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By Terence P. Holman

Instrumented load testing of high capacity micropiles, followed by detailed analysis and numerical modeling, provided an opportunity for real foundation performance to be incorporated into the design of a complex urban high-rise structure. This paper discusses a design-based load testing program and subsequent analysis for micropiles incorporated into a piled raft foundation beneath a portion of a high-rise residential structure in Brooklyn, New York. Preliminary numerical analysis, performed using the commercial finite element package PLAXIS 3D Foundation, indicated that soil stiffening and transferring heavy core loads to greater depths was required to minimize the total and differential settlements. High capacity micropiles were modeled below the tower core mat to create a piled raft effect, reducing the settlements to acceptable levels. Final design of the foundation and micropiles, and final numerical analysis of the proposed foundation system required an instrumented load testing program to provide the Owner and design team with a level of comfort. The instrumented load test provided data on the evolution of load transfer, including the mobilization of significant tip resistance, frequently ignored in design, and micropile axial stiffness. Final numerical analysis of the foundation system involved refining the PLAXIS model based on the micropile behavior and load transfer mechanism observed during the load test program. The authors believe that the combination of design-based load testing and numerical analysis in this project yielded a more refined foundation system with realistic expectations of performance.

Jan 1, 2007

By S. F. Hillis, J. E. Rourke, K. A. Szalay, O&apos

INTRODUCTION For the past 25 years, tunnel support requirements have frequently been determined, at least in North American practice, by classifying the rock according to the system proposed by Terzaghi (1), using one or more of the 8 Rock Conditions which he defined, the rock load then being selected within the range given for each Condition. However, there is a lack of published data comparing Terzaghi loads with actual measured rock loads, and it would appear that the degree of conservatism, or otherwise, of the Terzaghi approach is very often unknown. Excavation of 4 large diameter tunnels at the Tarbela Dam Project in Pakistan afforded an opportunity to compare Terzaghi and measured loads, through instrumentation of the steel ribs installed for temporary support, and by classification of the geology exposed during the tunnelling operations. In addition, the deformation of the rock surrounding the tunnels was monitored during excavation by means of borehole extensometers installed prior to the start of tunnelling. This paper describes the tunnel instrumentation and the results obtained therefrom, and relates these results to the Terzaghi load coefficients. It also discusses the effects of the methods of excavating the tunnels on the rock loads and rock deformations. PROJECT DESCRIPTION The Tarbela Dam Project is located on the Indus River in

Jan 1, 1974

By A. W. Hann

THE importance, to geologists and metallurgists, of knowing the mineralogical forms in which the silver occurs in ores has increased during the past few years, and will continue to increase as long as working hypotheses are converted into proved theories and rule of thumb methods are supplanted by scientific data. The methods used for the determination of these silver minerals have been: (1) careful study of polished ore sections with the microscope, and more recently, (2) metallurgical separation of the ground ore by flotation, tabling and panning, supplemented by microscopic examination of these separated minerals, and chemical analyses. During the course of some experimental work carried on by the testing department of the International Smelting Co. and myself, it became important to determine, in a general way, the distribution of the silver values in the minerals, as they exist in Tintic Standard and North Lilly siliceous oxidized lead-silver ores. These mines are in the East Tintic Mining District, State of Utah. In this work the second method was used. Differential flotation tests were run, separating the sulfide from the oxidized minerals, and the products were assayed. Various concentrates were carefully panned and the separated products assayed; special samples of ore were selected and assayed. The microscope was used only for the purpose of determin; ing whether the individual minerals were in the so-called "free" state. Analysis of Tintic Ores These chemical and mineralogical determinations showed the silver to be present as native silver, argento jarosite, argentite, and combined or inherent in the tetrahedrite, chalcopyrite, galena, pyrite, cerussite, anglesite, mimetite, malachite, iron oxide and occluded in the quartz. Careful microscopic work would probably show other forms in small amounts, such as the halide silver minerals and some of the antimony sulfide combinations. The tabulation of the analyses of the various products (Table 1) shows no evidences of fixed ratios of silver to any particular base metal.

Jan 1, 1929

By J Bryant

In recent years the mining industry has suffered from skill shortages in a range of disciplines including mine geology. As a consequence, many businesses operate with incompletely filled organisation charts and technical professionals are frequently thrust into roles earlier than previous generations of geologists, engineers and metallurgists. Exacerbating the difficulties managers face with recruiting suitably experienced professionals is the churn of people through roles. Churn may be caused by internal pressures related to the rapid increase in projects and opportunities within a company or by external factors including the high workforce mobility resulting from the advent of fly-in, fly-out (FIFO). Historically, new entrants into the mine geology profession often received on-the-job training from their more experienced colleagues. This training, supplemented with targeted skills and knowledge enhancement through dedicated short courses, ensured the wide range of skills, knowledge and abilities required in the complex role of mine geology were continually renewed. Faced with an influx of new graduates and a dearth of mine geology professionals in the critical ten to 15 year experience range, the industry needs to develop new paradigms to ensure that the full business benefit of the mine geology function is delivered. This is increasingly important as the complexity of business planning built on geologically-based variables grows. Mine geologists are now faced with the potential incorporation of geometallurgy and waste characterisation along with energy efficiency, carbon-economy and other environmental issues into their roles. Providing baseline data, models, operational control and reconciliation for a wider range of variables further stretches the already limited geological resources available to the industry and exposes personnel with relatively low levels of experience to potentially business transforming decision processes. This paper outlines a successful approach to mentoring at the individual and team level. It discusses what went well and what could have been done differently from both the mentor and menteeÆs perspective with examples from case studies and offers insights into a new approach to dealing with gaps in organisation charts and high turnover of personnel.

Jan 1, 2009

By S Paciornik

The traditional trading of iron ores is based on chemical specifications and particle size distribution. However, recent characterisation studies, that bring additional information like mineralogical composition and microstructural (textural) aspects, have become important. They contribute to determination of the iron ores downstream beneficiation operations and subsequent steelmaking processing, allowing improvements on both new and existing processes. Despite progress in commercial scanning electron microscope/energy dispersive spectrometer (SEM/EDS) automatic instruments in the last decade, these systems are not capable of performing the identification and discrimination of major iron ore minerals (haematite and magnetite) and the consequent description of its microstructure. On the other hand, reflected light microscopy (RLM) can easily distinguish the iron oxides by their reflectancies, but it cannot discriminate quartz and epoxy resin, which present similar colour on images. The present work proposes an innovative method to perform a quantitative mineralogy characterisation of iron ore based on RLM-SEM co-site microscopy. This technique combines images obtained by RLM and SEM through an automatic registration procedure that accurately aligns the two kinds of images of each field. In fact, it creates multi-dimensional images, which are then analysed using image processing and pattern recognition techniques. The case study is an itabiritic iron ore from Quadrilßtero Ferrffero (Brazil) which contains mainly quartz, goethite, magnetite and haematite. The discrimination of phases that are not distinguishable with either RLM (epoxy resin and quartz) or SEM (haematite and magnetite) can be performed through this multimodal approach, allowing the subsequent mineralogical quantification. The mineralogical quantification computed by image analysis was consistent with independently obtained results based on the Rietveld technique.

Jan 1, 2008

Application of Agitated Leaching for Iron Removal from Silica Using Sulfuric and Hydrochloric Acid In this research, iron removal from silica used in glass industry was investigated using agitated leaching method. Silica sample was provided from silica concentrate originating from Chalchoog Silica Mine located in Abhar, Iran. The sample contained silica, iron oxides and clay minerals. For characterization of samples XRD and XRF analysis and atomic absorption method were applied. Silica and iron oxide (Fe2O3) grade of head sample was 98.41 per cent and 0.067 per cent respectively. Two inorganic acids (sulfuric and hydrochloric acid) were used in agitated leaching tests. Two series of L9 orthogonal array of Taguchi design with replication were used to determine the effect of parameters including acid dosage, leaching duration, ambient temperature and solid content on iron removal. The statistical calculations and analysis of variance (ANOVA) were carried out by means of DX7.0, Minitab14.0 and Winrobust1.02 softwares and also statistical calculations were checked manually using Excel software. Also multivariate regression was applied in order to forecast Fe2O3 conent of final product. The optimum conditions for leaching tests which sulfuric acid was employed are as follows: 40 minutes leaching time, temperature of 85¦C, 40 g/L acid concentration and solid content of 20 per cent. Under this condition the amount of iron oxide in silica was decreased to 0.042 per cent. The optimum conditions for leaching tests which hydrochloric acid was employed are as follows: 80 minutes leaching time, temperature of 75¦C, 30 g/L acid concentration and solid content of 20 per cent. Under this condition the amount of iron oxide in silica was decreased to 0.035 per cent.

Sep 13, 2010

By T. H. Udayashankara

Soil pollution, a very serious environmental problem, has been attracting considerable attention in recent years. It is now generally recognized that land as a component of the environment deserves the same attention and protection as water and air. This recognition has arisen perhaps because of increased incidents of land pollution, the scarcity of land, and increased awareness and concern about long-term effects of land pollution on terrestrial and aquatic eco-systems and on ground water quality. Contamination of land results from a wide range of human activities, including industrial discharge process, disposal of wastewater and agriculture. The environmental impact of exploration, production and refining of crude oil is a major concern in developed and developing countries. Because of the known adverse effects of petroleum hydrocarbons on soil ecology and fertility there has been growing interest in the development of efficient technologies for the remediation of contaminated land, with a view toward making it available for further use. Crude oil is a natural product and as such is susceptible to degradation by naturally occurring micro flora. Bioremediation has become an important method for the restoration of oil-polluted environments. A bench scale study was conducted to evaluate the bioremediation technique in treating soil contaminated with transformer oil. The steps involved in this study are: (1) Preparation of contaminated soil, (2) Extraction of PAHs and PCBs from contaminated soil, (3) Treatment of contaminated soil in slurry batch reactor, and (4) Analysis of PAHs and PCBs by gas chromatography technique. The performance of reactor was assessed by measuring parameters like COD, PAHs and PCBs. The study was con-ducted for six different pulp densities ranging from 20% to 40%. The maximum removal of PAHs and PCBs was observed for 20% pulp density.

Jan 1, 2008

By Andrew D. McCallum, Russell A. Heins

"Until the advent of intensive cyanidation, gold gravity concentrates were generally treated by tabling. The table concentrates were smelted while table middlings and tailings were recycled to the milling circuit for further grinding and subsequent leaching in the CIP/CIL circuit. Gold recovery on production tables is relatively low, often only 30 percent, and rarely above 60 percent. Significant factors in tabling performance are; mineralogy and the operator’s experience and ability. Units have been developed by Gekko Systems to treat both batch and continuous gold concentrates. Unit sizes are determined by leach kinetics and the required residence time of the concentrate in the unit.Gekko commenced the commercialisation of intensive leaching of gravity gold concentrates in 1997 with the first commercial prototype of the InLine Leach Reactor (ILR). Over 20 units are now installed worldwide with half that number on the African continent. South African mines, South Deeps (Placer Dome WAJV) and Target (AvGold) have both installed InLine Leach Reactors. Ashanti Goldfields have placed the ILR on their standard equipment list and have six operating units with a seventh on order. AngloGold installed one of the first ILR production units at Morila in Mali.Gekko Systems successfully installed an ILR1000 Batch unit at the Antapite Mine in Peru in December 2002. The unit was installed to treat gravity concentrates and to replace a shaking table. Following installation, gravity gold recovery increased from 15% to 40% of total gold. The unit was operational from start up and the first gravity batch treated achieved 98% gold recovery. The gravity concentrates also have a high silver content and 95% recoveries on silver were also achieved.Preliminary testwork identified that the concentrates required additional oxygen to achieve peak performance. As a result of optimisation work in the laboratory, leach kinetics in the ILR have been excellent with only 6 hours residence required to achieve maximum gold extraction."

Jan 1, 2003

By E. Turner

This is the 3rd Paper in a series by this author, the first two being published at the two previous International Conferences. Since the Aachen Conference, Rio Tinto has carried out an extensive benchmarking exercise to see how we are positioned with respect to other leading companies (in our sector and other sectors of major economic importance). We need to be sure that Rio Tinto is at the forefront of best practises in Sustainable Development (SD) and is using the most effective tools and methods. This paper will present key findings from this work. Rio Tinto Minerals, working as representatives of IMA-Europe was a leading contributor to the European Commission DG Enterprise Voluntary Reporting Scheme for SD Indicators in the Non-Energy Extractive Industry. In Rio Tinto Minerals we have been using these SDIs in the management of our business and the paper will report on how they contribute to the management of our business and the paper will report on how they contribute to business value in: deepening customer relationships, eco-efficiency of operations, land use planning and permitting for new and expanding facilities, community relations, policy engagement with government authorities and strengthening the bond between the company and employees. We continue to support the Voluntary SDI Reporting Scheme, considering it to be important in the expanding EU and as a model for other regions globally. For example we have ore suppliers in developing countries and we use these SDIs in assisting them to better their performance, for we have an obligation to use our influence for continuous improvement. The paper will describe this work. Over the last 12 months our company has created a new Industrial Minerals unit called Rio Tinto Minerals which brings together all the borates, talc and salt operations, R&D, marketing, sales and customer care worldwide. The paper will present also the new Sustainability Policy of Rio Tinto Minerals.

Jan 1, 2007

About 60 persons are admitted to the graduate course every year after passing the entrance examinations. The entire course of studies is free of charge and the universities provide accommodation for the students who need it. The five years of studies are divided into 10 semesters. One semester lasts 15 weeks. Automatics can be studied at three separate faculties. At the University of Mining and Metallurgy, it is offered by the Faculty of Electrical Engineering, Automatics and Electronics as well as the Faculty of Mining and Metallurgical Machines (metrology can also be studied there); at the Silesian Technical University in Gliwice, the Faculty of Mining offers the course. The educational plans and programmes comprise 3 groups of subjects: common for a given course of studies (foreign languages, political science and the basic technical knowledge) common for the speciality and subjects of diploma courses. The whole time of studies covers about 4400 hours excluding 3 periods of professional training and the physical training. The classes, laboratory classes, seminars and design classes are obligatory and the attendance is strictly checked. Students may extend their knowledge by participating and working in the Science Clubs. The students' work is checked not only during the classes but also by the examinations held at'the end of respective semesters. Those who fail the exams can repeat them only if very important reasons are presented. At the very end of the studies there is a diploma examination together with a discussion on the diploma thesis, written by the student. The successful result entitles the student to recieve the title of "magister inzynier",M.Sc. of his speciality. The graduates, after working for 2 years, can attend another course of studies lasting 2 semesters and called "Postgraduate Course", or start "Doctoral Studies" finished by the defence of a doctor's thesis. In'these cases the expenses are usually covered by the graduates' employers.

Jan 1, 1985

By C Li

Removal of gangue minerals from ilmenite concentrates can beaccomplished by relatively low temperature roasting in controlled gasatmospheres to selectively enhance the magnetic separationcharacteristics of the ilmenite. At roasting temperatures below 800¦C the magnetising reactions are often not consistent with phase equilibria considerations. Metastable phases can nucleate and control the roasting products. In weathered ilmenites the phase assemblages and microstructures in the altered ilmenite grains can influence the roasting reactions. In this paper we give an overview of the phase chemistry of chemically weathered ilmenites and of metastable phases formed by low temperature roasting. We also report the results of roast experiments conducted in a neutral gas atmosphere. Major increases in magnetic properties after short roasting times at low temperatures were obtained for a range of ilmenite concentrates. For example heating a secondary ilmenite concentrate from Western Australia for 15 minutes in nitrogen at 600¦C gave an increase in the three kilogauss magnetic fraction from three to 92 wt per cent. The solid state phase changes accompanying the inert atmosphereroasts were characterised by combining elemental analyses withquantitative phase analyses of the ilmenite concentrates and their roast products. It was found that the phase reaction that is principally responsible for the increase in the magnetic properties of weathered ilmenites involves a transformation of disordered ferrous-containing pseudorutile to an ordered ilmenite-hematite solid solution containing typically ten to 35 mole per cent of the hematite component. Examples are given of the application of the inert atmosphere roast to effect separations of ilmenite from gangue minerals.

Jan 1, 2001

By F. Weinberg

WHEN impure Zn (< 99.99 pct)&apos;&apos;Z or Zn-Cd alloys3 are progressively solidified, a cell or "corrugation" substructure4 is produced in the solid, with a high impurity or solute concentration along the cell walls. When these materials are polished and suitably etched, etch pits are often observed along the cell walls. For the Zn-Cd alloys these etch pits have been associated with decorated dislocations, present in the corrugation boundaries to accommodate the lattice strain. In the course of an investigation of Zn-2 pct Au alloy, molten metal of this alloy was poured into cold water and the resultant solid pieces were sectioned, polished and etched with a Cr0 ethant. An extremely regular cell pattern was observed on the etched surface, similar in general to the corrugation structure previously reported for impure zinc and Zn-Cd alloys. At higher magnification, regularly spaced pits were observed along the cell boundaries. An example of the regular cell pattern at the center of a specimen is shown in the center and lower portions of Fig. 1; the top of the figure shows the pattern near the specimen surface. Typical etch pits in the cell walls are shown in Fig. 2. It was surprising that a cell pattern as regular as that shown in the center of Fig. 1 was produced at the very rapid solidification rates used (estimated as > 1 cm per sec). In addition, the distribution coefficient for the Zn-Au system is greater than 1. Accordingly, the center of the cells should be rich in solute and should etch

Jan 1, 1963

By Ibrahim Yusufoglu, Ahmet Orkun Kalpakli, Cem Kahruman, Sedat Ilhan

"The effects of oxalic acid concentration, temperature, stirring rate and particle size on the dissolution rate of synthetically prepared calcium molybdate were investigated. Dissolution of calcium molybdate in oxalic acid solutions takes place as a series - parallel type reaction. In the first reaction step, which proceeds according to the ""Langmuir - Hinshelwood Mechanism"", calcium aqua oxalato molybdate is formed as a complex chelate intermediate product. In the second reaction step, molybdic acid is formed during the slow hydrolysis of calcium aqua oxalato molybdate, and it reacts rapidly with oxalic acid to form the polymeric hydrogen oxalate dimolybdate chelate as an end product. Activation energies were calculated as 41.4 and 49.9 kJ mol-1 for the first and zero order reactions. The fractional conversion versus time relationship can be given by the following equation.IntroductionMolybdenum is used widely in electric-electronic, metal working, aerospace and aeronautic, nuclear, glass and petrochemical industries because of its high melting temperature and resistance against chemical effects. However, the largest molybdenum consumers are the iron-steel and super alloy industries where molybdenum is used as an alloying element. Industrially important molybdenum minerals are limited to molybdenite (M0S2), powellite (CaMo04) and wulfenite (PbMo04), which are considered as primary molybdenum resources. Secondary molybdenum resources are spent catalysts and scrap [1-4].Molybdenum has been produced by pyrometallurgical processes in the past. Since it is possible to process low grade molybdenum ores and industrial wastes by hydrometallurgical processes, which are more environmentally friendly than pyrometallurgical processes, the importance of the use of hydrometallurgical processes has increased in the molybdenum production industry."

Jan 1, 2012

By A. H. Daane, W. J. Wunderlin, B. J. Beaudry

In an earlier study at this laboratory,&apos; the authors investigated the solid solubility of holmium in copper, silver, and gold, and also the melting point of the first eutectic on the noble-metal-rich side in these systems. In a more recent study of the solubility of rare-earth metals in gold at this laboratory. Rider, Gschneidner, and McMasters2 noted that the reported eutectic temperature in the Ho-Au system was lower than the corresponding eutectics in systems of dysprosium and erbium with gold. A redetermination of the eutectic temperature in the Ho-Au system with the same alloy used in the original study showed the eutectic temperature to be 810°C instead of 778°C as originally reported. (The eutectic temperatures in the Ho-Ag and Ho-Cu systems were also redetermined and were found to be 795" and 864°C compared to 787° and 868°C, respectively, which were reported originally.) Since this large change in eutectic temperature made the solubility data appear questionable, new alloys were prepared, heat-treated, and examined metallographically. The procedure of sample preparation and heat treatment used in the original work&apos; was followed except longer heat treatments were used ranging from 7 days at 600°C to 6 hr at 900°C. The results obtained are shown in Fig. 1. There is good agreement between the two studies in the maximum solubility of holmium in gold. Since the slope of the solvus is less pronounced in the present study, the extrapolation to 550°C shows a solubility of 1.6 wt pct Ho in gold compared with 1.0 wt pct in the original work. Since additional data were obtained and longer heat treatments were used in the present study, the larger value is believed to be more accurate. The authors wish to express their appreciation to P. Rider and K. A. Gschneidner. Jr., for bringing this discrepancy to their attention, and also to D. Thompson for assisting in the present study.

Jan 1, 1965

By Grigori I. Voiloshnikov

"The long-term studies on development of the technology for precious metals recovery using activated carbons executed by Irkutsk Research Institute of Precious and Rare Metals and Diamonds (IRGIREDMET) were finished by successful introduction of ""Carbon-In-Pulp"" process in Russia (1984).The review of some studies, accompanied by development, testing, introduction and subsequent improvement of considered technology, carried out by IRGIREDMET is submitted in this paper.The basic regularities of gold and silver adsorption onto activated carbons from cyanide, thiourea, chloride and other solutions are investigated using various phisical-and-chemical methods ( X-ray photoelectron spectroscopy, Voltammetry, X-ray microanalysis etc.). Using voltammetry it was found that gold cyanide is adsorbed onto activated carbon without chemical changes and partial reduction of gold is possible only during drying of carbon samples before analysis. Metallic gold and silver may be dissolved in boiling cyanide solution at argon atmosphere when they are in contact with activated carbon surface. Gold adsorption mechanism for activated carbons has great differences from that for the ion exchange resins. So the most probable mechanism for gold adsorption from cyanide solution is adsorption of neutral molecules Me n+[Au(CN)2-]n.X-ray quantitative microanalysis technique was developed to investigate gold adsorption kinetics onto spherical activated carbon. Gold profiles in granules of activated carbon for various adsorption conditions were tested (carbon particle size, mixing efficiency, adsorption time etc.). Mathematical methods were used to determine gold diffusion coefficient within activated carbon granule.The properties of various types domestic and foreign activated carbons were tested and the demands to activated carbons suitable for gold extraction were determined. As a result foreign and Russian activated carbons AG-90, AG-95 were recommended for use at Russian gold plants. Domestic adsorbents are cheaper in comparison with foreign activated carbons. The methods to restore carbon adsorption activity including acid treatment and thermal reactivation were tested and implemented."

Jan 1, 2003

By Robert M. Dreyer

Although lateritic ore deposits are relatively flat-lying, surficial ore bodies, the evaluation of lateritic bauxite and nickel deposits is among the most difficult problems confronting an economic geologist. Laterite is a soil formed under tropical conditions resulting in the concentration, within the soil zone, of certain trivalent metals-principally iron and aluminum, but also, locally, nickel and manganese. The soil zone is divided into two parts: (a) the true soil or lateritic zone and (b) the zone of partially altered bed rock or saprolite. Whereas bauxite generally is confined to the lateritic zone, some nickel deposits occur in both the laterite and saprolite zones. The evaluation of bauxite and lateritic nickel deposits thus has both similarities and differences. These ores have been formed by supergene, soil-forming solutions moving downward through zones of widely varying permeability within the weathering rock. Because the permeability varies widely, both vertically and laterally, the extent of weathering may vary greatly within short distances. Because the weathering process varies widely, the degree of metal concentration may also vary widely. It is not at all uncommon for a laterite to change, within a few centimeters, from a virtually valueless rock to a high grade ore. Moreover, the depth of weathering, and hence the depth and form of the ore profile, vary greatly. Obviously, for this type of deposit, a few grab samples or a few drill holes are virtually worthless. The evaluation of such a deposit requires a sophisticated statistical study based on thousands of carefully selected samples. As a rule of thumb, the cost of evaluating a large bauxite or lateritic nickel deposit will be about one cent per ton of ore in the ground. Thus, the cost of evaluating a several hundred million ton deposit may be considerable.

Jan 8, 1978

By D. E. Piggott, B. E. Hartmann

The thought of constructing an intake shaft five miles from the shore and 142 feet below the surface of Lake Huron from the bottom up sounds like a questionable venture. Why would one want to raise a shaft from the bottom at the end of a 16 foot diameter, six mile long tunnel to within six feet of the bottom of Lake Huron? The answer lies in the fact that Lake Huron is seldom a tranquil lake. The construction period and workable days from the surface are limited. Two previous attempts to construct this intake shaft by conventional means had been thwarted by lake storms. These approaches were circular sheet-piling cofferdams with the intention of sinking a 30 foot OD, five foot wall thickness concrete casing in the center. However lake storms, particularly in the months of November and December, proved disasterous. The last attempt was halted in December 1970 when three of the seven circular cofferdams on the north side were destroyed by pounding waves. Then, due to the nature of the technical difficulties and limited construction schedule time, it seemed desirable to devise a way in which construction could proceed without being too lake-sensitive. Obviously, if men could work from the tunnel and proceed upward toward the bottom of the lake, not having to worry about the soil collapsing and bringing the lake in on their heads, the construction would be unimpeded by adverse weather. The answer to this, however, required techniques beyond the ordinary. Approximately two years previous to the start of this shaft, nine shafts had been efficiently constructed on the same project site

Jan 1, 1974

By N. J. Alderman, D. J. Clowes, N. I. Heywood

The effects were studied of the presence of comminuted flint on the rheological characteristics of chalk slurry pumped through a 92-km long pipeline from Kensworth Quarry to Rugby Cement Works in the UK, and their impact on the pipe flow conditions. Flow curves were measured for 63different chalk slurry samples; these were described by the Bingham plastic model. In addition to observing trends in the yield stress parameter and plastic viscosity in the model with variations in both flint concentration and dispersant additive, use was also made of slurry viscosity values at a reference shear rate of 60 s-1for the pipe flow. It was found that chalk slurry viscosity decreases with increasing flint content up to 10% by weight for a given additive concentration, and increases with increasing additive concentration from 0.7 to 1.0%, for a given flint content. The pipeline flow regimes were identified using the critical value of the Bingham Reynolds number for laminar flow breakdown. For Bench 11 (quarry bottom) chalk slurries, it was observed that all sections of the pipeline operate in the turbulent flow regime for the nine different formulations and for the three pipe diameters used along the pipeline. However, this was not always the case for Bench 1(quarry top) slurries. It was therefore recommended that chalk slurries prepared from Bench 1 should not be used because of the strong likelihood that laminar flow conditions will occur owing to the presence of higher clay concentrations within this bench. This, in turn, will lead to an unsafe operation of the pipeline because of the potential for coarse particle settling. Likewise, blending of chalk from Bench 1 with the lower benches such as Bench 11 could be problematic and this requires further experimentation.

Jan 1, 2007

By D. Bastin, J. Frenay, J. Dassas

"The Luiswishi deposit belongs to the Cu-Co deposits of the Southern Group of the Katangian Copper Belt and is operated by a joint venture between EGMF (Entreprises Générales Malta Forrest) and Gecamines (Générale des Carrières et des Mines). The Cu-Co ore is beneficiated by the sulphidization process at the NCK (New Concentrator of Kipushi) at Kipushi.Sulphidization followed by flotation with sulphydryl collectors is a common practice for the treatment of oxidized base metals ores. This process is complex and its application at the industrial scale is quite sensitive. In Central Africa it is also a cost intensive treatment as the sulphidizing agent has to be imported. In order to improve the metallurgical performances and to optimise the economics of the process, a laboratory research program was carried out by the Laboratory of Metallurgy and Mineral Processing (MTM) of the University of Liège in close collaboration with EGMF and Gecamines. This program included the study of various flotation reagents as dispersing, depressing and activating agents.This paper presents the results obtained with the use of ammonium sulphate as activator of the sulphidized xanthate flotation. Although ammonium sulphate has been mentioned in the literature as a promoting agent of the sulphidized xanthate flotation of malachite, its effects on the flotation of cobalt oxides was not known.The testworks were carried out on various oxidized siliceous ore types from the Luiswishi deposit. A 1.7 l Agitair laboratory flotation cell was used. NaHS and potassium amylxanthate were respectively choosen as sulphidizer and collector. A mixture of gasoil and tall oil (90/10) was used as secondary collector. A multistage sulphidization was realised. Values of pH were followed during the different tests and an ion selective electrode Ag/Ag2S was used to control the Es potentiel evolution during the stepwise addition of the sulphidizer."

Jan 1, 2003

By J. C. Platt

1 desire to call the attention of the Institute to what is believed to be a new improvement in &apos;the construction of journal-bearings, having for its object the reduction of original cost as well as cost of renewals. In an ordinary railroad car we find the space between the top of the axle and the top of the box is filled with a "brass," weighing from seven to ten pounds. Of this amount of metal a comparatively small portion is subjected to the wear which it is intended to meet. The balance is, practically, a filling material, which from habit has long been constructed of the same metal. The Defreest bearing is made of three parts, namely, a malleableiron back, a bronze bearing-piece, and between them a filling-piece of sheet lead. The bronze takes the wear of the axle, the iron fills up the space and acts as a backing to the bronze, and the lead, being soft, adapts itself to the inequalities in the surfaces of the iron and bronze castings, thus insuring a uniform bearing on all points, and making it unnecessary to bore out the iron or turn off the bronze to bring them to a perfect contact at all points. These three park are joined together by two soft brass rivets, with counter-sunk heads, to prevent separation in handling. A groove is cast in the iron, and a corresponding rib on the bronze, to prevent the latter from turning with the axle when in place. In renewals it is ordinarily necessary simply to drive out the rivets and renew the bronze and lead. The iron part is not subjected to much wear and should last for years. It is evident that the first cost of these journals, and also the cost of renewals, must be much less than the old form. This difference amounts, at the present price of materials, to $9.60 for an eightwheel car, in first cost, and $4.72 for renewals. These bearings have been in use, and found to do what is claimed for them.

Jan 1, 1880