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Stability-constrained multi-fluid CFD models for gas-liquid flow in bubble columns
Xiao, Qi1,2; Yang, Ning1; Li, Jinghai1
2013-08-30
Source PublicationCHEMICAL ENGINEERING SCIENCE
ISSN0009-2509
Volume100Issue:0Pages:279-292
AbstractWe have proposed a Dual-Bubble-Size (DBS) model featuring a stability condition describing the compromise of two dominant mechanisms, and then a stability-constrained multi-fluid model (SCMFA) integrating the DBS model into CFD simulation. This work further validates the model and extends to much higher flow rate, and then tentatively proposes a new model termed SCMF-B. It solves the conservative equations for a dense phase composed of small bubbles and liquid and a dilute phase involving large bubbles. The DBS model supplies the structure parameters of the two bubble classes such as the gas volume fraction of small bubbles, the ratio of drag coefficient to bubble diameter for large bubbles and the superficial gas velocity of large bubbles to close the SCMF-B model. A thorough comparison indicates that without any fitting parameters, the SCMF models are superior to the two-fluid model (TFM) with empirical drag correlations in the prediction of overall gas holdup, radial profile of gas holdup and liquid flow field over a wide range of operating gas velocities. By comparison, each SCMF model has its strength and weakness at different flow conditions. SCMF-B can better reproduce the plateau of overall gas holdup as a function of gas flow rate, and the relative error of radial profile of gas holdup is the smallest among all the models at relatively higher flow rate. SCMF-A is better for the lower and much higher gas flow rates. We also design a special and step-by-step strategy to ascertain the evolution from SCMF-A to SCMF-B. We find that the physical properties, flow rate and drag coefficient of different bubble classes have respective functions in the model evolution and only their synergistic effects could generate reasonable prediction. This suggests that the definition of two "fluids" in the SCMF-B in terms of the differences in dense and dilute phases, rather than the thermal physical properties, is reasonable only when all the above "external" and "internal" factors are taken into account. (C) 2013 Elsevier Ltd. All rights reserved.
KeywordCfd Simulation Bubble Columns Meso-scale Multi-scale Multiphase Flow Hydrodynamics
SubtypeArticle
WOS HeadingsScience & Technology ; Technology
DOI10.1016/j.ces.2013.02.027
Indexed BySCI ; ISTP
Language英语
WOS KeywordREGIME TRANSITIONS ; NUMERICAL-SIMULATION ; DRAG COEFFICIENT ; EMMS APPROACH ; SIZE MODEL ; SCALE-UP ; REACTORS ; VELOCITY ; COALESCENCE ; TURBULENCE
WOS Research AreaEngineering
WOS SubjectEngineering, Chemical
WOS IDWOS:000321965700030
Citation statistics
Cited Times:35[WOS]   [WOS Record]     [Related Records in WOS]
Document Type期刊论文
Identifierhttp://ir.ipe.ac.cn/handle/122111/13327
Collection研究所(批量导入)
Affiliation1.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
2.Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Shaanxi, Peoples R China
Recommended Citation
GB/T 7714
Xiao, Qi,Yang, Ning,Li, Jinghai. Stability-constrained multi-fluid CFD models for gas-liquid flow in bubble columns[J]. CHEMICAL ENGINEERING SCIENCE,2013,100(0):279-292.
APA Xiao, Qi,Yang, Ning,&Li, Jinghai.(2013).Stability-constrained multi-fluid CFD models for gas-liquid flow in bubble columns.CHEMICAL ENGINEERING SCIENCE,100(0),279-292.
MLA Xiao, Qi,et al."Stability-constrained multi-fluid CFD models for gas-liquid flow in bubble columns".CHEMICAL ENGINEERING SCIENCE 100.0(2013):279-292.
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