Home Study on mixing characteristics of viscoplastic fluid in a rigid-flexible impeller stirred tank
Article
Licensed
Unlicensed Requires Authentication

Study on mixing characteristics of viscoplastic fluid in a rigid-flexible impeller stirred tank

  • Deyin Gu EMAIL logo , Yinghua Song , Li Wen and Mei Ye
Published/Copyright: March 6, 2024

Abstract

The rigid-flexible impeller (RF impeller) was used in the mixing process of viscoplastic fluid, and the mixing performance of RF impeller was explored by using numerical simulation and experimental analysis. Results indicated that RF impeller could reduce the power consumption (P) and demonstrate the advantage of energy-saving compared with Rushton turbine (RT). RF impeller demonstrated a more pronounced force coupling effect between the impeller and surrounding fluid, and exhibited superior adaptability in the flow field compared with RT. Meanwhile, the utilization of RF impeller can effectively enhance the expansion of high velocity region, expand the cavern zone, and decrease the mixing efficiency number while maintaining constant P compared with RT, and the size of high velocity region and cavern zone could be increased with an increase in impeller speed. Moreover, the cavern structure was obtained through the visualization experiment, and the results were similar to that in the simulation. The findings suggested that incorporating rigid-flexible combination structure design of impeller blades could effectively expand the cavern zone, reduce the stagnant zone, and enhance the mixing efficiency in the viscoplastic fluid mixing process.


Corresponding author: Deyin Gu, School of Environment and Resources, Chongqing Technology and Business University, Chongqing 400060, China, E-mail:

Funding source: National Natural Science Foundation Project of China

Award Identifier / Grant number: 22208037

Award Identifier / Grant number: (KJQN202200805)

Award Identifier / Grant number: (S202311799023)

Funding source: Natural Science Foundation Project of Chongqing

Award Identifier / Grant number: (CSTB2022NSCQ-MSX0400)

  1. Research ethics: Not applicable.

  2. Informed consent: Not applicable.

  3. Author contributions: The authors have accepted responsibility for the entire content of this manuscript and approved its submission.

  4. Competing interests: The author(s) state no conflict of interest.

  5. Research funding: The study was supported by the National Natural Science Foundation Project of China (22208037), Natural Science Foundation Project of Chongqing (CSTB2022NSCQ-MSX0400), Science and Technology Research Program of Chongqing Municipal Education Commission (KJQN202200805), Chongqing Technology and Business University college students innovation and entrepreneurship training program (S202311799023).

  6. Data availability: Not applicable.

References

[1] H. Ameur, “Modifications in the Rushton turbine for mixing viscoplastic fluids.” Int. J. Food Eng. vol. 233, pp. 117–125, 2018. https://doi.org/10.1016/j.jfoodeng.2018.04.005.Search in Google Scholar

[2] Y. Y. Bao, et al.., “Power demand and mixing performance of coaxial mixers in a stirred tank with CMC solution,” Chin. J. Chem. Eng., vol. 23, pp. 623–632, 2015. https://doi.org/10.1016/j.cjche.2015.01.002.Search in Google Scholar

[3] A. W. Russell, et al.., “Mixing viscoplastic fluids in stirred vessels over multiple scales: an experimental and CFD approach,” Chem. Eng. Sci., vol. 208, pp. 115129, 2019. https://doi.org/10.1016/j.ces.2019.07.047.Search in Google Scholar

[4] B. Sajjadi, A. A. A. Raman, and R. Parthasarathy, “Fluid dynamic analysis of non-Newtonian flow behavior of municipal sludge simulant in anaerobic digesters using submerged, recirculating jets,” Chem. Eng. J., vol. 298, pp. 259–270, 2016. https://doi.org/10.1016/j.cej.2016.03.069.Search in Google Scholar

[5] H. Ameur, “Effect of some parameters on the performance of anchor impellers for stirring shear-thinning fluids in a cylindrical vessel,” J. Hydrodyn., vol. 28, pp. 699–675, 2016. https://doi.org/10.1016/s1001-6058(16)60671-6.Search in Google Scholar

[6] H. Ameur, “Mixing of complex fluids with flat and pitched bladed impellers: effect of blade attack angle and shear-thinning behavior,” Food Bioproducts Process., vol. 99, pp. 71–77, 2016. https://doi.org/10.1016/j.fbp.2016.04.004.Search in Google Scholar

[7] J. S. Ayala, et al.., “Two-dimensional shear rate field and flow structures of a pseudoplastic fluid in a stirred tank using particle image velocimetry,” Chem. Eng. Sci., vol. 248, pp. 117198, 2022. https://doi.org/10.1016/j.ces.2021.117198.Search in Google Scholar

[8] A. Kazemzadeh, F. Ein-Mozaffari, A. Lohi, and L. Pakzad, “Investigation of hydrodynamic performances of coaxial mixers in agitation of yield-pseudoplasitc fluids: single and double central impellers in combination with the anchor,” Chem. Eng. J., vol. 294, pp. 417–430, 2016. https://doi.org/10.1016/j.cej.2016.03.010.Search in Google Scholar

[9] M. G. Romano, et al.., “3D-PTV flow measurements of Newtonian and non-Newtonian fluid blending in a batch reactor in the transitional regime,” Chem. Eng. Sci., vol. 246, pp. 116969, 2021. https://doi.org/10.1016/j.ces.2021.116969.Search in Google Scholar

[10] J. Sossa-Echeverria and F. Taghipour, “Computational simulation of mixing flow of shear thinning non-Newtonian fluids with various impellers in a stirred tank,” Chem. Eng. Process. Process Intensif., vol. 93, pp. 66–78, 2015. https://doi.org/10.1016/j.cep.2015.04.009.Search in Google Scholar

[11] H. Ameur, “Newly modified curved-bladed impellers for process intensification: Energy saving in the agitation of Hershel-Bulkley fluids,” Chem. Eng. Process. Process Intensif., vol. 154, pp. 108009, 2020. https://doi.org/10.1016/j.cep.2020.108009.Search in Google Scholar

[12] L. Pakzad, F. Ein-Mozaffari, S. R. Upreti, and A. Lohi, “A novel and energy-efficient coaxial mixer for agitation of non-Newtonian fluids possessing yield stress,” Chem. Eng. Sci., vol. 101, pp. 642–654, 2013. https://doi.org/10.1016/j.ces.2013.07.027.Search in Google Scholar

[13] D. Y. Luan, S. F. Zhang, J. P. Lu, and X. G. Zhang, “Chaotic characteristics enhanced by impeller of perturbed six-bent-bladed turbine in stirred tank,” Results Phys., vol. 7, pp. 1524–1530, 2017. https://doi.org/10.1016/j.rinp.2017.04.030.Search in Google Scholar

[14] J. D. Eldredge and D. Pisani, “Passive locomotion of a simple articulated fish-like system in the wake of an obstacle,” J. Fluid Mech., vol. 607, pp. 279–288, 2008. https://doi.org/10.1017/s0022112008002218.Search in Google Scholar

[15] S. Karray, Z. Driss, H. Kchaou, and M. S. Abid, “Numerical simulation of fluid-structure interaction in a stirred vessel equipped with an anchor impeller,” J. Mech. Sci. Technol., vol. 25, pp. 1749–1760, 2011. https://doi.org/10.1007/s12206-011-0514-9.Search in Google Scholar

[16] J. D. Szezech, A. B. Schelin, I. L. Caldas, S. R. Lopes, P. J. Morrison, and R. L. Viana, “Finite-time rotation number: A fast indicator for chaotic dynamical structures,” Phys. Lett. A, vol. 377, pp. 452–456, 2013. https://doi.org/10.1016/j.physleta.2012.12.013.Search in Google Scholar

[17] R. L. Campbell and E. G. Paterson, “Fluid-structure interaction analysis of flexible turbomachinery,” J. Fluids Struct., vol. 27, pp. 1376–1391, 2011. https://doi.org/10.1016/j.jfluidstructs.2011.08.010.Search in Google Scholar

[18] Z. H. Liu, X. P. Zheng, D. Liu, Y. D. Wang, and C. Y. Tao, “Enhancement of liquid-liquid mixing in a mixer-settler by a double rigid-flexible combination impeller,” Chem. Eng. Process. Process Intensif., vol, 86, pp. 69–77, 2014. https://doi.org/10.1016/j.cep.2014.10.007.Search in Google Scholar

[19] G. Ascanio, S. Foucault, and P. A. Tanguy, “Time-periodic mixing of shear-thinning fluids,” Chem. Eng. Res. Design, vol. 82, pp. 1199–1203, 2004. https://doi.org/10.1205/cerd.82.9.1199.44155.Search in Google Scholar

[20] P. E. Arratia, J. Kukura, J. Lacombe, and F. J. Muzzion, “Mixing of shear-thinning fluids with yield stress in stirred tanks,” AIChE J., vol. 52, pp. 2310–2322, 2006. https://doi.org/10.1002/aic.10847.Search in Google Scholar

[21] A. Amanullah, S. A. Hjorth, and A. W. Nienow, “A new mathematical model to predict cavern diameters in highly shear thinning, power law liquids using axial flow impellers,” Chem. Eng. Sci., vol. 53, pp. 455–469, 1998. https://doi.org/10.1016/s0009-2509(97)00200-5.Search in Google Scholar

[22] D. Y. Luan, Z. R. Wang, H. Wang, S. S. Wang, L. B. Li, and Y. M. Chen, “Determination method of the cavern boundary viscosity in a stirred tank with pseudoplastic fluid,” AIChE J., vol. 66, pp. e16941, 2020. https://doi.org/10.1002/aic.16941.Search in Google Scholar

[23] S. S. Wang, H. Li, C. Y. Tao, R. L. Liu, Y. D. Wang, and Z. H. Liu, “Study on cavern evolution and performance of three mixers in agitation of yield-pseudoplastic fluids,” Chin. J. Chem. Eng., vol, 55, pp. 111–122, 2023. https://doi.org/10.1016/j.cjche.2022.06.001.Search in Google Scholar

[24] H. Ameur, “Energy efficiency of different impellers in stirred tank reactors,” Energy, vol. 93, pp. 1980–1988, 2015. https://doi.org/10.1016/j.energy.2015.10.084.Search in Google Scholar

[25] H. Ameur, D. Sahel, and Y. Kamla, “Energy efficiency of a deep hollow bladed impeller for mixing viscoplastic fluids in a cylindrical vessel,” Adv. Mech. Eng., vol. 9, pp. 1–7, 2017. https://doi.org/10.1177/1687814016687912.Search in Google Scholar

[26] L. Pakzad, F. Ein-Mozaffari, and P. Chan, “Using computational fluid dynamics modeling to study the mixing of pseudoplastic fluids with a Scaba 6SRGT impeller,” Chem. Eng. Process. Process Intensif., vol. 47, pp. 2218–2227,2008. https://doi.org/10.1016/j.cep.2007.12.003.Search in Google Scholar

[27] S. S. Wang, “Study on Cavern Axial Development Law of Pseudoplastic Fluid Stirred with Perturbed Six-Bent-Bladed Turbine Impeller,” Master’s thesis, Qingdao: Qingdao University of Science and Technology, 2021.Search in Google Scholar

[28] H. Ameur and C. Vial, “Modified scaba 6SRGT impellers for process intensification: Cavern size and energy saving when stirring viscoplastic fluids,” Chem. Eng. Process. Process Intensif., vol. 148, pp. 107795, 2020. https://doi.org/10.1016/j.cep.2019.107795.Search in Google Scholar

[29] R. A. Ghotli, M. S. Shafeeyan, M. R. Abbasi, A. A. A. Raman, and S. Ibrahim, “Macromixing study for various designs of impellers in a stirred vessel,” Chem. Eng. Process. Process Intensif., vol. 148, pp. 107794, 2020. https://doi.org/10.1016/j.cep.2019.107794.Search in Google Scholar

[30] A. Ochieng and M. S. Onyango, “Homogenization energy in a stirred tank,” Chem. Eng. Process. Process Intensif., vol. 47, pp. 1853–1860, 2008. https://doi.org/10.1016/j.cep.2007.10.014,Search in Google Scholar

Received: 2023-11-25
Accepted: 2024-02-16
Published Online: 2024-03-06

© 2024 Walter de Gruyter GmbH, Berlin/Boston

Downloaded on 10.9.2025 from https://www.degruyterbrill.com/document/doi/10.1515/ijcre-2023-0219/html
Scroll to top button