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Uday B. Pal. Agarwal, Ashish, 1975- Massachusetts Institute of Technology. Department of Materials Science and Engineering 2007-11-16T14:35:43Z 2007-11-16T14:35:43Z 1998 1998 http://hdl.handle.net/1721.1/39631 42075605 Thesis (S.M.)--Massachusetts Institute of Technology, Dept. of Materials Science and Engineering, 1998. Vita. Includes bibliographical references (leaf 63). The melting zone in a cupola has temperatures greater than 1773 K and a reducing atmosphere. This condition is suitable for the carbothermic reduction of silica. The key to the applicability of carbothermic reduction of silica for Ferro-alloy production is rapid in-situ production of SiC and its subsequent dissolution in the hot metal. The main objective of this investigation was to study the kinetics of the carbothermic reduction process and determine the optimum parameters for rapid and complete in-situ conversion of silica to SiC. At temperatures above 1773 K the key reactions in the carbothermic reduction process are (1) SiO2(s) + CO(g) = SiO(g) + C0 2(g), (2) SiO(g) + 2C(s) = SiC(s) + CO(g), (3) C(s) + C0 2(g) = 2CO(g). To meet the objective of this study, conditions must be such that the surface reactions occurring at the carbon and silica surfaces are rate limiting and the entire silica is converted to SiC. Pellet composition and structure in terms of carbon to silica ratio, their particle sizes and compaction pressure that ensure surface reaction is rate controlling, were determined. The gassolid reaction kinetics was mathematically modeled in terms of the process parameters. It was observed that the reaction kinetics improved by reducing both carbon and silica particle sizes. However, below a certain critical particle size there was no significant improvement in the reaction kinetics. For complete conversion of SiO2 to SiC, excess carbon and critical porosity are necessary to ensure that the entire SiO(g) generated by reaction (1) is consumed via reaction (2) within the pellet. by Ashish Agarwal. S.M. 64 leaves eng Massachusetts Institute of Technology M.I.T. theses are protected by copyright. They may be viewed from this source for any purpose, but reproduction or distribution in any format is prohibited without written permission. See provided URL for inquiries about permission. http://dspace.mit.edu/handle/1721.1/7582 Materials Science and Engineering Mechanism of silicon transfer in tuyere injected reactors by carbothermic reduction of silica Thesis application/pdf false Publication unknown unknown <Publication xmlns="https://www.openaire.eu/cerif-profile/1.1/" id="fe5eb472-c943-41e5-a0f9-c82ed4402315"> <Type xmlns="https://www.openaire.eu/cerif-profile/vocab/COAR_Publication_Types">http://purl.org/coar/resource_type/c_1843</Type> <Language>eng</Language> <Title>Mechanism of silicon transfer in tuyere injected reactors by carbothermic reduction of silica</Title> <PublishedIn> <Publication> </Publication> </PublishedIn> <PublicationDate>1998</PublicationDate> <Authors> <Author> <DisplayName>Agarwal, Ashish, 1975-</DisplayName> <Affiliation> <OrgUnit> </OrgUnit> </Affiliation> </Author> </Authors> <Editors> </Editors> <Publishers> <Publisher> <DisplayName>Massachusetts Institute of Technology</DisplayName> <OrgUnit /> </Publisher> </Publishers> <License>http://dspace.mit.edu/handle/1721.1/7582</License> <Keyword>Materials Science and Engineering</Keyword> <Abstract>The melting zone in a cupola has temperatures greater than 1773 K and a reducing atmosphere. This condition is suitable for the carbothermic reduction of silica. The key to the applicability of carbothermic reduction of silica for Ferro-alloy production is rapid in-situ production of SiC and its subsequent dissolution in the hot metal. The main objective of this investigation was to study the kinetics of the carbothermic reduction process and determine the optimum parameters for rapid and complete in-situ conversion of silica to SiC. At temperatures above 1773 K the key reactions in the carbothermic reduction process are (1) SiO2(s) + CO(g) = SiO(g) + C0 2(g), (2) SiO(g) + 2C(s) = SiC(s) + CO(g), (3) C(s) + C0 2(g) = 2CO(g). To meet the objective of this study, conditions must be such that the surface reactions occurring at the carbon and silica surfaces are rate limiting and the entire silica is converted to SiC. Pellet composition and structure in terms of carbon to silica ratio, their particle sizes and compaction pressure that ensure surface reaction is rate controlling, were determined. The gassolid reaction kinetics was mathematically modeled in terms of the process parameters. It was observed that the reaction kinetics improved by reducing both carbon and silica particle sizes. However, below a certain critical particle size there was no significant improvement in the reaction kinetics. For complete conversion of SiO2 to SiC, excess carbon and critical porosity are necessary to ensure that the entire SiO(g) generated by reaction (1) is consumed via reaction (2) within the pellet.</Abstract> <Access xmlns="http://purl.org/coar/access_right" > </Access> </Publication>