A centrifugal pump rotating at 1800 rpm delivers 0.4 m³/s at a head of 16 m. Calculate the specific speed of the pump and the power input. Assume overall efficiency of the pump as 0.70. If this pump were to operate at 900 rpm what would be the head, discharge and power required for homologous conditions? Assume overall efficiency unchanged at new rpm.
Given data:
Speed of pump N_1=1800 \mathrm{~rpm}
Discharge Q_1=0.4 \mathrm{~m}^3 / \mathrm{s}
Head H_1=16 \mathrm{~m}
Overall efficiency \eta_o=0.70
The power input to the pump is given by
P_1=\frac{\rho Q_1 g H_1}{\eta_o}
=\frac{1000 \times 0.4 \times 9.81 \times 16}{0.7}=89.69 \times 10^3 \mathrm{~W}=89.69 \mathrm{~kW}
The specific speed of the pump is given by Eq. (20.30) as
N_{S P}={\frac{N{\sqrt{Q}}}{(H)^{3/4}}} (20.30)
N_s=\frac{N_1 \sqrt{Q_1}}{H_1^{3 / 4}}
=\frac{1800 \sqrt{0.4}}{(16)^{3 / 4}}=142.3 \text { units }
Let Q_2, H_2 \text { and } P_2 be the discharge, head and power required for homologous condition, respectively. Using Eq. (20.31), we have
\left(\frac{Q}{N D^3}\right)_m=\left(\frac{Q}{N D^3}\right)_p (20.31)
\frac{Q_1}{N_1}=\frac{Q_2}{N_2} \left[\because D_1=D_2\right]
or Q_2=Q_1 \frac{N_2}{N_1}=0.4 \times \frac{900}{1800}=0.2 \mathrm{~m}^3 / \mathrm{s}
Using Eq. (20.32), we obtain
\left({\frac{g H}{N^{2}D^{2}}}\right)_{m}=\left({\frac{g H}{N^{2}D^{2}}}\right)_{p} (20.32)
\frac{H_1}{N_1^2}=\frac{H_2}{N_2^2}
or H_2=H_1 \frac{N_2^2}{N_1^2}=16 \times \frac{900^2}{1800^2}=4 \mathrm{~m}
Using Eq. (20.33), one can write
\left({\frac{P}{\rho N^{3}D^{5}}}\right)_{m}=\left({\frac{P}{\rho N^{3}D^{5}}}\right)_{p} (20.33)
\frac{P_1}{N_1^3}=\frac{P_2}{N_2^3}
or P_2=P_1 \frac{N_2^3}{N_1^3}=89.69 \times \frac{900^3}{1800^3}=11.21 \mathrm{~kW}