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Reduction kinetics ...
Reduction kinetics of commercial haematite pellet in a fixed bed at 1123-1273 K
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- Beheshti, Reza (författare)
- KTH,Materialvetenskap,Northern Research Institute Narvik, Norway
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Moosberg-Bustnes, John (författare)
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Kennedy, Mark W. (författare)
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Aune, Ragnhild E. (författare)
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(creator_code:org_t)
- 2016-03-18
- 2016
- Engelska.
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Ingår i: Ironmaking & steelmaking. - : Taylor & Francis. - 0301-9233 .- 1743-2812. ; 43:5, s. 394-402
- Relaterad länk:
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https://urn.kb.se/re...
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https://doi.org/10.1...
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Abstract
Ämnesord
Stäng
- In the present study a model for future use in the modelling of moving bed direct reduction reactors has been developed. The model of a fixed bed reactor for the production of sponge iron from haematite incorporates both heat-and mass-transfer, as well as the chemical reduction rate. The model results were compared to the experimental data obtained from a lab scale reactor in the temperature range 1123-1273 K, as well as to the output from a simple model assuming isothermal conditions. The H-2/CO ratio (beta) of the reducing gas was in all cases varied from 0.8 to 2.0. Overall the non-isothermal model developed permits a more accurate representation of the experimental data than the isothermal estimates, with a typical discrepancy of only 1.3%.
Ämnesord
- TEKNIK OCH TEKNOLOGIER -- Materialteknik -- Metallurgi och metalliska material (hsv//swe)
- ENGINEERING AND TECHNOLOGY -- Materials Engineering -- Metallurgy and Metallic Materials (hsv//eng)
Nyckelord
- Fixed bed
- Shrinking Core Model
- Gas-solid reaction
- Heat transfer
- Direct reduction
- Kinetics
- Haematite
Publikations- och innehållstyp
- ref (ämneskategori)
- art (ämneskategori)
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