Question 4.22: A pump is required to dewater a site as illustrated in Figur...

A pump is required to dewater a site as illustrated in Figure EP 4.22. It is required that the water (at 20^{◦} C) be pumped from reservoir 1 to reservoir 2 to an elevation of 150 m at a discharge of 0.45 m^{3}/sec. Assume that the total head loss due to both major (pipe friction) and minor losses (pipe components) is 0.7 m between points 1 and the suction side of the pump at points and 1.2 m between the discharge side of the pump at pointd and point 2. (a) Determine the maximum height, z_{s} to which the fluid may be pumped; otherwise, there will be no flow in the suction line at the suction side of the pump. (b) Determine the maximum allowable velocity of the flow in the pipe without causing cavitation. (c) Determine the minimum required design pipe size diameter in order to accommodate the maximum allowable velocity and the required flowrate. (d) Determine the required head to be delivered by the pump. (e) Determine the required hydraulic power output from the pump. (f) Assuming a typical pump efficiency of 80%, determine the required shaft power input to the pump by the motor. (g) Assuming a typical motor efficiency of 85%, determine the required chemical or electric power input to the motor. (h) Determine the resulting overall pump–motor system efficiency.

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(a) Assuming the datum is at point 1, to determine the maximum height, z_{s} to which the fluid may be pumped (in order to establish a flow in the suction line), the energy equation is applied between points 1 and s, assuming a vapor pressure, P_{V} of the liquid at point s in order to avoid cavitation, and assuming no flow in the suction line as follows:

Z_{1}: = 0m                   P_{1}:= 0 \frac{N}{m^{2}}                   V_{1}: = 0 \frac{m}{sec}                   V_{s}: = 0 \frac{m}{sec}
P_{V}:= 2.34 \times 10^{3} \frac{N}{m^{2}} \times 10^{3} \frac{N}{m^{2}} = -9.899 \times 10^{4} \frac{N}{m^{2}}
P_{s}:= P_{V} = -9.899 \times 10^{4} \frac{N}{m^{2}}                   h_{ftotal1s}: = 0.7 m
\rho : = 998 \frac{kg}{m^{3}}                   g: = 9.81 \frac{m}{sec^{2}}                   \gamma : = \rho .g = 9.79 \times 10^{3} \frac{kg}{m^{2}s^{2}}

Guess value:                   Z_{s}: = 9 m

Given

\frac{P_{1}}{\gamma } + Z_{1} + \frac{V^{2}_{1} }{2.g} – h_{ftotal1s} = \frac{P_{s}}{\gamma } + Z_{s} + \frac{V^{2}_{s} }{2.g}
Z_{s}: Find ( Z_{s}) = 9.41 m

However, in order to establish a nonzero flow in the suction line, the maximum height, z_{s} to which the fluid may be pumped will be set at z_{s} = 9 m .
(b) In order to determine the maximum allowable velocity of the flow in the pipe without causing cavitation at the suction side, s of the pump, the energy equation is applied between points 1 and s, assuming that the pressure at point s is the vapor pressure of the water at 20^{◦} C as follows:

Z_{s}: = 9 m

Guess value:                  V_{s}: = 1 \frac{m}{sec}

Given

\frac{P_{1}}{\gamma } + Z_{1} + \frac{V^{2}_{1} }{2.g} – h_{ftotal1s} = \frac{P_{s}}{\gamma } + Z_{s} + \frac{V^{2}_{s} }{2.g}
V_{s}: Find ( V_{s}) = 2.838 \frac{m}{s}

(c) To determine the minimum required design pipe size diameter in order to accommodate the maximum allowable velocity and the required flowrate, the continuity equation is applied as follows:

Q: = 0.45 \frac{m^{3}}{sec}

Guess value:                    D:= 1 m                       A: = 1 m^{2}

Given

Q = V_{s}.A
A= \frac{\pi .D^{2}}{4}
\left ( \begin{matrix} D \\ A \end{matrix} \right ) : = Find (D, A)
D = 0.449 m                         A: = 0.159 m^{2}

(d) The required head to be delivered by the pump is determined by applying the energy equation between points 1 and 2 as follows:

P_{2}: = 0 \frac{N}{m^{2}}                         V_{2}: = 0 \frac{m}{sec}                         Z_{2}: = 150 m
h_{ftotal1s}: = 0.7 m                         h_{ftotalds}: = 1.2 m

Guess value:                        h_{pump}: = 200 m

\frac{P_{1}}{\gamma } + Z_{1} + \frac{V^{2}_{1} }{2.g} – h_{ftotal1s} – h_{ftotalds} = \frac{P_{2}}{\gamma } + Z_{2} + \frac{V^{2}_{2} }{2.g}
h_{pump}: Find ( h_{pump}) = 151.9 m

Thus, the required head to be delivered by the pump, h_{pump} = 151.9 m must overcome the difference in elevation between the two reservoirs, Δz= 150 m and the total head loss due to pipe friction and pipe components between points 1 and 2, h_{f,total} = 0.7 m + 1.2 m = 1.9 m.
(e) The required hydraulic power output from the pump is computed by applying Equation 4.186 h_{pump} = \frac{(P_{p})_{out}}{\gamma Q} = \frac{(\eta _{pump})(P_{p})_{in}}{\gamma Q} = \frac{(\eta _{pump})(w T_{shaft,in})}{\gamma Q} as follows:

P_{pout}: = \gamma .Q. h_{pump} = 669.221 kW

(f) Assuming a typical pump efficiency of 80%, the required shaft power input to the pump by the motor is computed by applying Equation 4.165 \eta _{pump} = \frac{hydraulic power}{shaft power} = \frac{(\overset{\cdot }{W} _{pump})_{u}}{\overset{\cdot }{W} _{pump}} = \frac{(\overset{\cdot }{W} _{pump})_{u}}{\overset{\cdot }{W} _{shaft,in}} = \frac{(\overset{\cdot }{W} _{pump})_{u}}{wT _{shaft,in}} = \frac{(P_{p})_{out}}{(P_{p})_{in}} as follows:

\eta _{pump}: = 0.80

Guess value:                      P_{pin}: = 700 kW

Given

\eta _{pump} = \frac{P_{pout}}{P_{pin}}
P_{pin}: = Find ( P_{pin})= 836.527 kW

(g) Assuming a typical motor efficiency of 85%, the required chemical or electric power input to the motor is computed by applying Equation 4.169 \eta _{motor} = \frac{shaft power output from motor}{electric power input from electical source} =\frac{W_{shaft,out}}{W_{elect,in}} = \frac{P_{out of motor}}{P_{in of motor}} = \frac{(P_{m})_{out}}{(P_{m})_{in}} as follows:

P_{mout}: = P_{pin} = 836.527 kW                     \eta _{motor}: = 0.85

Guess value:                    P_{min}: = 800 kW

\eta _{motor} = \frac{P_{mout}}{P_{min}}
P_{min}: = Find (P_{min}) = 984.149 kW

(h) The resulting overall pump–motor system efficiency is computed by applying Equation 4.172 \eta _{pump – motor}= \frac{hydraulic power}{electric power} = \frac{(\overset{\cdot }{W_{pump}} )_{u}}{\overset{\cdot }{W_{elect,in}}} = \frac{(P_{p})_{out}}{(P_{p})_{in}} = \eta _{pump}\eta _{motor} as follows:

\eta _{pumpmotor}: = \frac{P_{pout}}{P_{min}} = 0.68                             \eta _{pumpmotor}: = \eta _{pump}. \eta _{motor} = 0.68

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