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Sökning: WFRF:(Tilliander Anders) > (2005-2009) > Dynamic Modeling of...

Dynamic Modeling of Steel, Slag and Gas Reactions during Initial Blowing in a Top-Blown Converter

Ersson, Mikael, 1977- (författare)
KTH,Tillämpad processmetallurgi
Höglund, Lars (författare)
KTH,Tillämpad processmetallurgi
Tilliander, Anders (författare)
KTH,Tillämpad processmetallurgi
visa fler...
Jonsson, Lage (författare)
KTH,Tillämpad processmetallurgi
Jönsson, Pär (författare)
KTH,Tillämpad processmetallurgi
visa färre...
 (creator_code:org_t)
2008
2008
Engelska.
Ingår i: ISIJ International. - 0915-1559 .- 1347-5460.
  • Tidskriftsartikel (övrigt vetenskapligt/konstnärligt)
Abstract Ämnesord
Stäng  
  • A dynamic modeling approach is presented where a computational fluid dynamics software is coupled to a thermodynamics software to obtain simulations of reactions between steel, slag and gas in a top-blown converter. For each simulation the transport of momentum, energy and mass of species as well as the thermodynamic equilibrium in each cell containing at least two phases was treated. The overall conclusion is that the present calculation procedure is successful for dynamic simulations of interaction between an oxygen gas jet with a melt and a slag. The predicted rate of decarburization was found to agree well with experimental data from laboratory trials. In addition, four cases where simulated for which the temperature, the dissolved carbon content and the dissolved oxygen content were varied. The most important findings from these comparisons were that: i) a higher initial oxygen concentration in the melt yields a larger decarburization rate, ii) carbon content also plays a big role for the desiliconization where a low carbon content is required for desiliconization to take place, iii) decarburization and desiliconization is largely influenced by the temperature at which reactions take place, where low temperature favors desiliconization and iv) the region affected by a lower carbon/silicon concentration (hot-spot region) directly below the jet was approximately 10 mm for the current setup.

Nyckelord

converter
CFD
thermodynamics
modeling
slag
gas
TECHNOLOGY
TEKNIKVETENSKAP

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