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By D. O. Tansey

This paper will describe the mechanisms involved in delay blasting and how they are applied with the use of D.S.B. It will examine the control of potential damage resulting from detonations, and show how good fragmentation and efficient recovery of this material blasted can be achieved.

Jan 1, 1979

By Erich J. Jacob, Volker O. Meldner

INTRODUCTION Our company has made persistent efforts to utilize the very latest cost-saving technology in tunnel design and construction. However, we were relatively late in joining the clan of slurry shield tunnelers. The challenge came in 1973, when our company was low bidder on a major sewer tunnel in Hamburg, West Germany. The tunnel was to be driven under the harbor region through coarse and fine sands with up to 60 ft hydrostatic head of water. Outer diameter was 15 ft, and length was 2.9 miles. This contract appeared right to enter the new field of slurry face tunneling. We gathered a design-engineering team to develop the machine, called it "Hydroshield", and used it on the project. The good performance of the prototype machine encouraged us to improve and modify the equipment design. The very latest model is now in use on a subway tunnel in Antwerp, Belgium. This tunnel is 21 ft outer diameter and 2.4 miles in total length. In terms of excavated volume it is the world's largest slurry shield contract. While the drive is still in full swing, we are currently preparing for 3 further Hydroshield applications, with diameters ranging from 12 to 32 ft. This paper describes the Hydroshield's salient design features, operational characteristics, construction reliability and performance levels, as experienced in West Germany and Belgium.

Jan 1, 1979

By D. Robert Weir, Verner B. Sefton

The reduction roast-ammonium carbonate leach-hydrogen reduction process for laterites has been under development by Sherritt Gordon for the past 20 years. The process can treat high iron or low iron laterites, with some process modification, and gives extractions of 88-93% Ni or 82-88% Ni, respectively. Five campaigns on a 1 tonne per day Pilot Plant and four campaigns on a 35 t/d Demonstration Plant have been carried out on laterite from three different deposits, and many other laterites have been investigated in the laboratory. The Marinduque Surigao Nickel Refinery in the Philippines was designed on the basis of this work. The process comprises roasting to selectively reduce the nickel and cobalt in the laterite, leaching the calcine in ammonium carbonate to dissolve the metals, recovery of cobalt by precipitation of a mixed metal sulphide, concentration of nickel from the carbonate solution by basic nickel carbonate precipitation and recovery of high purity nickel by hydrogen reduction of nickel from ammonium sulphate solution. Ion exchange has been developed as an alternative to BNC and for recovery of trace nickel from BNC barren liquor. Details of the development of some of the process steps through the laboratory to commercial plant are discussed. The process metallurgy has been confirmed in the commercial plant.

Jan 1, 1979

By T. T. Toomver

The evolution of Inco's Selective Reduction Smelting Process as practised today is described, beginning with the initial laboratory experiments on small samples to the processing of large bulk samples through pilot plant equipment. For both the Guatemalan and Indonesian (Soroako) ores, the initial screening tests using hydro-, vapo-, and pyro-metallurgical processes showed that the latter was the most promising both metallurgically and economically. Later, larger scale tests confirmed the earlier testwork.

Jan 1, 1979

By H. O. Harju

In July 1968, P.T. Inco Indonesia was granted a Contract of Work to explore and develop the nickel laterite resources on the southeastern peninsula of the island of Sulawesi. Since 1970, exploration has centred on the deposits at Soroako as the site for initial project development. This paper describes the exploration methods used to evaluate these rather unique laterite deposits, the geology of which is described in the first section of this volume.

Jan 1, 1979

By John D. Hanks

INTRODUCTION Chevron's Uranium Mill is located near Panna Maria, Texas; 70 miles southeast of San Antonio. Designed by Kaiser Engineering, the Mill will process a nominal 2500 dry T.P.D. of uranium bearing ore containing 15% uncombined moisture. Earl Torgerson, San Mateo, California, is the consulting metallurgist on process design. Feed to the plant consists of a mixture of high, medium and low grade sandy day ore; the average grade of the ore will be 0.7% throughout the life of the project. The ore is delivered to the mill via truck and stored by type in individual piles on a flat storage area. The ore is fed by conveyor to a semi-autogenous grinding mill. The SAG mill discharge slurry is pumped either to a storage tank or to the first of five mechanically agitated leach tanks where both H2SO and NaC103 are added. Following leaching, the slurry is mixed with thickener No. 2 overflow before being pumped to a six-thickener, countercurrent decantation circuit where the solution containing uranium is separated from the leach residue. The residue is washed essentially free of solubilized U308 values at the sixth thickener and discharged to an adjacent tailings pond. The first thickener overflow, containing approximately 0.4 grams U308 per liter, is filtered for clarification and sent to the liquid ion exchange (solvent extraction) section. The pregnant aqueous solution is mixed with organic solvent containing amine on which the complex uranyl sulfate ions are absorbed. The immiscible aqueous and organic solutions are mixed and separated in each of the four stages of solvent extraction. The final pregnant organic is directed to a stripping section. A strip solution containing (NH4)2S04 (ammonium sulfate) and NH4C1 (ammonium chloride) is contacted and separated from the organic in each of the four mixer-settler units. The strip solution is mixed with NH3 and the uranium precipitates along with trace amounts of sulfate, chloride, and ammonia. After washing in a thickener, the uranium precipitate or yellowcake is centrifuged and dried in a multiple hearth roaster. Overflow from the yellowcake thickener is recycled back to the stripping section of the solvent extraction circuit. The dried yellowcake concentrate contains more than 98% U308; diluents include H20, ammonia, chloride, etc.. Impurity concentratons in the product are sufficiently low, after drying, to permit direct shipment to refinement installations. ORE RECEIVING Ore from one or more mines will be stored on a pad adjacent to the uranium processing mill. Ore stored in the area may total 200,000 tons or more, which is equivalent to over a two month treatment reserve for the mill. In addition to providing surge capacity, the proposed storage facility permits natural oxidation of the ore and affords an area which, in turn, improve plant U308 recovery and reduces consumption of oxidizing reagents. The uranium bearing ore is segregated at the storage area into several distinct types. One group can be identified by its sandy, clay-like matrix and will be distinguished by its U308 concentration of high, medium, or low. Other ores contain substantial quantities of carbonaceous shale, typical of ore in the area. Feed is recovered from any one or combination of piles, in accordance with operating requirements and recovery factors. The run-of-mine ore, at 15% moisture, is transferred to a stationary, 24-inch by 24-inch grizzly. Undersize material falls into a 280-ton surge hopper located below grade, while oversize material is removed for preliminary size reduction. A sump-pump is located at the reclaim hopper to recover excess mositure and ore spillage for processing. Plant feed is continuously drawn from beneath the hopper at an average rate of 120 tons per hour by means of an apron feeder. The hopper is equipped with a low level safety system to protect the apron feeder assemble. The ore is transferred to a belt conveyor, elevated and discharged into a semi-autogeneous grinding (SAG) mill. Water addition at the discharge point is automatically controlled by a feed rate, moisture analyzer system located on the belt conveyor. GRINDING Minus 24-inch ore, at a rate of 120 mosit tons per hour and cyclone underflow at a rate of 137 moist tons per hour are combined with a controlled 186 gallons per minute fresh, warm plant process water. The mixture, at an average 68% solids, is fed to the SAG mill. The viscous mass is subjected to grinding at a temperature moderately above ambient resulting from use of the 140ºF well water. The 16.5'x5.0' Marcy Mill is driven by a 500 H.P. A.C. Motor. The mill will rotate at 73.4% of critical speed or 14.06 R.P.M. Eight percent of the mill's volume will be occupied by steel grinding balls; 22% by pulp. The mill is designed to rotate in either direction, in order to obtain maximum lifter and liner life. The SAG mill is equipped with a trommel having ½ -inch slots for removal of oversize material at its discharge and the large or oversize material is collected and either recirculated periodically or discarded. The undersize slurry is diluted to 64% solids with the addition of hot well water or mine water to the mill discharge sump. The flow is automatically controlled utilizing data from a gamma density meter. The slurry from the mill discharge sump is pumped to hydrocyclones to classify the particles. Underflow from the cyclones, at 80% + 28 mesh, is recycled to

Jan 1, 1979

By R. H. Brooks

Blasthole stoping methods were introduced at Birchtree Mine as an alternative to the original cut-and-fill and shrinkage stoping methods. The object was to take advantage of the ore structure and conditions, and achieve increased productivity. This paper outlines the design, operation and economics of three areas which utilized blasthole stoping. The 108areafrom 2300 level to 1500level was converted from cut-and-fill to sublevel blasthole stoping based on a block mining-and-filling sequence. The second area, the crown pillar of 110 mechanized cut-and-fill stope below 500 level, was recovered using horizontal rings drilled from raises within the ore zone. The third area, the 83 orebody from 1300 level to 1100 level, used the vertical crater retreat (VCR) method with large-diameter blastholes. Blasthole stoping has increased productivity and improved operating conditions.

Jan 1, 1979

By Stanley M. Moos

The Pueblo Viejo gold/silver mine, located in the Dominican Republic, started production in early 1974 processing ores averaging 4 g/tonne gold and 20 g/tonne silver at a rate of 7,250 tonnes/day. The ore milled is a silicified siltstone with average work index of about 8 that occurs as an extensive oxide capping of a primary sulfide orebody. The sulfide ores are refractory to conventional treatment process and extensive research work is now in progress to develop a treatment process for them. The ore deposit has a long history having been mined by the indigenous Arawak Indians (for some time in the early sixteenth century) prior to the arrival of the Spanish and then by the Spaniards. In the early 1950?s, Italian engineers attempted to process the sulfide ores. Mining by the Indians and Spanish was abandoned because of low grade and little coarse gold in the oxide ores and by the Italians because of the refractory nature of the sulfide ore. In 1969, Rosario Resources geologists discovered that there existed sufficient reserves of oxide ore for a viable mining operation and accordingly, the plant was designed, built and brought into production.

Jan 1, 1979

The appraisal of mineral reserves by a lender is carried out at the initial stages in developing a loan for a mine. The depth of investigations is influenced by the competence of the explorer, the type of commodity and knowledge of the geological environment. The lender looks for a reserve life which exceeds the term of the loan plus contingencies for events such as cost over-runs, adverse markets and production difficulties. The physical features of importance are discussed. Factors with direct financial implications are considered for their incorp- oration in sensitivity analyses to allow risk appraisal. When satisfied, the lender can then proceed to review cash flow forecasts, the basic strength of the project, then determine with the borrower the components and alternat- ives of a loan package.

Jan 1, 1979

By Fidel Vera Rosas

La presente investigación señala algunos acontecimientos producidos durante el proceso de mineralización del yacimiento San Cristóbal, Junín a través de mantos, vetas y cuerpos irregulares en la zona. Ademá de estos tres tipos de ocurrencias, se prevee la diseminación del cobre, cuyo estudio aún no está definido.

Nov 20, 1978

By Oscar Pugliesi

Dado que la minería es una de las actividades económicas más importantes del Perú, su desarrollo y aprovechamiento depende de un plan de recuperación económica que se implemente en el país. En este sentido, el objetivo del texto es realizar un análisis estructural del sector minero, preveer el cálculo de las inversiones requeridas en el sistema en el sector minero metalúrgico a corto plazo y mostrar las perspectivas y proyecciones de las exportaciones metales y concentrados para el período 1978-1980

Nov 20, 1978

By Alfredo Solano R

El presente trabajo señala la geología y estructura del yacimiento minero de Antamina, ubicado en el departamento de Ancash. Para ello, se describe su historia, su geología compuesta por rocas sedimentarias, ígneas, metamórficas; la mineralización, su exploración geofísica, técnicas de exploración y el cálculo de reservas encontradas.

Nov 20, 1978

By Fausto Valdeavellano

El presente texto es una sistematización sobre políticas de desarrollo minero y sus interrelaciones con la realidad nacional a través de un marco conceptual metodológico adecuado. Para ello, se considera las dimensiones del desarrollo minero, las alternativas tecnología-producto, los aportes de la minería al desarrollo integral y los instrumentos relevantes para la aplicación de las políticas que interesan. Asimismo se presenta formas de formular, aplicar y evaluar políticas y planes mineros, así como se perfila la búsqueda de un consenso nacional para la adecuación de dichas políticas.

Nov 20, 1978

By Jorge Rodríguez Velarde

El presente trabajo describe un esquema matemático que simula un proceso de lixiviación química a partir del estudio de las variables más importantes y sus correlaciones entre sí. Para ello, se revisa los diseños experimentales, el equipo utilizado, las variables principales del sistema experimental, control de operaciones, discusión de resultados y algunas correlaciones de variables.

Nov 20, 1978

By Juan Manuel Rivera Poma

El presente trabajo describe los métodos empleados para una buena administración y control de la fuerza laboral a través de la aplicación de técnicas en los temas de determinación de la carga de trabajo, los requerimientos del personal, distribución del personal a los requerimiento actuales de la labor y un sistema de control permanente de la fuerza laboral. En este sentido, fue CENTROMIN-PERÚ, quien realizó los análisis técnicos de los recursos humanos y costos por intermedio del Departamento de Ingeniería Industrial-División Sistemas y así mejorar la productividad y la eliminación de gastos innecesarios de la mina.

Nov 20, 1978

By . Adolfo Farfán C

El presente trabajo describe los problemas ocasionados por los incendios en la mina de Cerro de Pasco. Si bien es raro que se origine un incendio en minas de características especiales como la de Cerro de Pasco, no se descarta la posibilidad de un corto circuito o algún otro infortunio. Por ello, es necesario conocer las causas, zonas de vulnerabilidad, los métodos de minado, ventilación, los antecedentes del incendio, origen, combate, las cuadrillas de rescate minero y la prevención de este desastre.

Nov 20, 1978

By Mario Santillán

El objetivo del texto es señalar el aprovechamiento de zonas mineralizadas, cuya explotación por métodos convencionales no tuvo resultados económicos, sino solo a través de un sistema racionalizado de minería sin rieles. En este sentido, la explotación de los block mineralizados se realiza a un nivel mínimo de producción de 150 a 160 T.C.S diarias, donde las rampas de acceso para la explotación de otras vetas se constituyen en una forma integral de explotación. Asimismo se considera el planeamiento operacional a corto, medio y largo plazo, se evalúan las condiciones operacionales, la explotación, método de minado, cargui, extracción, sostenimiento, relleno, las necesidades de personal y selección de equipos y los costos de producción e inversión.

Nov 20, 1978

By Alberto Encinas

Debido a los avances tecnológicos de la minería en los últimos quince años, se ha previsto el uso de equipos sofisticados, donde la mejora de los mismos implica un reto de programación, implementación y financiación debido a que la mina y sus formas de trabajo tienen que adaptarse a las máquinas por adquirir, en vez de que las minas adquiridas se adapten a la mina u operacioes mineras. En este sentido, el texto describe la influencia de los avances tecnológicos de otros países para diseñar nuevos equipos que se adapten a nuestra realidad minera y así mecanizarlas de acuerdo a nuestras necesidades.

Nov 20, 1978

By Hugo Medina Medina

El presente trabajo refiere el proceso de mineralización de fluorita en la mina Pasto Bueno, Ancash, el cual por sus características mineralógicas y estructurales es considerado como potencialidad geoeconómica en tungsteno. El estudio de la evolución geo-técnica del yacimiento comprende la estratigrafía, geología económica y los rasgos de la evolución geo-técnica del yacimiento Pasto Bueno a través de un esquema vinculado al desarrollo geosinclinal andino mesozoico y los conceptos de la Neo-técnica global. Una vez realizado estos estudios, se busca una mejor exploración y desarrollo minero del tungsteno-fluorita en el territorio nacional a fin de autoabastecerse de la fluorita en el campo de la siderúrgica.

Nov 20, 1978

By Manuel Villanueva Bullón

El presente trabajo describe la factibilidad del programa por computadora en los proyectos de minado no masivo a cielo abierto. Dicho programa permite calcular la cubicación del mineral como del material estéril para los tres ángulos de talud diferentes, as leyes de veta sin diluir y las relaciones desmonte-mineral para cada sección y zona explotada. En este sentido, la utilización de la computadora ahorra tiempo en los cálculos, aprovechándolo en beneficio del planeamiento de operaciones mineras.

Nov 20, 1978