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This paper deals mainly with the modernization in the coal loading system at the loading piers of the Dominion Coal Company, Ltd., Sydney, Nova Scotia. The history of the operation is briefly outlined, and the construction of the Company's new pier is described in considerable de-tail. Particular attention is paid to the bins and conveyors, and to the loading tower. The paper concludes with a description of the S.S. Cape Breton Miner, built specifically for the coal trade, and the unloading facilities at Lakeview, Ontario. Coal Shipping at Sydney C OAL from the mines operated in Cape Breton by the Dominion Coal Company, Limited, has been shipped from the International Piers, situated on the east side of Sydney Harbour, for over sixty years. There were three piers, of which two were active-ly used in the shipping of coal until 1964. Nos. 2 and 3 were high piers about 600 feet long, of wooden construction throughout. They were founded on' rock-filled cribs and creosoted piles driven into the harbour bottom, and each had two decks which carried standard-gauge railway tracks.

Jan 1, 1965

By A. H. Tousley

The cement industry is on the horns of an economic dilemma. Within the last ten years, its over- capacity in the United States has varied from 139- 127% of demand (Fig. 1). The most direct effect of this is seen in cement prices, which reached a peak in 1960, retreated steadily through 1966 and only recently climbed back to the 1960 level again. With prices in a slump and production costs estimated to be up almost 30%, there has been a steady drain on cement profits. Since 1960, labor costs have increased 86% while fuel costs have risen 18%. Meanwhile, customer service costs have also soared owing to the competition for cement customers and the wider variety of available cement products. This search for sales advantage has in turn led to a higher Blaine number, which means more grinding and hence bigger mills, more power, and, once again, higher costs. New plants as well as expansions and revisions to existing plants are also costing more owing to higher

Jan 1, 1971

By Donald Ingvoldstad, Harold E. Lee

At Bunker Hill the original charge storage and preparation system was installed in 1917 to accommodate lead-silver gravity mill products. Only minor tonnages of wet fines such as vanner and flotation concentrates were received. Charge flux and diluent requirements were provided by an ample supply of siderite middlings and coarse limerock. While oversize material was crushed through Y4-in., the use of roll crushers in series resulted in a more or less granular, free-running charge of adequate porosity. Under such conditions, receipts could be proportioned directly from receiving bins, and suitable blending was obtained by passing the resultant layered composite through a small Stedman disintegrator. This elementary system served well for production and smelting of an extremely lead-rich sinter, in the low column blast furnace. Here sinter physical quality is less critical, and appreciable quantities of raw flux and oxidized ore may be charged directly to the blast furnace without seriously impairing furnace capacity.

Oct 1, 1956

By C. A. Sutherland

"Smelting of copper-gold ore from nearby Rossland mines started at Trail in the 1890s. As ore from the Rossland mines became exhausted, lead smelting offhand-sorted galena orefrom other British Columbia mines was initiated. With the development of flotation technology for the separation of lead, zinc, and iron sulphides in the first two decades of this century, the large Sullivan orebody at Kimberley, British Columbia, became the foundation for the growth of a major zinc and lead smelter at Trail. Lead smelting began in 1901, electrolytic zinc in 1916, and by 1984, the Trail metallurgical complex had produced 10 million tons of each metal. Its present capacity is 270000 tonnes per year of zinc and 110 000 tonnes/year of lead.This paper reviews the history of technological changes in the Trail production plants, emphasizing the zinc plant modernization program started in the 1970s, and also the planned introduction of the QSL oxygen lead smelting process in the late 1980s. Lead modernization will increase production capacity to a maximum of 160000 tonnes per year.IntroductionCopper-gold ore was discovered at Rossland, British Columbia, in the year 1890, starting a mining industry that was to last over three decade s. Selected ore was at first transported at high cost to distant U.S. smelters, so there naturally followed a decision to construct a small copper smelter to process the local ore to matte. It was built in 1896 at the mouth of Trail Creek on the Columbia River, about 10 km from Rossland. This little smelter was to develop and diversify in the next 90 years into the world's largest lead-zinc produce.The mining boom that occurred in the northwestern United States and southeastern British Columbia in the period of 1890 to 1910 saw the brief operation of many small local smelters. The only one to survive was the smelter at Trail. The circumstances that permitted its continued life and subsequent growth, form a fascinating history of business deals, litigation, and steady technical progress.Early investment in local railway transportation and options by F.A. Heinze, the smelter' s founder, attracted the attention of the Canadian Pacific Railway Company, which purchased Heinze' s assets in 1898. This provided the capital base for survival and growth of the smelter, which remained and prospered under the Canadian Pacific umbrella for almost ninety years. It was registered as the Consolidated Mining and Smelting Company of Canada Limited in 1906; in 1966, this name was shortened to Cominco Ltd."

Jan 1, 1988

By C. A. Sutherland

"Smelting of copper-gold ore from nearby Rossland mines started at Trail in the 1890s. As ore from the Rossland mines became exhausted, lead smelting of hand-sorted galena ore from other British Columbia mines was initiated. With the development of flotation technology for the separation of lead, zinc, and iron sulphides in the first two decades of this century, the large Sullivan orebody at Kimberley, British Columbia, became the f oundation for the growth of a major zinc and lead smelter at Trail. Lead smelting began in 1901, electrolytic zinc in 1916, and by 1984, the Trail metallurgical complex had produced 10 million tons of each metal. Its present capacity is 270000 tonnes per year of zinc and 110 000 tonnes/year of lead.This paper reviews the history of technological changes in the Trail production plants, emphasizing the zinc plant modernization program started in the 1970s, and also the planned introduction of the QSL oxygen lead smelting process in the late 1980s. Lead modernization will increase production capacity to a maximum of 160000 tonnes per year.IntroductionCopper-gold ore was discovered at Rossland, British Columbia, in the year 1890, starting a mining industry that was to last over three decade s. Selected ore was at first transported at high cost to distant U.S. smelters, so there naturally followed a decision to construct a small copper smelter to process the local ore to matte. It was built in 1896 at the mouth of Trail Creek on the Columbia River, about 10 km from Rossland. This little smelter was to develop and diversify in the next 90 years into the world 's largest lead-zinc producer).The mining boom that occurred in the northwestern United States and southeastern British Columbia in the period of 1890 to 1910 saw the brief operation of many small local smelters. The only one to survive was the smelter at Trail. The circumstances that permitted its continued life and subsequent growth, form a fascinating history of business deals, litigation, andsteady technical progress.Early investment in local railway transportation and options by F.A. Heinze, the smelter' s founder, attracted the attention of the Canadian Pacific Railway Company, which purchased Heinze' s assets in 1898. This provided the capital base for survival and growth of the smelter, which remained and prospered under the Canadian Pacific umbrella for almost ninety years. It was registered as the Consolidated Mining and Smelting Company of Canada Limited in 1906; in 1966, this name wasshortened to Cominco Ltd.The Rossland mines continued to supply copper ore for the smelter until the late 1920s, but lead-silver ore also became available from the contemporary mining boom in the Slocan area, about 80 km away. In 1901, the Trail smelter diversified into lead; and when the CM&S Co. acquired the St. Eugene Mine at Moyie and the Sullivan Mine at Kimberley, the smelter was guaranteed a firm supply of lead ore. The company also purchased the West Kootenay Power and Light Company, which even before the turn of the century had constructed the first of four hydroelectric generating plants on the Kootenay River near Trail. This acquisition assured the CM&S smelter and its local mines of a stable power supply and the opportunity to diversify into power intensive technology."

Jan 1, 1988

By K. Pienimäki

Boliden Harjavalta Oy has produced copper since 1945. The essential idea has always been continuous development of process efficiency and environmental friendliness by using the Best Available Techniques (BAT). The ongoing development step is to increase the production capacity up to 210 000 tpy of anode copper and 155 000 tpy of copper cathode. One of the focal issues in this action is modernization of the copper refinery to utilize permanent cathode technology. This paper describes the refinery project and the technology used in it.

Jan 1, 2007

By A. C. Legg

BCL Limited operates a nickel-copper flash smelting operation at Selebi-Phikwe, situated in north-eastern Botswana. The original furnace was commissioned in 1973 and produces a high grade sulphide matte, from its own concentrates plus additional custom feeds, which is shipped to refineries in Zimbabwe and Norway for further processing. In 2004 the company embarked on a study to modernize the flash smelting complex, with an emphasis on extending campaign life, improving the furnace integrity and enhancing throughput and process efficiency. First phase initiatives from this exercise, including the fundamental switch to a single concentrate burner operation of the flash smelting furnace, were implemented in July 2007. This paper summarizes experiences prior to implementation, details the specific improvements made to the flash smelting furnace and associated operations, highlights the improved plant performance after modernization, and outlines second phase expansion plans that are currently under consideration.

Jan 1, 2009

By J. Y. Aubut

The modernization of the CCR Refinery to permanent cathode technology is presently underway. The 360,000 mt/y refinery is being retrofitted to accept the Kidd process. Part of this modernization includes the installation of Kidd stripping machines, and the total replacement of the materials handling equipment. It also involves the reinforcement of building structures to accept the new equipment and the ability to operate in different modes. The future equipment will interface with some existing apparatus, which is being retained for future operations. The whole operation will be automated and will allow product traceability for quality purposes. This retrofit poses important challenges given the size and scope of the modernization project and because it is being undertaken concurrently with normal plant operations.

Jan 1, 1999

By Bruce V. Kiefer

A modernization project was undertaken by Kroman Celik Sanayii A.S. in order to improve their product quality, consistency and shape of the coil package, reduce maintenance and delays in rod mill, thereby increasing utilization and productivity. The project involved installation of a new Morgan Intelligent Pinch Roll and High Speed Laying Head, modifications to the existing controlled cooling conveyor, plus replacing the coil reforming station. The new pinch roll and laying head were to provide better control of the ring formation and consistency of the coil on the conveyor, while reducing delays on the conveyor. Changes to the controlled cooling conveyor included installation of new nozzle decks and Optimesh air distribution system along with re-arrangement of existing fans in order to improve both cooling rates and uniformity of cooling. This paper explains details and features of the newly-installed equipment technology. Resulting product and process improvements are presented, including increased tensile strength and uniformity, reduction in delays on the conveyor and reform tub, plus improvements in coil quality.

Oct 30, 2017

By Knut H. Hubert

The GRATE-KILN System plant at Svappavaara, Sweden, was constructed for LKAB by Allis-Chalmers under a turnkey contract and commissioned in 1969. The plant was designed to produce iron ore pellets from magnetite concentrate at 6100 mtpd using imported fuel oil. It represented the state of the art for plants of its type at the time. Fuel rated capacity was attained within one week of start-up. Product quality, power usage, fuel consumption and machine wear were within warranty limits during sustained production thereafter. As operator skills improved and gas handling system reserve capability was utilized, the plant frequently produced acceptable product at up to 115% of design capacity. During the period 1969 to 1976, market demands increased for high-quality pellets while energy costs rose steadily. At the same time, important advances in the design of GRATE-KILN Systems were being made in other plants constructed by Allis-Chalmers.

Jan 1, 1980

By Abhoy Mukherjee

The Luanshya Smelter is a traditional Reverberatory Smelter which once worked with up to three coal-fired reverbs, and now operates one Reverb and one hot Peirce- Smith Converter, projected to produce approximately 42.000 tons per year of copper anodes. The aim of this study is to select a smelting technology which best fits the upgrading of the Smelter, such that low capital and operating costs are achieved for the projected design production capacity of 60.000 tpy, limited by the available supplies of concentrates. An equally important requisite is the compliance of present and future environmental regulations, which determines the need to install and Acid Plant to treat the smelter primary gases. In the process selection study, the following technologies were analyzed, at a Conceptual Engineering level: the Oxy-fuel Burner Reverb, the Teniente Converter, the CONTOP Cyclone Smelting Reactor, and further, the Ausmelt Furnace, the engineering of which was provided by the proprietary firm. The engineering of the other processes was developed by INDEC, which also integrated the comparative analysis of the four options. The analysis of a comprehensive set of technical factors, including integrated smelter metallurgical models, together with the evaluations of economical features, led to the selection of the CONTOP Smelting Technology for the modernization of the Luanshya Smelter.

Jan 1, 1999

By Jack C. Haptonstall

Abstract-Minas de San Luis, S.A. operates the old Tayoltita mine located in the Sierra Madre Occidental in Durango, Mexico. Yearly production is 55 000 kg (1.7 million troy ox) of silver and 1000 kg (31,000 troy ox) of gold from milling 165 000 t/y (181,900 stpy) obtained from fissure veins. A 4.4 km (2.75 miles) adit, to intersect the veins below existing workings, was completed in 1974. The adit and ancillary projects facilitated extensive mechanization of the mine, ramp development of it, integration of duplicate facilities and elimination of obsolete facilities. It provided a deep-level access for exploration and development of the veins, and resulted in a 25% increase in production with the same labor force. The cost of the in-house financed project was $3.4 million.

Jan 2, 1978

By Jack C. Haptonstall

This paper describes the analytical characteristics of Western subbituminous coal and the manner in which these characteristics apply to their use in a utility-sized steam generator. It compares these characteristics with those of typical Midwestern coal and Eastern bituminous coal. The paper also reviews in detail the design considerations that must receive attention when various blends of these three coals, or any combinations thereof, are planned to be used. This research paper describes variations in analytical and utilization characteristics when coals from different origins are blended in order to achieve a predetermined sulfur content for the purpose of predicting sulfur oxides emissions as they affect environmental regulations and the resulting alterations in utilization characteristics such blending would cause, and how such blends of coal would affect a utility-sized steam generator.

Jan 1, 1979

By Jack C. Haptonstall

The Tayoltita Unit of Minas de San Luis, S. A. is situated in an isolated corner of the state of Durango, Mexico. The ore deposits in the region were first worked by Indians, but by 1757 the Spaniards had discovered them, and the first systematic exploitation of the mines commenced. By the early 1900's most of the mines had been acquired by American interests, and the San Luis Mining Company was organized. The modern period of exploitation, uninterrupted for the last 74 years, began. In 1962 the company was fully "Mexicenized" in compliance with the modification of the mining law, and the name was changed to Minas de San Luis, S. A. Tayoltita continues as one of Mexico's most important silver and gold mines. The ore is extracted in en extensive underground operation, mining epithermal fissure veins by selective methods. The ore is milled and treated in an efficient counter-current cyanide plant, where 95 % of the silver and 96 % of the gold is recovered. Current annual bullion output is 55,000 kg (1.7 million troy oz) of silver and 1000 kg (31,000 troy oz) of gold from milling 165,000 try (181,900 stpy). Rough, 33-kg (1000-troy oz) bullion bars are smelted at the mine, shipped by air to Mazatlan, Sinaloa, and are thence sold to the Met- Mex Peñoles smelter in Torreon, Coahuila. Ore reserves, blocked by very conservative methods, are currently at 540,000 tons (595,000 st). Ore reserve grade is 425 g of silver and 6 g of gold per ton (12.4 troy oz Ag and 0.18 troy oz Au per st).

Jan 1, 1976

By Milson de Andrade Júnior

A central termoelétrica número 1 (CTE#1) da Companhia Siderúrgica Nacional possui duas caldeiras em operação denominadas 8 e 9 com capacidade total de produção de vapor de 200 Toneladas por hora. Estas caldeiras fornecem vapor para os turbo geradores e turbo sopradores da CTE#1, além de vapor de processo para a Usina Presidente Vargas (UPV). As caldeiras entraram em operação em 1982/83 e seus sistemas de controle e instrumentação eram totalmente pneumáticos. Ao longo do tempo foi surgindo dificuldades para reposição e manutenção dos componentes pneumáticos, motivo pelo qual se iniciaram os estudos para substituição deste sistema. Em 2009 teve início um projeto para substituição do controle pneumático por um controle microprocessado feito por PLC redundante trabalhando com um supervisório scada e para substituição das malhas de instrumentação pneumática por instrumentação em rede fieldbus. A substituição completa dos componentes pneumáticos foi concluída em 2012. O novo sistema implantado trouxe diversas melhorias na performance, confiabilidade, segurança operacional e ergonomia. Este trabalho apresenta as causas que motivaram o projeto em questão, a metodologia utilizada para a sua implantação e os resultados alcançados com a aplicação de tecnologia moderna para controle e instrumentação de caldeiras.

Jul 31, 2018

By Douglas Leal Lemos

Na Aciaria-LD CSN obtém duas estações de gusa, chamadas de Estação Leste e Oeste. A logística de transporte do gusa produzido no Alto Forno até a Aciaria é feita através dos Carros Torpedos. Nas estações são feitos cambamentos dos carros para abastecer panelas de gusa, que levarão até os Conversores. Para efetuar este movimento de cambagem é necessário controlar dois motores de corrente continua e freios que obtém nos carros. Na UPV obtém vinte e sete carros torpedos em operação, assim o controle deve estar preparado para controlar todos. Antes da modernização o painel funcionava sem nenhuma tecnologia de controle e obtinha alto custo de manutenção. Em virtude destes aspectos novo sistema obtém conversores estáticos que controlam motores e controlador responsável para efetuar balanceamento de carga do gusa. Este projeto tem como objetivo garantir continuidade operacional do sistema além de gerar maior confiabilidade no equipamento e uma alta tecnologia para efetuar melhorias, analise de defeitos entre outros. O rendimento após a implantação é fantástica devido ao controle preciso obtido além da rastreabilidade de todas as variáveis do sistema e um custo de manutenção baixíssimo, tornando-se um equipamento no estado da arte.

Aug 16, 2017

By Silvio de Carvalho Sabença

Um forno a arco elétrico é um tipo de forno industrial que usa uma corrente elétrica alternada para produzir calor. Estes equipamentos servem como uma alternativa para os altos fornos tradicionais, e desempenham um papel importante na produção de aço. Em um forno de arco elétrico, a corrente elétrica passa através dos eletrodos de grafite, do aço e de outros metais, o que resulta na produção de aço de modo mais rápido e eficiente. A queda de tensão no arco é, praticamente, proporcional à distância entre o eletrodo e a carga. O eletrodo corresponde ao polo positivo (+) e a carga o negativo (-). Em corrente alternada os pólos, positivo e negativo, trocam de posição a cada meio ciclo da tensão de rede. Sob condições de arco, forma-se, no eletrodo e na carga, uma finíssima camada altamente ionizada devida a uma altíssima concentração do campo elétrico nestas zonas. No forno o arco se extingue quando a corrente se anula e reacende, quando a tensão volta a crescer. Devido a constantes quebra de eletrodo foi montado o grupo de trabalho com objetivo de reduzir o consumo dos eletrodos, otimização do consumo de energia, redução do Power On, aumento da potência média e redução nas quebras de eletrodos. Esta implantação foi extremamente importante pois o mesmo está garantindo a continuidade operacional, de forma segura e confiável, de um dos equipamentos mais importantes para a produção de aço na Usina.

Aug 17, 2017

By Ana Paola Villalva Braga

O objetivo deste trabalho é apresentar as soluções implementadas para modernização e automação do laminador piloto do Instituto de Pesquisas Tecnológicas do Estado de São Paulo-IPT, importante ferramenta de pesquisa do seu Centro de Tecnologia em Metalurgia e Materiais. O IPT, em parceria com o Laboratório de Fenômenos de Superfície da EPUSP, tem trabalhado nas duas últimas décadas com o desenvolvimento de ligas resistentes a desgaste, principalmente para uso em cilindros de trabalho para laminação a quente. Com recursos provenientes de projeto co-financiado pelo BNDES e pela Gerdau, o laminador piloto e o forno de indução para aquecimento de placas foram reformados e modernizados, permitindo que a célula de laminação trabalhe de forma autônoma e que os dados de processo sejam continuamente registrados. Nesse projeto estão sendo conduzidos ensaios de laminação de longa duração para caracterizar e quantificar o dano progressivo imposto aos cilindros pela laminação a quente de placas de aço carbono sob condições controladas de temperatura e grau de deformação e de refrigeração dos cilindros. A modernização do laminador envolveu 3 etapas: reforma e automação do laminador e do forno de aquecimento; montagem do sistema de refrigeração dos cilindros e instrumentação dos cilindros de trabalho.

Jul 30, 2018

By Alexandre Carvalho Martins

Este trabalho tem por objetivo apresentar o projeto de modernização do sistema de supervisão da Mina, Britagem e Concentrador I da unidade de Germano da Samarco Mineração. A principal motivação que levou a Samarco a modernização do sistema de supervisão foi o fato da aplicação atual já estar saturada, dificultando novas implementações, além de já apresentar limitações no diagnóstico de defeitos e intertravamentos. Na solução implementada, destaca-se a estratégia de virtualização adotada, o sistema para cadastramento e modificação em tempo real das entidades do CLP e as funcionalidades para gestão de alarmes.

Jul 30, 2018

By Mauro Martins Machado

As misturadoras da UPG têm como finalidade produzir uma mistura de gases denominada HN, combinando proporcionalmente o Hidrogênio e Nitrogênio (75/25 e 5/95) para gerar a atmosfera de proteção para os fornos das linhas de zincagem, linhas de recozimento de chapas, forno de caixa e linha de recozimento contínuo de chapas. Os antigos analisadores Hidros 100 (Fisher Rosemount) e Thermomat (Fuji) que operavam nas misturadoras foram fabricados na década de 90 e apresentava baixa confiabilidade operacional, dificuldades de ajustes, falhas intermitentes de difícil diagnóstico e risco de misturas não controladas de Hidrogênio com Nitrogênio. Além disso, não possuíam mais suporte técnico do fabricante e nem sobressalentes para manutenção. Nesse cenário, este trabalho tem como objetivo apresentar a modernização desses equipamentos por analisadores atuais de fácil operação e configuração, manutenção simples e diagnóstico de falhas integrado e com maior confiabilidade, fator imprescindível para garantir a disponibilidade de produção. Os novos analisadores implantados fornecem análises mais precisas e confiáveis em tempo real, para o sistema de controle de correção da mistura do HN. Os resultados obtidos foram significativos para as atuais condições de funcionamento. Representando aumento da segurança operacional, redução dos custos de manutenção com o equipamento e gerando ganhos de produtividade e de competitividade para as áreas consumidoras na UPV.

Sep 25, 2017