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Fluid Mechanics: Fundamentals and Applications

Yunus Cengel

Chapter 8

FLOW IN PIPES - all with Video Answers

Educators


Chapter Questions

Problem 1

Why are liquids usually transported in circular pipes?

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Problem 2

What is the physical significance of the Reynolds number? How is it defined for (a) flow in a circular pipe of inner diameter $D$ and (b) flow in a rectangular duct of cross section $a \times b$ ?

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Problem 3

Consider a person walking first in air and then in water at the same speed. For which motion will the Reynolds number be higher?

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Problem 4

Show that the Reynolds number for flow in a circular pipe of diameter $D$ can be expressed as $\mathrm{Re}=4 \dot{m} /(\pi D \mu)$.

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Problem 5

Which fluid at room temperature requires a larger pump to flow at a specified velocity in a given pipe: water or engine oil? Why?

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Problem 6

What is the generally accepted value of the Reynolds number above which the flow in smooth pipes is turbulent?

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Problem 7

Consider the flow of air and water in pipes of the same diameter, at the same temperature, and at the same mean velocity. Which flow is more likely to be turbulent? Why?

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Problem 8

What is hydraulic diameter? How is it defined? What is it equal to for a circular pipe of diameter $D$ ?

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Problem 9

How is the hydrodynamic entry length defined for flow in a pipe? Is the entry length longer in laminar or turbulent flow?

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Problem 10

Consider laminar flow in a circular pipe. Will the wall shear stress $\tau_w$ be higher near the inlet of the pipe or near the exit? Why? What would your response be if the flow were turbulent?

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Problem 11

How does surface roughness affect the pressure drop in a pipe if the flow is turbulent? What would your response be if the flow were laminar?

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Problem 12

How does the wall shear stress $\tau_w$ vary along the flow direction in the fully developed region in (a) laminar flow and (b) turbulent flow?

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Problem 13

What fluid property is responsible for the development of the velocity boundary layer? For what kinds of fluids will there be no velocity boundary layer in a pipe?

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Problem 14

In the fully developed region of flow in a circular pipe, will the velocity profile change in the flow direction?

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Problem 15

How is the friction factor for flow in a pipe related to the pressure loss? How is the pressure loss related to the pumping power requirement for a given mass flow rate?

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Problem 16

Someone claims that the shear stress at the center of a circular pipe during fully developed laminar flow is zero. Do you agree with this claim? Explain.

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Problem 17

Someone claims that in fully developed turbulent flow in a pipe, the shear stress is a maximum at the pipe surface. Do you agree with this claim? Explain.

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Problem 18

Consider fully developed flow in a circular pipe with negligible entrance effects. If the length of the pipe is doubled, the head loss will (a) double, (b) more than double, (c) less than double, (d) reduce by half, or (e) remain constant.

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Problem 19

Someone claims that the volume flow rate in a circular pipe with laminar flow can be determined by measuring the velocity at the centerline in the fully developed region, multiplying it by the cross-sectional area, and dividing the result by 2. Do you agree? Explain.

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Problem 20

Someone claims that the average velocity in a circular pipe in fully developed laminar flow can be determined by simply measuring the velocity at $R / 2$ (midway between the wall surface and the centerline). Do you agree? Explain.

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Problem 21

Consider fully developed laminar flow in a circular pipe. If the diameter of the pipe is reduced by half while the flow rate and the pipe length are held constant, the head loss will (a) double, (b) triple, (c) quadruple, (d) increase by a factor of 8 , or (e) increase by a factor of 16.

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Problem 22

What is the physical mechanism that causes the friction factor to be higher in turbulent flow?

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Problem 23

What is turbulent viscosity? What is it caused by?

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Problem 24

The head loss for a certain circular pipe is given by $h_L=0.0826 f L\left(\dot{V}^2 / D^5\right)$, where $f$ is the friction factor (dimensionless), $L$ is the pipe length, $V$ is the volumetric flow rate, and $D$ is the pipe diameter. Determine if the 0.0826 is a dimensional or dimensionless constant. Is this equation dimensionally homogeneous as it stands?

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Problem 25

Consider fully developed laminar flow in a circular pipe. If the viscosity of the fluid is reduced by half by heating while the flow rate is held constant, how will the head loss change?

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Problem 26

How is head loss related to pressure loss? For a given fluid, explain how you would convert head loss to pressure loss.

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Problem 27

Consider laminar flow of air in a circular pipe with perfectly smooth surfaces. Do you think the friction factor for this flow will be zero? Explain.

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Problem 28

Explain why the friction factor is independent of the Reynolds number at very large Reynolds numbers.

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Problem 29

$\mathrm{E}$ Oil at $80^{\circ} \mathrm{F}\left(\rho=56.8 \mathrm{lbm} / \mathrm{ft}^3\right.$ and $\mu=0.0278 \mathrm{lbm} / \mathrm{ft}$ - s) is flowing steadily in a 0.5 -in-diameter, 120 -ft-long pipe. During the flow, the pressure at the pipe inlet and exit is measured to be 120 psi and 14 psi , respectively. Determine the flow rate of oil through the pipe assuming the pipe is (a) horizontal, (b) inclined $20^{\circ}$ upward, and (c) inclined $20^{\circ}$ downward.

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Problem 30

Oil with a density of $850 \mathrm{~kg} / \mathrm{m}^3$ and kinematic viscosity of $0.00062 \mathrm{~m}^2 / \mathrm{s}$ is being discharged by a $5-\mathrm{mm}$-diameter, $40-\mathrm{m}$-long horizontal pipe from a storage tank open to the atmosphere. The height of the liquid level above the center of the pipe is 3 m . Disregarding the minor losses, determine the flow rate of oil through the pipe.
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Problem 31

Water at $10^{\circ} \mathrm{C}\left(\rho=999.7 \mathrm{~kg} / \mathrm{m}^3\right.$ and $\mu=1.307$ $\times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ ) is flowing steadily in a 0.20 -cm-diameter, $15-\mathrm{m}$-long pipe at an average velocity of $1.2 \mathrm{~m} / \mathrm{s}$. Determine (a) the pressure drop, (b) the head loss, and (c) the pumping power requirement to overcome this pressure drop. Answers: (a) 188 kPa , (b) 19.2 m , (c) 0.71 W

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Problem 32

Water at $15^{\circ} \mathrm{C}\left(\rho=999.1 \mathrm{~kg} / \mathrm{m}^3\right.$ and $\mu=1.138$ $\times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ ) is flowing steadily in a $30-\mathrm{m}$-long and $4-\mathrm{cm}$-diameter horizontal pipe made of stainless steel at a rate of $8 \mathrm{~L} / \mathrm{s}$. Determine (a) the pressure drop, (b) the head loss, and (c) the pumping power requirement to overcome this pressure drop.

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Problem 33

Heated air at 1 atm and $100^{\circ} \mathrm{F}$ is to be transported in a 400 - ft -long circular plastic duct at a rate of $12 \mathrm{ft}^3 / \mathrm{s}$. If the head loss in the pipe is not to exceed 50 ft , determine the minimum diameter of the duct.

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Problem 34

In fully developed laminar flow in a circular pipe, the velocity at $R / 2$ (midway between the wall surface and the centerline) is measured to be $6 \mathrm{~m} / \mathrm{s}$. Determine the velocity at the center of the pipe. Answer: $8 \mathrm{~m} / \mathrm{s}$

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Problem 35

The velocity profile in fully developed laminar flow in a circular pipe of inner radius $R=2 \mathrm{~cm}$, in $\mathrm{m} / \mathrm{s}$, is given by $u(r)=4\left(1-r^2 / R^2\right)$. Determine the average and maximum velocities in the pipe and the volume flow rate.

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Problem 36

Repeat Prob. 8-35 for a pipe of inner radius 7 cm .

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Problem 37

Consider an air solar collector that is 1 m wide and 5 m long and has a constant spacing of 3 cm between the glass cover and the collector plate. Air flows at an average temperature of $45^{\circ} \mathrm{C}$ at a rate of $0.15 \mathrm{~m}^3 / \mathrm{s}$ through the $1-\mathrm{m}$-wide edge of the collector along the $5-\mathrm{m}$-long passageway. Disregarding the entrance and roughness effects, determine the pressure drop in the collector. Answer: 29 Pa

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Problem 38

Consider the flow of oil with $\rho=894 \mathrm{~kg} / \mathrm{m}^3$ and $\mu$ $=2.33 \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ in a $40-\mathrm{cm}$-diameter pipeline at an average velocity of $0.5 \mathrm{~m} / \mathrm{s}$. A $300-\mathrm{m}$-long section of the pipeline passes through the icy waters of a lake. Disregarding the entrance effects, determine the pumping power required to overcome the pressure losses and to maintain the flow of oil in the pipe.

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Problem 39

Consider laminar flow of a fluid through a square channel with smooth surfaces. Now the average velocity of the fluid is doubled. Determine the change in the head loss of the fluid. Assume the flow regime remains unchanged.

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Problem 40

Repeat Prob. 8-39 for turbulent flow in smooth pipes for which the friction factor is given as $f=0.184 \mathrm{Re}^{-0.2}$. What would your answer be for fully turbulent flow in a rough pipe?

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Problem 41

Air enters a 7-m-long section of a rectangular duct of cross section $15 \mathrm{~cm} \times 20 \mathrm{~cm}$ made of commercial steel at 1 atm and $35^{\circ} \mathrm{C}$ at an average velocity of $7 \mathrm{~m} / \mathrm{s}$. Disregarding the entrance effects, determine the fan power needed to overcome the pressure losses in this section of the duct. Answer: 4.9 W

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Problem 42

Water at $60^{\circ} \mathrm{F}$ passes through 0.75 -in-internaldiameter copper tubes at a rate of $1.2 \mathrm{lbm} / \mathrm{s}$. Determine the pumping power per ft of pipe length required to maintain this flow at the specified rate.

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Problem 43

Oil with $\rho=876 \mathrm{~kg} / \mathrm{m}^3$ and $\mu=0.24 \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ is flowing through a $1.5-\mathrm{cm}$-diameter pipe that discharges into the atmosphere at 88 kPa . The absolute pressure 15 m before the exit is measured to be 135 kPa . Determine the flow rate of oil through the pipe if the pipe is (a) horizontal, (b) inclined $8^{\circ}$ upward from the horizontal, and (c) inclined $8^{\circ}$ downward from the horizontal.

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Problem 44

Glycerin at $40^{\circ} \mathrm{C}$ with $\rho=1252 \mathrm{~kg} / \mathrm{m}^3$ and $\mu$ $=0.27 \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ is flowing through a $2-\mathrm{cm}$-diameter, $25-\mathrm{m}$ long pipe that discharges into the atmosphere at 100 kPa . The flow rate through the pipe is $0.035 \mathrm{~L} / \mathrm{s}$. (a) Determine the absolute pressure 25 m before the pipe exit. (b) At what angle $\theta$ must the pipe be inclined downward from the horizontal for the pressure in the entire pipe to be atmospheric pressure and the flow rate to be maintained the same?

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Problem 45

In an air heating system, heated air at $40^{\circ} \mathrm{C}$ and 105 kPa absolute is distributed through a $0.2 \mathrm{~m} \times 0.3 \mathrm{~m}$ rectangular duct made of commercial steel at a rate of $0.5 \mathrm{~m}^3 / \mathrm{s}$. Determine the pressure drop and head loss through a $40-\mathrm{m}-$ long section of the duct. Answers: $128 \mathrm{~Pa}, 93.8 \mathrm{~m}$

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Problem 46

Glycerin at $40^{\circ} \mathrm{C}$ with $\rho=1252 \mathrm{~kg} / \mathrm{m}^3$ and $\mu$ $=0.27 \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ is flowing through a $5-\mathrm{cm}$-diameter horizontal smooth pipe with an average velocity of $3.5 \mathrm{~m} / \mathrm{s}$. Determine the pressure drop per 10 m of the pipe.

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Problem 47

Reconsider Prob. 8-46. Using EES (or other) software, investigate the effect of the pipe diameter on the pressure drop for the same constant flow rate. Let the pipe diameter vary from 1 to 10 cm in increments of 1 cm . Tabulate and plot the results, and draw conclusions.

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Problem 48

Air at 1 atm and $60^{\circ} \mathrm{F}$ is flowing through a $1 \mathrm{ft} \times 1 \mathrm{ft}$ square duct made of commercial steel at a rate of 1200 cfm . Determine the pressure drop and head loss per ft of the duct.

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Problem 49

Liquid ammonia at $-20^{\circ} \mathrm{C}$ is flowing through a 30 m -long section of a 5 -mm-diameter copper tube at a rate of $0.15 \mathrm{~kg} / \mathrm{s}$. Determine the pressure drop, the head loss, and the pumping power required to overcome the frictional losses in the tube. Answers: $4792 \mathrm{kPa}, 743 \mathrm{~m}, 1.08 \mathrm{~kW}$

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Problem 50

Shell-and-tube heat exchangers with hundreds of tubes housed in a shell are commonly used in practice for heat transfer between two fluids. Such a heat exchanger used in an active solar hot-water system transfers heat from a water-antifreeze solution flowing through the shell and the solar collector to fresh water flowing through the tubes at an average temperature of $60^{\circ} \mathrm{C}$ at a rate of $15 \mathrm{~L} / \mathrm{s}$. The heat exchanger contains 80 brass tubes 1 cm in inner diameter and 1.5 m in length. Disregarding inlet, exit, and header losses, determine the pressure drop across a single tube and the pumping power required by the tube-side fluid of the heat exchanger.

After operating a long time, 1-mm-thick scale builds up on the inner surfaces with an equivalent roughness of 0.4 mm . For the same pumping power input, determine the percent reduction in the flow rate of water through the tubes.

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Problem 51

What is minor loss in pipe flow? How is the minor loss coefficient $K_L$ defined?

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Problem 52

Define equivalent length for minor loss in pipe flow. How is it related to the minor loss coefficient?

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Problem 53

The effect of rounding of a pipe inlet on the loss coefficient is (a) negligible, (b) somewhat significant, or (c) very significant.

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Problem 54

The effect of rounding of a pipe exit on the loss coefficient is (a) negligible, (b) somewhat significant, or (c) very significant.

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Problem 55

Which has a greater minor loss coefficient during pipe flow: gradual expansion or gradual contraction? Why?

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Problem 56

A piping system involves sharp turns, and thus large minor head losses. One way of reducing the head loss is to replace the sharp turns by circular elbows. What is another way?

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Problem 57

During a retrofitting project of a fluid flow system to reduce the pumping power, it is proposed to install vanes
into the miter elbows or to replace the sharp turns in $90^{\circ}$ miter elbows by smooth curved bends. Which approach will result in a greater reduction in pumping power requirements?

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Problem 58

Water is to be withdrawn from a 3 -m-high water reservoir by drilling a $1.5-\mathrm{cm}$-diameter hole at the bottom surface. Disregarding the effect of the kinetic energy correction factor, determine the flow rate of water through the hole if (a) the entrance of the hole is well-rounded and (b) the entrance is sharp-edged.

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Problem 59

Consider flow from a water reservoir through a circular hole of diameter $D$ at the side wall at a vertical distance $H$ from the free surface. The flow rate through an actual hole with a sharp-edged entrance ( $K_L=0.5$ ) will be considerably less than the flow rate calculated assuming "frictionless" flow and thus zero loss for the hole. Disregarding the effect of the kinetic energy correction factor, obtain a relation for the "equivalent diameter" of the sharp-edged hole for use in frictionless flow relations.

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Problem 60

Repeat Prob. 8-59 for a slightly rounded entrance ( $K_L=0.12$ ).

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Problem 61

A horizontal pipe has an abrupt expansion from $D_1$ $=8 \mathrm{~cm}$ to $D_2=16 \mathrm{~cm}$. The water velocity in the smaller section is $10 \mathrm{~m} / \mathrm{s}$ and the flow is turbulent. The pressure in the smaller section is $P_1=300 \mathrm{kPa}$. Taking the kinetic energy correction factor to be 1.06 at both the inlet and the outlet, determine the downstream pressure $P_2$, and estimate the error that would have occurred if Bernoulli's equation had been used. Answers: $321 \mathrm{kPa}, 28 \mathrm{kPa}$

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Problem 62

A piping system involves two pipes of different diameters (but of identical length, material, and roughness) connected in series. How would you compare the (a) flow rates and (b) pressure drops in these two pipes?

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Problem 63

A piping system involves two pipes of different diameters (but of identical length, material, and roughness) connected in parallel. How would you compare the (a) flow rates and (b) pressure drops in these two pipes?

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Problem 64

A piping system involves two pipes of identical diameters but of different lengths connected in parallel. How would you compare the pressure drops in these two pipes?

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Problem 65

Water is pumped from a large lower reservoir to a higher reservoir. Someone claims that if the head loss is negligible, the required pump head is equal to the elevation difference between the free surfaces of the two reservoirs. Do you agree?

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Problem 66

A piping system equipped with a pump is operating steadily. Explain how the operating point (the flow rate and the head loss) is established.

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Problem 67

For a piping system, define the system curve, the characteristic curve, and the operating point on a head versus flow rate chart.

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Problem 68

Water at $20^{\circ} \mathrm{C}$ is to be pumped from a reservoir $\left(z_A=2 \mathrm{~m}\right)$ to another reservoir at a higher elevation $\left(z_B=9 \mathrm{~m}\right)$ through two 25 -m-long plastic pipes connected in parallel. The diameters of the two pipes are 3 cm and 5 cm . Water is to be pumped by a 68 percent efficient motor-pump unit that draws 7 kW of electric power during operation. The minor losses and the head loss in the pipes that connect the parallel pipes to the two reservoirs are considered to be negligible. Determine the total flow rate between the reservoirs and the flow rates through each of the parallel pipes.

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Problem 69

Water at $70^{\circ} \mathrm{F}$ flows by gravity from a large reservoir at a high elevation to a smaller one through a 120 - ft -long, 2 -in-diameter cast iron piping system that includes four standard flanged elbows, a well-rounded entrance, a sharp-edged exit, and a fully open gate valve. Taking the free surface of the lower reservoir as the reference level, determine the elevation $z_1$ of the higher reservoir for a flow rate of $10 \mathrm{ft}^3 / \mathrm{min}$.
Answer: 23.1 ft

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Problem 70

A 3-m-diameter tank is initially filled with water 2 m above the center of a sharp-edged 10 - cm -diameter orifice. The tank water surface is open to the atmosphere, and the orifice drains to the atmosphere. Neglecting the effect of the kinetic energy correction factor, calculate (a) the initial velocity from the tank and (b) the time required to empty the tank. Does the loss coefficient of the orifice cause a significant increase in the draining time of the tank?

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Problem 71

A 3-m-diameter tank is initially filled with water 2 m above the center of a sharp-edged 10 - cm -diameter orifice. The tank water surface is open to the atmosphere, and the orifice drains to the atmosphere through a $100-\mathrm{m}$-long pipe. The friction coefficient of the pipe can be taken to be 0.015 and the effect of the kinetic energy correction factor can be neglected. Determine (a) the initial velocity from the tank and (b) the time required to empty the tank.

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Problem 72

Reconsider Prob. 8-71. In order to drain the tank faster, a pump is installed near the tank exit. Determine how much pump power input is necessary to establish an average water velocity of $4 \mathrm{~m} / \mathrm{s}$ when the tank is full at $z=2 \mathrm{~m}$. Also, assuming the discharge velocity to remain constant, estimate the time required to drain the tank.

Someone suggests that it makes no difference whether the pump is located at the beginning or at the end of the pipe, and that the performance will be the same in either case, but

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another person argues that placing the pump near the end of the pipe may cause cavitation. The water temperature is $30^{\circ} \mathrm{C}$, so the water vapor pressure is $P_v=4.246 \mathrm{kPa}$ $=0.43 \mathrm{~m}-\mathrm{H}_2 \mathrm{O}$, and the system is located at sea level. Investigate if there is the possibility of cavitation and if we should be concerned about the location of the pump.

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Problem 73

Oil at $20^{\circ} \mathrm{C}$ is flowing through a vertical glass funnel that consists of a $15-\mathrm{cm}$-high cylindrical reservoir and a 1 cm -diameter, $25-\mathrm{cm}$-high pipe. The funnel is always maintained full by the addition of oil from a tank. Assuming the entrance effects to be negligible, determine the flow rate of oil through the funnel and calculate the "funnel effectiveness," which can be defined as the ratio of the actual flow rate through the funnel to the maximum flow rate for the "frictionless" case. Answers: $4.09 \times 10^{-6} \mathrm{~m}^3 / \mathrm{s}, 1.86$ percent

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Problem 74

Repeat Prob. 8-73 assuming (a) the diameter of the pipe is doubled and (b) the length of the pipe is doubled.

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Problem 75

Water at $15^{\circ} \mathrm{C}$ is drained from a large reservoir using two horizontal plastic pipes connected in series. The first pipe is 20 m long and has a $10-\mathrm{cm}$ diameter, while the second pipe is 35 m long and has a $4-\mathrm{cm}$ diameter. The water level in the reservoir is 18 m above the centerline of the pipe. The pipe entrance is sharp-edged, and the contraction between the two pipes is sudden. Neglecting the effect of the kinetic energy correction factor, determine the discharge rate of water from the reservoir.

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Problem 76

A farmer is to pump water at $70^{\circ} \mathrm{F}$ from a river to a water storage tank nearby using a 125 -ft-long, 5 -in-diameter plastic pipe with three flanged $90^{\circ}$ smooth bends. The water velocity near the river surface is $6 \mathrm{ft} / \mathrm{s}$, 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 $1.5 \mathrm{ft}^3 / \mathrm{s}$ and an overall pump efficiency of 70 percent, determine the required electric power input to the pump.

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Problem 77

Reconsider Prob. 8-76E. Using EES (or other) software, investigate the effect of the pipe diameter on the required electric power input to the pump. Let the pipe diameter vary from 1 to 10 in , in increments of 1 in . Tabulate and plot the results, and draw conclusions.

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Problem 78

A water tank filled with solar-heated water at $40^{\circ} \mathrm{C}$ is to be used for showers in a field using gravity-driven flow. The system includes 20 m of $1.5-\mathrm{cm}$-diameter galvanized iron piping with four miter bends $\left(90^{\circ}\right)$ without vanes and a wide-open globe valve. If water is to flow at a rate of $0.7 \mathrm{~L} / \mathrm{s}$ through the shower head, determine how high the water level in the tank must be from the exit level of the shower. Disregard the losses at the entrance and at the shower head, and neglect the effect of the kinetic energy correction factor.

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Problem 79

Two water reservoirs $A$ and $B$ are connected to each other through a $40-\mathrm{m}$-long, $2-\mathrm{cm}$-diameter cast iron pipe with a sharp-edged entrance. The pipe also involves a swing check valve and a fully open gate valve. The water level in both reservoirs is the same, but reservoir $A$ is pressurized by compressed air while reservoir $B$ is open to the atmosphere at 88 kPa . If the initial flow rate through the pipe is $1.2 \mathrm{~L} / \mathrm{s}$, determine the absolute air pressure on top of reservoir $A$. Take the water temperature to be $10^{\circ} \mathrm{C}$. Answer: 733 kPa

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Problem 80

A vented tanker is to be filled with fuel oil with $\rho$ $=920 \mathrm{~kg} / \mathrm{m}^3$ and $\mu=0.045 \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ from an underground reservoir using a $20-\mathrm{m}$-long, $5-\mathrm{cm}$-diameter plastic hose with a slightly rounded entrance and two $90^{\circ}$ smooth bends. The elevation difference between the oil level in the reservoir and the top of the tanker where the hose is discharged is 5 m . The capacity of the tanker is $18 \mathrm{~m}^3$ and the filling time is 30 min . Taking the kinetic energy correction factor at hose discharge to be 1.05 and assuming an overall pump efficiency of 82 percent, determine the required power input to the pump.

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Problem 81

Two pipes of identical length and material are connected in parallel. The diameter of pipe $A$ is twice the diameter of pipe B. Assuming the friction factor to be the same in both cases and disregarding minor losses, determine the ratio of the flow rates in the two pipes.

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Problem 82

A certain part of cast iron piping of a water distribution system involves a parallel section. Both parallel pipes have a diameter of 30 cm , and the flow is fully turbulent. One of the branches (pipe A) is 1000 m long while the other branch (pipe $B$ ) is 3000 m long. If the flow rate through pipe $A$ is $0.4 \mathrm{~m}^3 / \mathrm{s}$, determine the flow rate through pipe $B$. Disregard minor losses and assume the water temperature to be $15^{\circ} \mathrm{C}$. Show that the flow is fully turbulent, and thus the friction factor is independent of Reynolds number. Answer: $0.231 \mathrm{~m}^3 / \mathrm{s}$

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Problem 83

Repeat Prob. 8-82 assuming pipe $A$ has a halfwayclosed gate valve ( $K_L=2.1$ ) while pipe $B$ has a fully open globe valve ( $K_L=10$ ), and the other minor losses are negligible. Assume the flow to be fully turbulent.

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Problem 84

A geothermal district heating system involves the transport of geothermal water at $110^{\circ} \mathrm{C}$ from a geothermal well to a city at about the same elevation for a distance of 12 km at a rate of $1.5 \mathrm{~m}^3 / \mathrm{s}$ in $60-\mathrm{cm}$-diameter stainless-steel pipes. The fluid pressures at the wellhead and the arrival point in the city are to be the same. The minor losses are neg-
ligible because of the large length-to-diameter ratio and the relatively small number of components that cause minor losses. (a) Assuming the pump-motor efficiency to be 74 percent, determine the electric power consumption of the system for pumping. Would you recommend the use of a single large pump or several smaller pumps of the same total pumping power scattered along the pipeline? Explain. (b) Determine the daily cost of power consumption of the system if the unit cost of electricity is $\$ 0.06 / \mathrm{kWh}$. (c) The temperature of geothermal water is estimated to drop $0.5^{\circ} \mathrm{C}$ during this long flow. Determine if the frictional heating during flow can make up for this drop in temperature.

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Problem 85

Repeat Prob. 8-84 for cast iron pipes of the same diameter.

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Problem 86

A clothes dryer discharges air at 1 atm and $120^{\circ} \mathrm{F}$ at a rate of $1.2 \mathrm{ft}^3 / \mathrm{s}$ when its 5 -in-diameter, well-rounded vent with negligible loss is not connected to any duct. Determine the flow rate when the vent is connected to a 15 -ft-long, 5 -indiameter duct made of galvanized iron, with three $90^{\circ}$ flanged smooth bends. Take the friction factor of the duct to be 0.019 , and assume the fan power input to remain constant.
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Problem 87

In large buildings, hot water in a water tank is circulated through a loop so that the user doesn't have to wait for all the water in long piping to drain before hot water starts coming out. A certain recirculating loop involves 40 -m-long, $1.2-\mathrm{cm}$-diameter cast iron pipes with six $90^{\circ}$ threaded smooth bends and two fully open gate valves. If the average flow velocity through the loop is $2.5 \mathrm{~m} / \mathrm{s}$, determine the required power input for the recirculating pump. Take the average water temperature to be $60^{\circ} \mathrm{C}$ and the efficiency of the pump to be 70 percent. Answer: 0.217 kW

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Problem 88

Reconsider Prob. 8-87. Using EES (or other) software, investigate the effect of the average flow velocity on the power input to the recirculating pump. Let the velocity vary from 0 to $3 \mathrm{~m} / \mathrm{s}$ in increments of $0.3 \mathrm{~m} / \mathrm{s}$. Tabulate and plot the results.

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Problem 89

Repeat Prob. 8-87 for plastic pipes.

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Problem 90

What are the primary considerations when selecting a flowmeter to measure the flow rate of a fluid?

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Problem 91

Explain how flow rate is measured with a Pitot-static tube, and discuss its advantages and disadvantages with respect to cost, pressure drop, reliability, and accuracy.

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Problem 92

Explain how flow rate is measured with obstructiontype flowmeters. Compare orifice meters, flow nozzles, and Venturi meters with respect to cost, size, head loss, and accuracy.

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Problem 93

How do positive displacement flowmeters operate? Why are they commonly used to meter gasoline, water, and natural gas?

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Problem 94

Explain how flow rate is measured with a turbine flowmeter, and discuss how they compare to other types of flowmeters with respect to cost, head loss, and accuracy.

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Problem 95

What is the operating principle of variable-area flowmeters (rotameters)? How do they compare to other types of flowmeters with respect to cost, head loss, and reliability?

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Problem 96

What is the difference between the operating principles of thermal and laser Doppler anemometers?

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Problem 97

What is the difference between laser Doppler velocimetry (LDV) and particle image velocimetry (PIV)?

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Problem 98

The flow rate of ammonia at $10^{\circ} \mathrm{C}\left(\rho=624.6 \mathrm{~kg} / \mathrm{m}^3\right.$ and $\mu=1.697 \times 10^{-4} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ ) through a 3 -cm-diameter pipe is to be measured with a 1.5 -cm-diameter flow nozzle equipped with a differential pressure gage. If the gage reads a pressure differential of 4 kPa , determine the flow rate of ammonia through the pipe, and the average flow velocity.

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Problem 99

The flow rate of water through a $10-\mathrm{cm}$-diameter pipe is to be determined by measuring the water velocity at several locations along a cross section. For the set of measurements given in the table, determine the flow rate.
$$
\begin{array}{cc}
\hline r, \mathrm{~cm} & V, \mathrm{~m} / \mathrm{s} \\
\hline 0 & 6.4 \\
1 & 6.1 \\
2 & 5.2 \\
3 & 4.4 \\
4 & 2.0 \\
5 & 0.0 \\
\hline
\end{array}
$$

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Problem 100

An orifice with a 2 -in-diameter opening is used to measure the mass flow rate of water at $60^{\circ} \mathrm{F}\left(\rho=62.36 \mathrm{lbm} / \mathrm{ft}^3\right.$ and $\left.\mu=7.536 \times 10^{-4} \mathrm{lbm} / \mathrm{ft} \cdot \mathrm{s}\right)$ through a horizontal 4-in-diameter pipe. A mercury manometer is used to measure the pressure difference across the orifice. If the differential height of the manometer is read to be 6 in , determine the volume flow rate of water through the pipe, the average velocity, and the head loss caused by the orifice meter.

Figure Can't Copy

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Problem 101

Repeat Prob. 8-100E for a differential height of 9 in.

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Problem 102

The flow rate of water at $20^{\circ} \mathrm{C}\left(\rho=998 \mathrm{~kg} / \mathrm{m}^3\right.$ and $\mu=1.002 \times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ ) through a 50 -cm-diameter pipe is measured with an orifice meter with a $30-\mathrm{cm}$-diameter opening to be $250 \mathrm{~L} / \mathrm{s}$. Determine the pressure difference indicated by the orifice meter and the head loss.

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Problem 103

A Venturi meter equipped with a differential pressure gage is used to measure the flow rate of water at $15^{\circ} \mathrm{C}$ ( $\rho=999.1 \mathrm{~kg} / \mathrm{m}^3$ ) through a $5-\mathrm{cm}$-diameter horizontal pipe. The diameter of the Venturi neck is 3 cm , and the measured pressure drop is 5 kPa . Taking the discharge coefficient to be 0.98 , determine the volume flow rate of water and the average velocity through the pipe. Answers: $2.35 \mathrm{~L} / \mathrm{s}$ and $1.20 \mathrm{~m} / \mathrm{s}$
Figure Can't Copy

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Problem 104

Reconsider Prob. 8-103. Letting the pressure drop vary from 1 kPa to 10 kPa , evaluate the flow rate at intervals of 1 kPa , and plot it against the pressure drop.

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Problem 105

The mass flow rate of air at $20^{\circ} \mathrm{C}\left(\rho=1.204 \mathrm{~kg} / \mathrm{m}^3\right)$ through a 15 -cm-diameter duct is measured with a Venturi meter equipped with a water manometer. The Venturi neck has a diameter of 6 cm , and the manometer has a maximum differential height of 40 cm . Taking the discharge coefficient to be 0.98 , determine the maximum mass flow rate of air this Venturi meter can measure. Answer: $0.273 \mathrm{~kg} / \mathrm{s}$

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Problem 106

Repeat Prob. 8-105 for a Venturi neck diameter of 7.5 cm .

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Problem 107

A vertical Venturi meter equipped with a differential pressure gage shown in Fig. P8-107 is used to measure the
flow rate of liquid propane at $10^{\circ} \mathrm{C}\left(\rho=514.7 \mathrm{~kg} / \mathrm{m}^3\right)$ through an $8-\mathrm{cm}$-diameter vertical pipe. For a discharge coefficient of 0.98 , determine the volume flow rate of propane through the pipe.

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Problem 108

A flow nozzle equipped with a differential pressure gage is used to measure the flow rate of water at $10^{\circ} \mathrm{C}$ ( $\rho$ $=999.7 \mathrm{~kg} / \mathrm{m}^3$ and $\mu=1.307 \times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ ) through a $3-$ cm -diameter horizontal pipe. The nozzle exit diameter is 1.5 cm , and the measured pressure drop is 3 kPa . Determine the volume flow rate of water, the average velocity through the pipe, and the head loss.

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Problem 109

A 16-L kerosene tank ( $\rho=820 \mathrm{~kg} / \mathrm{m}^3$ ) is filled with a 2 -cm-diameter hose equipped with a 1.5 -cm-diameter nozzle meter. If it takes 20 s to fill the tank, determine the pressure difference indicated by the nozzle meter.

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Problem 110

The flow rate of water at $20^{\circ} \mathrm{C}\left(\rho=998 \mathrm{~kg} / \mathrm{m}^3\right.$ and $\mu=1.002 \times 10^{-3} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}$ ) through a 4 - cm -diameter pipe is measured with a 2 -cm-diameter nozzle meter equipped with an inverted air-water manometer. If the manometer indicates a differential water height of 32 cm , determine the volume flow rate of water and the head loss caused by the nozzle meter.

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Problem 111

The volume flow rate of liquid refrigerant-134a at $10^{\circ} \mathrm{F}\left(\rho=83.31 \mathrm{lbm} / \mathrm{ft}^3\right)$ is to be measured with a horizontal Venturi meter with a diameter of 5 in at the inlet and 2 in at the throat. If a differential pressure meter indicates a pressure drop of 7.4 psi , determine the flow rate of the refrigerant. Take the discharge coefficient of the Venturi meter to be 0.98 .

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Problem 112

The compressed air requirements of a manufacturing facility are met by a 150 -hp compressor that draws in air from the outside through an $8-\mathrm{m}$-long, $20-\mathrm{cm}$-diameter duct made of thin galvanized iron sheets. The compressor takes in air at a rate of $0.27 \mathrm{~m}^3 / \mathrm{s}$ at the outdoor conditions of $15^{\circ} \mathrm{C}$ and 95 kPa . Disregarding any minor losses, determine the useful power used by the compressor to overcome the frictional losses in this duct. Answer: 9.66 W

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Problem 113

A house built on a riverside is to be cooled in summer by utilizing the cool water of the river. A $15-\mathrm{m}$-long sec-
tion of a circular stainless-steel duct of $20-\mathrm{cm}$ diameter passes through the water. Air flows through the underwater section of the duct at $3 \mathrm{~m} / \mathrm{s}$ at an average temperature of $15^{\circ} \mathrm{C}$. For an overall fan efficiency of 62 percent, determine the fan power needed to overcome the flow resistance in this section of the duct.

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Problem 114

The velocity profile in fully developed laminar flow in a circular pipe, in $\mathrm{m} / \mathrm{s}$, is given by $u(r)=6\left(1-100 r^2\right)$, where $r$ is the radial distance from the centerline of the pipe in m . Determine (a) the radius of the pipe, (b) the average velocity through the pipe, and (c) the maximum velocity in the pipe.

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Problem 115

The velocity profile in a fully developed laminar flow of water at $40^{\circ} \mathrm{F}$ in a 80 -ft-long horizontal circular pipe, in $\mathrm{ft} / \mathrm{s}$, is given by $u(r)=0.8\left(1-625 r^2\right)$, where $r$ is the radial distance from the centerline of the pipe in ft . Determine (a) the volume flow rate of water through the pipe, (b) the pressure drop across the pipe, and (c) the useful pumping power required to overcome this pressure drop.

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Problem 116

Repeat Prob. 8-115E assuming the pipe is inclined $12^{\circ}$ from the horizontal and the flow is uphill.

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Problem 117

Consider flow from a reservoir through a horizontal pipe of length $L$ and diameter $D$ that penetrates into the side wall at a vertical distance $H$ from the free surface. The flow rate through an actual pipe with a reentrant section ( $K_L$ $=0.8$ ) will be considerably less than the flow rate through the hole calculated assuming "frictionless" flow and thus zero loss. Obtain a relation for the "equivalent diameter" of the reentrant pipe for use in relations for frictionless flow through a hole and determine its value for a pipe friction factor, length, and diameter of $0.018,10 \mathrm{~m}$, and 0.04 m , respectively. Assume the friction factor of the pipe to remain constant and the effect of the kinetic energy correction factor to be negligible.

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Problem 118

Water is to be withdrawn from a $5-\mathrm{m}$-high water reservoir by drilling a well-rounded 3-cm-diameter hole with negligible loss at the bottom surface and attaching a horizontal $90^{\circ}$ bend of negligible length. Taking the kinetic energy correction factor to be 1.05 , determine the flow rate of water through the bend if (a) the bend is a flanged smooth bend and (b) the bend is a miter bend without vanes.

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Problem 119

In a geothermal district heating system, 10,000 $\mathrm{kg} / \mathrm{s}$ of hot water must be delivered a distance of 10 km in a horizontal pipe. The minor losses are negligible, and the only significant energy loss will arise from pipe friction. The friction factor can be taken to be 0.015 . Specifying a larger-diameter pipe would reduce water velocity, velocity head, pipe friction, and thus power consumption. But a larger pipe would also cost more money initially to purchase and install. Otherwise stated, there is an optimum pipe diameter that will minimize the sum of pipe cost and future electric power cost.

Assume the system will run $24 \mathrm{~h} /$ day, every day, for 30 years. During this time the cost of electricity will remain constant at $\$ 0.06 / \mathrm{kWh}$. Assume system performance stays constant over the decades (this may not be true, especially if highly mineralized water is passed through the pipelinescale may form). The pump has an overall efficiency of 80 percent. The cost to purchase, install, and insulate a $10-\mathrm{km}$ pipe depends on the diameter $D$ and is given by Cost $=\$ 10^6 D^2$, where $D$ is in m . Assuming zero inflation and interest rate for simplicity and zero salvage value and zero maintenance cost, determine the optimum pipe diameter.

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Problem 120

Water at $15^{\circ} \mathrm{C}$ is to be discharged from a reservoir at a rate of $18 \mathrm{~L} / \mathrm{s}$ using two horizontal cast iron pipes connected in series and a pump between them. The first pipe is 20 m long and has a $6-\mathrm{cm}$ diameter, while the second pipe is 35 m long and has a $4-\mathrm{cm}$ diameter. The water level in the reservoir is 30 m above the centerline of the pipe. The pipe entrance is sharp-edged, and losses associated with the connection of the pump are negligible. Neglecting the effect of the kinetic energy correction factor, determine the required pumping head and the minimum pumping power to maintain the indicated flow rate.

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Problem 121

Reconsider Prob. 8-120. Using EES (or other) software, investigate the effect of the second pipe diameter on the required pumping head to maintain the
indicated flow rate. Let the diameter vary from 1 to 10 cm in increments of 1 cm . Tabulate and plot the results.

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Problem 122

Two pipes of identical diameter and material are connected in parallel. The length of pipe $A$ is twice the length of pipe $B$. Assuming the flow is fully turbulent in both pipes and thus the friction factor is independent of the Reynolds number and disregarding minor losses, determine the ratio of the flow rates in the two pipes.

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Problem 123

A pipeline that transports oil at $40^{\circ} \mathrm{C}$ at a rate of $3 \mathrm{~m}^3 / \mathrm{s}$ branches out into two parallel pipes made of commercial steel that reconnect downstream. Pipe A is 500 m long and has a diameter of 30 cm while pipe $B$ is 800 m long and has a diameter of 45 cm . The minor losses are considered to be negligible. Determine the flow rate through each of the parallel pipes.

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Problem 124

Repeat Prob. 8-123 for hot-water flow of a district heating system at $100^{\circ} \mathrm{C}$.

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Problem 125

A water fountain is to be installed at a remote location by attaching a cast iron pipe directly to a water main through which water is flowing at $70^{\circ} \mathrm{F}$ and 60 psig . The entrance to the pipe is sharp-edged, and the 50 -ft-long piping system involves three $90^{\circ}$ miter bends without vanes, a fully open gate valve, and an angle valve with a loss coefficient of 5 when fully open. If the system is to provide water at a rate of $20 \mathrm{gal} / \mathrm{min}$ and the elevation difference between the pipe and the fountain is negligible, determine the minimum diameter of the piping system.

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Problem 126

Repeat Prob. 8-125E for plastic pipes.

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Problem 127

In a hydroelectric power plant, water at $20^{\circ} \mathrm{C}$ is supplied to the turbine at a rate of $0.8 \mathrm{~m}^3 / \mathrm{s}$ through a $200-\mathrm{m}$ long, $0.35-\mathrm{m}$-diameter cast iron pipe. The elevation difference between the free surface of the reservoir and the turbine discharge is 70 m , and the combined turbine-generator efficiency is 84 percent. Disregarding the minor losses because of the large length-to-diameter ratio, determine the electric power output of this plant.

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Problem 128

In Prob. 8-127, the pipe diameter is tripled in order to reduce the pipe losses. Determine the percent increase in the net power output as a result of this modification.

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Problem 129

The drinking water needs of an office are met by large water bottles. One end of a 0.35 -in-diameter, 6 - ft -long plastic hose is inserted into the bottle placed on a high stand, while the other end with an on/off valve is maintained 3 ft below the bottom of the bottle. If the water level in the bottle is 1 ft when it is full, determine how long it will take to fill an $8-\mathrm{oz}$ glass ( $=0.00835 \mathrm{ft}^3$ ) (a) when the bottle is first opened and (b) when the bottle is almost empty. Take the total minor loss coefficient, including the on/off valve, to be 2.8 when it is fully open. Assume the water temperature to be the same as the room temperature of $70^{\circ} \mathrm{F}$.

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Problem 130

Reconsider Prob. 8-129E. Using EES (or other) software, investigate the effect of the hose diameter on the time required to fill a glass when the bottle is full. Let the diameter vary from 0.2 to 2 in , in increments of 0.2 in . Tabulate and plot the results.

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Problem 131

Reconsider Prob. 8-129E. The office worker who set up the siphoning system purchased a $12-\mathrm{ft}$-long reel of the plastic tube and wanted to use the whole thing to avoid cutting it in pieces, thinking that it is the elevation difference that makes siphoning work, and the length of the tube is not
important. So he used the entire 12 -ft-long tube. Assuming the turns or constrictions in the tube are not significant (being very optimistic) and the same elevation is maintained, determine the time it takes to fill a glass of water for both cases.

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Problem 132

A circular water pipe has an abrupt expansion from diameter $D_1=15 \mathrm{~cm}$ to $D_2=20 \mathrm{~cm}$. The pressure and the average water velocity in the smaller pipe are $P_1=120 \mathrm{kPa}$ and $10 \mathrm{~m} / \mathrm{s}$, respectively, and the flow is turbulent. By applying the continuity, momentum, and energy equations and disregarding the effects of the kinetic energy and momentumflux correction factors, show that the loss coefficient for sudden expansion is $K_L=\left(1-D_1^2 / D_2^2\right)^2$, and calculate $K_L$ and $P_2$ for the given case.

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Problem 133

The water at $20^{\circ} \mathrm{C}$ in a 10 -m-diameter, 2 -m-high aboveground swimming pool is to be emptied by unplugging a $3-\mathrm{cm}$-diameter, $25-\mathrm{m}$-long horizontal plastic pipe attached to the bottom of the pool. Determine the initial rate of discharge of water through the pipe and the time it will take to empty the swimming pool completely assuming the entrance to the pipe is well-rounded with negligible loss. Take the friction factor of the pipe to be 0.022 . Using the initial discharge velocity, check if this is a reasonable value for the friction factor.

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Problem 134

Reconsider Prob. 8-133. Using EES (or other) software, investigate the effect of the discharge pipe diameter on the time required to empty the pool completely. Let the diameter vary from 1 to 10 cm , in increments of 1 cm . Tabulate and plot the results.

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Problem 135

Repeat Prob. 8-133 for a sharp-edged entrance to the pipe with $K_L=0.5$. Is this "minor loss" truly "minor" or not?

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Problem 136

A system that consists of two interconnected cylindrical tanks with $D_1=30 \mathrm{~cm}$ and $D_2=12 \mathrm{~cm}$ is to be used to determine the discharge coefficient of a short $D_0=5 \mathrm{~mm}$ diameter orifice. At the beginning ( $t=0 \mathrm{~s}$ ), the fluid heights in the tanks are $h_1=50 \mathrm{~cm}$ and $h_2=15 \mathrm{~cm}$, as shown in Fig. P8-136. If it takes 170 s for the fluid levels in the two tanks to equalize and the flow to stop, determine the discharge coefficient of the orifice. Disregard any other losses associated with this flow.

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Problem 137

A highly viscous liquid discharges from a large container through a small-diameter tube in laminar flow. Disre-

garding entrance effects and velocity heads, obtain a relation for the variation of fluid depth in the tank with time.

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Problem 138

A student is to determine the kinematic viscosity of an oil using the system shown in Prob. 8-137. The initial fluid height in the tank is $H=40 \mathrm{~cm}$, the tube diameter is $d$ $=6 \mathrm{~mm}$, the tube length is $L=0.65 \mathrm{~m}$, and the tank diameter is $D=0.63 \mathrm{~m}$. The student observes that it takes 2842 s for the fluid level in the tank to drop to 36 cm . Find the fluid viscosity.

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Problem 139

Electronic boxes such as computers are commonly cooled by a fan. Write an essay on forced air cooling of electronic boxes and on the selection of the fan for electronic devices.

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Problem 140

Design an experiment to measure the viscosity of liquids using a vertical funnel with a cylindrical reservoir of height $h$ and a narrow flow section of diameter $D$ and length L. Making appropriate assumptions, obtain a relation for viscosity in terms of easily measurable quantities such as density and volume flow rate. Is there a need for the use of a correction factor?

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Problem 141

A pump is to be selected for a waterfall in a garden. The water collects in a pond at the bottom, and the elevation difference between the free surface of the pond and the location where the water is discharged is 3 m . The flow rate of water is to be at least $8 \mathrm{~L} / \mathrm{s}$. Select an appropriate motorpump unit for this job and identify three manufacturers with product model numbers and prices. Make a selection and explain why you selected that particular product. Also estimate the cost of annual power consumption of this unit assuming continuous operation.

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Problem 142

During a camping trip you notice that water is discharged from a high reservoir to a stream in the valley through a 30 -cm-diameter plastic pipe. The elevation difference between the free surface of the reservoir and the stream is 70 m . You conceive the idea of generating power from this water. Design a power plant that will produce the most power from this resource. Also, investigate the effect of power generation on the discharge rate of water. What discharge rate will maximize the power production?

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