2011
DOI: 10.1016/j.jct.2011.05.038
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Thermodynamic optimization of the (Na2O+SiO2+NaF+SiF4) reciprocal system using the Modified Quasichemical Model in the Quadruplet Approximation

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Cited by 32 publications
(34 citation statements)
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“…The properties of the liquid solution in the multicomponent system are adjusted with the extrapolation of binary parameters, in common ion and reciprocal systems, as described in [8], and with ternary parameters. The extrapolation of the model parameters requires the use of composition variables, v ij=k 2 and n ij=k 2 , described in [4,8], which affect the composition dependence of Dg AB=XY in all reactions similar to reactions (1) and (2). Recent modifications [9] for the extrapolation of model parameters in reciprocal systems have been presented in [2].…”
Section: Thermodynamic Modelingmentioning
confidence: 99%
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“…The properties of the liquid solution in the multicomponent system are adjusted with the extrapolation of binary parameters, in common ion and reciprocal systems, as described in [8], and with ternary parameters. The extrapolation of the model parameters requires the use of composition variables, v ij=k 2 and n ij=k 2 , described in [4,8], which affect the composition dependence of Dg AB=XY in all reactions similar to reactions (1) and (2). Recent modifications [9] for the extrapolation of model parameters in reciprocal systems have been presented in [2].…”
Section: Thermodynamic Modelingmentioning
confidence: 99%
“…The extrapolation of the model parameters requires the use of composition variables, v ij=k 2 and n ij=k 2 , described in [4,8], which affect the composition dependence of Dg AB=XY in all reactions similar to reactions (1) and (2). Recent modifications [9] for the extrapolation of model parameters in reciprocal systems have been presented in [2]. In common ion multicomponent systems, the extrapolation of binary parameters is made in each ternary subsystems according to two different possibilities [8]: a symmetric one and an asymmetric one, similar to the Kohler [10] and the Kohler-Toop [11] equations respectively.…”
Section: Thermodynamic Modelingmentioning
confidence: 99%
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