Effect of hydrodynamics on mass transfer in a gas-liquid oscillatory baffled column

Oliveira, Monica and Ni, X. (2004) Effect of hydrodynamics on mass transfer in a gas-liquid oscillatory baffled column. Chemical Engineering Journal, 99 (1). pp. 59-66. ISSN 1385-8947

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    Abstract

    In this paper, we present an experimental study on mass transfer of oxygen into water in an oscillatory baffled column (OBC). The objective of this work is to establish the contribution of individual parameters, such as the size of bubbles and the gas holdup, to the overall volumetric mass transfer coefficient (kLa). Our results show that the gas holdup is the most important factor. The liquid-side mass transfer coefficient (kL) is calculated directly from the experimental measurements of gas holdup, Sauter mean diameter and kLa, and an increase of kL with D32 is observed. The results also show that, above a critical level of fluid oscillation, the mass transfer coefficients are mainly governed by the oscillatory operating conditions, while independent of the type of gas sparger.

    Creators(s): Oliveira, Monica ORCID logoORCID: https://orcid.org/0000-0002-1836-4692 and Ni, X.;
    Item type:Article
    ID code:44235
    Keywords:fluid oscillation, mass transfer, bubble size, gas holdup, special interfacial area, Mechanical engineering and machinery, Chemical engineering
    Subjects:Technology > Mechanical engineering and machinery
    Technology > Chemical engineering
    Department:Faculty of Engineering > Mechanical and Aerospace Engineering
    Technology and Innovation Centre > Advanced Engineering and Manufacturing
    Depositing user: Pure Administrator
    Date deposited:27 Jun 2013 13:33
    Last modified:20 Jan 2021 20:45
    Related URLs:
    URI:https://strathprints.strath.ac.uk/id/eprint/44235
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