Abstract
Thermodynamic modeling of hydrate equilibrium conditions for sour gas mixture (CH4/C3H8/H2S) in the presence of pure water and thermodynamic inhibitor(s) (MEG, NaCl, and CaCl2) was investigated in this study. Hydrate and vapor phases were evaluated using the van der Waals and Plattueew model, and the Peng-Robinson EoS along with the classic van der Waals mixing rule, respectively. As a different approach, by combining non-synonymous salt ions and forming ion pairs, they can be considered as molecular species. So ion pair concept was used to investigate liquid phase and calculate water activity coefficient in this phase. For short-range and long-range forces, the NRTL molecular model and the Pitzer-Debye-Hückel equation was used, respectively. The results of experimental data in the previous work were compared with the results of the proposed model and PVTsim Nova 3.0 software, and it was discovered that they have an acceptable agreement together. The average deviation in pressure (AARDP %) related to the model is 0.36% to 4.34% and 3.41% to 5.68% related to the software.
HIGHLIGHTS
Thermodynamic modeling of sour gas mixture (CH4/C3H8/H2S) hydrate formation in the presence of thermodynamic inhibitors MEG, NaCl, and CaCl2
Evaluating hydrate and vapor phases using the van der Waals and Plattueew model, and the Peng-Robinson EoS along with the classic van der Waals mixing rule, respectively
Appling ion pair concept to calculate water activity coefficient in the non-ideality state of this phase
Using the NRTL non-electrolytic molecular model for short-range forces, and the Pitzer-Debye-Hückel equation for long-range forces
Agreement among the results of proposed model with the experimental data in the previous work and PVTsim Nova 3.0 software
Disclosure statement
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.