The Effects of Liquid Density and Impeller Size with Volute Clearance on the Performance of Radial Blade Centrifugal Pumps: An Experimental Approach


Authors : Clinton Nachukwu Idibia; Joseph Chukwuma Ofodu; Ebigenibo Genuine Saturday

Volume/Issue : Volume 9 - 2024, Issue 6 - June


Google Scholar : https://tinyurl.com/bdcr2yup

Scribd : https://tinyurl.com/2ttkf77a

DOI : https://doi.org/10.38124/ijisrt/IJISRT24JUN871

Note : A published paper may take 4-5 working days from the publication date to appear in PlumX Metrics, Semantic Scholar, and ResearchGate.


Abstract : This study was carried out to experimentally investigate the effect of impeller size with volute clearance and liquid density on the performance of radial blade centrifugal pumps. Three impeller sizes of 121.54mm, 109.38mm and 97.23mm with respective volute clearance of 6mm, 12mm and 18mm were considered, and five different liquid blend which comprise of water, two liquids that are denser than water and two other liquids that are less-dense than water (with respective liquid densities of: 1197 kg/m3 , 1097 kg/m3 , 1000kg/m3 , 898.2 kg/m3 and 798.4 kg/m3 ). In the experimental set-up, the pump flow capacity were varied from 12m3 /hr to 62m3 /hr at interval of 5m3 /hr and the corresponding pump power consumption, attained pump head were recorded and pump efficiency were determined. Microsoft excel was used to evaluate the trend, performance trend was used to develop the pump performance model showing the relationship between the various parameters. The results from the investigation revealed that with the various impeller sizes of 121.54mm, 109.38mm and 97.23mm of respective volute clearance of 6mm, 12mm and 18mm, the attained optimum efficiency were 74.42%, 54.78 and 33.54% respectively at a correspondence optimum pump head of 23.66m, 20.60m and 18.87m. The results also showed that there is a direct relationship between pump power consumption and process liquid density, while showing an inverse linear relationship between the pump instantaneous start up power and impeller diameter. It was therefore concluded among others that liquid with higher density will usually require higher power to initiate and maintain flow at constant flow rate and impeller size. It is then recommended among others that pump designers, application engineers and users of centrifugal pumps should consider possible increase in pump power consumption when working with a process application that has higher tendency for dynamic increase on the process fluid density.

References :

  1. Ahmed, F. (2015). Experimental and computational study of semi-open centrifugal pump. Research Gate Publication (No 293806626). 1145 – 1172.
  2. Caridad, A., & Kenyery, F. (2005). Slip factor for centrifugal impellers under single and two-phase flow conditions. Journal of Fluids Engineering, 127 (233), 317-321.
  3. Carravetta, A., Fecarotta, O. & Ramos, H. (2011). Numerical simulation on pump as turbine: mesh reliability and performance concerns. Proceedings of the international conference on clean electrical power (ICCEP), New York.
  4. Cheah, K., Lee, T. & Winoto, S. H & Zhao, Z.M. (2007). Numerical flow simulation in a centrifugal pump at design and off-design conditions. International Journal of Rotating Machinery, 2007, 1-8.
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  6. Gonzalez, J., Fernandez, J., Blanco, E. & Santolaria, C. (2002). Numerical simulation of the dynamic effects due to impeller-volute interaction in a centrifugal pump, transactions. American society of Mechanical Engineers Journal of Fluids Engineering, 12 (4), 348-355.
  7. Jafarzadeh, B., Hajari, A., Alishahi, M. & Akbari, M. (2021). Flow simulation of a low-specific-speed high-speed centrifugal pump. Applied Mathematical Modelling, 35 (1), 242-249.
  8. Yang, S., Liu, H., & Kong, F. (2014). Effects of the radial gap between impeller tips and volute tongue influencing the performance and pressure pulsations of pump as turbine. Journal of Fluids Engineering, 136 (5), 150–164.

This study was carried out to experimentally investigate the effect of impeller size with volute clearance and liquid density on the performance of radial blade centrifugal pumps. Three impeller sizes of 121.54mm, 109.38mm and 97.23mm with respective volute clearance of 6mm, 12mm and 18mm were considered, and five different liquid blend which comprise of water, two liquids that are denser than water and two other liquids that are less-dense than water (with respective liquid densities of: 1197 kg/m3 , 1097 kg/m3 , 1000kg/m3 , 898.2 kg/m3 and 798.4 kg/m3 ). In the experimental set-up, the pump flow capacity were varied from 12m3 /hr to 62m3 /hr at interval of 5m3 /hr and the corresponding pump power consumption, attained pump head were recorded and pump efficiency were determined. Microsoft excel was used to evaluate the trend, performance trend was used to develop the pump performance model showing the relationship between the various parameters. The results from the investigation revealed that with the various impeller sizes of 121.54mm, 109.38mm and 97.23mm of respective volute clearance of 6mm, 12mm and 18mm, the attained optimum efficiency were 74.42%, 54.78 and 33.54% respectively at a correspondence optimum pump head of 23.66m, 20.60m and 18.87m. The results also showed that there is a direct relationship between pump power consumption and process liquid density, while showing an inverse linear relationship between the pump instantaneous start up power and impeller diameter. It was therefore concluded among others that liquid with higher density will usually require higher power to initiate and maintain flow at constant flow rate and impeller size. It is then recommended among others that pump designers, application engineers and users of centrifugal pumps should consider possible increase in pump power consumption when working with a process application that has higher tendency for dynamic increase on the process fluid density.

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