Numerical Simulation of Gas-Liquid Flow in a Bubble Column by Intermittent Aeration in Newtonian Liquid/Non-Newtonian Liquid
The dynamic behaviors of gas-liquid two-phase flow were simulated in a lab-scale intermittent bubble column by Euler-Euler two-fluid model coupled with the PBM (population balance model) using two different liquid phases, i.e., Newtonian fluid (water)/non-Newtonian fluid (activated sludge). When non...
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Series: | International Journal of Chemical Engineering |
Online Access: | http://dx.doi.org/10.1155/2018/5254087 |
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doaj-94393e9833bb401d81e6fb2cc178a2e12021-07-02T01:52:09ZengHindawi LimitedInternational Journal of Chemical Engineering1687-806X1687-80782018-01-01201810.1155/2018/52540875254087Numerical Simulation of Gas-Liquid Flow in a Bubble Column by Intermittent Aeration in Newtonian Liquid/Non-Newtonian LiquidZheng Xipeng0Wang Le1Jia Xiaoxuan2Xiang Wenchuan3Yang Shunsheng4Southwest Jiaotong University, School of Civil Engineering, Cheng du, ChinaSouthwest Jiaotong University, School of Civil Engineering, Cheng du, ChinaSouthwest Jiaotong University, School of Civil Engineering, Cheng du, ChinaSouthwest Jiaotong University, School of Civil Engineering, Cheng du, ChinaSouthwest Jiaotong University, School of Civil Engineering, Cheng du, ChinaThe dynamic behaviors of gas-liquid two-phase flow were simulated in a lab-scale intermittent bubble column by Euler-Euler two-fluid model coupled with the PBM (population balance model) using two different liquid phases, i.e., Newtonian fluid (water)/non-Newtonian fluid (activated sludge). When non-Newtonian fluid was used during intermittent aeration, some interesting results were obtained. Two symmetric vortexes existed in the time-averaged flow field; the vertical time-averaged velocity of the liquid phase decreased with increasing anaerobic time; the average gas holdup distribution was like a trapezoid with long upper side and short lower side and affected by the dynamic viscosity of the liquid phase. Compared with non-Newtonian fluid, the use of Newtonian fluid as the liquid phase led to a more complicated time-averaged flow field structure and vertical time-averaged velocity distribution, higher average gas holdup, and the asymmetric column-shaped gas holdup distribution with increasing anaerobic time. For different liquid phases, the instantaneous flow field, instantaneous vertical velocity, and instantaneous gas holdup distribution all periodically changed with anaerobic time; however, different from Newtonian liquid phase, non-Newtonian liquid phase had no periodic oscillating instantaneous horizontal velocity.http://dx.doi.org/10.1155/2018/5254087 |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Zheng Xipeng Wang Le Jia Xiaoxuan Xiang Wenchuan Yang Shunsheng |
spellingShingle |
Zheng Xipeng Wang Le Jia Xiaoxuan Xiang Wenchuan Yang Shunsheng Numerical Simulation of Gas-Liquid Flow in a Bubble Column by Intermittent Aeration in Newtonian Liquid/Non-Newtonian Liquid International Journal of Chemical Engineering |
author_facet |
Zheng Xipeng Wang Le Jia Xiaoxuan Xiang Wenchuan Yang Shunsheng |
author_sort |
Zheng Xipeng |
title |
Numerical Simulation of Gas-Liquid Flow in a Bubble Column by Intermittent Aeration in Newtonian Liquid/Non-Newtonian Liquid |
title_short |
Numerical Simulation of Gas-Liquid Flow in a Bubble Column by Intermittent Aeration in Newtonian Liquid/Non-Newtonian Liquid |
title_full |
Numerical Simulation of Gas-Liquid Flow in a Bubble Column by Intermittent Aeration in Newtonian Liquid/Non-Newtonian Liquid |
title_fullStr |
Numerical Simulation of Gas-Liquid Flow in a Bubble Column by Intermittent Aeration in Newtonian Liquid/Non-Newtonian Liquid |
title_full_unstemmed |
Numerical Simulation of Gas-Liquid Flow in a Bubble Column by Intermittent Aeration in Newtonian Liquid/Non-Newtonian Liquid |
title_sort |
numerical simulation of gas-liquid flow in a bubble column by intermittent aeration in newtonian liquid/non-newtonian liquid |
publisher |
Hindawi Limited |
series |
International Journal of Chemical Engineering |
issn |
1687-806X 1687-8078 |
publishDate |
2018-01-01 |
description |
The dynamic behaviors of gas-liquid two-phase flow were simulated in a lab-scale intermittent bubble column by Euler-Euler two-fluid model coupled with the PBM (population balance model) using two different liquid phases, i.e., Newtonian fluid (water)/non-Newtonian fluid (activated sludge). When non-Newtonian fluid was used during intermittent aeration, some interesting results were obtained. Two symmetric vortexes existed in the time-averaged flow field; the vertical time-averaged velocity of the liquid phase decreased with increasing anaerobic time; the average gas holdup distribution was like a trapezoid with long upper side and short lower side and affected by the dynamic viscosity of the liquid phase. Compared with non-Newtonian fluid, the use of Newtonian fluid as the liquid phase led to a more complicated time-averaged flow field structure and vertical time-averaged velocity distribution, higher average gas holdup, and the asymmetric column-shaped gas holdup distribution with increasing anaerobic time. For different liquid phases, the instantaneous flow field, instantaneous vertical velocity, and instantaneous gas holdup distribution all periodically changed with anaerobic time; however, different from Newtonian liquid phase, non-Newtonian liquid phase had no periodic oscillating instantaneous horizontal velocity. |
url |
http://dx.doi.org/10.1155/2018/5254087 |
work_keys_str_mv |
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