CFD simulation of gas-liquid flow in a high-pressure bubble column with a modified population balance model
General reactor|Updated:2026-01-06
|
CFD simulation of gas-liquid flow in a high-pressure bubble column with a modified population balance model
Chinese Journal of Chemical EngineeringIssue 6, Pages: 1350-1358(2018)
Affiliations:
Beijing Key Laboratory of Fuels Cleaning and Advanced Catalytic Emission Reduction Technology, Beijing Institute of Petrochemical Technology,Beijing,China,102617
Author bio:
Funds:
DOI:
CLC:
Published:2018
Accepted:
Scan QR Code
Bo Zhang, Lingtong Kong, Haibo Jin, et al. CFD simulation of gas-liquid flow in a high-pressure bubble column with a modified population balance model[J]. Chinese Journal of Chemical Engineering, 2018, (6): 1350-1358.
DOI:
Bo Zhang, Lingtong Kong, Haibo Jin, et al. CFD simulation of gas-liquid flow in a high-pressure bubble column with a modified population balance model[J]. Chinese Journal of Chemical Engineering, 2018, (6): 1350-1358.DOI:
CFD simulation of gas-liquid flow in a high-pressure bubble column with a modified population balance model
for pressures according to the literature experimental results was introduced in the bubble coalescence efficiency term. Then
a coupled modified population balance model (PBM) with computational fluid dynamics (CFD) was used to simulate a high-pressure bubble column. The simulation results with and without C
e
were compared with the experimental data. The modified CFD-PBM coupled model was used to investigate its applicability to broader experimental conditions. These results showed that the modified CFD-PBM coupled model can predict the hydrodynamic behaviors under various operating conditions.
关键词
Keywords
references
The trial reading is over, you can activate your VIP account to continue reading.
Simulation of drop breakage in liquid-liquid system by coupling of CFD and PBM: Comparison of breakage kernels and effects of agitator configurations
CFD-PBM simulation of liquid-liquid dispersions in an industrial pulsed disc and doughnut column with directly measured breakup and coalescence kernels
Multiscale synergistic enhancement mechanism of solid—liquid mixing in multi-shaft stirred reactors under variable-speed operation
Experimental and modeling study of micromixing characteristics in a stirred tank integrated with annular jet flow
CFD investigation in the temperature effect on coal catalytic hydrogasification in the pressurized bubbling fluidized bed
Related Author
Rui Xie
Jun Li
Yang Jin
Da Zou
Ming Chen
Yang Zhongshu
Zhou Han
Cai Yubin
Related Institution
Department of Chemical Engineering, Sichuan University
Institute of Nuclear and New Energy Technology, Tsinghua University
State Key Laboratory of Heavy Oil Processing, China University of Petroleum (Beijing)
School of Chemistry and Chemical Engineering, Chongqing University
Department of Industrial Chemistry “Toso Montanari”, University of Bologna