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Updated: Apr 20, 2026

A Modeling and Simulation Method for Preliminary Design of an Electro-Variable Displacement Pump
Published on: June 1, 2022
Measurement and PC-SAFT modelling of three-phase behaviour
Iago Rodríguez-Palmeiro1, Oscar Rodríguez, Ana Soto
1Department of Chemical Engineering, University of Santiago de Compostela, E-15782, Santiago de Compostela, Spain. ana.soto@usc.es.
This study successfully modeled three-liquid-phase systems using the PC-SAFT equation of state, crucial for enhanced oil recovery surfactant formulation. The model accurately predicted phase behavior without fitting parameters, aiding surfactant screening.
Area of Science:
- Thermodynamics
- Chemical Engineering
- Physical Chemistry
Background:
- Multi-component systems with complex interactions present modeling challenges in thermodynamics.
- Three-liquid-phase systems are vital for applications like separation processes, catalysis, and enhanced oil recovery (EOR).
- Optimal surfactant flooding for EOR relies on formulations exhibiting three-phase behavior to achieve low interfacial tension.
Purpose of the Study:
- To apply the Perturbed Chain Statistical Association Fluid Theory (PC-SAFT) equation of state for predicting equilibrium in triphasic systems.
- To evaluate the PC-SAFT model's predictive capability using only pure-component parameters for ternary systems relevant to EOR.
- To assess the model's accuracy against experimental data for specific water-surfactant-oil systems.
Main Methods:
- Utilized the PC-SAFT equation of state for thermodynamic modeling.
- Focused on predicting phase equilibrium in ternary systems: (water + [C10mim][NTf2] + n-dodecane) and (water + [C12mim][NTf2] + n-dodecane).
- Employed solely pure-component parameters for initial model predictions, with optional binary interaction parameters for refinement.
Main Results:
- The PC-SAFT model accurately predicted the three-phase behavior of the studied ternary systems without requiring any fitting parameters.
- Excellent agreement was observed between experimental and predicted compositions for the systems at 298.15 K and atmospheric pressure.
- Slightly higher deviations at 348.15 K were noted, which could be mitigated by introducing a single binary interaction parameter.
Conclusions:
- The PC-SAFT equation of state is a powerful tool for predicting triphasic behavior in systems relevant to enhanced oil recovery.
- The model's ability to predict phase equilibrium using only pure-component parameters offers a significant advancement for upstream oil operations.
- This approach enables faster and more cost-effective initial screening of potential surfactants for EOR applications.
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