Find the rise in pressure in the impeller of a centrifugal pump through which water is flowing at the rate of 15 litres/s. The internal and external diameters of the impeller are 20 cm and 40 cm respectively. The widths of impeller at inlet and outlet are 1.6 cm and 0.8 cm. The pump is running at 1200 r.p.m. The water enters the impeller radially at inlet and impeller vane angle at outlet is 30°. Neglect losses through the impeller.

Impeller Pressure Rise Calculation

Problem Statement

Find the rise in pressure in the impeller of a centrifugal pump through which water is flowing at the rate of 15 litres/s. The internal and external diameters of the impeller are 20 cm and 40 cm respectively. The widths of impeller at inlet and outlet are 1.6 cm and 0.8 cm. The pump is running at 1200 r.p.m. The water enters the impeller radially at inlet and impeller vane angle at outlet is 30°. Neglect losses through the impeller.

Given Data & Constants

  • Discharge, \(Q = 15 \, \text{L/s} = 0.015 \, \text{m}^3/\text{s}\)
  • Internal diameter, \(D_1 = 20 \, \text{cm} = 0.2 \, \text{m}\)
  • External diameter, \(D_2 = 40 \, \text{cm} = 0.4 \, \text{m}\)
  • Inlet width, \(b_1 = 1.6 \, \text{cm} = 0.016 \, \text{m}\)
  • Outlet width, \(b_2 = 0.8 \, \text{cm} = 0.008 \, \text{m}\)
  • Speed, \(N = 1200 \, \text{r.p.m.}\)
  • Outlet vane angle, \(\phi = 30^\circ\)
  • Radial inlet: \(V_{w1} = 0\)
  • Density of water, \(\rho = 1000 \, \text{kg/m}^3\)
  • Acceleration due to gravity, \(g = 9.81 \, \text{m/s}^2\)

Solution

1. Calculate Tangential Velocities (\(u_1, u_2\))

$$ u_1 = \frac{\pi D_1 N}{60} = \frac{\pi \times 0.2 \times 1200}{60} \approx 12.566 \, \text{m/s} $$ $$ u_2 = \frac{\pi D_2 N}{60} = \frac{\pi \times 0.4 \times 1200}{60} \approx 25.133 \, \text{m/s} $$

2. Calculate Flow Velocities (\(V_{f1}, V_{f2}\))

The flow velocities are calculated from the discharge and the impeller area at inlet and outlet.

$$ V_{f1} = \frac{Q}{\pi D_1 b_1} = \frac{0.015}{\pi \times 0.2 \times 0.016} \approx 1.492 \, \text{m/s} $$ $$ V_{f2} = \frac{Q}{\pi D_2 b_2} = \frac{0.015}{\pi \times 0.4 \times 0.008} \approx 1.492 \, \text{m/s} $$

3. Determine Outlet Whirl Velocity (\(V_{w2}\))

$$ \tan(\phi) = \frac{V_{f2}}{u_2 - V_{w2}} \implies u_2 - V_{w2} = \frac{V_{f2}}{\tan(\phi)} $$ $$ V_{w2} = u_2 - \frac{V_{f2}}{\tan(\phi)} = 25.133 - \frac{1.492}{\tan(30^\circ)} $$ $$ V_{w2} \approx 25.133 - 2.584 \approx 22.549 \, \text{m/s} $$

4. Calculate Rise in Pressure Head in the Impeller

The pressure head rise is the total energy added (Euler Head) minus the gain in kinetic energy.

$$ \text{Pressure Head Rise} = \frac{P_2 - P_1}{\rho g} = \frac{1}{2g} \left[ (u_2^2 - u_1^2) - (V_{r2}^2 - V_{r1}^2) \right] $$ $$ \text{First, find relative velocities } V_{r1} \text{ and } V_{r2} $$ $$ V_{r1}^2 = V_{f1}^2 + u_1^2 = (1.492)^2 + (12.566)^2 = 2.226 + 157.904 = 160.13 $$ $$ V_{r2}^2 = V_{f2}^2 + (u_2 - V_{w2})^2 = (1.492)^2 + (2.584)^2 = 2.226 + 6.677 = 8.903 $$ $$ \text{Now substitute into the pressure head equation:} $$ $$ \frac{P_2 - P_1}{\rho g} = \frac{1}{2 \times 9.81} \left[ (25.133^2 - 12.566^2) - (8.903 - 160.13) \right] $$ $$ \frac{P_2 - P_1}{\rho g} = \frac{1}{19.62} \left[ (631.667 - 157.904) - (-151.227) \right] $$ $$ \frac{P_2 - P_1}{\rho g} = \frac{1}{19.62} [473.763 + 151.227] = \frac{624.99}{19.62} \approx 31.855 \, \text{m} $$
Final Result:

The rise in pressure head in the impeller is approximately \(31.86\) meters of water.

(This corresponds to a pressure of \(312.5 \, \text{kPa}\) or \(31.25 \, \text{N/cm}^2\))

Explanation of the Pressure Rise Calculation

The pressure rise within the impeller is a measure of the increase in static pressure of the fluid as it passes from the inlet (eye) to the outlet (tip). This is the primary function of the impeller. It's important to distinguish this from the total energy (or head) added by the pump.

The total energy added (Euler's Head) is converted into both an increase in pressure (potential energy) and an increase in the fluid's velocity (kinetic energy). To find only the pressure component, we must subtract the gain in kinetic energy from the total energy added. The formula used, \( \frac{1}{2g} [ (u_2^2 - u_1^2) - (V_{r2}^2 - V_{r1}^2) ] \), is a rearranged form of the energy equation across the impeller that directly yields the static pressure head rise.

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