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Fundamentals of Heat and Mass Transfer

Theodore L. Bergman, Adrienne S. Lavine, Frank P. Incropera

Chapter 1

Introduction - all with Video Answers

Educators


Chapter Questions

04:05

Problem 1

The thermal conductivity of a sheet of rigid, extruded insulation is reported to be $k=0.029 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The measured temperature difference across a 20 -mm-thick sheet of the material is $T_{1}-T_{2}=10^{\circ} \mathrm{C}$.
(a) What is the heat flux through a $2 \mathrm{~m} \times 2 \mathrm{~m}$ sheet of the insulation?
(b) What is the rate of heat transfer through the sheet of insulation?

Surjit Tewari
Surjit Tewari
Numerade Educator
02:20

Problem 2

The heat flux that is applied to the left face of a plane wall is $q^{\prime \prime}=20 \mathrm{~W} / \mathrm{m}^{2}$. The wall is of thickness $L=10$ $\mathrm{mm}$ and of thermal conductivity $k=12 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. If the surface temperatures of the wall are measured to be $50^{\circ} \mathrm{C}$ on the left side and $30^{\circ} \mathrm{C}$ on the right side, do steady-state conditions exist?

Anand Jangid
Anand Jangid
Numerade Educator
04:02

Problem 3

A concrete wall, which has a surface area of $20 \mathrm{~m}^{2}$ and is $0.30 \mathrm{~m}$ thick, separates conditioned room air from ambient air. The temperature of the inner surface of the wall is maintained at $25^{\circ} \mathrm{C}$, and the thermal conductivity of the concrete is $1 \mathrm{~W} / \mathrm{m}=\mathrm{K}$.
(a) Determine the heat loss through the wall for outer surface temperatures ranging from $-15^{\circ} \mathrm{C}$ to $38^{\circ} \mathrm{C}$, which correspond to winter and summer extremes, respectively. Display your results graphically.
(b) On your graph, also plot the heat loss as a function of the outer surface temperature for wall materials having thermal conductivities of $0.75$ and $1.25 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Explain the family of curves you have obtained.

Satpal Satpal
Satpal Satpal
Numerade Educator
01:06

Problem 4

The concrete slab of a basement is $11 \mathrm{~m}$ long, $8 \mathrm{~m}$ wide, and $0.20 \mathrm{~m}$ thick. During the winter, temperatures are nominally $17^{\circ} \mathrm{C}$ and $10^{\circ} \mathrm{C}$ at the top and bottom surfaces, respectively. If the concrete has a thermal conductivity of $1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, what is the rate of heat loss through the slab? If the basement is heated by a gas furnace operating at an efficiency of $\eta_{f}=0.90$ and natural gas is priced at $C_{g}=\$ 0.02 / \mathrm{MJ}$, what is the daily cost of the heat loss?

Dading Chen
Dading Chen
Numerade Educator
02:20

Problem 5

Consider Figure 1.3. The heat flux in the $x$-direction is $q_{x}^{\prime \prime}=10 \mathrm{~W} / \mathrm{m}^{2}$, the thermal conductivity and wall thickness are $k=2.3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$ and $L=20 \mathrm{~mm}$, respectively, and steady-state conditions exist. Determine the value of the temperature gradient in units of $\mathrm{K} / \mathrm{m}$. What is the value of the temperature gradient in units of ${ }^{\circ} \mathrm{C} / \mathrm{m}$ ?

Anand Jangid
Anand Jangid
Numerade Educator
01:39

Problem 6

The heat flux through a wood slab $50 \mathrm{~mm}$ thick, whose inner and outer surface temperatures are 40 and $20^{\circ} \mathrm{C}$, respectively, has been determined to be $40 \mathrm{~W} / \mathrm{m}^{2}$. What is the thermal conductivity of the wood?

Penny Riley
Penny Riley
Numerade Educator
01:53

Problem 7

The inner and outer surface temperatures of a glass window $5 \mathrm{~mm}$ thick are 15 and $5^{\circ} \mathrm{C}$. What is the heat loss through a $1 \mathrm{~m} \times 3 \mathrm{~m}$ window? The thermal conductivity of glass is $1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$.

Mayukh Banik
Mayukh Banik
Numerade Educator
03:25

Problem 8

A thermodynamic analysis of a proposed Brayton cycle gas turbine yields $P=5 \mathrm{MW}$ of net power production. The compressor, at an average temperature of $T_{c}=400^{\circ} \mathrm{C}$, is driven by the turbine at an average temperature of $T_{h}=1000^{\circ} \mathrm{C}$ by way of an $L=1$-m-long, $d=70-\mathrm{mm}-$ diameter shaft of thermal conductivity $k=40 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$.
(a) Compare the steady-state conduction rate through the shaft connecting the hot turbine to the warm compressor to the net power predicted by the thermodynamics-based analysis.
(b) A research team proposes to scale down the gas turbine of part (a), keeping all dimensions in the same proportions. The team assumes that the same hot and cold temperatures exist as in part (a) and that the net power output of the gas turbine is proportional to the overall volume of the device. Plot the ratio of the conduction through the shaft to the net power output of the turbine over the range $0.005 \mathrm{~m} \leq L \leq 1 \mathrm{~m}$. Is a scaled-down device with $L=0.005 \mathrm{~m}$ feasible?

Narayan Hari
Narayan Hari
Numerade Educator
03:46

Problem 9

A glass window of width $W=1 \mathrm{~m}$ and height $H=2 \mathrm{~m}$ is $5 \mathrm{~mm}$ thick and has a thermal conductivity of $k_{g}=$ $1.4 \mathrm{~W} / \mathrm{m}=\mathrm{K}$. If the inner and outer surface temperatures of the glass are $15^{\circ} \mathrm{C}$ and $-20^{\circ} \mathrm{C}$, respectively, on a cold winter day, what is the rate of heat loss through the glass? To reduce heat loss through windows, it is customary to use a double pane construction in which adjoining panes are separated by an air space. If the spacing is $10 \mathrm{~mm}$ and the glass surfaces in contact with the air have temperatures of $10^{\circ} \mathrm{C}$ and $-15^{\circ} \mathrm{C}$, what is the rate of heat loss from a $1 \mathrm{~m} \times 2 \mathrm{~m}$ window? The themal conductivity of air is $k_{a}=0.024 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$.

Manish Jain
Manish Jain
Numerade Educator
03:15

Problem 10

A freezer compartment consists of a cubical cavity that is $2 \mathrm{~m}$ on a side. Assume the bottom to be perfectly
insulated. What is the minimum thickness of styrofoam insulation $(k=0.030 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ that must be applied to the top and side walls to ensure a heat load of less than $500 \mathrm{~W}$, when the inner and outer surfaces are $-10$ and $35^{\circ} \mathrm{C}$ ?

Averell Hause
Averell Hause
Carnegie Mellon University
02:20

Problem 11

The heat flux that is applied to one face of a plane wall is $q^{\prime \prime}=20 \mathrm{~W} / \mathrm{m}^{2}$. The opposite face is exposed to air at temperature $30^{\circ} \mathrm{C}$, with a convection heat transfer coefficient of $20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The surface temperature of the wall exposed to air is measured and found to be $50^{\circ} \mathrm{C}$. Do steady-state conditions exist? If not, is the temperature of the wall increasing or decreasing with time?

Anand Jangid
Anand Jangid
Numerade Educator
02:18

Problem 12

An inexpensive food and beverage container is fabricated from 25 -mm-thick polystyrene $(k=0.023 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ and has interior dimensions of $0.8 \mathrm{~m} \times 0.6 \mathrm{~m} \times 0.6 \mathrm{~m}$. Under conditions for which an inner surface temperature of approximately $2^{\circ} \mathrm{C}$ is maintained by an ice-water mixture and an outer surface temperature of $20^{\circ} \mathrm{C}$ is maintained by the ambient, what is the heat flux through the container wall? Assuming negligible heat gain through the $0.8 \mathrm{~m} \times$ $0.6 \mathrm{~m}$ base of the cooler, what is the total heat load for the prescribed conditions?

Anand Jangid
Anand Jangid
Numerade Educator
02:02

Problem 13

What is the thickness required of a masonry wall having thermal conductivity $0.75 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$ if the heat rate is to be $80 \%$ of the heat rate through a composite structural wall having a thermal conductivity of $0.25 \mathrm{~W} / \mathrm{m}+\mathrm{K}$ and a thickness of $100 \mathrm{~mm}$ ? Both walls are subjected to the same surface temperature difference.

Ali Beker
Ali Beker
Numerade Educator
01:01

Problem 13

A wall is made from an inhomogeneous (nonuniform) material for which the thermal conductivity varies through the thickness according to $k=a x+b$, where $a$ and $b$ are constants. The heat flux is known to be constant. Determine expressions for the temperature gradient and the temperature distribution when the surface at $x=0$ is at temperature $T_{1}$.

Mayukh Banik
Mayukh Banik
Numerade Educator
01:01

Problem 14

A wall is made from an inhomogeneous (nonuniform) material for which the thermal conductivity varies through the thickness according to $k=a x+b$, where $a$ and $b$ are constants. The heat flux is known to be constant. Determine expressions for the temperature gradient and the temperature distribution when the surface at $x=0$ is at temperature $T_{1}$.

Mayukh Banik
Mayukh Banik
Numerade Educator
02:46

Problem 15

The 5 -mm-thick bottom of a $200-\mathrm{mm}$-diameter pan may be made from aluminum $(k=240 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ or copper $(k=390 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. When used to boil water, the surface of the bottom exposed to the water is nominally at $110^{\circ} \mathrm{C}$. If heat is transferred from the stove to the pan at a rate of $600 \mathrm{~W}$, what is the temperature of the surface in contact with the stove for each of the two materials?

Manish Jain
Manish Jain
Numerade Educator
01:27

Problem 16

A square silicon chip $(k=150 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ is of width $w=5 \mathrm{~mm}$ on a side and of thickness $t=1 \mathrm{~mm}$. The chip is mounted in a substrate such that its side and back surfaces are insulated, while the front surface is exposed to a coolant. If $4 \mathrm{~W}$ are being dissipated in circuits mounted to the back surface of the chip, what is the steady-state temperature difference between back and front surfaces?

Mayukh Banik
Mayukh Banik
Numerade Educator
03:51

Problem 17

For a boiling process such as shown in Figure $1.5 c$, the ambient temperature $T_{\infty}$ in Newton's law of cooling is replaced by the saturation temperature of the fluid $T_{\text {sat }}$. Consider a situation where the heat flux from the hot plate is $q^{\prime \prime}=20 \times 10^{5} \mathrm{~W} / \mathrm{m}^{2}$. If the fluid is water at atmospheric pressure and the convection heat transfer coefficient is $h_{w}=20 \times 10^{3} \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the upper surface temperature of the plate, $T_{s, w^{\circ}}$. In an effort to minimize the surface temperature, a technician proposes replacing the water with a dielectric fluid whose saturation temperature is $T_{\text {sat,d }}=52^{\circ} \mathrm{C}$. If the heat transfer coefficient associated with the dielectric fluid is $h_{d}=3 \times 10^{3} \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, will the technician's plan work?

Surendra Kumar
Surendra Kumar
Numerade Educator
02:50

Problem 18

You've experienced convection cooling if you've ever extended your hand out the window of a moving vehicle or into a flowing water stream. With the surface of your hand at a temperature of $30^{\circ} \mathrm{C}$, determine the convection heat flux for (a) a vehicle speed of $35 \mathrm{~km} / \mathrm{h}$ in air at $-5^{\circ} \mathrm{C}$ with a convection coefficient of 40 $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and (b) a velocity of $0.2 \mathrm{~m} / \mathrm{s}$ in a water stream at $10^{\circ} \mathrm{C}$ with a convection coefficient of $900 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Which condition would feel colder? Contrast these results with a heat loss of approximately $30 \mathrm{~W} / \mathrm{m}^{2}$ under normal room conditions.

Narayan Hari
Narayan Hari
Numerade Educator
00:56

Problem 19

Air at $40^{\circ} \mathrm{C}$ flows over a long, 25 -mm-diameter cylinder with an embedded electrical heater. In a series of tests, measurements were made of the power per unit length, $P^{\prime}$, required to maintain the cylinder surface temperature at $300^{\circ} \mathrm{C}$ for different free stream velocities $V$ of the air. The results are as follows:
\begin{tabular}{lccccc}
\hline Air velocity, $V(\mathrm{~m} / \mathrm{s})$ & 1 & 2 & 4 & 8 & 12 \\
Power, $P^{\prime}(\mathrm{W} / \mathrm{m})$ & 450 & 658 & 983 & 1507 & 1963 \\
\hline
\end{tabular}
(a) Determine the convection coefficient for each velocity, and display your results graphically.
(b) Assuming the dependence of the convection coefficient on the velocity to be of the form $h=C V^{n}$, determine the parameters $C$ and $n$ from the results of part (a).

Manik Pulyani
Manik Pulyani
Numerade Educator
01:01

Problem 20

A wall has inner and outer surface temperatures of 16 and $6^{\circ} \mathrm{C}$, respectively. The interior and exterior air temperatures are 20 and $5^{\circ} \mathrm{C}$, respectively. The inner and outer convection heat transfer coefficients are 5 and $20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. Calculate the heat flux from the interior air to the wall, from the wall to the exterior air, and from the wall to the interior air. Is the wall under steady-state conditions?

Mayukh Banik
Mayukh Banik
Numerade Educator
01:33

Problem 21

An electric resistance heater is embedded in a long cylinder of diameter $30 \mathrm{~mm}$. When water with a temperature of $25^{\circ} \mathrm{C}$ and velocity of $1 \mathrm{~m} / \mathrm{s}$ flows crosswise over the cylinder, the power per unit length required to maintain the surface at a uniform temperature of $90^{\circ} \mathrm{C}$ is $28 \mathrm{~kW} / \mathrm{m}$. When air, also at $25^{\circ} \mathrm{C}$, but with a velocity of $10 \mathrm{~m} / \mathrm{s}$ is flowing, the power per unit length required to maintain the same surface temperature is $400 \mathrm{~W} / \mathrm{m}$. Calculate and compare the convection coefficients for the flows of water and air.

Mayukh Banik
Mayukh Banik
Numerade Educator
02:17

Problem 22

The free convection heat transfer coefficient on a thin hot vertical plate suspended in still air can be determined from observations of the change in plate temperature with time as it cools. Assuming the plate is isothermal and radiation exchange with its surroundings is negligible, evaluate the convection coefficient at the instant of time when the plate temperature is $225^{\circ} \mathrm{C}$ and the change in plate temperature with time $(d T / d t)$ is $-0.022 \mathrm{~K} / \mathrm{s}$. The ambient air temperature is $25^{\circ} \mathrm{C}$ and the plate measures $0.3 \times 0.3 \mathrm{~m}$ with a mass of $3.75 \mathrm{~kg}$ and a specific heat of $2770 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.

Nicholas Mogoi
Nicholas Mogoi
Numerade Educator
03:12

Problem 23

A transmission case measures $W=0.30 \mathrm{~m}$ on a side and receives a power input of $P_{i}=150 \mathrm{hp}$ from the engine.
The switch is set to open at $70^{\circ} \mathrm{C}$, the maximum dryer air temperature. To operate the dryer at a lower air temperature, sufficient power is supplied to the heater such that the switch reaches $70^{\circ} \mathrm{C}\left(T_{\text {set }}\right)$ when the air temperature $T$ is less than $T_{\text {set. }}$. If the convection heat transfer coefficient between the air and the exposed switch surface of $30 \mathrm{~mm}^{2}$ is $25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, how much heater power $P_{e}$ is required when the desired dryer air temperature is $T_{\infty}=50^{\circ} \mathrm{C}$ ?

Abhishek Kumar
Abhishek Kumar
Numerade Educator
02:24

Problem 24

A cartridge electrical heater is shaped as a cylinder of length $L=200 \mathrm{~mm}$ and outer diameter $D=20 \mathrm{~mm}$. Under normal operating conditions, the heater dissipates $2 \mathrm{~kW}$ while submerged in a water flow that is at $20^{\circ} \mathrm{C}$ and provides a convection heat transfer coefficient of $h=5000 \mathrm{~W} / \mathrm{m}^{2}+\mathrm{K}$. Neglecting heat transfer from the ends of the heater, determine its surface temperature $T_{s}$. If the water flow is inadvertently terminated while the heater continues to operate, the heater surface is exposed to air that is also at $20^{\circ} \mathrm{C}$ but for which $h=50$ $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$. What is the corresponding surface temperature? What are the consequences of such an event?

Khoobchandra Agrawal
Khoobchandra Agrawal
Numerade Educator
01:41

Problem 25

A common procedure for measuring the velocity of an airstream involves the insertion of an electrically heated wire (called a hot-wire anemometer) into the airflow, with the axis of the wire oriented perpendicular to the flow direction. The electrical energy dissipated in the wire is assumed to be transferred to the air by forced convection. Hence, for a prescribed electrical power, the temperature of the wire depends on the convection coefficient, which, in turn, depends on the velocity of the air. Consider a wire of length $L=20 \mathrm{~mm}$ and diameter $D=0.5 \mathrm{~mm}$, for which a calibration of the form $V=6.25 \times 10^{-5} h^{2}$ has been determined. The velocity $V$ and the convection coefficient $h$ have units of $\mathrm{m} / \mathrm{s}$ and $\mathrm{W} / \mathrm{m}^{2}+\mathrm{K}$, respectively. In an application involving air at a temperature of $T_{\infty}=25^{\circ} \mathrm{C}$, the surface temperature of the anemometer is maintained at $T_{s}=75^{\circ} \mathrm{C}$ with a voltage drop of $5 \mathrm{~V}$ and an electric current of $0.1 \mathrm{~A}$. What is the velocity of the air?

Salamat Ali
Salamat Ali
Numerade Educator
08:44

Problem 26

A square isothermal chip is of width $w=5 \mathrm{~mm}$ on a side and is mounted in a substrate such that its side and back surfaces are well insulated; the front surface is exposed to the flow of a coolant at $T_{\infty}=15^{\circ} \mathrm{C}$. From reliability considerations, the chip temperature must not exceed $T=85^{\circ} \mathrm{C}$.
If the coolant is air and the corresponding convection coefficient is $h=200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, what is the maximum allowable chip power? If the coolant is a dielectric liquid for which $h=3000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, what is the maximum allowable power?

Yaqub Khan
Yaqub Khan
Numerade Educator
03:12

Problem 27

The temperature controller for a clothes dryer consists of a bimetallic switch mounted on an electrical heater attached to a wall-mounted insulation pad.
The switch is set to open at $70^{\circ} \mathrm{C}$, the maximum dryer air temperature. To operate the dryer at a lower air temperature, sufficient power is supplied to the heater such that the switch reaches $70^{\circ} \mathrm{C}\left(T_{\text {set }}\right)$ when the air temperature $T$ is less than $T_{\text {set. }}$. If the convection heat transfer coefficient between the air and the exposed switch surface of $30 \mathrm{~mm}^{2}$ is $25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, how much heater power $P_{e}$ is required when the desired dryer air temperature is $T_{\infty}=50^{\circ} \mathrm{C}$ ?

Abhishek Kumar
Abhishek Kumar
Numerade Educator
11:27

Problem 28

An overhead 25-m-long, uninsulated industrial steam pipe of $100-\mathrm{mm}$ diameter is routed through a building whose walls and air are at $25^{\circ} \mathrm{C}$. Pressurized steam maintains a pipe surface temperature of $150^{\circ} \mathrm{C}$, and the coefficient associated with natural convection is $h=10$ $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The surface emissivity is $\varepsilon=0.8$.
(a) What is the rate of heat loss from the steam line?
(b) If the steam is generated in a gas-fired boiler operating at an efficiency of $\eta_{f}=0.90$ and natural gas is priced at $C_{g}=\$ 0.02$ per $\mathrm{MJ}$, what is the annual cost of heat loss from the line?

Eric Mockensturm
Eric Mockensturm
Numerade Educator
02:33

Problem 29

Under conditions for which the same room temperature is maintained by a heating or cooling system, it is not uncommon for a person to feel chilled in the winter but comfortable in the summer. Provide a plausible explanation for this situation (with supporting calculations) by considering a room whose air temperature is maintained at $20^{\circ} \mathrm{C}$ throughout the year, while the walls of the room are nominally at $27^{\circ} \mathrm{C}$ and $14^{\circ} \mathrm{C}$ in the summer and winter, respectively. The exposed surface of a person in the room may be assumed to be at a temperature of $32^{\circ} \mathrm{C}$ throughout the year and to have an emissivity of $0.90$. The coefficient associated with heat transfer by natural convection between the person and the room air is approximately $2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.

Anand Jangid
Anand Jangid
Numerade Educator
01:33

Problem 30

A spherical interplanetary probe of $0.5-\mathrm{m}$ diameter contains electronics that dissipate $150 \mathrm{~W}$. If the probe surface has an emissivity of $0.8$ and the probe does not receive radiation from other surfaces, as, for example, from the sun, what is its surface temperature?

Mayukh Banik
Mayukh Banik
Numerade Educator
03:55

Problem 31

An instrumentation package has a spherical outer surface of diameter $D=100 \mathrm{~mm}$ and emissivity $\varepsilon=0.25$. The package is placed in a large space simulation chamber whose walls are maintained at $77 \mathrm{~K}$. If operation of the electronic components is restricted to the temperature range $40 \leq T \leq 85^{\circ} \mathrm{C}$, what is the range of acceptable power dissipation for the package? Display your results graphically, showing also the effect of variations in the emissivity by considering values of $0.20$ and $0.30$.

Dading Chen
Dading Chen
Numerade Educator
01:31

Problem 32

Consider the conditions of Problem 1.22. However, now the plate is in a vacuum with a surrounding temperature of $25^{\circ} \mathrm{C}$. What is the emissivity of the plate? What is the rate at which radiation is emitted by the surface?

Mayukh Banik
Mayukh Banik
Numerade Educator
01:19

Problem 33

If $T_{s} \approx T_{\text {sur }}$ in Equation $1.9$, the radiation heat transfer coefficient may be approximated as
$$
h_{r, a}=4 \varepsilon \sigma \bar{T}^{3}
$$
where $\bar{T} \equiv\left(T_{s}+T_{\text {sur }}\right) / 2$. We wish to assess the validity of this approximation by comparing values of $h_{r}$ and $h_{r, a}$ for the following conditions. In each case, represent your results graphically and comment on the validity of the approximation.
(a) Consider a surface of either polished aluminum ( $\varepsilon=$ $0.05)$ or black paint $(\varepsilon=0.9)$, whose temperature may exceed that of the surroundings $\left(T_{\text {sur }}=25^{\circ} \mathrm{C}\right)$ by 10 to $100^{\circ} \mathrm{C}$. Also compare your results with values of the coefficient associated with free convection in air $\left(T_{\infty}=T_{\text {sur }}\right)$, where $h\left(\mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\right)=0.98 \Delta T^{1 / 3}$.
(b) Consider initial conditions associated with placing a workpiece at $T_{s}=25^{\circ} \mathrm{C}$ in a large furnace whose wall temperature may be varied over the range $100 \leq$ $T_{\text {sur }} \leq 1000^{\circ} \mathrm{C}$. According to the surface finish or coating, its emissivity may assume values of $0.05$, $0.2$, and $0.9$. For each emissivity, plot the relative error, $\left(h_{r}-h_{r, a}\right) / h_{r}$, as a function of the furnace temperature.

Manik Pulyani
Manik Pulyani
Numerade Educator
07:59

Problem 34

A vacuum system, as used in sputtering electrically conducting thin films on microcircuits, is comprised of a baseplate maintained by an electrical heater at $300 \mathrm{~K}$ and a shroud within the enclosure maintained at $77 \mathrm{~K}$ by a liquid-nitrogen coolant loop. The circular baseplate, insulated on the lower side, is $0.3 \mathrm{~m}$ in diameter and has an emissivity of $0.25$.
(a) How much electrical power must be provided to the baseplate heater?
(b) At what rate must liquid nitrogen be supplied to the shroud if its heat of vaporization is $125 \mathrm{~kJ} / \mathrm{kg}$ ?
(c) To reduce the liquid nitrogen consumption, it is proposed to bond a thin sheet of aluminum foil $(\varepsilon=0.09)$ to the baseplate. Will this have the desired effect?

Ren Jie Tuieng
Ren Jie Tuieng
Numerade Educator
02:43

Problem 35

An electrical resistor is connected to a battery, as shown schematically. After a brief transient, the resistor assumes a nearly uniform, steady-state temperature of $95^{\circ} \mathrm{C}$, while the battery and lead wires remain at the ambient temperature of $25^{\circ} \mathrm{C}$. Neglect the electrical resistance of the lead wires.
(a) Consider the resistor as a system about which a control surface is placed and Equation $1.12 \mathrm{c}$ is applied. Determine the corresponding values of $\dot{E}_{\mathrm{in}}(\mathrm{W}), \dot{E}_{g}(\mathrm{~W}), \dot{E}_{\mathrm{oul}}(\mathrm{W})$, and $\dot{E}_{\mathrm{s}}(\mathrm{W})$. If a control surface is placed about the entire system, what are the values of $\dot{E}_{\text {in }}, \dot{E}_{g}, \dot{E}_{\text {out }}$, and $\dot{E}_{\mathrm{st}}$ ?
(b) If electrical energy is dissipated uniformly within the resistor, which is a cylinder of diameter $D=60 \mathrm{~mm}$ and length $L=250 \mathrm{~mm}$, what is the volumetric heat generation rate, $\dot{q}\left(\mathrm{~W} / \mathrm{m}^{3}\right)$ ?
(c) Neglecting radiation from the resistor, what is the convection coefficient?

Amit Srivastava
Amit Srivastava
Numerade Educator
01:25

Problem 36

Pressurized water $\left(p_{\text {in }}=10\right.$ bar, $\left.T_{\text {in }}=110^{\circ} \mathrm{C}\right)$ enters the bottom of an $L=10$-m-long vertical tube of diameter $D=100 \mathrm{~mm}$ at a mass flow rate of $\dot{m}=1.5 \mathrm{~kg} / \mathrm{s}$. The tube is located inside a combustion chamber, resulting in heat transfer to the tube. Superheated steam exits the top of the tube at $p_{\text {out }}=7$ bar, $T_{\text {out }}=600^{\circ} \mathrm{C}$. Determine the change in the rate at which the following quantities enter and exit the tube: (a) the combined thermal and flow work, (b) the mechanical energy, and (c) the total energy of the water. Also, (d) determine the heat transfer rate, $q$. Hint: Relevant properties may be obtained from a thermodynamics text.

Manik Pulyani
Manik Pulyani
Numerade Educator
03:14

Problem 37

Consider the tube and inlet conditions of Problem 1.36. Heat transfer at a rate of $q=3.89 \mathrm{MW}$ is delivered to the tube. For an exit pressure of $p=8$ bar, determine (a) the temperature of the water at the outlet as well as the change in (b) combined thermal and flow work, (c) mechanical energy, and (d) total energy of the water from the inlet to the outlet of the tube. Hint: As a first estimate, neglect the change in mechanical energy in solving part (a). Relevant properties may be obtained from a thermodynamics text.

Khoobchandra Agrawal
Khoobchandra Agrawal
Numerade Educator
00:56

Problem 38

An internally reversible refrigerator has a modified coefficient of performance accounting for realistic heat transfer processes of
$$
\mathrm{COP}_{m}=\frac{q_{\text {in }}}{\dot{W}}=\frac{q_{\text {in }}}{q_{\text {out }}-q_{\text {in }}}=\frac{T_{c, i}}{T_{h, i}-T_{c, i}}
$$
where $q_{\text {in }}$ is the refrigerator cooling rate, $q_{\text {out }}$ is the heat rejection rate, and $\dot{W}$ is the power input. Show that $\mathrm{COP}_{m}$ can be expressed in terms of the reservoir temperatures $T_{c}$ and $T_{h}$, the cold and hot thermal resistances $R_{L, c}$ and $R_{t, h}$, and $q_{\text {in }}$, as
$$
\mathrm{COP}_{m}=\frac{T_{c}-q_{\mathrm{in}} R_{\mathrm{tot}}}{T_{h}-T_{c}+q_{\mathrm{in}} R_{\mathrm{tot}}}
$$
where $R_{\mathrm{tot}}=R_{t, c}+R_{t, h}$. Also, show that the power input may be expressed as
$$
\dot{W}=q_{\mathrm{in}} \frac{T_{h}-T_{c}+q_{\mathrm{in}} R_{\mathrm{id \textrm {t }}}}{T_{c}-q_{\mathrm{in}} R_{\mathrm{tot}}}
$$

Hunza Gilgit
Hunza Gilgit
Numerade Educator
02:07

Problem 39

A household refrigerator operates with cold- and hot-temperature reservoirs of $T_{c}=5^{\circ} \mathrm{C}$ and $T_{h}=25^{\circ} \mathrm{C}$, respectively. When new, the cold and hot side resistances are $R_{c, n}=0.05 \mathrm{~K} / \mathrm{W}$ and $R_{h, n}=0.04 \mathrm{~K} / \mathrm{W}$, respectively. Over time, dust accumulates on the refrigerator's condenser coil, which is located behind the refrigerator, increasing the hot side resistance to $R_{h, d}=0.1 \mathrm{~K} / \mathrm{W}$. It is desired to have a refrigerator cooling rate of $q_{\text {in }}=750 \mathrm{~W}$. Using the results of Problem 1.38, determine the modified coefficient of performance and the required power input $\dot{W}$ under (a) clean and (b) dusty coil conditions.

Surendra Kumar
Surendra Kumar
Numerade Educator
01:27

Problem 40

Chips of width $L=15 \mathrm{~mm}$ on a side are mounted to a substrate that is installed in an enclosure whose walls and air are maintained at a temperature of $T_{\text {sur }}=25^{\circ} \mathrm{C}$. The chips have an emissivity of $\varepsilon=0.60$ and a maximum allowable temperature of $T_{s}=85^{\circ} \mathrm{C}$.
(a) If heat is rejected from the chips by radiation and natural convection, what is the maximum operating power of each chip? The convection coefficient depends on the chip-to-air temperature difference and may be approximated as $h=C\left(T_{s}-T_{\infty}\right)^{1 / 4}$, where $C=4.2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}^{5 / 4}$.
(b) If a fan is used to maintain airflow through the enclosure and heat transfer is by forced convection, with $h=250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, what is the maximum operating power?

Mayukh Banik
Mayukh Banik
Numerade Educator
00:52

Problem 41

Consider the transmission case of Problem $1.23$, but now allow for radiation exchange with the ground/ chassis, which may be approximated as large surroundings at $T_{\text {sur }}=30^{\circ} \mathrm{C}$. If the emissivity of the case is $\varepsilon=0.80$, what is the surface temperature?

Nikhil Choudhary
Nikhil Choudhary
Numerade Educator
01:00

Problem 42

1.42 One method for growing thin silicon sheets for photovoltaic solar panels is to pass two thin strings of high melting temperature material upward through a bath of molten silicon. The silicon solidifies on the strings near the surface of the molten pool, and the solid silicon sheet is pulled slowly upward out of the pool. The silicon is replenished by supplying the molten pool with solid silicon powder. Consider a silicon sheet that is $W_{\mathrm{si}}=85 \mathrm{~mm}$ wide and $t_{\mathrm{si}}=150 \mu \mathrm{m}$ thick that is pulled at a velocity of $V_{\mathrm{si}}=20 \mathrm{~mm} / \mathrm{min}$. The silicon is melted by supplying electric power to the cylindrical growth chamber of height $H=350 \mathrm{~mm}$ and diameter $D=300 \mathrm{~mm}$. The exposed surfaces of the growth chamber are at $T_{s}=$ $320 \mathrm{~K}$, the corresponding convection coefficient at the exposed surface is $h=8 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and the surface is characterized by an emissivity of $\varepsilon_{s}=0.9$. The solid silicon powder is at $T_{\mathrm{s}, i}=298 \mathrm{~K}$, and the solid silicon sheet exits the chamber at $T_{\text {si, } o}=420 \mathrm{~K}$. Both the surroundings and ambient temperatures are $T_{\infty}=T_{\text {sur }}=298 \mathrm{~K}$.
(a) Determine the electric power, $P_{\text {elec }}$, needed to operate the system at steady state.
(b) If the photovoltaic panel absorbs a time-averaged solar flux of $q_{\text {sol }}^{\prime \prime}=180 \mathrm{~W} / \mathrm{m}^{2}$ and the panel has a conversion efficiency (the ratio of solar power absorbed to electric power produced) of $\eta=0.20$, how long must the solar panel be operated to produce enough electric energy to offset the electric energy that was consumed in its manufacture?

Kratika Bhadauria
Kratika Bhadauria
Numerade Educator
12:12

Problem 43

Heat is transferred by radiation and convection between the inner surface of the nacelle of the wind turbine of Example $1.3$ and the outer surfaces of the gearbox and generator. The convection heat flux associated with the gearbox and the generator may be described by $q_{\text {conv, } \mathrm{gb}}^{\prime \prime}=h\left(T_{\mathrm{gb}}-T_{\infty}\right)$ and $q_{\text {conv,gen }}^{\prime \prime}=h\left(T_{\text {gen }}-T_{\infty}\right)$, respectively, where the ambient temperature $T_{\infty} \approx T_{s}$ (which is the nacelle temperature) and $h=40 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The outer surfaces of both the gearbox and the generator are characterized by an emissivity of $\varepsilon=0.9$. If the surface areas of the gearbox and generator are $A_{\mathrm{gb}}=6 \mathrm{~m}^{2}$ and $A_{\text {gen }}=4 \mathrm{~m}^{2}$, respectively, determine their surface temperatures.

Eric Mockensturm
Eric Mockensturm
Numerade Educator
02:10

Problem 44

Radioactive wastes are packed in a long, thin-walled cylindrical container. The wastes generate thermal energy nonuniformly according to the relation $\dot{q}=\dot{q}_{o}[1-$ $\left.\left(r / r_{\mathrm{o}}\right)^{2}\right]$, where $\dot{q}$ is the local rate of energy generation per unit volume, $\dot{q}_{o}$ is a constant, and $r_{\mathrm{o}}$ is the radius of the container. Steady-state conditions are maintained by submerging the container in a liquid that is at $T_{\infty}$ and provides a uniform convection coefficient $h$.
Obtain an expression for the total rate at which energy is generated in a unit length of the container. Use this result to obtain an expression for the temperature $T_{s}$ of the container wall.

Zulfiqar Ali
Zulfiqar Ali
Numerade Educator
01:31

Problem 45

An aluminum plate $4 \mathrm{~mm}$ thick is mounted in a horizontal position, and its bottom surface is well insulated. A special, thin coating is applied to the top surface such that it absorbs $80 \%$ of any incident solar radiation, while having an emissivity of $0.25$. The density $\rho$ and specific heat $c$ of aluminum are known to be $2700 \mathrm{~kg} / \mathrm{m}^{3}$ and $900 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$, respectively.
(a) Consider conditions for which the plate is at a temperature of $25^{\circ} \mathrm{C}$ and its top surface is suddenly exposed to ambient air at $T_{\infty}=20^{\circ} \mathrm{C}$ and to solar radiation that provides an incident flux of $900 \mathrm{~W} / \mathrm{m}^{2}$. The convection heat transfer coefficient between the surface and the air is $h=20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. What is the initial rate of change of the plate temperature?
(b) What will be the equilibrium temperature of the plate when steady-state conditions are reached?
(c) The surface radiative properties depend on the specific nature of the applied coating. Compute and plot the steady-state temperature as a function of the emissivity for $0.05 \leq \varepsilon \leq 1$, with all other conditions remaining as prescribed. Repeat your calculations for values of $\alpha_{S}=0.5$ and $1.0$, and plot the results with those obtained for $\alpha_{S}=0.8$. If the intent is to maximize the plate temperature, what is the most desirable combination of the plate emissivity and its absorptivity to solar radiation?

Mayukh Banik
Mayukh Banik
Numerade Educator
03:23

Problem 46

A blood warmer is to be used during the transfusion of blood to a patient. This device is to heat blood taken from the blood bank at $10^{\circ} \mathrm{C}$ to $37^{\circ} \mathrm{C}$ at a flow rate of $200 \mathrm{ml} / \mathrm{min}$. The blood passes through tubing of length $2 \mathrm{~m}$, with a rectangular cross section $6.4 \mathrm{~mm} \times 1.6 \mathrm{~mm}$ At what rate must heat be added to the blood to accomplish the required temperature increase? If the fluid originates from a large tank with nearly zero velocity and flows vertically downward for its 2-m length, estimate the magnitudes of kinetic and potential energy changes. Assume the blood's properties are similar to those of water.

Vinnu M
Vinnu M
Numerade Educator
02:59

Problem 47

Consider a carton of milk that is refrigerated at a temperature of $T_{m \mathrm{r}}=5^{\circ} \mathrm{C}$. The kitchen temperature on a hot summer day is $T_{\infty}=30^{\circ} \mathrm{C}$. If the four sides of the carton are of height and width $L=200 \mathrm{~mm}$ and $w=100 \mathrm{~mm}$, respectively, determine the heat transferred to the milk carton as it sits on the kitchen counter for durations of $t=10 \mathrm{~s}, 60 \mathrm{~s}$, and $300 \mathrm{~s}$ before it is returned to the refrigerator. The convection coefficient associated with natural convection on the sides of the carton is $h=10$ $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The surface emissivity is $0.90$. Assume the milk carton temperature remains at $5^{\circ} \mathrm{C}$ during the process. Your parents have taught you the importance of refrigerating certain foods from the food safety perspective. Comment on the importance of quickly returning the milk carton to the refrigerator from an energy conservation point of view.

Penny Riley
Penny Riley
Numerade Educator
04:55

Problem 48

The energy consumption associated with a home water heater has two components: (i) the energy that must be supplied to bring the temperature of groundwater to the heater storage temperature, as it is introduced to replace hot water that has been used; (ii) the energy needed to compensate for heat losses incurred while the water is stored at the prescribed temperature. In this problem, we will evaluate the first of these components for a family of four, whose daily hot water consumption is approximately $100 \mathrm{gal}$. If groundwater is available at $15^{\circ} \mathrm{C}$, what is the annual energy consumption associated with heating the water to a storage temperature of $55^{\circ} \mathrm{C}$ ? For a unit electrical power cost of $\$ 0.18 / \mathrm{kW} \cdot \mathrm{h}$, what is the annual cost associated with supplying hot water by means of (a) electric resistance heating or (b) a heat pump having a COP of 3 .

Hariprasad Annamalai
Hariprasad Annamalai
Numerade Educator
04:42

Problem 49

Liquid oxygen, which has a boiling point of $90 \mathrm{~K}$ and a latent heat of vaporization of $214 \mathrm{~kJ} / \mathrm{kg}$, is stored in a spherical container whose outer surface is of $500-\mathrm{mm}$ diameter and at a temperature of $-10^{\circ} \mathrm{C}$. The container is housed in a laboratory whose air and walls are at $25^{\circ} \mathrm{C}$.
(a) If the surface emissivity is $0.20$ and the heat transfer coefficient associated with free convection at the outer surface of the container is $10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, what is the rate, in $\mathrm{kg} / \mathrm{s}$, at which oxygen vapor must be vented from the system?
(b) Moisture in the ambient air will result in frost formation on the container, causing the surface emissivity to increase. Assuming the surface temperature and convection coefficient to remain at $-10^{\circ} \mathrm{C}$ and $10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively, compute the oxygen evaporation rate $(\mathrm{kg} / \mathrm{s})$ as a function of surface emissivity over the range $0.2 \leq \varepsilon \leq 0.94$.

Abhishek Kumar
Abhishek Kumar
Numerade Educator
01:01

Problem 50

The emissivity of galvanized steel sheet, a common roofing material, is $\varepsilon=0.13$ at temperatures around $300 \mathrm{~K}$, while its absorptivity for solar irradiation is $\alpha_{S}=0.65$. Would the neighborhood cat be comfortable walking on a roof constructed of the material on a day when $G_{S}=750 \mathrm{~W} / \mathrm{m}^{2}, T_{\infty}=16^{\circ} \mathrm{C}$, and $h=7$ $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$ ? Assume the bottom surface of the steel is insulated.

Mayukh Banik
Mayukh Banik
Numerade Educator
04:34

Problem 51

Three electric resistance heaters of length $L=250 \mathrm{~mm}$ and diameter $D=25 \mathrm{~mm}$ are submerged in a 10 -gal tank of water, which is initially at $295 \mathrm{~K}$. The water may be assumed to have a density and specific heat of $\rho=990 \mathrm{~kg} / \mathrm{m}^{3}$ and $c=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.
(a) If the heaters are activated, each dissipating $q_{1}=500 \mathrm{~W}$, estimate the time required to bring the water to a temperature of $335 \mathrm{~K}$.
(b) If the natural convection coefficient is given by an expression of the form $h=370\left(T_{s}-T\right)^{1 / 3}$, where $T_{s}$ and $T$ are temperatures of the heater surface and water, respectively, what is the temperature of each heater shortly after activation and just before deactivation? Units of $h$ and $\left(T_{s}-T\right)$ are $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and $\mathrm{K}$, respectively.
(c) If the heaters are inadvertently activated when the tank is empty, the natural convection coefficient associated with heat transfer to the ambient air at $T_{\infty}=300 \mathrm{~K}$ may be approximated as $h=0.70$ $\left(T_{s}-T_{\infty}\right)^{1 / 3}$. If the temperature of the tank walls is also $300 \mathrm{~K}$ and the emissivity of the heater surface is $\varepsilon=0.85$, what is the surface temperature of each heater under steady-state conditions?

Manne Andergronde
Manne Andergronde
Numerade Educator
01:42

Problem 52

A hair dryer may be idealized as a circular duct through which a small fan draws ambient air and within which the air is heated as it flows over a coiled electric resistance wire.
(a) If a dryer is designed to operate with an electric power consumption of $P_{\text {elec }}=500 \mathrm{~W}$ and to heat air from an ambient temperature of $T_{i}=20^{\circ} \mathrm{C}$ to a discharge temperature of $T_{o}=45^{\circ} \mathrm{C}$, at what volumetric flow rate $\forall$ should the fan operate? Heat loss from the casing to the ambient air and the surroundings may be neglected. If the duct has a diameter of $D=70 \mathrm{~mm}$, what is the discharge velocity $V_{o}$ of the air? The density and specific heat of the air may be approximated as $\rho=1.10 \mathrm{~kg} / \mathrm{m}^{3}$ and $c_{p}=1007$ $\mathrm{J} / \mathrm{kg} \cdot \mathrm{K}$, respectively.
(b) Consider a dryer duct length of $L=150 \mathrm{~mm}$ and a surface emissivity of $\varepsilon=0.8$. If the coefficient associated with heat transfer by natural convection from the casing to the ambient air is $h=4$ $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and the temperature of the air and the surroundings is $T_{\infty}=T_{\text {sur }}=20^{\circ} \mathrm{C}$, confirm that the heat loss from the casing is, in fact, negligible. The casing may be assumed to have an average surface temperature of $T_{\mathrm{s}}=40^{\circ} \mathrm{C}$.

Naman Kumar
Naman Kumar
Numerade Educator
02:59

Problem 53

In one stage of an annealing process, 304 stainless steel sheet is taken from $300 \mathrm{~K}$ to $1250 \mathrm{~K}$ as it passes through an electrically heated oven at a speed of $V_{s}=10 \mathrm{~mm} / \mathrm{s}$. The sheet thickness and width are $t_{s}=8 \mathrm{~mm}$ and $W_{s}=2 \mathrm{~m}$, respectively, while the height, width, and length of the oven are $H_{o}=2 \mathrm{~m}$, $W_{o}=2.4 \mathrm{~m}$, and $L_{o}=25 \mathrm{~m}$, respectively. The top and four sides of the oven are exposed to ambient air and large surroundings, each at $300 \mathrm{~K}$, and the corresponding surface temperature, convection coefficient, and emissivity are $T_{s}=350 \mathrm{~K}, h=10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and $\varepsilon_{s}=0.8$. The bottom surface of the oven is also at $350 \mathrm{~K}$ and rests on a $0.5$-m-thick concrete pad whose base is at $300 \mathrm{~K}$. Estimate the required electric power input, $P_{\text {elec }}$, to the oven.

Khoobchandra Agrawal
Khoobchandra Agrawal
Numerade Educator
03:40

Problem 54

Convection ovens operate on the principle of inducing forced convection inside the oven chamber with a fan. A small cake is to be baked in an oven when the convection feature is disabled. For this situation, the free convection coefficient associated with the cake and its pan is $h_{\mathrm{fr}}=3 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The oven air and wall are at temperatures $T_{\infty}=T_{\text {sur }}=180^{\circ} \mathrm{C}$. Determine the heat flux delivered to the cake pan and cake batter when they are initially inserted into the oven and are at a temperature of $T_{i}=24^{\circ} \mathrm{C}$. If the convection feature is activated, the forced convection heat transfer coefficient is $h_{\mathrm{fo}}=27 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. What is the heat flux at the batter or pan surface when the oven is operated in the convection mode? Assume a value of $0.97$ for the emissivity of the cake batter and pan.

Erica Bischoff
Erica Bischoff
Numerade Educator
11:24

Problem 55

Annealing, an important step in semiconductor materials processing, can be accomplished by rapidly heating the silicon wafer to a high temperature for a short period of time. The schematic shows a method involving the use of a hot plate operating at an elevated temperature $T_{h}$. The wafer, initially at a temperature of $T_{w, i}$, is suddenly positioned at a gap separation distance $L$ from the hot plate. The purpose of the analysis is to compare the heat fluxes by conduction through the gas within the gap and by radiation exchange between the hot plate and the cool wafer. The initial time rate of change in the temperature of the wafer, $\left(d T_{w} / d t\right)_{i}$, is also of interest. Approximating the surfaces of the hot plate and the wafer as blackbodies and assuming their diameter $D$ to be much larger than the spacing $L$, the radiative heat flux may be expressed as $q_{\text {rad }}^{\prime \prime}=\sigma\left(T_{h}^{4}-T_{w}^{4}\right)$. The silicon wafer has a thickness of $d=0.78 \mathrm{~mm}$, a density of $2700 \mathrm{~kg} / \mathrm{m}^{3}$, and a specific heat of 875 $\mathrm{J} / \mathrm{kg} \cdot \mathrm{K}$. The thermal conductivity of the gas in the gap is $0.0436 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$.
(a) For $T_{h}=600^{\circ} \mathrm{C}$ and $T_{w, i}=20^{\circ} \mathrm{C}$, calculate the radiative heat flux and the heat flux by conduction across a gap distance of $L=0.2 \mathrm{~mm}$. Also determine the value of $\left(d T_{\mathrm{w}} / d t\right)_{i}$, resulting from each of the heating modes.
(b) For gap distances of $0.2,0.5$, and $1.0 \mathrm{~mm}$, determine the heat fluxes and temperature-time change as a function of the hot plate temperature for $300 \leq$ $T_{h} \leq 1300^{\circ} \mathrm{C}$. Display your results graphically. Comment on the relative importance of the two heat

Nathan Prins
Nathan Prins
Numerade Educator
02:31

Problem 56

In the thermal processing of semiconductor materials, annealing is accomplished by heating a silicon wafer according to a temperature-time recipe and then maintaining a fixed elevated temperature for a prescribed period of time. For the process tool arrangement shown as follows, the wafer is in an evacuated chamber whose walls are maintained at $27^{\circ} \mathrm{C}$ and within which heating lamps maintain a radiant flux $q_{s}^{\prime \prime}$ at its upper surface. The wafer is $0.78 \mathrm{~mm}$ thick, has a thermal conductivity of $30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, and an emissivity that equals its absorptivity to the radiant flux $\left(\varepsilon=\alpha_{l}=0.65\right.$ ). For $q_{s}^{\prime \prime}=3.0 \times 10^{5} \mathrm{~W} / \mathrm{m}^{2}$, the temperature on its lower surface is measured by a radiation thermometer and found to have a value of $T_{w, l}=997^{\circ} \mathrm{C}$.
To avoid warping the wafer and inducing slip planes in the crystal structure, the temperature difference across the thickness of the wafer must be less than $2^{\circ} \mathrm{C}$. Is this condition being met?

Chai Santi
Chai Santi
Numerade Educator
11:24

Problem 57

A furnace for processing semiconductor materials is formed by a silicon carbide chamber that is zone-heated on the top section and cooled on the lower section. With the elevator in the lowest position, a robot arm inserts the silicon wafer on the mounting pins. In a production operation, the wafer is rapidly moved toward the hot zone to achieve the temperature-time history required for the process recipe. In this position, the top and bottom surfaces of the wafer exchange radiation with the hot and cool zones, respectively, of the chamber. The zone temperatures are $T_{h}=1500 \mathrm{~K}$ and $T_{c}=330 \mathrm{~K}$, and the emissivity and thickness of the wafer are $\varepsilon=0.65$ and $d=0.78 \mathrm{~mm}$, respectively. With the ambient gas at $T_{\infty}=700 \mathrm{~K}$, convection coefficients at the upper and lower surfaces of the wafer are 8 and $4 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The silicon wafer has a density of $2700 \mathrm{~kg} / \mathrm{m}^{3}$ and a specific heat of $875 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.
(a) For an initial condition corresponding to a wafer temperature of $T_{w, i}=300 \mathrm{~K}$ and the position of the wafer shown schematically, determine the corresponding time rate of change of the wafer temperature, $\left(d T_{w} / d t\right)_{i^{*}}$
(b) Determine the steady-state temperature reached by the wafer if it remains in this position. How significant is convection heat transfer for this situation? Sketch how you would expect the wafer temperature to vary as a function of vertical distance.

Nathan Prins
Nathan Prins
Numerade Educator
12:21

Problem 58

Single fuel cells such as the one of Example $1.5$ can be scaled up by arranging them into a fuel cell stack. A stack consists of multiple electrolytic membranes that are sandwiched between electrically conducting bipolar plates. Air and hydrogen are fed to each membrane through fiw channels within each bipolar plate, as shown in the sketch. With this stack arrangement, the individual fuel cells are connected in series, electrically, producing a stack voltage of $E_{\text {stack }}=N \times E_{c}$, where $E_{c}$ is the voltage produced across each membrane and $N$ is the number of membranes in the stack. The electrical current is the same for each membrane. The cell voltage, $E_{c}$, as well as the cell efficiency, increases with temperature (the air and hydrogen fed to the stack are humidified to allow operation at temperatures greater than in Example 1.5), but the membranes will fail at temperatures exceeding $T \approx 85^{\circ} \mathrm{C}$. Consider $L \times w$ membranes, where $L=w=100 \mathrm{~mm}$, of thickness $t_{m}=0.43 \mathrm{~mm}$, that each produce $E_{c}=0.6 \mathrm{~V}$ at $I=60 \mathrm{~A}$, and $\dot{E}_{c g}=45 \mathrm{~W}$ of thermal energy when operating at $T=80^{\circ} \mathrm{C}$. The external surfaces of the stack are exposed to air at $T_{\infty}=25^{\circ} \mathrm{C}$ and surroundings at $T_{\text {sur }}=30^{\circ} \mathrm{C}$, with $\varepsilon=0.88$ and $h=150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.
(a) Find the electrical power produced by a stack that is $L_{\text {stack }}=200 \mathrm{~mm}$ long, for bipolar plate thickness in the range $1 \mathrm{~mm}<t_{\text {bp }}<10 \mathrm{~mm}$. Determine the total thermal energy generated by the stack.
(b) Calculate the surface temperature and explain whether the stack needs to be internally heated or cooled to operate at the optimal internal temperature of $80^{\circ} \mathrm{C}$ for various bipolar plate thicknesses.
(c) Identify how the internal stack operating temperature might be lowered or raised for a given bipolar plate thickness, and discuss design changes that would promote a more uniform temperature distribution within the stack. How would changes in the external air and surroundings temperature affect your answer? Which membrane in the stack is most likely to fail due to high operating temperature?

Sanjeev Kumar
Sanjeev Kumar
Numerade Educator
02:29

Problem 59

Consider the wind turbine of Example 1.3. To reduce the nacelle temperature to $T_{s}=30^{\circ} \mathrm{C}$, the nacelle is vented and a fan is installed to force ambient air into and out of the nacelle enclosure. What is the minimum mass flow rate of air required if the air temperature increases to the nacelle surface temperature before exiting the nacelle? The specific heat of air is $1007 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.

Dominador Tan
Dominador Tan
Numerade Educator
01:19

Problem 60

Consider the conducting rod of Example $1.4$ under steady-state conditions. As suggested in Comment 3 , the temperature of the rod may be controlled by varying the speed of airflow over the rod, which, in turn, alters the convection heat transfer coefficient. To consider the effect of the convection coefficient, generate plots of $T$ versus $I$ for values of $h=50,100$, and $250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Would variations in the surface emissivity have a significant effect on the rod temperature?

Narayan Hari
Narayan Hari
Numerade Educator
07:25

Problem 61

A long bus bar (cylindrical rod used for making electrical connections) of diameter $D$ is installed in a large conduit having a surface temperature of $30^{\circ} \mathrm{C}$ and in which the ambient air temperature is $T_{\infty}=$ $30^{\circ} \mathrm{C}$. The electrical resistivity, $\rho_{e}(\mu \Omega \cdot \mathrm{m})$, of the bar material is a function of temperature, $\rho_{e, o}=\rho_{e}$ $\left[1+\alpha\left(T-T_{o}\right)\right]$, where $\rho_{e, o}=0.0171 \mu \Omega \cdot \mathrm{m}, T_{o}=$ $25^{\circ} \mathrm{C}$, and $\alpha=0.00396 \mathrm{~K}^{-1}$. The bar experiences free convection in the ambient air, and the convection coefficient depends on the bar diameter, as well as on the difference between the surface and ambient temperatures. The governing relation is of the form, $h=C D^{-0.25}\left(T-T_{\infty}\right)^{0.25}$, where $C=1.21$ $\mathrm{W} \cdot \mathrm{m}^{-1.75} \cdot \mathrm{K}^{-1.25}$. The emissivity of the bar surface is $\varepsilon=0.85$.
(a) Recognizing that the electrical resistance per unit length of the bar is $R_{e}^{\prime}=\rho_{c} / A_{c}$, where $A_{c}$ is its cross-sectional area, calculate the current-carrying capacity of a 20 -mm-diameter bus bar if its temperature is not to exceed $65^{\circ} \mathrm{C}$. Compare the relative importance of heat transfer by free convection and radiation exchange.
(b) To assess the trade-off between current-carrying capacity, operating temperature, and bar diameter, for diameters of 10,20 , and $40 \mathrm{~mm}$, plot the bar temperature $T$ as a function of current for the range $100 \leq I \leq 5000 \mathrm{~A}$. Also plot the ratio of the heat transfer by convection to the total heat transfer.

Arun Bana
Arun Bana
Numerade Educator
01:37

Problem 62

A small sphere of reference-grade iron with a specific heat of $447 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$ and a mass of $0.515 \mathrm{~kg}$ is suddenly immersed in a water-ice mixture. Fine thermocouple wires suspend the sphere, and the temperature is observed to change from 15 to $14^{\circ} \mathrm{C}$ in $6.35 \mathrm{~s}$. The experiment is repeated with a metallic sphere of the same diameter, but of unknown composition with a mass of $1.263 \mathrm{~kg}$. If the same observed temperature change occurs in $4.59 \mathrm{~s}$, what is the specific heat of the unknown material?

Manne Andergronde
Manne Andergronde
Numerade Educator
04:05

Problem 63

A $50 \mathrm{~mm} \times 45 \mathrm{~mm} \times 20 \mathrm{~mm}$ cell phone charger has a surface temperature of $T_{s}=33^{\circ} \mathrm{C}$ when plugged into an electrical wall outlet but not in use. The surface of the charger is of emissivity $\varepsilon=0.92$ and is subject to a free convection heat transfer coefficient of $h=4.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The room air and wall temperatures are $T_{\infty}=22^{\circ} \mathrm{C}$ and $T_{\text {sur }}=20^{\circ} \mathrm{C}$, respectively. If electricity costs $C=\$ 0.18 / \mathrm{kW} \cdot \mathrm{h}$, determine the daily cost of leaving the charger plugged in when not in use.

Satpal Satpal
Satpal Satpal
Numerade Educator
09:01

Problem 64

A spherical, stainless steel (AISI 302) canister is used to store reacting chemicals that provide for a uniform heat flux $q_{i}^{\prime \prime}$ to its inner surface. The canister is suddenly submerged in a liquid bath of temperature $T_{\infty}<T_{i}$, where $T_{i}$ is the initial temperature of the canister wall.
(a) Assuming negligible temperature gradients in the canister wall and a constant heat flux $q_{i}^{\prime \prime}$, develop an equation that governs the variation of the wall temperature with time during the transient process. What is the initial rate of change of the wall temperature if $q_{i}^{\prime \prime}=10^{5} \mathrm{~W} / \mathrm{m}^{2}$ ?
(b) What is the steady-state temperature of the wall?
(c) The convection coefficient depends on the velocity associated with fluid flow over the canister and whether the wall temperature is large enough to induce boiling in the liquid. Compute and plot the steady-state temperature as a function of $h$ for the range $100 \leq h \leq 10,000 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Is there a value of $h$ below which operation would be unacceptable?

Averell Hause
Averell Hause
Carnegie Mellon University
01:00

Problem 65

A freezer compartment is covered with a 2 -mm-thick layer of frost at the time it malfunctions. If the compartment is in ambient air at $20^{\circ} \mathrm{C}$ and a coefficient of $h=2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ characterizes heat transfer by natural convection from the exposed surface of the layer, estimate the time required to completely melt the frost. The frost may be assumed to have a mass density of $700 \mathrm{~kg} / \mathrm{m}^{3}$ and a latent heat of fusion of $334 \mathrm{~kJ} / \mathrm{kg}$.

Kratika Bhadauria
Kratika Bhadauria
Numerade Educator
04:34

Problem 66

A vertical slab of Wood's metal is joined to a substrate on one surface and is melted as it is uniformly irradiated by a laser source on the opposite surface. The metal is initially at its fusion temperature of $T_{f}=72^{\circ} \mathrm{C}$, and the melt runs off by gravity as soon as it is formed. The absorptivity of the metal to the laser radiation is $\alpha_{1}=0.4$, and its latent heat of fusion is $h_{s f}=33 \mathrm{~kJ} / \mathrm{kg}$.
(a) Neglecting heat transfer from the irradiated surface by convection or radiation exchange with the surroundings, determine the instantaneous rate of melting in $\mathrm{kg} / \mathrm{s} \cdot \mathrm{m}^{2}$ if the laser irradiation is $5 \mathrm{~kW} / \mathrm{m}^{2}$. How much material is removed if irradiation is maintained for a period of $2 \mathrm{~s}$ ?
(b) Allowing for convection to ambient air, with $T_{\infty}=20^{\circ} \mathrm{C}$ and $h=15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and radiation exchange with large surroundings $(\varepsilon=0.4$, $T_{\text {sur }}=20^{\circ} \mathrm{C}$ ), determine the instantaneous rate of melting during irradiation.

Ren Jie Tuieng
Ren Jie Tuieng
Numerade Educator
02:25

Problem 67

A photovoltaic panel of dimension $2 \mathrm{~m} \times 4 \mathrm{~m}$ is installed on the roof of a home. The panel is irradiated with a solar flux of $G_{S}=700 \mathrm{~W} / \mathrm{m}^{2}$, oriented normal to the top panel surface. The absorptivity of the panel to the solar irradiation is $\alpha_{S}=0.83$, and the efficiency of conversion of the absorbed flux to electrical power is $\eta=P / \alpha_{S} G_{S} A=0.553-0.001 \mathrm{~K}^{-1} T_{p}$, where $T_{p}$ is the panel temperature expressed in kelvins and $A$ is the solar panel area. Determine the electrical power generated for
(a) a still summer day, in which $T_{\text {sur }}=T_{\infty}=35^{\circ} \mathrm{C}$, $h=10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and (b) a breezy winter day, for which $T_{\text {sur }}=T_{\infty}=-15^{\circ} \mathrm{C}, h=30 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The panel emissivity is $\varepsilon=0.90$.

Mayukh Banik
Mayukh Banik
Numerade Educator
01:25

Problem 68

Following the hot vacuum forming of a paper-pulp mixture, the product, an egg carton, is transported on a conveyor for $18 \mathrm{~s}$ toward the entrance of a gas-fired oven where it is dried to a desired final water content. Very little water evaporates during the travel time. So, to increase the productivity of the line, it is proposed that a bank of infrared radiation heaters, which provide a uniform radiant flux of $5000 \mathrm{~W} / \mathrm{m}^{2}$, be installed over the conveyor. The carton has an exposed area of $0.0625 \mathrm{~m}^{2}$ and a mass of $0.220 \mathrm{~kg}, 75 \%$ of which is water after the forming process.
The chief engineer of your plant will approve the purchase of the heaters if they can reduce the water content by $10 \%$ of the total mass. Would you recommend the purchase? Assume the heat of vaporization of water is $h_{f g}=2400 \mathrm{~kJ} / \mathrm{kg}$.

Manik Pulyani
Manik Pulyani
Numerade Educator
06:47

Problem 69

Electronic power devices are mounted to a heat sink having an exposed surface area of $0.045 \mathrm{~m}^{2}$ and an emissivity of $0.80$. When the devices dissipate a total power of $20 \mathrm{~W}$ and the air and surroundings are at $27^{\circ} \mathrm{C}$, the average sink temperature is $42^{\circ} \mathrm{C}$. What average temperature will the heat sink reach when the devices dissipate $30 \mathrm{~W}$ for the same environmental condition?

Keshav Singh
Keshav Singh
Numerade Educator
04:57

Problem 70

A computer consists of an array of five printed circuit boards (PCBs), each dissipating $P_{b}=20 \mathrm{~W}$ of power. Cooling of the electronic components on a board is provided by the forced flow of air, equally distributed in passages formed by adjoining boards, and the convection coefficient associated with heat transfer from the components to the air is approximately $h=200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Air enters the computer console at a temperature of $T_{i}=20^{\circ} \mathrm{C}$, and flow is driven by a fan whose power consumption is $P_{f}=25 \mathrm{~W}$.
(a) If the temperature rise of the airflow, $\left(T_{o}-T_{i}\right)$, is not to exceed $15^{\circ} \mathrm{C}$, what is the minimum allowable volumetric flow rate $\dot{\forall}$ of the air? The density and specific heat of the air may be approximated as $\rho=1.161$ $\mathrm{kg} / \mathrm{m}^{3}$ and $c_{p}=1007 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$, respectively.
(b) The component that is most susceptible to thermal failure dissipates $1 \mathrm{~W} / \mathrm{cm}^{2}$ of surface area. To minimize the potential for thermal failure, where should the component be installed on a PCB? What is its surface temperature at this location?

Dading Chen
Dading Chen
Numerade Educator
09:01

Problem 71

Consider a surface-mount type transistor on a circuit board whose temperature is maintained at $35^{\circ} \mathrm{C}$. Air at $20^{\circ} \mathrm{C}$ flows over the upper surface of dimensions $4 \mathrm{~mm} \times$ $8 \mathrm{~mm}$ with a convection coefficient of $50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Three wire leads, each of cross section $1 \mathrm{~mm} \times 0.25 \mathrm{~mm}$ and length $4 \mathrm{~mm}$, conduct heat from the case to the circuit board. The gap between the case and the board is $0.2 \mathrm{~mm}$.
(a) Assuming the case is isothermal and neglecting radiation, estimate the case temperature when $150 \mathrm{~mW}$ is dissipated by the transistor and (i) stagnant air or (ii) a conductive paste fills the gap. The thermal conductivities of the wire leads, air, and conductive paste are $25,0.0263$, and $0.12 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, respectively.
(b) Using the conductive paste to fill the gap, we wish to determine the extent to which increased heat dissipation may be accommodated, subject to the constraint that the case temperature not exceed $40^{\circ} \mathrm{C}$. Options include increasing the air speed to achieve a larger convection coefficient $h$ and/or changing the lead wire material to one of larger thermal conductivity. Independently considering leads fabricated from materials with thermal conductivities of 200 and $400 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$, compute and plot the maximum allowable heat dissipation for variations in $h$ over the range $50 \leq h \leq 250 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.

Averell Hause
Averell Hause
Carnegie Mellon University
03:53

Problem 72

The roof of a car in a parking lot absorbs a solar radiant flux of $800 \mathrm{~W} / \mathrm{m}^{2}$, and the underside is perfectly insulated. The convection coefficient between the roof and the ambient air is $12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.
(a) Neglecting radiation exchange with the surroundings, calculate the temperature of the roof under steadystate conditions if the ambient air temperature is $20^{\circ} \mathrm{C}$.
(b) For the same ambient air temperature, calculate the temperature of the roof if its surface emissivity is $0.8$.
(c) The convection coefficient depends on airflow conditions over the roof, increasing with increasing air speed. Compute and plot the roof temperature as a function of $h$ for $2 \leq h \leq 200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.

Narayan Hari
Narayan Hari
Numerade Educator
02:17

Problem 73

Consider the conditions of Problem $1.22$, but the surroundings temperature is $25^{\circ} \mathrm{C}$ and radiation exchange with the surroundings is not negligible. If the convection coefficient is $6.4 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and the emissivity of the plate is $\varepsilon=0.42$, determine the time rate of change of the plate temperature, $d T / d t$, when the plate temperature is $225^{\circ} \mathrm{C}$. Evaluate the heat loss by convection and the heat loss by radiation.

Nicholas Mogoi
Nicholas Mogoi
Numerade Educator
02:55

Problem 74

Most of the energy we consume as food is converted to thermal energy in the process of performing all our bodily functions and is ultimately lost as heat from our bodies. Consider a person who consumes $2100 \mathrm{kcal}$ per day (note that what are commonly referred to as food calories are actually kilocalories), of which $2000 \mathrm{kcal}$ is converted to thermal energy. (The remaining $100 \mathrm{kcal}$ is used to do work on the environment.) The person has a surface area of $1.8 \mathrm{~m}^{2}$ and is dressed in a bathing suit.
(a) The person is in a room at $20^{\circ} \mathrm{C}$, with a convection heat transfer coefficient of $3 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. At this air temperature, the person is not perspiring much. Estimate the person's average skin temperature.
(b) If the temperature of the environment were $33^{\circ} \mathrm{C}$, what rate of perspiration would be needed to maintain a comfortable skin temperature of $33^{\circ} \mathrm{C}$ ?

Khoobchandra Agrawal
Khoobchandra Agrawal
Numerade Educator
01:26

Problem 75

Consider Problem 1.1.
(a) If the exposed cold surface of the insulation is at $T_{2}=20^{\circ} \mathrm{C}$, what is the value of the convection heat transfer coefficient on the cold side of the insulation if the surroundings temperature is $T_{\text {sur }}=320 \mathrm{~K}$, the ambient temperature is $T_{\infty}=5^{\circ} \mathrm{C}$, and the emissivity is $\varepsilon=0.95$ ? Express your results in units of $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and $\mathrm{W} / \mathrm{m}^{2} \cdot{ }^{\circ} \mathrm{C}$.
(b) Using the convective heat transfer coefficient you calculated in part (a), determine the surface temperature, $T_{2}$, as the emissivity of the surface is varied over the range $0.05 \leq \varepsilon \leq 0.95$. The hot wall temperature of the insulation remains fixed at $T_{1}=30^{\circ} \mathrm{C}$. Display your results graphically.

Narayan Hari
Narayan Hari
Numerade Educator
09:01

Problem 76

The wall of an oven used to cure plastic parts is of thickness $L=0.05 \mathrm{~m}$ and is exposed to large surroundings and air at its outer surface. The air and the surroundings are at $300 \mathrm{~K}$.
(a) If the temperature of the outer surface is $400 \mathrm{~K}$ and its convection coefficient and emissivity are
$h=20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and $\varepsilon=0.8$, respectively, what is the temperature of the inner surface if the wall has a thermal conductivity of $k=0.7 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ ?
(b) Consider conditions for which the temperature of the inner surface is maintained at $600 \mathrm{~K}$, while the air and large surroundings to which the outer surface is exposed are maintained at $300 \mathrm{~K}$. Explore the effects of variations in $k, h$, and $\varepsilon$ on (i) the temperature of the outer surface, (ii) the heat flux through the wall, and (iii) the heat fluxes associated with convection and radiation heat transfer from the outer surface. Specifically, compute and plot the foregoing dependent variables for parametric variations about baseline conditions of $k=10 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, h=20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and $\varepsilon=0.5$. The suggested ranges of the independent variables are $0.1 \leq k \leq 400 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, 2 \leq h \leq$ $200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and $0.05 \leq \varepsilon \leq 1$. Discuss the physical implications of your results. Under what conditions will the temperature of the outer surface be less than $45^{\circ} \mathrm{C}$, which is a reasonable upper limit to avoid burn injuries if contact is made?

Averell Hause
Averell Hause
Carnegie Mellon University
02:34

Problem 77

An experiment to determine the convection coefficient associated with airflow over the surface of a thick stainless steel casting involves the insertion of thermocouples into the casting at distances of 10 and $20 \mathrm{~mm}$ from the surface along a hypothetical line normal to the surface. The steel has a thermal conductivity of $15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. If the thermocouples measure temperatures of 50 and $40^{\circ} \mathrm{C}$ in the steel when the air temperature is $100^{\circ} \mathrm{C}$, what is the convection coefficient?

Naman Kumar
Naman Kumar
Numerade Educator
04:40

Problem 78

A thin electrical heating element provides a uniform heat flux $q_{o}^{\prime \prime}$ to the outer surface of a duct through which airflows. The duct wall has a thickness of $10 \mathrm{~mm}$ and a thermal conductivity of $20 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$.
(a) At a particular location, the air temperature is $30^{\circ} \mathrm{C}$ and the convection heat transfer coefficient between the air and inner surface of the duct is $100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. What heat flux $q_{o}^{\prime \prime}$ is required to maintain the inner surface of the duct at $T_{i}=85^{\circ} \mathrm{C}$ ?
(b) For the conditions of part (a), what is the temperature $\left(T_{o}\right)$ of the duct surface next to the heater?
(c) With $T_{i}=85^{\circ} \mathrm{C}$, compute and plot $q_{o}^{\prime \prime}$ and $T_{o}$ as a function of the air-side convection coefficient $h$ for the range $10 \leq h \leq 200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Briefly discuss your results.

Hariprasad Annamalai
Hariprasad Annamalai
Numerade Educator
04:40

Problem 79

A rectangular forced air heating duct is suspended from the ceiling of a basement whose air and walls are at a temperature of $T_{\infty}=T_{\text {sur }}=5^{\circ} \mathrm{C}$. The duct is $15 \mathrm{~m}$ long, and its cross section is $350 \mathrm{~mm} \times 200 \mathrm{~mm}$.
(a) For an uninsulated duct whose average surface temperature is $50^{\circ} \mathrm{C}$, estimate the rate of heat loss from the duct. The surface emissivity and convection coefficient are approximately $0.5$ and $4 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively.
(b) If heated air enters the duct at $58^{\circ} \mathrm{C}$ and a velocity of $4 \mathrm{~m} / \mathrm{s}$ and the heat loss corresponds to the result of part (a), what is the outlet temperature? The density and specific heat of the air may be assumed to be $\rho=1.10 \mathrm{~kg} / \mathrm{m}^{3}$ and $c_{p}=1008 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$, respectively.

Hariprasad Annamalai
Hariprasad Annamalai
Numerade Educator
05:56

Problem 80

Consider the steam pipe of Example 1.2. The facilities manager wants you to recommend methods for reducing the heat loss to the room, and two options are proposed. The first option would restrict air movement around the outer surface of the pipe and thereby reduce the convection coefficient by a factor of two. The second option would coat the outer surface of the pipe with a low emissivity ( $\varepsilon=0.4$ ) paint.
(a) Which of the foregoing options would you recommend?
(b) To prepare for a presentation of your recommendation to management, generate a graph of the heat loss $q^{\prime}$ as a function of the convection coefficient for $2 \leq h \leq 20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ and emissivities of $0.2$, $0.4$, and $0.8$. Comment on the relative efficacy of reducing heat losses associated with convection and radiation.

Dading Chen
Dading Chen
Numerade Educator
01:16

Problem 81

During its manufacture, plate glass at $600^{\circ} \mathrm{C}$ is cooled by passing air over its surface such that the convection heat transfer coefficient is $h=5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. To prevent cracking, it is known that the temperature gradient must not exceed $15^{\circ} \mathrm{C} / \mathrm{mm}$ at any point in the glass during the cooling process. If the thermal conductivity of the glass is $1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$ and its surface emissivity is $0.8$, what is the lowest temperature of the air that can initially be used for the cooling? Assume that the temperature of the air equals that of the surroundings.

Dominador Tan
Dominador Tan
Numerade Educator
01:31

Problem 82

The curing process of Example $1.9$ involves exposure of the plate to irradiation from an infrared lamp and attendant cooling by convection and radiation exchange with the surroundings. Alternatively, in lieu of the lamp, heating may be achieved by inserting the plate in an oven whose walls (the surroundings) are maintained at an elevated temperature.
(a) Consider conditions for which the oven walls are at $200^{\circ} \mathrm{C}$, airflow over the plate is characterized by $T_{\infty}=20^{\circ} \mathrm{C}$ and $h=15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and the coating has an emissivity of $\varepsilon=0.5$. What is the temperature of the plate?
(b) For ambient air temperatures of 20,40 , and $60^{\circ} \mathrm{C}$, determine the plate temperature as a function of the oven wall temperature over the range from 150 to $250^{\circ} \mathrm{C}$. Plot your results, and identify conditions for which acceptable curing temperatures between 100 and $110^{\circ} \mathrm{C}$ may be maintained.

Mayukh Banik
Mayukh Banik
Numerade Educator
01:31

Problem 83

The diameter and surface emissivity of an electrically heated plate are $D=300 \mathrm{~mm}$ and $\varepsilon=0.80$, respectively.
(a) Estimate the power needed to maintain a surface temperature of $200^{\circ} \mathrm{C}$ in a room for which the air and the walls are at $25^{\circ} \mathrm{C}$. The coefficient characterizing heat transfer by natural convection depends on the surface temperature and, in units of $\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}$, may be approximated by an expression of the form $h=0.80\left(T_{s}-T_{\infty}\right)^{1 / 3}$.
(b) Assess the effect of surface temperature on the power requirement, as well as on the relative contributions of convection and radiation to heat transfer from the surface.

Mayukh Banik
Mayukh Banik
Numerade Educator
07:25

Problem 84

Bus bars proposed for use in a power transmission station have a rectangular cross section of height $H=600 \mathrm{~mm}$ and width $W=200 \mathrm{~mm}$. The electrical resistivity, $\rho_{e}(\mu \Omega \cdot \mathrm{m})$, of the bar material is a function of temperature, $\rho_{e}=\rho_{e, o}\left[1+\alpha\left(T-T_{o}\right)\right]$, where $\rho_{e, a}=$ $0.0828 \mu \Omega \cdot \mathrm{m}, T_{o}=25^{\circ} \mathrm{C}$, and $\alpha=0.0040 \mathrm{~K}^{-1}$. The emissivity of the bar's painted surface is $0.8$, and the temperature of the surroundings is $30^{\circ} \mathrm{C}$. The convection coefficient between the bar and the ambient air at $30^{\circ} \mathrm{C}$ is $10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.
(a) Assuming the bar has a uniform temperature $T$, calculate the steady-state temperature when a current of $60,000 \mathrm{~A}$ passes through the bar.
(b) Compute and plot the steady-state temperature of the bar as a function of the convection coefficient for $10 \leq h \leq 100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. What minimum convection coefficient is required to maintain a safe-operating temperature below $120^{\circ} \mathrm{C}$ ? Will increasing the emissivity significantly affect this result?

Arun Bana
Arun Bana
Numerade Educator
02:28

Problem 85

A solar flux of $700 \mathrm{~W} / \mathrm{m}^{2}$ is incident on a flat-plate solar collector used to heat water. The area of the collector is $3 \mathrm{~m}^{2}$, and $90 \%$ of the solar radiation passes through the cover glass and is absorbed by the absorber plate. The remaining $10 \%$ is reflected away from the collector. Water flows through the tube passages on the back side of the absorber plate and is heated from an inlet temperature $T_{i}$ to an outlet temperature $T_{o}$. The cover glass, operating at a temperature of $30^{\circ} \mathrm{C}$, has an emissivity of $0.94$ and experiences radiation exchange with the sky at $-10^{\circ} \mathrm{C}$. The convection coefficient between the cover glass and the ambient air at $25^{\circ} \mathrm{C}$ is $10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$.
(a) Perform an overall energy balance on the collector to obtain an expression for the rate at which useful heat is collected per unit area of the collector, $q_{11}^{\prime \prime}$. Determine the value of $q_{u r^{\prime \prime}}$.
(b) Calculate the temperature rise of the water, $T_{o}-T_{i}$, if the flow rate is $0.01 \mathrm{~kg} / \mathrm{s}$. Assume the specific heat of the water to be $4179 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.
(c) The collector efficiency $\eta$ is defined as the ratio of the useful heat collected to the rate at which solar energy is incident on the collector. What is the value of $\eta$ ?

Ma Ednelyn Lim
Ma Ednelyn Lim
Numerade Educator
01:32

Problem 86

In analyzing the performance of a thermal system, the engineer must be able to identify the relevant heat transfer processes. Only then can the system behavior be properly quantified. For the following systems, identify the pertinent processes, designating them by appropriately labeled arrows on a sketch of the system. Answer additional questions that appear in the problem statement.
(a) Identify the heat transfer processes that determine the temperature of an asphalt pavement on a summer day. Write an energy balance for the surface of the pavement.
(b) Microwave radiation is known to be transmitted by plastics, glass, and ceramics but to be absorbed by materials having polar molecules such as water. Water molecules exposed to microwave radiation align and reverse alignment with the microwave radiation at frequencies up to $10^{9} \mathrm{~s}^{-1}$, causing heat to be generated. Contrast cooking in a microwave oven with cooking in a conventional radiant or convection oven. In each case, what is the physical mechanism responsible for heating the food? Which oven has the greater energy utilization efficiency? Why? Microwave heating is being considered for drying clothes. How would the operation of a microwave clothes dryer differ from a conventional dryer? Which is likely to have the greater energy utilization efficiency? Why?
(c) To prevent freezing of the liquid water inside the fuel cell of an automobile, the water is drained to an onboard storage tank when the automobile is not in use. (The water is transferred from the tank back to the fuel cell when the automobile is turned on.) Consider a fuel cell-powered automobile that is parked outside on a very cold evening with $T_{\infty}=-20^{\circ} \mathrm{C}$. The storage tank is initially empty at $T_{i, t}=-20^{\circ} \mathrm{C}$, when liquid water, at atmospheric pressure and temperature $T_{i, w}=50^{\circ} \mathrm{C}$, is introduced into the tank. The tank has a wall thickness $t_{t}$ and is blanketed with insulation of thickness $t_{\text {ins }}$. Identify the heat transfer processes that will promote freezing of the water. Will the likelihood of freezing change as the insulation thickness is modified? Will the likelihood of freezing depend on the tank wall's thickness and material? Would freezing of the water be more likely if plastic (low thermal conductivity) or stainless steel (moderate thermal conductivity) tubing is used to transfer the water to and from the tank? Is there an optimal tank shape that would minimize the probability of the water freezing? Would freezing be more likely or less likely to occur if a thin sheet of aluminum foil (high thermal conductivity, low emissivity) is applied to the outside of the insulation?
(d) Your grandmother is concerned about reducing her winter heating bills. Her strategy is to loosely fit rigid polystyrene sheets of insulation over her double-pane windows right after the first freezing weather arrives in the autumn. Identify the relevant heat transfer processes on a cold winter night when the foamed insulation sheet is placed (i) on the inner surface and (ii) on the outer surface of her window. To avoid condensation damage, which configuration is preferred? Condensation on the window pane does not occur when the foamed insulation is not in place.
(e) There is considerable interest in developing building materials with improved insulating qualities. The development of such materials would do much to enhance energy conservation by reducing space heating requirements. It has been suggested that superior structural and insulating qualities could be obtained by using the composite shown. The material consists of a honeycomb, with cells of square cross section, sandwiched between solid slabs. The cells are filled with air, and the slabs, as well as the honeycomb matrix, are fabricated from plastics of low thermal conductivity. For heat transfer normal to the slabs, identify all heat transfer processes pertinent to the performance of the composite. Suggest ways in which this performance could be enhanced.
(f) A thermocouple junction (bead) is used to measure the temperature of a hot gas stream flowing through a channel by inserting the junction into the mainstream of the gas. The surface of the channel is cooled such that its temperature is well below that of the gas. Identify the heat transfer processes associated with the junction surface. Will the junction sense a temperature that is less than, equal to, or greater than the gas temperature? A radiation shield is a small, openended tube that encloses the thermocouple junction, yet allows for passage of the gas through the tube. How does use of such a shield improve the accuracy of the temperature measurement?
(g) A double-glazed, glass fire screen is inserted between a wood-burning fireplace and the interior of a room. The screen consists of two vertical glass plates that are separated by a space through which room air may flow (the space is open at the top and bottom). Identify the heat transfer processes associated with the fire screen.
(h) A thermocouple junction is used to measure the temperature of a solid material. The junction is inserted into a small circular hole and is held in place by epoxy. Identify the heat transfer processes associated with the junction. Will the junction sense a temperature less than, equal to, or greater than the solid temperature? How will the thermal conductivity of the epoxy affect the junction temperature?

Aadit Sharma
Aadit Sharma
Numerade Educator
05:41

Problem 87

In considering the following problems involving heat transfer in the natural environment (outdoors), recognize that solar radiation is comprised of long and short wavelength components. If this radiation is incident on a semitransparent medium, such as water or glass, two things will happen to the nonreflected portion of the radiation. The long wavelength component will be absorbed at the surface of the medium, whereas the short wavelength component will be transmitted by the surface.
(a) The number of panes in a window can strongly influence the heat loss from a heated room to the outside ambient air. Compare the single- and double-paned units shown by identifying relevant heat transfer processes for each case.
(b) In a typical flat-plate solar collector, energy is collected by a working fluid that is circulated through tubes that are in good contact with the back face of an absorber plate. The back face is insulated from the surroundings, and the absorber plate receives solar radiation on its front face, which is typically covered by one or more transparent plates. Identify the relevant heat transfer processes, first for the absorber plate with no cover plate and then for the absorber plate with a single cover plate.
(c) The solar energy collector design shown in the schematic has been used for agricultural applications. Air is blown through a long duct whose cross section is in the form of an equilateral triangle. One side of the triangle is comprised of a double-paned, semitransparent cover; the other two sides are constructed from aluminum sheets painted flat black on the inside and covered on the outside with a layer of styrofoam insulation. During sunny periods, air entering the system is heated for delivery to either a greenhouse, grain drying unit, or storage system.
Identify all heat transfer processes associated with the cover plates, the absorber plate(s), and the air.
(d) Evacuated-tube solar collectors are capable of improved performance relative to flat-plate collectors. The design consists of an inner tube enclosed in an outer tube that is transparent to solar radiation. The annular space between the tubes is evacuated. The outer, opaque surface of the inner tube absorbs solar radiation, and a working fluid is passed through the tube to collect the solar energy. The collector design generally consists of a row of such tubes arranged in front of a reflecting panel. Identify all heat transfer processes relevant to the performance of this device.

Ren Jie Tuieng
Ren Jie Tuieng
Numerade Educator