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PICE 2017
Hosted at Department of Chemical Engineering
AISSMS COE, Pune-1
26 March 2017
Justin K George ,Dr. Vivek Vitankar, Dr. Kanhaiya R Jethani
Department of Chemical Engineering
AISSMS COE, Pune-1
Contents
 Introduction
 Objective
 PBTD Impeller Without Baffle
 PBTD impeller With Baffle
 Comparative Study of PBTD With & Without Baffle
 PBTU Impeller
 Rushton Turbine
 Conclusions
 References
 Fluid flows are governed by partial differential equations
 CFD is the art of replacing PDE systems by a set of algebraic
equations
 CFD provides a qualitative (and quantitative) prediction of fluid
flows by
• mathematical modeling (partial differential equations)
• numerical methods ( discretization and solution techniques)
• software tools (solvers ,pre-and post processing utilities)
Introduction
Objective
• Detailed study of flow in
 PBTD Impeller Vessel without baffle
 PBTD impeller with baffle
 Role of baffle in Mixing
 PBTU Impeller Vessel
 Rushton Turbine Vessel
with the help of CFD .
Parameters Dimensions
Tank diameter, T 0.5 m
Impeller diameter, D 0.17 m
Clearance, C 0.165 m
Height of liquid, H 0.5 m
Baffle width, Bw 0.05 m
Baffle thickness, BT 0.0045 m
Dimensions of the Vessel
Impeller Speed = 468.6 rpm
Geometry of PBTD Impeller Vessel(without baffle)
Velocity Contour of PBTD Without Baffle
Velocity Vector of PBTD Without Baffle
Velocity Streamline of PBTD Without Baffle
Geometry of PBTD Impeller Vessel (with baffle)
Velocity Contour of PBTD With Baffle
Velocity Vector of PBTD With Baffle
Velocity Streamlines of PBTD With Baffle
Geometry of PBTD With & Without Baffle
Velocity Vector Comparison
Streamline Comparison
WITHOUT BAFFLE WITH BAFFLE
Tangential Velocity Comparison
Geometry of PBTU Impeller Vessel
Velocity Contour of PBTU Impeller
Velocity Vector of PBTU Impeller
Velocity Streamline of PBTU Impeller
Geometry of Rushton Turbine Vessel
Velocity Contour of Rushton Turbine
Velocity Vector of Rushton Turbine
Velocity Streamline of Rushton Turbine
Conclusion
 CFD helps to study the fluid flow inside the system.
 MFR model is implemented to simulate the agitated impeller
involving rotating blades in CSTR
 Baffles helps to convert the tangential velocity into radial &
axial velocity components.
 The flow changes by changing the impeller in the same vessel
& with same speed.
References1. T. Kumaresan, Jyeshtharaj B. Joshi (2005). Effect of impeller design on the flow pattern and mixing in stirred tanks,
Chemical Engineering Journal 115 (2006) 173–193
2. Smith J.M. (1990). Industrial needs for mixing research. Trans. Inst. Chem. Eng.68A, 3–6.
3. Nienow A.W. (1996).Mixing studies: a comparison of Rushton turbines with some modern impellers. Chem. Eng Res. Des.
74A, 417–423.
4. Kraume M. and Zehner P. (2001). Experience with experimental standards for measurements of various parameters in stirred
tanks: a comparative test. Trans.Inst. Chem. Eng. 79A, 811–818.
5. Javed K.H.,MahmudT. and Zhu J.M. (2006). Numerical simulation of turbulent batch mixing in a vessel agitated by a
Rushton turbine. Chem. Eng. Process. 45(2), 99–112.
6. Montante G., Lee K., Brucato C.A. and Yianneskis M. (2001). Numerical simulations of the dependency of flow pattern on
impeller clearance in stirred vessels. Chem. Eng.Sci.56, 3751– 3770.
7. BujalskiW., Jaworski Z. and NienowW. (2002). CFD study of homogenization with dual Rushton turbine – comparison with
experimental results II: the multiple frame of reference. Trans. Inst. Chem. Eng. 80A, 97–104.
8. Marchisio D.L. (2009). Large eddy simulation of mixing and reaction in a confined impinging jets reactor. Comput. Chem.
Eng. 33(2), 408–420.
9. Mavros P., Mann R., Vlaer S.D. and Bertr J. (2001). Experimental visualisation and CFD simulation of flow patterns induced
by a novel energy-saving dual configuration impeller in stirred vessels. Trans. Inst. Chem.Eng 78A, 857– 866.
10. Nienow A.W. (1997). On impeller circulation and mixing effectiveness in the turbulent flow regime. Chem. Eng. Sci.
52,2557–2565.
11. Sharma R.N. and Shaikh A.A.(2003). Solids suspension in stirred tanks with pitched blade turbines. Chem. Eng Sci.58,
2123–2140
12. Ranade, V.V., Joshi, J.B., 1989. Flow generated by pitched bladed turbine part i: experimental. Chemical Engineering
Communications 81, 197–224.
13. Ranade, V.V., Mishra, V.P., Saraph, V.S., Deshpande, G.B., Joshi, J.B., 1992. Comparison of axial flow impellers using
LDA. Industrial & Engineering Chemistry Research 31, 2370–2379.
14. Oshinowo, L., Jaworski, Z., Dyster, K.N., Marshall, E., Nienow, A.W., 2000. Predicting the tangential velocity field in
stirred tanks using the multiple reference frames (MRF) model with validation by LDA measurements. In: Proceedings of 10th
European Conference on Mixing, Delft, Netherlands, pp. 247–253.
15. Patwardhan, A.W., 2001. Prediction of flow characteristics and energy balance for a variety of down flow impellers.
Industrial & Engineering Chemical Research 40, 3806–3816.
Cfd study of cstr for different impellers

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Cfd study of cstr for different impellers

  • 1. PICE 2017 Hosted at Department of Chemical Engineering AISSMS COE, Pune-1 26 March 2017 Justin K George ,Dr. Vivek Vitankar, Dr. Kanhaiya R Jethani Department of Chemical Engineering AISSMS COE, Pune-1
  • 2. Contents  Introduction  Objective  PBTD Impeller Without Baffle  PBTD impeller With Baffle  Comparative Study of PBTD With & Without Baffle  PBTU Impeller  Rushton Turbine  Conclusions  References
  • 3.  Fluid flows are governed by partial differential equations  CFD is the art of replacing PDE systems by a set of algebraic equations  CFD provides a qualitative (and quantitative) prediction of fluid flows by • mathematical modeling (partial differential equations) • numerical methods ( discretization and solution techniques) • software tools (solvers ,pre-and post processing utilities) Introduction
  • 4. Objective • Detailed study of flow in  PBTD Impeller Vessel without baffle  PBTD impeller with baffle  Role of baffle in Mixing  PBTU Impeller Vessel  Rushton Turbine Vessel with the help of CFD .
  • 5. Parameters Dimensions Tank diameter, T 0.5 m Impeller diameter, D 0.17 m Clearance, C 0.165 m Height of liquid, H 0.5 m Baffle width, Bw 0.05 m Baffle thickness, BT 0.0045 m Dimensions of the Vessel Impeller Speed = 468.6 rpm
  • 6.
  • 7. Geometry of PBTD Impeller Vessel(without baffle)
  • 8. Velocity Contour of PBTD Without Baffle
  • 9.
  • 10. Velocity Vector of PBTD Without Baffle
  • 11.
  • 12. Velocity Streamline of PBTD Without Baffle
  • 13.
  • 14.
  • 15.
  • 16. Geometry of PBTD Impeller Vessel (with baffle)
  • 17. Velocity Contour of PBTD With Baffle
  • 18.
  • 19. Velocity Vector of PBTD With Baffle
  • 20.
  • 21. Velocity Streamlines of PBTD With Baffle
  • 22.
  • 23.
  • 24.
  • 25. Geometry of PBTD With & Without Baffle
  • 28.
  • 29. WITHOUT BAFFLE WITH BAFFLE Tangential Velocity Comparison
  • 30.
  • 31. Geometry of PBTU Impeller Vessel
  • 32. Velocity Contour of PBTU Impeller
  • 33.
  • 34. Velocity Vector of PBTU Impeller
  • 35.
  • 36. Velocity Streamline of PBTU Impeller
  • 37.
  • 38.
  • 39.
  • 40. Geometry of Rushton Turbine Vessel
  • 41. Velocity Contour of Rushton Turbine
  • 42.
  • 43. Velocity Vector of Rushton Turbine
  • 44.
  • 45. Velocity Streamline of Rushton Turbine
  • 46.
  • 47.
  • 48. Conclusion  CFD helps to study the fluid flow inside the system.  MFR model is implemented to simulate the agitated impeller involving rotating blades in CSTR  Baffles helps to convert the tangential velocity into radial & axial velocity components.  The flow changes by changing the impeller in the same vessel & with same speed.
  • 49. References1. T. Kumaresan, Jyeshtharaj B. Joshi (2005). Effect of impeller design on the flow pattern and mixing in stirred tanks, Chemical Engineering Journal 115 (2006) 173–193 2. Smith J.M. (1990). Industrial needs for mixing research. Trans. Inst. Chem. Eng.68A, 3–6. 3. Nienow A.W. (1996).Mixing studies: a comparison of Rushton turbines with some modern impellers. Chem. Eng Res. Des. 74A, 417–423. 4. Kraume M. and Zehner P. (2001). Experience with experimental standards for measurements of various parameters in stirred tanks: a comparative test. Trans.Inst. Chem. Eng. 79A, 811–818. 5. Javed K.H.,MahmudT. and Zhu J.M. (2006). Numerical simulation of turbulent batch mixing in a vessel agitated by a Rushton turbine. Chem. Eng. Process. 45(2), 99–112. 6. Montante G., Lee K., Brucato C.A. and Yianneskis M. (2001). Numerical simulations of the dependency of flow pattern on impeller clearance in stirred vessels. Chem. Eng.Sci.56, 3751– 3770. 7. BujalskiW., Jaworski Z. and NienowW. (2002). CFD study of homogenization with dual Rushton turbine – comparison with experimental results II: the multiple frame of reference. Trans. Inst. Chem. Eng. 80A, 97–104. 8. Marchisio D.L. (2009). Large eddy simulation of mixing and reaction in a confined impinging jets reactor. Comput. Chem. Eng. 33(2), 408–420. 9. Mavros P., Mann R., Vlaer S.D. and Bertr J. (2001). Experimental visualisation and CFD simulation of flow patterns induced by a novel energy-saving dual configuration impeller in stirred vessels. Trans. Inst. Chem.Eng 78A, 857– 866. 10. Nienow A.W. (1997). On impeller circulation and mixing effectiveness in the turbulent flow regime. Chem. Eng. Sci. 52,2557–2565. 11. Sharma R.N. and Shaikh A.A.(2003). Solids suspension in stirred tanks with pitched blade turbines. Chem. Eng Sci.58, 2123–2140 12. Ranade, V.V., Joshi, J.B., 1989. Flow generated by pitched bladed turbine part i: experimental. Chemical Engineering Communications 81, 197–224. 13. Ranade, V.V., Mishra, V.P., Saraph, V.S., Deshpande, G.B., Joshi, J.B., 1992. Comparison of axial flow impellers using LDA. Industrial & Engineering Chemistry Research 31, 2370–2379. 14. Oshinowo, L., Jaworski, Z., Dyster, K.N., Marshall, E., Nienow, A.W., 2000. Predicting the tangential velocity field in stirred tanks using the multiple reference frames (MRF) model with validation by LDA measurements. In: Proceedings of 10th European Conference on Mixing, Delft, Netherlands, pp. 247–253. 15. Patwardhan, A.W., 2001. Prediction of flow characteristics and energy balance for a variety of down flow impellers. Industrial & Engineering Chemical Research 40, 3806–3816.