A farmer is to pump water at 70°F from a river to a water storage tank nearby using a 125-ft-long, 5-in-diameter plastic pipe with three flanged 90° smooth bends. The water velocity near the river surface is 6 ft/s, and the pipe inlet is placed in the river normal to the flow direction of water to take advantage of the dynamic pressure. The elevation difference between the river and the free surface of the tank is 12 ft. For a flow rate of 1.5 ft3/s and an overall pump efficiency of 75 percent, determine the required electric power input to the pump. The density and dynamic viscosity of water at 70°F are rho = 62.30 lbm/ft3 and μ = 2.360 lbm/ft·h = 6.556 × 10–4 lbm/ft·s. The roughness of a galvanized iron pipe is ε = 0.0005 ft.

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Answer:

Input power given to the pump is 4.09 kw

Explanation:

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The required electric power input to the pump is 3.82 kW

In fluid mechanics, the required electric power input to the pump is the mechanical power taken by the pump shaft and can be calculated by going through the following process.

The first process is to determine the velocity of the water by using the formula:

[tex]\mathbf{V = \dfrac{Q}{A}}[/tex]

where;

  • V = velocity of the water
  • Q = flow rate discharge = 1.5 ft³/s
  • A = area of the pipe

[tex]\mathbf{V = \dfrac{Q}{\dfrac{\pi}{4}\times D^2 }}[/tex]

[tex]\mathbf{V = \dfrac{1.5}{\dfrac{\pi}{4}\times (\dfrac{5}{12})^2 }}[/tex]

V = 11.0 ft/s

The next process is to find the Reynolds number by using the following equation;

[tex]\mathbf{Re= \dfrac{\rho VD}{\mu}}[/tex]

From the parameters given:

  • density [tex]\rho[/tex] = 62.30 lbm/ft³
  • Velocity  V = 11.0 ft/s
  • Diameter of the pipe = 5 inches
  • the viscosity μ = 6.556 × 10⁻⁴ lbm/ft.s

[tex]\mathbf{Re= \dfrac{62.30 \ lbm.ft^3 \times 11.0 \ ft/s \times (\dfrac{5}{12}) ft}{6.556 \times 10^{-4} \ lbm /ft.s}}[/tex]

Re = 435542.5

We will realize that the Reynolds number is greater than 4000, as a result of that, we need to determine the friction factor by using the Colebrook equation which can be expressed as:

[tex]\mathbf{\dfrac{1}{\sqrt{f}} = -2log \Bigg [ \dfrac{\varepsilon/D}{3.7}+ \dfrac{2.51}{Re \sqrt{f}} \Bigg]}[/tex]

From the above equation:

  • The friction factor = f
  • The roughness = ξ = 0
  • Reynolds number Re = 435542.5
  • Diameter of the pipe D = 5/12 ft

[tex]\mathbf{\dfrac{1}{\sqrt{f}} = -2log \Bigg [ \dfrac{0/(5/12)}{3.7}+ \dfrac{2.51}{435542.5 \sqrt{f}} \Bigg]}[/tex]

[tex]\mathbf{\dfrac{1}{\sqrt{f}} = -2log \Bigg [ \dfrac{2.51}{435542.5 \sqrt{f}} \Bigg]}[/tex]

Making friction factor (f) the subject of the formula and solving for (f), we have:

Friction factor f = 0.01349

The next process involves estimating the sum of loss coefficients by using the formula:

[tex]\mathbf{\sum K_L = K_{L. entrance}+3K_{L. elbow}+ K_{L. exit}}[/tex]

For a turbulent flow, using the table of loss coefficients of various pipe parts:

where;

  • L = loss coefficients

[tex]\mathbf{\sum K_L = 0+3(0.3)+1}[/tex]

[tex]\mathbf{\sum K_L = 1.90}[/tex]  

From this, the total head loss [tex]\mathbf{h_L}[/tex] is computed as:

[tex]\mathbf{h_L = \Big[f \dfrac{L}{D} + \sum K_L \Big] \dfrac{V^2}{2g}}[/tex]

[tex]\mathbf{h_L = \Big[0.01349 ( \dfrac{125}{5/12} )+ 1.90 \Big] \dfrac{11.0^2}{2(32.2)}}[/tex]

[tex]\mathbf{h_L = 11.17 \ ft}[/tex]

However, we need to apply Bernoulli's equation to estimate the pump head input because we require the head input to overpower the potential head and velocity loss.

Now, using Bernoulli's equation, we have:

[tex]\mathbf{\dfrac{P_1}{\rho g}+ \dfrac{V_1^2}{2g}+ Z_1 + h_p = \dfrac{P_2}{\rho g} + \dfrac{V_2^2}{2g}+Z_2 + h_L}[/tex]

where;

  • [tex]\mathbf{P_1, V_1,Z_1}[/tex] = pressure, velocity, and height at the inlet of the hose.
  • [tex]\mathbf{P_2, V_2,Z_2}[/tex] = pressure, velocity, and height at the exit of the hose

From above equation, we have:

[tex]\mathbf{\dfrac{P_{atm}}{\rho g}= \dfrac{6}{2 \times 32.2 } + 0 + h_p = \dfrac{P_{atm}}{\rho g} + \dfrac{0^2}{2g} +12 + 11.17 }[/tex]

The head pump input [tex]\mathbf{h_p}[/tex] is:

[tex]\mathbf{h_p = 12 + 11.17 - \dfrac{6^2}{2 \times 32.2}}[/tex]

[tex]\mathbf{h_p = 22.61 ft}[/tex]

Finally, using the formula for calculating the required electric power input to the pump, we have:

[tex]\mathbf{P = \dfrac{\rho \times g \tmes Q h_p}{\eta}}[/tex]

where;

  • The electric power input into the pump = P
  • The gravitational constant = g
  • The discharge rate = Q
  • The efficiency of the pump = η

[tex]\mathbf{P = \dfrac{62.3 \times 32.2 \times 1.5 \times 22.61}{0.75}\times \dfrac{1}{32.2} \times \dfrac{1}{737}}[/tex]

P = 3.82 kW

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