2014
DOI: 10.1016/j.calphad.2013.08.007
|View full text |Cite
|
Sign up to set email alerts
|

On the abilities and limitations of the linear, exponential and combined models to describe the temperature dependence of the excess Gibbs energy of solutions

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
15
0

Year Published

2014
2014
2023
2023

Publication Types

Select...
6

Relationship

0
6

Authors

Journals

citations
Cited by 31 publications
(15 citation statements)
references
References 36 publications
0
15
0
Order By: Relevance
“…[28][29][30][31] For a regular solution, S m is the ideal entropy of random mixing: In the present study, (Ru 1-x ,Ce x )O 2 is considered a generalized regular solution, and O a function of T and x.…”
Section: Thermodynamic Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…[28][29][30][31] For a regular solution, S m is the ideal entropy of random mixing: In the present study, (Ru 1-x ,Ce x )O 2 is considered a generalized regular solution, and O a function of T and x.…”
Section: Thermodynamic Methodsmentioning
confidence: 99%
“…In comparison, exponential models (O = H 0 exp ÀT/t ) may describe more complex behaviors and give good approximations for most binary systems. With the exponential model for instance, the G-x relations of (Ru 1Àx ,Ce x )O 2 at varied temperatures can be obtained based on eqn (9), (10), (20), (21), (30) and (31), the lattice instabilities and the results in Table 3. With the exponential model for instance, the G-x relations of (Ru 1Àx ,Ce x )O 2 at varied temperatures can be obtained based on eqn (9), (10), (20), (21), (30) and (31), the lattice instabilities and the results in Table 3.…”
Section: View Article Onlinementioning
confidence: 99%
“…So, the linear temperature dependence of polynomial coefficients of the liquid phase does not give physically reasonable values for the thermodynamic functions DG, DH, and DS at very low or high temperatures. [24] Most often, in the description…”
Section: Ideal Associated Solutions (Ias)mentioning
confidence: 99%
“…1. Attempts have been made to improve the modeling of temperature dependences, [24] but they require the introduction of new free parameters, although the associated solution model already gives reasonable temperature dependences of DG, DH, and DS from just D f H liq n and D f S liq n . The associated solution model, when used for systems with strong interaction between the components, is obviously free from the drawbacks listed above: both D f H liq n and D f S liq n have negative sign, and all the conditions (9-13) for DH and DG ex are met.…”
Section: Ideal Associated Solutions (Ias)mentioning
confidence: 99%
“…Other models having some degree of built‐in temperature dependence or the option of determining temperature‐dependent parameter values include COSMO‐RS, COSMO‐SAC, NRTL‐SAC, F‐SAC, linear solvation energy relationship (LSER) models such as the SPACE model, and models based on Hansen solubility parameters . Methods used to quantify temperature dependence include those involving correlation of partial molar excess enthalpy (for example, using a LSER expression and Kamlet–Taft molecular descriptors), methods involving combination of an excess Gibbs energy expression with an equation of state, and a method involving incorporation of a temperature‐dependence parameter related to relative excess enthalpy and entropy directly into the excess Gibbs energy expression . Modeling of activity coefficients, excess enthalpy and entropy, and phase equilibrium properties in general are active research areas with a variety of approaches including quantum mechanical charge density calculations, molecular modeling and molecular dynamics simulations, and phase stability analysis .…”
Section: Introductionmentioning
confidence: 99%