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By J. Oyunaa, P. Munkhbaatar, A. Sarnai

"The molybdenum mining process used at Mongolia Erdenet Company is a selective flotation of molybdenite from the copper porphyry ores in which the extraction of molybdenum comes as a byproduct of the ongoing copper production.The mineralogical composition of molybdenum concentrate is 99.4% molybdenite (MoS2), 0.09% molybdenum oxide (MoO3), 0.52% powellite (CaMoO4) and wulfenite (PbMoO4) and content 47.76– 47.92% molybdenum, 1.5–2.67% copper, 0.04% renium.From compared solvents sodium and carbonate and ammonia are like extracted molybdenum than hydrochloric acid, which contained 96.23–97.72 p.c. of its total amount. Hence to take into consideration abundance, cheap and suitable for analysis and processing the molybdenum concentrate ammonia is choosing as a basic solvent. By direct evaporation of ammonia extract solution, we obtained ammonium ortomolybdate, which contains 73.47% MoO3. INTRODUCTIONMolybdenum occurs in the earth’s crust in an abundance of about 10–14%, mainly as molybdenite, MoS2. Small quantities are also associated with other metals having similar chemical properties. Thus wulfenite (PbMoO4) is found in oxidized parts of sulfidic lead deposits in many regions of the world; powellite [Ca(Mo,W)O4] is a calcium molybdate usually formed from the modification of molybdenite in deposits containing tungsten as scheelite (CaWO4) and tungsten substitutes for molybdenum up to about 10%. Ferrimolybdite (Fe2Mo3O12·8H2O) is the product of oxidation of molybdenite in the presence of iron (III) compounds. Molybdenite is the primary source of molybdenum. Should demand for molybdenum rise so that additional sources become necessary, wulfenite, powellite, and ferrimolybdite may become commercially significant. Molybdenum ore is mined by underground and open-pit methods. A typical primary molybdenum ore body contains 0.05–0.25% Mo, and secondary ore bodies (copper porphyry ores) average 0.3–1.6% Cu and 0.01–0.05% Mo. Flotation remains the preferred and almost exclusive method of upgrading the molybdenite mineral to an industrial-grade molybdenite concentrate containing 90–95% MoS2, the balance being gangue (Habashi, 1997)."

Jan 1, 2016

By David Gwyther

There is increasing recognition that in order for a development project to proceed successfully, it must first obtain a ?social licence to operate? from concerned stakeholders. Obtaining this ?licence? is in many ways a separate process to the legal one which involves, among other things, submitting an environmental and social impact assessment (ESIA) to the appropriate regulatory authority for review. Essentially, the function of an ESIA is to present a project?s technical, financial and social benefits, together with its environmental and social impacts in a transparent way to enable regulators to make an informed decision about whether the benefits outweigh the impacts, and thus whether or not the proposed project should proceed. The focus in the early days of ESIAs was primarily technical and was aimed to answer two fundamental questions: ?Can the project be built?? and ?Can we minimise impacts to a level that is acceptable to the community?? Basically, the ESIA process was a technical test of competence, but more recently, ESIAs have become much more than this. The main ESIA risk is now more akin to a test of a project?s legitimacy ? i.e., with more weight placed on the social licence, or the political test of moral authority ? with the process involving stakeholders from multiple backgrounds and disciplines, including some anti-development NGOs/civil society groups with their views on mining, (particularly in developing nations), often already pre-determined. Within the backdrop of this potential maelstrom, now enter a proposal for a new industry (such as deep sea mineral extraction).

Jan 1, 2011

By Steven McCutcheon

As most of us have learned through prior and often frustrating experience, anyone proposing to construct a new or expanded mining-ore processing facility must first contend with a rather complex array of environmental laws and permitting regulations administered by a number of different Federal, State and local agencies. At our lost count, there were about 55 federal enactments affecting base and precious metals projects. Applicable State and local laws will usually increase that number significantly. The time and costs associated with complying with all these various regulatory programs usually constitutes one of the major areas of uncertainty in the development of a proposed project. There are many in the mining industry who firmly believe that these environmental regulation and permit programs necessarily causes significant delays and increased costs in the development of a project. This belief, unfortunately, is probably a result of a basic misunderstanding of how the environmental permitting and regulatory system actually works.

Jan 1, 1984

By Theodore H. Eyde

In 1971, the Minerals Division of The Superior Oil Company acquired exploration rights to an unpatented claim group in the Superior (Pioneer), Arizona mining district, lying west of the Concentrator fault. This major post-mineral fault displaces the Magma vein-fault, which is mined in the Magma Mine at Superior, Arizona. The Magma vein-fault and the enclosing section of pre-mineral rocks consisting of Paleozoic and younger Precambrian sediments and diabase, is overlain by a thick section of post-mineral rocks, consisting of the Gila conglomerate, the Apache Leap dacite, and the Whitetail conglomerate. Geologic information on the thickness and attitudes of the rocks obtained from previous diamond drilling indicated that the section of post-mineral rocks might be from 3,000 to over 4,010 feet thick in the target area. (Figure 1) The Magma vein-fault is a steeply dipping vein which has produced nearly a billion dollars of copper, zinc, silver, and gold. It has been mined continuously for nearly 10,000 feet along the strike and nearly 5,000, feet vertically down the dip. It ranges from less than a foot to over 50 feet wide and contains sulfide mineralization con¬sisting of pyrite, chalcopyrite, bornite, and chalcocite.

Jan 1, 1973

By Theodore H. Eyde

The Superior Oil Co. drilled two holes, 4720 and 5940 ft, respectively, using conventional oilfield rotary drilling equipment. The results indicated that large rotary drills can be adapted to mineral exploration purposes with few modifications. The principal advantages are: a large hole diameter, excellent samples of cuttings, a geolograph which is a constant drilling record, rapid penetration even in hard rocks, and the ability to use electric logs for measuring the properties of the rock being penetrated. The disadvantages are the high cost of mobilization, drilling, and oilfield service at remote locations. Though the oilfield sampling techniques are adequate for identifying lithology, improvements are necessary to obtain representative samples for analytical purposes. As deeper targets are explored, mineral exploration organizations will have to resort to rotary drilling.

Jan 1, 1975

By A. Eltringham

Operations downstream of mining and beneficiation are still being subjected to increasing scrutiny as highly capitalized projects have been either slow to achieve their targets or have actually failed to do so. Leaching and smelting projects have fundamentally high calls on capital and technology as reaction rates are increased and the capture and disposal of unwanted products are subjected to greater restrictions. Separating value from waste inherently becomes riskier as the purification of the desired product imposes greater demands on the process to produce benign wastes. When we superimpose on the chemistry of the project severe predictions of throughput rates, that bring in facets of manufacturing, we are introducing complexities that the records show are not handled well. This paper discusses some of the more common challenges that operators face and what methods are available and are likely to be successful in preventing the loss of value as projects are brought on-stream. This thinking needs to start much earlier and at greater intensity than our industry has normally chosen to employ.

Jan 1, 2011

By Nilce Alves Santos, Vânia Lúcia de Lima Andrade, Keila Lane Carvalho Gonçalves, Harold Wyslouzi1

"When confronted with the difficult decisions on advancing an exploration project to the feasibility and construction stages, it is important to know how various regions of the ore body will react in the milling and concentration processes. While bench scale test work is common and inexpensive, the results and information provided are somewhat limited due to the difficulty in accurately predicting the effects of recirculating middling streams or gradual changes in solution chemistry.Conventional Pilot Plants, processing 100 to 1,000 kg/hour of sample ore, provide the detailed engineering data required to develop a final process flowsheet and to size the equipment. They are, however, expensive to set-up and operate, and are really only viable for major projects that are well advancedIn the latter part of 1999, the Mineral Development Center at CVRD (MDC) purchased a new piece of mineral processing equipment which can run continuous flotation tests using drill core samples. To evaluate its performance, and to compare it with conventional testing methods, various types of flotation tests were carried out using two different types of copper ore. The limitations and advantages of open circuit and locked cycle bench tests, as well as the Mini Pilot Plant and the Conventional Pilot Plant were evaluated.Open circuit tests carried out at the bench scale only provide basic information. More complete and trustworthy information is obtained, in terms of the recirculation of flows and reaching a permanent and stable flotation regime, as the dynamics and complexity of the tests increases. The data obtained showed that the MPP’s metallurgical performance was equivalent to that of a conventional pilot plant."

Jan 1, 2002

By Katia Vutova, Vania Vassileva

Investigations and results on the refining of tungsten scrap applying electron beam melting (EBM) in vacuum are presented and discussed. In this work EB melting experiments were performed in single or double-melt operations with different power inputs and refining times for tungsten purification and recovery of multiple metals (including refractory and other metals such as Mo, Nb, Cu, Zn, etc.), which are alloyed elements or impurities with high concentrations in the initial materials. Evaluations for extraction of some valuable metals, generated in the condensate at their removal from the liquid metal during the refining process are provided. Efficient technological regimes for e-beam melting and refining that enable the simultaneous production of pure metal ingots and condensates that can be used directly or can be used for subsequent extraction of expensive and valuable metals are presented.

Jan 1, 2016

By J. Botula

In the region of the North-Bohemian Coal Basin and its environment, there, in a row of places, are found the accumulations of rocks of the sedimentary and pyro clastic origin, the preliminary composition of those shows the possibility of their being utilized for the production of ecologically sparing natural Fe- and Ti- pigments and filling substances. In many places of the regions of Chomutov and Podborany and near Bilina and also in other places, there are found raw stocks perspective for the preparation of yellow up to ochre-brown, red, brown-red and green dyes. The target of project is the verification of dispensable reserves, their mineralogical composition and chemical and physical attributes, verification of treatment ways of Fe-and Ti-pigments separation (hydrocyclones, magnetic and electrostatic separation) and their stabilization and technological painting attributes for applications in colors, coating and plastic masses, mortar mixtures etc.

Jan 1, 2014

By A. N. Zagorodnyaya, Ye. G. Bochevskaya, E. A. Sargelova, Z. S. Abisheva, A. S. Sharipova

"In Kazakhstan, there is a unique sulphide copper deposit, in the ores containing the natural isotope of osmium-187 (more than 90 %). In the pyrometallurgical processing of concentrates for the target metal, osmium is mainly sublimated, with wet cleaning of metallurgical gases (dust and gas mixture) 40 % of it together with rhenium passes into washing solutions (wash acid). On the basis of this acid, the production of ammonium perrhenate was organized at the enterprise of the RSE ""Zhezkazganredmet"" and for the first time in the world practice - the isotope of osmium-187. However, the degree of its recovery from solutions does not exceed 8 % of the amount supplied with the charge or 25 % of the amount that was received for extraction. But the bulk of it (~ 75 %) remains in the raffinate, discharged to sewage treatment plants (wastewater). The studies presented in this work are aimed at solving the problem of osmium isotope-187 extracting from wastewater, which are a potential source of increasing metal production in Kazakhstan. The aim of this work is the development and scientific justification of osmium deposition regimes from wastewater using such reagents as thiosulfate and sodium sulphide. The influence of various physicochemical factors on the precipitation of the osmium was studied and optimal conditions for its maximum transition to sediment were chosen. An original method for obtaining osmium concentrate in the presence of sodium thiosulfate with the addition of potassium iodide from a new type of wastewater - man-made ammonia solutions has been developed. These solutions were combined mother liquors of solid-phase stripping operations and dissolution of pulp of crude ammonium perrhenate. On the basis of the obtained results, a settling technology for extraction of the osmium from man-made ammonia rhenium-containing solutions was introduced at RSE ""Zhezkazganredmet"". It should be noted that the degree of extraction of osmium, depending on its concentration in solutions entering on the settlement, and taking into account the addition of sulfuric acid, will vary from 60 to 90 %. The recovery of osmium during the test period was 58 %."

Jan 1, 2018

By J. P. Harrison, N. Bozorgzadeh, M. Dolowy-Busch

"It is common in rock engineering practice to characterize the triaxial strength of intact rock by using only data samples of small size. Practical guidelines such as ASTM support such sample sizes. In this paper, we investigate the reliability of the Hoek-Brown strength criterion estimated from such samples. For this purpose, we use an unusually large published set of triaxial strength data to randomly select a large number of data samples of small size to simulate the situation that frequently encounters in practice. The samples are generated with different arrangements with regards to the confining pressure. We fit the Hoek-Brown criterion to each of these samples, obtain estimates of strength parameters and compare them to those obtained from the complete data set. Our analysis suggests that estimates based on small samples are not reliable and can lead to both over- and under-estimation of strength.Additionally, we use these small samples to investigate the statistical methods for obtaining design values of strength as suggested by limit state design standards such as Eurocode 7. We show that, if used in conjunction with small samples, these methods do not guarantee a safe estimate of strength and in many cases lead to highly over-conservative estimates.We present a potential solution to this problem by augmenting the small data sets with Bayesian informative priors to give much more reliable estimates of strength. We conclude with suggestions for the development of informative prior distributions."

Jan 1, 2015

By O. J. R. Baena, D. E. Chaverra, C. D. L. Ramirez

Cyanide is one of the most used reagents in the precious metal extraction process; as well as the most efficient from the point of view of the dissolution process; but it is also a toxic product that requires a lot of care in handling. Likewise, the residual solutions of the process must be followed because they can be a risk of contamination of water, animals and human health. In the artisanal processes of obtaining gold and silver, neutralization of the residual solutions is used to passivate the present cyanide. During this process ammonium cyanate is formed which decomposes rapidly in the presence of air and sunlight in carbon dioxide and ammonia gas, contributing to the greenhouse effect. In this work the use of the ammonium cyanate obtained in the process of neutralization of the cyanide solutions as a reagent to obtain urea is proposed. Urea was obtained indirectly through the use of the reagent kit UREA/BUN-COLOR. The process is effective at pH ≤ 4.5 with a rapid increase in solution temperature, and addition of hydrogen peroxide. The urea crystals begin to form at 50°C. The cyanide / urea ratio obtained was 1 / 7.5 INTRODUCTION In the processes of extractive gold metallurgy, the use of cyanide leaching is perhaps the most widely used method worldwide; by the ease of operation, its low cost and high levels of precious metal recovery. However, neutralization, in most processing plants, is not done properly, and leftovers of solution with free cyanide are dumped in concentrations harmful to the environment, in particular animals and humans. Cyanide can enter surface water through releases from industries using cyanides. Due to its high toxicity, the presence of cyanide in water is a matter of great concern (Jawale et al., 2017). The pollution generated by the effluents from the leaching of gold ores is one of the main obstacles of social opposition presented by mining activity due to the impact of both surface and groundwater. During the cyanide decomposition process, a compound known as ammonium cyanate OCN(NH4), which is a raw material for the manufacture of urea, CO(NH2)2 is generated. In the case of good neutralization, cyanide is no longer a toxic compound through oxidizing reagents, but as a result, there is the generation and emission of ammonia and carbon dioxide into the atmosphere, generating both a greenhouse effect (Gómez, 2012). This is evidenced by the strong effervescence of the reaction, and a penetrating smell of ammonia, which can irritate respiratory mucous membranes and eyes; however because they are greenhouse gases they are considered pollutants.

Jan 1, 2019

By Daniel Lovera, Freddy Sojo, Edwin Manrique

El agua de mina es un problema constante en las empresas minero metalúrgicas debido a su alta acidez y contenido de iones disueltos. Esto ocasiona constantes desembolsos para su tratamiento antes de ser desechado. Mientras los concentrados de cobre por su alto contenido de calcopirita requieren del proceso de tostación para recuperar el cobre valioso generando emisión de gases contaminantes. En esta investigación se emplea 4 soluciones de lixiviación con el agua de mina como componente principal y diferentes concentraciones de cloruro de sodio (NaCl), nitrato de sodio (NaNO3) e hipoclorito de calcio (Ca(ClO)2). El concentrado empleado contiene principalmente calcopirita.

Sep 29, 2023

By Steven D. Botts

El presente texto describe el proceso de obtención de permisos y licencias del proyecto Antamina desarrollado en el Perú. En este sentido, el compromiso de construir y operar el proyecto con pleno cumplimiento de la ley peruana de parte de la Compañía Minera Antamina, estableció la base para una relación productiva con las autoridades reguladoras y los participantes locales. Para ello, se requirió de un esfuerzo concertado para identificar la totalidad de permisos requeridos, determinar los procedimientos adecuados a seguir, educar a las autoridades, proporcionar el apoyo logístico requerido y los participantes la información sobre el desarrollo del proyecto, con la finalidad de sustentar el proceso de obtención de permisos. En consecuencia, la experiencia del proceso del proyecto demostró que el diálogo y la participación de la comunidad genera impactos positivos en el cronograma de su construcción y evita el conflicto social a futuro.

Jul 31, 2003

By Bertha Farfán del Carpio Vera

En este resumen se presenta los estudios iniciales que nos permitirán descubrir nuevas propiedades de estos 2 elementos, al ser transformados en áridos livianos, cuando luego de un proceso de precipitación química y a través de la catálisis heterogénea, son depositados en una sustancia de soporte conocida como zeolita clinoptilolita. Ambos metales Pb y Zn, adhieren totalmente a la zeolita, la cual se comporta como un catalizador metálico dispersado, siendo los metales Pb y Zn, los que se depositan sobre la anterior pasta para formar los pellets.Luego de mezclarse completamente, el soporte y el material catalítico se compactan, se someten a un proceso de extrusión.

Sep 1, 2017

By Jacinto Sack Arzola

El presente trabajo señala el proceso de obtención de zinc en la refinería de Zinc Minero Perú, cuya primer barra la obtuvo en 1981 e inició su producción en 1982. Asimismo se describe el diagrama de flujo de la planta electrolítica de zinc, donde el tratamiento de los residuos lixiviados de zinc se desarrolla a través del método jarosita, cuya purificación de la solución de sulfato de zinc es contínua y se desarrolla en dos etapas: la electrodisposición que se realiza en cátodos tipo jumbo,, y el manipuleo y deslaminado de los cátodos que son semiatomáticos.

Nov 8, 1982

By Leonardo Pereira

Este trabalho reporta a viabilidade de realizar o tratamento térmico de austêmpera, para obtenção de um Ferro Dúctil Austemperado (ADI), utilizando uma liga de Zn-Al-Mg-Cu, como meio de resfriamento e permanência em patamar, durante o processo de tratamento térmico. Por meio da obtenção da curva de resfriamento da liga Zamac 5, constatou-se a viabilidade de realização da austêmpera em temperaturas superiores a 380ºC. A partir de corpos de prova de ferro fundido nodular de matriz predominantemente perlítica, instrumentados e austenitizados a 870°C e 900°C, avaliou-se a taxa de resfriamento promovida pela liga Zamac 5, até a temperatura de 400°C. O tratamento mostrou-se eficiente, utilizando a liga como meio de austêmpera, sendo registradas taxas de resfriamento superiores a 6°C/s. A análise morfológica constatou a formação de ausferrita, sem a presença de perlita, caracterizando assim a formação do ADI.

Oct 30, 2017

By Maria Cristina Yukiko Nakayama

Este trabalho estuda a obtenção do cobalto metálico a partir da redução de pós de óxido de cobalto (Co3O4) usando como agentes redutores o plasma frio de hidrogênio e o gás de hidrogênio. A redução a plasma foi realizada sob tensão de 540 V e largura do pulso na faixa de 140-170ms, e da mesma forma que na redução a gás foram usadas as seguintes condições: fluxo de 300 cm3/min de hidrogênio, pressão de 530 Pa, temperaturas de 250º, 300ºC, 350ºC e 380ºC e tempos de 10 a 120 min. Os resultados mostraram que o processo de redução ocorre em duas etapas: Co3O4?CoO?Co. Na parte mais externa das partículas parcialmente reduzidas verificou-se a presença de altas concentrações de cobalto e no centro das mesmas, altas concentrações de oxigênio, o que indica que a redução se dá da superfície para o núcleo. Constatou-se que em 300oC após 120 min é possível obter frações de metal reduzido aproximadas de 0,93 quando é utilizado o plasma frio de hidrogênio, enquanto o gás permite obter frações de apenas 0,3. A energia de ativação para a redução por plasma de hidrogênio é de 35,38 kJ/mol, ao passo que a associada ao gás de hidrogênio é de 90,79 kJ/mol.

Aug 16, 2017

By Andre Luiz Nunis da Silva

Didímio metálico foi obtido no Instituto de Pesquisas Tecnológicas do Estado de São Paulo, a partir do óxido de didímio, o qual foi produzido pela extração por solventes de óxidos de terras raras do concentrado obtido na mina de nióbio da Companhia Brasileira de Metalurgia e Mineração - CBMM. Foram investigadas duas rotas tecnológicas, metalotérmica e redução eletroquímica, ambas ocorrendo em sais fundidos. Foi possível produzir didímio com um mínimo de 99 % de pureza por ambas as rotas, mas a rota metalotérmica demanda uma etapa de processamento adicional para remover impurezas e agentes redutores.

Oct 30, 2017

By Mateus Alves Segundo Paulino

No estudo de escórias de fornos elétricos a arco (FEA), o sistema CaO-SiO2-MgOFeO se destaca em importância quando os temas são a proteção aos refratários básicos e a produção de ‘escória espumante’. A importância da obtenção da escória espumante no FEA reside no fato reconhecido de que ela traz diversas vantagens para a produção de aço, tais como: economia considerável de energia elétrica, proteção de painéis, redução de ruído, redução no consumo de eletrodos, etc. Levando-se em conta que diversos fatores ligados à composição química são de grande importância na produção e estabilidade de bolhas de CO, neste trabalho diferentes diagramas de fase são produzidos como ferramentas para a previsão da composição das escórias mais favoráveis para a formação da espuma. São consideradas na investigação algumas características relevantes encontradas no FEA tais como: basicidade da escória, temperatura de 1.600°C e teores de FeO e MgO variáveis (que refletem os diversos níveis de oxidação do banho).

Jul 30, 2018