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11 
Energy in Thermal Processes 
CLICKER QUESTIONS 
Question J2.01 
Description: Introducing “heat” and identifying preconceptions about it. 
Question 
Which of the following phrases best describes heat? 
1. The total energy possessed by a body 
2. The fl ow of temperature to or from a body 
3. The amount of energy dissipated by friction 
4. The total energy fl owing between two bodies at different temperatures 
5. The useful work that could be extracted from a body 
Commentary 
Purpose: To explore your preconceptions about the meaning of the word “heat,” and relate those to the 
formal physics term and concept. 
Discussion: In colloquial usage, the word “heat” is often used to refer to temperature or to the amount of 
thermal energy stored in a body. In physics, “heat” means thermal energy fl owing into or out of a body. We 
don’t use the word to refer to the thermal energy possessed by a body. (Unfortunately, many texts use the 
redundant phrase “heat fl ow.)” 
Sometimes people talk about friction converting kinetic energy into heat. This also is inaccurate; it may 
convert kinetic energy into thermal (as well as vibrational) energy, but that is only heat while it is fl owing 
between bodies. 
Key Points: 
• Heat refers to thermal energy fl owing into or out of a body, not thermal energy in general. 
• Heat is not the same thing as temperature, though they are closely related. 
For Instructors Only 
Any time you introduce new physics vocabulary that involves words students already know from other 
contexts (such as everyday language), you should investigate to fi nd out what connotations those words 
already have for students. This accomplishes two things: it alerts you to potential misunderstandings and 
misconceptions, and makes students aware of their own associations so they can be defensive about distin-guishing 
them from the proper physics meaning. 
525
526 Chapter 11 
Question J2.02 
Description: Introducing and distinguishing heat capacity and specifi c heat. 
Question 
Two objects made from the same material have different masses and different initial temperatures as shown. 
If the bodies are placed in thermal contact, the fi nal equilibrium temperature is most nearly: 
2 
1 
2M 
M 
20° C 60° C 
1. 27°C 
2. 33°C 
3. 40°C 
4. 47°C 
5. None of the above 
6. Cannot be determined 
Commentary 
Purpose: To understand heat capacity, distinguish it from specifi c heat, and apply it to thermal 
equilibration. 
Discussion: When the objects are placed in thermal contact, heat will fl ow from the warmer one to the 
colder. As it does, the warmer one will cool down and the colder one will warm up. In this question, 
the warmer one is larger and has more material to cool down, so its temperature will not change as rapidly 
as the smaller one’s will. 
The concept of “heat capacity” quantifi es this. If the two objects are made from the same material, they 
have the same specifi c heat: the amount of heat required to change the temperature of 1 g of the material 
by 1°C. However, the heat capacity of an object is the heat required to change the temperature of the entire 
object by 1°C. So, if the objects are made of the same material and object 2 has twice the mass, it must 
have twice the heat capacity. 
This means that for every degree that object 2 cools, the heat transferred will warm object 1 by two 
degrees. The initial temperature difference is 40°C. Object 1 will warm up by 23 of that, and object 2 will 
cool by 13 of it. Thus, the fi nal temperature must be about 47°C: answer (4). 
Key Points: 
• When two objects are placed in thermal equilibrium, the thermal energy lost by one is gained by the 
other. It is not true that the temperature lost by one is gained by the other. Energy, not temperature, is 
conserved. 
• Make sure you understand the difference between specifi c heat and heat capacity.
Energy in Thermal Processes 527 
• An object’s heat capacity is the heat required to change its temperature by 1°C. 
• A material’s specifi c heat is the heat required to change the temperature of 1 g of if by 1°C. 
• The heat capacity of an object made of one material is its mass times the material’s specifi c heat. 
For Instructors Only 
This question is designed to confront and resolve confusion between heat capacity and specifi c heat. 
A related concept that you may want to connect to is “molar specifi c heat”, the heat required to change the 
temperature of one mole of a material by 1°C. 
Answer (1) is the sum of the initial temperatures divided by three (the mass in units of M ), a misguided 
attempt at averaging. 
Answer (2) indicates an error translating the conceptual representation to the algebraic: students have taken 
the factor of two for mass mass into account, but applied it to the wrong side of the equation (a common 
and well-documented error in forming algebraic representations of verbal statements). 
Answer (3)—typically the most common—is the unweighted average of the starting temperatures. Students 
can arrive at this by simplistically splitting the difference, or by reasoning with the specifi c heat instead of 
the heat capacity. In either case, the are neglecting the difference in the objects’ masses. 
The question does not explicitly state that the material’s specifi c heat is independent of temperature. We 
are assuming it is. If students do not detect and articulate this ambiguity, you can raise it yourself and ask 
how a temperature-dependent specifi c heat might affect the answer. (Even if you don’t wish to spend time 
discussing the question, you can mention it as an aside so that top-end students have something extra to 
keep engaged with. We fi nd it productive to throw the bright and easily bored an extra bone to chew on now 
and then.) 
Question J2.03 
Description: Understanding temperature and heat fl ow in a familiar context, and paying attention to 
environmental effects. 
Question 
To have your coffee be as hot as possible when you drink it later, when should you add room temperature 
cream? 
1. As soon as the coffee is served 
2. Just before you drink it 
3. Either; it makes no difference. 
4. It is impossible to determine. 
Commentary 
Purpose: To explore energy exchanges in everyday situations. 
Discussion: When two liquids are mixed, such as the coffee and the cream in this situation, the hot coffee 
loses some energy and the cream gains the same amount of energy, so that they come to some fi nal temper-ature 
between the two initial temperatures. The specifi c fi nal temperature depends upon the masses, specifi c 
heats, and initial temperatures of the coffee and cream.
528 Chapter 11 
If the coffee and cream existed in isolation, and no heat could leave the system, it wouldn’t matter when 
they were mixed. However, the hot coffee—before or after cream is added—is constantly losing heat to 
the surrounding air. The coffee will take a long time to reach room temperature, but we know that it will 
eventually occur. The rate at which energy is exchanged depends on the difference in temperature between 
the coffee and the air: The larger the difference in temperature, the larger the rate of energy exchange. If 
the cream is added early, the temperature difference between coffee and air is smaller than if it is not, so 
less heat escapes to the air. The coffee will be hotter if you add the cream right away. 
Key Points: 
• The rate at which heat fl ows between two objects or substances is proportional to the temperature 
difference between them. 
• When two substances of different temperatures are mixed, the new, combined temperature is 
somewhere between the initial temperatures. 
• Sometimes heat lost to or gained from a system’s environment is signifi cant in analyzing a situation. 
For Instructors Only 
Many students will neglect the effect of the environment on the temperature of the coffee. In some 
ways, they have been taught to neglect the environment. Some students will think that the answer is 
impossible to determine, because they recognize the importance of the environment but have not been 
taught how to compute its effect. 
The correct answer will seem counterintuitive to some students. They simply will not believe that to keep 
something hot, you need to cool it down fi rst! 
Question J2.04 
Description: Reasoning about temperature and thermal equilibrium. 
Question 
Two identical thermodynamic systems, one at T1 and the other at T2, are placed in thermal contact. When 
they reach thermal equilibrium, what is true about the fi nal temperature? 
1. Tfinal  1 (T + T ) 
2 1 2 
2. T = 1 ( T + T ) 
final2 1 2 
3. T  1 ( T + T ) 
final2 1 2 
4. Not enough information 
Commentary 
Purpose: To develop your ability to reason about temperature and thermal equilibrium. 
Discussion: You might think it is impossible to determine, because you are not told enough about the 
systems, but it turns out that you know all that you need to know. Since the systems are “identical,” it 
means that as they are exchanging energy by heat, their temperatures are changing by the exact same 
amount. Therefore, when they are done, their temperatures must also have changed by the exact same 
amount, which means they end up at the average of their temperatures: answer (2).
Energy in Thermal Processes 529 
Let’s assume that T1 is smaller than T2. Mathematically, the change in temperature of the cooler 
system is 1 
(T + T ) − T = 2 (T2 − T1). The change in temperature of the warmer system is 
2 1 2 1 1 
1 
2 2 1 − ( − ) = ( − ), the same result. 
T 1 
T T T T 2 
2 1 2 
For Instructors Only 
Some students might choose the correct response for the wrong reasons, so it is useful to fi nd out why 
students are choosing their answers. 
Some of the more thoughtful students will think that it is impossible to determine, either because so little is 
said about the systems, or because the correct answer just seems too simple and they suspect a catch. 
(Actually, we are implicitly assuming that the systems have a constant heat capacity. Since the heat lost 
by one system must equal the heat gained by the other, if heat capacity varies with temperature, the fi nal 
temperature is not necessarily midway between T1 and T1. Answer (4) is defensible with this reasoning.) 
Question J9.01 
Description: Understanding Stefan’s law. 
Texts: Principles of Physics, Scientists  Engineers 
Question 
By what factor would the total power from a black body be modifi ed if the surface area were to decrease by 
a factor of two while the temperature was doubled? 
1. 116 
2. 18 
3. 14 
4. 1 
5. 4 
6. 8 
7. None of the above 
8. Cannot be determined 
Commentary 
Purpose: To check your understanding of the primary quantities upon which black-body radiation power 
depends. 
Discussion: Along with conduction and convection, radiation is one of the important energy fl ow 
processes, and you should be familiar with the primary factors governing the rate at which energy is 
radiated. According to the Stefan-Boltzmann law, the power radiated from a black body is proportional to 
the surface area of the body and to the fourth power of the body’s Kelvin temperature. Thus, if the 
temperature is doubled and the surface area halved, the power radiated would change by 242  8.
530 Chapter 11 
Key Points: 
• The power radiated from a black body is proportional to the surface area of the body. 
• The power radiated from a black body is proportional to the fourth power of the body’s Kelvin 
temperature. 
For Instructors Only 
Students frequently obtain the inverse of the correct response, obtaining 18 rather than 8. In general, it is 
important to ask students how they arrived at their answers in order to distinguish algebra mistakes from 
misremembered formulas or erroneous thinking. 
It is useful to extend the discussion of this question by contrasting radiation to the other energy fl ow 
processes. Black body radiation is unique in that the power radiated depends upon the properties of the 
body itself, not to differences between the body and its environment. 
QUICK QUIZZES 
1. (a) Water, glass, iron. Because it has the highest specifi c heat (4 186 J kg⋅°C), water has the 
smallest change in temperature. Glass is next (837 J kg⋅°C), and iron (448 J kg⋅°C) is last. 
(b) Iron, glass, water. For a given temperature increase, the energy transfer by heat is proportional 
to the specifi c heat. 
2. (b). The slopes are proportional to the reciprocal of the specifi c heat, so larger specifi c heat results 
in a smaller slope, meaning more energy to achieve a given change in temperature. 
3. (c). The blanket acts as a thermal insulator, slowing the transfer of energy by heat from the air 
into the cube. 
4. (b). The rate of energy transfer by conduction through a rod is proportional to the difference in 
the temperatures of the ends of the rod. When the rods are in parallel, each rod experiences the 
full difference in the temperatures of the two regions. If the rods are connected in series, neither 
rod will experience the full temperature difference between the two regions, and hence neither 
will conduct energy as rapidly as it did in the parallel connection. 
5. (a) 4. From Stefan’s law, the power radiated from an object at absolute temperature T is 
proportional to the surface area of that object. Star A has twice the radius and four times the 
surface area of star B. (b) 16. From Stefan’s law, the power radiated from an object having 
surface area A is proportional to the fourth power of the absolute temperature. Thus, 
P P A B B 
=σ Ae (2T )4 = 24 (σ AeT 4 
) = 16 . (c) 64. When star A has both twice the radius and twice 
B the absolute temperature of star B, the ratio of the radiated powers is 
P 
P 
A 
B 
4 
( )( ) 
= A A 
= 4 
2 B B 
4 2 
1 
4 
( A 
2 ) ( 2 
) ) = = ( )( ) = 
4 1( A 
R T 
R T B 
( ) 
B 
σ 
σ 
σ π 
σ π 
A eT 
A eT 
R T 
R 
T 
4 
B B 
2 
B 
4 
B 
2 2 64 
2 4 
2 4
Energy in Thermal Processes 531 
ANSWERS TO MULTIPLE CHOICE QUESTIONS 
1. From the mechanical equivalent of heat, 1 cal = 4.186 J. Therefore, 
. × = × ( )⎛⎝ 
3 50 10 3 50 10 
4 186 
1 
. 3 . 3 
⎞⎠ 
cal cal 
J 
cal 
= 1.47 × 104 J 
and (b) is the correct choice for this question. 
5 5 1 1 . × = ( . × )⎛ 
2. 7 80 10 7 80 10 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
J J 
cal 
4.186 J 
Cal 
cal 
186 
Cal 103 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= , so (a) is the correct choice. 
3. The required energy input is 
Q = mc(ΔT ) = (5.00 kg)(128 J kg ⋅°C)(327°C − 20.0°C) = 1 96 × 10. 5 J 
and the correct response is (e). 
4. The energy which must be added to the 0°C ice to melt it, leaving liquid at 0°C, is 
= = (2.00 kg)(3.33 × 105 J kg) = 6.66 × 105 J 
Q mLf 
1 
= − = 9 30 × 105 − 6 66 × 105 = 2 64 × 105 total . J . J . J of energy 
Once this is done, there is Q Q Q 2 1 
still available to raise the temperature of the liquid. The change in temperature this produces is 
Q 
mc f = − = = × 
ΔT T 
2 64 10 
( ) 0 
4 186 
2 
5 
°C 
J 
2.00 kg water 
. 
J kg °C 
°C 
( ⋅ ) = 31 5 . 
so the fi nal temperature is Tf= 0°C + 31.5°C = 31.5°C and the correct choice is (c). 
5. The rate of energy transfer by conduction through a wall of area A and thickness L is 
P = kA(T − T ) L h c , where k is the thermal conductivity of the material making up the wall, while 
T T h c and are the temperatures on the hotter and cooler sides of the wall, respectively. For the case 
given, the transfer rate will be 
P = 
J 
⋅ ⋅ 
⎛⎝ 
⎞⎠ 
( ) ( − ) 
( − )= × = × 
× 
0 10 48 0 
25 14 
. . 
s m °C 
m 
°C °C 
4.00 
2 
10 
3 3 
1 3 10 1 3 10 2 
m 
. J s . W 
and the (d) is the correct answer. 
6. The power radiated by an object with emissivity e, surface area A, and absolute temperature T, 
in a location with absolute ambient temperature T, is given by P =σ Ae(T 4 − T 4 
) 
00 
where σ = 5.669 6 × 10−8 W m2 ⋅K4 is a constant. Thus, for the given spherical object 
(A = 4π r2 ), we have 
P = (5 669 6 ×10−8 ⋅ )4 (2 00 )2 (0 450) 408 . . . W m K m 2 4 π K K ( ) − ( ) ⎡⎣ 
⎤⎦ 
4 4 298 
yielding P = 2.54 × 104 W, so (e) is the correct choice. 
7. The temperature of the ice must be raised to the melting point, ΔT = +20 0 . °C, before it will start 
to melt. The total energy input required to melt the 2.00-kg of ice is 
= ( ) + = ( ) ( ⋅ ) ice kg J kg °C ° Δ 2 00 2 090 20 0 . . C J kg J ( ) + × ⎡⎣ 
Q mc T mLf 
⎤⎦ 
3.33 105 = 7.50 × 105 
The time the heating element will need to supply this quantity of energy is 
Δt 
Q = = × 
× 
= ⎛ 
P 
7 50 10 
10 
750 
. 5 J 
1.00 J s 
s 
1 min 
3 ⎝ 60 s 
⎞⎠ 
= 12 5. min 
making (d) the correct choice.
532 Chapter 11 
8. We use −Q = Q hot cold or −m c (T − T ) = m c (T − T ) x x f x,i w w f w,i to compute the specifi c heat of 
the unknown material and fi nd 
c 
m c T T 
m T T x 
w w f wi 
x f xi 
= 
( − ) 
, ( ) 
= − ( − ) , 
( ⋅ )( − ) 
( ) − 
0.400 kg 4 186 J kg °C °C °C 
J kg °C ( ) = × ⋅ 
0.250 kg °C 
36 0 20 0 
36 0 9 
. . 
. 5 0 
1 82 103 
. 
. 
°C 
which is a match for the specifi c heat of Beryllium, so (b) is the correct choice. 
9. Since less energy was required to produce a 5°C rise in the temperature of the ice than was 
required to produce a 5°C rise in temperature of an equal mass of water, we conclude that the 
specifi c heat of ice (c = Q m(ΔT )) is less than that of water. Thus, choice (d) is correct. 
10. With e e A B = , r r A B = 2 , and T T A B = 2 , the ratio of the power output of A to that of B is 
P 
P 
A 
B 
4 
A A A 
B B B 
A A 
B B 
A 
B 
A e T 
A e T 
r T 
r T 
r 
r 
σ 
σ 
π 
π 
= = = 
4 
2 4 
2 4 
4 
4 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= ( ) ( ) = ( ) = 
2 4 
2 4 6 2 2 2 64 
T 
T 
A 
B 
making (e) the correct choice. 
11. By agitating the coffee inside this sealed, insulated container, the person is raising the internal 
energy of the coffee, which will result is a rise in the temperature of the coffee. However, doing 
this for only a few minutes, the temperature rise will be quite small. The correct response to this 
question is (d). 
12. One would like the poker to be capable of absorbing a large amount of energy, but undergo a 
small rise in temperature. This means it should be made of a material with a high specifi c heat 
capacity. Also, it is desirable that energy absorbed by the end of the poker in the fi re be conducted 
to the person holding the other end very slowly. Thus, the material should have a low thermal 
conductivity. The correct choice is (d). 
ANSWERS TO EVEN-NUMBERED CONCEPTUAL QUESTIONS 
2. In winter the produce is protected from freezing. The specifi c heat of Earth is so high that soil 
freezes only to a depth of a few inches in temperate regions. Throughout the year the temperature 
will stay nearly constant day and night. Factors to be considered are the insulating properties of 
the soil, the absence of a path for energy to be radiated away from or to the vegetables, and the 
hindrance of the formation of convection currents in the small, enclosed space. 
4. The high thermal capacity of the barrel of water and its high heat of fusion mean that a large 
amount of energy would have to leak out of the cellar before the water and produce froze solid. 
Evaporation of the water keeps the relative humidity high to protect foodstuffs from drying out. 
6. Yes, if you know the specifi c heat of zinc and copper, you can determine the relative fraction 
of each by heating a known weight of pennies to a specifi c initial temperature, say 100° C, then 
dump them into a known quantity of water, at say 20° C. The equation for conservation of energy 
will be 
m xc x T m c pennies water wa [ ⋅ + ( − ) ]( ° − ) = Cu Zn 1 c 100 C ter (T − 20°C) 
The equilibrium temperature, T, and the masses will be measured. The specifi c heats are known, 
so the fraction of metal that is copper, x, can be computed.
Energy in Thermal Processes 533 
8. Write mwatercwater (1°C) = (ρairV )cair (1°C), to fi nd 
V 
( × ) water water 
m c 
= = 
c 
air air 
kg J kg 
ρ 
1.0 103 (4 186 ⋅⋅ ° 
C 
) 
( )( × 
× ⋅ ° 
)= m 3 
kg m J kg C 
3 
1 3 1 0 10 
3 2 10 3 
3 
. . 
. 
10. The black car absorbs more of the incoming energy from the Sun than does the white car, making 
it more likely to cook the egg. 
12. Keep them dry. The air pockets in the pad conduct energy slowly. Wet pads absorb some energy 
in warming up themselves, but the pot would still be hot and the water would quickly conduct a 
lot of energy to your hand. 
PROBLEM SOLUTIONS 
11.1 As mass m of water drops from top to bottom of the falls, the gravitational potential energy 
given up (and hence, the kinetic energy gained) is Q = mgh. If all of this goes into raising the 
temperature, the rise in temperature will be 
ΔT 
= = = ( 
Q 
mc 
mgh 
mc 
)( ) 
water water 
9 . 
80 m s2 807 m 
4 18 
6 
1 89 
J kg °C 
°C 
⋅ 
= . 
and the fi nal temperature is T T T f i = + Δ = 15.0°C+1.89°C = 16.9°C . 
11.2 Q = mc(ΔT ) = (1.50 kg)(230 J kg ⋅°C)(150°C − 20.0°C) = 4.49 × 104 J = 44.9 kJ 
11.3 The mass of water involved is 
ρ 103 kg (4 00 × 1011 ) = 4 00 × 1014 
m V = =⎛⎝ 
⎞⎠ 
m 
. 3 . g 
m k 3 
(a) Q = mc(ΔT ) = (4.00 × 1014 kg)(4 186 J kg ⋅°C)(1.00°C) = 1.67 × 1018 J 
(b) The power input is P = 1 000 MW= 1.00 ×109 J s , so, 
t 
Q = = × 
18 ⎛ 
1 
9 
× × 
P 
1 . 
67 10 
1 . 
00 10 
J 
J s 
yr 
3.156 10 s 7 ⎝ ⎜ 
⎞ 
⎠ ⎟= 52 9 . yr 
11.4 The change in temperature of the rod is 
ΔT 
= = × 
Q 
mc 
4 
1 
( )( ) = 900 
31 7 
.00 10 J 
° 
0.350 kg J kg C 
. °C 
and the change in the length is 
ΔL = L (ΔT ) 
= × ( ) ⎡⎣ 
− − ( ) 
⎤⎦ 
α 0 
6 1 24 10 °C 20.0 cm (31.7°C) = 1.52 × 10−2 cm = 0.152 mm 
Q 
mc f = − = =( 
11.5 ΔT T 
750 
0 168 
25 
°C 
)( ⋅ ) cal 
75 g . cal g °C 
= 60°C 
so 
Tf= 25°C + 60°C = 85°C
534 Chapter 11 
11.6 (a) Q = 
⎛ 
103 4 186 
⎞ 540 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎛ 
⎝ ⎜ 
Cal 
cal 
1 Cal 
J 
. 
1 cal 
⎠ ⎟ 
= 2.3 × 106 J 
(b) The work done lifting her weight mg up one stair of height h is W mgh 1 = . Thus, the total 
work done in climbing N stairs is W = Nmgh, and we have W = Nmgh = Q or 
N 
= = × 
Q 
mgh 
2 3 10 
( )( = 9 80 )( 0 15 
) 2 
. 6 
J 
. . 
55 kg m s2 m .8 × 104 stairs 
(c) If only 25% of the energy from the donut goes into mechanical energy, we have 
N 
0 25 0 25 2 8 104 . 
0 25 
Q 
= × mgh 
Q 
mgh 
= = 
⎛ 
. . ( . stairs) = 7.0 × 103 stairs 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
net = Δ = ( − ) = ( kg) ( m s) − 1 
2 2 v v . ⎡⎣ 
11.7 (a) W KE mf 
2 
1 
2 
2 75 11 0 0 
0 
⎤⎦ 
= 4.54 × 103 J → 4.5 × 103 J 
W 
× J 
(b) P= net = = × = t 
5.0 s 
J s W 
Δ 
4 54 10 
9 1 10 910 
3 
. 2 
. 
(c) If the mechanical energy is 25% of the energy gained from converting food energy, then 
W Q net = 0.25(Δ ) and P = 0.25 (ΔQ) Δt, so the food energy conversion rate is 
Δ 
Q 
t 
Δ 
P = 
0 25 
= =⎛⎝ 
⎞⎠ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
910 1 
. 
J s 
0.25 
Cal 
4 186 J 
0.87 Cal s 
(d) The excess thermal energy is transported by conduction and convection to the surface of the 
skin and disposed of through the evaporation of sweat. 
11.8 (a) The instantaneous power is P = Fv , where F is the applied force and v is the instantaneous 
velocity. 
(b) From Newton’s second law, F ma net = , and the kinematics equation v = v + 0 at 
with v0 = 0, the instantaneous power expression given above may be written as 
P = Fv = (ma)(0 + at ) or P = ma2t 
(c) a 
= = − 
Δ v v 0 
= 11 0 
= 
Δ 
t t 
− 
0 
5 00 
2 20 
. 
. 
. 
m s 
s 
m s2 
(d) P = ma2t = ( )( ) t = ( ⋅ )⋅ 2 75.0 kg 2.20 m s2 363 kg m2 s4 t = (363 W s)⋅ t 
(e) Maximum instantaneous power occurs when t = t = max 5.00 s, so 
Pmax = (363 J s2 )(5.00 s) = 1.82 × 103 J s 
If this corresponds to 25.0% of the rate of using food energy, that rate must be 
Δ 
Δ 
Q 
t 
= P = × ⎛ max 
. 
1 . 
82 10 
0 250 . 
3 J s Cal 
0 250 
1 
4 186 
J ⎝ ⎜ 
⎞ 
⎠ ⎟ 
= 1.74 Cal s 
11.9 The mechanical energy transformed into internal energy of the bullet is 
Q KE m m i i i = ( ) = ( ) = 12 
12 
12 
v v2. Thus, the change in temperature of the bullet is 
2 14 
ΔT 
i = = = ( 
Q 
mc 
m 
mc 
) 
( ⋅ ) = 
14 
2 2 300 
4 1 
v 
lead 
m s 
28 J kg °C 
176°C
Energy in Thermal Processes 535 
11.10 The internal energy added to the system equals the gravitational potential energy given up by the 
2 falling blocks, or Q = ΔPEg = 2mbgh. Thus, 
ΔT 
2 2 1.50 kg)(9.80 m s2 ) 3.00 m 
= = = ( 
Q 
m c 
m gh 
b 
m c w w 
w w 
kg J kg °C 
C 
( ) 
( )( ⋅ ) = 
0 200 4 186 
0 105 
. 
. ° 
11.11 The quantity of energy transferred from the water-cup combination in a time interval of 
1 minute is 
Q mc mc T = ( ) + ( ) ⎡⎣ 
⎤⎦ 
( ) 
water cup 
= ( kg 
) 
Δ 
0.800 4 186 
J 
kg C 
0.200 900 
kg 
J 
⎛ 
⋅ kg C 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
+ ( ) ⋅ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎡ 
⎣ ⎢ 
° ° 
⎤ 
⎦ ⎥ 
(1.5°C) = 5.3 × 103 J 
The rate of energy transfer is 
P= = × = = Q 
Δt 
5 3 10 
88 88 
. 3 J 
60 s 
J 
s 
W 
11.12 (a) The mechanical energy converted into internal energy of the block is 
Q KE m i i = = 0 85 0 85 12 
. ( ) . ( v2 ). The change in temperature of the block will be 
ΔT 
i = = ( ) = ( ) 
Q 
mc 
0 85 m 
0 85 3 0 
mc 
Cu Cu 
m s 
87 
2 3 
12 
2 2 . v . . 
J kg C 
C 
( ⋅ )= × − 
° 
9.9 10 3 ° 
(b) The remaining energy is absorbed by the horizontal surface on which the block slides. 
11.13 From ΔL =α L (ΔT ) 0 , the required increase in temperature is found, using Table 10.1, as 
Δ Δ 
T 
= = × 
L 
L 
− 
3 0 10 
10 13 
( × ( ) ) 
α − 6 
− steel 
m 
0 11 °C 
3 
1 
. 
( ) 
°C yd 
yd 
3.0 ft 
ft 
1 m 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎛ 
⎞ 
⎟ 
⎠ ⎜⎝ = 
1 3 281 
23 
. 
The mass of the rail is 
m 
= =( )( ) ⎛ 
w 
g 
⎝ ⎜ 
70 lb yd 13 yd 
9.80 m s 
4.448 N 
2 1 lb 
⎞ 
⎠ ⎟ 
= 4.1 × 102 kg 
so the required thermal energy (assuming that c c steel iron = ) is 
Q = mc ( T ) = ( × )( ⋅ )( steel Δ 4.1 102 kg 448 J kg °C 23°C) = 4.2 × 106 J 
11.14 (a) From the relation between compressive stress and strain, F A = Y (ΔL L ) 0 , where Y is 
Young’s modulus of the material. From the discussion on linear expansion, the strain due to 
thermal expansion can be written as (ΔL L ) (ΔT ) 0 =α , where α is the coeffi cient of linear 
expansion. Thus, the stress becomes F A = Y [α (ΔT )] . 
(b) If the concrete slab has mass m, the thermal energy required to produce a change in 
temperature ΔT is Q = mc(ΔT ) where c is the specifi c heat of concrete. Using the result 
from part (a), the absorbed thermal energy required to produce compressive stress F A is 
Q mc 
F A 
Y 
= ⎛⎝ 
⎞⎠ 
α 
or Q 
mc 
Y 
F 
A 
= ⎛⎝ 
⎞⎠ 
α 
continued on next page
536 Chapter 11 
(c) The mass of the given concrete slab is 
m V = = × ( ) × ( )( ) − ρ 2 40 10 4 00 10 1 00 1 3 2 . . . . kg m m m 3 00 96 0 m kg ( ) ⎡⎣ 
⎤⎦ 
= . 
(d) If the maximum compressive stress concrete can withstand is F A = 2.00 × 107 Pa, the 
maximum thermal energy this slab can absorb before starting to break up is found, using 
Table 10.1, to be 
F 
A max 
Q 
mc 
Y 
max 
. 
. 
= ⎛⎝ 
⎞⎠ 
= ( )( ⋅ ) 
α 
96 0 880 
2 1 
kg J kg °C 
( )( ) ( × 7 
) = × 10 12 × 10− ( ) − 
2 00 10 6 10 6 1 
Pa °C 
. Pa .7 × 106 J 
(e) The change in temperature of the slab as it absorbs the thermal energy computed above is 
ΔT 
= = × 
Q 
mc 
6 7 10 
( )( ) = 79 
° 880 
⋅ . 6 J 
96.0 kg J kg °C 
C 
(f ) The rate the slab absorbs solar energy is 
P P absorbed solar = 0.5 = 0.5(1.00 × 103 W) = 5 × 102 J s 
so the time required to absorb the thermal energy computed in (d) above is 
t 
Q = = × 
. 6 1 
× 
⎛ 
⎝ ⎜ 
⎞ 
Pabsorbed 
2 
J 
5 Js 
h 
3 600 s 
6 7 10 
10 
⎠ ⎟ 
∼ 4 h 
11.15 When thermal equilibrium is reached, the water and aluminum will have a common temperature 
of Tf = 65 0 . °C. Assuming that the water-aluminum system is thermally isolated from the 
environment, Q Q cold hot = − , so mc T T m c T T w w f iw f i ( − ) = − ( − ) , Al Al ,Al , or 
m 
Al Al ,Al −( kg) 
m c T T 
c T T w 
f i 
w f iw 
= 
− ( − ) 
( − ) = 
, 
( ⋅ )( − ) 
1.85 900 65 0 
J kg °C °C 150°C 
65 0 
( 4 186 J kg ⋅ °C 
) 
. 
. °C °C 
kg 
( − ) = 
25 0 
0 845 
. 
. 
11.16 If N pellets are used, the mass of the lead is Nmpellet . Since the energy lost by the lead must equal 
the energy absorbed by the water, 
Nm c T mc T pellet lead water (Δ ) = [ (Δ )] 
or the number of pellets required is 
N 
= w w w ( ) 
Δ 
Δ pellet lead lead 
0.500 kg 4 186 25 0 20 0 
m c T 
m c T 
= ( ) 
( J kg ⋅ C )( C − C 
) 
128 
( 1.00 × 10-3 kg 
) 
° . ° . ° 
( J kg⋅ C)( C− C) = 
° 200° 25 0° 
467 
.
Energy in Thermal Processes 537 
11.17 The total energy absorbed by the cup, stirrer, and water equals the energy given up by the silver 
sample. Thus, 
mccAl mscCu mwcw T w mc T Ag [ + + ](Δ ) = [ Δ ] 
Solving for the mass of the cup gives 
m 
= ( m c 
)( c 
)− − 
s w w T 
T 
m c m c c 
w 
⎡ 
⎣ ⎢ 
⎤ 
⎦ ⎥ 
1 
Al 
Ag Ag 
Ag 
Cu 
Δ 
Δ 
, 
or 
mc = ( )( ) ( − ) 
g 40 g (387) − ( )( ) ⎡ 
( − ) 1 − ( ) 
900 
400 234 
87 32 
32 27 
⎣ ⎢ 
⎤ 
225 g 4 186 = 80 g 
⎦ ⎥ 
11.18 The mass of water is 
m V w w w = ρ = (1.00 g cm3 )(100 cm3 ) = 100 g = 0.100 kg 
For each bullet, the energy absorbed by the bullet equals the energy given up by the water, so 
m c T m c T b b w w ( − 20°C) = (90°C − ). Solving for the fi nal temperature gives 
T 
= m c ( 90°C ) + m c 
( 20°C 
) 
w w b b 
+ 
m c m c 
w w b b 
. 
For the silver bullet, m c b b = 5.0 × 10−3 kg and = 234 J kg ⋅°C, giving 
Tsilver 
°C 
= 
(0.100)(4 186)(90 ) + (5.0 × 10−3 )(234) 20 
89 8 3 
0 100 4 186 5 0 10 234 
°C 
°C 
( ) 
( )( ) + ( × )( ) = . . − 
. 
For the copper bullet, m c b b = 5.0 × 10−3 kg and = 387 J kg ⋅°C, which yields 
Tcopper 
°C 
= 
(0.100)(4 186)(90 ) + (5.0 × 10−3 )(387) 20 
89 7 3 
0 100 4 186 5 0 10 387 
°C 
°C 
( ) 
( )( ) + ( × )( ) = . . − 
. 
Thus, the copper bullet wins the showdown of the water cups. 
11.19 The total energy given up by the copper and the unknown sample equals the total energy 
absorbed by the calorimeter and water. Hence, 
m c T m c T mc m c T Cu Cu Cu unk unk unk c Al w w w Δ + Δ = [ + ](Δ ) 
Solving for the specifi c heat of the unknown material gives 
c 
m c m c T m c T 
c w w w 
m T 
unk 
Al Cu Cu Cu 
unk unk 
= 
[ + ](Δ ) − Δ 
Δ 
, or 
{ ( ) 
= g J kg °C g ( )( ) ( )( ⋅ ) + 1 
cunk g °C 
70 80 
100 900 250 ( ) ⋅ ( ) ⎡⎣ 
⎤⎦ 
− ( ) 
4 186 10 
50 
J kg °C °C 
g (387 J kg ⋅°C)(60°C)} = 1.8 × 103 J kg ⋅°C
538 Chapter 11 
11.20 The energy absorbed by the water equals the energy given up by the iron and they come to 
thermal equilibrium at 100°F. Thus, considering cooling 1.00 kg of iron, we have 
mwcw (ΔT )w = m c ΔT Fe Fe Fe or m 
1.00 kg c Δ 
T 
Fe Fe = ( ) 
( ) 
c T w 
Δ 
w w 
giving 
mw = 
( ) 
(1 00 )(448 ⋅ )(500 − 100 ) 1 9 
5 . kg J kg °C °F °F °C °F 
( = 
4 186 J kg ⋅ °C )( 100 °F − 75 °F ) ( 1 
°C °F 
) 1 7 
9 
5 
. kg 
11.21 Since the temperature of the water and the steel container is unchanged, and neither substance 
undergoes a phase change, the internal energy of these materials is constant. Thus, all the energy 
given up by the copper is absorbed by the aluminum, giving m c T m c T Al Al Al Cu Cu Cu (Δ ) = Δ , or 
m 
c 
c 
T 
T 
= 
Cu 
Cu m Al 
Al 
Cu 
Al 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
( ) 
⎡ 
⎣ ⎢ 
⎤ 
⎦ ⎥ 
= ⎛ 
Δ 
Δ 
387 
⎝ 900 
⎞⎠ 
− 
− 
⎛⎝ 
200 2 6 102 ° ° 
° ° 
( )= × 85 
25 
⎞⎠ 
C 25C 
C 5.0 C 
g . g = 0.26 kg 
11.22 The kinetic energy given up by the car is absorbed as internal energy by the four brake drums 
(a total mass of 32 kg of iron). Thus, ΔKE = Q = m c (ΔT ) drums Fe or 
ΔT 
1 v ( kg )( m s 
) 
= i = m 
2 
m c 
2 1 500 30 
32 
2 1 
2 
( )( ) = 
°C ⋅ car 
drums Fe 
448 
kg J kg °C 
47 
11.23 (a) Assuming that the tin-lead-water mixture is thermally isolated from the environment, 
we have 
Q Q cold hot = − or m c T T m c T T m c T T w w f iw f i f i ( − ) = − ( − )− − , Sn Sn ,Sn Pb Pb ,Pb ( ) 
and since m m m Sn Pb metal = = = 0.400 kg and T T T i, i, . Sn Pb hot = = = 60 0°C, this yields 
T 
m c T m c c T 
w w iw 
( + ) 
m c m c f 
w w 
= 
+ ( + ) 
+ 
, metal Sn Pb hot 
c 
metal Sn Pb 
= ( )( ⋅ )( ) + 
1.00 kg 4 186 J kg °C 20.0 °C 
0.400 227 128 60 0 
1 00 
kg J kg °C J kg °C °C 
kg 
( )( ⋅ + ⋅ )( . ) 
( . )(4 186 J kg ⋅°C) + (0.400 kg)(227 J kg ⋅°C + 128 J kg ⋅°C) 
yielding Tf = 21 3 . °C 
(b) If an alloy containing a mass mSn of tin and a mass mPb of lead undergoes a rise in tempera-ture 
ΔT, the thermal energy absorbed would be Q = Q +Q Sn Pb, or 
m m c T m c T m c T Sn Pb alloy Sn Sn Pb Pb ( + ) ( Δ ) = ( Δ )+ ( Δ ) giving c 
m c m c 
Sn Sn Pb Pb 
m m alloy 
Sn Pb 
= 
+ 
+ 
If the alloy is a half-and-half mixture, so m m Sn Pb = , this reduces to c c c alloy Sn Pb = ( + ) 2 and 
yields 
calloy 
= 227 J kg ⋅ °C + 128 
J kg ⋅ °C 
= J kg ⋅ °C 2 
178 
continued on next page
Energy in Thermal Processes 539 
(c) For a substance forming monatomic molecules, the number of atoms in a mass equal to the 
molecular weight of that material is Avogadro’s number, NA. Thus, the number of tin atoms 
in mSn = 0.400 kg = 400 g of tin with a molecular weight of MSn = 118.7 g mol is 
N 
m 
M 
Sn 
NSn A 
Sn 
g 
118.7 g mol 
= 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
400 
(6.02 × 1023 mol−1 ) = 2.03 × 1024 
and, for the lead, 
N 
m 
M 
Pb 
NPb A 
Pb 
g 
207.2 g mol 
= 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
400 
(6.02 × 1023 mol-1 ) = 1.16 × 1024 
(d) We have 
N 
N 
Sn 
Pb 
= × 
= 2 03 10 
1 16 10 
× 
1 75 
24 
24 
. 
. 
. 
and observe that 
c 
c 
Sn 
Pb 
= ⋅ 
227 
J kg °C 
= 128 
J kg °C 
⋅ 
1.77 
from which we conclude that the specific heat of an element is proportional to the 
number of atoms per unit mass of that element. 
11.24 Assuming that the unknown-water-calorimeter system is thermally isolated from the 
environment, −Q = Q hot cold, or −m c T − T = m c T − T + m c T − T x x f ix ww f iw f i ( ) ( ) ( , , Al Al ,Al ) 
and, since T T T i,w i, = = = . Al cold 25 0°C, we have c m c m c T T m T T x w w f x i x f = ( + )( − ) ( − ) Al Al cold , 
or 
cx = 
⋅ ( ) ⎡⎣ 
(0.285 kg)(4 186 J kg ⋅°C) + (0.150 kg) 900 J kg °C °C 
kg °C 
⎤⎦ 
( − ) 
( ) − 
32 0 25 0 
0 125 95 0 32 
. . 
. ( . .0°C) 
yielding cx= 1.18 × 103 J kg ⋅°C . 
11.25 Remember that energy must be supplied to melt the ice before its temperature will begin to rise. 
Then, assuming a thermally isolated system, Q Q cold hot = − , or 
m L m c T m c T ice f ice water f w water f + ( − 0°C) = − ( − 25°C) 
and 
T 
25°C (825 g )(4 186 J kg ⋅°C)(25°C) − (75 g )(3.33 × 105 J kg) 
m c m L 
w f 
m m c f 
w 
= 
( ) − 
water ice 
( + ) = ice water 
(75 g + 825 g )(4 186 J kg ⋅°C) 
yielding Tf = 16°C .
540 Chapter 11 
11.26 The total energy input required is 
Q = ( energy to melt 50 g of ice 
) 
+ 
energy ( to warm 50 g of water to 100°C) 
+ energy to vaporize 5.0 g water 
50 g 
( ) 
= ( ) L c L f + (50 g) (100 C − 0 C) + (5.0 g) water ° ° v 
Thus, 
⎛ 
Q = ( ) × 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
0.050 kg 
J 
kg 
3.33 105 
+(0.050 kg) 
J 
k 
4 186 
g °C 
100°C 0°C 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
( − ) 
⎛ 
+ ( × ) × 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
5.0 10− kg 
J 
kg 
3 2.26 106 
which gives Q = 4.9 × 104 J = 49 kJ . 
11.27 The conservation of energy equation for this process is 
(energy to melt ice) + (energy to warm melted ice to T ) = (energy to cool water to T ) 
or 
m L m c T m c T ice f ice w w w + ( − 0°C) = (80°C − ) 
This yields 
T 
m c m L 
w w f 
m m c 
w w 
= 
( ) − 
( + ) 
80°C ice 
ice 
so 
T = 
(1.0 kg)(4 186 J kg ⋅°C)(80°C) − (0.100 kg) 3.33 10 
1 1 4 186 
65 
( × 5 J kg 
) 
( )( ⋅ ) = 
kg J kg °C 
°C 
. 
11.28 The energy required is the following sum of terms: 
Q = ( ) 
energy to reach melting point 
(energy to melt) + energy to reach boiling point 
+ 
( ) 
+ ( e 
nergy to vaporize) + (energy to reach 110°C) 
Mathematically, 
Q m c L c L c f w = [ − (− )]+ + ( − ) + + ice s 0°C 10°C 100°C 0°C v team °C °C 110 100 − ( ) ⎡⎣⎤⎦ 
This yields 
⎛ 
Q = ( × ) ⋅ 
40 10−3 kg 2 090 (10 ) + 3 33 × 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
J 
kg °C 
°C . 10 
⎛ J 
4 186 
5 J 
kg 
J 
kg 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎡ 
⎣ ⎢ 
+ 
⋅°C 
100 °C 
2.26 106 + 2 010 
J 
kg 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
( ) + ⎛ × 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
kg °C 
°C 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
( )⎤ 
⎦ ⎥ 
10 
or 
Q = 1.2 × 105 J = 0.12 MJ
Energy in Thermal Processes 541 
11.29 Assuming all work done against friction is used to melt snow, the energy balance equation is 
⋅ = snow . Since f = μk (m g) skier , the distance traveled is 
f s m Lf 
s 
m L 
f 
m g 
= ( ) = 
k 
( )( × ) snow 
skier 
kg J kg 
μ 
1.0 3.33 105 
0.20 kg m s 
( )( )= × = 
2 3 103 2 3 
m km 75 9 . 
80 2 
. . 
11.30 (a) Observe that the equilibrium temperature will lie between the two extreme temperatures 
(−10.0°C and +30.0°C) of the mixed materials. Also, observe that a water-ice change 
of phase can be expected in this temperature range, but that neither aluminum nor ethyl 
alcohol undergoes a change of phase in this temperature range. The thermal energy 
transfers we can anticipate as the system come to an equilibrium temperature are: 
ice at − 10.0°C to ice at 0°C; ice at 0°C to liquid water at 0°C; water at 0°C to 
water at T; aluminum at 20.0°C to aluminum at T; ethyl alcohol at 30.0°C 
to ethyl alcohol at T. 
(b) Q m (kg) c (J kg ⋅°C) L (J kg) Tf (°C) Ti (°C) Expression 
Qice 1.00 2 090 0 −10 0 . m c ice ice [0 − (−10.0°C)] 
Qmelt 1.00 3.33 × 105 0 0 m Lice f 
Qwater 1.00 4 186 T 0 m c T ice water ( − 0) 
QAl 0.500 900 T 20.0 m c T Al Al [ − 20.0°C] 
Qalc 6.00 2 430 T 30.0 m c T alc alc [ − 30.0°C] 
(c) m c m L m c T m ice ice ice f ice water Al (10.0°C)+ + ( − 0)+ c T m c T Al alc alc [ − 20.0°C]+ [ − 30.0°C] = 0 
(d) T 
( ) + ( ) − Al Al alc alc ice ice 20.0°C 30.0°C 10.0°C 
( ) + ⎡⎣ 
m c m c m c 
= 
ice water Al Al alc alc 
⎤⎦ 
+ + 
L 
m c m c m c 
f 
Substituting in numeric values from the table in (b) above gives 
T = 
(0.500)(900)(20.0) + (6.00)(2 430)(30.0) − 1.00 2 090 10 0 3 33 10 
1 00 4 186 0 
5 ( ) ( )( ) + × ⎡⎣ 
⎤⎦ 
( )( ) + 
. . 
. ( .500)(900) + (6.00)(2 430) 
and yields T = 4.81°C .
542 Chapter 11 
11.31 Assume that all the ice melts. If this yields a result T  0, the assumption is valid, otherwise the 
problem must be solved again based on a different premise. If all ice melts, energy conservation 
(Qcold = −Q) 
yields 
hot m c L c T mc ice ice f w w °C 78°C °C 0 0 − − ( ) [ ] + + − ( ) ⎡⎣ 
⎤⎦ 
= − w ( + m c )(T − ) cal Cu 25°C 
or 
T 
+ ( )( ) − ( ) + ⎡⎣ 
⎤ cal Cu ice ice 25°C 78°C ⎦ 
(m + m )c + m c w ice w cal Cu 
m c m c m c L w w f = 
With m m m c w w = 0.560 kg, = 0.080 g, = 0.040 g, cal ice = 4 186 J kg ⋅°C, 
J kg °C J kg °C, and Cu ice c = 387 ⋅ , c = 2 090 ⋅ L = 3 f .33 ×105 J kg 
this gives 
T = 
( )( ) + ( )( ) ⎡⎣ 
0.560 4 186 0.080 387 (25°C) − 0.040 2 090 3 33 10 
⎤⎦ 
0 560 0 040 4 
5 ( ) ( )( ) + × ⎡⎣ 
⎤⎦ 
( + ) 
78°C . 
. . ( 186) + 0.080(387) 
or T = 16°C and the assumption that all ice melts is seen to be valid. 
11.32 At a rate of 400 kcal h, the excess internal energy that must be eliminated in a half-hour run is 
Q = × ⎛⎝ 
3 h . 
⎞⎠ 
⎛⎝ 
⎞⎠ 
4 186 
cal 
h 
J 
400 10 ( 0 500 
) 
1 cal 
. = 8.37 × 105 J 
The mass of water that will be evaporated by this amount of excess energy is 
m 
= = × 
Q 
L evaporated 6 
J 
× 
2.5 10 J kg 
= 
v 
8 37 10 
0 33 
. 5 
. kg 
The mass of fat burned (and thus, the mass of water produced at a rate of 1 gram of water per 
gram of fat burned) is 
mproduced 
(400 kcal h )(0.500 h 
) 
= 9.0 kcal gram 
of fat 
= 22 g = 22 × 10−3 kg 
so the fraction of water needs provided by burning fat is 
f 
= = × = 
m 
m 
− 
produced 
evaporated 
kg 
kg 
22 10 
0 33 
0 
3 
. 
.066 or 6.6%
Energy in Thermal Processes 543 
11.33 The mass of 2.0 liters of water is mw = ρV = (103 kg m3 )(2.0 × 10−3 m3 ) = 2.0 kg. 
The energy required to raise the temperature of the water (and pot) up to the boiling point of 
water is 
Q mc mc T boil w w Al Al = ( + )(Δ ) 
or 
= ( )⎛ 
J 2.0 4 186 + (0.25 ) 900 
Qboil kg 
J 
kg 
kg 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
kg 
°C °C J 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎡ 
⎣ ⎢ 
⎤ 
⎦ ⎥ 
(100 − 20 ) = 6.9 × 105 
The time required for the 14 000 Btu h burner to produce this much energy is 
t 
Q 
boil 
boil 
Btu h 
. 5 J 
1 Btu 
Btu h 
= = × 
14 000 
6 9 10 
14 000 
h min × 3 
1.054 10 J 
⎛⎝ 
⎞⎠ 
= 4.7 × 10−2 = 2.8 
Once the boiling temperature is reached, the additional energy required to evaporate all of the 
water is 
Q mL evaporate w = = ( kg)( × J kg) = × v 2.0 2.26 106 4.5 106 J 
and the time required for the burner to produce this energy is 
t 
Q 
boil 
evaporate 
Btu h 
J 
. 6 
B 
= = × 
14 000 
4 5 10 
14 000 
tu h 
Btu 
h min 3 
1 
1.054 10 J 
0 31 18 
× 
⎛⎝ 
⎞⎠ 
= . = 
11.34 In 1 hour, the energy dissipated by the runner is 
ΔE = P ⋅t = (300 J s)(3 600 s) = 1.08 ×106 J 
Ninety percent, or Q = 0.900(1.08 × 106 J) = 9.72 × 105 J, of this is used to evaporate bodily 
fl uids. The mass of fl uid evaporated is 
m 
= = × 
Q 
L 
× 
= 
v 
9 72 10 
10 
0 403 
5 
6 
. 
. 
J 
2.41 J kg 
kg 
Assuming the fl uid is primarily water, the volume of fl uid evaporated in 1 hour is 
V 
. 6 
0 403 
= m = = ( 4 03 × 10 
− ) 
ρ 
4 10 
. 
kg 
1 000 kg m 
m 
cm 
3 
3 
3 
3 
3 
m 
cm 
1 
403 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
=
544 Chapter 11 
11.35 The energy required to melt 50 g of ice is 
Q m Lf 
1 = = (0 050 )(333 ) = 16 7 ice . kg kJ kg . kJ 
The energy needed to warm 50 g of melted ice from 0°C to 100°C is 
Q m c T 2 w = ( ) = (0 050 )(4 ⋅ ) 100 ice Δ . kg .186 kJ kg °C ( °C) = 20.9 kJ 
(a) If 10 g of steam is used, the energy it will give up as it condenses is 
Q mL3 s = = (0 010 )(2 ) = 22 6 v . kg 260 kJ kg . kJ 
Since Q Q 3 1  , all of the ice will melt. However, Q Q Q 3 1 2  + , so the fi nal temperature is less 
than 100°C. From conservation of energy, we fi nd 
0 = [ + (100 − )] v 
m L c T m L c T ice f w steam w °C °C + − ( ) ⎡⎣ 
⎤⎦ 
or 
T 
+ ( 100 
°C ) ⎡⎣ 
v m L c m L 
steam ice 
w f = 
m m 
⎤⎦ 
− 
( + 
ice steam 
)cw 
giving 
T = 
10 g 2.26 106 4 186 100 − (50 g)(3.33 × ) 
( ) × + ( )( ) ⎡⎣ 
⎤⎦ 
10 
( + )( ) = 
50 10 4 186 
40 
5 
g g 
°C 
(b) If only 1.0 g of steam is used, then Q′ = m L = 3 s v 2.26 kJ. The energy 1.0 g of condensed 
steam can give up as it cools from 100°C to 0°C is 
= (Δ ) = (1.0 × 10−3 kg)(4.186 kJ kg ⋅°C)(100°C) = 0.419 kJ 
Q mc T 4 s w 
Since Q′ +Q 3 4 is less than Q1, not all of the 50 g of ice will melt, so the fi nal temperature will 
be 0°C . The mass of ice which melts as the steam condenses and the condensate cools to 
0°C is 
m 
= ( + ) 3 4 2 26 = × −3 
= ′ + 
Q Q 
Lf 
8 0 10 
. 
. 
0.419 kJ 
333 kJ kg 
kg = 8.0 g 
11.36 First, we use the ideal gas law (with V = 0.600 L = 0.600 × 10−3 m3 and T = 37.0°C = 310 K) to 
determine the quantity of water vapor in each exhaled breath: 
PV nRT n 
PV 
RT 
= ⇒ = = 
(3.20 × 103 Pa)(0.600 × 10−3 m3 ) 
( ⋅ )( ) = × − 
8 31 310 
7 45 10 4 
. 
. 
J mol K K 
mol 
or 
m = nM = ( × )⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
− 
water mol 
g 
mol 
⎛ 
1 k 
1 34 10 5 7.45 10 4 18.0 
g 
g 
kg 103 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= . × − 
The energy required to vaporize this much water, and hence the energy carried from the body 
with each breath is 
Q = mL = ( × − )( × ) = 
v 1.34 10 5 kg 2.26 106 J kg 30.3 J 
The rate of losing energy by exhaling humid air is then 
P = ⋅( ) =⎛⎝ 
⎞⎠ 
Q 
J 
breath 
b 
respiration rate 30.3 22.0 
reaths 
min 
= 1 
min 
60 s 
W ⎛⎝ 
⎞⎠ 
⎛⎝ 
⎞⎠ 
11 1 .
Energy in Thermal Processes 545 
11.37 (a) The bullet loses all of its kinetic energy as it is stopped by the ice. Also, thermal energy 
is transferred from the bullet to the ice as the bullet cools from 30.0°C to the fi nal 
temperature. The sum of these two quantities of energy equals the energy required to melt 
part of the ice. The final temperature is 0°C because not all of the ice melts. 
(b) The total energy transferred from the bullet to the ice is 
1 
2 
Q KE = i + mbulletclead 0°C− 30 0°C = mbullet i + m 
. v2 bullet lead °C 
kg 
c 30 0 
3 00 10 
J kg °C °C ( ) + ( ⋅ )( ) 
⎡ 
⎣ 
2 40 10 3 
2 
. 
. 
. 
( ) 
= ( × ) × − m s 
⎢⎢ 
⎤ 
⎦ 
⎥⎥ 
= 
2 
2 
128 30.0 97.9 J 
The mass of ice that melts when this quantity of thermal energy is absorbed is 
m 
Q 
Lf 
= ( ) = 
× 
. 4 
= × − 
water 
J 
J kg 
k 
97 9 
3 33 10 
2 94 10 5 
. 
. g 
10 g 
1 kg 
g 
⎛ 3 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= 0.294 
11.38 (a) The rate of energy transfer by conduction through a material of area A, thickness L, with 
thermal conductivity k, and temperatures T T h c  on opposite sides is P = kA(T − T ) L h c . 
For the given windowpane, this is 
P = 
J 
⋅ ⋅ 
⎛⎝ ⎜ 
⎞⎠ ⎟ 
( )( ) ⎡⎣ 
⎤⎦ 
( − 
) 
0 84 1 0 2 0 
25 
. . . 
s m °C 
m m 
°C 0 
10 
6 8 103 6 8 103 °C 
= × = × − . . 
J s W 2 
× 
0.62 m 
(b) The total energy lost per day is 
E = P ⋅ Δt = (6.8 × 103 J s)(8.64 × 104 s) = 5.9 × 108 J 
11.39 The thermal conductivity of concrete is k = 1.3 J s ⋅m⋅°C, so the energy transfer rate through the 
slab is 
P = 
( − ) = 
kA 
h c J 
1 3 ( ( 5 0 
) ⋅ ⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
T T 
L 
20 
. . 
s m °C 
m 
°C 2 ) 
= × = × 12 − m 
× 
1.1 103 1.1 103 
J s W 10 2 
11.40 (a) The R value of a material is R = L k, where L is its thickness and k is the thermal 
conductivity. The R values of the three layers covering the core tissues in this body are 
as follows: 
Rskin 
= × 
m m 2 
K W ⋅ 
0.020 W m K 
= × ⋅ 
− 
1 0 10 − 
5 0 10 
3 
. 2 
. 
Rfat 
= × 
m m 2 
K W ⋅ 
0.20 W m K 
= × ⋅ 
− 
0 50 10 − 
2 5 10 
2 
. 2 
. 
and 
Rtissue 
= × 
m m 2 
K W ⋅ 
0.50 W m K 
= × ⋅ 
− 
3 0 10 − 
6 0 10 
2 
. 2 
. 
so the total R value of the three layers taken together is 
= 3 
( + + ) × ⋅ = × 
R Ri 
i 
total 
m2 K 
W 
= Σ 
= 
− 
1 
m 2 ⋅K 2 
⋅ 
5.0 2.5 6.0 10 2 14 10−2 = 0 14 W 
m K 
W 
. 
continued on next page
546 Chapter 11 
(b) The rate of energy transfer by conduction through these three layers with a surface area of 
A = 2.0 m2 and temperature difference of ΔT = (37 − 0)°C = 37°C = 37 K is 
P = ( ) = ( )( ) 
2 0 37 
0 14 
m K 
m KW 
= × A T 
R 
⋅ 
Δ 
total 
2 
2 
5 3 
. 
. 
. 102 W 
11.41 P = ⎛⎝ ⎜ 
⎞⎠ ⎟ 
kA 
Δ 
T 
L 
, with k = 
⋅ ⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
0 200 
10 4 186 
. 
cal . 
cm °C s 
cm 
1 m 
J 
1 c 
2 
al 
J 
s m °C 
⎛⎝ 
⎞⎠ 
= 
⋅ ⋅ 
83 7 . 
Thus, the energy transfer rate is 
P = 
J 
⋅ ⋅ 
⎛⎝ 
⎞⎠ 
[( )( )] ° − 
83 7 8 00 50 0 
200 2 
. . . 
s m °C 
m m 
C 0 0 
1 50 10 
4 02 10 402 
2 
8 
. 
. 
. 
°C 
m 
J 
s 
MW 
× 
⎛⎝ 
⎞⎠ 
= × = 
− 
11.42 The total surface area of the house is 
A = A + A + A + A side walls end walls gables roof 
where 
Aside walls 
= 2[(5.00 m) × (10.0 m)] = 100 m2 
Aend walls 
= 2[(5.00 m) × (8.00 m)] = 80.0 m2 
A = 2[1 ( base ) × ( altitude )] = 2 (8 00 m) × 
gables 2 
1 
2 [ . (4.00 m) tan 37.0°] = 24.1 m2 
Aroof 
= 2 ( 10.0 m ) × ( 4.00 m cos37.0 ° ) = 100 
m 2 ⎡⎣ 
⎤⎦ 
Thus, 
A = 100 m2 + 80.0 m2 + 24.1 m2 + 100 m2 = 304 m2 
With an average thickness of 0.210 m, average thermal conductivity of 4.8 × 10−4 kW m⋅°C, and 
a 25.0°C difference between inside and outside temperatures, the energy transfer from the house 
to the outside air each day is 
= ( ) = t ⎡ ( ) 
E t 
kA T 
L 
⎣ ⎢ 
⎤ 
⎦ ⎥( ) = 
( × − ⋅ ) 
P Δ 
Δ 
Δ 
4.8 10 4 kW m °C 304 25 0 
. 
( 86 400 
) m °C 
0.210 m 
s 
⎡ ( 2 )( ) 
⎣ ⎢⎢ 
⎤ 
⎦ ⎥⎥ 
or 
E = 1.5 × 106 kJ = 1.5 × 109 J 
The volume of gas that must be burned to replace this energy is 
V 
= E 
= × 
heat of combustion 
( 
J 
1 5 10 
kcal m3 
9 300 
. 9 
)( ) = 
4 186 
39 
J kcal 
m3 
11.43 R R R R R i = Σ = + + outside 
air film 
shingles sheathing + R + R + R cellulose dry wall inside 
air film 
R = [ + + + ( ) + + ] ⋅ 
0.17 0.87 1.32 3 3.70 0.45 0.17 
ft2 °F 
Btu h 
2 
= ⋅ 
ft °F 
Btu h 
14
Energy in Thermal Processes 547 
11.44 The rate of energy transfer through a compound slab is 
P = ( ) = A T 
Δ , where Σ 
R 
R L k i i 
(a) For the thermopane, R = R + R + R = R + R pane trapped air pane pane trapped 2 air. 
Thus, 
R = × 
+ × − − 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
2 
0.50 10 2 m 1.0 10 2 
0.84 W m °C 
m 
0.0234 W m °C 
2 
m °C 
W 
⋅ 
= ⋅ 
0.44 
and 
P = ( )( ) 
⋅ 
= 
1 0 23 
0 44 
52 
. 
. 
m °C 
m °CW 
W 
2 
2 
(b) For the 1.0 cm thick pane of glass: 
R = × 
= × ⋅ − 
1 0 10 − 
⋅ 
1 2 10 
2 
. 2 
. 
m 
0.84 W m °C 
2 
m °C 
W 
so 
( 1 0 )( 23 
) 
P = = × = − 
× ⋅ 
1 
. 
m °C 
1 . 
9 103 1 .2 10 m °C W 
W 
2 
2 2 .9 kW , 37 times greater 
11.45 When the temperature of the junction stabilizes, the energy transfer rate must be the same for each 
of the rods, or P P Cu Al = . The cross-sectional areas of the rods are equal, and if the temperature of 
the junction is 50°C, the temperature difference is ΔT = 50°C for each rod. 
Thus, 
Δ Δ 
k A = 
Al = 
P P Cu Cu 
Cu 
Al 
Al 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
T 
L 
k A 
T 
L 
, 
which gives 
L 
k 
k 
Al 
L Al 
Cu 
Cu 
W m °C 
97 W m °C 
= 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= ⋅ 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ 
238 
3 ⎟ ( ) = 15 cm 9.0 cm 
11.46 The energy transfer rate is 
P= = = (Δ )( × ) 
Q 
t 
5.0 3.33 105 
( )( ) = 
ice f kg J kg 
m L 
Δ Δ 
t 
8.0 h 
3 600 
58 
s 1 h 
W 
Thus, P = kA(ΔT L) gives the thermal conductivity as 
k 
= ⋅ 
L 
( ) = 
A T 
( )( × ) 
( ) − 
− P 
Δ 
W . 
2 m 
m2 °C 
58 2 0 10 
0 80 25 
W m °C ( )= × − ⋅ 
. 5 0 
7 2 10 2 
. 
. 
°C
548 Chapter 11 
11.47 The absolute temperature of the sphere is T = 473 K and that of the surroundings is T0 = 295 K. 
For a perfect black-body radiator, the emissivity is e = 1. The net power radiated by the sphere is 
Pnet 
W 
m K 
2 4 
= ( − ) 
= × 
⋅ 
⎛⎝ ⎜ 
⎞⎠ ⎟ 
− 
σ 
π 
Ae T 4 T 
4 
0 
5.67 10 8 4 0.060 473 2 2 4 4 m K 95 K ( ) ⎡⎣ 
⎤⎦ 
( ) − ( ) ⎡⎣ 
⎤⎦ 
or 
Pnet = 1.1×102 W= 0.11 kW 
11.48 Since 97.0% of the incident energy is refl ected, the rate of energy absorption from the sunlight is 
Pabsorbed= 3.00%× (I ⋅ A) = 0.0300(I ⋅ A), where I is the intensity of the solar radiation. 
Pabsorbed 
= 0 0300(1 40 × 103 W m2 )(1 00 × 103 m)2 . . . = 4.20 × 107 W 
Assuming the sail radiates equally from both sides (so A = 2(1 00 ) = 2 00 × 10 . km 2 . 6 m2), the rate 
at which it will radiate energy to a 0 K environment when it has absolute temperature T is 
Prad 2 4 
W 
m K 
= ( − ) = × 
⋅ 
⎛⎝ 
⎞⎠ 
W 
K 
4 ( )( )⋅ = × ⎛⎝ 
σ Ae T 4 0 5.669 6 10−8 2.00 × 106 m 2 
0 03 4 3 40 10 3 4 
⎞⎠ 
. T . − ⋅T 
At the equilibrium temperature, where P P rad absorbed = , we then have 
− W ⋅ = × 
3 40 10 4 20 10 3 4 7 . . × ⎛⎝ 
⎞⎠ 
K 
W 4 T or T = × 
× 
⎡ 
⎣ ⎢ 
⎤ 
= − 
⎦ ⎥ 
4 20 10 
3 40 10 
333 
7 
3 
1 4 
. 
. 
W 
W K 
K 4 
11.49 The absolute temperatures of the two stars are T T X Y = 6 000 K and = 12 000 K. Thus, the ratio 
of their radiated powers is 
P 
P 
Y 
X 
σ Y 
= ( ) = 
σ 
X 
Y 
X 
AeT 
AeT 
T 
T 
= = 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
4 
4 
4 
4 2 16 
11.50 The net power radiated is Pnet=σ Ae(T 4 − T ) 
4 , so the temperature of the radiator is 
0 
T T 
Ae 
= ⎡ + 
⎣ ⎢ 
⎤ 
⎦ ⎥ 
4 
0 
1 
P 4 net 
σ 
If the temperature of the surroundings is T0 = 22°C = 295 K, 
T = ( ) + 
25 
W 
295 
( 5 67 × 10 − ⋅ ) 2 5 × 10 
− 4 
8 5 K 
. W m2 K4 . m2 
K °C 
( )( ) 
⎡ 
⎣ ⎢⎢ 
⎤ 
⎦ ⎥⎥ 
= × = × 
0 90 
2 1 10 1 8 10 
1 
4 
3 3 
. 
. . 
11.51 At a pressure of 1 atm, water boils at 100°C. Thus, the temperature on the interior of the copper 
kettle is 100°C and the energy transfer rate through it is 
P = ⎛⎝ ⎜ 
⎞⎠ ⎟ 
= 
W 
m °C 
⋅ 
⎛⎝ ⎜ 
⎞⎠ ⎟ 
( ) ⎡⎣ 
⎤⎦ 
kA 
Δ 
T 
L 
397 0 10 2 
π . m 
102 100 
2 0 10 
1 2 10 12 
3 
4 
°C °C 
m 
W k 
− 
× 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= × = 
. − 
. W
Energy in Thermal Processes 549 
11.52 The mass of the water in the heater is 
ρ ⎞ 10 50 0 
m V = =⎛⎝ 
3 kg 3 786 
m 
⎞⎠ 
( )⎛ 
⎝ ⎜ 
gal 
L 
. 
3 1 gal . 
⎠ ⎟ 
⎛ 
⎝ ⎜ 
⎞ 
= 1 
10 
189 3 
⎠ ⎟ 
m 
L 
kg 
3 
The energy required to raise the temperature of the water from 20.0°C to 60.0°C is 
Q = mc(ΔT ) = (189 kg)(4 186 J kg)(60.0°C− 20.0°C) = 3.17 ×107 J 
The time required for the water heater to transfer this energy is 
t 
Q = = × ⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= 
P 
3 17 10 1 
1 83 
. 7 
. 
J 
4 800 J s 
h 
3 600 s 
h 
11.53 The energy conservation equation is 
m c m L m m c m c Pb Pb ice f ice w w cup C (98°C − 12°C) = + ( + ) + u °C °C ⎡⎣ 
⎤⎦ 
(12 − 0 ) 
This gives 
mPb 
J 
kg °C 
128 86°C 0 040 kg 3 33 10 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
( ) = ( . ) . × 5 
0 24 
J kg 
kg 
( ) 
+ . ( ) ⋅ ( ) + ( ) ⋅ ( ) ⎡⎣ 
⎤⎦4 186 J kg °C 0.100 kg 357 J kg °C (12°C) 
or mPb = 2.3 kg . 
11.54 The energy needed is 
Q = mc( T ) = ( V )c( T ) 
= ⎛⎝ 
⎡ ( ) 
⎞⎠ 
⎣ ⎢ 
Δ ρ Δ 
103 1 00 kg 
m 
. 3 ⎤ 
m 3 
⎦ ⎥ 
(4 186 J kg)(40.0°C) = 1.67 × 108 J 
The power input is P = (550 W m2 )(6.00 m2 ) = 3.30 ×103 J s, so the time required is 
t 
Q = = × 
× 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= 
P 
1 67 10 
3 30 10 
1 
1 
8 
3 
. 
. 
J 
J s 
h 
3 600 s 
4 1 . h 
11.55 The conservation of energy equation is 
m c m c T m c T w w ( + )( − ) = ( − ) cup glass Cu Cu 27°C 90°C 
This gives 
T 
Cu Cu cup glass 90°C 27°C 
m c m c m c 
m c 
w w 
w w 
= 
( ) + ( + )( ) 
+ 
m c m c cup glass Cu Cu + 
or 
T = 
(0.200)(387)(90°C) + (0.400)(4 186) + (0.300) 837 27 
( ) ⎡⎣ 
29 ( )( ) = °C 
0 400 4 186 0 300 837 0 
⎤⎦ 
( ) 
( )( ) + ( )( ) + 
°C 
. . .200 387
550 Chapter 11 
11.56 (a) The energy delivered to the heating element (a resistor) is transferred to the liquid nitrogen, 
causing part of it to vaporize in a liquid-to-gas phase transition. The total energy delivered 
to the element equals the product of the power and the time interval of 4.0 h. 
(b) The mass of nitrogen vaporized in a 4.0 h period is 
m 
Q 
L 
⋅( ) = ( )( )( ) 
P Δ t 
25 4 0 3 
= = 
L f f 
J s . h s h 
. 
× 
2 01 
600 
10 
= . kg 
1 8 5 J kg 
11.57 Assuming the aluminum-water-calorimeter system is thermally isolated from the environment, 
Q Q cold hot = − , or 
m c T T mc T T m c T Al Al f i Al w w f i w cal cal f ( − ) = − ( − )− − , , Ti,cal ( ) 
Since Tf = 66 3 . °C and T T i, i,w . cal = = 70 0°C, this gives 
c 
m c m c T T 
, 
w w iw f 
m T T 
f i 
Al 
cal cal 
Al Al 
= 
( + )( − ) 
( − ) 
, 
or 
cAl 
0.400 kg 
4 186 + (0.040 ) 630 
J 
kg °C 
kg 
J 
= 
⎛ 
( ) ⋅ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
kg °C 
°C 
kg 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎡ 
⎣ ⎢ 
⎤ 
⎦ ⎥ 
( − ) 
( ) 
70 0 66 3 
( − ) = × 
0 200 66 
. . 
. . . 
. 
3 270 
8 00 102 
J 
kg °C 
°C ⋅ 
The variation between this result and the value from Table 11.1 is 
⎛ 
variation × = − 
% = % 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
accepted value 
100 
800 900 
900 
100 11 1 
J kg °C 
J kg °C 
⋅ 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
× % = . % 
which is within the 15% tolerance. 
11.58 (a) With a body temperature of T = 37°C + 273 = 310 K and surroundings at temperature 
T0 = 24°C + 273 = 297 K, the rate of energy transfer by radiation is 
Prad 
W 
m K 
2 4 
= ( − ) 
= × 
⋅ 
⎛⎝ 
⎞⎠ 
− 
σ Ae T 4 T 
4 
0 
8 5 669 6 10 2 0 . . m K K W 2 ( )( ) ( ) − ( ) ⎡⎣ 
⎤⎦ 
0 97 310 297 = 1 6 × 10 . 4 4 . 2 
(b) The rate of energy transfer by evaporation of sweat is 
Psweat 
W ( )( )= × 
Q ) × 
t 
0.40 2.43 10 kg J kJ 
v, sweat 
kg 3 kJ 
= = = ( 
mL 
Δ Δt 
3 600 s 
10 
2 7 10 
3 
. 2 
(c) The rate of energy transfer by evaporation from the lungs is 
Plungs 
kJ 
h 
h 
3 600 s 
J 
1 kJ 
=⎛⎝ 
⎞⎠ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎛ 
⎝ 
38 
1 103 
⎜ 
⎞ 
⎠ ⎟ 
= 11W 
(d) The excess thermal energy that must be dissipated is 
P P excess metabolic 
kJ 
h 
= = × ⎛⎝ 
⎞⎠ 
0.80 0.80 2.50 103 
1 10 
5 6 10 
3 
h 2 
3 600 s 
J 
1 kJ 
W 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= . × 
so the rate energy must be transferred by conduction and convection is 
P P P P P cc = − ( + + ) = . − . − excess rad sweat lungs (5 6 1 6 2.7 − .11) × 102 W = 1.2 × 102 W
Energy in Thermal Processes 551 
11.59 The rate at which energy must be added to the water is 
P= = 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
= ⎛⎝ ⎜ 
⎞⎠ ⎟ 
Δ 
Δ 
Δ 
Δ 
Q 
t 
m 
t 
Lv 0 500 
1 
. 
kg 
min 
min 
60 s 
J 
kg 
⎛⎝ ⎜ 
⎞⎠ ⎟ 
⎡ 
⎣ ⎢ 
⎤ 
⎦ ⎥ 
2.26 × 
106 = 1.88 ×104 W 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
From P = kA(T −100°C) L, the temperature of the bottom surface is 
T 
°C ( ) 
P . W . m 
= + ⋅ = + 
L 
k A 
( × ) × − 
100 100 
1 88 104 0 500 10 2 
°C °C 
109 2 . 
⎡⎣ 
( 238 W m ⋅ °C ) ( m 
) ⎤⎦ 
= 
π 0 120 
11.60 The energy added to the air in one hour is 
Q t = ( ) = ( ) ⎡⎣ 
P ( ) = × total 10 200 W 3 600 s 7.2 0 106 J 
⎤⎦ 
and the mass of air in the room is 
m = ρV = (1.3 kg m3 )[(6.0 m)(15.0 m)(3.0 m)] = 3.5 × 102 kg 
The change in temperature is 
ΔT 
= = × 
Q 
mc 
7 2 10 
( = 3 5 × 10 )( 837 
⋅ ) 25 
6 
2 
. 
. 
J 
kg J kg °C 
°C 
giving T = T + T = + = 0 Δ 20°C 25°C 45°C . 
11.61 In the steady state, P P Au Ag = , or 
k A 
80 . 0 °C − T 
30 . 0 °C ⎛⎝ 
L 
= T 
k A 
⎛⎝ 
− ⎞⎠ 
L Au Ag 
⎞⎠ 
This gives 
T 
80.0°C 30.0°C 314 80.0°C) + ( ) 
= Au Ag ( 
k k 
k k 
= 
( ) + ( ) 
+ 
Au Ag 
+ 
= 427 30 0 
314 427 
51 2 
. 
. 
°C 
°C 
11.62 (a) The rate work is done against friction is 
P = f ⋅ v = (50 N)(40 m s) = 2.0 ×103 J s = 2.0 kW 
(b) In a time interval of 10 s, the energy added to the 10-kg of iron is 
Q = P ⋅t = (2.0 ×103 J s)(10 s) = 2.0 ×104 J 
and the change in temperature is 
ΔT 
= = × 
Q 
mc 
2 0 10 
( )( ) = 448 
⋅ 4 5 
. 4 
. 
J 
10 kg J kg °C 
°C
552 Chapter 11 
11.63 (a) The energy required to raise the temperature of the brakes to the melting point at 660°C is 
Q = mc(ΔT ) = (6.0 kg)(900 J kg ⋅°C)(660°C − 20°C) = 3.46 × 106 J 
The internal energy added to the brakes on each stop is 
1 2 2 
2 
Q KE mi 
1 
1 
2 
= Δ = = (1 500 )(25 ) = 4 69 ×1 car v kg m s . 05 J 
The number of stops before reaching the melting point is 
N 
= = × 
Q 
Q 
× 
= 
1 
6 
5 
3 46 10 
4 69 10 
7 
. 
. 
J 
J 
stops 
(b) This calculation assumes no energy loss to the surroundings and that all internal energy 
generated stays with the brakes. Neither of these will be true in a realistic case. 
11.64 When liquids 1 and 2 are mixed, the conservation of energy equation is 
7 
3 
=⎛⎝ 
⎞⎠ 
mc mc 1 2 (17°C−10°C) = (20°C−17°C), or c c 2 1 
When liquids 2 and 3 are mixed, energy conservation yields 
28 
3 
= =⎛⎝ 
⎞⎠ 
mc mc 3 2 (30°C− 28°C) = (28°C− 20°C), or c c c 3 2 1 4 
Then, mixing liquids 1 and 3 will give mc T mc T 1 3 ( −10°C) = (30°C− ) 
or 
T 
= ( ) + ( ) 
10 30 10 28 3 30 
°C °C °C °C 
c c 
+ 
c c 
= 
+ ( )( ) 
+ 
1 3 
1 3 
1 
( ) = 28 °C 
28 3 
11.65 (a) The internal energy ΔQ added to the volume ΔV of liquid that fl ows through the calorimeter 
in time Δt is ΔQ = (Δm)c (ΔT ) = ρ(ΔV)c (ΔT ). Thus, the rate of adding energy is 
Δ 
Δ 
Δ Δ 
Δ 
Q 
t 
c T 
V 
t 
= ( )⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
ρ 
where ΔV Δt is the fl ow rate through the calorimeter. 
(b) From the result of part (a), the specifi c heat is 
c 
Δ Δ 
Q t 
T V t 
J s 
= = ρ ( Δ )( Δ Δ 
) ( )( ) 
40 
. g cm3 . °C .5 
0 72 5 8 3 
. = .7 ×103 J kg ⋅°C 
2 7 
10 
2 
3 
cm s 
J 
g °C 
g 
1 kg 
( 3 ) 
= 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟
Energy in Thermal Processes 553 
= + = 2(π 2 )+ (2π ), or 
11.66 (a) The surface area of the stove is A A A r rh stove ends cylindrical 
side 
Astove = 2 (0 200 m) + 2 (0 200 m)(0 500 m) = 0 2 π . π . . .880 m2 
The temperature of the stove is Ts= − = = 59 
(400°F 32.0°F) 204°C 477 K while that of 
the air in the room is Tr= 5 − = = 
9 (70.0°F 32.0°F) 21.1°C 294 K. If the emissivity of the 
stove is e = 0.920, the net power radiated to the room is 
P = σA eT ( 4 − T 4 
) 
stove s r 
= ( × − ⋅ ) 
⎡⎣ 
5 . 67 10 8 W m2 K4 
( 0 . 880 m 2 )( ) ( K ) − ( K ) ⎤⎦ 
0 920 477 294 4 4 . 
or 
P = 2.03 × 103 W 
(b) The total surface area of the walls and ceiling of the room is 
A = 4A + A = 4[(8 00 )(25 0 )] + 25 wall ceiling . ft . ft .0 1 43 10 ( ft)2 = . × 3 ft2 
If the temperature of the room is constant, the power lost by conduction through the walls 
and ceiling must equal the power radiated by the stove. Thus, from thermal conduction 
equation, P = A(T − T ) R h c i Σ , the net R value needed in the walls and ceiling is 
ΣR 
( − ) = 
A T T 
i 
= h c 
( × )( − ) 
P 
1.43 103 ft2 70.0°F 32.0°F 
2.03 10 J s 
J 
Btu 
⎝ ⎜⎞ 
h 
⎛⎝ ⎜ 
⎞⎠ ⎟⎛ 
× 3 3 600 s 
⎠ 
1 054 
1 
1 
⎟ 
or 
ΣRi= 7.84 ft2 ⋅ °F ⋅ h Btu 
11.67 A volume of 1.0 L of water has a mass of m = ρV = (103 kg m3 )(1.0 × 10−3 m3 ) = 1.0 kg. 
The energy required to raise the temperature of the water to 100°C and then completely evaporate 
it is Q = mc(ΔT )+ mLv, or 
Q = (1.0 kg)(4 186 J kg⋅°C)(100°C− 20°C) + (1.0 kg)(2.26 ×106 J kg) = 2.59 ×106 J 
The power input to the water from the solar cooker is 
P = ( ) = ( )( ) ( ) efficiency IA 0 50 600 
0 50 
4 
2 
. 
. 
W m 
m 2 ⎡π 
⎣ ⎢⎢ 
⎤ 
⎦ ⎥⎥ 
= 59 W 
so the time required to evaporate the water is 
t 
= Q = 2 . 59 × 10 
6 
J 
= ( 4 . 
4 × 10 
4 
s 
)⎛ 
P 59 
J s 
⎝ 
1 h 
⎜ 3 600 s 
⎞ 
⎠ ⎟ 
= 12 h
554 Chapter 11 
11.68 (a) From the thermal conductivity equation, P = − ( ) ⎡⎣ 
⎤⎦ 
kA T T L h c , the total energy lost by 
conduction through the insulation during the 24-h period will be 
Q 
kA 
L 
= P ( )+P ( ) = ( − )+ 1 2 12 0 12 0 37 0 23 0 . . . . h h °C °C 37 0 16 0 12 0 . . . °C °C h − ( ) ⎡⎣ 
⎤⎦ 
( ) 
or 
Q = 
( 0 012 0 ⋅ )( 0 490 
) + 
0 095 0 
⎛⎝ 
[ 14 0 21 
]( )J . . 
. 
. . 
J s m°C m 
m 
°C 
2 
0 120 
3 600 
s 
°C h 9 36 104 
1 h 
⎞⎠ 
. = . × 
The mass of molten wax which will give off this much energy as it solidifi es (all at 37°C) is 
m 
= = × 
Q 
Lf 
= 9 36 10 
× 
0 457 
kg 3 
. 4 
. 
J 
205 10 J kg 
(b) If the test samples and the inner surface of the insulation is preheated to 37.0°C during 
the assembly of the box, nothing undergoes a temperature change during the test period. 
Thus, the masses of the samples and insulation do not enter into the calculation. Only the 
duration of the test, inside and outside temperatures, along with the surface area, thickness, 
and thermal conductivity of the insulation need to be known. 
11.69 The energy m kilograms of steam give up as it (i) cools to the boiling point of 100°C, 
(ii) condenses into a liquid, and (iii) cools on down to the fi nal temperature of 50.0°C is 
m = ( )+ + ( ) 
= 
Q mc T mL mc T 
m 
steam liquid 
water 
2.0 
Δ Δ 1 v 2 
( 1 × 10 3 J kg ⋅ °C ) ( 130 °C − 100 °C )+ 2.26 × 106 
J ⎡⎣ 
kg +(4 186 J kg ⋅°C) 100°C− 50 0 
2 53 106 
. 
. 
°C 
J kg 
( )⎤⎦ 
= m( × ) 
The energy needed to raise the temperature of the 200-g of original water and the 100-g glass 
container from 20.0°C to 50.0°C is 
Q mc mc T needed w w g g kg J kg °C = + ( ) = ( ) ⋅ Δ 0 200 4 186 . ( ) + ( ) ⋅ ( ) ⎡⎣ 
⎤⎦ 
( ) 
= 
0 100 837 30 0 
2 76 
. . 
. 
kg J kg °C °C 
× 104 J 
Equating the energy available from the steam to the energy required gives 
m(2.53 × 106 J kg) = 2.76 × 104 J or m = × 
= = 2 76 10 
2 53 10 
× 
0 010 9 10 9 
4 
6 
. 
. 
. . 
J 
J kg 
kg g
Energy in Thermal Processes 555 
11.70 We approximate the latent heat of vaporization of water on the skin (at 37°C) by asking how 
much energy would be needed to raise the temperature of 1.0 kg of water to the boiling point and 
evaporate it. The answer is 
≈ (Δ )+ °C = ( J kg ⋅°C)( °C− 37°C)+ 2.26 ×106 J kg 
37°C 100 4 186 100 
L c T L v water 
v 
or 
37°C ≈ 2.5 ×106 J kg 
Lv 
Assuming that you are approximately 2.0 m tall and 0.30 m wide, you will cover an area of 
A = (2.0 m)(0.30 m) = 0.60 m2 of the beach, and the energy you receive from the sunlight in one 
hour is 
Q = IA(Δt ) = (1 000 W m2 )(0.60 m2 )(3 600 s) = 2.2 × 106 J 
The quantity of water this much energy could evaporate from your body is 
m 
= ≈ × 
Q 
L 
2 2 10 
2 5 10 
0 9 °C 
× 
= 
37 
v 
6 
6 
J 
J kg 
kg 
. 
. 
. 
The volume of this quantity of water is 
V 
0 9. kg 
10 kg m 
= m = ≈ − 3 3 
= 
ρ 
10 m 1 L 3 3 
Thus, you will need to drink almost a liter of water each hour to stay hydrated. Note, of course, 
that any perspiration that drips off your body does not contribute to the cooling process, so 
drink up! 
11.71 During the fi rst 50 minutes, the energy input is used converting m kilograms of ice at 0°C into 
= = (3.33 × 105 J kg), so the constant 
liquid water at 0°C. The energy required is Q mL m 1 f 
power input must be 
Q ( × ) 
t 
P = ( ) = 
m 
1 
1 
3 33 105 
. J kg 
Δ 50 
min 
During the last 10 minutes, the same constant power input raises the temperature of water having 
a total mass of (m + 10 kg) by 2.0°C. The power input needed to do this is 
Q ( + ) 
t 
( ⋅ )(2.0 ) 
kg kg J kg °C °C 
10 10 4 186 
m 2 
P = ( ) = 
( m + ) c ( T 
) 
( ) = 
t 
2 2 
Δ 
Δ 
Δ 
10 min 
Since the power input is the same in the two periods, we have 
10 4 186 ( . × 5 ) = 
m 3 33 10 m 
50 
J kg ( + )( ⋅ 
min 
kg J kg °C)(2.0°C) 
10 min 
which simplifi es to (8.0)m = m + 10 kg, or 
m= = 10 
1 4 
kg 
7.0 
. kg
556 Chapter 11 
11.72 (a) First, energy must be removed from the liquid water to cool it to 0°C. Next, energy must 
be removed from the water at 0°C to freeze it, which corresponds to a liquid-to-solid phase 
transition. Finally, once all the water has frozen, additional energy must be removed from 
the ice to cool it from 0°C to –8.00°C. 
(b) The total energy that must be removed is 
Q = Q + Q + Q cool water 
to 0°C 
freeze 
at 0°C 
cool ice 
to 8.00°C 
ice °C °C 
− 
= m c − T + m L + m c T − w w i w f w f 0 0 
or 
⎛ 
Q = ( × ) ⋅ 
75.0 10−3 kg 4 186 −20.0 + 3.33 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
J 
kg °C 
°C × + 
⋅ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
− 
⎡ 
⎣ ⎢ 
⎤ 
⎦ ⎥ 
= 
10 2 090 8 00 
3 2 
5 J 
kg 
J 
kg °C 
. °C 
. 5 × 104 J = 32.5 kJ 
11.73 (a) In steady state, the energy transfer rate is the same for each of the rods, or 
P P Al Fe = . Thus, k A 
100 °C − T 
0 °C ⎛⎝ 
L 
= T 
k A 
⎛⎝ 
− ⎞⎠ 
L Al Fe 
⎞⎠ 
giving 
T 
k 
k k 
= 
+ 
⎛ 
⎝ ⎜ 
⎞ 
⎠ ⎟ 
( ) = 
+ 
⎛⎝ 
⎞⎠ 
Al 
Al Fe 
100°C 
238 
238 79 5 
10 
. 
( 0°C) = 75.0°C 
(b) If L = 15 cm and A = 5.0 cm2, the energy conducted in 30 min is 
P ( × − ) − Al 
Q = ⋅ t = 
⋅ 
⎛⎝ ⎜ 
⎞⎠ ⎟ 
4 100 7 . 
2 
W 
m °C 
m 
°C 
238 5 0 10 
5 0 
0 15 
1 800 
3 6 104 
. 
. 
. 
°C 
m 
s 
J 
⎛⎝ ⎜ 
⎞⎠ ⎟ 
⎡ 
⎣ ⎢ 
⎤ 
⎦ ⎥ 
( ) 
= × = 36 kJ

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Solucionario Fundamentos de Física 9na edición Capitulo 11

  • 1. 11 Energy in Thermal Processes CLICKER QUESTIONS Question J2.01 Description: Introducing “heat” and identifying preconceptions about it. Question Which of the following phrases best describes heat? 1. The total energy possessed by a body 2. The fl ow of temperature to or from a body 3. The amount of energy dissipated by friction 4. The total energy fl owing between two bodies at different temperatures 5. The useful work that could be extracted from a body Commentary Purpose: To explore your preconceptions about the meaning of the word “heat,” and relate those to the formal physics term and concept. Discussion: In colloquial usage, the word “heat” is often used to refer to temperature or to the amount of thermal energy stored in a body. In physics, “heat” means thermal energy fl owing into or out of a body. We don’t use the word to refer to the thermal energy possessed by a body. (Unfortunately, many texts use the redundant phrase “heat fl ow.)” Sometimes people talk about friction converting kinetic energy into heat. This also is inaccurate; it may convert kinetic energy into thermal (as well as vibrational) energy, but that is only heat while it is fl owing between bodies. Key Points: • Heat refers to thermal energy fl owing into or out of a body, not thermal energy in general. • Heat is not the same thing as temperature, though they are closely related. For Instructors Only Any time you introduce new physics vocabulary that involves words students already know from other contexts (such as everyday language), you should investigate to fi nd out what connotations those words already have for students. This accomplishes two things: it alerts you to potential misunderstandings and misconceptions, and makes students aware of their own associations so they can be defensive about distin-guishing them from the proper physics meaning. 525
  • 2. 526 Chapter 11 Question J2.02 Description: Introducing and distinguishing heat capacity and specifi c heat. Question Two objects made from the same material have different masses and different initial temperatures as shown. If the bodies are placed in thermal contact, the fi nal equilibrium temperature is most nearly: 2 1 2M M 20° C 60° C 1. 27°C 2. 33°C 3. 40°C 4. 47°C 5. None of the above 6. Cannot be determined Commentary Purpose: To understand heat capacity, distinguish it from specifi c heat, and apply it to thermal equilibration. Discussion: When the objects are placed in thermal contact, heat will fl ow from the warmer one to the colder. As it does, the warmer one will cool down and the colder one will warm up. In this question, the warmer one is larger and has more material to cool down, so its temperature will not change as rapidly as the smaller one’s will. The concept of “heat capacity” quantifi es this. If the two objects are made from the same material, they have the same specifi c heat: the amount of heat required to change the temperature of 1 g of the material by 1°C. However, the heat capacity of an object is the heat required to change the temperature of the entire object by 1°C. So, if the objects are made of the same material and object 2 has twice the mass, it must have twice the heat capacity. This means that for every degree that object 2 cools, the heat transferred will warm object 1 by two degrees. The initial temperature difference is 40°C. Object 1 will warm up by 23 of that, and object 2 will cool by 13 of it. Thus, the fi nal temperature must be about 47°C: answer (4). Key Points: • When two objects are placed in thermal equilibrium, the thermal energy lost by one is gained by the other. It is not true that the temperature lost by one is gained by the other. Energy, not temperature, is conserved. • Make sure you understand the difference between specifi c heat and heat capacity.
  • 3. Energy in Thermal Processes 527 • An object’s heat capacity is the heat required to change its temperature by 1°C. • A material’s specifi c heat is the heat required to change the temperature of 1 g of if by 1°C. • The heat capacity of an object made of one material is its mass times the material’s specifi c heat. For Instructors Only This question is designed to confront and resolve confusion between heat capacity and specifi c heat. A related concept that you may want to connect to is “molar specifi c heat”, the heat required to change the temperature of one mole of a material by 1°C. Answer (1) is the sum of the initial temperatures divided by three (the mass in units of M ), a misguided attempt at averaging. Answer (2) indicates an error translating the conceptual representation to the algebraic: students have taken the factor of two for mass mass into account, but applied it to the wrong side of the equation (a common and well-documented error in forming algebraic representations of verbal statements). Answer (3)—typically the most common—is the unweighted average of the starting temperatures. Students can arrive at this by simplistically splitting the difference, or by reasoning with the specifi c heat instead of the heat capacity. In either case, the are neglecting the difference in the objects’ masses. The question does not explicitly state that the material’s specifi c heat is independent of temperature. We are assuming it is. If students do not detect and articulate this ambiguity, you can raise it yourself and ask how a temperature-dependent specifi c heat might affect the answer. (Even if you don’t wish to spend time discussing the question, you can mention it as an aside so that top-end students have something extra to keep engaged with. We fi nd it productive to throw the bright and easily bored an extra bone to chew on now and then.) Question J2.03 Description: Understanding temperature and heat fl ow in a familiar context, and paying attention to environmental effects. Question To have your coffee be as hot as possible when you drink it later, when should you add room temperature cream? 1. As soon as the coffee is served 2. Just before you drink it 3. Either; it makes no difference. 4. It is impossible to determine. Commentary Purpose: To explore energy exchanges in everyday situations. Discussion: When two liquids are mixed, such as the coffee and the cream in this situation, the hot coffee loses some energy and the cream gains the same amount of energy, so that they come to some fi nal temper-ature between the two initial temperatures. The specifi c fi nal temperature depends upon the masses, specifi c heats, and initial temperatures of the coffee and cream.
  • 4. 528 Chapter 11 If the coffee and cream existed in isolation, and no heat could leave the system, it wouldn’t matter when they were mixed. However, the hot coffee—before or after cream is added—is constantly losing heat to the surrounding air. The coffee will take a long time to reach room temperature, but we know that it will eventually occur. The rate at which energy is exchanged depends on the difference in temperature between the coffee and the air: The larger the difference in temperature, the larger the rate of energy exchange. If the cream is added early, the temperature difference between coffee and air is smaller than if it is not, so less heat escapes to the air. The coffee will be hotter if you add the cream right away. Key Points: • The rate at which heat fl ows between two objects or substances is proportional to the temperature difference between them. • When two substances of different temperatures are mixed, the new, combined temperature is somewhere between the initial temperatures. • Sometimes heat lost to or gained from a system’s environment is signifi cant in analyzing a situation. For Instructors Only Many students will neglect the effect of the environment on the temperature of the coffee. In some ways, they have been taught to neglect the environment. Some students will think that the answer is impossible to determine, because they recognize the importance of the environment but have not been taught how to compute its effect. The correct answer will seem counterintuitive to some students. They simply will not believe that to keep something hot, you need to cool it down fi rst! Question J2.04 Description: Reasoning about temperature and thermal equilibrium. Question Two identical thermodynamic systems, one at T1 and the other at T2, are placed in thermal contact. When they reach thermal equilibrium, what is true about the fi nal temperature? 1. Tfinal 1 (T + T ) 2 1 2 2. T = 1 ( T + T ) final2 1 2 3. T 1 ( T + T ) final2 1 2 4. Not enough information Commentary Purpose: To develop your ability to reason about temperature and thermal equilibrium. Discussion: You might think it is impossible to determine, because you are not told enough about the systems, but it turns out that you know all that you need to know. Since the systems are “identical,” it means that as they are exchanging energy by heat, their temperatures are changing by the exact same amount. Therefore, when they are done, their temperatures must also have changed by the exact same amount, which means they end up at the average of their temperatures: answer (2).
  • 5. Energy in Thermal Processes 529 Let’s assume that T1 is smaller than T2. Mathematically, the change in temperature of the cooler system is 1 (T + T ) − T = 2 (T2 − T1). The change in temperature of the warmer system is 2 1 2 1 1 1 2 2 1 − ( − ) = ( − ), the same result. T 1 T T T T 2 2 1 2 For Instructors Only Some students might choose the correct response for the wrong reasons, so it is useful to fi nd out why students are choosing their answers. Some of the more thoughtful students will think that it is impossible to determine, either because so little is said about the systems, or because the correct answer just seems too simple and they suspect a catch. (Actually, we are implicitly assuming that the systems have a constant heat capacity. Since the heat lost by one system must equal the heat gained by the other, if heat capacity varies with temperature, the fi nal temperature is not necessarily midway between T1 and T1. Answer (4) is defensible with this reasoning.) Question J9.01 Description: Understanding Stefan’s law. Texts: Principles of Physics, Scientists Engineers Question By what factor would the total power from a black body be modifi ed if the surface area were to decrease by a factor of two while the temperature was doubled? 1. 116 2. 18 3. 14 4. 1 5. 4 6. 8 7. None of the above 8. Cannot be determined Commentary Purpose: To check your understanding of the primary quantities upon which black-body radiation power depends. Discussion: Along with conduction and convection, radiation is one of the important energy fl ow processes, and you should be familiar with the primary factors governing the rate at which energy is radiated. According to the Stefan-Boltzmann law, the power radiated from a black body is proportional to the surface area of the body and to the fourth power of the body’s Kelvin temperature. Thus, if the temperature is doubled and the surface area halved, the power radiated would change by 242 8.
  • 6. 530 Chapter 11 Key Points: • The power radiated from a black body is proportional to the surface area of the body. • The power radiated from a black body is proportional to the fourth power of the body’s Kelvin temperature. For Instructors Only Students frequently obtain the inverse of the correct response, obtaining 18 rather than 8. In general, it is important to ask students how they arrived at their answers in order to distinguish algebra mistakes from misremembered formulas or erroneous thinking. It is useful to extend the discussion of this question by contrasting radiation to the other energy fl ow processes. Black body radiation is unique in that the power radiated depends upon the properties of the body itself, not to differences between the body and its environment. QUICK QUIZZES 1. (a) Water, glass, iron. Because it has the highest specifi c heat (4 186 J kg⋅°C), water has the smallest change in temperature. Glass is next (837 J kg⋅°C), and iron (448 J kg⋅°C) is last. (b) Iron, glass, water. For a given temperature increase, the energy transfer by heat is proportional to the specifi c heat. 2. (b). The slopes are proportional to the reciprocal of the specifi c heat, so larger specifi c heat results in a smaller slope, meaning more energy to achieve a given change in temperature. 3. (c). The blanket acts as a thermal insulator, slowing the transfer of energy by heat from the air into the cube. 4. (b). The rate of energy transfer by conduction through a rod is proportional to the difference in the temperatures of the ends of the rod. When the rods are in parallel, each rod experiences the full difference in the temperatures of the two regions. If the rods are connected in series, neither rod will experience the full temperature difference between the two regions, and hence neither will conduct energy as rapidly as it did in the parallel connection. 5. (a) 4. From Stefan’s law, the power radiated from an object at absolute temperature T is proportional to the surface area of that object. Star A has twice the radius and four times the surface area of star B. (b) 16. From Stefan’s law, the power radiated from an object having surface area A is proportional to the fourth power of the absolute temperature. Thus, P P A B B =σ Ae (2T )4 = 24 (σ AeT 4 ) = 16 . (c) 64. When star A has both twice the radius and twice B the absolute temperature of star B, the ratio of the radiated powers is P P A B 4 ( )( ) = A A = 4 2 B B 4 2 1 4 ( A 2 ) ( 2 ) ) = = ( )( ) = 4 1( A R T R T B ( ) B σ σ σ π σ π A eT A eT R T R T 4 B B 2 B 4 B 2 2 64 2 4 2 4
  • 7. Energy in Thermal Processes 531 ANSWERS TO MULTIPLE CHOICE QUESTIONS 1. From the mechanical equivalent of heat, 1 cal = 4.186 J. Therefore, . × = × ( )⎛⎝ 3 50 10 3 50 10 4 186 1 . 3 . 3 ⎞⎠ cal cal J cal = 1.47 × 104 J and (b) is the correct choice for this question. 5 5 1 1 . × = ( . × )⎛ 2. 7 80 10 7 80 10 ⎝ ⎜ ⎞ ⎠ ⎟ J J cal 4.186 J Cal cal 186 Cal 103 ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = , so (a) is the correct choice. 3. The required energy input is Q = mc(ΔT ) = (5.00 kg)(128 J kg ⋅°C)(327°C − 20.0°C) = 1 96 × 10. 5 J and the correct response is (e). 4. The energy which must be added to the 0°C ice to melt it, leaving liquid at 0°C, is = = (2.00 kg)(3.33 × 105 J kg) = 6.66 × 105 J Q mLf 1 = − = 9 30 × 105 − 6 66 × 105 = 2 64 × 105 total . J . J . J of energy Once this is done, there is Q Q Q 2 1 still available to raise the temperature of the liquid. The change in temperature this produces is Q mc f = − = = × ΔT T 2 64 10 ( ) 0 4 186 2 5 °C J 2.00 kg water . J kg °C °C ( ⋅ ) = 31 5 . so the fi nal temperature is Tf= 0°C + 31.5°C = 31.5°C and the correct choice is (c). 5. The rate of energy transfer by conduction through a wall of area A and thickness L is P = kA(T − T ) L h c , where k is the thermal conductivity of the material making up the wall, while T T h c and are the temperatures on the hotter and cooler sides of the wall, respectively. For the case given, the transfer rate will be P = J ⋅ ⋅ ⎛⎝ ⎞⎠ ( ) ( − ) ( − )= × = × × 0 10 48 0 25 14 . . s m °C m °C °C 4.00 2 10 3 3 1 3 10 1 3 10 2 m . J s . W and the (d) is the correct answer. 6. The power radiated by an object with emissivity e, surface area A, and absolute temperature T, in a location with absolute ambient temperature T, is given by P =σ Ae(T 4 − T 4 ) 00 where σ = 5.669 6 × 10−8 W m2 ⋅K4 is a constant. Thus, for the given spherical object (A = 4π r2 ), we have P = (5 669 6 ×10−8 ⋅ )4 (2 00 )2 (0 450) 408 . . . W m K m 2 4 π K K ( ) − ( ) ⎡⎣ ⎤⎦ 4 4 298 yielding P = 2.54 × 104 W, so (e) is the correct choice. 7. The temperature of the ice must be raised to the melting point, ΔT = +20 0 . °C, before it will start to melt. The total energy input required to melt the 2.00-kg of ice is = ( ) + = ( ) ( ⋅ ) ice kg J kg °C ° Δ 2 00 2 090 20 0 . . C J kg J ( ) + × ⎡⎣ Q mc T mLf ⎤⎦ 3.33 105 = 7.50 × 105 The time the heating element will need to supply this quantity of energy is Δt Q = = × × = ⎛ P 7 50 10 10 750 . 5 J 1.00 J s s 1 min 3 ⎝ 60 s ⎞⎠ = 12 5. min making (d) the correct choice.
  • 8. 532 Chapter 11 8. We use −Q = Q hot cold or −m c (T − T ) = m c (T − T ) x x f x,i w w f w,i to compute the specifi c heat of the unknown material and fi nd c m c T T m T T x w w f wi x f xi = ( − ) , ( ) = − ( − ) , ( ⋅ )( − ) ( ) − 0.400 kg 4 186 J kg °C °C °C J kg °C ( ) = × ⋅ 0.250 kg °C 36 0 20 0 36 0 9 . . . 5 0 1 82 103 . . °C which is a match for the specifi c heat of Beryllium, so (b) is the correct choice. 9. Since less energy was required to produce a 5°C rise in the temperature of the ice than was required to produce a 5°C rise in temperature of an equal mass of water, we conclude that the specifi c heat of ice (c = Q m(ΔT )) is less than that of water. Thus, choice (d) is correct. 10. With e e A B = , r r A B = 2 , and T T A B = 2 , the ratio of the power output of A to that of B is P P A B 4 A A A B B B A A B B A B A e T A e T r T r T r r σ σ π π = = = 4 2 4 2 4 4 4 ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = ( ) ( ) = ( ) = 2 4 2 4 6 2 2 2 64 T T A B making (e) the correct choice. 11. By agitating the coffee inside this sealed, insulated container, the person is raising the internal energy of the coffee, which will result is a rise in the temperature of the coffee. However, doing this for only a few minutes, the temperature rise will be quite small. The correct response to this question is (d). 12. One would like the poker to be capable of absorbing a large amount of energy, but undergo a small rise in temperature. This means it should be made of a material with a high specifi c heat capacity. Also, it is desirable that energy absorbed by the end of the poker in the fi re be conducted to the person holding the other end very slowly. Thus, the material should have a low thermal conductivity. The correct choice is (d). ANSWERS TO EVEN-NUMBERED CONCEPTUAL QUESTIONS 2. In winter the produce is protected from freezing. The specifi c heat of Earth is so high that soil freezes only to a depth of a few inches in temperate regions. Throughout the year the temperature will stay nearly constant day and night. Factors to be considered are the insulating properties of the soil, the absence of a path for energy to be radiated away from or to the vegetables, and the hindrance of the formation of convection currents in the small, enclosed space. 4. The high thermal capacity of the barrel of water and its high heat of fusion mean that a large amount of energy would have to leak out of the cellar before the water and produce froze solid. Evaporation of the water keeps the relative humidity high to protect foodstuffs from drying out. 6. Yes, if you know the specifi c heat of zinc and copper, you can determine the relative fraction of each by heating a known weight of pennies to a specifi c initial temperature, say 100° C, then dump them into a known quantity of water, at say 20° C. The equation for conservation of energy will be m xc x T m c pennies water wa [ ⋅ + ( − ) ]( ° − ) = Cu Zn 1 c 100 C ter (T − 20°C) The equilibrium temperature, T, and the masses will be measured. The specifi c heats are known, so the fraction of metal that is copper, x, can be computed.
  • 9. Energy in Thermal Processes 533 8. Write mwatercwater (1°C) = (ρairV )cair (1°C), to fi nd V ( × ) water water m c = = c air air kg J kg ρ 1.0 103 (4 186 ⋅⋅ ° C ) ( )( × × ⋅ ° )= m 3 kg m J kg C 3 1 3 1 0 10 3 2 10 3 3 . . . 10. The black car absorbs more of the incoming energy from the Sun than does the white car, making it more likely to cook the egg. 12. Keep them dry. The air pockets in the pad conduct energy slowly. Wet pads absorb some energy in warming up themselves, but the pot would still be hot and the water would quickly conduct a lot of energy to your hand. PROBLEM SOLUTIONS 11.1 As mass m of water drops from top to bottom of the falls, the gravitational potential energy given up (and hence, the kinetic energy gained) is Q = mgh. If all of this goes into raising the temperature, the rise in temperature will be ΔT = = = ( Q mc mgh mc )( ) water water 9 . 80 m s2 807 m 4 18 6 1 89 J kg °C °C ⋅ = . and the fi nal temperature is T T T f i = + Δ = 15.0°C+1.89°C = 16.9°C . 11.2 Q = mc(ΔT ) = (1.50 kg)(230 J kg ⋅°C)(150°C − 20.0°C) = 4.49 × 104 J = 44.9 kJ 11.3 The mass of water involved is ρ 103 kg (4 00 × 1011 ) = 4 00 × 1014 m V = =⎛⎝ ⎞⎠ m . 3 . g m k 3 (a) Q = mc(ΔT ) = (4.00 × 1014 kg)(4 186 J kg ⋅°C)(1.00°C) = 1.67 × 1018 J (b) The power input is P = 1 000 MW= 1.00 ×109 J s , so, t Q = = × 18 ⎛ 1 9 × × P 1 . 67 10 1 . 00 10 J J s yr 3.156 10 s 7 ⎝ ⎜ ⎞ ⎠ ⎟= 52 9 . yr 11.4 The change in temperature of the rod is ΔT = = × Q mc 4 1 ( )( ) = 900 31 7 .00 10 J ° 0.350 kg J kg C . °C and the change in the length is ΔL = L (ΔT ) = × ( ) ⎡⎣ − − ( ) ⎤⎦ α 0 6 1 24 10 °C 20.0 cm (31.7°C) = 1.52 × 10−2 cm = 0.152 mm Q mc f = − = =( 11.5 ΔT T 750 0 168 25 °C )( ⋅ ) cal 75 g . cal g °C = 60°C so Tf= 25°C + 60°C = 85°C
  • 10. 534 Chapter 11 11.6 (a) Q = ⎛ 103 4 186 ⎞ 540 ⎝ ⎜ ⎞ ⎠ ⎟ ⎛ ⎝ ⎜ Cal cal 1 Cal J . 1 cal ⎠ ⎟ = 2.3 × 106 J (b) The work done lifting her weight mg up one stair of height h is W mgh 1 = . Thus, the total work done in climbing N stairs is W = Nmgh, and we have W = Nmgh = Q or N = = × Q mgh 2 3 10 ( )( = 9 80 )( 0 15 ) 2 . 6 J . . 55 kg m s2 m .8 × 104 stairs (c) If only 25% of the energy from the donut goes into mechanical energy, we have N 0 25 0 25 2 8 104 . 0 25 Q = × mgh Q mgh = = ⎛ . . ( . stairs) = 7.0 × 103 stairs ⎝ ⎜ ⎞ ⎠ ⎟ net = Δ = ( − ) = ( kg) ( m s) − 1 2 2 v v . ⎡⎣ 11.7 (a) W KE mf 2 1 2 2 75 11 0 0 0 ⎤⎦ = 4.54 × 103 J → 4.5 × 103 J W × J (b) P= net = = × = t 5.0 s J s W Δ 4 54 10 9 1 10 910 3 . 2 . (c) If the mechanical energy is 25% of the energy gained from converting food energy, then W Q net = 0.25(Δ ) and P = 0.25 (ΔQ) Δt, so the food energy conversion rate is Δ Q t Δ P = 0 25 = =⎛⎝ ⎞⎠ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ 910 1 . J s 0.25 Cal 4 186 J 0.87 Cal s (d) The excess thermal energy is transported by conduction and convection to the surface of the skin and disposed of through the evaporation of sweat. 11.8 (a) The instantaneous power is P = Fv , where F is the applied force and v is the instantaneous velocity. (b) From Newton’s second law, F ma net = , and the kinematics equation v = v + 0 at with v0 = 0, the instantaneous power expression given above may be written as P = Fv = (ma)(0 + at ) or P = ma2t (c) a = = − Δ v v 0 = 11 0 = Δ t t − 0 5 00 2 20 . . . m s s m s2 (d) P = ma2t = ( )( ) t = ( ⋅ )⋅ 2 75.0 kg 2.20 m s2 363 kg m2 s4 t = (363 W s)⋅ t (e) Maximum instantaneous power occurs when t = t = max 5.00 s, so Pmax = (363 J s2 )(5.00 s) = 1.82 × 103 J s If this corresponds to 25.0% of the rate of using food energy, that rate must be Δ Δ Q t = P = × ⎛ max . 1 . 82 10 0 250 . 3 J s Cal 0 250 1 4 186 J ⎝ ⎜ ⎞ ⎠ ⎟ = 1.74 Cal s 11.9 The mechanical energy transformed into internal energy of the bullet is Q KE m m i i i = ( ) = ( ) = 12 12 12 v v2. Thus, the change in temperature of the bullet is 2 14 ΔT i = = = ( Q mc m mc ) ( ⋅ ) = 14 2 2 300 4 1 v lead m s 28 J kg °C 176°C
  • 11. Energy in Thermal Processes 535 11.10 The internal energy added to the system equals the gravitational potential energy given up by the 2 falling blocks, or Q = ΔPEg = 2mbgh. Thus, ΔT 2 2 1.50 kg)(9.80 m s2 ) 3.00 m = = = ( Q m c m gh b m c w w w w kg J kg °C C ( ) ( )( ⋅ ) = 0 200 4 186 0 105 . . ° 11.11 The quantity of energy transferred from the water-cup combination in a time interval of 1 minute is Q mc mc T = ( ) + ( ) ⎡⎣ ⎤⎦ ( ) water cup = ( kg ) Δ 0.800 4 186 J kg C 0.200 900 kg J ⎛ ⋅ kg C ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ + ( ) ⋅ ⎝ ⎜ ⎞ ⎠ ⎟ ⎡ ⎣ ⎢ ° ° ⎤ ⎦ ⎥ (1.5°C) = 5.3 × 103 J The rate of energy transfer is P= = × = = Q Δt 5 3 10 88 88 . 3 J 60 s J s W 11.12 (a) The mechanical energy converted into internal energy of the block is Q KE m i i = = 0 85 0 85 12 . ( ) . ( v2 ). The change in temperature of the block will be ΔT i = = ( ) = ( ) Q mc 0 85 m 0 85 3 0 mc Cu Cu m s 87 2 3 12 2 2 . v . . J kg C C ( ⋅ )= × − ° 9.9 10 3 ° (b) The remaining energy is absorbed by the horizontal surface on which the block slides. 11.13 From ΔL =α L (ΔT ) 0 , the required increase in temperature is found, using Table 10.1, as Δ Δ T = = × L L − 3 0 10 10 13 ( × ( ) ) α − 6 − steel m 0 11 °C 3 1 . ( ) °C yd yd 3.0 ft ft 1 m ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ⎛ ⎞ ⎟ ⎠ ⎜⎝ = 1 3 281 23 . The mass of the rail is m = =( )( ) ⎛ w g ⎝ ⎜ 70 lb yd 13 yd 9.80 m s 4.448 N 2 1 lb ⎞ ⎠ ⎟ = 4.1 × 102 kg so the required thermal energy (assuming that c c steel iron = ) is Q = mc ( T ) = ( × )( ⋅ )( steel Δ 4.1 102 kg 448 J kg °C 23°C) = 4.2 × 106 J 11.14 (a) From the relation between compressive stress and strain, F A = Y (ΔL L ) 0 , where Y is Young’s modulus of the material. From the discussion on linear expansion, the strain due to thermal expansion can be written as (ΔL L ) (ΔT ) 0 =α , where α is the coeffi cient of linear expansion. Thus, the stress becomes F A = Y [α (ΔT )] . (b) If the concrete slab has mass m, the thermal energy required to produce a change in temperature ΔT is Q = mc(ΔT ) where c is the specifi c heat of concrete. Using the result from part (a), the absorbed thermal energy required to produce compressive stress F A is Q mc F A Y = ⎛⎝ ⎞⎠ α or Q mc Y F A = ⎛⎝ ⎞⎠ α continued on next page
  • 12. 536 Chapter 11 (c) The mass of the given concrete slab is m V = = × ( ) × ( )( ) − ρ 2 40 10 4 00 10 1 00 1 3 2 . . . . kg m m m 3 00 96 0 m kg ( ) ⎡⎣ ⎤⎦ = . (d) If the maximum compressive stress concrete can withstand is F A = 2.00 × 107 Pa, the maximum thermal energy this slab can absorb before starting to break up is found, using Table 10.1, to be F A max Q mc Y max . . = ⎛⎝ ⎞⎠ = ( )( ⋅ ) α 96 0 880 2 1 kg J kg °C ( )( ) ( × 7 ) = × 10 12 × 10− ( ) − 2 00 10 6 10 6 1 Pa °C . Pa .7 × 106 J (e) The change in temperature of the slab as it absorbs the thermal energy computed above is ΔT = = × Q mc 6 7 10 ( )( ) = 79 ° 880 ⋅ . 6 J 96.0 kg J kg °C C (f ) The rate the slab absorbs solar energy is P P absorbed solar = 0.5 = 0.5(1.00 × 103 W) = 5 × 102 J s so the time required to absorb the thermal energy computed in (d) above is t Q = = × . 6 1 × ⎛ ⎝ ⎜ ⎞ Pabsorbed 2 J 5 Js h 3 600 s 6 7 10 10 ⎠ ⎟ ∼ 4 h 11.15 When thermal equilibrium is reached, the water and aluminum will have a common temperature of Tf = 65 0 . °C. Assuming that the water-aluminum system is thermally isolated from the environment, Q Q cold hot = − , so mc T T m c T T w w f iw f i ( − ) = − ( − ) , Al Al ,Al , or m Al Al ,Al −( kg) m c T T c T T w f i w f iw = − ( − ) ( − ) = , ( ⋅ )( − ) 1.85 900 65 0 J kg °C °C 150°C 65 0 ( 4 186 J kg ⋅ °C ) . . °C °C kg ( − ) = 25 0 0 845 . . 11.16 If N pellets are used, the mass of the lead is Nmpellet . Since the energy lost by the lead must equal the energy absorbed by the water, Nm c T mc T pellet lead water (Δ ) = [ (Δ )] or the number of pellets required is N = w w w ( ) Δ Δ pellet lead lead 0.500 kg 4 186 25 0 20 0 m c T m c T = ( ) ( J kg ⋅ C )( C − C ) 128 ( 1.00 × 10-3 kg ) ° . ° . ° ( J kg⋅ C)( C− C) = ° 200° 25 0° 467 .
  • 13. Energy in Thermal Processes 537 11.17 The total energy absorbed by the cup, stirrer, and water equals the energy given up by the silver sample. Thus, mccAl mscCu mwcw T w mc T Ag [ + + ](Δ ) = [ Δ ] Solving for the mass of the cup gives m = ( m c )( c )− − s w w T T m c m c c w ⎡ ⎣ ⎢ ⎤ ⎦ ⎥ 1 Al Ag Ag Ag Cu Δ Δ , or mc = ( )( ) ( − ) g 40 g (387) − ( )( ) ⎡ ( − ) 1 − ( ) 900 400 234 87 32 32 27 ⎣ ⎢ ⎤ 225 g 4 186 = 80 g ⎦ ⎥ 11.18 The mass of water is m V w w w = ρ = (1.00 g cm3 )(100 cm3 ) = 100 g = 0.100 kg For each bullet, the energy absorbed by the bullet equals the energy given up by the water, so m c T m c T b b w w ( − 20°C) = (90°C − ). Solving for the fi nal temperature gives T = m c ( 90°C ) + m c ( 20°C ) w w b b + m c m c w w b b . For the silver bullet, m c b b = 5.0 × 10−3 kg and = 234 J kg ⋅°C, giving Tsilver °C = (0.100)(4 186)(90 ) + (5.0 × 10−3 )(234) 20 89 8 3 0 100 4 186 5 0 10 234 °C °C ( ) ( )( ) + ( × )( ) = . . − . For the copper bullet, m c b b = 5.0 × 10−3 kg and = 387 J kg ⋅°C, which yields Tcopper °C = (0.100)(4 186)(90 ) + (5.0 × 10−3 )(387) 20 89 7 3 0 100 4 186 5 0 10 387 °C °C ( ) ( )( ) + ( × )( ) = . . − . Thus, the copper bullet wins the showdown of the water cups. 11.19 The total energy given up by the copper and the unknown sample equals the total energy absorbed by the calorimeter and water. Hence, m c T m c T mc m c T Cu Cu Cu unk unk unk c Al w w w Δ + Δ = [ + ](Δ ) Solving for the specifi c heat of the unknown material gives c m c m c T m c T c w w w m T unk Al Cu Cu Cu unk unk = [ + ](Δ ) − Δ Δ , or { ( ) = g J kg °C g ( )( ) ( )( ⋅ ) + 1 cunk g °C 70 80 100 900 250 ( ) ⋅ ( ) ⎡⎣ ⎤⎦ − ( ) 4 186 10 50 J kg °C °C g (387 J kg ⋅°C)(60°C)} = 1.8 × 103 J kg ⋅°C
  • 14. 538 Chapter 11 11.20 The energy absorbed by the water equals the energy given up by the iron and they come to thermal equilibrium at 100°F. Thus, considering cooling 1.00 kg of iron, we have mwcw (ΔT )w = m c ΔT Fe Fe Fe or m 1.00 kg c Δ T Fe Fe = ( ) ( ) c T w Δ w w giving mw = ( ) (1 00 )(448 ⋅ )(500 − 100 ) 1 9 5 . kg J kg °C °F °F °C °F ( = 4 186 J kg ⋅ °C )( 100 °F − 75 °F ) ( 1 °C °F ) 1 7 9 5 . kg 11.21 Since the temperature of the water and the steel container is unchanged, and neither substance undergoes a phase change, the internal energy of these materials is constant. Thus, all the energy given up by the copper is absorbed by the aluminum, giving m c T m c T Al Al Al Cu Cu Cu (Δ ) = Δ , or m c c T T = Cu Cu m Al Al Cu Al ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ( ) ⎡ ⎣ ⎢ ⎤ ⎦ ⎥ = ⎛ Δ Δ 387 ⎝ 900 ⎞⎠ − − ⎛⎝ 200 2 6 102 ° ° ° ° ( )= × 85 25 ⎞⎠ C 25C C 5.0 C g . g = 0.26 kg 11.22 The kinetic energy given up by the car is absorbed as internal energy by the four brake drums (a total mass of 32 kg of iron). Thus, ΔKE = Q = m c (ΔT ) drums Fe or ΔT 1 v ( kg )( m s ) = i = m 2 m c 2 1 500 30 32 2 1 2 ( )( ) = °C ⋅ car drums Fe 448 kg J kg °C 47 11.23 (a) Assuming that the tin-lead-water mixture is thermally isolated from the environment, we have Q Q cold hot = − or m c T T m c T T m c T T w w f iw f i f i ( − ) = − ( − )− − , Sn Sn ,Sn Pb Pb ,Pb ( ) and since m m m Sn Pb metal = = = 0.400 kg and T T T i, i, . Sn Pb hot = = = 60 0°C, this yields T m c T m c c T w w iw ( + ) m c m c f w w = + ( + ) + , metal Sn Pb hot c metal Sn Pb = ( )( ⋅ )( ) + 1.00 kg 4 186 J kg °C 20.0 °C 0.400 227 128 60 0 1 00 kg J kg °C J kg °C °C kg ( )( ⋅ + ⋅ )( . ) ( . )(4 186 J kg ⋅°C) + (0.400 kg)(227 J kg ⋅°C + 128 J kg ⋅°C) yielding Tf = 21 3 . °C (b) If an alloy containing a mass mSn of tin and a mass mPb of lead undergoes a rise in tempera-ture ΔT, the thermal energy absorbed would be Q = Q +Q Sn Pb, or m m c T m c T m c T Sn Pb alloy Sn Sn Pb Pb ( + ) ( Δ ) = ( Δ )+ ( Δ ) giving c m c m c Sn Sn Pb Pb m m alloy Sn Pb = + + If the alloy is a half-and-half mixture, so m m Sn Pb = , this reduces to c c c alloy Sn Pb = ( + ) 2 and yields calloy = 227 J kg ⋅ °C + 128 J kg ⋅ °C = J kg ⋅ °C 2 178 continued on next page
  • 15. Energy in Thermal Processes 539 (c) For a substance forming monatomic molecules, the number of atoms in a mass equal to the molecular weight of that material is Avogadro’s number, NA. Thus, the number of tin atoms in mSn = 0.400 kg = 400 g of tin with a molecular weight of MSn = 118.7 g mol is N m M Sn NSn A Sn g 118.7 g mol = ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ 400 (6.02 × 1023 mol−1 ) = 2.03 × 1024 and, for the lead, N m M Pb NPb A Pb g 207.2 g mol = ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ 400 (6.02 × 1023 mol-1 ) = 1.16 × 1024 (d) We have N N Sn Pb = × = 2 03 10 1 16 10 × 1 75 24 24 . . . and observe that c c Sn Pb = ⋅ 227 J kg °C = 128 J kg °C ⋅ 1.77 from which we conclude that the specific heat of an element is proportional to the number of atoms per unit mass of that element. 11.24 Assuming that the unknown-water-calorimeter system is thermally isolated from the environment, −Q = Q hot cold, or −m c T − T = m c T − T + m c T − T x x f ix ww f iw f i ( ) ( ) ( , , Al Al ,Al ) and, since T T T i,w i, = = = . Al cold 25 0°C, we have c m c m c T T m T T x w w f x i x f = ( + )( − ) ( − ) Al Al cold , or cx = ⋅ ( ) ⎡⎣ (0.285 kg)(4 186 J kg ⋅°C) + (0.150 kg) 900 J kg °C °C kg °C ⎤⎦ ( − ) ( ) − 32 0 25 0 0 125 95 0 32 . . . ( . .0°C) yielding cx= 1.18 × 103 J kg ⋅°C . 11.25 Remember that energy must be supplied to melt the ice before its temperature will begin to rise. Then, assuming a thermally isolated system, Q Q cold hot = − , or m L m c T m c T ice f ice water f w water f + ( − 0°C) = − ( − 25°C) and T 25°C (825 g )(4 186 J kg ⋅°C)(25°C) − (75 g )(3.33 × 105 J kg) m c m L w f m m c f w = ( ) − water ice ( + ) = ice water (75 g + 825 g )(4 186 J kg ⋅°C) yielding Tf = 16°C .
  • 16. 540 Chapter 11 11.26 The total energy input required is Q = ( energy to melt 50 g of ice ) + energy ( to warm 50 g of water to 100°C) + energy to vaporize 5.0 g water 50 g ( ) = ( ) L c L f + (50 g) (100 C − 0 C) + (5.0 g) water ° ° v Thus, ⎛ Q = ( ) × ⎝ ⎜ ⎞ ⎠ ⎟ 0.050 kg J kg 3.33 105 +(0.050 kg) J k 4 186 g °C 100°C 0°C ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ( − ) ⎛ + ( × ) × ⎝ ⎜ ⎞ ⎠ ⎟ 5.0 10− kg J kg 3 2.26 106 which gives Q = 4.9 × 104 J = 49 kJ . 11.27 The conservation of energy equation for this process is (energy to melt ice) + (energy to warm melted ice to T ) = (energy to cool water to T ) or m L m c T m c T ice f ice w w w + ( − 0°C) = (80°C − ) This yields T m c m L w w f m m c w w = ( ) − ( + ) 80°C ice ice so T = (1.0 kg)(4 186 J kg ⋅°C)(80°C) − (0.100 kg) 3.33 10 1 1 4 186 65 ( × 5 J kg ) ( )( ⋅ ) = kg J kg °C °C . 11.28 The energy required is the following sum of terms: Q = ( ) energy to reach melting point (energy to melt) + energy to reach boiling point + ( ) + ( e nergy to vaporize) + (energy to reach 110°C) Mathematically, Q m c L c L c f w = [ − (− )]+ + ( − ) + + ice s 0°C 10°C 100°C 0°C v team °C °C 110 100 − ( ) ⎡⎣⎤⎦ This yields ⎛ Q = ( × ) ⋅ 40 10−3 kg 2 090 (10 ) + 3 33 × ⎝ ⎜ ⎞ ⎠ ⎟ J kg °C °C . 10 ⎛ J 4 186 5 J kg J kg ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ⎡ ⎣ ⎢ + ⋅°C 100 °C 2.26 106 + 2 010 J kg ⎝ ⎜ ⎞ ⎠ ⎟ ( ) + ⎛ × ⎝ ⎜ ⎞ ⎠ ⎟ kg °C °C ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ( )⎤ ⎦ ⎥ 10 or Q = 1.2 × 105 J = 0.12 MJ
  • 17. Energy in Thermal Processes 541 11.29 Assuming all work done against friction is used to melt snow, the energy balance equation is ⋅ = snow . Since f = μk (m g) skier , the distance traveled is f s m Lf s m L f m g = ( ) = k ( )( × ) snow skier kg J kg μ 1.0 3.33 105 0.20 kg m s ( )( )= × = 2 3 103 2 3 m km 75 9 . 80 2 . . 11.30 (a) Observe that the equilibrium temperature will lie between the two extreme temperatures (−10.0°C and +30.0°C) of the mixed materials. Also, observe that a water-ice change of phase can be expected in this temperature range, but that neither aluminum nor ethyl alcohol undergoes a change of phase in this temperature range. The thermal energy transfers we can anticipate as the system come to an equilibrium temperature are: ice at − 10.0°C to ice at 0°C; ice at 0°C to liquid water at 0°C; water at 0°C to water at T; aluminum at 20.0°C to aluminum at T; ethyl alcohol at 30.0°C to ethyl alcohol at T. (b) Q m (kg) c (J kg ⋅°C) L (J kg) Tf (°C) Ti (°C) Expression Qice 1.00 2 090 0 −10 0 . m c ice ice [0 − (−10.0°C)] Qmelt 1.00 3.33 × 105 0 0 m Lice f Qwater 1.00 4 186 T 0 m c T ice water ( − 0) QAl 0.500 900 T 20.0 m c T Al Al [ − 20.0°C] Qalc 6.00 2 430 T 30.0 m c T alc alc [ − 30.0°C] (c) m c m L m c T m ice ice ice f ice water Al (10.0°C)+ + ( − 0)+ c T m c T Al alc alc [ − 20.0°C]+ [ − 30.0°C] = 0 (d) T ( ) + ( ) − Al Al alc alc ice ice 20.0°C 30.0°C 10.0°C ( ) + ⎡⎣ m c m c m c = ice water Al Al alc alc ⎤⎦ + + L m c m c m c f Substituting in numeric values from the table in (b) above gives T = (0.500)(900)(20.0) + (6.00)(2 430)(30.0) − 1.00 2 090 10 0 3 33 10 1 00 4 186 0 5 ( ) ( )( ) + × ⎡⎣ ⎤⎦ ( )( ) + . . . ( .500)(900) + (6.00)(2 430) and yields T = 4.81°C .
  • 18. 542 Chapter 11 11.31 Assume that all the ice melts. If this yields a result T 0, the assumption is valid, otherwise the problem must be solved again based on a different premise. If all ice melts, energy conservation (Qcold = −Q) yields hot m c L c T mc ice ice f w w °C 78°C °C 0 0 − − ( ) [ ] + + − ( ) ⎡⎣ ⎤⎦ = − w ( + m c )(T − ) cal Cu 25°C or T + ( )( ) − ( ) + ⎡⎣ ⎤ cal Cu ice ice 25°C 78°C ⎦ (m + m )c + m c w ice w cal Cu m c m c m c L w w f = With m m m c w w = 0.560 kg, = 0.080 g, = 0.040 g, cal ice = 4 186 J kg ⋅°C, J kg °C J kg °C, and Cu ice c = 387 ⋅ , c = 2 090 ⋅ L = 3 f .33 ×105 J kg this gives T = ( )( ) + ( )( ) ⎡⎣ 0.560 4 186 0.080 387 (25°C) − 0.040 2 090 3 33 10 ⎤⎦ 0 560 0 040 4 5 ( ) ( )( ) + × ⎡⎣ ⎤⎦ ( + ) 78°C . . . ( 186) + 0.080(387) or T = 16°C and the assumption that all ice melts is seen to be valid. 11.32 At a rate of 400 kcal h, the excess internal energy that must be eliminated in a half-hour run is Q = × ⎛⎝ 3 h . ⎞⎠ ⎛⎝ ⎞⎠ 4 186 cal h J 400 10 ( 0 500 ) 1 cal . = 8.37 × 105 J The mass of water that will be evaporated by this amount of excess energy is m = = × Q L evaporated 6 J × 2.5 10 J kg = v 8 37 10 0 33 . 5 . kg The mass of fat burned (and thus, the mass of water produced at a rate of 1 gram of water per gram of fat burned) is mproduced (400 kcal h )(0.500 h ) = 9.0 kcal gram of fat = 22 g = 22 × 10−3 kg so the fraction of water needs provided by burning fat is f = = × = m m − produced evaporated kg kg 22 10 0 33 0 3 . .066 or 6.6%
  • 19. Energy in Thermal Processes 543 11.33 The mass of 2.0 liters of water is mw = ρV = (103 kg m3 )(2.0 × 10−3 m3 ) = 2.0 kg. The energy required to raise the temperature of the water (and pot) up to the boiling point of water is Q mc mc T boil w w Al Al = ( + )(Δ ) or = ( )⎛ J 2.0 4 186 + (0.25 ) 900 Qboil kg J kg kg ⎝ ⎜ ⎞ ⎠ ⎟ kg °C °C J ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ⎡ ⎣ ⎢ ⎤ ⎦ ⎥ (100 − 20 ) = 6.9 × 105 The time required for the 14 000 Btu h burner to produce this much energy is t Q boil boil Btu h . 5 J 1 Btu Btu h = = × 14 000 6 9 10 14 000 h min × 3 1.054 10 J ⎛⎝ ⎞⎠ = 4.7 × 10−2 = 2.8 Once the boiling temperature is reached, the additional energy required to evaporate all of the water is Q mL evaporate w = = ( kg)( × J kg) = × v 2.0 2.26 106 4.5 106 J and the time required for the burner to produce this energy is t Q boil evaporate Btu h J . 6 B = = × 14 000 4 5 10 14 000 tu h Btu h min 3 1 1.054 10 J 0 31 18 × ⎛⎝ ⎞⎠ = . = 11.34 In 1 hour, the energy dissipated by the runner is ΔE = P ⋅t = (300 J s)(3 600 s) = 1.08 ×106 J Ninety percent, or Q = 0.900(1.08 × 106 J) = 9.72 × 105 J, of this is used to evaporate bodily fl uids. The mass of fl uid evaporated is m = = × Q L × = v 9 72 10 10 0 403 5 6 . . J 2.41 J kg kg Assuming the fl uid is primarily water, the volume of fl uid evaporated in 1 hour is V . 6 0 403 = m = = ( 4 03 × 10 − ) ρ 4 10 . kg 1 000 kg m m cm 3 3 3 3 3 m cm 1 403 ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ =
  • 20. 544 Chapter 11 11.35 The energy required to melt 50 g of ice is Q m Lf 1 = = (0 050 )(333 ) = 16 7 ice . kg kJ kg . kJ The energy needed to warm 50 g of melted ice from 0°C to 100°C is Q m c T 2 w = ( ) = (0 050 )(4 ⋅ ) 100 ice Δ . kg .186 kJ kg °C ( °C) = 20.9 kJ (a) If 10 g of steam is used, the energy it will give up as it condenses is Q mL3 s = = (0 010 )(2 ) = 22 6 v . kg 260 kJ kg . kJ Since Q Q 3 1 , all of the ice will melt. However, Q Q Q 3 1 2 + , so the fi nal temperature is less than 100°C. From conservation of energy, we fi nd 0 = [ + (100 − )] v m L c T m L c T ice f w steam w °C °C + − ( ) ⎡⎣ ⎤⎦ or T + ( 100 °C ) ⎡⎣ v m L c m L steam ice w f = m m ⎤⎦ − ( + ice steam )cw giving T = 10 g 2.26 106 4 186 100 − (50 g)(3.33 × ) ( ) × + ( )( ) ⎡⎣ ⎤⎦ 10 ( + )( ) = 50 10 4 186 40 5 g g °C (b) If only 1.0 g of steam is used, then Q′ = m L = 3 s v 2.26 kJ. The energy 1.0 g of condensed steam can give up as it cools from 100°C to 0°C is = (Δ ) = (1.0 × 10−3 kg)(4.186 kJ kg ⋅°C)(100°C) = 0.419 kJ Q mc T 4 s w Since Q′ +Q 3 4 is less than Q1, not all of the 50 g of ice will melt, so the fi nal temperature will be 0°C . The mass of ice which melts as the steam condenses and the condensate cools to 0°C is m = ( + ) 3 4 2 26 = × −3 = ′ + Q Q Lf 8 0 10 . . 0.419 kJ 333 kJ kg kg = 8.0 g 11.36 First, we use the ideal gas law (with V = 0.600 L = 0.600 × 10−3 m3 and T = 37.0°C = 310 K) to determine the quantity of water vapor in each exhaled breath: PV nRT n PV RT = ⇒ = = (3.20 × 103 Pa)(0.600 × 10−3 m3 ) ( ⋅ )( ) = × − 8 31 310 7 45 10 4 . . J mol K K mol or m = nM = ( × )⎛ ⎝ ⎜ ⎞ ⎠ ⎟ − water mol g mol ⎛ 1 k 1 34 10 5 7.45 10 4 18.0 g g kg 103 ⎝ ⎜ ⎞ ⎠ ⎟ = . × − The energy required to vaporize this much water, and hence the energy carried from the body with each breath is Q = mL = ( × − )( × ) = v 1.34 10 5 kg 2.26 106 J kg 30.3 J The rate of losing energy by exhaling humid air is then P = ⋅( ) =⎛⎝ ⎞⎠ Q J breath b respiration rate 30.3 22.0 reaths min = 1 min 60 s W ⎛⎝ ⎞⎠ ⎛⎝ ⎞⎠ 11 1 .
  • 21. Energy in Thermal Processes 545 11.37 (a) The bullet loses all of its kinetic energy as it is stopped by the ice. Also, thermal energy is transferred from the bullet to the ice as the bullet cools from 30.0°C to the fi nal temperature. The sum of these two quantities of energy equals the energy required to melt part of the ice. The final temperature is 0°C because not all of the ice melts. (b) The total energy transferred from the bullet to the ice is 1 2 Q KE = i + mbulletclead 0°C− 30 0°C = mbullet i + m . v2 bullet lead °C kg c 30 0 3 00 10 J kg °C °C ( ) + ( ⋅ )( ) ⎡ ⎣ 2 40 10 3 2 . . . ( ) = ( × ) × − m s ⎢⎢ ⎤ ⎦ ⎥⎥ = 2 2 128 30.0 97.9 J The mass of ice that melts when this quantity of thermal energy is absorbed is m Q Lf = ( ) = × . 4 = × − water J J kg k 97 9 3 33 10 2 94 10 5 . . g 10 g 1 kg g ⎛ 3 ⎝ ⎜ ⎞ ⎠ ⎟ = 0.294 11.38 (a) The rate of energy transfer by conduction through a material of area A, thickness L, with thermal conductivity k, and temperatures T T h c on opposite sides is P = kA(T − T ) L h c . For the given windowpane, this is P = J ⋅ ⋅ ⎛⎝ ⎜ ⎞⎠ ⎟ ( )( ) ⎡⎣ ⎤⎦ ( − ) 0 84 1 0 2 0 25 . . . s m °C m m °C 0 10 6 8 103 6 8 103 °C = × = × − . . J s W 2 × 0.62 m (b) The total energy lost per day is E = P ⋅ Δt = (6.8 × 103 J s)(8.64 × 104 s) = 5.9 × 108 J 11.39 The thermal conductivity of concrete is k = 1.3 J s ⋅m⋅°C, so the energy transfer rate through the slab is P = ( − ) = kA h c J 1 3 ( ( 5 0 ) ⋅ ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ T T L 20 . . s m °C m °C 2 ) = × = × 12 − m × 1.1 103 1.1 103 J s W 10 2 11.40 (a) The R value of a material is R = L k, where L is its thickness and k is the thermal conductivity. The R values of the three layers covering the core tissues in this body are as follows: Rskin = × m m 2 K W ⋅ 0.020 W m K = × ⋅ − 1 0 10 − 5 0 10 3 . 2 . Rfat = × m m 2 K W ⋅ 0.20 W m K = × ⋅ − 0 50 10 − 2 5 10 2 . 2 . and Rtissue = × m m 2 K W ⋅ 0.50 W m K = × ⋅ − 3 0 10 − 6 0 10 2 . 2 . so the total R value of the three layers taken together is = 3 ( + + ) × ⋅ = × R Ri i total m2 K W = Σ = − 1 m 2 ⋅K 2 ⋅ 5.0 2.5 6.0 10 2 14 10−2 = 0 14 W m K W . continued on next page
  • 22. 546 Chapter 11 (b) The rate of energy transfer by conduction through these three layers with a surface area of A = 2.0 m2 and temperature difference of ΔT = (37 − 0)°C = 37°C = 37 K is P = ( ) = ( )( ) 2 0 37 0 14 m K m KW = × A T R ⋅ Δ total 2 2 5 3 . . . 102 W 11.41 P = ⎛⎝ ⎜ ⎞⎠ ⎟ kA Δ T L , with k = ⋅ ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ 0 200 10 4 186 . cal . cm °C s cm 1 m J 1 c 2 al J s m °C ⎛⎝ ⎞⎠ = ⋅ ⋅ 83 7 . Thus, the energy transfer rate is P = J ⋅ ⋅ ⎛⎝ ⎞⎠ [( )( )] ° − 83 7 8 00 50 0 200 2 . . . s m °C m m C 0 0 1 50 10 4 02 10 402 2 8 . . . °C m J s MW × ⎛⎝ ⎞⎠ = × = − 11.42 The total surface area of the house is A = A + A + A + A side walls end walls gables roof where Aside walls = 2[(5.00 m) × (10.0 m)] = 100 m2 Aend walls = 2[(5.00 m) × (8.00 m)] = 80.0 m2 A = 2[1 ( base ) × ( altitude )] = 2 (8 00 m) × gables 2 1 2 [ . (4.00 m) tan 37.0°] = 24.1 m2 Aroof = 2 ( 10.0 m ) × ( 4.00 m cos37.0 ° ) = 100 m 2 ⎡⎣ ⎤⎦ Thus, A = 100 m2 + 80.0 m2 + 24.1 m2 + 100 m2 = 304 m2 With an average thickness of 0.210 m, average thermal conductivity of 4.8 × 10−4 kW m⋅°C, and a 25.0°C difference between inside and outside temperatures, the energy transfer from the house to the outside air each day is = ( ) = t ⎡ ( ) E t kA T L ⎣ ⎢ ⎤ ⎦ ⎥( ) = ( × − ⋅ ) P Δ Δ Δ 4.8 10 4 kW m °C 304 25 0 . ( 86 400 ) m °C 0.210 m s ⎡ ( 2 )( ) ⎣ ⎢⎢ ⎤ ⎦ ⎥⎥ or E = 1.5 × 106 kJ = 1.5 × 109 J The volume of gas that must be burned to replace this energy is V = E = × heat of combustion ( J 1 5 10 kcal m3 9 300 . 9 )( ) = 4 186 39 J kcal m3 11.43 R R R R R i = Σ = + + outside air film shingles sheathing + R + R + R cellulose dry wall inside air film R = [ + + + ( ) + + ] ⋅ 0.17 0.87 1.32 3 3.70 0.45 0.17 ft2 °F Btu h 2 = ⋅ ft °F Btu h 14
  • 23. Energy in Thermal Processes 547 11.44 The rate of energy transfer through a compound slab is P = ( ) = A T Δ , where Σ R R L k i i (a) For the thermopane, R = R + R + R = R + R pane trapped air pane pane trapped 2 air. Thus, R = × + × − − ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ 2 0.50 10 2 m 1.0 10 2 0.84 W m °C m 0.0234 W m °C 2 m °C W ⋅ = ⋅ 0.44 and P = ( )( ) ⋅ = 1 0 23 0 44 52 . . m °C m °CW W 2 2 (b) For the 1.0 cm thick pane of glass: R = × = × ⋅ − 1 0 10 − ⋅ 1 2 10 2 . 2 . m 0.84 W m °C 2 m °C W so ( 1 0 )( 23 ) P = = × = − × ⋅ 1 . m °C 1 . 9 103 1 .2 10 m °C W W 2 2 2 .9 kW , 37 times greater 11.45 When the temperature of the junction stabilizes, the energy transfer rate must be the same for each of the rods, or P P Cu Al = . The cross-sectional areas of the rods are equal, and if the temperature of the junction is 50°C, the temperature difference is ΔT = 50°C for each rod. Thus, Δ Δ k A = Al = P P Cu Cu Cu Al Al ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ T L k A T L , which gives L k k Al L Al Cu Cu W m °C 97 W m °C = ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = ⋅ ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ 238 3 ⎟ ( ) = 15 cm 9.0 cm 11.46 The energy transfer rate is P= = = (Δ )( × ) Q t 5.0 3.33 105 ( )( ) = ice f kg J kg m L Δ Δ t 8.0 h 3 600 58 s 1 h W Thus, P = kA(ΔT L) gives the thermal conductivity as k = ⋅ L ( ) = A T ( )( × ) ( ) − − P Δ W . 2 m m2 °C 58 2 0 10 0 80 25 W m °C ( )= × − ⋅ . 5 0 7 2 10 2 . . °C
  • 24. 548 Chapter 11 11.47 The absolute temperature of the sphere is T = 473 K and that of the surroundings is T0 = 295 K. For a perfect black-body radiator, the emissivity is e = 1. The net power radiated by the sphere is Pnet W m K 2 4 = ( − ) = × ⋅ ⎛⎝ ⎜ ⎞⎠ ⎟ − σ π Ae T 4 T 4 0 5.67 10 8 4 0.060 473 2 2 4 4 m K 95 K ( ) ⎡⎣ ⎤⎦ ( ) − ( ) ⎡⎣ ⎤⎦ or Pnet = 1.1×102 W= 0.11 kW 11.48 Since 97.0% of the incident energy is refl ected, the rate of energy absorption from the sunlight is Pabsorbed= 3.00%× (I ⋅ A) = 0.0300(I ⋅ A), where I is the intensity of the solar radiation. Pabsorbed = 0 0300(1 40 × 103 W m2 )(1 00 × 103 m)2 . . . = 4.20 × 107 W Assuming the sail radiates equally from both sides (so A = 2(1 00 ) = 2 00 × 10 . km 2 . 6 m2), the rate at which it will radiate energy to a 0 K environment when it has absolute temperature T is Prad 2 4 W m K = ( − ) = × ⋅ ⎛⎝ ⎞⎠ W K 4 ( )( )⋅ = × ⎛⎝ σ Ae T 4 0 5.669 6 10−8 2.00 × 106 m 2 0 03 4 3 40 10 3 4 ⎞⎠ . T . − ⋅T At the equilibrium temperature, where P P rad absorbed = , we then have − W ⋅ = × 3 40 10 4 20 10 3 4 7 . . × ⎛⎝ ⎞⎠ K W 4 T or T = × × ⎡ ⎣ ⎢ ⎤ = − ⎦ ⎥ 4 20 10 3 40 10 333 7 3 1 4 . . W W K K 4 11.49 The absolute temperatures of the two stars are T T X Y = 6 000 K and = 12 000 K. Thus, the ratio of their radiated powers is P P Y X σ Y = ( ) = σ X Y X AeT AeT T T = = ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ 4 4 4 4 2 16 11.50 The net power radiated is Pnet=σ Ae(T 4 − T ) 4 , so the temperature of the radiator is 0 T T Ae = ⎡ + ⎣ ⎢ ⎤ ⎦ ⎥ 4 0 1 P 4 net σ If the temperature of the surroundings is T0 = 22°C = 295 K, T = ( ) + 25 W 295 ( 5 67 × 10 − ⋅ ) 2 5 × 10 − 4 8 5 K . W m2 K4 . m2 K °C ( )( ) ⎡ ⎣ ⎢⎢ ⎤ ⎦ ⎥⎥ = × = × 0 90 2 1 10 1 8 10 1 4 3 3 . . . 11.51 At a pressure of 1 atm, water boils at 100°C. Thus, the temperature on the interior of the copper kettle is 100°C and the energy transfer rate through it is P = ⎛⎝ ⎜ ⎞⎠ ⎟ = W m °C ⋅ ⎛⎝ ⎜ ⎞⎠ ⎟ ( ) ⎡⎣ ⎤⎦ kA Δ T L 397 0 10 2 π . m 102 100 2 0 10 1 2 10 12 3 4 °C °C m W k − × ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = × = . − . W
  • 25. Energy in Thermal Processes 549 11.52 The mass of the water in the heater is ρ ⎞ 10 50 0 m V = =⎛⎝ 3 kg 3 786 m ⎞⎠ ( )⎛ ⎝ ⎜ gal L . 3 1 gal . ⎠ ⎟ ⎛ ⎝ ⎜ ⎞ = 1 10 189 3 ⎠ ⎟ m L kg 3 The energy required to raise the temperature of the water from 20.0°C to 60.0°C is Q = mc(ΔT ) = (189 kg)(4 186 J kg)(60.0°C− 20.0°C) = 3.17 ×107 J The time required for the water heater to transfer this energy is t Q = = × ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = P 3 17 10 1 1 83 . 7 . J 4 800 J s h 3 600 s h 11.53 The energy conservation equation is m c m L m m c m c Pb Pb ice f ice w w cup C (98°C − 12°C) = + ( + ) + u °C °C ⎡⎣ ⎤⎦ (12 − 0 ) This gives mPb J kg °C 128 86°C 0 040 kg 3 33 10 ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ( ) = ( . ) . × 5 0 24 J kg kg ( ) + . ( ) ⋅ ( ) + ( ) ⋅ ( ) ⎡⎣ ⎤⎦4 186 J kg °C 0.100 kg 357 J kg °C (12°C) or mPb = 2.3 kg . 11.54 The energy needed is Q = mc( T ) = ( V )c( T ) = ⎛⎝ ⎡ ( ) ⎞⎠ ⎣ ⎢ Δ ρ Δ 103 1 00 kg m . 3 ⎤ m 3 ⎦ ⎥ (4 186 J kg)(40.0°C) = 1.67 × 108 J The power input is P = (550 W m2 )(6.00 m2 ) = 3.30 ×103 J s, so the time required is t Q = = × × ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = P 1 67 10 3 30 10 1 1 8 3 . . J J s h 3 600 s 4 1 . h 11.55 The conservation of energy equation is m c m c T m c T w w ( + )( − ) = ( − ) cup glass Cu Cu 27°C 90°C This gives T Cu Cu cup glass 90°C 27°C m c m c m c m c w w w w = ( ) + ( + )( ) + m c m c cup glass Cu Cu + or T = (0.200)(387)(90°C) + (0.400)(4 186) + (0.300) 837 27 ( ) ⎡⎣ 29 ( )( ) = °C 0 400 4 186 0 300 837 0 ⎤⎦ ( ) ( )( ) + ( )( ) + °C . . .200 387
  • 26. 550 Chapter 11 11.56 (a) The energy delivered to the heating element (a resistor) is transferred to the liquid nitrogen, causing part of it to vaporize in a liquid-to-gas phase transition. The total energy delivered to the element equals the product of the power and the time interval of 4.0 h. (b) The mass of nitrogen vaporized in a 4.0 h period is m Q L ⋅( ) = ( )( )( ) P Δ t 25 4 0 3 = = L f f J s . h s h . × 2 01 600 10 = . kg 1 8 5 J kg 11.57 Assuming the aluminum-water-calorimeter system is thermally isolated from the environment, Q Q cold hot = − , or m c T T mc T T m c T Al Al f i Al w w f i w cal cal f ( − ) = − ( − )− − , , Ti,cal ( ) Since Tf = 66 3 . °C and T T i, i,w . cal = = 70 0°C, this gives c m c m c T T , w w iw f m T T f i Al cal cal Al Al = ( + )( − ) ( − ) , or cAl 0.400 kg 4 186 + (0.040 ) 630 J kg °C kg J = ⎛ ( ) ⋅ ⎝ ⎜ ⎞ ⎠ ⎟ kg °C °C kg ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ⎡ ⎣ ⎢ ⎤ ⎦ ⎥ ( − ) ( ) 70 0 66 3 ( − ) = × 0 200 66 . . . . . . 3 270 8 00 102 J kg °C °C ⋅ The variation between this result and the value from Table 11.1 is ⎛ variation × = − % = % ⎝ ⎜ ⎞ ⎠ ⎟ accepted value 100 800 900 900 100 11 1 J kg °C J kg °C ⋅ ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ × % = . % which is within the 15% tolerance. 11.58 (a) With a body temperature of T = 37°C + 273 = 310 K and surroundings at temperature T0 = 24°C + 273 = 297 K, the rate of energy transfer by radiation is Prad W m K 2 4 = ( − ) = × ⋅ ⎛⎝ ⎞⎠ − σ Ae T 4 T 4 0 8 5 669 6 10 2 0 . . m K K W 2 ( )( ) ( ) − ( ) ⎡⎣ ⎤⎦ 0 97 310 297 = 1 6 × 10 . 4 4 . 2 (b) The rate of energy transfer by evaporation of sweat is Psweat W ( )( )= × Q ) × t 0.40 2.43 10 kg J kJ v, sweat kg 3 kJ = = = ( mL Δ Δt 3 600 s 10 2 7 10 3 . 2 (c) The rate of energy transfer by evaporation from the lungs is Plungs kJ h h 3 600 s J 1 kJ =⎛⎝ ⎞⎠ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ⎛ ⎝ 38 1 103 ⎜ ⎞ ⎠ ⎟ = 11W (d) The excess thermal energy that must be dissipated is P P excess metabolic kJ h = = × ⎛⎝ ⎞⎠ 0.80 0.80 2.50 103 1 10 5 6 10 3 h 2 3 600 s J 1 kJ W ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = . × so the rate energy must be transferred by conduction and convection is P P P P P cc = − ( + + ) = . − . − excess rad sweat lungs (5 6 1 6 2.7 − .11) × 102 W = 1.2 × 102 W
  • 27. Energy in Thermal Processes 551 11.59 The rate at which energy must be added to the water is P= = ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ = ⎛⎝ ⎜ ⎞⎠ ⎟ Δ Δ Δ Δ Q t m t Lv 0 500 1 . kg min min 60 s J kg ⎛⎝ ⎜ ⎞⎠ ⎟ ⎡ ⎣ ⎢ ⎤ ⎦ ⎥ 2.26 × 106 = 1.88 ×104 W ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ From P = kA(T −100°C) L, the temperature of the bottom surface is T °C ( ) P . W . m = + ⋅ = + L k A ( × ) × − 100 100 1 88 104 0 500 10 2 °C °C 109 2 . ⎡⎣ ( 238 W m ⋅ °C ) ( m ) ⎤⎦ = π 0 120 11.60 The energy added to the air in one hour is Q t = ( ) = ( ) ⎡⎣ P ( ) = × total 10 200 W 3 600 s 7.2 0 106 J ⎤⎦ and the mass of air in the room is m = ρV = (1.3 kg m3 )[(6.0 m)(15.0 m)(3.0 m)] = 3.5 × 102 kg The change in temperature is ΔT = = × Q mc 7 2 10 ( = 3 5 × 10 )( 837 ⋅ ) 25 6 2 . . J kg J kg °C °C giving T = T + T = + = 0 Δ 20°C 25°C 45°C . 11.61 In the steady state, P P Au Ag = , or k A 80 . 0 °C − T 30 . 0 °C ⎛⎝ L = T k A ⎛⎝ − ⎞⎠ L Au Ag ⎞⎠ This gives T 80.0°C 30.0°C 314 80.0°C) + ( ) = Au Ag ( k k k k = ( ) + ( ) + Au Ag + = 427 30 0 314 427 51 2 . . °C °C 11.62 (a) The rate work is done against friction is P = f ⋅ v = (50 N)(40 m s) = 2.0 ×103 J s = 2.0 kW (b) In a time interval of 10 s, the energy added to the 10-kg of iron is Q = P ⋅t = (2.0 ×103 J s)(10 s) = 2.0 ×104 J and the change in temperature is ΔT = = × Q mc 2 0 10 ( )( ) = 448 ⋅ 4 5 . 4 . J 10 kg J kg °C °C
  • 28. 552 Chapter 11 11.63 (a) The energy required to raise the temperature of the brakes to the melting point at 660°C is Q = mc(ΔT ) = (6.0 kg)(900 J kg ⋅°C)(660°C − 20°C) = 3.46 × 106 J The internal energy added to the brakes on each stop is 1 2 2 2 Q KE mi 1 1 2 = Δ = = (1 500 )(25 ) = 4 69 ×1 car v kg m s . 05 J The number of stops before reaching the melting point is N = = × Q Q × = 1 6 5 3 46 10 4 69 10 7 . . J J stops (b) This calculation assumes no energy loss to the surroundings and that all internal energy generated stays with the brakes. Neither of these will be true in a realistic case. 11.64 When liquids 1 and 2 are mixed, the conservation of energy equation is 7 3 =⎛⎝ ⎞⎠ mc mc 1 2 (17°C−10°C) = (20°C−17°C), or c c 2 1 When liquids 2 and 3 are mixed, energy conservation yields 28 3 = =⎛⎝ ⎞⎠ mc mc 3 2 (30°C− 28°C) = (28°C− 20°C), or c c c 3 2 1 4 Then, mixing liquids 1 and 3 will give mc T mc T 1 3 ( −10°C) = (30°C− ) or T = ( ) + ( ) 10 30 10 28 3 30 °C °C °C °C c c + c c = + ( )( ) + 1 3 1 3 1 ( ) = 28 °C 28 3 11.65 (a) The internal energy ΔQ added to the volume ΔV of liquid that fl ows through the calorimeter in time Δt is ΔQ = (Δm)c (ΔT ) = ρ(ΔV)c (ΔT ). Thus, the rate of adding energy is Δ Δ Δ Δ Δ Q t c T V t = ( )⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ρ where ΔV Δt is the fl ow rate through the calorimeter. (b) From the result of part (a), the specifi c heat is c Δ Δ Q t T V t J s = = ρ ( Δ )( Δ Δ ) ( )( ) 40 . g cm3 . °C .5 0 72 5 8 3 . = .7 ×103 J kg ⋅°C 2 7 10 2 3 cm s J g °C g 1 kg ( 3 ) = ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟
  • 29. Energy in Thermal Processes 553 = + = 2(π 2 )+ (2π ), or 11.66 (a) The surface area of the stove is A A A r rh stove ends cylindrical side Astove = 2 (0 200 m) + 2 (0 200 m)(0 500 m) = 0 2 π . π . . .880 m2 The temperature of the stove is Ts= − = = 59 (400°F 32.0°F) 204°C 477 K while that of the air in the room is Tr= 5 − = = 9 (70.0°F 32.0°F) 21.1°C 294 K. If the emissivity of the stove is e = 0.920, the net power radiated to the room is P = σA eT ( 4 − T 4 ) stove s r = ( × − ⋅ ) ⎡⎣ 5 . 67 10 8 W m2 K4 ( 0 . 880 m 2 )( ) ( K ) − ( K ) ⎤⎦ 0 920 477 294 4 4 . or P = 2.03 × 103 W (b) The total surface area of the walls and ceiling of the room is A = 4A + A = 4[(8 00 )(25 0 )] + 25 wall ceiling . ft . ft .0 1 43 10 ( ft)2 = . × 3 ft2 If the temperature of the room is constant, the power lost by conduction through the walls and ceiling must equal the power radiated by the stove. Thus, from thermal conduction equation, P = A(T − T ) R h c i Σ , the net R value needed in the walls and ceiling is ΣR ( − ) = A T T i = h c ( × )( − ) P 1.43 103 ft2 70.0°F 32.0°F 2.03 10 J s J Btu ⎝ ⎜⎞ h ⎛⎝ ⎜ ⎞⎠ ⎟⎛ × 3 3 600 s ⎠ 1 054 1 1 ⎟ or ΣRi= 7.84 ft2 ⋅ °F ⋅ h Btu 11.67 A volume of 1.0 L of water has a mass of m = ρV = (103 kg m3 )(1.0 × 10−3 m3 ) = 1.0 kg. The energy required to raise the temperature of the water to 100°C and then completely evaporate it is Q = mc(ΔT )+ mLv, or Q = (1.0 kg)(4 186 J kg⋅°C)(100°C− 20°C) + (1.0 kg)(2.26 ×106 J kg) = 2.59 ×106 J The power input to the water from the solar cooker is P = ( ) = ( )( ) ( ) efficiency IA 0 50 600 0 50 4 2 . . W m m 2 ⎡π ⎣ ⎢⎢ ⎤ ⎦ ⎥⎥ = 59 W so the time required to evaporate the water is t = Q = 2 . 59 × 10 6 J = ( 4 . 4 × 10 4 s )⎛ P 59 J s ⎝ 1 h ⎜ 3 600 s ⎞ ⎠ ⎟ = 12 h
  • 30. 554 Chapter 11 11.68 (a) From the thermal conductivity equation, P = − ( ) ⎡⎣ ⎤⎦ kA T T L h c , the total energy lost by conduction through the insulation during the 24-h period will be Q kA L = P ( )+P ( ) = ( − )+ 1 2 12 0 12 0 37 0 23 0 . . . . h h °C °C 37 0 16 0 12 0 . . . °C °C h − ( ) ⎡⎣ ⎤⎦ ( ) or Q = ( 0 012 0 ⋅ )( 0 490 ) + 0 095 0 ⎛⎝ [ 14 0 21 ]( )J . . . . . J s m°C m m °C 2 0 120 3 600 s °C h 9 36 104 1 h ⎞⎠ . = . × The mass of molten wax which will give off this much energy as it solidifi es (all at 37°C) is m = = × Q Lf = 9 36 10 × 0 457 kg 3 . 4 . J 205 10 J kg (b) If the test samples and the inner surface of the insulation is preheated to 37.0°C during the assembly of the box, nothing undergoes a temperature change during the test period. Thus, the masses of the samples and insulation do not enter into the calculation. Only the duration of the test, inside and outside temperatures, along with the surface area, thickness, and thermal conductivity of the insulation need to be known. 11.69 The energy m kilograms of steam give up as it (i) cools to the boiling point of 100°C, (ii) condenses into a liquid, and (iii) cools on down to the fi nal temperature of 50.0°C is m = ( )+ + ( ) = Q mc T mL mc T m steam liquid water 2.0 Δ Δ 1 v 2 ( 1 × 10 3 J kg ⋅ °C ) ( 130 °C − 100 °C )+ 2.26 × 106 J ⎡⎣ kg +(4 186 J kg ⋅°C) 100°C− 50 0 2 53 106 . . °C J kg ( )⎤⎦ = m( × ) The energy needed to raise the temperature of the 200-g of original water and the 100-g glass container from 20.0°C to 50.0°C is Q mc mc T needed w w g g kg J kg °C = + ( ) = ( ) ⋅ Δ 0 200 4 186 . ( ) + ( ) ⋅ ( ) ⎡⎣ ⎤⎦ ( ) = 0 100 837 30 0 2 76 . . . kg J kg °C °C × 104 J Equating the energy available from the steam to the energy required gives m(2.53 × 106 J kg) = 2.76 × 104 J or m = × = = 2 76 10 2 53 10 × 0 010 9 10 9 4 6 . . . . J J kg kg g
  • 31. Energy in Thermal Processes 555 11.70 We approximate the latent heat of vaporization of water on the skin (at 37°C) by asking how much energy would be needed to raise the temperature of 1.0 kg of water to the boiling point and evaporate it. The answer is ≈ (Δ )+ °C = ( J kg ⋅°C)( °C− 37°C)+ 2.26 ×106 J kg 37°C 100 4 186 100 L c T L v water v or 37°C ≈ 2.5 ×106 J kg Lv Assuming that you are approximately 2.0 m tall and 0.30 m wide, you will cover an area of A = (2.0 m)(0.30 m) = 0.60 m2 of the beach, and the energy you receive from the sunlight in one hour is Q = IA(Δt ) = (1 000 W m2 )(0.60 m2 )(3 600 s) = 2.2 × 106 J The quantity of water this much energy could evaporate from your body is m = ≈ × Q L 2 2 10 2 5 10 0 9 °C × = 37 v 6 6 J J kg kg . . . The volume of this quantity of water is V 0 9. kg 10 kg m = m = ≈ − 3 3 = ρ 10 m 1 L 3 3 Thus, you will need to drink almost a liter of water each hour to stay hydrated. Note, of course, that any perspiration that drips off your body does not contribute to the cooling process, so drink up! 11.71 During the fi rst 50 minutes, the energy input is used converting m kilograms of ice at 0°C into = = (3.33 × 105 J kg), so the constant liquid water at 0°C. The energy required is Q mL m 1 f power input must be Q ( × ) t P = ( ) = m 1 1 3 33 105 . J kg Δ 50 min During the last 10 minutes, the same constant power input raises the temperature of water having a total mass of (m + 10 kg) by 2.0°C. The power input needed to do this is Q ( + ) t ( ⋅ )(2.0 ) kg kg J kg °C °C 10 10 4 186 m 2 P = ( ) = ( m + ) c ( T ) ( ) = t 2 2 Δ Δ Δ 10 min Since the power input is the same in the two periods, we have 10 4 186 ( . × 5 ) = m 3 33 10 m 50 J kg ( + )( ⋅ min kg J kg °C)(2.0°C) 10 min which simplifi es to (8.0)m = m + 10 kg, or m= = 10 1 4 kg 7.0 . kg
  • 32. 556 Chapter 11 11.72 (a) First, energy must be removed from the liquid water to cool it to 0°C. Next, energy must be removed from the water at 0°C to freeze it, which corresponds to a liquid-to-solid phase transition. Finally, once all the water has frozen, additional energy must be removed from the ice to cool it from 0°C to –8.00°C. (b) The total energy that must be removed is Q = Q + Q + Q cool water to 0°C freeze at 0°C cool ice to 8.00°C ice °C °C − = m c − T + m L + m c T − w w i w f w f 0 0 or ⎛ Q = ( × ) ⋅ 75.0 10−3 kg 4 186 −20.0 + 3.33 ⎝ ⎜ ⎞ ⎠ ⎟ J kg °C °C × + ⋅ ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ − ⎡ ⎣ ⎢ ⎤ ⎦ ⎥ = 10 2 090 8 00 3 2 5 J kg J kg °C . °C . 5 × 104 J = 32.5 kJ 11.73 (a) In steady state, the energy transfer rate is the same for each of the rods, or P P Al Fe = . Thus, k A 100 °C − T 0 °C ⎛⎝ L = T k A ⎛⎝ − ⎞⎠ L Al Fe ⎞⎠ giving T k k k = + ⎛ ⎝ ⎜ ⎞ ⎠ ⎟ ( ) = + ⎛⎝ ⎞⎠ Al Al Fe 100°C 238 238 79 5 10 . ( 0°C) = 75.0°C (b) If L = 15 cm and A = 5.0 cm2, the energy conducted in 30 min is P ( × − ) − Al Q = ⋅ t = ⋅ ⎛⎝ ⎜ ⎞⎠ ⎟ 4 100 7 . 2 W m °C m °C 238 5 0 10 5 0 0 15 1 800 3 6 104 . . . °C m s J ⎛⎝ ⎜ ⎞⎠ ⎟ ⎡ ⎣ ⎢ ⎤ ⎦ ⎥ ( ) = × = 36 kJ