Kinetic Model for the Reaction Between Iron Oxide in Molten Slag and Carbon in Molten Iron via CO--CO sub 2 Bubble
The kinetic model for the reaction between iron oxide in molten slag and C in molten iron was developed, assuming carbon monoxide and CO sub 2 in the bubble on slag/metal interface was a ferrying medium for oxygen. The overall reaction was a combination of two reactions: reduction of FeO by carbon m...
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Veröffentlicht in: | Tetsu to hagane 1990-11, Vol.76 (11), p.2011-1018 |
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description | The kinetic model for the reaction between iron oxide in molten slag and C in molten iron was developed, assuming carbon monoxide and CO sub 2 in the bubble on slag/metal interface was a ferrying medium for oxygen. The overall reaction was a combination of two reactions: reduction of FeO by carbon monoxide and oxidation of the C by CO sub 2 . The slag/gas and gas/metal interfacial area were evaluated by calculating the shape of the bubbles and their occupying area on the slag/metal interface. The shape of the bubble was calculated assuming mechanical balance of surface and interfacial tensions and gravity. The bubble occupancy area was estimated by simulating the growth and detachment of the bubbles on slag/metal interaface. The calculated results are that the ratio of the slag/gas interfacial area to gas/metal is > 5, and that gas/metal interfacial area is < 30% of apparent slag/metal interface. Assuming the rate limiting step is either of the interfacial reactions, the overall reaction rate was calculated. The calculated rate is slower than published experimental data, suggesting that the two stage reaction mechanism could not be adequate with in this model. Graphs. 25 ref.--AA |
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The overall reaction was a combination of two reactions: reduction of FeO by carbon monoxide and oxidation of the C by CO sub 2 . The slag/gas and gas/metal interfacial area were evaluated by calculating the shape of the bubbles and their occupying area on the slag/metal interface. The shape of the bubble was calculated assuming mechanical balance of surface and interfacial tensions and gravity. The bubble occupancy area was estimated by simulating the growth and detachment of the bubbles on slag/metal interaface. The calculated results are that the ratio of the slag/gas interfacial area to gas/metal is > 5, and that gas/metal interfacial area is < 30% of apparent slag/metal interface. Assuming the rate limiting step is either of the interfacial reactions, the overall reaction rate was calculated. The calculated rate is slower than published experimental data, suggesting that the two stage reaction mechanism could not be adequate with in this model. Graphs. 25 ref.--AA</description><identifier>ISSN: 0021-1575</identifier><language>jpn</language><ispartof>Tetsu to hagane, 1990-11, Vol.76 (11), p.2011-1018</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780</link.rule.ids></links><search><creatorcontrib>Shibata, K</creatorcontrib><creatorcontrib>Kitamura, T</creatorcontrib><creatorcontrib>Tokumitsu, N</creatorcontrib><title>Kinetic Model for the Reaction Between Iron Oxide in Molten Slag and Carbon in Molten Iron via CO--CO sub 2 Bubble</title><title>Tetsu to hagane</title><description>The kinetic model for the reaction between iron oxide in molten slag and C in molten iron was developed, assuming carbon monoxide and CO sub 2 in the bubble on slag/metal interface was a ferrying medium for oxygen. The overall reaction was a combination of two reactions: reduction of FeO by carbon monoxide and oxidation of the C by CO sub 2 . The slag/gas and gas/metal interfacial area were evaluated by calculating the shape of the bubbles and their occupying area on the slag/metal interface. The shape of the bubble was calculated assuming mechanical balance of surface and interfacial tensions and gravity. The bubble occupancy area was estimated by simulating the growth and detachment of the bubbles on slag/metal interaface. The calculated results are that the ratio of the slag/gas interfacial area to gas/metal is > 5, and that gas/metal interfacial area is < 30% of apparent slag/metal interface. Assuming the rate limiting step is either of the interfacial reactions, the overall reaction rate was calculated. The calculated rate is slower than published experimental data, suggesting that the two stage reaction mechanism could not be adequate with in this model. 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The overall reaction was a combination of two reactions: reduction of FeO by carbon monoxide and oxidation of the C by CO sub 2 . The slag/gas and gas/metal interfacial area were evaluated by calculating the shape of the bubbles and their occupying area on the slag/metal interface. The shape of the bubble was calculated assuming mechanical balance of surface and interfacial tensions and gravity. The bubble occupancy area was estimated by simulating the growth and detachment of the bubbles on slag/metal interaface. The calculated results are that the ratio of the slag/gas interfacial area to gas/metal is > 5, and that gas/metal interfacial area is < 30% of apparent slag/metal interface. Assuming the rate limiting step is either of the interfacial reactions, the overall reaction rate was calculated. The calculated rate is slower than published experimental data, suggesting that the two stage reaction mechanism could not be adequate with in this model. Graphs. 25 ref.--AA</abstract></addata></record> |
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title | Kinetic Model for the Reaction Between Iron Oxide in Molten Slag and Carbon in Molten Iron via CO--CO sub 2 Bubble |
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