CFD Study of the Mixing of Pseudoplastic Fluids with Yield Stress in a Two-Staged Stirred Tank

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Abstract:

The 3D flow field generated by two-stage impellers in the agitation of xanthan gum, a pseudoplastic fluid with yield stress, was simulated using the commerical CFD package. The effect of impeller speed and impeller spacing on power number, cavern size and viscosity distribution was investigated in this work. The results showed that the power number was slightly influenced by impeller spacing. Higher impeller speed and larger impeller spacing contributed to creation of a bigger cavern. The range of high viscosity zone between the impellers increased with an increase in impeller spacing. Impeller speed and impeller spacing could be used as important parameters to improve the mixing performance of multi-stage impellers in the mixing of pseudoplastic fluids with yield stress.

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Advanced Materials Research (Volumes 354-355)

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604-608

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October 2011

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© 2012 Trans Tech Publications Ltd. All Rights Reserved

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[1] M. Zlokarnik: Stirring: Theory and Practice (Wiley-VCH, Weinheim, Germany 2001)

Google Scholar

[2] E. Galindo and A.W. Nienow: Biotechnol. Prog. Vol. 8 (1992), p.233

Google Scholar

[3] A. Amanullah, S.A. Hjorth and A.W. Nienow: Food Bioprod. Process. Vol. 75 (1997), p.232

Google Scholar

[4] T.P. Elson: Chem. Eng. Commun. Vol. 96 (1990), p.303

Google Scholar

[5] E. Galindo and A.W. Nienow: Chem. Eng. Technol. Vol. 16 (1993), p.102

Google Scholar

[6] D.Y. Luan, S.J. Zhou, S.Y. Chen and S.P. Chu: Chin. J. Process. Eng. Vol. 10 (2010), p.1054

Google Scholar

[7] P.M. Armenante, C. Luo, C.C. Chou, I. Fort and J. Medek: Chem. Eng. Sci. Vol. 52 (1997), p.3483

Google Scholar

[8] A.K. Sahu, P. Kummar and J.B. Joshi: Ind. Eng. Chem. Res. Vol. 37 (1998) , p.2116

Google Scholar

[9] S.S. Murthy and S. Jayanti: AIChE J. Vol. 49 (2003), p.30

Google Scholar

[10] F. Ein-Mozaffari and S.R. Upreti: Chem. Eng. Res. Des. Vol. 87 (2009), p.515

Google Scholar

[11] C.W. Macosko: Rheology: Principles, Measurements & Applications (Wiley-VCH, New York 1994)

Google Scholar

[12] P. Prajapati and F. Ein-Mozaffari: Chem. Eng. Technol. Vol. 32 (2009), p.1211

Google Scholar

[13] A.B. Metzner and R.E. Otto: AIChE J. Vol. 3 (1957), p.3

Google Scholar

[14] M.Alliet-Gaubert, R.Sardeing, C. Xuereb, P.Hobbes, B.Letellier and P.Swaels: Chem. Eng. Process. Vol. 45 (2006), p.415

DOI: 10.1016/j.cep.2005.11.003

Google Scholar

[15] A. Amanullah, S.A. Hjorth and A.W. Nienow: Chem. Eng. Sci. Vol. 53 (1998), p.455

Google Scholar

[16] P.E. Arratia, J. Kukura, J. Lacombe and F.J. Muzzio: AIChE J. Vol. 52 (2006), p.2310

Google Scholar