张硕
Associate Professor Supervisor of Master's Candidates
Gender:Male
Alma Mater:德国柏林工业大学
Degree:Doctoral Degree
School/Department:控制科学与工程学院
E-Mail:shuozhang@dlut.edu.cn
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Indexed by:期刊论文
Date of Publication:2017-01-01
Journal:IEEE ACCESS
Included Journals:SCIE、EI、Scopus
Volume:5
Page Number:2711-2719
ISSN No.:2169-3536
Key Words:Internal loop airlift reactor; computational modeling; PBM-CFD; bubble size distribution; experiment validation
Abstract:This paper investigated the problem of overall gas holdup and the oxygen mass transfer in the internal loop airlift reactor by numerical modeling and experimental validation. The population balance model (PBM) was introduced as the general model to characterize the bubble behaviors, i.e., bubble breakage and coalescence. Bubble coalescence, as a result of fluid turbulent eddy, bubble rise difference, and bubble wake entrainment, was considered in the PBM kernels. Meanwhile, bubble breakage, owing to eddy collision and large bubble instability, was included in the PBM kernels. A class method was applied to numerically solve the population balance equations. Based on the lab-scale internal loop airlift reactor, experiments and CFD simulations have been carried on simultaneously. The comparison between them demonstrated that CFD simulation results had good agreement between the experimental data and validated the effectiveness of the PBM model indirectly. Therefore, the PBM-CFD modeling provides an effective method for the problem of scale up. Finally, the flow regime transition of gas holdup difference and small bubble volume fraction are investigated in an internal loop airlift reactor.