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By S. Burling

Australia has a number of uranium deposits, but they vary significantly in their mineralogy, grade and textural characteristics. Therefore, information from traditional (or conventional) sources regarding the fundamentals of leaching the uranium and gangue minerals is not always applicable when studying particular ores. Empirical studies on particular ores can be effective in understanding leach systems and can lead to improvements in process design, but there remains a lack of fundamental understanding which is necessary for ongoing process optimisation as ore bodies continue to vary. ANSTO Minerals has undertaken a program of work to address some of the fundamental questions of uranium leaching, including the unexpected impact for some ore types of leaching at high oxidation potential.

Aug 1, 2010

By B. Szpunar

Structural and mechanical changes of urania are investigated when oxidized to U3O8. The CASTEP ab-initio quantum mechanical program, employing density functional theory is used. The total energy technique is implemented to investigate changes in the lattice constants. The ab-initio calculations predict a 36% increase in the volume per uranium atom when transforming from UO2 to U3O8, which agrees very well with experimental data. The implication of this prediction on the linear expansion and fuel fragmentation is discussed. The calculated elastic constants of urania are in good agreement with experiment. The predicted mechanical properties of UO2 and U3O8 are compared.

Aug 1, 2010

By K. Fukuda

The volatilization behavior of heavy metal in electric ash melting furnaces has a strong relation with its distribution between molten salt and slag. In this study, the distribution ratios of heavy metals between molten salt and slag phases were measured using a hermetic cell. The experimental results showed a relatively rapid loss of Pb and Zn from the salt in the first few hours followed by slow heavy metal vaporization with an almost fixed metal distribution between molten salt and slag. The distribution ratios of Pb and Zn decreased with increasing slag basicity. The mechanism of this effect can be explained by the chlorinated reaction of PbO and ZnO by CaC12.

Jan 1, 2004

By Geoffrey C. Streeton

A continual objective of mine operations is to reduce ground control costs without compromising the overall safety or performance of the installed ground support. Any change in the ground support regime must not result in a less secure or safe workplace. The due diligence required to implement a change in rockbolting practice is extensive, particularly when the new bolting system has not been used at any other mining operation. Factors such as yield, shear strength and embedment strength must all be investigated to gain an understanding of how the rockbolt can be expected to perform. This paper also discusses the substantial cost reductions and efficiency gains which can be achieved through the introduction of the Jumbolt rockbolt.

May 1, 2001

By M. J. A. Ruszala

Aggregates production is a huge global industry which uses an enormous amount of energy and produces a massive amount of unsalable fines. Reducing the amount of energy used per tonne of product and/or the amount of fines produced, would make a quarry more efficient. This reduction would make the quarry more environmentally friendly and profitable. This research looks at modelling Mountsorrel Quarry, a granite quarry in the United Kingdom (UK), using JKSimMet and Split-Desktop software packages in conjunction with the European Union (EU) project, EE-Quarry. Samples submitted to drop weight tests confirmed Mountsorrel Quarry granite as an extremely hard granite. Rock fracture data (t10) and energy of comminution (ECS) data were obtained from analysing the results. Split-Desktop image analysis software was utilized to determine the particle size distribution (PSD) of the primary crusher feed, as it contains particles too large to screen manually. It was also found that <1% of the feed is fines, which at Mountsorrel Quarry are classed as particles smaller than 5 mm, and that no particles were larger than 3,810 mm. JKSimMet was used to create a flowsheet of Mountsorrel Quarry. The crusher product PSDs were simulated and found to have strong correlations with experimental data, calculated by screening samples from conveyor belts, especially in the fines region, with a mean difference of 1%. The simulated primary crusher product PSD showed that it contains ~6% fines. A simulation over the entire quarry showed the product to be within the size range produced at Mountsorrel Quarry, and with a simulated fines content of 13%. When the CSS on the primary crusher was altered from 165.1 mm (the operating size on site) to 100.0 mm, it increased the overall percentage of fines produced by 3%, increased the power draw by 140.6 kW, but reduced the overall plant production percentage of fines by 2%. Two blasts were analysed on adjacent rock faces. They had identical blast designs, but the order of deck detonation varied; the first blast detonated the bottom deck before the top and vice versa in the second blast. For each blast, measurements of the feed PSD to the primary crusher, the number of particles that required secondary breakage on the quarry floor, acoustic levels and vibration readings were measured. No significant difference was identified between the two blasts in any of the parameters measured. In conclusion, a working model of Mountsorrel Quarry has been made in JKSimMet that has been validated against data from site and Split-Desktop has been used to simulate the primary crusher feed PSD, something that was previously unknown. The effect of reversing the order of deck detonation in a two deck blast was also analysed but with no significant difference between the two blasts found.

Aug 1, 2013

By R. S. Jr. Stronach

"IntroductionThe property of Campbell Red Lake Mines, Limited, is in Balmer township, Red Lake area, Patricia portion of Kenora district, Ontario. It consists of a group of twelve claims which had been staked and re-staked a number of times before George W. and Colin A. Campbell staked them in 1944. Messrs. Brewis and White incorporated Campbell Red Lake Mines, Limited, in July, 1944, to acquire these claims from the Campbell brothers, and in November of the same year re-assigned their option on the controlling interest of the treasury shares to the Dome Exploration Company (Quebec), Limited, a wholly owned subsidiary of Dome Mines, Limited.A long known exposure of sulphides on the northeasterly portion of the property, which returned low gold assays, on sampling, was the only showing of interest at this time. However, Dr. H. C. Horwood's report and map of the district had recently been published and favourable structure W3.S indicated in Balmer township. It was on the strength of this showing and Dr. Horwood's report that Dome Exploration became interested in the property.Between. January, 1945, and April, 1946, a diamond drilling programme was carried out, with completion of sixty-one holes. Five holes proved the surface showing to hold no commercial interest, so routine cross-sectioning of the property from north to south was started. The fourth hole of the series returned excellent ore intersections and from that time on the programme changed to one of extending these values. The final results of the drilling showed that what is now known as the A zone has a continuous length of some 1,200 feet, a width of 4½ feet, and an overall grade of about 0.5 oz. gold per ton. There were many other intersections of ore grade outside this A zone which could not be successfully correlated .at that time, but underground work has opened many of them. It may be said here that practically all the work to date has been confined to the southeast claims of the property."

Jan 1, 1950

By L. Long

Stirred milling of nickel laterites offers possibilities for improving liberation and selective size reduction of soft nickel-bearing minerals in laterites. Batch grinding tests were performed in a Netzsch LME4 stirred mill on siliceous goethitic (SG), goethitic (G), and saprolitic (SAP) nickel laterite samples (- 2000 ?m particle size) to evaluate the effect of stirrer speed, solid content, water salinity and grinding time. A fine mineral product (-38 µm) was used to evaluate the effect of selective grinding and Ni upgrade. The optimum grinding time for the highest Ni upgrade was 0.25 min, 0.1 min and 0.1 min for the SG, G, and SAP nickel laterite, respectively. A new feed (38-2000 µm) for each nickel laterite sample was prepared for batch grinding tests under the optimum grinding conditions. Upon grinding the 38-2000 µm feed, the - 38 µm product confirmed the effect of selective grinding and nickel upgrade. Size classification followed by stirred milling is a suggested process for Ni upgrade. The best Ni upgrade result was achieved on the SG nickel laterite among the three samples. The Ni grade increased from 0.85% to 1.37%, with 27.8% Ni recovery. Bottle roll leach tests showed that for SG and SAP samples selective grinding had no dramatic effect on Ni extraction due to the slow leach rate of hard mineral particles. Stirred milling of G sample increased the surface area of goethite, resulting in higher Ni extraction. Gravity concentration through a Knelson Concentrator was not effective in the further treatment of the stirred milling products either due to the poor operating conditions or due to the mineralogy characteristics of the feed samples. The energy requirement in the stirred milling was investigated. The first pass of the signature plots study is critical for the purpose of selective grinding, because the best result on selective grinding is achieved in the early stage of the grinding process.

Aug 1, 2013

By Helmer Kraemer

One of the CIM 2003 conference themes is ?Globalization and the impact on mine operations?. In this context, the first official version of the new ?International Rock Excavation Data Exchange Standard? (IREDES) is being released. This new standard is a highly flexible data interface for exchange of information between production equipment and central computer systems. The standard was defined by global players in the mining industry and will soon be used to enhance local operations of global mining companies. Beside the standard definition now other aspects are coming into focus: The question how to design and how to implement IREDES compliant data exchange in practice. Implementation of IREDES covers the following aspects: !" Implementation on in-field production systems !" Communication and networking !" Implementation on databases and commercial IT systems In-field production systems are characterized by a big variety of different automation systems. Therefor, different IREDES implementation philosophies have to apply to those systems. One philosophy uses an integrated IREDES compliant automation system on every machine. The alternative method uses one shared IREDES compliant ?Proxy server? for a number of machines connected to this server using proprietary interfaces. Communication and networking can be integrated openly and independently from hardware infrastructures. The only precondition is that communication and networking has to be Ethernet - TCP/IP protocol compatible. IREDES Implementation on the commercial IT level means to exchange IREDES data sets with databases, simulation software, office packages and special applications. Interfacing is easy as long as the software or the database system provides an interface to the Extensible Markup Language (XML).

May 1, 2003

By G. Song

This paper reports the anodizing voltage, gas evolution and sparking behaviors of an anodized coating formed on AZ91D in a silicate containing solution. According to their responses to an anodizing current, a four-stage anodizing mechanism is proposed. At the same time, the formed coating is characterized in terms of its microstructure, composition, thickness and corrosion performance. It was found that deposition of MgSiO3, Mg(OH)2 and MgO as well as dehydration of Mg(OH)2 are involved in the anodising process; the vigorous gas evolution accompanied by intensive sparking and the corresponding negative anodising efficiency in the later stage of the anodising process are closely associated with thermal decomposition of water due to the high temperature resulting from the intense sparking on the surface of the anodized alloy; the thickness, porosity, and composition of the anodised coating on a magnesium alloy depend on the final anodising cell voltage; and the corrosion resistance of a thick but porous coating containing more silicates appears to be more corrosion resistant than a thin but compact coating containing less silicates.

Jan 1, 2006

By I. A. Menshikh, S. A. Kotov, N. L. Shinkarkin

All the cycle for conversion of natural and reprocessed uranium of ROSATOM’s “TVEL” Fuel Company is concentrated at the Siberian Chemical Plant. Conversion capacities are located on two sites, i.e. the Radiochemical Plant, which refines feedstock, and the Conversion Plant, which produces uranium oxides and uranium hexafluoride. Liquid radioactive waste arising in the process, after pretreatment, is transferred to a dedicated national operator for underground disposal. Environmental strategies pursued by the Fuel Company involve the introduction of process solutions intended to eliminate liquid radioactive waste and convert it into a solid phase. In the 5–7 years coming, work will be performed to refurbish and upgrade conversion facilities of the Siberian Chemical Plant that will principally change its radioactive waste management scheme. This paper describes the current waste management scheme and sets out planned schemes for management of natural and reprocessed uranium waste, which will be implemented in the refurbishment of conversion facilities of the Siberian Chemical Plant. The new technologies for the management of liquid radioactive waste from uranium conversion described in the present paper have an undeniable advantage over the current technology mainly due to significantly less environmental harm.

Jan 1, 2020

By H. Kuboyama

The synergistic effects of polymer additives such as gelatin and polyethylene glycol) (PEG) and Cl- on Cu electrodeposition have been investigated by measuring the polarization curves for Cu deposition, by rotating ring-disk electrode technique and by AC impedance measurements. The cathode potential for Cu deposition was greatly polarized in solutions containing both Cl- and gelatin or PEG, showing evident synergistic effect of polymer additives and Cl- on Cu deposition. The cathode potential was shifted to the less noble direction with increasing the concentration of Cl- in solutions containing polymer additives and showed the maximum polarization at Cl- concentration range between 0.1 and 1 mmol/L. The rotating ring-disk electrode technique revealed that Cu deposition in solutions containing small amounts of Cl- proceeded with initial formation of adsorbed intermediate CuClad. The Cole-Cole plots obtained by AC impedance techniques suggest that the reduction of CuClad is suppressed by polymer additives. The morphology of Cu deposited from solutions containing both PEG and Cl- showed the compacted surface composed of smaller grains due to an increase in the overpotential for Cu deposition.

Jan 1, 2007

By M. McKim

"Due to the fact that there were no formal papers submitted for this session we can only print the discussions of the papers. a) Maqnetic Mill Liners : M. MckimE. MarcotteFalconbridge LimitedReplyIn looking at the slides on magnetic mill liners a question comes to mind, particularly in the case of a large diameter mill using large grinding media, concerning the potential hazzards which may exist from large chuncks of steel hanging in the mill. Would you comment.The magnetism was sufficiently strong from liner to liner to hold ........................ .(We are sorry but we could not transcribe the full reply to this question as no microphone was used by the speaker and i't was impossible for us to complete the rest).·"

Jan 1, 1984

By O. Kangal, G. Önal, G. Bulut, A. Gül

The recovery of copper and cobalt from the ancient copper slags, located in Küre-Turkey, is investigated. Fayalitic type of ancient copper slags containing 1.41% Cu, 0.53% Co and 53.16% Fe were subject to the experimental study. Magnetic separation, gravity concentration and flotation test were conducted. The results of magnetic separation and gravity concentration were not satisfactory. However, a concentrate containing 9.57% Cu could be produced with 44.7% recovery by flotation. Copper and cobalt that remained in the flotation tailings was recovered by roasting with sulfuric acid followed by hot water leaching. Complete cobalt dissolution was observed in 1 hour of roasting at 150°C and 3:1 acid/slag ratio, whereas the copper recovery was 83%.

Jan 1, 2004

By S. -H. Sohn, M. -K. Cho, G. -G. Hong

In order to evaluate the properties of coating materials for BOF, the effects of dolomites (dolomite and light burned dolomite) addition on durability of coating materials were investigated. In all coating materials, matrix was dicalcium ferrite(C2F) and both free MgO and dicalcium silicate(C2S) were precipitated. Fe203 content must be controlled to improve the adhesion and durability of coating materials for BOF during oxygen blowing process. The amount of dolomites added to BOF slag must be controlled in optimum condition with high refractoriness of C2S to improve the adhesion of coating materials for BOF. The weight ratio of converter slag to dolomite must be below 8 to improve the adhesion and durability of coating materials simultaneously.

Jan 1, 2004

By Bennett McLaughlin

The Penna Shaft is the deepest single?lift shaft in North America. AGNICO-EAGLE started sinking the Penna shaft in 1995 with a hoisting plant capable of hoisting 1 800 tonnes per day from a 2 240-metre deep shaft. Exploration success at depth lead to the replacement of the existing double drum hoist by another double drum hoist capable of hoisting 7 000 tonnes per day. The use of another double drum hoist, instead of a Blair Multi-Rope winder, to hoist 24,5-tonne skips was only made possible by lowering the safety factor. This paper describes recent experiences at Penna and in South Africa, and examines the possibility of extending the double drum hoisting system to a depth of three kilometres.

May 1, 2003

By Gordon Nelson

The Homestake gold mine is one of the largest and oldest continuously operating gold mines in orth Ame rica. To date this mine has produced in excess of 128.000.000 tons of ore containing almost 34 million ounces of gold . Gold mine ralization is restricted to the Homestake Formation. This unit is a metamorphosed iron-formation which is enclosed by pellitic metasedime nts below (Poorman Formation) and a pellitic to qua rt zitic unit (Elli son Formation) above. The e ntire Precambrian sequence. in the Lead area. has been subjected to a multi-stage defo rmation episode which ha c reated an extremely complex structural setting for the Homestake orebodies. Metamorphic grade inc reases from greenschi st ro amphibolite in a northeast d irecti on acros the mine area. Present thickness of the Home take fo rmation va ric from O to »400 fee t. The amount of thicke ning and th inning which is attributable to tectonic deformation or original sedimenta ry di fferences is not known. Orebodies constitute onl y a small pe rcentage of the Homestake Formation and do not occur along a pa rticul ar stratigraphic pos ition within the unit. Gold i assoc iated with inc reased py rrhotite and a rsenopyrite concentrations within the iron formation. Inc reased \ cin qua rt z development and chl oritic alteration usuall y accompany this minerali zation. Local remobilizati on of mine ralization due to metamorphi sm has occurred. Homestake mine ralization has been shown to be of sy ngeneti c origin . Because no feeder zones have yet been recognized a di stal source for the mine ralization is inferred .

Jan 1, 1986

By M. D. Quinn

THE sand and gravel used for backfilling at the Hollinger mine is obtained from deposits in a low range of hills some three miles north of the mine, where the Company owns a number of claims. The material is transported to the mine by aerial tram. Shipments from these deposits to the Hollinger mine commenced in June, 1927, and since May, 1936, sand has been supplied also to the McIntyre mine. During 1942, Hollinger requirements were 1,700 tons per day, and 900 tons per day was delivered to McIntyre. For the past seven years production has averaged 900,000 tons annually, and total deliveries to the end of 1942 were 13,129,022 tons, of which 11,075,339 tons went to Hollinger and 2,053,683 tons to McIntyre. Some years ago, when the original pit was approaching exhaustion, new workings were opened on claims east and south of the tramway terminal. It soon became apparent that the sand varies considerably in character from place to place. The weight per cubic foot was found to range from 85 to 130 lb., and the water percolation rate from 2 to 50 inches per hour. As the mine requirement is a sand with percolation rate of 6 inches or better per hour, it was evident that in certain parts of the deposits the material was not suitable for use as backfill. As a consequence, it was decided to carry out a programme of systematic sampling of the claims in order to select the areas containing suitable material for back-fill and at the same time estimate the tonnage available.

Jan 1, 1944

By S. Afshar, E. Dajoux, C. Allaire

For various reasons, molten salts, mainly chlorides and fluorides, are used in the aluminum industry. In the holding and melting furnaces, these salts may have different roles such as protecting the metal from oxidation, reducing the metal content of the skim or removing inclusions or impurities from the metal bath. However, the use of these salts may also have some undesirable effects such as easy attack of the furnace lining refractory materials by molten aluminum. The aim of the present investigation was to clarify and to compare the effects of chloride versus fluoride salts, on the corrosion process of the aluminosilicate based refractory materials. A laboratory test and procedure, simulating the conditions at the metal line in the aluminum treatment furnaces, was used. Different aluminum alloys (A1-5wt.%Mg, A1-5.5wt.%Zn and 7075 alloy) and chloride or fluoride salts (MgC12, KC1, CaCl2, NaC1, MgF2, CaF2, NaF and cryolite) were used as well as several aluminosilicate materials. Thermogravimetric measurements were also carried out in order to analyze the effect of the salts on the oxidation of molten aluminum alloys. The experimental results showed that fluoride salts are more aggressive than chlorides against the tested refractory products. It is postulated that the fluorides prevent the formation of a protective oxide layer on the metal surface, favoring at the same time the corrosion of refractories. Moreover, it was found that the presence of Na in fluoride salts increases significantly the aggressiveness of the aluminum alloy towards the refractory samples.

Jan 1, 2004

The following guidelines have been recommended by the Diamond Exploration Best Practices Committee established by the Canadian Institute of Mining, Metallurgy and Petroleum. These guidelines are applicable to public companies and their consultants reporting diamond exploration results. In respect of these guidelines, Diamond Exploration Results are results derived from the initial activities undertaken to investigate a diamond bearing prospect or deposit, to generate tonnage, grade and value estimates that cannot be classified as a Mineral Resource or Mineral Reserve. They do not address the earlier stage reporting of geophysical, geochemical or kimberlite indicator mineral results. Public reports of Diamond Exploration Results relating to mineralization not classified as Mineral Resource or Mineral Reserve must address the confidence limits of the result and contain sufficient information to allow a considered and balanced judgement of the significance of the results. The objective of these guidelines is to assist public companies and consultants in making appropriate disclosure of diamond exploration results by reporting in a manner which is: ??Uniform within the diamond exploration industry; ??Consistent with reporting from other industry sectors; ??Comprehensive; ??Unambiguous. The guidelines are not prescriptive. Materiality is the overriding principle that determines the information that should be disclosed. However, where a company or consultant deviates from the guidelines, the disclosure or technical report should state the extent to which the guidelines have not been followed, and the reasons for the deviation. The guidelines do not in any way replace jurisdictional reporting requirements (For example, the requirement for Canadian reporting issuers to comply with Canadian Securities Administrators National Instrument 43-101 by having technical disclosure endorsed by a Qualified Person as defined in that legislation).

May 1, 2003

By J. Marks

The measurement of greenhouse gas (GHG) emissions from primary aluminium production and inventory of these emissions of carbon dioxide and PF Cs have become an important issue for primary aluminium producers. Most global producers have either voluntary emission goals or emissions limits established through national regulatory requirements. International good practices for inventory of these emissions for national governments are established through the Intergovernmental Panel on Climate Change (IPCC). The current good practices, last updated in 2000, are being revised and are expected to be adopted by governments in the spring of 2006. There are a number of changes expected in the guidance that will impact how facilities account for their GHG emissions. This paper describes the changes to the guidance and the implications of these changes for aluminium producers.

Jan 1, 2006