessary to design a system to prepare and place paste backfill. Testwork must determine dewatering characteristics, strength of mixes and friction in pipelines. Plants must be well engineered and controlled with PLCs because high quality control is necessary to prevent plugged pipelines and excessive pressures. Relatively small amounts of cement (3% to 5%) produce stiff backfill material 1.5 to 3.5 MPa (217 to 507 psi). The advantages of paste backfill in a mining operation include reduced mine dewatering, labor and materials savings, reduced tailings impoundment requirements, good support properties and reduced spills underground. In certain cases where more than 30% of the weight of the ore is sold as a product, the entire tailings stream can be placed underground. Paste technology can he used for surface or underground placement of tailings.

Jan 1, 1995

By P. E. Nielsen, T. L. Loga, B. B. Mauko

A numerical model is presented which simulates the dynamic fracturing process for a circular geometry fracture in a uniform stress medium. The dependence of crack aperture and net pressure in the crack upon various dominant parameters of the fracturing process is discussed. An analysis of a 75% nitrogen foam fracture in a coal seam at 5600 feet (1707 m) is also presented. The analysis is based upon the discussed parametric trends, the job records of treatment parameters, and a Nolte plot of net downhole pressure. It is interpreted that fracturing with water, in pre-foam fracture pump tests, resulted in significant fracture height growth. However, the subsequent foam fracture had reduced height growth due to the high effective viscosity of the foam and due to the higher magnitudes of elastic modulus and stress in the bounding rock strata with respect to the coal.

Jan 1, 1986

By T. M. Campoy, J. R. Jones

When extending the life of an existing mine in Appalachia, it is common to acquire the adjacent reserves and extend the existing mine into it. The existing mine is often renovated to accommodate the new conditions. The existing mining system and the track and belt haulage systems may he modified while the new property is integrated into the old one. All of these changes create new constraints for the mine ventilation system (MVS) that require proper planning and control procedures. This paper presents a study that was carried out for the ventilation system of a newly expanded underground coal mine in the Appalachian region. The process of correcting the ventilation system of the existing mine is discussed. That is followed by a discussion of some of the stages of controlling the expanded system. Numerical data for these steps are also presented.

Jan 1, 1994

By J. Drelich, J. Pletka

Lost foam casting is a process in which a polymeric material is formed into the shape of the part to be cast. Parts that are more complex are fabricated by simply gluing several patterns together. The pattern is then coated with a refractory material consisting of a mineral mixture and binders. Finally, hot metal is poured into the pattern, evaporating the expanded polystyrene and taking the shape of the coating shell. Prior to casting, a significant number of the patterns are damaged and inevitably landfilled. In this study, a process was developed for the recovery of expanded polystyrene from the coating and glue contaminants. The process consists of shredding, impact comminution, size classification and pneumatic separation. It is successful in separating up to 97% of the contaminants, while recovering 95% of the polystyrene. Key words: Casting, Lost foam process, Expanded polystyrene recovery

Jan 1, 2003

By S. Behl

A major limitation in developing successful selective, flocculation schemes is the difficulty encountered in adsorbing the polymeric flocculant only on the desired substrate. In this paper, a correlation between selectivity of flocculant adsorption and separation efficiency is outlined, and a potential technique to achieve selective adsorption of flocculants is discussed.

Jan 1, 1994

By Y. J. Wang

The concept of subsystem characteristic curves for multiple-fan ventilation networks is presented through the construction of characteristic curves for two-fan, series-parallel networks. By considering fans as the individual network branches, the multiple-fan network is viewed as consisting of two components: any one fan branch, which is called the reference fan branch, and its associated subsystem. Thus, F subsystems can be designated for the network with F fan branches. Each subsystem contains one or more fan branches. The subsystem characteristic curve is the pressure-vs.-quantity curve of the subsystem. As illustrated in the example networks, the subsystem characteristic curve is not a strictly increasing curve and does not pass through the origin. The intersection of the characteristic curves for the subsystem and the reference fan branch represents an operating point. Multiple intersections therefore represent multiple operating points.

Jan 1, 1994

By T. W. West

INTRODUCTION This paper presents an assessment of conventional flotation technology. In addition it presents some ideas which can be used to change the perception of what may be done with conventional flotation equipment to maximize its efficiency. Perspective of Conventional Flotation Technology 1. Flotation in many coal preparation plants is defined as something between a necessary evil and a non-viable concept because: -Too much art is required on a continuous basis to achieve uniformly acceptable results. -It is expensive, the capital cost in dollars per ton of circuit feed for flotation and dewatering is high. -It is a difficult process to use when SO2 reduction governs system design and equipment selection. -It creates a product (fine coal froth) that is difficult to dewater in the presence of BTU/lb as-received pressures. -It is a difficult process to control from a management standpoint, there are no dependable set points to rely on. 2. Many froth cell circuits are 0.5m x 0 (nominal 28 M x 0) feed which is sourced from screen/cyclone underflows. The original intent was to obtain maximum yield at acceptable product quality and moisture using disc filters. (See Figure #1) 3. An alternate to conventional flotation and its perceived to be limits of efficiency, capital costs, etc. is to move towards such developing flotation technologies as column flotation, reverse flotation, and microbubbles. A lot of work is being done to move these concepts thru pilot stages into full scale, commercial plant operation. The majority of the coal producers and coal preparation plant designers view these concepts as being in the development/pilot plant stages. OBJECTIVES Based on the preceeding comments of the perspectives of the coal producers and plant designers, the options are limited. They can make do with what they have available to them in the way of industry standard equipment and practices or they can move forward with developing technology. I feel there is a third option: what can we really do today with what is available to us, without reinventing the wheel? APPROACH 1. When processing coal against ash and SO2 restrictions, the fine clean coal stream can be the best stream on the clean coal conveyor due to the release by size and the ability to create a high BTU/low sulfur (dry basis) product. 2. Targets: -Consistent raw coal size consist in the plant feed . -Do not put pyrites in the froth cells. -Adjust criteria defining good flotation away from yield towards maximum BTU recovery at minimum ash. -Limit the froth cell feed size consist to 0.15 mm x 0 (nominal 100M x 0). -Establish and maintain a correct, consistent percent solids in the froth cell feed. -Select flotation reagents with care. -Introduce reagents in the proper sequence.

Jan 1, 1988

By Steve Rule, Jose Roberto Vago, Walter de Moura

Cerro Vangaurdia Gold Mine is a joint venture between AngloGold (the operator), Perez Companc and Formicruz and is situated in the southern province of Santa Cruz, in Argentina, approximately 2,150 km south of the capital, Buenos Aires. The mine is located in a severe, semi-arid environment with very cold winters and little annual rainfall (200mm). It is an open-pit operation, mining several narrow, shallow epithermal quartz veins with . gold and silver mineralisation. Commissioning of the plant commenced in September 1998 and the first dore bar was poured towards the end of the same month. The nominal capacity of the plant is 55,000 tonnes per month, with a design capacity of 60,000 tonnes per month. Prior to finalising the design, an extensive testwork programme was undertaken at Nova Lima, in Brazil, in which all parts of the process were evaluated together on a pilot-plant scale. The process flowsheet selected at Ce1rn Vanguardia is quite novel, in that it includes milling in cyanide, as well as a cyanide recovery and recycling plant on the tailings section of the treatment plant is included. The cyanide recovery process selected was a version of the acidification - volatilization - reabsorption (AVR) process, known as Cyanisorb™. The selection of the Cyanisorb™ process in the plant design was as a direct consequence of two factors:

Jan 1, 2000

By Andreas Rubo, Stephen Gos

Over the past couple of decades several endeavours have been made to develop lixiviants with the intention of replacing cyanide in gold leaching. In 1980s these endeavours were largely economically driven, due to cyanide shortages at that time. In more recent times, the driving force has shifted to occupational health and environmental considerations. It is often argued that the high acute toxicity of cyanide alone makes it worthwhile considering to replace it completely by less toxic alternative lixiviants. This has led to having to consider more criteria in the choice of any alternative lixiviants, which have often not been taken into account in the past. The intention of this paper is to review these alternative lixiviants and also review the criteria, which have ultimately led to most of these lixiviants never having found any large scale application, if they passed laboratory stage at all. It is also intended to show, that by handling and treating cyanide in a proper manner, the overall profile for the use of cyanide compared to these alternative lixiviants is very favourable. The question to really be answered is whether there is actually any chemical or process applicable to gold leaching that does not show the high toxicity potential of cyanide and that is still favourable with regard to looking at a broader spectrum of criteria and not only acute toxicity.

Jan 1, 2000

By Brock H. Morrison

One of the major criterion of any mechanised tunnelling operation is to minimize downtime of the tunnelling machine by employing the most efficient muck handling system space and economic factors permit. A tunnelling machine which remains idle during a large percentage of the available shift working time is a luxury no contractor can afford. There are several possible reasons for non-productivity of a tunnelling machine ... the inability of the muck handling system to keep pace with the tunnelling machine on a continuous basis is one major cause. In large diameter tunnels, where several trains or more than one muck hauling unit can operate simultaneously, downtime of the tunnelling machine may be kept to an acceptable level. On small to medium diameter tunnels, 8 feet to 14 feet in diameter, the muck removal support system is normally restricted in capacity, resulting in an excessive tunnelling machine downtime as the tunnel extends from the shaft. There is a need for an efficient, continuous and economical muck removal system for small to medium size tunnels being driven by a hard rock machine. This paper is intended to provide an insite into pneumatic conveying, and explain the Radmark System; its development and utilisation in the tunnelling and mining fields. STATE OF THE ART Pneumatic conveying is the transportation of bulk materials

Jan 1, 1997

"INTRODUCTION Foam, unless intentionally created, in any industrial process presents operational problems, or at a minimum, is a nuisance. Some foam problems are unique to a given industry and others are common across many industries. A few problems foam presents to any particular industry are: (a) Poor Housekeeping, (b) Environmental impact, (c) Safety Hazards, (d) Slower Production Rates and, (e) Reduced quality of the end product. Defoamers address these issues. Sadly, the assumption in most industries is all defoamers are alike. In reality, a lot of chemistry is involved in the manufacture of even the simplest defoamer sold today and rarely are any two defoamers “just alike”. Today’s defoamers can include polymer chemistry, fatty esters, alkoxylated alcohols, silicone chemistry, silicone surfactants, ethoxylated and propoxylated block polymers, and a tremendous amount of emulsion chemistry just to name a few. This paper will discuss the various types of defoamers, defoaming mechanisms, the advantages and disadvantages of defoamer selections, and how to choose the proper defoamer for your application. Before a discussion of defoamer can be brought about, foam generation and composition must be discussed. WHAT IS FOAM? Foam is a colloidal suspension of a gas dispersed in a liquid. Most often foam consists of air dispersed in water. If a stream of air is introduced into a liquid, the bubbles produced assume a spherical shape. As the density of the bubble is less than the liquid the bubble rises. When the individual bubbles reach and pass through a surfactant free liquid they collapse. Air from the bubble dissipates and the liquid previously surrounding the bubble flows back.It should be noted a pure liquid will not foam. In the case of air dispersed in water a surfactant is necessary to make the water support a stable foam. A surfactant is a term used to describe a surface active agent; a compound with a hydrophilic end and a hydrophobic end on the same molecule."

Jan 1, 2016

By Geoff Beale

In terms of their hydrogeology, most open pit mines can be divided into three categories. There are mines that occur above the water table, mines that extend below the water table in high permeability rocks and mines that extend below the water table in low permeability, tight formations. Mines that occur above the water table do not experience major ground water seepage. It may some- times be necessary to construct in-pit trenches and sumps to remove water from precipitation. But dewatering or enhanced drainage measures are typically not required. Open pits that extend below the water table in high permeability rocks find it cost-effective to pump from dewatering wells. This is done to lower the water table below the working pit floors, creating dry or depressurized conditions in advance of mining. If the rocks in the mining area are homogenous, complete drainage of the entire mining area may be achievable by pumping from wells. In this case, it is not necessary to consider drain- age enhancement. However, there are many open pits and excava- [ ] tions that can lower the water table using conventional wells, but for which drainage enhancement is also an integral part of the dewatering system. The Sleeper Mine in Nevada is an example of this. Hydraulic layering at Sleeper has prevented downward drainage of water as the main water table is lowered. In addition, there are many mines that have areas of low permeability wall rocks that do not freely drain as the surrounding water table is lowered. Ground water seepage also creates difficulties in mines that occur below the water table but for which lowering of the water table using conventional wells is not feasible because of the overall low permeability of the rocks. The volumes of water involved may be small. However, it is necessary to deal with all of the water inside the pit as mining proceeds. It is not possible to dissipate pore pressures in the wall rocks in advance of excavation.

Jan 1, 1997

By John Keay, Douglas R. Shaw, Gregory J. Olso

Rhodes Mining NL, Perth, Australia, is developing the Lahoca Gold Project which is located in Hungary, about 30 km from the town of Eger. The preliminary resource is estimated to contain approximately 1.5 million ounces of gold. The project is being evaluated for an annual process capacity of 2 million tonnes. The test samples contain just over 2 g Ault and 6% sulfur as sulfide. Copper and arsenic levels are approximately 0.2 and 0.1 %, respectively. The ore is refractory due to submicroscopic gold occurrences and structural associations with pyrite. A small amount of the gold is finely encapsulated in quartz. Approximately 30% of the gold in the crushed ore is soluble in cyanide and up to about 55% is cyanide-recoverable with ultra­fine grinding. The ore has little preg-robbing ability. Metallurgical test work done by Colorado Minerals Research Institute (CMRI) and other investigators has shown that as much as 85 to over 90% of the gold was recovered by the relatively severe conditions of pressure oxidation or roasting of the whole ore or a flotation concentrate. The Lahoca ore responds to flotation with gold recoveries of 87% into a low grade concentrate. Subsequently, with a view toward defining a process route with potentially more attractive economics, Rhodes Mining and CMRI conducted an extensive review of biooxidation technologies and concluded that, in particular, heap biooxidation methods promised lower process costs which normally are associated with heap leaching. Based on the study, which included the analysis of the closely related practices of copper dump/heap bioleaching now well established in that industry, CMRI conducted simulated heap biooxidation experiments which evaluated factors such as ultra fine ore crushing, agglomeration techniques, heap design, forced aeration oxygen supply, and whether or not the heap is irrigated. Separate flask biooxidation tests at Little Bear Laboratories showed that the finely crushed ore is biooxidized readily, with a near linear relationship between sulfide oxidation and gold cyanide solubility. Gold recoveries of as high as 66% have resulted after biooxidation of crushed ore. This paper highlights the metallurgical developments of the Lahoca project, and focuses on recent biooxidation laboratory test work aimed at enhancing the treatment of crushed ore.

Jan 1, 1997

By William Mayrsohn

INTRODUCTION The net smelter return (NSR) calculations made on various smelter-refiner alternatives, is usually done by taking the gross metal value less metal deductions, smelter-refiner charges and transportation-insurance costs. An important further step in the calculations is the financial charges imputed by refining time, transportation delays, to the time gold is returned (if tolled) or paid for if bought by the refiner. Metal that is priced in advance of payment also requires a forward premium that the mine may or may not be getting. This is a hidden cost that is often omitted from the calculations. Segmentation of each of the above costs are vital to see where improvements can be made through negotiations, better choice of metal pricing or transportation alternatives. BASIC NSR CALCULATIONS SMELTER-REFINER CHARGES Payable Metals - Treatment Refining Charges: Since these can vary from one smelter to another, the effect of a $25 per ounce price increase/decrease should be calculated and kept in mind. This effect is compared to differences in refining/treatment charge and a total smelter/refiner cost on a cost per ounce of dore, gold, or a dry ton of concentrate. Transportation - Insurance: Research has to be done on transportation alternatives perhaps with some assistance from the smelters, railroads or trucking companies. For dore, the U.S. postal service is viable and inexpensive. For railroads, deal with the regional office ie., B&N El Paso, if production warrants regular bulk shipments. Spot rates tend to be higher. A small mine producing concentrates usually goes to the nearest smelter due to extremely high transportation costs. Here is where a refiner can help. Insurance-Quotes for rates on dore/ concentrates are easily obtainable, but the mine has to shop for the best rates. Your insurance broker is the best source of this information. Differences between Mine and Smelter/Refiners Metal losses can be caused by the following: - Concentrate dry weight differences caused by moisture determination or faulty scales (often at the mine). - Sample bias by poor preparation practices on either side ie., grinding of the sample removing gold; or a poorly mixed concentrate. Dore bullion has no such difficulties.

Jan 1, 1987