Search Documents

By Michael J. Mujadin

Since the late 60's, planners at American Natural have known that natural gas supplies from traditional sources will be insufficient to maintain a consistently high level of service in the near future. This dwindling of traditional gas reserves will force American Natural and other gas companies to seek new and more exotic sources of supply. In recent years a number of alternative supply sources were considered, including arctic gas, LNG, and SNG based on naptha, LPG and coal feedstocks. Several combinations, all of which included SNG from coal were selected as the most suitable alternative sources of gas supply for American Natural, and thus our company embarked on the formation of a coal gasification project in the early 70's. Work began with the evaluation of available coal supplies in the United States in late 1970. Western North Dakota was selected for several reasons: large contiguous reserves of lignite were available near the surface, similar to German brown coal for which the Lurgi gasification process was originally developed; the conditions for land reclamation in the area are favorable; and the people in the area have a positive attitude toward well ordered development.

Jan 1, 1977

Recent start-up of a new 3450 t/d (3800 stpd) copper-zinc concentrator complex in northern Manitoba, Canada, is expected to open new reserves and dramatically cut transportation costs for Hudson Bay Mining and Smelting Co.'s Snow Lake operations. The new $C33-million mill is located in Stall Lake, Manitoba, and includes a new crushing and grinding facility and two flotation circuits for the production of 23-25% copper and 55% zinc concentrates. A small amount of lead concentrate will also be recovered. The plant will produce some 145 000 t/y (160,000 stpy) of concentrates, to be shipped by rail to the firm's Flin Flon copper smelter and zinc refinery complex, located 177 km (110 miles) to the west on the Saskatchewan-Manitoba border.

Jan 9, 1979

By John H. Wright

The United States Antarctic Program (USAP), through its principal support contractor Raytheon Polar Services Co. (RPSC), has recently completed a three-year project comprising nearly 936 m (3,071 ft) of undersnow utility tunnels at Amundsen-Scott Station, South Pole, Antarctica. The tunnel serves the new station facilities that are currently under construction. It houses the piping that conveys fresh water from current and future water well sites, as well as waste water to repositories in abandoned wells. The undersnow tunnels permit year-round access for system operations and maintenance. The network of tunnels is entirely unlined and unsupported. And, for the most part, it maintains a rectangular cross section of 1.8-m-wide x 3-m-high (6 x 10 ft).The tunnel runs from 6 to 14 m (18 to 45 ft) below the surface. Eight 1-m- (3.3-ft-) diam raises bored from the surface serve the network as emergency escapeways.

Jan 1, 2002

By R. J. Wahrer

In 1996, the Office of Surface Mining (OSM) and the U.S. Fish and Wildlife Service (FWS) completed an Endangered Species Act (ESA) programmatic Section 7 consultation. From the resultant Biological Opinion, it was found that coal mining operations conducted under federally approved state regulatory programs would not likely jeopardize the continuation of federally listed species nor result in the destruction or adverse modification of critical habitats. The requirements of the ESA and their integration into the SMCRA permitting process and the responsibilities of the regulatory agency, the FWS and the coal operator will be discussed. Guidance on the development of protection and enhancement plans will be provided and site-specific examples given.

Jan 1, 2003

By R A. Farnfield

Measurement of the environmental impact of ground vibration from blasting operations is based almost exclusively on the peak vibration level generated. This measurement is known as the Peak Particle Velocity or PPV. The recorded PPV is used to assess the impact of the vibration both in terms of structural damage and human response. Limits for vibration are almost universally quoted in terms of PPV levels and, as a consequence, blast design for vibration control is centred around techniques for the control of this peak value.

Jan 1, 1996

By A. M. Gaudin

THE so-called Kick law' is generally accepted to . mean that for each reduction to one-half in particle diameter, in a unit weight, the same amount of work is required. In crushing-efficiency calculations on crushing tests it is customary, when basing the calculation on Kick's law, to assign ordinal numbers to each standard sieve size. These ordinal numbers increase by a constant difference with each successive sieve aperture, because standard sieve apertures are in constant ratio. Minus 200-mesh is generally assumed as equivalent to 37 microns in size. By definition, the ordinal number multiplied by the per cent material of any size is equal to the energy units in the material of that size in a unit weight of sample. The sum of all energy units is the energy units content of a unit weight of sample, whether it be crusher feed or product. The difference between the energy units in the product and that in the feed is the tangible result of the work input per unit weight of feed. From this the amount of work necessary for one energy unit may be calculated. This has been done for a quartz crushing-test made at the Intermountain Experiment Station of the U. S. Bureau of Mines at Salt Lake City, in which the net work going to crushing was carefully measured. The results of this crushing test are given in Table 1.'

Jan 1, 1929

By S. W. Marcuson

In the late 1960's concerns about the natural environment reached high levels within North America and provided activists with suitable platforms for exerting influence over the general public and politicians. In response a host of regulatory mechanisms were developed, statutes, voluntary measures, land grants, codes of practices etc. Emerging environmental awareness from the era provided impetus for rapid technological change that encompassed all industries, especially the base metal business. The resulting clean up impacted all aspects of copper production, dealing with issues such as waste disposal, water and air quality with specific impact on emissions of sulfur dioxide and particulate. This paper provides a perspective of these changes reviewing the macro-economic impact of environmental movement in mining with its specific implications to the copper smelting industry. The fundamental challenges that were faced by the old, but capital-intensive North American plants and the approaches taken to deal with the changing times are reviewed with special emphasis on the conceptual approach to smelter S02 abatement and different paths taken in the USA and Canada. The role of economics, sustainable R&D and presence of technical infrastructure that facilitated the change process is elucidated, and speculations are made about the future state of pyrometallurgy and the natural environment. Cu2007 -

Jan 1, 2007

By G. H. Lewis

This work was completed in a 440 KW pilot-scale combustor in preparation for a 50,000 Kg/hr industrial steam boiler limestone injection test program. The main objectives of the work were to: (1) identify the variables which affect sulfur capture, (2) determine the maximum sulfur removal, and (3) determine the effect of limestone addition on furnace operability and heat transfer. The variables which were identified as being important in sulfur capture were: Ca/S molar ratio, flue gas temperature at the limestone injection location, and limestone particle residence time. The maximum sulfur dioxide removal was 72%. The addition of limestone increased the particle deposition rate in the combustor; however, all deposits were easily removed by an air lance.

Jan 1, 1985

By G. H. Lewis, C. L. Krcil, N. S. Harding, D. E. Havekotte

INTRODUCTION Limestone injection work was completed in a 440-kW (1.5-million Btu per hour) pilot-scale combustor in preparation for a 50,000-kg/h (110,000-lb per hour) industrial steam boiler limestone injection test program. The main objectives were to: (1) identify the important variables that affect sulfur capture, (2) determine the maximum SO2 removal, and (3) determine the effect of limestone addition on furnace operability and heat transfer. A more detailed report is given by Lewis et al. (1985). The test program was divided into two phases. The objectives of Phase I were to determine the important variables that affect SO2 reduction and to investigate the effect of limestone addition on combustor operation and heat transfer surfaces. The objective of Phase II was to determine, using only the important variables identified during Phase I, the conditions that resulted in the greatest sulfur dioxide reduction. Phase I Test program Using one limestone, five variables were identified as having an effect on SO2 reduction. These are noted with their respective ranges: heat release rate [103 to 166 kW/m3 (10,000 to 16,000 Btu per hour-cu ft)], Ca/S molar ratio (0 to 3), flue gas oxygen concentration (3% to 5%), additive particle size [90% -150 µm (-100 mesh) and 90% -45 µm (-325 mesh)], and burner stoichiometry (SR = 0.75 and >1.15). A 2.3% sulfur northern West Virginia coal, pulverized to a nominal grind of 70% -75 µm (-200 mesh), was burned for the tests. The limestone used was obtained from a Maysville, KY, quarry and contained 51.75% (wt) CaO. An 11-run statistically designed program (plus three duplicates) was used to screen the five variables. The effect of limestone injection on the combustor heat transfer surfaces was determined by comparing the heat transfer rates through a slag panel and fouling probes during periods with and without limestone injection. Combustor operation was determined by noting any operating problems that occurred during the tests. Test procedure After furnace wall temperatures had stabilized at operating conditions, heat transfer surfaces (slag panel and fouling probes) and the convection section were blown clean, and a four-hour test was begun. The

Jan 1, 1987

By D. A. Bordin, C. J. Newman, R. J. St. Eloi

"The requirements for a metallurgical acid plant treating smelter gases are both unique and demanding in terms of sulphur dioxide treatment and emission control. Since start up in 1981, the copper smelter at the Kidd Creek Division of Falconbridge Limited has undergone several major expansions. The expansion and modification of the acid plant has been an integral part of this process. Both production demands and government regulations dictate that this metallurgical acid plant be unique in terms of operating flexibility. The variable capacity to treat a wide range of sulphur dioxide concentrations, and the operating flexibility to control emissions are the topics of this paper.INTRODUCTIONThe Kidd Creek Division of Falconbridge Limitied is a base metal mining and metallurgical complex located in Timmins, Ontario. The discovery of the original copper-zinc-silver orebody was announced in April, 1964. Mining operations began in 1966 with a 9000 tonne per day concentrator coming on stream in November of that year. In April 1972, a 108 000 tonne per year zinc plant was commissioned. Over the years the facilities have been expanded, such that the concentrator now has the capacity to process 13 000 tonnes of ore per day . To expand zinc production, the world's second installation of the Cominco/Sherritt pressure leaching facility was completed in 1983 to bring total zinc production capacity to 125 000 tonnes per year. In 1973, serious planning for a smelter operation began. In early 1975, after studying both continuous smelting and flash smelting processes, a decision was made to proceed with the technology offered by Mitsubishi Metal Corporation of Japan. The Mitsubishi Continuous Smelting Process was to be used for the smelter and the Onahama No.3 tankhouse technology for the copper refinery.The smelter, which uses the Mitsubishi Continuous Smelting Process for the continuous production of blister copper from concentrate, went on line in June 1981. It has been expanded from its original capacity of 60 000 tonnes to 100 000 tonnes per year of copper.From the very early design stages for the metallurgical complex, the company had adopted a policy of constructing and operating modern plants which would meet existing and anticipated environmental standards. With this in mind, the decision was made to utilize the proven technology of fixing sulphur dioxide emissions, in the form of sulphuric acid. A 636 tonne per day single absorption contact acid plant was built to serve the zinc plant in 1972. In 1981, an 883 tonne per day double absorption contact plant was built to serve the needs of the copper smelter. The copper smelter acid plant has since been expanded to a design capacity of 1692 tonnes per day and it is the main focus of this paper."

Jan 1, 1989

By Mao Chen, Baojun Zhao, Zhixiang Cui, Leonel Contreras, Chuanbing Wei

Bottom blown oxygen copper smelting process developed at Dongying Fangyuan Nonferrous Metals shows many advantages such as flexible feed requirement, high productivity, low energy consumption and high direct copper recovery. However, the weak acid generated during the process is not stable which influences the waste management and continuous operation. The amount of the weak acid is determined by SO3 formed in copper smelting process. SO3 can be formed inside copper smelting furnace and boiler at different conditions. Effects of temperature and oxygen partial pressure on the formation of SO3 during copper smelting process have been discussed thermodynamically. Understanding of the mechanisms for SO3 formation will enable the operation of bottom blown copper smelting furnace to be optimized and generation of the weak acid in the process can be managed. The fundamentals developed in this study can also be applied to other copper smelting processes.

Jan 1, 2016

By Will H. Coghill

FLOTATION has been so closely allied with the sulfide minerals and their early and associated oily reagents that the term "oil flotation" has erroneously been applied to the entire flotation process. Today, the term "chemical flotation" might be used to advantage. Flotation literature has dealt primarily with the removal of sulfides. from non-sulfide gangues, and the separation of one sulfide from another.. Now, the application of the process to the separation of nonsulfide minerals is coming to the fore; and from the standpoint of the number of commercial minerals involved, the flotation of nonsulfides offers the larger field. Here, soap or soap-forming substances, such as the fatty acids and their derivatives, are used; hence there may well be a subdivision of the chemical flotation process called "soap flotation." Early experimenters learned that it was easy to form a froth or foam that would carry a part or all of the ore charge over the lip of the flotation machine; but this could not be regarded as flotation because of the lack of selectivity. Doubtless soap was one of the first reagents tried, and doubtless it was rejected on account of its gangue-carrying properties. Now this same gangue-carrying ability makes soap an acceptable reagent, for we are dealing with that, which among sulfides, is considered "gangue." As in the flotation of sulfides, so in the flotation of nonsulfides, the selective flocculation of the mineral and the dispersion of the gangue are the first objectives. In fact, these two phenomena epitomize flotation. They depend upon the unlike surface properties of the respective minerals; and, as long as the components of an ore have unlike surface properties, a separation is possible, at least in theory. Often in nonsulfide flotation it makes little difference which mineral floats and which is depressed; generally only a separation is sought.

Jan 1, 1932

By Will Coghill

FLOTATION has been so closely allied with the sulfide minerals and their early and associated oily reagents that the term "oil flotation" has erroneously been applied to the entire flotation process. Today, the term "chemical flotation" might be used to advantage. Flotation literature has dealt primarily with the removal of sulfides from non-sulfide gangues, and the separation of one sulfide from another. Now, the application of the process to the separation of nonsulfide minerals is coming to the fore; and from the standpoint of the number of commercial minerals involved, the flotation of nonsulfides offers the larger field. Here, soap or soap-forming substances, such as the fatty acids and their derivatives, are used; hence there may well be a subdivision of the chemical flotation process called "soap flotation." Early experimenters learned that it was easy to form a froth or foam that would carry a part or all of the ore charge over the lip of the flotation machine; but this could not be regarded as flotation because of the lack of selectivity. Doubtless soap was one of the first reagents tried, and doubtless it was rejected on account of its gangue-carrying properties. Now this same gangue-carrying ability makes soap an acceptable reagent, for we are dealing with that, which among sulfides, is considered "gan-gue." As in the flotation of sulfides, so in the flotation of nonsulfides, the selective flocculation of the mineral and the dispersion of the gangue are the first objectives. In fact, these two phenomena epitomize flotation. They depend upon the unlike surface properties of the respective miner-als; and as long as the components of an ore have unlike surface proper-ties, a separation is possible, at least in theory. Often in nonsulfide flotation it makes little difference which mineral floats and which is depressed; generally only a separation is sought.

Jan 1, 1932

By C. W. Ryan

THIS paper contains a brief sketch of the geology of soapstone in the Piedmont section of Virginia, in the southern portion of Nelson County; also a description of methods of prospecting, developing quarries, quarrying and and milling methods in that section. The paper is intended for those who have little information regarding soapstone; undoubtedly men of practical experience will find many points for criticism.

Jan 1, 1929

By Georg Petersen

Uno de los principales problemas económicos en el Perú es el aprovechamiento del recurso de aguas subterráneas que están confinadas en diferentes reservorios en los valles de las Costa y fuera de ellos. En este sentido, el presente texto describe el origen de las aguas subterráneas - en tanto depende del clima y condiciones, así como su aprovechamiento. Las condiciones del agua subterránea que existen en los valles de ríos permanentes, varían entre la Sierra y la Costa. Finalmente, el aprovechamiento de las aguas subterráneas se practica por pozos tubulares o revestidos de ladrillo o concreto. En los valles de los ríos Rímac, Chincha y Nazca se han construido también galerías filtrantes de gran extensión. En Nazca, este sistema ha sido en uso ya en tiempos pre-coloniales.

Nov 1, 1959

By George Petersen G.

El siguiente texto describe la genealogía de la pegmatita, composición, precios y las regiones compuesta de este mineral en el litoral peruano. Las pegmatitas son rocas ígneas que se forman al enfriarse la magma, constituyéndose en un etapa de transición y sistema mixto entre los depósitos líquidos magmáticos. Su textura es de grano grueso y está asociada a las rocas ácidas como el granito y la granodiorita. De acuerdo a su genealogía se dividen en dos grupos: facies pegmatítico-magmática y enumatolítica. Las pegmatitas del litoral peruano contiene minerales no metálicos como ortoclasa, mica y cuarzo. Las zonas que comprenden mica son Matarani. Quilca y Atico (Arequipa), la zona de feldespatos se encuentra en Samanco (Chimbote), y la zona de cristal de roca y minerales radioactivos, en la región de Casma (Ancash).

Jul 20, 1961

By George. Petersen

"El trabajo refiere algunos aspectos del depósito de estaño en el yacimiento de Condiriquiña (Puno), como en zonas de Apurimac, Lima, Pasco, Ancash, Cajamarca del Perú. Se conoce que los principales depósitos de estaño provienen de los ramales cordilleranos de Bolivia, abarcando una serie de yacimientos. En vista de una posterior demanda del producto, fue necesario que el Perú inicie una exploración de este metal en territorios adyacentes a Bolivia. Sin embargo, las exploraciones no se concretaron más que a las inmrediaciones del lago Titicaca. Posteriormente se descubrió minerales de estaño en diversas partes de nuestro territorio,aunque que ningún depósito explorado tenga un resultado de valor económico-industrial considerable. El aspecto geoquímico del estaño no tiene relaciones con el fierro, cromo, silicio, careciendo de estaño en los depósitos líquidos magmáticos y en las rocas ígneas de naturaleza básica. Durante los procesos metalogenéticos el estaño se concentra y constituye un elemento característico de la cristalización residual; presentándose tanto en el alcance neumatolítico ácidocomo en el hidrotermal. En consecuencia, los depósitos de estaño son de origen neumatólítico, cuyas masas y filones de catiserita están asociados con un batolito de granito, de edad oligocénico. Así, las rocas encajonantes consisten en pizarras y cuarcitas de Ordovicito, se transforman en rocas greisen o ígneas. Finalmente, los depósitos estanníferos se clasifican según sus alcances genéticos en depósitos supergenos e hipogenos, los cuales se dividen en depósitos pegmatítico, neumalotílicos, de transición neumatolíticos-hidrotermales y los depósitos hidrotermales."

Jul 20, 1959

By Jorge Injoque Espinoza

El presente trabajo describe la mineralogía de la plata, cobalto, níquel y oro en los principales depósitos de cobre y hierro de la faja costera. Para la descripción de los depósitos se revisan los trabajos de Injoque, así como en diversos estudios de mineragrafía, microsonda y geoquímica.

Nov 1, 1985

Las primeras exploraciones de la atmósfera Jibrese se iniciaron en 1934 por medio de los vuelos a alturas de 6,000 m. y globos pilotos. En 1938 J. A. Broggi, G. Petersen G. y G. H. Wagner practicaron una serie de ascenciones de globos pilotos. En ese sentido, se describe una reseña histórica y una interpretación de las cuatro capas de vientos al ser observados sobre Lima (Perú) y datos sobre las temperaturas observadas en las alturas de 6,000 y 12,500 m.

May 1, 1958

By Benjamín Leiding Valdés

"Ante la demanda industrial del cobre en el desarrollo minero, se hace necesario revisar su proceso de producción y repercusión a nivel mundial y peruano. Por tanto, el objetivo del texto describe algunos aspectos de su rentabilidad desde 1947 hasta la actualidad. De acuerdo a este último año de estudio, EE.UU. mantiene el liderazgo de producción con 29%, Chile, ocupa el segundo lugar con 14%, Rodesi, en el tercero con 12% y el cuarto lugar lo disputan Rusia y Canadá. Así, la producción norteamericana de cobre al igual que la chilena se ajusta a las demandas de consumo, mientras que la de los tres países restantes va en ascendencia. De otro lado, la mejoría de precio a nivel mundial, permitió que el conjunto de los demás países restantes ocupe el 18% de la producción, destacándose entre ellos Perú, Japón y México, seguidos de Unión de Sud África, Felipinas, Yugoeslaviay Chipre con más de 40 mil toneladas de producción de cobre. Asimismo, de acuerdo al aprovechamiento del plan de extensión, la distribución de la producción mundial del cobre primario ha mejorado tanto que en 1956 sobrepasó el consumo, aunque mantuvo su auge de precio. Sin embargo, en 1958 dicha situación cambió por el agotamiento de las reservas, ocasionando un perjuicio para los primeros países productores y un aumento para los últimos. En este sentido, los pequeños productores se convierten en las fuentes de producción de la última década, ubicando a Chile y Perú como los principales productores en América Latina. La producción chilena proviene en un 90% de su gran minería y en el 10% de su mediana y pequeña minería y sus principales mineras son Chuquiquimata en Antofogasta, El Teniente en O' Higgiins y El Salvador en Atacama. Mientras que la producción cuprífera peruana se ha duplicado en los últimos 10 años, sobrepasando las 65 mil toneladas por año. La gran minería de cobre en el Perú se inicia en los últimos años a través de la explotación del yacimiento minero de Toquepala, perteneciente a la Southern Perú Copper Corporation, estimando una reserva de 500 millones de toneladas de minerales de 1% de cobre por mes. La minería mediana peruana de cobre se encuentra en las minas de Cerro de Pasco y Morococha, en Junín, donde los minerales son concentrados y posteriormente fundidos en La Oroya. En conclusión, tanto Chile como Perú se constituyen como los dos más grandes productores de cobre sudamericanos que contribuyen al abastecimiento del mineral en este continente como en Europa, Estados Unidos y Norteamérica, no solo por sus reservas sino por la bondad de sus yacimientos. ."

Jul 20, 1959