CFD simulation of gas-liquid stirred vessel: VC, S33, and L33 flow regimes
A comprehensive computational model based on the Eulerian–Eulerian approach was developed to simulate gas–liquid flows in a stirred vessel. A separate submodel was developed to quantitatively understand the influence of turbulence and presence of neighboring bubbles on drag acting on bubbles. This s...
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| Published in | AIChE journal Vol. 52; no. 5; pp. 1654 - 1672 |
|---|---|
| Main Authors | , |
| Format | Journal Article |
| Language | English |
| Published |
Hoboken
Wiley Subscription Services, Inc., A Wiley Company
01.05.2006
Wiley Subscription Services American Institute of Chemical Engineers |
| Subjects | |
| Online Access | Get full text |
| ISSN | 0001-1541 1547-5905 |
| DOI | 10.1002/aic.10762 |
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| Abstract | A comprehensive computational model based on the Eulerian–Eulerian approach was developed to simulate gas–liquid flows in a stirred vessel. A separate submodel was developed to quantitatively understand the influence of turbulence and presence of neighboring bubbles on drag acting on bubbles. This submodel was used to identify an appropriate correlation for estimating the interphase drag force. The standard k–ϵ turbulence model was used to simulate turbulent gas–liquid flows in a stirred vessel. A computational snapshot approach was used to simulate motion of the standard Rushton turbine in a fully baffled vessel. The computational model was mapped onto FLUENT4.5, a commercial CFD solver. The model predictions were compared with the previously published experimental data of Bombac and co‐workers. The model was used to simulate three distinct flow regimes in gas–liquid stirred vessels: vortex clinging (VC), alternating small cavities (S33), and alternating large cavities (L33). The predicted results show reasonably good agreement with the experimental data for all three regimes. The computational model and results discussed in this work would be useful for understanding and simulating gas holdup distribution and flow regimes in stirred vessels. © 2006 American Institute of Chemical Engineers AIChE J, 2006 |
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| AbstractList | A comprehensive computational model based on the Eulerian-Eulerian approach was developed to simulate gas-liquid flows in a stirred vessel. A separate submodel was developed to quantitatively understand the influence of turbulence and presence of neighboring bubbles on drag acting on bubbles. This submodel was used to identify an appropriate correlation for estimating the interphase drag force. The standard k- turbulence model was used to simulate turbulent gas-liquid flows in a stirred vessel. A computational snapshot approach was used to simulate motion of the standard Rushton turbine in a fully baffled vessel. The computational model was mapped onto FLUENT4.5, a commercial CFD solver. The model predictions were compared with the previously published experimental data of Bombac and co-workers. The model was used to simulate three distinct flow regimes in gas-liquid stirred vessels: vortex clinging (VC), alternating small cavities (S33), and alternating large cavities (L33). The predicted results show reasonably good agreement with the experimental data for all three regimes. The computational model and results discussed in this work would be useful for understanding and simulating gas holdup distribution and flow regimes in stirred vessels. A comprehensive computational model based on the Eulerian–Eulerian approach was developed to simulate gas–liquid flows in a stirred vessel. A separate submodel was developed to quantitatively understand the influence of turbulence and presence of neighboring bubbles on drag acting on bubbles. This submodel was used to identify an appropriate correlation for estimating the interphase drag force. The standard k–ϵ turbulence model was used to simulate turbulent gas–liquid flows in a stirred vessel. A computational snapshot approach was used to simulate motion of the standard Rushton turbine in a fully baffled vessel. The computational model was mapped onto FLUENT4.5, a commercial CFD solver. The model predictions were compared with the previously published experimental data of Bombac and co‐workers. The model was used to simulate three distinct flow regimes in gas–liquid stirred vessels: vortex clinging (VC), alternating small cavities (S33), and alternating large cavities (L33). The predicted results show reasonably good agreement with the experimental data for all three regimes. The computational model and results discussed in this work would be useful for understanding and simulating gas holdup distribution and flow regimes in stirred vessels. © 2006 American Institute of Chemical Engineers AIChE J, 2006 A comprehensive computational model based on the Eulerian-Eulerian approach was developed to simulate gas-liquid flows in a stirred vessel. A separate submodel was developed to quantitatively understand the influence of turbulence and presence of neighboring bubbles on drag acting on bubbles. This submodel was used to identify an appropriate correlation for estimating the interphase drag force. The standard k- turbulence model was used to simulate turbulent gas-liquid flows in a stirred vessel. A computational snapshot approach was used to simulate motion of the standard Rushton turbine in a fully baffled vessel. The computational model was mapped onto FLUENT4.5, a commercial CFD solver. The model predictions were compared with the previously published experimental data of Bombac and co-workers. The model was used to simulate three distinct flow regimes in gas-liquid stirred vessels: vortex clinging (VC), alternating small cavities (S33), and alternating large cavities (L33). The predicted results show reasonably good agreement with the experimental data for all three regimes. The computational model and results discussed in this work would be useful for understanding and simulating gas holdup distribution and flow regimes in stirred vessels. [PUBLICATION ABSTRACT] |
| Author | Ranade, Vivek V. Khopkar, Avinash R. |
| Author_xml | – sequence: 1 givenname: Avinash R. surname: Khopkar fullname: Khopkar, Avinash R. organization: Industrial Flow Modelling Group, National Chemical Laboratory, Pune 411 008, India – sequence: 2 givenname: Vivek V. surname: Ranade fullname: Ranade, Vivek V. email: vv.ranade@ncl.res.in organization: Industrial Flow Modelling Group, National Chemical Laboratory, Pune 411 008, India |
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| Keywords | Gas holdup computational fluid dynamics (CFD) Euler equation Stirred vessel Correlation Turbulence Two phase flow Computational fluid dynamics gas holdup distribution Interphase Hydrodynamics Turbine impeller Forecast model Modeling Rusliton turbine Bubble Flow regime Drag Correlation analysis Gas liquid flow flow regimes Vortex |
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The effect of free stream turbulence on the drag coefficient of spheres. Proceedings Chemeca'70 Vol. 1. Melbourne, Australia: Butterworths; 1970:1-13. Hughmark G. Power requirements and interfacial area in gas-liquid turbine agitated systems. Ind Eng Chem Proc Des Dev. 1980; 19: 641-646. Ranade VV, van den Akker HEA. A computational snapshot of gas-liquid flow in baffled stirred reactors. Chem Eng Sci. 1994; 49: 5175-5192. Lane GL, Schwarz MP, Evans GM. Computational modelling of gas-liquid flow in mechanically stirred tanks. Chem Eng Sci. 2005; 60: 2203-2214. Prakash O, Gupta SN, Mishra P. Newtonian and inelastic non-Newtonian flow across tube banks. Ind Eng Chem Res. 1987; 26: 1365-1372. Pinelli D, Montante G, Magelli F. Dispersion coefficients and settling velocities of solids in slurry vessels stirred with different types of multiple impellers. Chem Eng Sci. 2004; 59: 3081-3089. 1997; 336 1997; 43 1971; 49 2002; 57 1958; 36 1992; 17 1999; 121 1996; 51 2001c 1985; 40 1994; 49 2004 2005; 60 2002 1992; 38 2001b; 79A 1970; 1 1998; 45 1978 1999 1990; 45 1980; 19 1979; 25 2000 1997; 75 1997; 52 2004; 59 2005; 51 1992; 118 1999; 54 1984 1992; 47 1994; 72 1998; 76 2003; 42 1987; 26 e_1_2_7_5_2 Clift R (e_1_2_7_30_2) 1978 e_1_2_7_4_2 e_1_2_7_2_2 e_1_2_7_9_2 e_1_2_7_8_2 e_1_2_7_7_2 e_1_2_7_19_2 e_1_2_7_18_2 Calderbank PH (e_1_2_7_39_2) 1958; 36 e_1_2_7_17_2 e_1_2_7_16_2 e_1_2_7_15_2 e_1_2_7_14_2 e_1_2_7_40_2 e_1_2_7_13_2 e_1_2_7_41_2 e_1_2_7_12_2 e_1_2_7_11_2 e_1_2_7_10_2 e_1_2_7_26_2 e_1_2_7_27_2 e_1_2_7_28_2 e_1_2_7_29_2 e_1_2_7_25_2 e_1_2_7_24_2 e_1_2_7_23_2 e_1_2_7_31_2 e_1_2_7_22_2 e_1_2_7_32_2 Ranade VV (e_1_2_7_3_2) 2002 e_1_2_7_21_2 e_1_2_7_33_2 e_1_2_7_20_2 e_1_2_7_34_2 e_1_2_7_35_2 e_1_2_7_37_2 e_1_2_7_38_2 Uhleherr PHT (e_1_2_7_36_2) 1970 Bakker A (e_1_2_7_6_2) 1994; 72 |
| References_xml | – reference: Khopkar AR, Aubin J, Xureb C, Le Sauze N, Bertrand J, Ranade VV. Gas-liquid flow generated by a pitched blade turbine: Particle velocimetry measurements and CFD simulations. Ind Eng Chem Res. 2003; 42: 5318-5332. – reference: Ranade VV, van den Akker HEA. A computational snapshot of gas-liquid flow in baffled stirred reactors. Chem Eng Sci. 1994; 49: 5175-5192. – reference: Prakash O, Gupta SN, Mishra P. Newtonian and inelastic non-Newtonian flow across tube banks. Ind Eng Chem Res. 1987; 26: 1365-1372. – reference: Gunjal PR, Ranade VV, Chaudhari RV. Computational study of a single-phase flow in packed beds of sphere. AIChE J. 2005; 51: 365-378. – reference: Cui YQ, van der Lans RGJM, Luben KChAM. Local power uptake in gas-liquid systems with single and multiple Rushton turbines. Chem Eng Sci. 1996; 51: 2631-2636. – reference: Clift R, Grace JR, Weber ME. Bubbles, Drops, and Particles. New York, NY: Academic Press; 1978. – reference: Ishii M, Zuber N. 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| Snippet | A comprehensive computational model based on the Eulerian–Eulerian approach was developed to simulate gas–liquid flows in a stirred vessel. A separate submodel... A comprehensive computational model based on the Eulerian-Eulerian approach was developed to simulate gas-liquid flows in a stirred vessel. A separate submodel... |
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| SubjectTerms | Applied sciences Bubbles Chemical engineering computational fluid dynamics (CFD) Exact sciences and technology Experimental data flow regimes Fluid dynamics gas holdup distribution Gases Hydrodynamics of contact apparatus Liquids Mixing Rushton turbine stirred vessel Turbines Turbulence models Turbulent flow |
| Title | CFD simulation of gas-liquid stirred vessel: VC, S33, and L33 flow regimes |
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