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Question

The brake power of a centrifugal pump having an impeller diameter of 200 mm is 1.86 kW. If the impeller is replaced with another impeller of 180 mm diameter, the brake power of the pump in kW will be ________.

Centrifugal Pump Power Calculation Using Affinity Laws

This problem involves calculating the change in brake power of a centrifugal pump when the impeller diameter is altered. We can use the pump affinity laws, specifically the relationship between brake power and impeller diameter.

Pump Affinity Law for Power

For a centrifugal pump operating at a constant speed, the brake power ($P$) required is directly proportional to the cube of the impeller diameter ($D$). This can be expressed mathematically as:

$ P \propto D^3 $

Therefore, the ratio of brake power for two different impeller diameters ($D_1$ and $D_2$) is:

$ \frac{P_2}{P_1} = \left(\frac{D_2}{D_1}\right)^3 $

Calculating New Brake Power

We are given:

  • Initial brake power, $P_1 = 1.86$ kW
  • Initial impeller diameter, $D_1 = 200$ mm
  • New impeller diameter, $D_2 = 180$ mm

We need to find the new brake power, $P_2$. Rearranging the formula:

$ P_2 = P_1 \times \left(\frac{D_2}{D_1}\right)^3 $

Substitute the given values:

$ P_2 = 1.86 \text{ kW} \times \left(\frac{180 \text{ mm}}{200 \text{ mm}}\right)^3 $

First, calculate the ratio of the diameters:

$ \frac{180}{200} = 0.9 $

Now, cube this ratio:

$ (0.9)^3 = 0.729 $

Finally, calculate $P_2$:

$ P_2 = 1.86 \text{ kW} \times 0.729 $

$ P_2 \approx 1.35594 \text{ kW} $

The calculated brake power is approximately 1.356 kW. This value falls within the range of 1.35 kW to 1.36 kW.

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Important Questions from Pump Characteristics

  1. Impeller speed of a centrifugal pump is increased by $30\%$. The power requirement of the pump increases by $n$ times. The value of $n$ is ________. (Rounded off to two decimal places)
  2. A centrifugal pump having an overall efficiency of $75\%$ requires $6 \text{ kW}$ power at $1450 \text{ rpm}$ to deliver water against a suction head of $5 \text{ m}$ and a delivery head of $12 \text{ m}$. If the pump runs at $1650$ $\text{rpm}$ and frictional head losses are negligible, the total head developed by the pump in metres will be
  3. At a speed of 1800 rpm, a centrifugal pump discharges 50 L s$^{-1}$ at its best point of efficiency for a total head of 25 m. The specific speed of the pump in rpm (round off to 2 decimal places) is ________
  4. Discharge from a centrifugal pump operating at $1000$ rpm with a total head of $30$ m is $300$ L $min^{-1}$. The pump efficiency is $65\%$. If speed of the pump is increased to $1200$ rpm, the power required to operate the pump in kW is ________ (rounded off to $2$ decimal places).
    Consider acceleration due to gravity = $9.81$ m $s^{-2}$.
  5. A six-stage centrifugal pump delivers 120 L $s^{-1}$ against a total head of 510 m. If the design speed of this pump is 1450 rpm, the specific speed of the pump will be ______________.

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