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By D. J. Archambeault, A. Saigal

Substantial cost savings have been demonstrated by material design changes after initial product development. As more information about a product's operating environment becomes available to a designer, it is possible to consider a more costeffective material that still meets or exceeds the design intent, such as minimum low cycle fatigue life. This is especially true in the aircraft engine industry, where precise operating cycle data is not available until after the first engine is built and tested. A methodology for predicting estimated low cycle fatigue life has been developed to investigate potential material change candidates for an aft cooling plate. A twodimensional macromechanical finite element model (FEM) has been developed using ANSYS and used to determine the effects of varying material properties. It is shown that slight changes in density, coefficient of thermal expansion and modulus of elasticity have profound effects on component and effective stresses, and therefore, estimated low cycle fatigue (ELCF) life. Aerospace

Jan 1, 2006

By R. A. Elliott

This paper describes the development of an infra-red ore dryer at the Mines Branch. The dryer utilizes an infra-red heat source mounted over a stainless-steel belt to dry ores and concentrates of varying particle size and moisture content. It has been found to ?be successful in meeting Mines Branch requirements of minimum dusting loss and ease of cleaning to decrease ,contamination between various batches of dried products. It is described with the hope that it might .prove useful in other laboratories where there are similar problems. It might have an application in the drying of concentrates containing high values where dust losses would result in a considerable loss of revenue; also for small batches of material or an intermittent drying problem.

Jan 1, 1958

By A. R. Kinkel JR.

"The Buffalo Ankerite mine is in the southern part of the Porcupine gold district of northern Ontario. The mine has a history of exploration and development reaching back to 1911, and has been operated continuously since 1932. From 1932 to 1942 a total of 510,874 oz. gold was produced from the mine. In 1941 the production was 71,654 oz. from 448,621 tons of ore.With few exceptions, the ore-bearing veins did not crop out. They were discovered during the prospecting of the prominent outcrops of barren or low-grade quartz-carbonate breccia near the veins.GEOLOGICAL SETTINGThe Porcupine gold district lies in an area of folded and sheared Precambrian lavas, sediments, and intrusives. The Buffalo Ankerite mine is in the southern part of a large fold. The structure appears to be a continuation of the Vipond cross anticline and accompanying syncline described in earlier papers (1, 2). The orebodies lie along both flanks of the synclinal part of the fold, and are known as the north and south vein systems, respectively. No mineable veins have been found on the axis of the syncline (Fig. 1).The rocks found in the mine area are pillow lava, dacite, conglomerate, quartz porphyry, tuff, and fragmental lava. The tuff and fragmental lava are now largely altered to chlorite schist. Productive veins have been found only in pillow lava, dacite, and conglomerate, but a minor amount of gold occurs in some of the quartz porphyry. The Porcupine Creek fault, a zone of intense shearing over 1,000 feet in width, lies immediately south of the mine. A spur fault branches to the northwest from the Porcupine Creek fault, separating the north from the south vein systems ( Fig. 1) ."

Jan 1, 1954

By A. Burduk

The traditional approach to managing information flow between a mine underground and overground, applied in copper mines of KGHM Polska Miedz S.A., is mostly based on exchanging spoken information using the mine telephone network and printed documentation. This way of information flow significantly influences effective use of time of a shift foreman employed at a mining division. In order to minimise multiplication of significant information generated as paper documentation, a concept of an IT system module to input basic data concerning operation of the mining division was developed. The idea is based on computer software that permits inputting data in the underground and their immediate sending to the overground. The above-mentioned solution will permit significant reduction of administrative work time that each foreman has to do on each shift. The time saved on filling forms and communication will permit the foreman and the other workers involved in information flow to spend more time for execution of their basic duties. In the case of the supervision employees working in the overground, the IT system will allow all the interested persons to be informed directly, with no necessity to transfer the information on the situation in the given mining division by turns from one to another. On the other hand, saving time on administrative works will permit the foreman employed in the underground executing more detailed inspection of workplaces in his subordinate mine division. Thus, availability of the foreman for the mining division operation will be improved. KEYWORDS

Aug 1, 2013

By G. W. Brooks

This short article is quite different to the general run of papers that are presented to the Institute, but no apology is offered because I consider that first-aid and mine-rescue work are of equal importance to many other subjects that are dealt with in our Transactions. Members of the Institute should be as much interested in the safety of persons engaged in the mining industry as they are in the practical methods of modern mining. We must not only do our best to conserve life and property by adopting every known device to that end, but we must also prepare ourselves so that we may take prompt and effective action when life is in danger, or when property is subject to loss. The need for such preparation in Alberta is perhaps greater than in most places where mining is carried on, and we must spare no effort to assemble at every mine men who are well trained in first-aid and mine-rescue work. The large area over which the mines are distributed renders central training stations out of the question, hence the need for local rescue-teams. Hospitals with skilled staffs, close enough to the mines to be convenient, also seem to be out of the question; therefore the greater need of a high standard of first-aid training for the people in our mining camps. The Government mine-rescue cars are supplied with the equipment necessary for training persons in this essential work and also for dealing with disasters should they occur. The question then arises: are there a sufficient number of men who are trained ? If so we can rest assured that what is possible to be done will be done. But if a sufficient number of trained men are not available much loss of life and damage to property is likely to result.

Jan 1, 1925

By Brian Lewis

"IntroductionThe ion exchange process is classed as a purification and concentration stage. In the uranium industry it is used to separate, and recover uranium, from a solution produced in the leach and subsequent solid washing circuit, that contains uranium as well as some impurities. The final product from this circuit is a solution, containing uranium at a 15 to 25 fold increase in concentration, with a chemical composition suitable for the ""Precipitation"" circuit.The process is a reversible chemical ""ION"" exchange, between a solution, and solid phase, with the ""resin"" being the solid phase. Various chemical changes in the solution phase will permit the resin to remove uranium from a solution or have the uranium removed from the resin back into a solution phase. The former loads uranium onto the resin, and is called the ""adsorption cycle"", and the removal or stripping is known as the ""elution cycle"".Ion Exchange resin is a semi-rigid polystyrene spherical bead, approximately 10 to 30 mesh. It is used by placing the resin in a vessel, so that a porous bed of resin is formed, through which the solution may flow.There are many different types of vessels, and systems used to hold the resin, but it is not the intention of this chapter to describe them all, but to describe two methods used in Elliot Lake. These are the ""fixed bed"", and ""moving bed"" systems, the condition of the bed during normal operation signifies the name of the system.Chemical and Physical Characteristicslon Exchange ResinThe resin used is a strange base Anionic resin, semi-rigid, and spherical in shape. The size of the wet resin is approximately 9007o between 20 and 40 mesh. Physically the beads of resin are broken early, but some have lasted over 15 years and are still in use."

Jan 1, 1989

By Chris J. Pritchard

Pumpable, two-component resins for anchoring rock bolts provides significant advantages over traditional cartridge resin and cement grout systems where fast and easily adaptable support is required for difficult ground conditions. Cartridge resin anchoring with rock bolts is often ineffective in oversized, fractured and washed-out holes. Cement grouting of cable bolts is frequently plagued with QA and QC issues related to the grouting process. Installation of cable bolts with resin injection techniques is routinely completed in cycle allowing blasting immediately after cable bolting. Xstrata Nickel has evaluated the Minova Resin Injection System since 2007. The Nickel Rim Mine and partner Minova have tested and validated the Resin Injection process for bolting procedures including Hollow Fiberglass Bolts, Rebar, Modified Cone Bolts and Cable Bolts. The resin injection process is adaptable to most bolting processes and equipment. Currently, Nickel Rim Mine use 2 resin injection products with different set times to grout deep cable bolts and development support in highly variable ground conditions. The product predictability and adaptability in application along with a high crew acceptance continues to make this support process part of an adaptable ground support system. Product consistency and quality significantly reduce the quality control concerns for ground support in highly variable ground conditions.

May 1, 2011

By Paul E. Mather, Matthew J. M. Krane

Anode or fire refining is the final pyrometallurgical step in the production of copper anode. Part of this process purifies liquid copper by reducing its dissolved oxygen with a natural gas-steam mixture. Until now there have been no transient models of this process coupling the injected gas jet mass transport with its chemical reactions. A transient, 1D flow, chemical reaction model was made to estimate the time-dependent behavior of anode copper composition, soot formation, and the transient gas jet composition along its height. Model estimates were made for reduction rate, soot emission rate, and exergy loss and destruction distributions for two melt temperatures and a range of steam addition rates. It was found that increases to melt temperature and steam addition rate increased reduction rate and decreased soot emission, while having little effect on exergetic performance. Estimates for reduction histories were compared to industrial data. INTRODUCTION Anode/fire refining is the final pyrometallurgical step in the production of copper anodes; it is essential for removing dissolved gases which cause porosity in cast anodes. Despite its significance, the open literature appears devoid of any transient models of the entire process; furthermore, there are very little published process data with which to validate any models made. This dual dearth of modelling work and process data inhibits studies of the tradeoffs between process and performance changes, desirable for decreasing reduction time and soot formation as well as quantifying changes in the exergy losses and destructions of the process. This work introduces a reduced-order, transient model of reduction during fire refining, examines performance trends with operating conditions, and compares model estimates with industrial data. Overview of anode refining The purpose of anode refining is to produce liquid copper which can be cast with minimal gas porosity, which disrupts the downstream electrorefining process. Dissolved sulfur is removed first, then oxygen, by reactions with different injected gases. The removal of oxygen (the reduction step) is the subject of this proceeding and is effected by the bubbling of natural gas, typically mixed with steam, through the melt from tuyeres. A typical refining run reduces dissolved oxygen from 3000 ppm to 300 ppm in 2–3 hours (Schlesinger, King, Sole, & Davenport, 2011). The refined copper is then cast as anodes. Figure 1 shows a schematic of the furnace vessel.

Jan 1, 2019

By Y. M. Shneerson, I. V. Fomenko, M. A. Pleshkov, E. A. Ospanov, A. A. Shakhalov, S. S. Naboychenko

Low-grade copper concentrates (with copper content less than 20%) often contain impurities such as arsenic, zinc, lead, mercury, antimony and bismuth. The pyrometallurgical treatment of such concentrates is associated with several problems, which will ultimately affect the cost and the quality of copper cathodes as well as by-products. SRC Hydrometallurgy proposed a complex hydrometallurgical technology which allows the removal of impurities and the enrichment of low-grade copper concentrates to a quality which will be more suitable for pyrometallurgical processing. Laboratory batch tests and pilot plant results for the pressure leaching steps are shown in this paper. The key parameters of the leaching steps were determined and optimized. The quality of possible by-products were also determined. The developed flowsheet includes two pressure leaching steps: pressure oxidation (POX) and hydrothermal alteration (HTA). Both operations are carried out at 170°C with subsequent flotation of POX and HTA residues and recovery of copper, zinc and lead into separate concentrates for further processing. The development of the flowsheet was based on the Balkhash Zinc Plant (Balkhash, Kazakhstan), which had been non-operational since 2009. The developed flowsheet for processing of low-grade concentrates will utilize 80% of the existing equipment of the Balkhash Zinc Plant, thus leading to a significant reduction in required capital expenditure. INTRODUCTION As the age of copper mining operations advance, copper grades continue to diminish and impurity levels increase. Therefore, copper producers are forced to look for new innovative hydrometallurgical technologies which are able to handle low-grade raw materials and solve problems associated with impurities in an economically justifiable way. New technologies allow to extract valuable components selectively and to process low-grade concentrates which had previously been marked as non-technological and economically unviable. Hydrometallurgical technologies for processing of copper-containing materials can be divided into two main categories: chloride and sulfate (atmospheric, autoclave and bacterial) based technologies. Since the 1970s, many autoclave techniques for the processing of copper-containing materials have been developed and implemented (Naboichenko, 2002; Dreisinger, 2005; Habashi, 2009; Shneerson, 2011). The mineralogical composition of the ore (or concentrates), geographical location of the deposit, distance from industrial areas, availability of existing treatment facilities, availability of skilled labor, cost of electricity and cost of neutralization are some of the factors which are usually considered when the appropriate technology is selected (Halbe, 2002).

Jan 1, 2019

By P. Taskinen, A. Jokilaakso

The Flash Smelting Process for copper and nickel production has been one of the most successful new metallurgical process developments in the 20th century. The experimental data from laboratory scale investigations of studies has produced information and insight into the reaction mechanisms and kinetics of the flash reactions of copper concentrates. Advanced computer models coupling chemical reactions with a Computational Fluid Dynamics (CFD) software became possible with the development of commercial CFD software together with increased computing power. Currently, there are both experimental and CFD modelling, including also CFD–DEM coupling (Discrete Element Method), studies ongoing for investigating the kinetics of matte – slag reactions in the flash smelting furnace (FSF) settler. The ultimate goal of the modelling work is to develop a comprehensive FSF model for studying the behavior of changing raw materials, both primary and secondary, and distribution of their elements between the matte, slag, and gas phases. The use of User-Defined-Functions (UDF) is one way to digitalize metallurgical knowledge and experimental information to be used for supporting process experts and development of artificial intelligence applications in metallurgy. In this paper, a review of the development of the FSF reaction shaft modelling and experimental investigations, and the current work for the settler reactions’ experiments and modelling are presented. INTRODUCTION The Outotec Flash Smelting process (Bryk, Ryselin, Honkasalo, & Malmström 1958) has been used in the copper and nickel industry for 70 years with continuous support from experimental investigations by many research groups in academia, among others Jorgensen and Segnit (1977); Jokilaakso, Suominen, Taskinen and Lilius (1991), Chaubal and Sohn (1986), Kim and Themelis (1986), and in industry Mäkinen and Jåfs (1982); Kojo, Lahtinen and Miettinen (2009); Tuominen, Pienimäki and Fagerlund (2016). It has been developed also for pyrite and lead smelting (Asteljoki, Sulanto & Talonen, 1984). A schematic illustration of the FSF and other main parts of the process is depicted in Figure 1. Also, two and three dimensional physical water or gas models have extensively been used in product and process development (Lilja & Rajainmäki 1995). During the recent decades, computer based models have increasingly been adopted in the FSF research and development (Ahokainen & Jokilaakso, 1998); Ahokainen, Jokilaakso, Taskinen & Kytö, 2006; Hahn & Sohn, 1990; Jorgensen & Elliot, 1992; Zhou, Zhou, Chen & Mao, 2014; White, Haywood, Ranasinghe & Chen, 2015) to name a few, but also in supporting engineering and sales of the technology (Miettinen 2017). Even though the reactions of the sulfidic concentrate particles have been included in the reaction shaft modelling, the complete FSF model with both gas-solid/drop and molten slag/matte drop has so far been and still is too demanding for today’s computer hardware.

Jan 1, 2019

By H. Helmstaedt, P. Thurston, R. Harrap

"Evolution of the continental lithosphere over Earth’s 4.6 billion year history is one of the fundamental questions of geoscience. Much of the Earth’s present-day continental crust formed during the first 2 billion years, the Archean eon, of the planet’s lifetime and thus, Archean processes of lithospheric formation must be studied in order to address this question. Until recently, the processes of Archean lithospheric evolution were thought to be fundamentally different from present-day plate tectonic processes. However, subsequent evidence suggests that the growth of Archean continents may be explained in terms of modern tectonic accretionary tectonics similar to those presently operating in the southwest Pacific region. The evidence supporting this hypothesis was compiled largely by Canadian geoscientists working in the Superior Province of the Canadian Shield in northwestern Ontario, over the past 15 years. Study of Archean rocks is also economically important because the Archean rocks of the world, although comprising only a relatively small fraction of the exposed continental crust, contain much of the world’s mineral wealth, including more than half of the world’s gold, as well as significant base metal reserves. Furthermore, the vast majority of primary economic diamond deposits are derived from the lithospheric roots beneath Archean cratons.The LITHOPROBE Western Superior Transect is located within the western part of the Superior Province in northwestern Ontario (Fig. 1). The Superior Province is the largest and best exposed Archean crustal block in the world and forms the nucleus of the North American continent. The internal structure of the Superior Province records a history of the processes that formed the earliest lithospheric elements of the Earth into cratons, thus providing an ideal laboratory for investigating early crustal evolution. The Western Superior Province is characterized by a regional pattern of alternating, 100 km to 200 km wide geological belts (Fig. 2). The observed geologic relationships between and within these subprovinces have been explained in terms of a modern tectonic model of terrane accretion. Oceanic floor, volcanic island arcs, oceanic sediments and continental fragments were accreted successively from north to south against the southern margin of a cratonic nucleus (North Caribou terrane, Fig. 2) which grew steadily in size with the arrival of new terranes through geologic time. If this model is correct, it suggests that the tectonic processes operating today have been active without major variation over the past 3 billion years."

Jan 1, 1998

By Burden of Occupational Cancer in Canada Project Team, Demers P. A., Kim J., Arrandale V. H., Jardine K.

"In 2012 diesel engine exhaust (DEE) was classified as a human carcinogen by the International Agency for Research on Cancer (IARC) and is one of the most common workplace carcinogens internationally. We estimate that approximately 2.4% of lung cancers (n=560) and a suspected 2.7% of bladder cancers (n=200) are attributable to occupational exposure to DEE annually in Canada. High levels of exposure to DEE in mining results in a disproportionate number of cancers in this sector (approximately 220 lung and 20 suspected bladder cancers annually). These could be prevented by reducing the number of workers exposed and level of exposure. KEYWORDS Bladder cancer, Diesel engine exhaust, Economic burden, Lung cancer, Mining, Occupational cancer, Prevention, Regulation INTRODUCTION Diesel engine exhaust is a complex mixture of gases and particulates containing known and suspected carcinogens such as benzene, polycyclic aromatic hydrocarbons (PAHs), and metals. Approximately 900,000 Canadians are exposed to diesel engine exhaust at work, making it the most prevalent occupational lung carcinogen in Canada (CAREX Canada). Diesel engine exhaust is recognized as one of the most common workplace carcinogens in the world, but its classification as a human carcinogen by the International Agency for Research on Cancer (IARC) was relatively recent. In 2012, after decades of mounting evidence, diesel engine exhaust was upgraded from a probable (IARC Group 2A) to a definite human carcinogen (IARC Group 1) (IARC, 2014). The IARC evaluation was based on strong evidence in humans for an increased risk of lung cancer, as well as strong evidence in animal studies. The key human evidence considered by IARC was from epidemiologic studies of workers in truck transportation, rail transportation, and mining industries, where the use of diesel engines is widespread. These studies provided strong sufficient evidence for an increased risk of lung cancer, as well as limited evidence for bladder cancer. The human studies used particulate matter, generally measured as elemental carbon (EC) or total carbon, as a surrogate for diesel engine exhaust to assess the risk associated with level of exposure. The animal studies reviewed by IARC showed sufficient evidence for cancer with exposure to whole diesel exhaust and the particulate matter fraction of diesel exhaust, but not for the gas phase components."

Jan 1, 2019

By T. G. Joseph

The strain softening relationship developed in part 1 is now applied to coal. Having determined the post-failure stress-strain curve for coal specimens, this information can then be used in a finite element program, such as Phase 2, to examine the post failure characteristics of coal pillars. Using example data, the strength of coal pillars of different width/height ratios are estimated and compared with well-known empirical pillar size-strength relationships. In addition, the post-failure stress-strain behaviour of a coal pillar is compared with an empirical relationship reported in the literature.

May 1, 2002

By J. Mullins

Coal was first banked by the Dominion Coal Company, Limited, in 1898, near No. 2 Colliery, the same site as is presently used for that purpose. Though today there are banks at Glace Bay, Sydney, and Sydney Mines, these notes, except when otherwise desirable, will be confined to describing the practice as developed at the No. 2 Banking Station, Glace Bay, as being typical of methods obtaining at all sites. Storing The manner in which the coal was piled is illustrated diagrammatically in the accompanying sketch. A train of coal was brought on the main trestle, which extended the full length of the banking ground at a height of 22 to 39 feet above the natural surface, and dumped into bins which were integral with the trestle work. Chutes from these bins permitted the coal to be fed into 3-ton cars, which were horse drawn laterally on narrow gauge tracks laid about 10 ft. centres, to a maximum distance of 400ft. from the trestle. These cars were end-dump and as the pile extended laterally the narrow gauge tracks were lengthened by shorter or longer filling pieces, so that their ends were always kept at the brow of the bank. Much coal, however, had to be dumped directly on the tracks and hand trimmed to fill the valleys, and level off, between the tracks.

Jan 1, 1931

By Bryan Tisch

Goal of GMGE ??To advance mine reclamation through the beneficial use of organic residuals for the sustainable establishment of bioenergy crops and other productive land uses Objectives ??To advance the current ?standard? of mine reclamation by demonstrating that mining lands can safely become agriculturally ?productive? through the use of organic residuals. ??To generate and compile sound scientific data that can be utilized by stakeholders to better assess the environmental impacts of utilizing these materials. ??To complete a manual of best practices regarding the utilization of organic residuals on mine lands. *Considerable effort to be placed on operations/implementation side of utilizing residuals ?rather than just pure research

May 1, 2011

By Andrew D. Lapworth

The use of geological and grade models has been standard practice in mine design for many years now, with a wide range of software available to create and analyze the models. Although geotechnical parameters are also of vital importance for mine planning, there has been very little in the way of commercially available systems for integrating geotechnical data into the mine planning and design process. Sirovision is a new technology based on digital photography for automated, safe and accurate 3D mapping of geological and geotechnical features in rock faces. Datamine has integrated this capability into its product range so that Sirovision becomes an integral part of day-to-day face mapping, mine geology and geological / geotechnical modeling in both open pit and underground mines. This results in improved fragmentation for loading, hauling and processing, and for open pits local geotechnical conditions can be taken into account to improve slope design and control. This paper describes some of the ways that geotechnical modeling can be used to create more refined and cost effective mine designs and then discusses the role of Sirovision in enabling the raw data required for such modeling to be collected quickly, safely and reliably.

May 1, 2007

By Sina Mostaghel, M. Guo, E. Klaffenbach

The current paper is focused on evaluating the behavior of copper in a copper production slag and the assessment of metal recovery possibilities. For this reason, thermodynamic calculations were carried out to determine the influence of parameters such as slag composition, temperature and oxygen partial pressure on recovery of non-ferrous elements. It was found that the formation of a solid face centered cubic (fcc) phase, mainly consisting of iron, limits the extent of reduction that can be achieved for an industrial process. However, it could be discovered that solubility of iron in the Cu-rich liquid alloy strongly depends on presence of other elements, particularly arsenic. As part of the results of this study, the solubility of Cu in the slag at onset of fcc phase formation is presented as function of temperature, oxygen partial pressure and concentration of MgO and CaO. It was concluded that lower temperature (1200°C) and higher CaO addition (16 mass-% in this study), would result in the highest achievable copper recovery from slag. INTRODUCTION Copper slag is produced as a by-product of the copper production process. The slag is still containing a high amount of copper and other valuable metals. This demands further treatment of the slag as a secondary source of metals. In addition, the physical/mechanical properties of slag allow its use in several applications such as hydraulic engineering, civil engineering, as an abrasive and many more. These applications help reducing the use of natural resources like rock and sand. By decreasing the content of heavy metals such as Cu, Pb, Zn and As in the slag, its application in abovementioned fields becomes more attractive as the probability of releasing these elements to the environment is further reduced. To develop a pyrometallurgical slag reduction process, it is necessary to understand what describes the end point of the reduction. This point is expected at maximum copper recovery without facing operational challenges. Existing literature provide some information on the effect of different parameters such as temperature or concentration of different slag formers, on solubility of copper and heavy metals in different phases. However, due to complexity of industrial slags, equilibrium experiments and accurate thermodynamic modelling are essential to be able to reliably predict the behavior of different elements in the system and determine the end-point of reduction.

Jan 1, 2019

By Felix D. Klebe

Efficient, high volume, mine load out operations have evolved in recent years to include more sophisticated control systems that integrate with mission critical equipment such as weighing systems. Traditional weighing systems often involve static weighment of individual railcars and either manual or serial transmission of scale data to a database application. In recent years integration of railcar or truck weight data into a loadout operation via direct PLC or Ethernet communication between the weighing terminal and the loadout control system has been realized. Furthermore, use of dynamic railcar weighing where railcars are automatically weighed while moving has increased productivity in a variety of mining applications.

May 1, 2008

By Paul Graham

Presentation Focus ? What is LTUG / What do we do? ? History of LTUG ? Examples of Benefits from LTUG Participation ? Encourage Participation What is LTUG? ? An informal gathering of surface mining companies to discuss and work issues of common interest and to share information and best practices around large tires.

May 1, 2008

By S. Eckert, M. Reuter, O. Keplinger, D. Obiso, N. Shevchenko, M. Akashi

We report on laboratory experiments focusing on bubbling phenomena arising from gas injection through a top submerged lance (TSL) in a liquid metal layer. The objective of this study is to reveal the characteristics of the formation and behaviour of the particular bubbles at different gas flow rates and submergence depths of lance. Visualization was performed in the eutectic alloy GaInSn using X-ray radiography. Argon bubbles were injected through the injection positions at three different submergence depths. Essential parameters such as the bubble size, bubble shape, detachment frequency and the two- dimensional gas distribution in the flat vessel were obtained by image processing. The results show that the deep position of the submerged lance causes an asymmetric large-scale circulation inside the fluid vessel. Bubble detachment frequencies were calculated by Fast Fourier Transformation from fluctuations of the image intensity in the vicinity of the nozzle injection point. This frequency does not show strong variations with respect to changes of the gas flow rate and the submergence depth of the nozzle. An increasing gas flow rate results in an increasing two-dimensional projected bubble area and the occurrence of a significant number of small bubbles being trapped by the strong fluid flow in the liquid metal layer. INTRODUCTION The Top Submerged Lance (TSL) process has been an essential component of the metallurgical industry since the emergence of first concepts about 50 years ago (Floyd, 2005). The process, which is characterized by blowing reactive gas through the submerged lance into a liquid bath, was developed mainly for improving the tin smelting process and has been applied for waste treatment or the production of several metals such as copper, lead, nickel and zinc. The productivity of the reactor is determined mainly by the efficiency of the chemical reaction between the gas or solid particles and the liquid. To achieve a high efficiency requires good exchange between the gas-liquid phase and therefore a large interface area. The efficiency changes greatly with the number and size of bubbles injected from the nozzle and the extent of splashing on the free surface. The degree of turbulence in the bath plays a decisive role here. For the reason, the design of an efficient TSL process requires a profound knowledge of the fluid dynamics especially for complex multiphase flows.

Jan 1, 2019