Horizontal producers deliverability in SAGD and solvent aided-SAGD processes: pure and partial solvent injection

M Irani, N Sabet, F Bashtani - Fuel, 2021 - Elsevier
The subcool or thermodynamic trapping for solvent applications is inefficient since solvent
viscosity is only a weak function of temperature. Another factor that affects the efficiency of …

Three-Phase equilibrium computations for hydrocarbon–water mixtures using a reduced variables method

M Connolly, H Pan, H Tchelepi - Industrial & Engineering …, 2019 - ACS Publications
Thermal compositional simulation requires phase-equilibrium calculations for at least three
fluid phases. The use of precomputed equilibrium ratios (K-values) has long been justified …

Comparison of EoS-Based and K-Values-Based Methods for Three-Phase Thermal Simulation

R Zaydullin, DV Voskov, HA Tchelepi - Transport in Porous Media, 2017 - Springer
This paper presents a detailed numerical analysis of two methods for phase-behavior
computations associated with thermal compositional reservoir simulation. Specifically, we …

Reduced method for rapid multiphase isenthalpic flash in thermal simulation

M Connolly, H Pan, M Imai, HA Tchelepi - Chemical Engineering Science, 2021 - Elsevier
Thermal enhanced oil recovery (EOR) involves the complex interplay of mass and energy
transport processes with phase behavior. Hydrocarbon and water components partition …

[HTML][HTML] Full-EoS based thermal multiphase compositional simulation of CO2 and steam injection processes

M Petitfrere, DV Nichita, D Voskov, R Zaydullin… - Journal of Petroleum …, 2020 - Elsevier
Several compositional reservoir simulators based on equations of state (EoS) have been
designed. Yet, few of them can deal with thermal processes such as steam injection and no …

An isenthalpic-based compositional framework for nonlinear thermal simulation

M Connolly - 2018 - search.proquest.com
Thermal enhanced oil recovery (EOR) involves the complex interplay of mass and energy
transport with phase behavior. Hydrocarbon and water components partition across multiple …

Three-phase equilibrium calculations of water/hydrocarbon/nonhydrocarbon systems based on the equation of state (EOS) in thermal processes

X Ma, S Wu, G Huang, T Fan - ACS omega, 2021 - ACS Publications
A simple and novel approach is proposed to represent the mutual solubility of water and
hydrocarbon components based on equations of state at high temperatures in thermal …

Phase-state identification bypass method for three-phase thermal compositional simulation

R Zaydullin, DV Voskov, HA Tchelepi - Computational Geosciences, 2016 - Springer
In this paper, we propose a strategy to bypass the phase identification of fluid mixtures that
can form three, or more, phases. The strategy is used for reservoir simulation of …

Complete equation of state thermal formulation for simulation of CO2 storage

A Moncorgé, M Petitfrère, S Thibeau - SPE Journal, 2022 - onepetro.org
Storage of carbon dioxide (CO 2) in depleted gas reservoirs or large aquifers is one of the
available solutions to reduce anthropogenic greenhouse gas emissions. Numerical …

Comprehensive Enthalpy-Based Phase Behavior for EOS-Based Compositional Thermal Simulation

HE Barrios-Molano, K Sepehrnoori - SPE Improved Oil Recovery …, 2024 - onepetro.org
This work presents the selection of the most adequate isenthalpic flash method for EOS-
based compositional thermal simulation. Five multi-component isenthalpic flash methods …