Interfacial mass transfer of single <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML" altimg="si1.svg" display="inline" id="d1e1721"> <mml:msub> <mml:mrow> <mml:mtext>CO</mml:mtext> </mml:mrow> <mml:mrow> <mml:mn>2</mml:mn> </mml:mrow> </mml:m

Bubble velocity jump discontinuity is a distinctive characteristic of rising bubbles in the presence of viscoelasticity. This study reveals how interfacial mass transfer of single carbon dioxide bubbles stabilizes this discontinuity through two mechanisms. When bubbles experience sufficient exposure to elasticity, they shift smoothly from a high- to low-velocity branch, reproducing the behavior of non-dissolving bubbles with their pointed tip elongating downwards. Otherwise, they preserve the pointed tip and remain in the high-velocity regime even after shrinking to a size smaller than the critical one. These characteristics affect the liquid-side mass transfer coefficient, either enhancing it under the first mechanism or reducing it under the second one. The influence of viscoelasticity, bubble size, and dissolution time is characterized through empirical correlations incorporating the Weissenberg number, which are found accurate in estimating the bubble motion in viscoelastic liquids with dissolution. • CO 2 bubble dissolution in viscoelastic polyacrylamide solutions is investigated. • Two distinct dissolution mechanisms are revealed. • Critical dissolution time relative to relaxation time is identified. • Time-dependent mass transfer coefficient for bubble sizes of 3–5.5 mm is estimated. • Dimensionless correlations including viscoelasticity and dissolution are proposed.

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Publication Details

Journal
International Journal of Multiphase Flow
Published
2026-03-05
DOI
https://doi.org/10.1016/j.ijmultiphaseflow.2026.105679
Primary Topic
Fluid Dynamics and Mixing
Type
article
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article

Interfacial mass transfer of single <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML" altimg="si1.svg" display="inline" id="d1e1721"> <mml:msub> <mml:mrow> <mml:mtext>CO</mml:mtext> </mml:mrow> <mml:mrow> <mml:mn>2</mml:mn> </mml:mrow> </mml:m

Hauna Fathmadinda Hosen, Jannike Solsvik
International Journal of Multiphase Flow
Fluid Dynamics and Mixing
article

Interfacial mass transfer of single <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML" altimg="si1.svg" display="inline" id="d1e1721"> <mml:msub> <mml:mrow> <mml:mtext>CO</mml:mtext> </mml:mrow> <mml:mrow> <mml:mn>2</mml:mn> </mml:mrow> </mml:m

Hauna Fathmadinda Hosen, Jannike Solsvik
article en

Abstract

Bubble velocity jump discontinuity is a distinctive characteristic of rising bubbles in the presence of viscoelasticity. This study reveals how interfacial mass transfer of single carbon dioxide bubbles stabilizes this discontinuity through two mechanisms. When bubbles experience sufficient exposure to elasticity, they shift smoothly from a high- to low-velocity branch, reproducing the behavior of non-dissolving bubbles with their pointed tip elongating downwards. Otherwise, they preserve the pointed tip and remain in the high-velocity regime even after shrinking to a size smaller than the critical one. These characteristics affect the liquid-side mass transfer coefficient, either enhancing it under the first mechanism or reducing it under the second one. The influence of viscoelasticity, bubble size, and dissolution time is characterized through empirical correlations incorporating the Weissenberg number, which are found accurate in estimating the bubble motion in viscoelastic liquids with dissolution. • CO 2 bubble dissolution in viscoelastic polyacrylamide solutions is investigated. • Two distinct dissolution mechanisms are revealed. • Critical dissolution time relative to relaxation time is identified. • Time-dependent mass transfer coefficient for bubble sizes of 3–5.5 mm is estimated. • Dimensionless correlations including viscoelasticity and dissolution are proposed.

International Journal of Multiphase FlowVol. 199
Norwegian University of Science and Technology (NO)
Openalex Percentile: Top 34%
Fluid Dynamics and Mixing
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