Abstract

The original Shan-Chen’s pseudopotential Lattice Boltzmann Model (LBM) has continuously evolved during the past two decades. However, despite its capability to simulate multiphase flows, the model still faces challenges when applied to multicomponent-multiphase flows in complex geometries with a moderately high-density ratio. Furthermore, classical cubic equations of state usually incorporated into the model cannot accurately predict fluid thermodynamics in the near-critical region. This paper addresses these issues by incorporating a crossover Peng–Robinson equation of state into LBM and further improving the model to consider the density and the critical temperature differences between the CO2 and water during the injection of the CO2 in a water-saturated 2D homogeneous porous medium. The numerical model is first validated by analyzing the supercritical CO2 penetration into a single narrow channel initially filled with H2O, depicting the fundamental role of the driving pressure gradient to overcome the capillary resistance in near one and higher density ratios. Significant differences are observed by extending the model to the injection of CO2 into a 2D homogeneous porous medium when using a flat versus a curved inlet velocity profile.

Highlights

  • Carbon Dioxide (CO2 ) and other greenhouse gases are key contributors to climate change

  • We showed that crossover PR Equations of State (EoS) improved the model accuracy for fluids at near/supercritical conditions compared to the classical PR EoS

  • The detailed comparison of the thermodynamic behavior of CO2 and H2 O at various temperatures predicted by PR and crossover PR EoS showed that PR EoS dramatically improves the model accuracy, which is more noticeable in the liquid phase

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Summary

Introduction

Carbon Dioxide (CO2 ) and other greenhouse gases (i.e., methane, nitrous oxide, among others) are key contributors to climate change. According to the Energy Information Administration (EIA) estimates, the global emission of CO2 alone can rise to 6.41 billion tonnes by 2030 [1]. Various mitigation measures have been proposed to tackle global climate change. Among those proposed solutions, we use CO2 in different applications such as Hot-Dry Rock (HDR) systems, heat engines, selective extraction processes, reclamation processes of metals from industrial effluents, and chemical reactions [2,3]. CO2 sequestration is recognized as one of the key strategies for reducing CO2 emission rates. Due to its low critical temperature (31 ◦ C), CO2 is in supercritical (for example, in CO2 sequestration) or in near-critical (as in air conditioning and cooling systems [4,5]) state

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