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By Sangwhui Cho

In comminution processes including crushing, grinding and pulverizing, the efficiency of the comminution system is very low. Since the early 1980s, research has been conducted to increase the efficiency of pulverizing mills. Additionally, the application of microprocessors and Personal Computers to process control have come into general use. Given appropriate models of the process and control algorithms, these systems can economically control comminution processes. The ring-roller type mineral pulverizer is known as an energy saving mill. In this study, a control strategy to increase the efficiency of this type mill is explained.

Jan 1, 1992

By B. C. Flintoff

In general, process control systems in solid-solid separation have not evolved to the same level as in flotation circuit control. Perhaps one of the more significant contributing factors in this regard is the lack of suitable on-line analytical instrumentation. In spite of the obstacles, some interesting work has been done. This paper presents a review of current industrial control strategies in ore sorting, dense media separation, gravity separation and electrical and magnetic separation.

Jan 1, 1986

By K. C. Carriere

INTRODUCTION The purpose of this paper is to introduce the reader to basic control strategies for solid/liquid separation in mineral processing and to indicate some of the implementation difficulties to be encountered, without becoming overly involved in details of process, equipment or software. It is assumed that the reader has some familiarity with control systems and with dewatering processes, since exploration of these topics would require considerably more length. The paper is organized into three parts: first a general discussion on the need for control of dewatering processes and of the general criteria involved, next a more detailed elaboration on control strategies for the various unit operations, and finally a case study showing a specific approach towards such a project. Motivation & Objectives The justification for implementing any control system in an industrial plant is to improve operations and thereby to increase profitability. Without this motivation, the system will likely be perceived as unnecessary and will decline into disuse, an expensive and troublesome monument to someone's ill-conceived ideas. However, when a control strategy is correctly conceived, implemented and integrated into operations, it can provide significant advantages in operating ease and efficiency, and a handsome return on investment. In general terms, the objectives in establishing a control system are: • stabilization of process disturbances maintenance of product quality • maximization of throughput • dearer definition of process • protection of personnel and equipment A successful control strategy must address at least some of the above criteria. However, the most important requirement is a commitment on the part of plant personnel and management to start up, operate and maintain the system, and to upgrade it to reflect current process status and operational philosophy. Process Applications In this paper, control strategies will be explored for the most common methods of dewatering of mineral pulps. These unit operations include: drying, centrifuging, filtering and sedimentation. While the first three are important, they do not tend to be as complex as sedimentation, and thus will not be as exhaustively treated. Sedimentation is very widely applied, not

Jan 1, 1986

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 Alexander Filimonov, Yury Bloshteyn

Ventilation of gas mines keeps necessary sanitation and hygienic conditions for labor in mines and increases the safety by dilution and removal of hazardous and dangerous gases in accordance with the safety rules. Several different concepts exist at the present time to design mine ventilation control systems. But technical ideas have been developed inadequately and technological solutions have not been investigated experimentally enough to build a serviceable system. This paper presents a new concept of high- efficiency mine ventilation process control system (MVPCS). The methods of modern system engineering (Kalman, 1969) are used to establish its functional and algorithmic structure. A three level hierarchical principle of system building is considered.

Jan 1, 1991

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 Bob Thomas

The roof drill operator productivity can be enhanced by the introduction of control technology The operators control station can be improved by considering human factors such as handle forces and control location. The smaller electrical controls can be located much easier than the traditional hands on valves. The operators control can he improved by using processors with programmable subroutines that assist the operator in the decision making process. For example to increase feed rate - to slow rotation - to avoid clogged steels - etc. The overall affect is to improve drilling and bolting consistency. The control system uses a dedicated processor packaged as an intrinsically safe control station. The roof drill operator is assisted in the drilling; arid bolting by a closed loop feedback system. The processor monitors the drilling parameters such as feed force, feed rate, rotation torque, RPM, drill position, and vacuum condition Based on the drilling parameters the processor executes pre-determined condition statements intended to enhance drilling The drill operator has an active display to alert him to the real time machine status. For example if the feed were to slow or delay due to a high vacuum level the display would show "high vacuum". The dedicated processor is available on the arm feed style machines, The prototype machines used programmable logic controllers to develop the feedback relations. The ability to record drilling parameters was extremely helpful in this development project. The extended use of the recording feature will aid operators in mapping the mine roofs Interpreting the recorded drilling parameters can reveal a void in the top or hard competent drilling The prototype machines also showed the importance of vacuum monitoring This feature is extremely valuable in softer materials, The benefits of the control system range from efficient use of the consumable bolting materials to uniform operator performance.

Jan 1, 1999

By Modesto Pereira Júnior

A operação da moagem é de grande importância na mineração, uma vez que é a área da fragmentação que requer maiores investimentos, há maior gasto de energia e seu desempenho afeta diretamente a taxa de recuperação do mineral de interesse. O controle do circuito de moagem é desafiador por se tratar de um sistema multivariável, não-linear e por se caracterizar pela existência de forte acoplamento entre variáveis e diferentes atrasos de tempo. Na indústria, grande parte desses circuitos é controlada apenas por PIDs. Nesses casos, quando há perturbações no sistema, tais como variação do tamanho das partículas na alimentação ou variação na dureza do minério, a interferência de operadores alterando setpoints é exigida para manter a estabilidade do sistema. Neste trabalho é desenvolvido um controlador fuzzy multivariável aplicado a um simulador de moagem. A camada de controle proposta encontra-se acima da camada regulatória. O objetivo é o de variar dinamicamente os setpoints dos PIDs para maximizar a taxa de produção dentro de uma faixa granulométrica.

Oct 30, 2017

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 Leandro Carrijo Gomes

O grande desafio para as empresas, principalmente as de grande porte, é ter controles desenvolvidos e simplificados de seus processos eliminando as vulnerabilidades encontradas, aumentando a produtividade, evitando desperdícios assim reduzindo custos e garantindo um bom nível de serviço para seus clientes, sejam eles internos ou externos. Este trabalho tem como objetivo demonstrar os ganhos obtidos com a criação de uma ferramenta automatizada de controle de materiais sobressalentes que são debitados do estoque contábil e que ficam aguardando sua aplicação em eventos de manutenção programados. Para alcançar o objetivo, foi desenvolvida uma transação no sistema SAP que possibilita a inserção de todas as informações necessárias para controle destes materiais eliminando a necessidade de controles paralelos. Com esta nova transação, conseguimos manter a rastreabilidade dos materiais em todas as etapas do processo até a aplicação pelo usuário final, trabalhando dentro do sistema homologado pela empresa, além de reduzir os estoques, devido a ter visibilidade destes materiais pelo setor de planejamento de materiais, evitando compras desnecessárias.

Aug 17, 2017

By Marcelo deCastro Souza

Neste artigo é descrito o desenvolvimento e implementação de uma nova estratégia de controle para Prensa de Rolos Polycom da POLYSIUS, utilizada no processo de pelotização da Samarco Mineração S.A. A estratégia de controle é redesenhada com objetivo de otimizar o processo e aumentar a eficiência do equipamento. Como resultado do trabalho foi verificado um aumento significativo da superfície específica do pellet feed de saída.

Aug 16, 2017

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 Fabio Schusterschitz da Silva Araújo

A unidade do Grupo SIMEC em Pindamonhangaba tem capacidade de produção de 560 mil toneladas/ano de produtos destinados à construção civil. Para abastecer a planta, é utilizada água de poço com pH, condutividade e alcalinidade altas, além de restrições quanto à disponibilidade. Isto gera desafios para o seu uso, e para a água de reposição do sistema de resfriamento dos moldes a água passa por um sistema de osmose reversa. No primeiro semestre de 2016, houve contaminação da água de molde, com a formação de uma incrustação de coloração branca, de aspecto oleoso e diferente das incrustações normalmente encontradas. Este fenômeno reduziu significativamente a vida dos moldes, o que levou à necessidade de paradas constantes para a troca e aumento significativos dos custos. Foi montado um grupo de trabalho de todas as áreas envolvidas, operação, manutenção e condicionamento químico para descobrir as causas e corrigir o problema. Este trabalho mostra as causas, as ações tomadas e os resultados obtidos.

Oct 30, 2017

By Cristiane Vilma Rocha Galiazzi

As matérias primas para Alto Forno devem ter qualidade física adequada para melhor controle do processo e estabilidade operacional. A distribuição granulométrica e consequentemente sua estabilidade são importantes, pois interferem na porosidade e permeabilidade no interior do Alto-Forno, criando assim uma condição adequada e específica de marcha com reflexo na estabilidade da produção de gusa. A Sinterização da ThyssenKrupp Companhia Siderúrgica do Atlântico (TKCSA) foi projetada sem britagem secundária, devido à fase de ajustes no processo operacional e baixa produtividade havia dificuldade para controlar a fração grossa do sinter (> 50 mm), impactando na distribuição granulométrica do sinter. Visando reduzir os desvios da qualidade física, estudou-se a melhor relação da altura de camada x velocidade da esteira encontrando um ponto de equilíbrio entre os níveis de produção e qualidade especificada que, juntamente com o início da operação do britador secundário, resultou na garantia da qualidade física do sinter para os Altos Fornos. Este trabalho tem como objetivo apresentar o desenvolvimento e resultados deste estudo.

Aug 1, 2018

By Bruno Serafim Parra

O novo laminador de tiras a quente da Usiminas, instalado na usina de Cubatão em 2012, tem como diferencial o alto nível de automatismo para fornecer bobinas com melhor qualidade. Dentre os modelos matemáticos de controle existentes no laminador, apresenta-se o Automatic Profile Flatness Control (APFC), responsável pela medição de planicidade e controle de perfil das bobinas. Através da resposta do medidor de planicidade e do medidor de perfil na saída do trem acabador, o modelo utiliza informações gerais do laminador para gerar uma resposta dinâmica e eficiente da forma do material durante seu processamento. O modelo utiliza ferramentas dedicadas para o controle de forma, como o sistema de pair cross, que é o cruzamento voluntário dos cilindros entre tiras, o sistema de roll shift, responsável pela movimentação longitudinal dos cilindros entre tiras e o roll bender, este dinâmico, trabalhando na deformação dos cilindros. Desde o início da laminação comercial, o desempenho da planicidade do material apresentou evolução significativa na nos índices de qualidade e produtividade do laminador.

Aug 16, 2017

By Dalton Martins Neto, Sandro Valério Maia Larrubia, Alexandre Patricio Vieira da Silveira

A TERNIUM Brasil, Rio de Janeiro, tem em sua operação dois Altos-Fornos idênticos. Ambos iniciaram operação em 2010, Alto-Forno 01 em 13/07/2010 e Alto-Forno 02 em 06/12/2010. Em Dezembro de 2016 e Janeiro de 2017 ocorreu alguns eventos de rompimento de conjunto de sopro por temperatura alta ocasionando paradas emergências nos Altos-Fornos, perdas de produção e instabilidade operacional. Diante deste problema, a antecipação de possíveis falhas no conjunto de sopro por temperatura alta foi fundamental para garantir operação estável dos altos-fornos. Analisar o processo, verificar procedimentos, pesquisar e aplicar novos materiais para adequar as condições operacionais é essencial para evitar o rompimento de conjunto de sopro por temperatura alta e elevar vida útil dos mesmos.

Oct 1, 2019