2022
DOI: 10.1002/srin.202200056
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Numerical Treatment of Oxide Particle Dissolution in Multicomponent Slags with Local Gibbs Energy Minimization

Abstract: Herein, a diffusion model for the dissolution of oxide particles in multicomponent slag systems is developed. It is assumed in this model that a sharp-interface separates the solid particle from the liquid slag. Minimization of the Gibbs energy provides the conditions at the interface. The differential equations for multicomponent diffusion in the liquid slag are solved numerically via a finite-difference scheme. It is indicated via parameter studies that the diffusion controlled dissolution kinetics may resul… Show more

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Cited by 6 publications
(4 citation statements)
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“…phases in the binary CaO -SiO 2 system are taken from the assessment of Eriksson and Pelton [35] . The calculations are executed by means of a recently developed thermodynamic software package [36] .…”
Section: ½3mentioning
confidence: 99%
“…phases in the binary CaO -SiO 2 system are taken from the assessment of Eriksson and Pelton [35] . The calculations are executed by means of a recently developed thermodynamic software package [36] .…”
Section: ½3mentioning
confidence: 99%
“…The nonequilibrium models can further be classified based on the kinetics that are captured. Some of them are developed from the mass diffusion viewpoint and consider homogeneous spatial temperature fields . One such approach is the Scheil Gulliver that considers no solid diffusion and infinite liquid diffusivity .…”
Section: Introductionmentioning
confidence: 99%
“…Some of them are developed from the mass diffusion viewpoint and consider homogeneous spatial temperature fields. 22 One such approach is the Scheil Gulliver that considers no solid diffusion and infinite liquid diffusivity. 23 This might be restricted in terms of describing phase transformations for melt having limited diffusivity.…”
Section: Introductionmentioning
confidence: 99%
“…In several reported CLSM dissolution studies [9,10,[12][13][14][15][16][17][18][19][20][21][22][23], all of the influencing phenomena and parameters, particularly the effects of slag bath motion and Stefan flow, were not incorporated into the evaluation methods. Ogris and Gamsjaeger [26] accounted for Stefan flow, but the effect of bath motion was not considered. However, both of the phenomena were incorporated in Ref.…”
Section: Introductionmentioning
confidence: 99%