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FLUIDIZED-BED REDUCTION OF IRON-ORE FINES BY COAL FINES

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dc.contributor.author Haque, R.
dc.contributor.author Ray, H.S.
dc.contributor.author Mukherjee, A.
dc.date.accessioned 2018-10-01T12:19:23Z
dc.date.available 2018-10-01T12:19:23Z
dc.date.issued 1991
dc.identifier.citation ISIJ International, 31(11), 1991: 1279-1285
dc.identifier.issn 0915-1559
dc.identifier.uri http://ore.immt.res.in/handle/2018/338
dc.description.abstract Reduction of iron ore fines by coal fines in a bed fluidized by air has been studied, The investigation includes study of the kinetic aspect of reduction and effect of major process variables. The variables used are time, temperature, coal/ore ratio and air flow rate. The kinetic data of reduction fit the first order reaction model. Within the range of variables studied, an increase in reaction temperature and coal/ore ratio of the reduction mixture result in higher reduction rate, whereas, increase in air flow rate adversely affects the reduction rate. The activation energy for the reduction reaction is found to be about 1 55 kJ/mol.
dc.language en
dc.publisher Iron Steel Inst Japan Keidanren Kaikan
dc.relation.isreferencedby SCI
dc.rights Copyright [1991]. All efforts have been made to respect the copyright to the best of our knowledge. Inadvertent omissions, if brought to our notice, stand for correction and withdrawal of document from this repository.
dc.subject Materials Sciences
dc.subject Materials Sciences
dc.title FLUIDIZED-BED REDUCTION OF IRON-ORE FINES BY COAL FINES
dc.type Journal Article
dc.affiliation.author CSIR-IMMT, Bhubaneswar 751013, Odisha, India


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