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By J Seppelt, G S. Lane, E Wang

Newcrest’s Cadia concentrator operated from 1998 to 2012 with a traditional SABC grinding circuit treating Cadia open pit ore. The Cadia comminution circuit was well characterised through surveys and data that are available in the public domain, and became a benchmark standard for the industry and practitioners modelling large SAG mill based circuits. In 2012, the HPGR-based crushing circuit was introduced in front of the SAG mill to increase throughput when treating the Cadia East ore that was derived from an underground block cave. This ore was expected to be more competent and have a coarser run-of-mine size distribution.Numerous previous papers have described the design and commissioning of the Cadia HPGR-based circuit.This paper describes the improvement in comminution energy consumption resulting from the introduction of the HPGR, including identifying the impact of process complexity and an increase in ancillary energy consumption for conveyors, screening, and crushing.CITATION:Lane, G S, Seppelt, J and Wang, E, 2018. Quantifying the energy efficiency transformation at Cadia due to HPGR crushing, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 141–152 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By F Shi, W Huang, D Seaman, K Runge

High Voltage Pulse (HVP) technology is a novel process that could potentially be the step-change needed in ore processability in the mining industry. The propensity of high voltage pulses towards mineral-enriched ore particles during treatment makes this technology selective and has the potential to enable ore pre-concentration by size separation. In this study, the potential for pre-concentration of a low grade copper-gold ore sample subjected to HVP pretreatment is investigated and compared to that achievable after mechanical breakage in JKMRC’s rotary breakage tester (JKRBT). The data show that a better pre-concentration result can be achieved after HVP processing than conventional breakage. The gold pre-concentration potential is much better than that observed for copper. 4D HVP pre-concentration characteristic curves were produced to assess the metallurgical performance possible as a function of energy input. The case study shows that when targeting a nominal metal recovery of 90 per cent for gold, the HVP pre-concentration technique can split the low grade ore (0.9 ppm gold and 0.28 per cent copper in the feed size 26.5-37.5 mm) into two components – a low grade oversize material (0.3 ppm gold and 0.15 per cent copper) and a high grade undersize material (1.0 ppm gold and 0.3 per cent copper). The mass split to the low grade is 23 per cent. Under this mass split scenario, gold recovery to screen undersize is 90 per cent and copper recovery is 85 per cent. The HVP treatment of this feed size requires a specific energy (spark) of 2.8 kWh/t.There is further research that would be required before industrial uptake of the HVP pre-concentration technology would be possible. This paper also outlines the research challenges that need to be overcome.CITATION:Huang, W, Shi, F, Antonio, C, Runge, K and Seaman, D, 2018. High-voltage pulse pre-concentration study using a low-grade copper-gold ore, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 327–338 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By B Lumsden, R Smiles

Independence Group’s Jaguar Mine treats a polymetallic ore producing a copper concentrate and zinc concentrate. Effective separation of the sulfides requires relatively fine grinding with flotation feed P80 of about 75µm. Zn losses to final tails are greater than 60 per cent and <32 µm. When magnetic conditioning was first installed in 2010 it showed about an 8 per cent reduction of zinc in final tail and on some ores a similar benefit for silver as well. Current testwork is showing about a 12 per cent reduction in zinc and silver in final tail, consistent with the original testwork. Sizing of the final tail during the tests showed that the reduction of zinc and silver losses were only in the <32 µm fraction, as would be expected from an aggregation process. However, the most surprising result was about a 4 per cent reduction in zinc and silver in the plant feed with a >99 per cent statistical certainty. The reduction in zinc and silver in the feed is also only in the <32 µm fraction. Therefore, because the magnetic conditioning of Zn flotation feed cannot impact plant ore feed grade the hypothesis is that the magnetic conditioning is reducing the fine mineral from downstream processes, like filtering and thickening, returning to the plant feed in the recycled process water. This hypothesis is consistent with plant observation of dirty concentrate thickener overflow and measurements of solids in the overflow, as well as the average % Zn grade in cyclone overflow that correlates with the magnetic conditioning ON and OFF days. This paper presents these plant test results.CITATION:Smiles, R and Lumsden, B, 2018. Improving fine sulfide mineral recovery in Independence Group’s Jaguar Mine zinc circuit, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 433–440 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By G R. Ballantyne, V Souto, K Bartram

Particle sorting allows partially liberated minerals to be separated prior to energy intensive fine grinding. Sensors select particles for separation and air, water or mechanical ejectors are used to physically deflect those selected. To achieve effective separation there has to be sufficient liberation, accurate detection and presentation of a separated monolayer of particles. These three physical constraints determine the particle size limits, the sorting technology utilised, the separation efficiency, and the throughput that can be achieved. The combination of all these factors controls the effective limits on the degree to which sorting can reduce the specific comminution requirements and increasing energy efficiency. This paper will explore two case studies: the application of sorting in base metal mining and precious metal mining.CITATION:Ballantyne, G R, Hilden, M, Bartram, K and Souto, V, 2018. Characterising energy efficiency of particle sorting, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 531–540 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By J Geronimo, P Kumar, Z Yussupova, M Yahyaei, M Powell

This work goes beyond the general perception of how the well-known mine to mill process can be applied, by applying deeper knowledge along the mining chain. Grade deportment and dilution are considered at the mining stage, and modelled with the new SMI blast movement simulator, linking with the block model data. Assessing the shift to a considerably more competent section of the orebody is quantified via substantial milling trials at standard and higher-intensity blasts. These were stockpiled for batch processing through the mill to ensure feed integrity. The trial work included operating the mill at widely different fillings to develop Grindcurve milling responses. Additionally, model informed process control is initiated via a mill prediction tool.It has been found that accounting for blast movement for the higher intensity blasts could generate additional value of around $1.5M per blast. With the high-intensity blast and changing mill control, the plant was easily able to exceed projected mill throughputs with the far more competent Pipeline ore. Strategies to shift the workload and debottleneck the milling circuit were proposed and proven during the milling trials, demonstrating an increase in throughput of 7 per cent despite running at a lower SAG mill speed, and potential of 16 per cent for increasing the SAG mill to standard operating speed. A number of process improvement opportunities have been identified to enhance current productivity and ensure long term capability to process the considerably more competent future ores. All of this is being linked in with the major digitisation program at the Barrick Cortez site, with an objective of linking all the data into a mine-wide process optimisation system, that can embed the processes by providing process-wide data access and production support via the future dynamic models linking ore body knowledge to productivity along the full process chain.CITATION:Powell, M, Yahyaei, M, Geronimo, J, Yussupova, Z and Kumar, P, 2018. The designed approach to mill liner optimisation – experience at Pustynnoye mine, Kazakhstan, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 595–612 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By M L. Muller, A R. O’Donnell

The Mount Isa Mines (MIM) Copper Concentrator has an extensive history of reagent trials, with different reagents coming in and out of favour over the years. The research and use of carbon depressants is particularly prevalent, as carbonaceous pyrite is a major source of concentrate dilution. Years of research led to the use of naphthalene sulphonate due to its excellent carbon depression properties. However, due to rising reagent costs carbon depression ceased in the late 1990s. This led to the loss of knowledge about the use and value of naphthalene sulphonate. Cyanide is used at the Copper Concentrator for the sole purpose of pyrite depression and over the years multiple projects have been devoted to finding alternatives to it. In 2012 the neighbouring MIM Lead-Zinc Concentrator replaced cyanide with naphthalene sulphonate which resulted in cost savings and the elimination of a hazardous reagent. In 2013, plant trials were conducted at the Copper Concentrator in hopes to replicate the outcomes obtained at the Lead-Zinc Concentrator. The results of the trials conducted at the Copper Concentrator showed that naphthalene sulphonate could not replace cyanide and this work was set aside to pursue more promising projects. Further research conducted in 2014 found that mineralogy and a better understanding of the depressing mechanism of naphthalene sulphonate held the key to improved pyrite depression at the Copper Concentrator. The findings showed that Mount Isa copper ore contains two forms of pyrite; euhedral pyrite (cubic pyrite) and framboidal pyrite (carbon rimmed spheres of pyrite), both of which require different reagents to sufficiently depress them. Naphthalene sulphonate was found to be an excellent carbon depressant, suitable for depressing graphite and framboidal pyrite, whilst cyanide specifically targets euhedral pyrite.In 2015 laboratory test work was conducted to examine the use of naphthalene sulphonate in conjunction with cyanide to selectively target both forms of pyrite. This work led to a full plant trial, the results of which showed a significant increase in plant performance, with higher copper concentrate grades and recoveries being achieved. This paper aims to focus on the benefits and importance of understanding past work and linking a detailed knowledge of feed mineralogy to reagent selection for improved plant outcomes.CITATION:O’Donnell, A R and Muller, M L, 2018. Selectively targeting hydrophobic gangue minerals at the Mount Isa Mines Copper Concentrator, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 413–421 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By A Price, D Okle, K Brooks

The operation of flotation plants has been improved over the years by use of fundamentally based design techniques, a better understanding of reagent chemistry, online metal analysis and the use of digital control systems. However, optimal operation of flotation banks is not consistently achieved using manual operation. The reason for this is that the system is a highly interacting one, with changes in air addition, cell interface level and reagent dosages all being available, without it necessarily being clear as to which change should be made for a particular situation.This situation is made more complex by the fact that the feed to a flotation bank can vary in flowrate, composition and density over a fairly short period of time. It is not possible for a human operator to reject these disturbances, given the extent of the operation that is typically being monitored.Model predictive control (MPC) is a control and optimisation technique, developed in the oil refining industry, that aims to manage just such interacting multiple input multiple output (MIMO) systems. This technology makes use of linear dynamic models of the plant, that are experimentally derived. These models are then used in a receding horizon strategy to determine an optimal trajectory of the inputs to the system.MPC has been applied to four areas of the lead zinc flotation unit at Mount Isa mines. A total of 31 cells are being controlled by the system, which varies air to the cells, levels and reagent addition on a minute-by minute basis. The MPC controls concentrate and tail grades, reagent dosages, as well as recoveries to ranges set by the plant metallurgists.The development of the MPCs is discussed, together with the benefits realised. The key factors in insuring an ongoing return on investment are described.CITATION:Price, A, Okle, D and Brooks, K, 2018. Glencore Mount Isa lead zinc flotation circuit – experiences from the implementation of model predictive control, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 101–110 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By T D. H McGrath, W P. Staunton

Benchmarking, comparing an operation or process with the industry standard, is known to be a useful method for identifying plant optimisation opportunities, and in many cases providing the pathway to realise the benefits. The difficulty is generating the database of plant data necessary for a benchmarking exercise. Larger companies can benchmark internally; this option is not available to smaller companies, and the full value can only be realised with a comprehensive “industry wide” approach.The Gold Technology Group at Curtin University through the AMIRA P420 series of projects has undertaken several comprehensive metallurgical industry surveys in the gold industry over the last two decades. Analysis of these surveys has demonstrated areas where many operations can benefit from re-assessment of their operating practices.This paper will review the work undertaken by the Group in this area, in particular the 1999 surveys of gold companies in the Australasian region, and the 2012 international survey of the industry. The challenges of, and opportunities arising from these surveys will be discussed. Some of the highlights from analysis of these databases will be presented as well as noting changes in processing practices observed by the Group over the last 20 years.CITATION:McGrath, T D H and Staunton, W P, 2018. Keeping up with the Joneses – the value of industry surveys and benchmarking, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 509–516 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By L Mikhael Gurieff, D Baas

The Phu Kham Copper-Gold Operation (Phu Kham Operation) is located in the Lao People's Democratic Republic and is owned and operated by the Lao-registered company, Phu Bia Mining Limited (PBM). Australian-headquartered copper and gold producer, PanAust Limited holds a 90 per cent interest in PBM; the Government of Laos owns the remaining 10 per cent. The Phu Kham Operation was commissioned in 2008 with an initial concentrator nameplate throughput of 12 million tonnes per annum (Mt/a). Subsequent improvement projects, including the Phu Kham Upgrade Project (PKU), completed in 2012, and the Phu Kham Increased Recovery Project (IRP), completed in 2013, increased the design throughput to 18 Mt/yr. In 2016, the actual mill throughput exceeded 19 Mt/a, this throughput is budgeted to be maintained until the end of 2020.The concentrator flotation circuit upgrade, completed during the IRP, called for a non-selective bulk sulphide concentrate to be generated from the rougher circuit. This in turn caused the mechanical flotation cells in the cleaner circuit, particularly those in the second cleaner bank, to become volumetrically overload. The overload reduced the cleaner circuit performance to approximately 92 per cent copper recovery at a 23 per cent copper concentrate grade, below the expected 95 per cent recovery. This bottleneck restricted copper units entering the plant to approximately 14.5 tonnes per hour (t/h) due to uncontrolled recirculating load build-up in the mechanical cleaning circuit.Maintaining the operating methodologies would have led to a copper production shortfall beyond 2016, to address this shortfall the Phu Kham Operation looked to optimise the Jameson Cell and mechanical cleaner circuit performance. The work included fundamental application of flotation practice and modelling, mineralogical analysis, bubble size analysis, plant surveys and test work. The results were used to develop and implement an innovative automated control system strategy incorporating flotation theory and operating strategies. The automation has the ability to quickly adapt to disturbances in the circuit and maintain optimised performance with little or no intervention by flotation operators.Upon completion, cleaner recovery increased to 95 per cent at a final concentrate grade of 23 per cent copper, and copper units entering the plant increased to 17.5 t/h.CITATION:Baas, D and Mikhael Gurieff, L, 2018. Developing flotation circuit control and automation for the Phu Kham Copper-Gold Operation concentrator, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 37–58 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By B Wong, R G. Coleman

In flotation, the selection of the size, number and type of cell for a particular duty depends on two important factors. Firstly, the required flotation residence time and secondly, the physical constraints of how much concentrate can be recovered for a given froth surface area and concentrate lip length. The residence time is influenced by ore type and characteristics such as liberation, kinetics and reagent dosage. The amount of concentrate that can be recovered for a given froth surface area and lip length depends on ore type and other characteristics such as particle size, specific gravity and mineral grade. Residence time is determined through a combination of laboratory-scale test work and design scale-up factors. However the critical froth transport parameters such as froth carry rate and froth lip loading cannot be determined in a laboratory. This is because the froth is scraped during a laboratory flotation test and thus does not exhibit natural behaviour, and it is not possible to scale-up froth transport distance or air rate. These values are generally compared via calculation to rule-of-thumb maximum values to establish if these values will be exceeded by the flotation cell selection.This paper first reviews these critical froth transport parameters and then discusses actual parameter values across diverse operating sites, with varying cell duties, cell sizes and types, orebodies and particle sizes. These values are compared against the industry rule-of-thumb to test the applicability of the rule-of-thumb to actual performance. Options are also presented for adjusting these parameters in operating flotation cells.CITATION:Coleman, R G and Wong, B, 2018. Flotation launder design and the measurement of critical froth transport parameters, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 353–362 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By J K. Claflin, S R. La Brooy, A M. Claflin

Rotary kilns have been in service in the gold industry to regenerate carbon for 65 years. At the time oxide ores with gold head grades of 8 to 10 g/t were being treated. Carbon could be regenerated adequately at 650°C and solution losses were less than 1%. Forty years ago, research indicated that heavily fouled carbon from flotation circuits had to be held at 750 to 850°C for ten to twenty minutes for full reactivation (Avraamides and La Brooy, 1987), gold head grades were typically 5 g/t and solution losses typically 0.02 ppm – still less than 1%. In 2017 it was determined (Claflin et al., 2017) that a residence time of less than 1 minute at 750°C can be adequate to reactivate carbon fouled with organics sufficiently to achieve 0.005 ppm solution losses in a flotation tailings leach plant.With the potential for discovery head grades to drop below 0.6 g/t, solution losses of 0.02 ppm represent over 3% loss. Tight operation of the whole carbon circuit is required to keep gold solution losses below 1% going forward.There are alternatives to a rotary carbon kiln, e.g. vertical kilns of which the Minfurn, Rintoul and Combustion Air kilns are examples. The alternative kilns can be heated using electrical heating elements, induction, and microwave. These kilns can operate successfully under the right conditions, however, they are almost exclusively for small carbon throughputs and are not suitable for the large carbon advance rates that are required to process low head grade ore deposits. Large throughput carbon kilns are are almost exclusively fossil fuel fired rotary kilns and the subject of this paper. In the view of the principal author, a fossil fuel fired vertical carbon kiln is preferred to a rotary kiln, however, it is not currently used in the industry.Thermal regeneration of activated carbon has a major impact on gold recovery in the carbon circuit. The carbon kiln and associated equipment constitute 3 to 5% of the capital cost for an oxide processing plant and up to 10% of the capital cost if flotation tails are leached. Despite the capital cost and impact on recovery, the carbon kiln is often poorly selected, operated and maintained.Six years ago Ausenco embarked on the Carbon Kiln Initiative to reduce solution gold losses. This body of knowledge has been published in a series of papers culminating in this paper on how to:1. Select a kiln appropriate for the flowsheet;2. Maintain the kiln to achieve design operation; and3. Operate the kiln to minimise costs and maximise reactivation.CITATION:Claflin, J K, La Brooy, S R and Claflin, A M, 2018. Carbon kiln selection, operation and maintenance, in Proceedings 14th AusIMM Mill Operators' Conference 2018, pp 251–274 (The Australasian Institute of Mining and Metallurgy: Melbourne).

Aug 29, 2018

By José Wilmar Calderón-Hernández

Aços inoxidáveis supermartensíticos (AISM) surgiram em meados dos anos 1990, após algumas empresas petroleiras e centros de pesquisa empreenderem projetos para desenvolver aços inoxidáveis com boa resistência mecânica e resistência à corrosão. A força motriz destes projetos foi a procura de aços inoxidáveis alternativos para os aços duplex e superduplex na extração de reservas de petróleo “offshore”, devido a seu alto custo e a problemas de produção naquela época. Os AISM são derivados dos aços martensíticos inoxidáveis convencionais, possuem menor teor de carbono, para permitir melhor soldabilidade e melhorar a resistência à corrosão, adição de níquel para evitar a presencia de ferrita delta (d) e adição de Mo, que também aumenta a resistência à corrosão. Através de ensaios de polarização potenciodinâmica foi avaliada a resistência à corrosão de um AISM 13Cr-5Ni-2Mo, denominado neste trabalho como AIS_2Mo, para três diferentes ambientes, NaCl, NaCl+CO2 e NaCl+H2S (soluções desaeradas). O material foi recebido como chapas laminadas a quente, as quais foram normalizadas a 1.050°C (½ hora/ar) e posteriormente revenidas a 600°C (2 horas/óleo). O melhor desempenho foi observado no eletrólito contendo apenas NaCl, com potencial de pite ao redor de 40 mV (ECS); o ambiente mais agressivo foi a mistura NaCl+H2S, com potencial de pite ao redor de -300mV (ECS), a mistura NaCl+CO2 teve potencial de pite intermediário, com valor 60 mV (ECS) abaixo do eletrólito contendo só NaCl.

Aug 8, 2018

By Gilberto Álvares da Silva

New elements have been inserted in NiTi lately, resulting in ternary alloys with specific characteristics beyond Shape Memory Effect and Superelasticity. Among all others alloying elements, the Ag additions itself gives potential antibacterial activity to that smart material. So on, the elaboration procedures of ternary NiTiAg alloys was studied in order to obtain a melting procedure to ensure further studies on this alloy. Microstructural and thermal analyses were used to evaluate the VAR-remelting production of NiTiAg with 4.0% wt silver content. The microstructure is composed by a NiTi matrix, pure Ag precipitates, and, scarcely, TiC inclusions. Heat treatments at high temperature could not dilute those Ag particles, but could lead to the precipitation of new ones. The silver element reduces the temperature of the martensitic transformation, yielding a material with superelastic behavior, beyond induces the R-phase on cooling stage of this alloy.

Aug 8, 2018

By Vera Lúcia Othéro de Brito

Literature has shown that spinel Co-Mn ferrite have potential application in magneto-mechanical sensors, due to its relatively high magnetoelastic sensitivity. In this work, Co-Mn ferrite was processed by means of the ceramic method, using Fe2O3, MnO and Co3O4 as raw materials. Samples were liquid-phase sintered, using Bi2O3 additive as liquid-phase former. X-ray fluorescence analysis was carried out in the raw materials in order to evaluate their impurity content. Atomic absorption spectrometry analysis was used for quantifying the Co/Mn/Fe proportion in the ferrite. The microstructure of the sintered sample was analyzed by means of Scanning Electron Microscopy. The magnetization and magnetostrictive behavior of the ferrite were evaluated, obtaining curves for magnetic hysteresis, magnetostriction and magnetoelastic sensitivity. The impurity inclusions and the Bi-rich particles formed from the liquid phase were characterized. The sintered ferrite had a total magnetostriction of -126ppm, which is lower than the values reported in literature for a Co-Mn ferrite of similar composition. It was verified that sintering was carried out within a critical temperature range, in which the decomposition of Mn ferrites may occur when sintering in air. This decomposition affects the magnetic properties of the material, and it may be avoided by using controlled sintering atmospheres.

Aug 8, 2018

By Mateus Luiz Gamba

O titânio e suas ligas são aplicados em grande escala em implantes ósseos por apresentarem excelentes resultados de biocompatibilidade. No entanto, ainda não existe um consenso na literatura com relação à influência das características morfológicas destes implantes na osseointegração, principalmente na definição da melhor rugosidade e energia superficial. Vários trabalhos têm sido realizados com o intuito de comparar diferentes tratamentos superficiais empregados para otimizar a adesão, o crescimento e a proliferação celular. O presente trabalho tem como objetivo apresentar uma base de dados sobre características superfícies versus osseointegração para experimentos de biocompatibilidade realizados in vitro. Foram feitas coletas e análise de dados qualitativos usando métodos analíticos em artigos científicos publicados em periódicos internacionais, sendo considerados na pesquisa artigos que utilizaram superfícies de Ti/TiO2 e células osteoblásticas. Os principais atributos definidos para a base de dados foram rugosidade, tamanho da célula, energia da superfície e/ou ângulo de contato, tipo de tratamento superficial, viabilidade e a resposta observada na cultura celular. Espera-se que esse artigo contribua para que futuros trabalhos possam utilizar métodos e estudos que permitam auxiliar na descoberta de conhecimento através de padrões que acelerem o processo de osseointegração impactando diretamente na recuperação do paciente implantado e na sua qualidade de vida.

Aug 8, 2018

By Carlos Gonzalo Alvarez Rosario

A reciclagem de resíduos eletroeletrônicos (REEs) é importante tanto no aspecto ambiental quanto econômico, uma vez que através do reaproveitamento do REE há diminuição da quantidade de resíduos a ser destinados, além disso, contribui para a sustentabilidade do setor minero metalúrgico, pois é possível a recuperação dos metais provenientes de REEs. Presentes na maioria dos equipamentos eletroeletrônicos, as Placas de Circuito Impresso (PCIs) são compostas por materiais cerâmicos, metálicos e poliméricos. Além disso, a heterogeneidade do material influi diretamente no tipo de processamento/tratamento a ser utilizado, desta forma a caracterização prévia do resíduo é uma etapa fundamental para determinação da rota de processamento a ser utilizada. Assim, no presente estudo é apresentado o processo de caracterização de PCIs proveniente de computadores obsoletos objetivando a determinação e quantificação dos metais presentes, de forma a estudar a influência dos mesmos em processos de biolixiviação futuros. A rota de processamento físico incluiu inicialmente processo manual utilizando guilhotina e, posteriormente, moinho de martelos com grelhas de aberturas de 6 mm e 2 mm. A caracterização foi realizada através de ensaios de perda ao fogo, lixiviação ácida e MEV/EDS e a concentração dos metais foi determinada por ICP-OES. Os resultados mostraram que 50% do material particulado tem granulometria maior que 0,25 mm; as PCIs estudadas possuem 35,6% de metais, 27,2% de polímeros e 37,2% de cerâmicos. Dos metais presentes nas placas o mais representativo foi o cobre com 21,4% em massa enquanto que metais como Fe e Al apresentaram 1,1% e 1,9% em massa.

Aug 8, 2018

By José Eudes Lima Santos

Neste trabalho foi estudado o efeito da variação da densidade de corrente, temperatura e pH do banho eletrolítico na eletrodeposição da liga Ni-Mo-P utilizando citrato de sódio como agente complexante em função do comportamento anticorrosivo da mesma, da composição química e morfologia dos revestimentos. A caracterização das camadas foi feita por microscopia eletrônica de varredura (MEV) e energia dispersiva de raios-X (EDX). Os ensaios de corrosão foram realizados à temperatura ambiente em NaCl 0,1 M por polarização potenciodiâmica linear (PPL). Como ferramenta de otimização foi utilizado um planejamento fatorial completo 23 associado a metodologia da superfície de resposta (MSR). As propriedades de corrosão e composição química dos revestimentos de Ni-Mo-P obtidos mostraram ser dependentes da densidade de corrente, temperatura e pH do banho eletrolítico. A ausência de trincas foi verificada para revesimentos com baixo conteúdo de molibdênio e mostrou ser necessário para obtenção de eletrodepósitos com boas propriedades de resistência à corrosão. Os resultados revelaram que o revestimento que apresentou melhor resistência à corrosão foi obtido em densidade de corrente 100 mA cm-2, temperatura de 40°C e pH 9,0 com composição de 87 wt.% Ni, 6 wt.% Mo e 7 wt.% P e sua superfice exibiu morfologia nodular.

Aug 8, 2018

By Paulo Sergio Olivio Filho

A aspersão térmica é utilizada para produzir revestimento quando há necessidade de aumentar a vida útil de sistemas e peças, podendo ser também utilizada na recuperação delas, em alguns casos. Com o intuito de compreender melhor o processo de aspersão térmica por chama a pó, o objetivo deste trabalho é analisar os fatores influentes no aumento de espessura depositada pelo processo, utilizando o delineamento de experimento de Taguchi para avaliar os fatores e níveis dos fatores que geram as melhores condições de aplicação para o revestimento. Para isto, foram escolhidos três fatores de controle com três níveis cada um, dos quais foi possível seu controle em laboratório. A deposição foi realizada em chapas de aço SAE1020, e revestida com pó de alumínio não atomizado. A seção transversal dos revestimentos foi analisada por microscópio ótico. Os resultados dos experimentos foram analisados através de estatística descritiva, gráfica e análise pelo delineamento de Taguchi, baseada na análise de Sinal/Ruído. Sendo evidente que os fatores do processo são estatisticamente significativos: número de passes, fluxo de nitrogênio e a taxa de alimentação de pó. Esta análise se mostrou eficaz, gerando os resultados esperados para otimização dos parâmetros do processo.

Aug 8, 2018

By Rodrigo Perito Cardoso

Low-temperature nitriding of stainless steels is applied to obtain wear resistant surfaces without losing its corrosion resistance. The treatment consists in introducing nitrogen into the steel surface avoiding chromium nitride precipitation. The corrosion resistance of martensitic stainless steels is expected to be improved if the treatment parameters are correctly selected. It can be related to ?Fe2-3N and a'N phase formation on the treated surface. In the present work the influence of the pretreatment and treatment temperature on corrosion resistance of plasma nitrided AISI 420 steel samples is studied. Annealed, as-quenched and 400ºC-tempered samples were nitrided at 300, 350, 400, 450 and 500°C, for 6 h at 600 V. The pressure was 3 Torr and the gas mixture was composed of 70%N2, 20%H2 and 10%Ar, at a gas flow rate of 3.34×106 Nm3s-1. Plasma was generated using a square-wave pulsed DC power supply and the sample temperature was controlled by the duty cycle. The modified layers were characterized by optical microscopy, X-ray diffraction and microhardness measurement. The corrosion resistance was studied by electrochemical characterization, by means of Open circuit potential and Anodic polarization curves. The maximum surface hardness was achieved at 400°C. This temperature seems to be near the limit temperature for low-temperature treatment aiming to improve or at least to keep unaltered the corrosion resistance in relation to that verified for non-treated steel samples. Results confirm that the pretreatment and treatment temperature significantly affects the corrosion resistance of the treated surface.

Aug 8, 2018

By Nathanael Wagner Sales Morais

Os aços maraging tem grande importância tecnológica devido sua aplicação nas industrias aeroespacial e nuclear. Uma das aplicações para esse material é a fabricação de cilindros de alta resistência pelo processo de estampagem profunda, logo o conhecimento da textura cristalográfica torna-se fundamental. Este trabalho investigou o efeito da laminação à frio seguida por um recozimento sobre a microestrutura, textura e anisotropia plástica no aço maraging 350. A anisotropia foi medida pelo cálculo dos coeficientes de Lankford e dos coeficientes de anisotropia normal (Rm) e planar (?R). Os resultados mostraram o aumento na deformação a frio gera um aumento na intensidade da fibra acompanhada de um aumento no valor de Rm. As análises metalográficas mostram que maiores reduções induzem à um precipitação intermetálica após o recozimento.

Aug 8, 2018