TUHH Open Research
Help
New user? Click here to register.Have you forgotten your password?
Communities & Collections
Publications
Research Data
People
Institutions
Projects
  1. Home
  2. Publications
  3. Publications
  4. An experimental study on the time dependence of diffusive mass transfer of single oxygen bubbles

An experimental study on the time dependence of diffusive mass transfer of single oxygen bubbles

Citation Link: https://doi.org/10.15480/882.17780
Publikationstyp
Journal Article
Date Issued
2026-12-15
Sprache
English
Author(s)
Kursula, Lotta
Mehrphasenströmungen V-5
Takagi, Sayaka
Mehrphasenströmungen V-5
Hoffmann, Marko
Mehrphasenströmungen V-5
Kexel, Felix
Mehrphasenströmungen V-5
Schlüter, Michael
Mehrphasenströmungen V-5
TORE-DOI
10.15480/882.17780
TORE-URI
https://hdl.handle.net/11420/64214
Journal
International journal of heat and mass transfer
Volume
271
Article Number
129352
Citation
International Journal of Heat and Mass Transfer 271: 129352 (2026)
Publisher DOI
10.1016/j.ijheatmasstransfer.2026.129352
Scopus ID
2-s2.0-105045966237
Publisher
Elsevier
Is Supplemented By
10.15480/882.17032
In the vast majority of gas–liquid engineering applications, the liquid phase contains a range of dissolved gaseous species. These dissolved process gases transfer from the liquid phase to the gaseous phase countercurrent to the typically desired mass transfer of gas to liquid. In process design, the resulting change in the composition of the gaseous phase is usually neglected, although a temporal change in the composition of the gaseous phase can directly influence the mass transfer performance over time. The current fundamental study quantifies the mass transfer performance of oxygen bubbles to liquid phases saturated with another gas. For this purpose, the oxygen mass transfer from a bubble to degassed, helium-, nitrogen-, argon- and carbon dioxide-saturated water is studied. Light Sheet Fluorescence Microscopy is used as imaging system for Planar Laser-induced Fluorescence measurements of dissolved oxygen concentration fields, delivering local instantaneous Sherwood numbers, diffusion coefficients and mass transfer coefficients. For the first time, the study showcases that the mass transfer performance from a gaseous dispersed to a liquid continuous phase is independent of time if mass transfer occurs in one direction only. If mass transfer occurs in both directions, the mass transfer performance of the dispersed phase is significantly lower and its time dependence higher to liquids containing gaseous species with high solubilities, such as carbon dioxide in water. Furthermore, the results suggest that applying intrinsic values, such as diffusion or mass transfer coefficients, obtained for binary systems in multicomponent systems can lead to high uncertainty.
Subjects
Gas–liquid mass transfer
LSFM
PLIF
Sherwood number
DDC Class
660: Chemistry; Chemical Engineering
Funding(s)
Feinblasen für biokatalytische Prozesse: Mikroskalige Phänomene und neuartige Anwendungen
Projekt DEAL
Lizenz
https://creativecommons.org/licenses/by/4.0/
Publication version
publishedVersion
Loading...
Thumbnail Image
Download
Name

1-s2.0-S0017931026010288-main.pdf

Type

Main Article

Size

2.09 MB

Format

Adobe PDF

TUHH
Weiterführende Links
  • Contact
  • Send Feedback
  • Cookie settings
  • Privacy policy
  • Impress
DSpace Software

Built with DSpace-CRIS software - Extension maintained and optimized by 4Science
Design by effective webwork GmbH

  • Deutsche NationalbibliothekDeutsche Nationalbibliothek
  • ORCiD Member OrganizationORCiD Member Organization
  • DataCiteDataCite
  • Re3DataRe3Data
  • OpenDOAROpenDOAR
  • OpenAireOpenAire
  • BASE Bielefeld Academic Search EngineBASE Bielefeld Academic Search Engine
Feedback