Dynamics of particle-scale liquid distribution in Pseudo-2D packed beds: Measurements and volume-of-fluid simulations

• Particle-resolved VOF simulations of gas–liquid flow through pseudo-2D packed beds. • Experimental validation of dynamic local liquid distribution and interface length. • Impact of gas/liquid flow rate and void size on force dynamics and liquid spreading. • 3D regime map showing the correlation between governing forces and liquid spreading. • Role of prewetting conditions on the dynamics of local liquid distribution. In this work, three-dimensional (3D) particle-resolved Volume-of-Fluid simulations of liquid spreading in pseudo-two-dimensional (pseudo-2D) beds as a function of liquid flow rate (Q L ), gas/liquid flow rate ratio (Q G /Q L ), and void-size (d v ) are performed. The predictions are validated with the corresponding measurements performed using high-speed imaging in terms of liquid-holdup, interface length, and time-evolution of the gas–liquid interface. The relationship between the dynamics of liquid spreading and the governing forces is investigated using AB I , Weber ( We I ), and modified-Froude (Fr m ). Our analysis reveals that the liquid spreading through the pseudo-2D domain is predominantly governed by the gravitational force [ AB I < 1]. As Q L increases, the relative magnitude of the inertial force becomes comparable to the gravitational force at the beginning of liquid injection [ AB I ∼ 1; We I > 1], enhancing lateral liquid spreading. An increase in Q G /Q L led to an increase in the gas-phase inertial force, which resists lateral liquid spreading. Moreover, the decrease in d v results in an increase in the relative contribution of inertial and capillary force at the beginning and final stages, respectively, leading to an increase in the lateral liquid spreading. A regime map relating the extent of lateral liquid spreading and governing forces is also proposed with the aid of AB I , We I , and Fr m . Finally, the laterally oriented liquid bridges in the prewetted beds are found to facilitate liquid spreading in the lateral direction, leading to enhanced lateral liquid spreading in prewetted beds compared to dry beds.

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-03-09
DOI
https://doi.org/10.1016/j.cej.2025.161417
Citations
1
Primary Topic
Heat and Mass Transfer in Porous Media
Type
article
Field-Weighted Citation Impact
1.33
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article

Dynamics of particle-scale liquid distribution in Pseudo-2D packed beds: Measurements and volume-of-fluid simulations

Rohit S. Gulia, Vivek V. Buwa, Aniket S. Ambekar
1 citations
Chemical Engineering Journal
Heat and Mass Transfer in Porous Media
1.33
article

Dynamics of particle-scale liquid distribution in Pseudo-2D packed beds: Measurements and volume-of-fluid simulations

Rohit S. Gulia, Vivek V. Buwa, Aniket S. Ambekar
article en
1 citations

Abstract

• Particle-resolved VOF simulations of gas–liquid flow through pseudo-2D packed beds. • Experimental validation of dynamic local liquid distribution and interface length. • Impact of gas/liquid flow rate and void size on force dynamics and liquid spreading. • 3D regime map showing the correlation between governing forces and liquid spreading. • Role of prewetting conditions on the dynamics of local liquid distribution. In this work, three-dimensional (3D) particle-resolved Volume-of-Fluid simulations of liquid spreading in pseudo-two-dimensional (pseudo-2D) beds as a function of liquid flow rate (Q L ), gas/liquid flow rate ratio (Q G /Q L ), and void-size (d v ) are performed. The predictions are validated with the corresponding measurements performed using high-speed imaging in terms of liquid-holdup, interface length, and time-evolution of the gas–liquid interface. The relationship between the dynamics of liquid spreading and the governing forces is investigated using AB I , Weber ( We I ), and modified-Froude (Fr m ). Our analysis reveals that the liquid spreading through the pseudo-2D domain is predominantly governed by the gravitational force [ AB I < 1]. As Q L increases, the relative magnitude of the inertial force becomes comparable to the gravitational force at the beginning of liquid injection [ AB I ∼ 1; We I > 1], enhancing lateral liquid spreading. An increase in Q G /Q L led to an increase in the gas-phase inertial force, which resists lateral liquid spreading. Moreover, the decrease in d v results in an increase in the relative contribution of inertial and capillary force at the beginning and final stages, respectively, leading to an increase in the lateral liquid spreading. A regime map relating the extent of lateral liquid spreading and governing forces is also proposed with the aid of AB I , We I , and Fr m . Finally, the laterally oriented liquid bridges in the prewetted beds are found to facilitate liquid spreading in the lateral direction, leading to enhanced lateral liquid spreading in prewetted beds compared to dry beds.

Chemical Engineering JournalVol. 509
Indian Institute of Technology Delhi (IN)
Openalex Percentile: Top 26%
Heat and Mass Transfer in Porous Media
1.33
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