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By Charles R. Wraith

The property of the Roan Antelope Copper Mines, Ltd., is situated at Luanshya, north central part of Northern Rhodesia, and is connected with the main line of the Rhodesia Railways, Ltd., by a 24-mile branch line from N'dola. Most of the material and supplies that are not available in Africa are shipped into the country via Beira, on the East Coast of Africa, a distance of 1473 miles from Luanshya and the nearest ocean port. The output of copper is shipped by rail to Beira and thence by boat to the market. Passenger travel is mostly via Cape Town, a distance of 2162 miles from Luanshya. Excellent passenger trains operate on regular schedules between Cape Town and Northern Rhodesia. Luanshya is 13" south of the equator at an elevation of 4000 ft. above sea level, and has a mild healthful climate. During the rainy season, from October to March, the rainfall averages 53 in. The area is profusely covered with vegetation. An ample supply of water for industrial and domestic purposes is available throughout the year. The more important supplies for smelting purposcs, such as wood, coal, limestone, silica, quartzite, and clay for "dolly" mud, are conveniently available. Excellent grades of coal, coke and firebrick are obtained from the Wankie Colliery Co., Ltd., Southern Rhodesia. The Wankie colliery has just completed the erection of equipment for the manufacture of silica brick. An ample supply of quartzite of good grade is available for this purpose. Silica brick is also obtained from the Belgian Congo and from India. Limestone is quarried from a large deposit a few miles from Bwana Mkubwa, which is 30 miles by rail from the smelter. An abundant supply of clay for " dolly " mud and for lining launders is available within a short distance of the smelter. Metallurgy Copper is contained in the ore as chalcocite, chalcopyrite and bornite. Chalcocite predominates in the eastern end of the orebody almost to the exclusion of other copper minerals. The amount of chalcocite decreases with a corresponding increase of chalcopyrite and bornite toward the western extension, where the latter predominate.

Jan 1, 1934

By D. W. Alexander

In 1993, CONSOL began investigating new methods of permanently filling coal mine shafts, which after ventilation is stopped, may contain a potentially hazardous atmosphere. Fill materials such as fly ash/cement can be pumped, are non-combustible and non-incendiary but tend to flow into the mine entries. A non-flowable mixture has been developed that minimizes the volume of fill used. The paper presents our recent shaft filling experience including fly ash material properties, mix designs, field problems, placement success, and gas testing techniques.

Jan 1, 1996

By T. M. Ruff, W. G. McCoy, M. J. Beus, S. Iverson, W. Hasz

Technology to enhance safety during mine hoisting has been developed by researchers at the Spokane Research Laboratory of the National Institute for Occupational Safety and Health. Assessment of current hoisting technology suggests that monitoring conveyance position and load directly from the skip or cage top offers several significant safety advantages. Wireless data transmission schemes and a package consisting of sensors, batteries, and a charger mounted on the wire rope and skip have been developed. A state-of-the-art automated hoisting test facility was constructed to test the concept in a controlled laboratory setting. Field tests in a full-size shaft are underway.

Jan 1, 1999

By A. Esterhuizen

Since 2005 Two Rivers Platinum Mine has set out on an initiative to actively monitor and control ground conditions on a daily basis, by making use of borehole cameras and pro-actively amending the support and mining strategies based on day-to-day observations of the hangingwall conditions. Today the borehole camera observations form part of the Rock Engineering Department?s daily function, and the size and frequency of falls of ground and ensuing accident rates have been drastically reduced since implementation of the system. The Two Rivers Platinum fall-of-ground management system aims to support 100% of the possible fallout thickness, based on ongoing data gathering and interpretation, thereby ensuring safety and limiting support cost.

Jan 1, 2014

By Elisa Araujo Santos Darsie

A busca na melhoria da qualidade dos aços, principalmente no caso de aços limpos, fez com que o distribuidor de lingotamento continuo também seja empregado para a remoção das inclusões responsáveis por prejudicar as propriedades mecânicas dos aços. Uma melhor eficiência desta função do distribuidor pode ser atingida com o conhecimento das características do escoamento do banho metálico de modo que se possam propor modificações na configuração do distribuidor. Esses fenômenos de escoamento e remoção de inclusões podem ser simulados mediante a utilização da modelagem física. O objetivo deste trabalho é avaliar quatro configurações internas de distribuidor por meio da qualificação do escoamento via ensaio de linhas de fluxo e quantificação de inclusões passantes pelo veio com o ensaio de remoção de inclusões. As variáveis de controle utilizadas neste estudo são: velocidade de lingotamento, presença de barreiras e presença de tubo longo. Os resultados apresentados para o distribuidor em questão mostram que para os casos com o tubo longo, o uso da barreira torna o escoamento predominantemente ascendente eliminando o curto-circuito e favorável a remoção de inclusões passando de 29,76 para 24,29% de inclusões passantes pelo veio. Enquanto que para os casos sem tubo longo, o uso da barreira proposta diminuiu o contato do aço com a escória sobrenadante, aumentou o curto-circuito e aumentou também o percentual de inclusões passantes pelo veio de 2,56 para 3,01%.

Aug 8, 2018

By R. G. Reddy

Nickel solubilities in spent pickling solutions (i.e. HF-HNO3-H2O solutions ) were measured as a function of HF and HNO3 acid concentrations. The chemical analysis of the industrial pickling solutions and sludges were made. The stable phases observed in the sludges are FeF3?3H2O, and ( FeCr ) F3?3H2O. Pure Ni, and stainless steel type 316 were used in this study. The results showed that the solubility of Ni increased with increase in concentrations of HF in pickling solution at a fixed concentration of HNO3: An excellent agreement between the experimental solubility data and the theoretical data was obtained. X-ray diffraction analysis showed that the solid solubility product formed is mainly NiF2?4H2O compound.

Jan 1, 1992

By Deren Zhu

The principle of roof control in longwall mining is to control main roof fractures so as to reduce roof weighting, plus reasonable and effective design of supports to reduce the convergence and premature caving of the immediate roof. This paper introduces a comprehensive test for better roof control based on the geological conditions of coal seam No. 16 in Zaozhuan Colliery, China.

Jan 1, 1990

CHARGING of an open-hearth heat is begun as soon as possible after the previous heat has been tapped. Ordinarily, about 40 min. is required to drain and dress the furnace hearth, make up the tap hole, and perform routine repairs of the banks. Repairs to the upper back wall and to the front wall and jambs can ordinarily be done while the first scrap charge is being heated and are therefore allowed to wait in order to save furnace time. Any major repairs required on the hearth or other parts of the furnace necessitate longer delays, because such repairs must be made while the furnace is empty. Although charging practice varies considerably in detail with the type and proportions of scrap and iron used, many factors are common to all varieties of' charge. Such general considerations are dealt with first. GENERAL CHARGING PRACTICE Charge materials are discussed in detail in Chapter IV; the present chapter is concerned with the charging, melting, and proportioning of the raw materials in the various types of furnace practice. Charging Equipment and Stock Handling. The physical equipment available for loading and weighing the stock, transporting it to the furnace, and charging it may have a major effect on charging practice. Limestone, scrap, and all other solid melting stock are charged mechanically by means of equipment described in Chapter I (see also Fig. 18, page 33). It is generally desirable to charge the scrap about as fast as the physical volume can be got into the furnace. A limiting factor may be the height to which the scrap may be piled in the furnace without deflecting the flame to such an extent that it will impinge on the roof or walls and thus damage the refractories, but light scrap may often be piled up near the roof since the flame usually "cuts it down" rapidly before impingement on any roof area can persist long enough to do appreciable harm. When the nature of the scrap and the handling facilities are adequate to meet the aim of rapid charging, little thought is given to this feature of operation. Unfortunately, at times

Jan 1, 1944

By Gaétan Bourdages

A clarification technology used by municipalities to produce high-quality drinking water, polish sewage treatment plant effluent and handle combined sewer overflows has recently found new applications in the mines and iron and steel industry. This patented process, known as ACTIFLO®, utilizes microsand in a ballasted flocculation process to enhance the settling characteristics of suspended solids, increasing the efficiency sufficiently to achieve a clarifier footprint that is smaller than the one of a conventional clarifier. ACTIFLO® rise rates vary from 40 to 170 m/h with a total system hydraulic retention time of about 10 minutes. The result is a clarification system so compact that a full-scale system can operate as a trailer-mounted unit for temporary applications or as a permanent installation in facilities with space limitations. This paper explains the process and presents case studies in which this innovative technology was used at mines and steelmaking facilities to meet compliance requirements.

Feb 1, 2008

By A. Y. Senchenko, S. G. Rybkin, A. V. Aksenov

"Oxidized nickel ores are important source for nickel production in Russia. Considerable explored reserves of oxidized nickel ores with relatively low nickel content, about 0.6-1.4%, are concentrated in the Ural region of Russia. Conventional process flowsheet with the use of blast matte smelting, applied in particularly by JSC “Ufaleynickel”, proves itself as extremely low-margin technology. This paper will examine development of a new more cost-efficient process involving integrated treatment of oxidized nickel ores using the ore from Serovskoye deposit as an example. Target products of this process are hydrate residues containing up to 15 % of nickel and 0.3 % of cobalt, as well as saleable salts of magnesium sulphate and ammonium suplphate. This innovative process includes roasting of a mixture composed of ground ore and sulphuric acid at 650 °?. Sulphate roasted product is then leached in a weak sulphuric acid solution with the following separation of liquid from insoluble solids. Sulphate solution is neutralized by aqua ammonia in two stages until media pH is 3.0-3.5 and 7.5-8.0 with detachment of iron- and nickel-bearing hydrate residues respectively. The mother solution is boiled out resulting in salt crystals which are then dried and roasted at 500-600 °? to obtain magnesium sulphate. The gases generated during salts roasting are captured with production of ammonium sulphate. The developed technology demonstrates higher potential in terms of its economics and eco-efficiency comparing with the conventional process. This innovative technology for integrated process of oxidized nickel ores was patented in Russia.INTRODUCTION Development and industrial implementation of efficient technologies to process oxidized nickel ores is a very important task for non-ferrous metallurgy of Russia. The main reasons for the required technical upgrade of the plants processing oxidized nickel ores is depletion of rich ores, increase of energy resources costs, amplification of environmental and production standards. Due to this, transition from conventional pyrometallurgy to cost-effective hydrometallurgical technologies of ore liberation and solutions processing is logical and corresponds to the worldwide practice of Ni production from oxidized nickel ores."

Jan 1, 2018

By P. F. Ziemkiewicz

This project evaluated the performance of nine passive treatment methods by studying 137 treatment units in eight eastern states. Performance was normalized according to construction cost, projected service life and tons of acid load treated. Results were dimensioned as $/tons of acid load treated/year. These costs were then compared to those of chemical treatment. Sites that achieved acid load reductions at costs below those of chemical treatment were considered successful. In addition to evaluating the performance of the treatment methods, this paper describes the various passive treatment systems, their applications and performance data for individual treatment units.

Jan 1, 2003

Jan 1, 1947

By Gustavo Brunello

Motor Failure Rates and Cost ? Motor failure rate is estimated: 3-5% per year. ? In Mining, Pulp and Paper industry failure rate is up to 12%. ? Sometimes process downtime costs are higher than motor ?? Motor failures are due: Electrical 32% Mechanical 31% Environmental 36%

Feb 1, 2008

By B. K. Mishra, R. K. Rajamani

Discrete element is a numerical technique for describing the collision dynamics and motion of an assembly of particles. In particular, calculations are done on full three-dimensional space with a force-contact law for collisions and Newton’s law for subsequent motion. It may be said that there is no empiricism in this approach. The paper describes the full scale simulation of large diameter semiautogenous grinding mill of size 40X24 ft. It is shown that the simulation predicts the power draft of plant size mill extremely accurately. Also these simulations have been adapted uniquely to assess the motion of pebbles and slurry in pulp lifters. The passage of slurry from pulp lifters into trunnion is extremely important since flow-back and carryover must be avoided at all cost. The dynamics of slurry flow through pulp lifters is also described in this paper.

Jan 1, 2003

By W. A. Calhoun

A method for concentration of the nickel-cobalt-bearing mineral, siegenite, from a table middling has been developed by the Bureau of Mines at Rolla, Mo. The table middling is composed of a complex series of sulfide minerals, occurring in mill operations in the southeast Missouri "lead belt." In these operations the siegenite is lost as a separate concentrate, being diverted to other products. The procedure also includes recovering commercial-grade concentrates of copper and lead. A low-grade zinc concentrate, a potential coproduct, was also made.

Jan 1, 1962

By V. E. Homme, M. M. Wong

Tests were made in reactors ranging from 12 to 30 inches in diameter to develop methods for the preparation of sodium chloride - titanium lower chlorides ( dichloride and trichloride ) melts that contain titanium predominantly in the divalent state . Such melts are desirable as a starting material for the production of titanium metal or as an electrolyte for electrorefining of titanium . Sodium reduction of TiCl with an 18 - hour period of holding the reaction products in the molten state produced melts that contained titanium lower chlorides in TiCl₂ - to - TiCl , molar ratio of approximately 8 to 1. Sodium reduction of TiCl in a reactor with a shielded pipe weir , that required no melt -holding period , produced melts with a TiCl₂ - toTiCl , molar ratio as low as 4 to 1 . Reduction of TiCl4 with scrap titanium metal in molten sodium chloride produced relatively pure melts containing about 27 percent titanium in a Ticl₂ - to - Ticl , molar ratio of approximately 4 to 1 .

Jan 1, 1964

The Wellington Dam catchment has high value water, agriculture and coal and power generating resources. These conflicting land uses are managed through consultation and regulation. The Wellington Dam catchment is unique in that the Collie Coal Basin is located almost to the edge of the dam and has coal mining and power generation as its primary land use. Currently the dam is only used for irrigation due to its high salinity. The State Government has committed to reduce the damÆs salt levels to below 600 mg/L by 2015 so that it can be considered for public drinking water supply. The coal industry in conjunction with the community and State Government has worked together to enhance the water quality within the Wellington Dam to maximise its value and use by using mine dewater for industry, diverting saline Collie River flows, providing environmental (social) flows and enhancing water quality of mine voids to encourage new industry to the Collie Region. Both surface and groundwater in the coal basin are generally fresh, whereas the salinity in the Collie River East Branch generally ranges between 3000 to 20 000 mg/L and 1700 to 10 000 mg/L in the South Branch. Mine dewatering is currently two to three times greater than the recharge to the coal basin. As a result, all mine dewater is sent to power stations in the area, with excess discharged into drainage lines which flow into the South Branch of the Collie River. To maintain environmental and social flows some groundwater is also pumped to the South and East Branches of the Collie River during summer months. Completed mine voids are used for recreation and options for aquaculture are promising. However, handback criteria are yet to be finalised.

Jan 1, 2006

By F. W. Denton

Much has been written about the possibilities of the Vermilion and Mesabi ranges of northern Minnesota as producers of large quantities of high-grade iron-ore. The Mesabi range in particular has attracted considerable attention on account of the proximity of the ore-deposits to the surface, which has been as-

Jan 1, 1898

By A. Palit, M. K. Mohanty

This investigation has concentrated on optimizing the newly developed Pansep linear screen and developing empirical models to predict the screening performance. Most empirical models developed in the past to predict the performance for industrial screens are suitable for the vibratory screens. Understandably, these models are deficient in predicting the performance of linear screens due to the difference in their operating principle. Thus, the main objective of this study has been to develop empirical models suitable for linear screens to predict the partition coefficient for a given size fraction as a function of the aperture size. The inadequacy of the conventional model equation originally developed for vibratory screen has been demonstrated and a modified equation developed to predict the partition coefficient as a function of the normalized mean particle size (d/d50c). In addition, new model equations have been developed for linear screens to predict the screening efficiency as a function of the separation size(d50) and to predict the separation size as a function of the screen aperture. It is believed that these model equations will be useful for the plant operators in selecting the mesh panels of correct aperture size and in predicting the product size distribution based on the selected aperture size.

Jan 1, 2003

By R. V. Ramani, V. T. Burgos, J. A. McClay

The data for Test I describes an underground bituminous coal mine operation in a 48 inch seam, with an estimated production rate of 1,056,000 tons per year. The system includes four continuous mining sections, conveyor belt haulage, and a rail network for supply and personnel transportation. This section illustrates the input data sequence and the various report formats which may be selected for the printing of results. As explained earlier, at the present time, the elements of the Cost Data Library must be read in with the regular data input. Thus, in the input data listing, immediately following the required user input, are cards which contain the inputs of the cost library. Examination of the cost reports indicate the absence of cost values for some categories for which the system would normally be expected to incur costs. This situation has arisen due to the format of the cost data provided in the U. S. Bureau of Mines reports. An example of this is the charge of $20/ton for brattice cloth while no charge is indicated for stoppings. The test report data provided a single figure for ventilation cost without a supplemental breakdown. Thus the cost indicated for brattice cloth is actually the total ventilation cost. These explanations hold true for the data input and output for Test II, Appendix III.

Jan 1, 1975