Abstract
Detailed particle-image velocimetry (PIV) measurements of flow fields inside semi-open impellers have been performed to understand better the internal flow patterns that are responsible for the unique performance of these centrifugal pumps operated in the range of very low specific speed. Two impellers, one equipped with six radial blades (impeller A) and the other with four conventional backward-swept blades (impeller B), are tested in a centrifugal pump designed to be operated at a non-dimensional specific speed of ns=0.24. Complex flow patterns captured by PIV are discussed in conjunction with the overall pump performance measured separately. It is revealed that impeller A achieves higher effective head than impeller B even though the flow patterns in impeller A are more complex, exhibiting secondary flows and reverse flows in the impeller passage. It is shown that both the localized strong outward flow at the pressure side of each blade outlet and the strong outward through-flow along the suction side of each blade are responsible for the better head performance of impeller A.
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Abbreviations
- A 2 :
-
impeller outlet area, =2πr2b2
- b :
-
impeller passage height (m)
- c :
-
tip clearance (m)
- C p :
-
pressure coefficient, =(p−ps)/(ρu22/2)
- d p :
-
particle diameter (m)
- f :
-
focal length (mm)
- g :
-
acceleration of gravity (m/s2)
- H :
-
effective head (m)
- n :
-
rotational speed (rev/min)
- n s :
-
non-dimensional specific speed
- P :
-
pump power (W)
- p :
-
static pressure measured at impeller outlet (Pa)
- p s :
-
static pressure measured at pump suction area (Pa)
- Q :
-
volume flow rate (m3/min)
- Q 0 :
-
volume flow rate (m3/min) at the best efficiency point (BEP)
- Q d :
-
designed flow rate (m3/min)
- Re :
-
Reynolds number, =u2r2/ν
- r :
-
impeller radius (m)
- u :
-
tangential velocity of impeller (m/s)
- u d :
-
drift velocity (m/s)
- vr, v θ :
-
phase-averaged absolute radial and tangential velocities (m/s)
- \( \overline{{v_{{\text{r}}} }} ,\overline{{v_{\theta } }} \) :
-
time-averaged (or ensemble-averaged) absolute radial and tangential velocities (m/s)
- \( \overline{\overline {v_{{\theta 2}} }} \) :
-
periphery-averaged absolute tangential velocity at the impeller outlet (m/s)
- z :
-
wall-normal distance from suction cover surface (m)
- β :
-
blade angle
- γ :
-
algebraic spiral angle of volute
- η :
-
pump efficiency, =ρgQH/P×100 (%)
- θ :
-
tangential angle measured from volute tongue
- θ s :
-
tangential angle measured at the suction side of impeller blade
- ν :
-
kinematic viscosity (m2/s)
- ρ :
-
density of working fluid (kg/m3)
- τ :
-
torque coefficient, \( = P/0.5\rho A_{2} u^{3}_{2} \)
- φ :
-
discharge coefficient, =Q/A2u2
- ψ :
-
head coefficient, \( = \frac{H} {{{u^{{\text{2}}}_{{\text{2}}} } \mathord{\left/ {\vphantom {{u^{{\text{2}}}_{{\text{2}}} } {2g}}} \right. \kern-\nulldelimiterspace} {2g}}} \)
- ω :
-
angular velocity of impeller (rad/s)
- 2:
-
quantities at impeller outlet
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Choi, YD., Nishino, K., Kurokawa, J. et al. PIV measurement of internal flow characteristics of very low specific speed semi-open impeller. Exp Fluids 37, 617–630 (2004). https://doi.org/10.1007/s00348-004-0838-7
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DOI: https://doi.org/10.1007/s00348-004-0838-7