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 :
- Ahmed, F. (2015). Experimental and computational study of semi-open centrifugal pump. Research Gate Publication (No 293806626). 1145 – 1172.
- 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.
- 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.
- 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.
- Choi, D., Kurokawa, J. & Matsui, J. (2006). Performance and internal flow characteristics of a very low specific speed centrifugal pump. Journal of Fluids Engineering, 12 (8), 341-349.
- 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.
- 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.
- 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.