Normal paraffin (
N
-alkane)-based wax is well known
as a severe problem in petroleum production, transportation, and processing.
Implementing suitable solutions for wax-related problems requires
vast technical knowledge and investigation of the wax disappearance
temperature (WDT) of multicomponent systems in petroleum-dominated
systems. In this study, the WDTs of a quaternary system comprising
different mixtures of
n
-undecane +
n
-tetradecane +
n
-hexadecane +
n
-octadecane were measured using a visual-based diagnosis apparatus
under atmospheric pressure. On the other hand, the WDTs of the studied
systems are predicted by applying a solid solution model without any
adjustable parameter. Two approaches namely γ–φ
and γ–γ are assessed. In the (γ–φ)
approach, perturbed-chain statistical associating fluid theory (PC-SAFT)
is applied for liquid phase modeling, while the solid phase is described
using different activity coefficient models. In the (γ–γ)
approach, nonidealities of both the liquid and solid phases are investigated
using different combinations of activity coefficient models such as
ideal solution, regular solution theory, predictive Wilson, predictive
UNIQUAC, and UNIFAC. Comparison of experimental data and thermodynamic
modeling results indicates that applying the predictive UNIQUAC model
for describing the nonideality of the solid phase and the regular
solution model for the liquid phase is the best combination for the
aforementioned system with the average absolute deviation (AAD) of
0.8 K.