Skip to main content
Log in

Numerical simulation and analysis of power consumption and Metzner-Otto constant for impeller of 6PBT

  • Published:
Chinese Journal of Mechanical Engineering Submit manuscript

Abstract

Majority of non-Newtonian fluids are pseudoplastic with shear-thinning property, which means that the viscosity will be different in different parts of the stirred tank. In such mixing process, it is difficult to predict accurately the power consumption and mean shear rate for designing novel impeller. Metzner-Otto method is a widely accepted method to solve these questions in mixing non-Newtonian fluids. As a result, Metzner-Otto constant will become a key factor to achieve an optimum way of economical mixing. In this paper, taking glycerine and xanthan gum solutions as research system, the power consumption, stirred by the impeller composed of perturbed six-bent-bladed turbine (6PBT) with differently geometrical characteristics in a cylindrical vessel, is studied by means of computational fluid dynamics (CFD). The flow is modeled as laminar and a multiple reference frame (MRF) approach is used to solve the discretized equations of motion. In order to determine the capability of CFD to forecast the flow process, the torque test experiment is used to measure the glycerine solution power consumption. The rheological properties of the xanthan gum solutions are determined by a Brookfield rheometer. It is observed that the power consumption predicted by numerical simulation agrees well with those measured using torque experiment method in stirring glycerine solution, which validate the numerical model. Metzner-Otto constant is almost not correlated with the flow behavior index of pseudoplastic fluids. This paper establishes the complete correlations of power constant and Metzner-Otto constant with impeller geometrical characteristics through linear regression analysis, which provides the valuable instructions and references for accurately predicting the power consumption and mean shear rate of pseudoplastic fluids in laminar flow, comparatively.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

References

  1. EIN-MOZAFFARI F, UPRETI S R. Using ultrasonic doppler velocimetry and CFD modeling to investigate the mixing of non-Newtonian fluids possessing yield stress[J]. Chem Eng Res Des, 2009, 87(4): 515–523.

    Article  Google Scholar 

  2. METZNER A B, OTTO R E. Agitation of non-Newtonian fluids[J]. AIChE J, 1957, 3(1): 3–11.

    Article  Google Scholar 

  3. SESTAK J, ZITNY R, HOUSKA M. Anchor-agitated systems: Power input correlation for pseudoplastic and thixotropic fluids in equilibrium[J]. AIChE J, 1986, 32(1): 155–158.

    Article  Google Scholar 

  4. TANGUY P A, LACROIX R, BERTRAND F, et al. Finite element analysis of viscous mixing with a helical ribbon-screw impeller[J]. AIChE J, 1992, 38(6): 939–944.

    Article  Google Scholar 

  5. BECKNER J L, SMITH J M. Anchor-agitated systems: Power input with Newtonian and pseudo-plastic fluids[J]. Trans Instn Chem Engrs, 1966, 44(6): 224–236.

    Google Scholar 

  6. SAWINSKY J, BALINT A, BENDE S. Conversion for laminar flow of bingham plastic fluids in an isothermal tube reactor[J]. Chem Eng Sci, 1988, 43(5): 1209–1211.

    Article  Google Scholar 

  7. CALDERBANK P H, MOO-YANG M B. Power characteristics of agitators for mixing of Newtonian and non-Newtonian fluids[J]. Trans Instn Chem Engrs, 1961, 39(5): 337–347.

    Google Scholar 

  8. SCHILO D. Power requirements of tangential stirrers for stirring non-Newtonian liquids[J]. Chem Ing Tech, 1969, 41(5–6): 253–259.

    Article  Google Scholar 

  9. TANGUY P A, THIBAULT F, DE LA FUENTE E B. A new investigation of the Metzner-Otto concept for anchor mixing impellers[J]. Can J Chem Eng, 1996, 74(2): 222–228.

    Article  Google Scholar 

  10. CARREAU P J, CHHABRA R P, CHENG J. Effect of rheological properties on power consumption with helical ribbon agitators[J]. AIChE J, 1993, 39(9): 1421–1430.

    Article  Google Scholar 

  11. POLLARD J, KANTYKA T A. Heat transfer to agitated non-Newtonian fluids [J]. Trans Instn Chem Engrs, 1969, 47(1): 21–27.

    Google Scholar 

  12. RIEGER F, NOVAK V. Power consumption scale-up in agitating non-Newtonian fluids[J]. Chem Eng Sci, 1974, 29(11): 2229–2234.

    Article  Google Scholar 

  13. BRITO-DE LA FUENTE E, CHOPLIN L, TANGUY P A. Mixing with helical ribbon impellers: effect of highly shear thinning behaviour and impeller geometry [J]. Chem Eng Res Des, 1997, 75A1(A1): 45–52.

    Article  Google Scholar 

  14. LUAN Deyu, ZHOU Shenjie, CHEN Songying, et al., Investigation on the chaotic agitation of pseudoplastic fluid with a perturbed six-bent-bladed impeller [J]. China Chem Eng, 2011, 39(9): 41–46. (in Chinese)

    Google Scholar 

  15. NOVAK V, RIEGER F. Homogenization with helical screw agitator[J]. Trans Inst Chem Eng, 1969, 47(10): 335–340.

    Google Scholar 

  16. PAKZAD L, EIN-MOZAFFARI F, CHAN P. Using electrical resistance tomography and computational fluid dynamics modeling to study the formation of cavern in the mixing of pseudoplastic fluids possessing yield stress[J]. Chem Eng Sci, 2008, 63(9): 2508–2522.

    Article  Google Scholar 

  17. SAEED S, EIN-MOZAFFARI F. Using dynamic tests to study the continuous mixing of xanthan gum solutions[J]. Chem Technol Biotechnol, 2008, 83(4): 559–568.

    Article  Google Scholar 

  18. AMANULLAH A, HJORTH S A, NIENOW A W. Cavern sizes generated in highly shear thinning viscous fluids by SCABA 3SHP1 impeller[J]. FoodBioprod Process, 1997, 75(4): 232–238.

    Article  Google Scholar 

  19. WANG Jiajun, FENG Lianfeng, GU Xueping, et al. Power consumption of inner-outer helical ribbon impellers in viscous Newtonian and non-Newtonian fluids[J]. Chem Eng Sci, 2000, 55(12): 2339–2342.

    Article  Google Scholar 

  20. BRUCATO A, CIOFALO M, CRISFI F, et al. Numerical prediction of flow fields in baffled stirred vessels: a comparison of alternative modeling approaches[J]. Chem Eng Sci, 1998, 53(21): 3653–3684.

    Article  Google Scholar 

  21. DEEN N G, SOLBERG T, HJERTAGER B H. Flow generated by an aerated Rushton impeller: Two-phase PIV experiments and numerical simulations[J]. Can J Chem Eng, 2002, 80(4): 638–652.

    Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Deyu Luan.

Additional information

Supported by Shandong Provincial Science and Technology Development planning Program of China (Grant No. 2013YD09007), and Scientific Foundation of Qingdao University of Science and Technology of China

LUAN Deyu, born in 1964, is currently a vice-professor at Qingdao University of Science and Technology, China. He received his PhD degree from Shandong Universtiy, China, in 2012. His research interests include the efficient technology of procession equipment, fluid mechanics engineering, numerical simulation technology.

CHEN Qiao, born in 1989, received bachelor degree from Qingdao University of Science and Technology, China, in 2012. He is currently studying the chaotic mixing of non-Newtonian fluids in stirred tank.

ZHOU Shenjie, born in 1958, is currently a professor at Shandong University, China. He received his PhD degree from Tongji Universtiy, China, in 2000. His research interests include the efficient technology of procession equipment, micro-mechanics system, numerical simulation technology.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Luan, D., Chen, Q. & Zhou, S. Numerical simulation and analysis of power consumption and Metzner-Otto constant for impeller of 6PBT. Chin. J. Mech. Eng. 27, 635–640 (2014). https://doi.org/10.3901/CJME.2014.03.635

Download citation

  • Received:

  • Revised:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.3901/CJME.2014.03.635

Keywords

Navigation