8 |
Yang N, Xiao Q. A mesoscale approach for population balance modeling of bubble size distribution in bubble column reactors[J]. Chemical Engineering Science, 2017, 170: 241-250.
|
9 |
肖颀, 杨宁. 基于EMMS模型的搅拌釜内气液两相流数值模拟[J]. 化工学报, 2016, 67(7): 2732-2739.
|
|
Xiao Q, Yang N. Numerical simulation of gas-liquid flow in stirred tanks based on EMMS model[J]. CIESC Journal, 2016, 67(7): 2732-2739.
|
10 |
Luo H A, Svendsen H F. Theoretical model for drop and bubble breakup in turbulent dispersions[J]. AIChE Journal, 1996, 42(5): 1225-1233.
|
11 |
Han L C, Luo H A, Liu Y J. A theoretical model for droplet breakup in turbulent dispersions[J]. Chemical Engineering Science, 2011, 66(4): 766-776.
|
12 |
Han L C, Gong S G, Li Y Q, et al. Influence of energy spectrum distribution on drop breakage in turbulent flows[J]. Chemical Engineering Science, 2014, 117: 55-70.
|
13 |
Han L C, Gong S G, Ding Y W, et al. Consideration of low viscous droplet breakage in the framework of the wide energy spectrum and the multiple fragments[J]. AIChE Journal, 2015, 61(7): 2147-2168.
|
14 |
Solsvik J, Tangen S, Jakobsen H A. On the constitutive equations for fluid particle breakage[J]. Reviews in Chemical Engineering, 2013, 29(5): 241-356.
|
15 |
Shi W B, Yang X G, Sommerfeld M, et al. Modelling of mass transfer for gas-liquid two-phase flow in bubble column reactor with a bubble breakage model considering bubble-induced turbulence[J]. Chemical Engineering Journal, 2019, 371: 470-485.
|
16 |
Luo P, Wu J, Pan X, et al. Gas-liquid mass transfer behavior in a surface-aerated vessel stirred by a novel long-short blades agitator[J]. AIChE Journal, 2016, 62(4): 1322-1330.
|
17 |
Martínez-Delgadillo S A, Alonzo-Garcia A, Mendoza-Escamilla V X, et al. Analysis of the turbulent flow and trailing vortices induced by new design grooved blade impellers in a baffled tank[J]. Chemical Engineering Journal, 2019, 358: 225-235.
|
18 |
Mule G M, Kulkarni A A. Mixing of medium viscosity liquids in a stirred tank with fractal impeller[J]. Theoretical Foundations of Chemical Engineering, 2016, 50(6): 914-921.
|
1 |
Straathof A J J, Wahl S A, Benjamin K R, et al. Grand research challenges for sustainable industrial biotechnology[J]. Trends in Biotechnology, 2019, 37(10): 1042-1050.
|
2 |
Amer B, Baidoo E E K. Omics-driven biotechnology for industrial applications[J]. Frontiers in Bioengineering and Biotechnology, 2021, 9: 613307.
|
19 |
Gaddis E S. Mass transfer in gas-liquid contactors[J]. Chemical Engineering and Processing: Process Intensification, 1999, 38(4/5/6): 503-510.
|
20 |
Montante G, Horn D, Paglianti A. Gas-liquid flow and bubble size distribution in stirred tanks[J]. Chemical Engineering Science, 2008, 63(8): 2107-2118.
|
21 |
Khopkar A R, Rammohan A R, Ranade V V, et al. Gas-liquid flow generated by a Rushton turbine in stirred vessel: CARPT/CT measurements and CFD simulations[J]. Chemical Engineering Science, 2005, 60(8/9): 2215-2229.
|
22 |
Sanyal J, Vásquez S, Roy S, et al. Numerical simulation of gas-liquid dynamics in cylindrical bubble column reactors[J]. Chemical Engineering Science, 1999, 54(21): 5071-5083.
|
23 |
van Baten J M, Krishna R. CFD simulations of a bubble column operating in the homogeneous and heterogeneous flow regimes[J]. Chemical Engineering & Technology, 2002, 25(11): 1081-1086.
|
24 |
Schiller L, Naumann A. A drag coefficient correlation[J]. Zeitschrift des Vereins Deutscher Ingenieure, 1935, 77: 318-320.
|
25 |
Orszag S A, Yakhot V, Flannery W S, et al. Renormalization group modeling and turbulence simulations[C]// Proceedings of International Conference on Near-Wall Turbulent Flows. 1993.
|
26 |
Prince M J, Blanch H W. Bubble coalescence and break-up in air-sparged bubble columns[J]. AIChE Journal, 1990, 36(10): 1485-1499.
|
27 |
Wang T F, Wang J F, Jin Y. A novel theoretical breakup kernel function for bubbles/droplets in a turbulent flow[J]. Chemical Engineering Science, 2003, 58(20): 4629-4637.
|
28 |
Garcia-Ochoa F, Gomez E. Bioreactor scale-up and oxygen transfer rate in microbial processes: an overview[J]. Biotechnology Advances, 2009, 27(2): 153-176.
|
29 |
Danckwerts P V. Significance of liquid-film coefficients in gas absorption[M]//Insights Into Chemical Engineering. Amsterdam: Elsevier, 1981: 51-75.
|
30 |
Kerdouss F, Bannari A, Proulx P, et al. Two-phase mass transfer coefficient prediction in stirred vessel with a CFD model[J]. Computers & Chemical Engineering, 2008, 32(8): 1943-1955.
|
31 |
Xiao H, Geng S J, Chen A Q, et al. Bubble formation in continuous liquid phase under industrial jetting conditions[J]. Chemical Engineering Science, 2019, 200: 214-224.
|
3 |
Maluta F, Paglianti A, Montante G. Modelling of biohydrogen production in stirred fermenters by computational fluid dynamics[J]. Process Safety and Environmental Protection, 2019, 125: 342-357.
|
4 |
Wang H N, Jia X Q, Wang X, et al. CFD modeling of hydrodynamic characteristics of a gas-liquid two-phase stirred tank[J]. Applied Mathematical Modelling, 2014, 38(1): 63-92.
|
5 |
Shen X Z, Hibiki T. Bubble coalescence and breakup model evaluation and development for two-phase bubbly flows[J]. International Journal of Multiphase Flow, 2018, 109: 131-149.
|
6 |
Zhang X B, Luo Z H. Effects of bubble coalescence and breakup models on the simulation of bubble columns[J]. Chemical Engineering Science, 2020, 226: 115850.
|
7 |
Luo H. Coalescence, breakup and liquid circulation in bubble column reactors[D]. Trondheim: Norwegian Institute of Technology, 1993.
|