Hydrodynamics and gas-liquid mass transfer in an oscillatory flow reactor: Influence of liquid properties

被引:2
作者
Almeida, F. [1 ,2 ]
Rocha, F. [1 ,2 ]
Teixeira, J. A. [3 ,4 ]
Ferreira, A. [1 ,2 ,5 ]
机构
[1] Univ Porto, Fac Engn, Lab Proc Engn, LEPABE, Rua Dr, P-4200465 Porto, Portugal
[2] Univ Porto, Fac Engn, ALiCE Associate Lab Chem Engn, Rua Dr Roberto Frias, Rua Dr, P-4200465 Porto, Portugal
[3] Univ Minho, Ctr Biol Engn, CEB, P-4710057 Braga, Portugal
[4] Univ Minho, Fac Engn, Associate Lab Biotechnol Bioengn & Microelectromec, LABBELS, Rua Univ, P-4710057 Braga, Portugal
[5] Univ Porto, Fac Engn, Lab Proc Engn Environm Biotechnol & Energy,, LEPABE, Rua Dr, P-4200465 Porto, Portugal
关键词
Oscillatory flow reactor; Gas-liquid mass transfer; Gas holdup; Sauter mean diameter; Design of experiments (DoE); Multiphase reactors; LOOP AIRLIFT REACTOR; BUBBLE-COLUMN; HOLD-UP; ALCOHOL ADDITION; PHYSICAL-PROPERTIES; OXYGEN-TRANSFER; IMAGE-ANALYSIS; CIRCULATION; BEHAVIOR; SIZE;
D O I
10.1016/j.cherd.2023.03.030
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Liquid properties, such as, surface tension and viscosity are important parameters as they control gas-liquid mass transfer in bioprocesses. An oscillatory flow reactor provided with smooth periodic constrictions (OFR-SPC) was considered to evaluate its potential for mass transfer performance in non-pure gas-liquid systems. The effect of surface tension and viscosity on the volumetric (k(L)a) and liquid-side mass transfer coefficients (k(L)), interfacial area, (a), gas holdup (epsilon(G)) and bubbles' dynamics were investigated under different operational conditions (oscillation amplitude (x(0)) and frequency (f) and superficial gas velocity (u(g))). Two liquid phases, ethanol and sucrose aqueous solutions covering a range of surface tension and viscosity values were used. For the bubble size distribution (BSD) measurements an image analysis technique was used. A Design of Experiment (DoE) methodology was implemented in this work to establish the relation of x(0), f, u(g), surface tension and viscosity with k(L)a. According to the results, changes in the liquid properties and operational conditions showed marked effects on bubble's size and mass transfer. However, surface tension and viscosity had no significant influence on epsilon(G), contrary to the reported for common contactors, where epsilon(G) increased in the presence of ethanol and decreased at moderate/high viscosities. Moreover, it was found that increasing the oscillatory movement notably improved k(L), and k(L)a (2-6-fold), either in ethanol or sucrose solutions, compared to common reactors, even with moderate power consumption (similar to 105 W m(-3)). This improvement resulted from the bubbles' breakage, which originates bubbles with small and approximately the same size (homogeneous regime) enhancing a, instead, lower oscillations resulted in large bubbles (heterogeneous regime). The results demonstrate that the OFR-SPC can ensure outstanding mass transfer rates, with potential and feasibility for use in gas-liquid bioprocesses, where mass transfer and liquid properties are important. (c) 2023 The Authors. Published by Elsevier Ltd on behalf of Institution of Chemical Engineers. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).
引用
收藏
页码:179 / 197
页数:19
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