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The hydrological cycle in nature, with particular reference to Australia . 2. The definition of water pollution drawing on the experience of several major countries. 3. A description of the pollutants in water, and why they are pollutants. 4. The classification of waters as defined by major overseas countries. 5. The criteria and standards developed by major overseas countries for the classification of waters. 6. A brief- summary of the legislation adopted by overseas countries for the control of water pollution, and of the organisation and administration of controls. 7. A study of Australian legislation and administration of controls of water pollution. 8. General observations and conclusions.

Jan 1, 1971

By Humberto Tronconi Coelho

The use of friction dampers are wide proposed for a variety of mechanical systems for which it is not possible to apply viscoelastic materials, fluid based dampers or others viscous dampers. An important example is the application of friction dampers in aircraft engines to reduce the blades vibration amplitudes. In most cases, friction dampers have been studied in a passive way, however, a significant improvement can be achieved by controlling the normal force in the contact region. The aim of this paper is to study four control strategies for friction dampers based on three different hysteresis cycles. The first control strategy maximizes the energy removal in each harmonic oscillation cycle, by calculating the optimum normal force based on the last displacement peak. The second control strategy combines the first one with the maximum energy removal strategy used in the smart spring devices. Finally, is presented the strategy which homogenously modulates the friction force. Numerical studies were performed with these four strategies defining the performance metrics. The best control strategy was applied experimentally. The experimental test rig was fully identified and its parameters were used for numerical simulations. The obtained results have shown the good performance for the friction damper and selected strategy, also, the agreement between numerical and experimental results.

Jul 31, 2018

By Luis G. Bergh

Today, large size mechanical flotation cells of 100 to 300 m3 are used in rougher operation in different flotation industrial plants, in Chile and worldwide. However, in spite of the advances in fundamental research and the notable growing in equipment size, with more complete instrumentation systems, there are still a lack of reliable data for industrial flotation modeling and simulation to advance in better control systems design. In this work, a model of a rougher flotation circuit, based on operating variables and parameters fitted from industrial data, obtained in some previous work, is used to develop a set of logic rules in order to aid operating decisions. The simulator was first used to sensitize the effect of changing the froth depth profile on target variables, and then to find out the best profile to reject common disturbances coming into the plant. The flotation circuit simulator was redesigned to incorporate an expert system following the proposed control algorithm. Several tests were performed to evaluate the control responses to different correlated series of input variables, such as feed grade, tonnage, particle size distribution, and solid percentage. Control alternatives are discussed based on the circuit simulator. Keywords: modeling, industrial data, flotation control, mineral processing.

Sep 1, 2012

By Jay P. Chapman

The basic control requirement for multi-pump, long distance slurry pipelines are discussed and a particular example of an operating slurry pipeline using programmable controllers is presented.

Jan 1, 1983

By R West

The Olympic Dam smelter facility processes copper concentrate feed using direct-to-blister smelting technology to support the current site production rate of 225 000 t/a copper. The metallurgical control of the Olympic Dam smelter is largely managed from a single central control room. Control room operation and management is therefore a key function in ensuring safe and reliable operation of the smelter, including identifying and initiating control of abnormal events. As part of a consolidated smelter reliability improvement program, a team consisting of process and control system engineers was formed. The teamÆs charter was to address and resolve the alarm flooding issues being faced by the control room technicians and the lack of an up-to-date base of supporting functional documentation. The project was successfully resourced with WorleyParsons metallurgists, Citect PLC technicians and the on-site technical team. Implementation was conducted over a 12 month period with the goal of achieving best practice alarm levels. The goal was achieved through a systematic process of alarm design review that analysed every configured alarm versus best practice design standards. Innovative concepts such as group-based alarms, first-up interlock displays, graphic only alarming, alarm help and alarm shelving were developed and implemented in conjunction with improved alarm masking. Total configured alarms were reduced from 20 000 to 5000 while the alarm rates were reduced from in excess of 200 alarms per hour per controlling technician to best practice levels of less than 12 alarms per hour per controlling technician. Completion of this program has provided a firm foundation for implementing further control optimisation and was a key activity in supporting sustained smelter reliability levels.

Jan 1, 2005

By Michel Ruel

"PID loops – also known as base layers or regulatory controls – form the foundation of any plant’s control layer and it is generally accepted that PID loop health has a direct impact on the plant’s bottom line. Keeping these thousands of control loops in good health has a direct impact on the plant’s bottom line: it reduces variability, improves quality and throughput, and decreases energy costs and raw material usage. This has been well proven and documented in many articles. In the last ten years, technology has evolved: control engineers can now keep track of control loop performance and link it to the root causes of variability. However, they lack industry-wide best practices and criteria for determining what can be considered as excellent, good, fair, or poor performance. To ensure that PID control loops continue to perform well and meet their objectives, control engineers need a combination of (a) an appropriate monitoring technology and (b) best practices for doing the maintenance of base layer controls.Most plants have limited resources and operate with an increasing number of constraints; therefore, using the right tools and including reports in daily workflow is key for success. This paper suggests roles and responsibilities of key players needed to work toward control performance best practices and discuss organisational changes to succeed.INTRODUCTIONAlthough PID controllers are reliable workhorses in the process industry, they are often underrated. Since the 1980’s, computer control has evolved and the control algorithms used by control engineers have become increasingly complex. However, PID controllers still handle over 90% of the control loops in operating plants. Table 1 shows the savings that can be realized by achieving best-practice in several different process control categories (Brisk, 2004). The savings are expressed as a percentage of production costs."

Jan 1, 2011

In 1987 the control strategies at the then ZC Mines' New Broken Hill Consolidated concentrator were a miscellaneous mixture of computer hardware and technology for ISA, grinding and residue thickener control. Field instrumentation was based on current-to-air technology of approximately the 1960s. Decisions were made to rationalise computer and field instrumentation technologies; the object being to consolidate control loops into one system to enable expansion of the system to include all facets of plant operation. The first stage was to install a DEC Micro PDP 11/23 computer and serial line communication as recommended by AMDEL Ltd, for the ISA system, as discussed by Walsh and Freeman (1988). The second stage was to select and install a distributed control system for the centralisation of the control loops into one system, and to replace field instrumentation with state-of-the-art technology. This paper deals with the second stage of the rationalisation, in an attempt to give an insight into what is required when personnel are faced with such a decision, details of costs involved in keeping a system functioning and utilised; and the requirement to train personnel for acceptance of further control strategies.

Jan 1, 1991

By J. P. Matoney

The operation of a modern coal preparation plant, particularly in western Canada, is a very complex task. Most western Canadian operations are processing two or more, sometimes up to ten, different seams through the same plant. This requires a sophisticated multi-circuit plant that needs close operational control. Add the soft nature and large amounts of natural fines of western Canadian coal and you have a formidable cleaning task. To assist in the operation, programmable controllers and sophisticated control concepts are being more widely used. Two of the newest coal preparation plants in Canada have been designed by Raymond Kaiser Engineers Inc. and its Canadian subsidiary, Phillips Barratt Kaiser Engineering, Ltd. The use of programmable controllers and control systems will be illustrated by showing their application in a "typical" western Canadian coal plant. This example will cover flowsheet design, control concept systems application, and possible future uses.

Jan 1, 1983

By Pedro Henrique Barbosa Souza

A Aperam é uma grande consumidora de gases do ar, principalmente Argônio. A produção de Argônio é feita através de coluna de destilação, onde são também extraídos Oxigênio e Nitrogênio. A modalidade de contrato adotada pela Aperam é do tipo take-or-pay para todos os gases, porém nem todo Oxigênio produzido era consumido. A Aperam então desenvolveu um projeto visando aproveitar esta “sobra” de Oxigênio no seu forno Walking Beam, para enriquecimento do ar de combustão. A utilização de Oxigênio permite reduzir, de maneira indireta, o consumo de Gás Natural neste forno. Após a implantação do projeto a Aperam está apta a consumir acima da capacidade de Oxigênio produzida, sendo necessário implementar uma estratégia de controle que permita limitar a máxima velocidade deste gás na tubulação (risco de explosões) e reduzir a interferência entre os diversos consumidores, o que poderia provocar desarmes ou oscilações na estequiometria dos gases. Para isto foi aplicado técnicas de controle antecipatório. Este trabalho irá abordar as estratégias de controle utilizadas, sua sintonia e os resultados obtidos.

Jul 30, 2018

By Alexandre de Freitas Gomes de Mendonça

O pick-up de nitrogênio no aço deve ser evitado nos processos de fabricação em uma Aciaria de alto desempenho. Entretanto, o pick-up de nitrogênio pode ocorrer em inúmeros pontos na Aciaria, principalmente quando o aço líquido é exposto ao ar atmosférico. Alguns locais de controle têm grande relevância no resultado do pickup, tais como: durante o vazamento do aço do convertedor para a panela, no refino secundário durante a agitação excessiva do aço e no lingotamento contínuo devido a aspiração de ar atmosférico nas conexões. Neste trabalho, o foco do controle da incorporação de nitrogênio é no lingotamento contínuo e, para efeito de estudo, tomou-se como referência um pick-up de nitrogênio de até 5 ppm. Os dados históricos mostram que menos de 64,6% das corridas encontravam-se com pick-up de nitrogênio abaixo de 5 ppm. Assim, visando reduzir esse pick-up foi proposto um ajuste no ângulo da sede da válvula longa, melhoria do projeto do gasket e capacitação da equipe de operação. Após a efetivação dessas ações de controle esse número passou para 97,7% das corridas lingotadas.

Jul 30, 2018

By Otaviano Donizeti Valadão de Freitas

Ruídos elétricos afetam os circuitos lógicos e conseqüentemente podem comprometer a confiabilidade nos controles de processos, e para minimizar as influências desses ruídos, algumas medidas básicas foram tomadas, com instalações adequadas de todo o sistema, como padronização do aterramento, encaminhamento de cabos, etc. Depois que as medidas foram implementadas, o resultado foi um sistema mais confiável. Se apenas um fio for encaminhado de forma incorreta ou se o aterramento estiver inadequado, pode ser suficiente para causar problemas. A experiência mostra que é muito difícil que todas as medidas sejam aplicadas integralmente, mas se não forem tomadas pelo menos as medidas básicas, o sistema ficará suscetível.

Sep 25, 2017

By Mirian Mamani

El presente texto señala el magmatismo de los Andes peruanos y la influencia de la madurez cortical de los depósitos minerales y su posterior delineación de las fuentes de mineralización.

Nov 1, 2013

By Pascal P. Percy

Dado el elevado costo de transporte que implica el traslado de mineral aurífero en la compañía minera La Poderosa, se ha elaborado un proyecto denominado "Proyecto de transporte sobre rieles" donde se garantiza el acarreo de 550 t/d a partir de 1994 y se reduce los costos del transporte a 56%. En este sentido, el presente trabajo describe la ejecución del proyecto a través del uso de túneles, chimeneas y trocha en superficie, reemplazando la os volquetes y camiones. Asimismo, el proyecto desarrolla la ejecución del túnel en forma convencional a través del metraje, logrando un control estricto de los tiempos empleados en cada operación unitaria, la utilización adecuada de los recursos, coordinación de los trabajos a realizarse y los servicios requeridos.

Nov 24, 1993

By Rildo Rodríguez, Dante Soberon

En el presente estudio se ha tomado en consideración diferentes aspectos geológicos que ayudan a determinar importantes controles estructurales que estuvieron activos en diferentes etapas de la evolución andina. El reflejo de la actividad de estas fallas se manifiesta por la presencia de controles estratigráficos, cambio brusco en la dirección de los ejes de pliegues y emplazamiento de pequeños cuerpos magmáticos, así mismo se encuentran relacionado al emplazamiento de mineralización de estaño, oro, uranio y tierras raras.

May 1, 2008

By Maylin Mendoza, Sheyla Pinto, Edwars Espinoza

En Cerro Lindo , la producción anual del oro en los últimos 05 años ha fluctuado entre los 3,500-4,500 Oz/troy, con una ley promedio de 0.05 g/t adquiriendo mayor importancia dentro de la cadena de producción de la unidad minera Cerro Lindo. Por ello con este trabajo se buscó caracterizar el comportamiento del Au en un yacimiento Tipo VMS- bimodal félsico, donde el Au, no es un elemento principal, y por ello, muchos en nuestras campañas de exploración le restamos importancia, sin saber el valor agregado que le puede dar a lo largo de nuestra producción; con este trabajo queremos mostrar esta nueva metodología basada en una visión más integral donde el conocimiento geológico nos lleva a incrementar valor a nuestros yacimientos.

Sep 29, 2023

By Franberni Sánchez

Litológicamente, las andesitas porfiríticas son las principales rocas hospedantes, seguido por dioritas y hornfels. Tectónicamente se han registrado tres eventos de deformación: El primero y el segundo están relacionados a una compresión regional NNE-SSO y NE-SO respectivamente, gobernadas por movimientos dextrales. El tercero está relacionado a una compresión regional ONO-ESE gobernada por movimientos sinestrales.

May 1, 2008

By Luis de Montreul

El conocimiento de los controles mineralógicos, tipos de ocurrencias y otras características mineralógicas de los depósitos auríferos permite plantear una adecuada exploración geológica-minera y seleccionar un óptimo tratamiento metalúrgico. Por ello, se busca establecer la relación entro el oro y determinados minerales metálicos y no metálicos para obtener una mejor recuperación de este elemento valioso. En ese sentido, el presente texto presenta ejemplos de controles mineralógicos en seis yacimientos aurífero de cinco Fajas mineralizadas del Perú.

Jul 1, 1987

By T. M. Jones

This paper outlines the development of the theory of controlled district recirculation and indicates the advances in understanding and technology which have enabled a major change in established ventilation practice. An insight is presented into the possible future use of controlled district recirculation as acceptable practice in mine ventilation planning.

Jan 1, 1987

By D. S. Saxena, Jack K. Tuttle

Lack of understanding of useful applications of explosives on construction work stem primarily from the fact that explosion is commonly associated with destruction. On rock excavation and other construction works a certain quantity of explosive is harnessed to perform useful work at the source e.g. blasts to disintegrate rock. Development in rock blasting techniques, including the use of multiple-row blasting with short delay ignition, have made it impossible to excavate rocks close to or below buildings even in closely built-up areas. To permit the use of explosives on construction projects, in ways that will not damage existing structures, guidelines have been developed from careful measurements of intensity of ground vibrations. Accurate electronic instruments are now available for doing this. PLANNING AND CONTROL Blasting operations must be carefully planned and carried out to avoid discomfort to persons or damage to property. This increase in the use of rock blasting in city areas alone has led to a number of problems due to ground vibrations, air shock waves, and the psychological effect of noise. While the latter seldom if ever causes damage, it does create irritation and discomfort to persons living or working near the blasting sites. A result of this is a steady increase in the number of complaints in respect of damage to houses and other premises. Many such complaints are genuine and damage may undoubtedly be caused when incorrect blasting techniques are used.

Jan 1, 1997

By Ivor Jenkins

PROCESSES employing controlled atmospheres in the heat-treatment of metals and alloys are now well established on an industrial scale, and the general principles involved and the advantages to be gained in the use of the technique have received considerable publicity over a period of years. During this time the greatest emphasis has been on the establishment of the process in industry, the main effort being devoted to development work on various types of atmospheres, their useful fields of application and the design of suitable heat-treatment furnaces in which they are to be used. The various types of controlled atmospheres are fairly well standardized, but there still remains a considerable field for the investigation of related problems, in connection with both the gas-generating equipment and the surface chemistry of the heat-treatment of metals, especially in complex controlled atmospheres. This paper describes certain investigations of this nature that were carried out in England up to 1939. The development of processes employing controlled atmospheres has been associated to a very large extent with the heat-treatment of steels, both because of the major importance of steel in industry and the many diverse and difficult problems of surface chemistry involved when steels of such a wide range of composition are heated in the presence of active gases Controlled atmospheres such as dissociated and burnt ammonia or charcoal gas are used in the heat-treatment of low-carbon and high-carbon steels, but from certain points of view a suitable atmosphere generated by the partial combustion of city gas is to be preferred. Both the ammonia derivatives are comparatively expensive, and even if the burnt ammonia is regenerated, thereby reducing operating costs, the capital expenditure of the gas plant may make it prohibitive for the smaller type of furnace installation. Charcoal-gas generators are not without their operating difficulties: especially those associated with the quality of the charcoal, clinker formation and the removal of carbon dust from the generated gas. City gas has the advantage of being comparatively cheap and "on tap" in most if not all industrial centers. The use of raw city gas as a protective atmosphere in the heat-treatment of steels has been described,1 but it presents certain difficulties because of its complex composition and its explosive nature when mixed with air. These factors, together with the tendency toward sooting at elevated temperatures, arising mainly from the hydrocarbon gases present, all militate against its use as a protective atmosphere in industrial furnaces. The following analysis, based on the analyses of city gas in different localities in Great Britain, indicates the wide limits existing

Jan 1, 1947