Experimental investigation of supersaturation decay induced by bubble evolution in a pipe flow

• Experiments quantify O 2 supersaturation decay in 20 mm horizontal pipe flow. • Patented in-situ sampler yields desorption rate with ±0.06 uncertainty. • Desorption rate rises with pipe length but is insensitive to Reynolds number. • Even after 8.4 m only ∼50 % of initial supersaturation is removed. • Kress–Keyes mass-transfer correlation matches data; Lamont–Scott and Avdeev do not. Bubble formation caused by oxygen supersaturation can influence gas–liquid separation and heat exchange in polymer-electrolyte-membrane (PEM) electrolyser loops, yet the rate at which the dissolved-oxygen level relaxes toward equilibrium in turbulent pipe flow is poorly quantified. This study measures that relaxation in a dedicated test facility. Oxygen-saturated water (170 mg/l, 3.86 bar, 18 °C) was depressurised to 1 bar, generating a saturation ratio of 3.86. The liquid then flowed through three PVC pipes of different lengths (inner diameter = 20 mm) at seven volumetric flow rates corresponding to Reynolds numbers between 6 500 and 27 000. Outlet concentrations were obtained with a self-developed in-situ sampling technique whose combined uncertainty, propagated from the primary measurements, is ±0.06 in the dimensionless degree of desorption Θ des , excluding potential systematic bias from the sampling process. Θ des rose with contact length—0.32 (short), 0.40 (medium) and 0.48 (long)—but was independent of flow velocity, showing that the residence-time reduction at higher velocities is offset by a proportional increase in the mass-transfer coefficient. Even after the long configuration (up to 35 s residence) roughly half of the initial supersaturation remained, confirming strong kinetic limitations. A previously published axial cell model reproduced the data when the turbulent mass-transfer coefficient was calculated with the Kress–Keyes correlation; alternative correlations (Lamont–Scott, Avdeev) over-predicted desorption. The results provide benchmark data for oxygen release in a turbulent water flow at moderate supersaturation.

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Publication Details

Journal
Chemical Engineering Science
Published
2026-01-28
DOI
https://doi.org/10.1016/j.ces.2026.123435
Primary Topic
Polymer Science and PVC
Type
article
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article

Experimental investigation of supersaturation decay induced by bubble evolution in a pipe flow

Montadhar Guesmi, Simon Unz, M. Beckmann, J. Manthey et al.
Chemical Engineering Science
Polymer Science and PVC
article

Experimental investigation of supersaturation decay induced by bubble evolution in a pipe flow

Montadhar Guesmi, Simon Unz, M. Beckmann, J. Manthey, H. Mehdipour
article en

Abstract

• Experiments quantify O 2 supersaturation decay in 20 mm horizontal pipe flow. • Patented in-situ sampler yields desorption rate with ±0.06 uncertainty. • Desorption rate rises with pipe length but is insensitive to Reynolds number. • Even after 8.4 m only ∼50 % of initial supersaturation is removed. • Kress–Keyes mass-transfer correlation matches data; Lamont–Scott and Avdeev do not. Bubble formation caused by oxygen supersaturation can influence gas–liquid separation and heat exchange in polymer-electrolyte-membrane (PEM) electrolyser loops, yet the rate at which the dissolved-oxygen level relaxes toward equilibrium in turbulent pipe flow is poorly quantified. This study measures that relaxation in a dedicated test facility. Oxygen-saturated water (170 mg/l, 3.86 bar, 18 °C) was depressurised to 1 bar, generating a saturation ratio of 3.86. The liquid then flowed through three PVC pipes of different lengths (inner diameter = 20 mm) at seven volumetric flow rates corresponding to Reynolds numbers between 6 500 and 27 000. Outlet concentrations were obtained with a self-developed in-situ sampling technique whose combined uncertainty, propagated from the primary measurements, is ±0.06 in the dimensionless degree of desorption Θ des , excluding potential systematic bias from the sampling process. Θ des rose with contact length—0.32 (short), 0.40 (medium) and 0.48 (long)—but was independent of flow velocity, showing that the residence-time reduction at higher velocities is offset by a proportional increase in the mass-transfer coefficient. Even after the long configuration (up to 35 s residence) roughly half of the initial supersaturation remained, confirming strong kinetic limitations. A previously published axial cell model reproduced the data when the turbulent mass-transfer coefficient was calculated with the Kress–Keyes correlation; alternative correlations (Lamont–Scott, Avdeev) over-predicted desorption. The results provide benchmark data for oxygen release in a turbulent water flow at moderate supersaturation.

Chemical Engineering ScienceVol. 325
Technische Universität Dresden (DE)
Clean water and sanitation
Openalex Percentile: Top 75%
Polymer Science and PVC
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