Three-Phase Equilibrium of Hydrocarbon Mixtures in Nanopores: A Volume-Temperature Flash Calculation Approach

Abstract The thermodynamic properties and phase behaviors of nanoconfined fluids are crucial for accurately simulating fluid transport in shale nanopores. However, the commonly used cubic equations of state (EOS) with critical parameter shifts fail to account for fluid/pore wall interactions, leading to inaccuracies in predicting fluid properties within nanopores. More precise ab initio methodologies like density functional theory and molecular simulation demand extensive computational resources, limiting their practical application in large-scale reservoir simulations. Therefore, we aim to develop an efficient and accurate method based on a modified EOS to calculate the phase behaviors of fluids confined in nanopores. A fast and robust VT-flash calculation algorithm is proposed to determine the three-phase behavior of fluids in nanopores using a modified EOS that accounts for both confinement effects and fluid-wall interactions. The algorithm is based on directly minimizing the tangent plane distance or Helmholtz free energy using the Trust-Region modified Newton iteration method. The developed model is validated by comparing adsorption experimental results in nanopores and the fluid phase behavior of the bulk fluid. Then the model is used to analyze the phase behavior of pure fluids and fluid mixtures in nanopores. For pure component systems, fluid–solid interactions result in a sorbed phase with higher density than the bulk fluid, leading to increased spreading pressure. Both confinement effects and fluid–wall interactions significantly influence phase behavior: their combined action causes the two-phase envelope to shrink as pore size decreases. Confinement effects increase fluid covolume, while fluid–wall interactions weaken intermolecular attractions, lowering the critical temperature in smaller pores. Additionally, critical density increases in moderately sized pores due to the formation of dense sorbed layers, but decreases in smaller pores where confinement dominates through covolume expansion. The proposed algorithm provides an efficient and physically grounded framework for modeling multiphase behavior in nanopores and can be extended to simulate CO2-enhanced oil recovery and storage in shale reservoirs.

Authors

Institutions

Publication Details

Journal
SPE Annual Technical Conference and Exhibition
Published
2025-10-13
DOI
https://doi.org/10.2118/228085-ms
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
Field-Weighted Citation Impact
0.00
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Three-Phase Equilibrium of Hydrocarbon Mixtures in Nanopores: A Volume-Temperature Flash Calculation Approach

Ming Ma, Hamid Emami‐Meybodi
SPE Annual Technical Conference and Exhibition
Phase Equilibria and Thermodynamics
article

Three-Phase Equilibrium of Hydrocarbon Mixtures in Nanopores: A Volume-Temperature Flash Calculation Approach

Ming Ma, Hamid Emami‐Meybodi
article en

Abstract

Abstract The thermodynamic properties and phase behaviors of nanoconfined fluids are crucial for accurately simulating fluid transport in shale nanopores. However, the commonly used cubic equations of state (EOS) with critical parameter shifts fail to account for fluid/pore wall interactions, leading to inaccuracies in predicting fluid properties within nanopores. More precise ab initio methodologies like density functional theory and molecular simulation demand extensive computational resources, limiting their practical application in large-scale reservoir simulations. Therefore, we aim to develop an efficient and accurate method based on a modified EOS to calculate the phase behaviors of fluids confined in nanopores. A fast and robust VT-flash calculation algorithm is proposed to determine the three-phase behavior of fluids in nanopores using a modified EOS that accounts for both confinement effects and fluid-wall interactions. The algorithm is based on directly minimizing the tangent plane distance or Helmholtz free energy using the Trust-Region modified Newton iteration method. The developed model is validated by comparing adsorption experimental results in nanopores and the fluid phase behavior of the bulk fluid. Then the model is used to analyze the phase behavior of pure fluids and fluid mixtures in nanopores. For pure component systems, fluid–solid interactions result in a sorbed phase with higher density than the bulk fluid, leading to increased spreading pressure. Both confinement effects and fluid–wall interactions significantly influence phase behavior: their combined action causes the two-phase envelope to shrink as pore size decreases. Confinement effects increase fluid covolume, while fluid–wall interactions weaken intermolecular attractions, lowering the critical temperature in smaller pores. Additionally, critical density increases in moderately sized pores due to the formation of dense sorbed layers, but decreases in smaller pores where confinement dominates through covolume expansion. The proposed algorithm provides an efficient and physically grounded framework for modeling multiphase behavior in nanopores and can be extended to simulate CO2-enhanced oil recovery and storage in shale reservoirs.

SPE Annual Technical Conference and Exhibition
Pennsylvania State University (US)
Openalex Percentile: Top 43%
Phase Equilibria and Thermodynamics
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.