Numerical simulation on the terminal rise velocity and mass transfer rate of single sub-millimeter bubbles. (31st December 2021)
- Record Type:
- Journal Article
- Title:
- Numerical simulation on the terminal rise velocity and mass transfer rate of single sub-millimeter bubbles. (31st December 2021)
- Main Title:
- Numerical simulation on the terminal rise velocity and mass transfer rate of single sub-millimeter bubbles
- Authors:
- Li, Chengxiang
Cui, Yizhou
Shi, Xiaogang
Gao, Jinsen
Lan, Xingying - Abstract:
- Graphical abstract: Highlights: The terminal rise velocity and the liquid-side mass transfer coefficient of single sub-millimeter bubbles are obtained through numerical simulation. Accuracy of the simulation is verified by comparison with literature equations and experimental data. The literature equations are valid in a limited range and cannot predict the behavior of sub-millimeter bubbles over the whole size range. New equations are proposed for calculating the terminal rise velocity and the liquid-side mass transfer coefficient of sub-millimeter bubbles. The reason why the liquid-side mass transfer coefficient of small fully contaminated bubbles keeps roughly constant is discussed. Abstract: Gas–liquid reactors containing bubbles are intensively used in the chemical industry. However, the gas–liquid mass transfer is usually the rate-limiting step. One possible way to intensify the mass transfer is the application of sub-millimeter bubbles (1–1000 μm) which efficiently increase interfacial area. Literature usually focused on bubbles larger than 1000 μm, and it still needs to be studied whether the frequently-used literature equations for terminal rise velocity and mass transfer can accurately predict the behavior of sub-millimeter bubbles. Therefore, the terminal rise velocity and mass transfer rate of single sub-millimeter bubbles were obtained by numerical simulation. It was found that the literature equations could not accurately predict the behavior of sub-millimeterGraphical abstract: Highlights: The terminal rise velocity and the liquid-side mass transfer coefficient of single sub-millimeter bubbles are obtained through numerical simulation. Accuracy of the simulation is verified by comparison with literature equations and experimental data. The literature equations are valid in a limited range and cannot predict the behavior of sub-millimeter bubbles over the whole size range. New equations are proposed for calculating the terminal rise velocity and the liquid-side mass transfer coefficient of sub-millimeter bubbles. The reason why the liquid-side mass transfer coefficient of small fully contaminated bubbles keeps roughly constant is discussed. Abstract: Gas–liquid reactors containing bubbles are intensively used in the chemical industry. However, the gas–liquid mass transfer is usually the rate-limiting step. One possible way to intensify the mass transfer is the application of sub-millimeter bubbles (1–1000 μm) which efficiently increase interfacial area. Literature usually focused on bubbles larger than 1000 μm, and it still needs to be studied whether the frequently-used literature equations for terminal rise velocity and mass transfer can accurately predict the behavior of sub-millimeter bubbles. Therefore, the terminal rise velocity and mass transfer rate of single sub-millimeter bubbles were obtained by numerical simulation. It was found that the literature equations could not accurately predict the behavior of sub-millimeter bubbles over the whole size range. New equations were proposed to improve calculation accuracy, with which the terminal rise velocity and mass transfer rate of sub-millimeter bubbles can be accurately predicted. … (more)
- Is Part Of:
- Chemical engineering science. Volume 246(2021)
- Journal:
- Chemical engineering science
- Issue:
- Volume 246(2021)
- Issue Display:
- Volume 246, Issue 2021 (2021)
- Year:
- 2021
- Volume:
- 246
- Issue:
- 2021
- Issue Sort Value:
- 2021-0246-2021-0000
- Page Start:
- Page End:
- Publication Date:
- 2021-12-31
- Subjects:
- Sub-millimeter bubbles -- Mass transfer -- Bubble terminal rise velocity -- Computational fluid dynamics
Chemical engineering -- Periodicals
Génie chimique -- Périodiques
Chemical engineering
Periodicals
Electronic journals
660 - Journal URLs:
- http://www.sciencedirect.com/science/journal/00092509 ↗
http://www.elsevier.com/journals ↗ - DOI:
- 10.1016/j.ces.2021.116963 ↗
- Languages:
- English
- ISSNs:
- 0009-2509
- Deposit Type:
- Legaldeposit
- View Content:
- Available online (eLD content is only available in our Reading Rooms) ↗
- Physical Locations:
- British Library DSC - 3146.000000
British Library DSC - BLDSS-3PM
British Library HMNTS - ELD Digital store - Ingest File:
- 18900.xml