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Carbothermal solid state reduction of manganese oxide and ores in different gas atmospheresKononov, Ring, Materials Science & Engineering, Faculty of Science, UNSW January 2008 (has links)
The aim of the project was to establish rate and mechanisms of solid state reduction of manganese ores. The project studied carbothermal reduction of manganese oxide MnO, two Groote Eylandt (Australian) and Wessels (South African) manganese ores in hydrogen, helium and argon atmospheres at temperatures up to 1400C for MnO and 1200C for manganese ores. Experiments were conducted in the fixed bed reactor with on-line off-gas analysis. The major findings are as follows. ?? Rate and degree of reduction of MnO and ores increased with increasing temperature. ?? Reduction of MnO and manganese ores at temperatures up to 1200C was faster in helium than in argon, and much faster in hydrogen than in helium. The difference in MnO reduction in hydrogen and helium decreased with increasing temperature to 1400C. ?? Addition of up to 7 vol% of carbon monoxide to hydrogen had no effect on MnO reduction at 1200C. ?? In the process of carbothermal reduction of ores in hydrogen at 1200C, silica was reduced. ?? Reduction of both GE ores was slower than of Wessels ore. This was attributed to high content of iron oxide in the Wessels ore. ?? Carbon content in the graphite-ore mixture had a strong effect on phases formed in the process of reduction; thus, in the reduction of Wessels ore with 12-16 wt% C, a-Mn and Mn23C6 were formed; when carbon content was above 20 wt%, oxides were reduced to carbide (Mn,Fe)7C3. ?? Kinetic analysis showed that mass transfer of intermediate CO2 from oxide to graphite in carbothermal reduction in inert atmosphere was a contributing factor in the rate control. ?? High rate of reduction of manganese oxide in hydrogen was attributed to formation of methane which facilitated mass transfer of carbon from graphite to oxide. Hydrogen was also directly involved in reduction of manganese ore reducing iron oxides to metallic iron and higher manganese oxides to MnO. Reduction of Wessels and Groote Eyland Premium Fines ores in the solid state is feasible at temperatures up to 1200C; while temperature for solid state reduction of Groote Eyland Premium Sands is limited by 1100C.
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Carbothermal solid state reduction of manganese oxide and ores in different gas atmospheresKononov, Ring, Materials Science & Engineering, Faculty of Science, UNSW January 2008 (has links)
The aim of the project was to establish rate and mechanisms of solid state reduction of manganese ores. The project studied carbothermal reduction of manganese oxide MnO, two Groote Eylandt (Australian) and Wessels (South African) manganese ores in hydrogen, helium and argon atmospheres at temperatures up to 1400C for MnO and 1200C for manganese ores. Experiments were conducted in the fixed bed reactor with on-line off-gas analysis. The major findings are as follows. ?? Rate and degree of reduction of MnO and ores increased with increasing temperature. ?? Reduction of MnO and manganese ores at temperatures up to 1200C was faster in helium than in argon, and much faster in hydrogen than in helium. The difference in MnO reduction in hydrogen and helium decreased with increasing temperature to 1400C. ?? Addition of up to 7 vol% of carbon monoxide to hydrogen had no effect on MnO reduction at 1200C. ?? In the process of carbothermal reduction of ores in hydrogen at 1200C, silica was reduced. ?? Reduction of both GE ores was slower than of Wessels ore. This was attributed to high content of iron oxide in the Wessels ore. ?? Carbon content in the graphite-ore mixture had a strong effect on phases formed in the process of reduction; thus, in the reduction of Wessels ore with 12-16 wt% C, a-Mn and Mn23C6 were formed; when carbon content was above 20 wt%, oxides were reduced to carbide (Mn,Fe)7C3. ?? Kinetic analysis showed that mass transfer of intermediate CO2 from oxide to graphite in carbothermal reduction in inert atmosphere was a contributing factor in the rate control. ?? High rate of reduction of manganese oxide in hydrogen was attributed to formation of methane which facilitated mass transfer of carbon from graphite to oxide. Hydrogen was also directly involved in reduction of manganese ore reducing iron oxides to metallic iron and higher manganese oxides to MnO. Reduction of Wessels and Groote Eyland Premium Fines ores in the solid state is feasible at temperatures up to 1200C; while temperature for solid state reduction of Groote Eyland Premium Sands is limited by 1100C.
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Sintese e caracterizacao de ceramicas biomorficasRAMBO, CARLOS R. 09 October 2014 (has links)
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Desenvolvimento, processamento e caracterizacao de compositos ceramicos Sisub(3)Nsub(4)-SiCsub(w)BALDACIM, SANDRO A. 09 October 2014 (has links)
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Desenvolvimento de um sistema de protecao antioxidante para o composito carbono-carbonoCAIRO, CARLOS A.A. 09 October 2014 (has links)
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Resistência ao choque térmico de carbeto de silício sinterizado via fase líquida / Thermal shock resistance of liquid phase sintered silicon carbideMELLO, ROBERTA M. de 22 June 2016 (has links)
Submitted by Claudinei Pracidelli (cpracide@ipen.br) on 2016-06-22T11:45:07Z
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Sintese e caracterizacao de ceramicas biomorficasRAMBO, CARLOS R. 09 October 2014 (has links)
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Desenvolvimento, processamento e caracterizacao de compositos ceramicos Sisub(3)Nsub(4)-SiCsub(w)BALDACIM, SANDRO A. 09 October 2014 (has links)
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Desenvolvimento de um sistema de protecao antioxidante para o composito carbono-carbonoCAIRO, CARLOS A.A. 09 October 2014 (has links)
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Resistência ao choque térmico de carbeto de silício sinterizado via fase líquida / Thermal shock resistance of liquid phase sintered silicon carbideMELLO, ROBERTA M. de 22 June 2016 (has links)
Submitted by Claudinei Pracidelli (cpracide@ipen.br) on 2016-06-22T11:45:07Z
No. of bitstreams: 0 / Made available in DSpace on 2016-06-22T11:45:07Z (GMT). No. of bitstreams: 0 / O comportamento dos materiais cerâmicos quanto à resistência ao choque térmico é um tema de grande interesse, devido às aplicações em que a confiabilidade frente a variações bruscas de temperatura é necessária. Neste trabalho foi estudado como a variação na proporção dos aditivos Y2O3:Al2O3 e diferentes parâmetros no processamento do carbeto de silício sinterizado via fase líquida como, tipo e temperatura de sinterização, podem influenciar na resistência ao choque térmico deste material. As misturas foram preparadas com 90%SiC+10%Y2O3:Al2O3 em mol, variando as proporções molares dos óxidos entre 2:1 e 1:4, com e sem prévia reação dos aditivos. As misturas foram compactadas e sinterizadas em forno resistivo de grafite nas temperaturas de 1750°C, 1850°C e 1950°C e, por prensagem a quente, a 1750°C e 1850°C, sendo avaliadas quanto à densificação. Após análise dos resultados preliminares, a sinterização sem pressão e as misturas com proporções 1:3 e 1:4 de Y2O3:Al2O3 previamente reagidos foram selecionadas para o estudo da resistência ao choque térmico. Os ciclos térmicos foram realizados com aquecimento em temperaturas de 600°C, 750°C e 900°C e resfriamento brusco em água em temperatura ambiente. A avaliação das amostras quanto à resistência ao choque térmico, feita por meio da determinação de módulo de elasticidade, porosidade, resistência à flexão e por análise microestrutural de trincas. As amostras sinterizadas na temperatura de 1950°C são as que apresentam o melhor desempenho em relação à resistência ao choque térmico, enquanto a variação na proporção Y2O3:Al2O3 de 1:3 para 1:4 não altera significativamente esta propriedade. Nas condições utilizadas, a temperatura máxima de aplicação do SiC sinterizado via fase líquida deve ser limitada a 750°C, permitindo seu uso como trocadores de calor, rolamentos, mancais de bombas submersas, turbinas a gás e sensor de motores automotivos e aeronáuticos. / Tese (Doutorado em Tecnologia Nuclear) / IPEN/T / Instituto de Pesquisas Energeticas e Nucleares - IPEN-CNEN/SP
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