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By F. K. Letowski

Leaching of zinc sulphide concentrate by nitric acid which is simultaneously regenerated by oxygen in the reactive froth has been investigated. The reactive froth was formed by a recycled zinc sulphate electrolyte containing nitric acid, a mixture of gaseous 02 and NOx, entrapped in the foam and particles of the zinc concentrate suspended in the foam. In the reactive froth the multiple regeneration of nitric acid proceeded owing to the encapsulated oxygen and amount of nitric acid used can be considerably lower than in the continuous liquid phase. 93 to 97% of zinc was extracted to a solution containing 30 to 409/1 HNO, during 40 to 60 min of leaching in a batch reactor without regeneration of nitric acid. 50 to 100% of the consumed nitric acid was regenerated during continuous leaching in froth carried out in the ‘flotation column’-type reactor at 80 to 90°C and under pressure of 100 to 200kPa. The rate of HNO, regeneration in the froth was proportional to oxygen pressure and inversely proportional to nitric acid concentration in the froth. A two-stage process flowsheet is proposed. In the first, the reduction stage, removal of nitric acid from the leach solution directed to standard purification and electrolysis is carried out by its reduction to nitric oxide using fresh concentrate in the froth. In the second, the oxidation stage, nitric acid is continuously regenerated by oxygen in the froth.

Jan 1, 1995

By E. G. Kelly

Many methods of evaluating the efficiency of mineral separations have been described in the literature. In most cases, these present the efficiency as a single number. This paper argues that single-number measures of efficiency are inadequate because they seldom allow reliable comparisons, and are unlikely to correspond to the optimum operating conditions. To realistically make comparisons, it is necessary to distinguish the particle-induced component from the equipment- induced component. In a number of situations where the separating property can be identified (such as in gravity concentration and classification), this can often be done. However, in more complicated systems, such as flotation, this has not been possible. A technique is described whereby particle and equipment contributions to efficiency can be distinguished without the need to define the separation property. Because smelter schedules define a boundary correlation between grade and recovery, they generate some of the better single¬-number measures of efficiency, but even these have limitations.

Jan 1, 1991

By Alain GSELL

The aluminous nature of the laterites capping the Minim Martap plateaus - named after two neighbouring villages - and the small nearby upland of Ngaoundal, was discovered by the Cameroon Mines and Geology Division in 1958. These deposits of worldwide importance, are located in the Ngaoundere region, some 500 km (300 miles) north-east from the port of Douala (as the crow flies). They constitute the major part of the Cameroonese mining potential. The study of the deposits and their economic development has been entrusted to SEBACAM, Societe d'Etudes des Bauxites du Cameroun, a company in which the Cameroon government participates. The bauxites originate from the transformation into laterite of lavas which covered a Precambrian basement during the Upper Cretaceous period and the Lower Tertiary era. The entire Minim Martap deposit comprises bauxite plateaus ranging in area from a few acres to several square miles. The average thickness of the bauxite layer varies from 10 metres at Minim Martap to 17 metres at Ngaoundal. The mineral constituents of the bauxite are gibbsite trihydrate, kaolinite and the usual iron and titanium oxides. Treatment of the ore does not involve any particular technical problems. Proven exploitable reserves amount to 560 million tonnes of dry bauxite with a reactive silica content of 1.80% and an available alumina content of 43.70% at Minim Martap, and 120

Jan 1, 1984

By D. R. Lowe

Silicic volcanic ash and its alteration product, bentonite (montmorillonite and cristobalite), occur widely within sedimentary phosphate deposits. The genetic link, if any, between volcanism and phosphate deposition has yet to be satisfactorily established The phosphatic member of the Santa Margarita Formation (upper Miocene) in northwestern Ventura County, California, consists of approximately 15 per cent volcanic ash and bentonite. Ash and bentonite units greater than one foot thick can be subdivided into a lower zone of airfall origin and an upper zone of mixed ash and terrigenous detritus washed in from surrounding land areas. This upper zone also contains up to 20 percent phosphate pellets. These thick volcaniclastic units are typically overlain sharply by thin beds (less than 6 inches thick) of relatively pure, silica-cemented pelletal phosphorite. The shelf basin in which the phosphatic sediments accumulated was characterized by quiet, reducing but not euxenic bottom waters; Abundant decaying organic debris, mainly diatoms, served as a reservoir of readily available phosphate. The sudden influx of a large volume of silicic volcanic ash into this basin and its subsequent alteration to montmorillonite had two profound effects on thechemistry of the interstitial and bottom waters: (1) during alteration magnesium was removed from these waters and incorporated into the montmorillonite lattice, and (2) the pH of these waters increased as alteration progressed Both of these effects led to the crystallization in the bottom waters of carbonate fluorapatite. This accumulated as thin phosphorite beds immediately above the volcaniclastic units.

Jan 1, 1972

By Byron Belew, Juris R. Harlamovs, D. B. Dreisinger, John L. Watson, G. A. Kordosky, Thomas O. O’Keefe

Unwanted impurities, present in raw materials, are often coextracted along with desired constituents during leaching. Due to its abundance and ease of extraction, the presence of ferric iron in leach solutions, solvent extraction circuits, and subsequently in electrowinning circuits, has always been a problem. In the case of zinc hydrometallurgical processing, iron is frequently an impurity in leach solutions. Purification of such solutions by solvent extraction, using di (2-ethylhexyl) phosphoric acid (D2EHPA) in a kerosene diluent, results in ferric ions being readily extracted along with zinc into the organic phase. Ferric iron has proven difficult to strip from the organic phase, but it is known that ferrous iron may be easily stripped from D2EHPA, and hence a process to effect reduction of iron present in the organic would have great potential. This research investigated a process to directly reduce ferric to ferrous iron in the organic phase, and to strip the ferrous iron using a dilute acid solution. The process utilized metallic zinc as the reductant and a low concentration sulfuric acid stripping solution. The results of the laboratory tests illustrated that iron could be readily removed from the organic phase by simultaneous direct reduction and acid stripping. The reductive stripping process was subsequently utilized in industry at the laboratory and pilot plant levels. The results of the industrial tests were encouraging and demonstrated the potential of this novel concept.

Jan 1, 1993

By Lynda T. Holden, Philip L. LeHoux

Barneys Canyon Mine is a 1.8 million t.p.y. gold heap leach operation near Salt Lake City, Utah. The gold recovery plant has been operating since September of 1989. Carbon elution is done at atmospheric pressure with a high temperature caustic solution. No cyanide is used in the process. Operating experience is discussed.

Jan 1, 1990

By Tad S. Golosinski

The paper presents the computing stream of the mining engineering curriculum at he Western Australian School of Mines (WASM), a branch of Curtin University of Technology. Learning to use computers begins during the first semester of the initial year of studies and culminates in the Mine Design Project done during the last semester of study. It covers all areas of computing which are judged to be of importance to the graduate.

Jan 1, 1996

By K. K. Bhattacharyya, S. Bhattacharya, S. Dey

Coal batch flotation tests were conducted both with and without collector and with one- and two-stage additions of frother. The recovery of combustibles and the flotation rate constant were found to be higher with two-stage frother addition, both with and without collector.

Jan 1, 1998

By S. Bozinis

In this paper, blast design considerations and implementation that lead to reduced vibrations will be presented. In addition, blast vibration data collected during hard and semi-hard rocks blasting in the proximity of an inhabited area will be analyzed and presented. In all cases maximum vibration levels are kept below the limits set by DIN 4150.

Jan 1, 2006

By W. A. Cincilla, S. C. Tadolini

INTRODUCTION Resin bolting systems continue to gain popularity in underground coal mines in the United States, and their general success under a wide range of geological and operational conditions is well documented. In 1984, 36% of all bolts used were resin-grouted systems. However, many questions dealing with basic support mechanisms and the influence of various factors on bolt effectiveness in situ remain only partially answered. The Bureau of Mines' Denver Research Center conducted a major research project to investigate the influence of installation procedures on the effectiveness of resin-grouted roof bolts. The project consisted of two main studies: the first dealing with the contribution of bearing plates to the load-carrying capability of the bolt; the second examining the relationship between installed grout column and the anchorage capacity as measured by the standard pull-out test. Additionally, a finite-element computer model and other analytical and empirical techniques were applied to aid in the basic understanding of the test procedures and to examine the load transfer mechanism in resin-grouted bolts, which to date has not been comprehensively assessed. The plate study includes field test results from two mines (Fig. 1). At these test sites two behavioral parameters were measured: the actual loads that bearing plates were subjected to when installed in conjunction with full-column resin grouted bolts, and the roof movements generated by the applied loads. Results indicate that bearing plates are subjected to varying degrees of loading, which range from conventional installation pressures of 2.2 kN (500 lb), up to a measured load of 142.4 kN (32,000 lb) when the immediate roof is shifting and deforming. These measured loads indicate that the bearing plate is an integral part of the support system. Differential sag stations, installed to monitor roof displacements in the test sites, show the highest degrees of loading occur in conjunction with the largest amounts of movement. The column-length study addresses possible reductions in anchorage capacity of "full column" bolts. These reductions could result from such factors as the loss of grout to surrounding strata, or improper mixing of catalyst and resin. Field test sites were established at eleven mines located in major coal mining districts throughout the United States (Fig. 1). Four major roof-rock types were represented in the study: shale,

Jan 1, 1986

By Lewis Gordon, Alan Morrow, Aundra Nix

At the ASARCO Mission Mill, a multivariable, predictive controller was used to optimize parallel grinding circuits, improving throughput and product size. Using a dynamic model of the grinding circuit developed from on-line testing the software manipulates 4 variables to control 14 quality and constraint variables in each circuit. Traditionally, model-based control in grinding is difficult due to ore changes. This is addressed via a novel method to predict mill overload and automatic model switching.

Jan 1, 2000

By I. K. Gilmore

PCS Phosphate operates an open-pit phosphate mine in the central coastal plane of North Carolina. The company has mining and refining facilities located on the south shore of the Pamlico River. Phosphate ore is recovered at the Aurora facility by open-cast mining techniques. Walking draglines and bucketwheel excavators remove the overburden and mine the phosphate ore. The mined ore is slurried about 8 km (5 miles) to the processing plant. At the plant, the phosphate ore slurry is passed through screens to remove material coarser than 2 mm (10 mesh) and then pumped through hydrocyclones to remove material finer than 75 mm (200 mesh). The resulting phosphate and sand mixture is treated with various reagents and subjected to an anionic flotation process. A cationic flotation process removes the sand from the final phosphate concentrate.

Jan 1, 1995

By Surendra K. Mishra

The principles of dewatering fine coal has been examined in terms of solid- liquid separation. It is noted that the physical and physico-chemical properties of the particle-liquid system influence the rate and degree of moisture removal. Using postulated models the roles of polymers, surfactants and other physical means as dewatering aid are discussed.

Jan 1, 1988

By Arol, A. I., I. Iwasaki

The presence of calcium ion in iron ore pulps causes heterocoagulation of rnontmorillonite on hematite leading to indiscriminate dispersion. Two methods were investigated to control the adverse effect of montmorillonite: a chemical method using such complexing agents as EDTA and sodium tripoly- phosphate, and a mechanical method involving ultra- sonic treatment. Their roles in controlling the adverse effect were investigated by zeta potential measurements, starch adsorption tests, and flocculation and selective flocculation tests.

Jan 1, 1988

By F. L. Wilke

Truck haulage costs form a major part of the total mining costs in hard rock open pit, mining operations. In order to minimize these costs one has to - determine the optimal truck fleet (type, size and number of trucks), and. simultaneously - determine the optimal organization of running the haulage system, i.e. especially select the optimal dispatching strategy in order to ensure maximal utilization of the trucks, and simultaneously - establish a reliable maintenance and servicing system to guarantee maximal availability.

Jan 1, 1982

By James A. Everts

Calcined bauxites are classified by their major end uses - abrasives and refractories. Target properties are dictated by application and processing requirements. The chemical and physical properties of premium grade calcined bauxites are far more stringent than metallurgical bauxite and this limits the sources and availability. Premium grade calcined bauxites are considered to be strategically critical to the industrialized countries of the world. Subject to disruptions in the key source countries, adequate supplies of premium grade calcined bauxites are anticipated in the foreseeable future.

Jan 1, 1984

By D. W. Fuerstenau

Experiments using an optically polished Pyrex disk and aqueous dodecylammonium acetate (DAA) films showed that the velocity with which the films recede increases markedly if the runs are repeated at short time intervals, where equilibrium cannot be reattained. This results from DAA molecules being desorbed from the disappearing liquid-air interface and being deposited on the solid-air interface being formed. Controlled experiments with Pyrex particles in a modified Hallimond tube showed a similar increase in flotation rate, again due to excess adsorption of DAA molecules that were transferred to the solid-air interface from the bubble on contact.

Jan 1, 2002

By R. Sripriya, Ch. V. G. K. Murty, N. D. Rao, P. V. T. Rao, A. Ramu

Studies were carried out to improve the performance of hydrocyclones at Tata Steel's chrome ore beneficiation plant in Sukinda, India. The optimal cut point of the hydrocyclones was determined in the laboratory using a stub cyclone. In the tests, the operating and design variables, including spigot diameter, density of feed slurry and inlet pressure, were varied. Subsequently, plant trials were carried out, and attempts were made to develop a model of the hydrocyclone using the Rao, Lynch and Plitt model. The cyclone efficiency was represented by the parti¬tion curve, and the performance was evaluated mathematically from a reduced efficiency curve, represented by the equation:

Jan 1, 2000

By Sheldon Shepherd

Fifty years ago, belt scales were mechanical devices based on a complex weight balancing design. Today's systems use load cells to assess material weight, belt speed sensors and microprocessor-based integrators to continuously compute the rate of material transferred along a conveyor. Belt scales have become important assets to a plant. They help maximize the use of raw materials, control inventories and aid in the manufacture of a consistent product. Choosing and installing a belt scale system may seem complicated but it can be simplified by following a few guidelines.

Jan 1, 1999

By Mengxiong Guo, Xuxin Shao, Yong Bao

In the paper, the adsorption properties of dissolved ions on the surface of collophane and dolomite are studied using zeta potential measurement, ESCA and UV adsorption spectrum both in distilled water and in the supernatant of each other. The effect of dissolved ions on the flotation separation of collophane and dolomite under SCO depressant and oleate is discussed on the basis of above analyses.

Jan 1, 1993