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Chapter
7 -- Conservation of Energy |
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Updated
--- 28 October 2006 |
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Hint |
Answer |
Update Date |
7.1 |
Consider
the lunar module as the system for both Parts (a) and (b). Both approaches to
the solution should give the same answer. Be very careful with signs.
The first answer may seem strange since it says that the answer does not
depend upon the direction of motion as long as the vertical speed of the
lunar module is 3 m/s. To clarify this, think about the change in elevation it would take for the module to reach the ground. When the module is traveling up at 3 m/s, it will keep going up until it slows to zero velocity and then returns to its initial elevation (and coincidentally the same 3 m/s velocity) but this time it will be moving in the opposite direction. This is exactly the same case as occurs when you start with a 3 m/s velocity moving towards the moon. Thus it will take more time for the lunar module to land if it initially travelling up; however, the distance it can safely "fall" is the same. This also explains why it can safely fall a greater distance if their is no initial velocity. |
If V1 = 3 m/s ↑ or ↓, then If V1 = 0 m/s then |
19Oct05 |
7.2 |
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7.3 |
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7.4 |
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7.5 |
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7.6 |
(a)
Apply the definition of mechanical work. (b) Apply the energy balance to a system that includes the collar and the spring. Based on an examination of this system assume no heat transfer and negligible changes in internal energy. (If you somehow forgot to include the spring V2 = 4.2 m/s). Remember that spring energy is related to the spring extension from the unextended length, i.e. in State 1 the spring already has energy stored in it since it is extended 0.5 m. Why is it easier to put the spring inside the system? |
(a)
W1-2,in = 64.95 N-m (b) V2 = 4.927 m/s |
19Oct05 |
7.7 |
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7.8 |
Reference
in Problem is incorrect. It should be to Problem 7.7 The answer to this
problem depends on how you interpret "the last 5 feet of the ramp."
The answer reported here assumes that the package travels a total of ten feet
before it stops and that the last five of these ten feet has the friction
strip. |
mk
= 1.17 |
19Oct05 |
7.9 |
(a)
What would be wrong with including the piston inside the system? (b) Apply the defining equation for PdV work into the system. Work each process individually and see how P and V are related so that you can perform the integration. (See section on PdV work in text.) (c) Sketch the three processes on a P-V graph to scale. The areas under each curve represents the absolute value of the work for the process. The enclosed area represents the net work into the system for the process. (d) The net work in is just the sum of the work for each process. (For kicks, write the closed system, finite-time form of the energy balance for the three stage process. Because this is a cycle the final and intial states are identical and Efinal = Einitial. What does this say about the net heat transfer into the system for this process.? |
(a) System should be the gas. (b) W1-2,in = 128.8 kJ; (d) Wnet,in -191.2 kJ |
19Oct05 |
7.10 |
Application
of finite-time form of conservation of energy plus the definitions of kinetic
energy and gravitational potential energy. Careful with units. |
DEk = 186.5
ft-lbf |
01Nov05 |
7.11 |
(b)
Application of rate form of conservation of energy to a closed system and
understanding of dE/dt. |
(b) dE/dt = 2.0 kW at 1.2 h and 0 kW at 2.4 h. |
19Oct05 |
7.12 |
System
boundary should surround the gas and "cut" the paddle wheel shaft.
Use definition of PdV work and finite time form of conservation of energy. |
2790
J |
19Oct05 |
7.13 |
(a)
Treat the gas as your system. Now use PdV work relation to find the work
during the change in state. BUT how do you find P. Look at the piston
as a system for Cons. of Linear Momentum and assume that acceleration of the
system is negligible. How is pressure inside the gas acting on the left side
of the piston related to the Patm and the force of the
spring acting against the exterior of the piston? Now if you think about the
mechanical work done by the piston against Patm and Fspring
you can find where the energy goes -- into the spring or into the atmosphere. (b) Definition of shaft work in terms of torque and angle of rotation (c) Too answer (c) you must apply the cons. of energy equation to a system. What's inside this system? If you include part of the stirring device inside your system, you must assume what about its mass or internal energy change to get ΔU for the gass. |
(a)
Win = -115.6 J for the gas (b) Wshaft, in = 427.3 J (c) ΔU = 311.7 J for gas |
19Oct05 |
7.14 |
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7.15 |
Application
of rate form of conservation of mass and conservation of energy to the compressor.
Note that many of the assumptions given in the problem are best applied
after you apply conservation of mass and collect the mass flow rate terms. |
(b)
4.2 |
19Oct05 |
7.16 |
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7.17 |
A
pretty standard COE problem. Note, to solve for Part c) you will need a
system boundary that cuts through the shaft. Use the internet to find any
unit conversions you may need. |
a)
194000 Btu/h b)
258 amps c)
111.8 ft.lb |
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7.18 |
(a)
Apply conservation of mass to the entire system of heat exchanger and
turbine. |
(a)
800 kg/s |
19Oct05 |
7.19 |
(a)
Strategy is to apply the rate form of the conservation of energy and mass equations.
Use the open system around the gas turbine to find the shaft power out of the
system. Use the closed system around the generator to find the electrical
power out. (You could also find the electrical power out by using a combined
open system that includes both systems.) (b) Use the definition of shaft power to relate the torque to the rotational speed. Most common source of error is the unit conversion from "rpm" , revolutions per minute, to "rad/s", radians per second. |
(a)
Shaft power out = 800 Btu/s |
19Oct05 |
7.20 |
(a)
Application of rate-form of conservation of energy and mass to the correct system.
Carefully consider your options. Where are the boundaries on which I know
something? How can I relate the given information to the change in specific
enthalpy across the air compressor for the air? |
(a)
703.5 kg/min |
24Oct06 |
7.21 |
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7.22 |
First---
Error in Problem Statement. It should say repeat 7.21 (not 8.21) |
(a)
0.1169 gram |
19Oct05 |
7.23 |
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7.24 |
Two
possible systems: volume occupied by water in the tank OR volume occupied by
water and heating element in the tank. One of these systems has electric
power transfers and no heat transfer and the other has only
heat transfer with no electric power. If you pick the one with no electric
power transfer, then you need a second system to actually find the electric
power input. To find the resistance just remember Ohms Law V=IR and
the definition of electric power IV where V is now voltage
difference. |
(a)
0.4157 lbm/s |
19Oct05 |
7.25 |
Apply
problem information and definitions to answer questions where possible. If you need to relate input and output energy transfers then you must apply the general energy equation to the appropriate system. (g) Here you must look as the contents of the tank. Determine the increase of internal energy for this system during the time interval. Now using the constitutive relation relating u and T, relate ΔT to Δu. |
(a)
120 rpm and 100 rpm |
19Oct05 |
7.26 |
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7.27 |
What
should your system be if you want to know the heat transfer rate from the
pump by itself? What's the appropriate substance model for liquid water and
how can you use it to relate changes in enthalpy to changes in temperature
and pressure. |
(a)
2.80 kW out of the system |
19Oct05 |
7.28 |
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7.29 |
Apply
conservation of energy (finite-time form) to the gas in the system and assume
the CO2 acts like an ideal gas with room-temperature specific
heats. Also use definition of PdV work. |
W1-2,in = -112.5 kJ |
19Oct05 |
7.30 |
All
sorts of good stuff in this problem! You will need COM, ideal gas model, COE,
constitutive relations, and definition of mass flow rate. Note that the air
and the oil do not mix. |
a)
93.8F b)
5.85 ft2 c)
0.00267 ft2 |
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7.31 |
Consider
the air as a closed system. Is this a finite-time or rate problem? Is the air
a steady-state system? What types of work transfers of energy are possible
for the air? What can you say about the process that the air undergoes as its
volume is decreased? What substance model can you use to relate changes in
internal energy to changes in other properties, e.g. temperature and
pressure? |
Win = 16.64 kJ |
24Oct05 |
7.32 |
Apply
conservation of mass and energy to the pump assuming that the incompressible
model describes the behavior of the liquid. Notice how even a small
increase in temperature results in a tremendous increase in shaft power into
the pump. |
(a)
D2/D1 = 0.577 |
19Oct05 |
7.33 |
Is
this a steady-state or a finite-time problem? Is this an open or a
closed system? What energy transfers are important for a nozzle? A nozzle is
a device designed to increase the kinetic energy of a flowing fluid without
any energy transfers across the non-flow boundaries of the device. Be VERY
careful with units. |
V2 = 333 m/s |
24Oct05 |
7.34 |
Same
as Problem 7.33, but a different substance model. Be VERY careful with units. |
(a)
V2 = 20.0 m/s |
19Oct05 |
7.35 |
(b)
Application of Ohm's law and definition of electric power |
(b)
0.0144 watts; 1.2 mA |
19Oct05 |
7.36 |
(a)
Consider definition of average power for an ac system. |
(a)
1.046 amps |
19Oct05 |
7.37 |
Same
approach as for 7.38 only this time you do not know the change in internal
energy, work and heat transfer for each process. So you will have to these
before you can find the cycle information. You have four processes you must
consider. Treat helium as an ideal gas. |
None available I think its a refrigerator, what do you think? |
19Oct05 |
7.38 |
(a)
Apply finite-time form of the conservation of energy to the gas and evaluate the
energy transfers and changes for each process. It is suggested that you
consider each process sequentially, i.e. 1-2, 2-3, 3-4, and 4-1. A correct
solution should complete the table so that Qnet,in = Wnet,out
and ∆Ucycle = 0. |
(a)
??? |
19Oct05 |
7.39 |
(a)
Apply finite-time form of the conservation of energy to the gas and evaluate
the energy transfers and changes for each process. It is suggested that you
consider each process sequentially, i.e. 1-2, 2-3, 3-4, and 4-1. A correct
solution should complete the table so that Qnet,in = Wnet,out
and ∆Ucycle = 0. |
Process
2-3 For the complete cycle, |
19Oct05 |
7.40 |
(a)
Show your work. -- Definition of COP for a Heat Pump |
(a)
3.02 |
19Oct05 |
7.41 |
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7.42 |
Apply
Work-Energy Principle for a particle to the bucket. Pay careful attention to
the work term and the fact that it is the integral of a dot product between
the net surface force on the bucket and displacement of the bucket, F�ds.
How are the vectors F and ds oriented with respect to
each other? |
4.05
m/s |
19Oct05 |
7.43 |
The
only (?) system for this problem is the package. It is also suggested that
you consider the overall process 1 → 3 as the sum of subprocess
1→2 and subprocess 2→3. State 1 is the initial state of the
package; State 2 is the state of the package as it reaches point B at
the bottom of the ramp; and State 3 is the state of the package at
Point C. For each subprocess, draw a free-body diagram showing all surface
forces, then apply the work-energy principle (mechanical energy balance)
to each subprocess. Be careful about the sign of the work term for 2→3. |
d
= 20.271 ft |
19Oct05 |
7.44 |
(a)
& (b) Apply the energy balance to a system consisting of the mass
attached to the bungee cord and the bungee cord. Also be careful about
calculating the deflection of the spring, i.e. the extension/compression of
the spring from its unloaded length. Make the standard assumptions to recover
the mechanical energy balance, i.e. no heat transfer and no changes in
internal energy. (c) Use Conservation of Linear Momentum OR if you know how velocity changes with position you might be able to differentiate that expression with respect to time. |
(a)
533 lbf/ft |
19Oct05 |
7.45 |
Since
the two springs initially support the large block, they have an initial
deflection. Note that that you must treat this as a two step process. First
an impact problem and then frictionless motion. Be careful to identify your
systems from each step of the process. (Do you have to use the same system
for each process? NO!) |
0.271
ft |
19Oct05 |
7.46 |
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7.47 |
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7.48 |
At
first look you might assume that this is only a MEB problem with a system
including both blocks and the spring; however, it has the telltale impact
(friction inside the system) that makes the MEB invalid. (Mechanical energy
is not conserved in this process; however, the all inclusive energy is
conserved.) Thus, this requires analysis as a two-step process: |
(a)
1.00 m ; (b) 0.817 m |
19Oct05 |
7.49 |
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7.50 |
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7.51 |
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7.52 |
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(a)
900 K; (b) Win = 1050 kJ |
28Oct05 |
7.57 |
Never,
ever, ever use COE during an impact! You can use COE before an impact, you
can use COE after an impact, but never use COE during an impact! That is what
the finite-form of COLM is for. |
a)
19.7 m/s b)
5.7 m |
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7.60 |
The
change in height between the inlet of the pump and the inlet of the hot water
tank is not negligible. You will have to account for this change in
specific potential energy in your equations. |
a)
0.0359 kg/s b)
7.94 W c)
2.14 m2 |
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7.69 |
See
the hint for 7.57. |
a)
vb,before_impact = [2(mbgL + 1/2kd2)/(mb)]1/2 b)
v = (mbvb,after impact)/(mb+mm) |
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7.71 |
You
do not have any equations to compute enthalpy h at a specific state, you only have equations to compute the
change in enthalpy from one state to another. Therefore, you must write your
equations so they contain terms like (h1 - h3) and (h3
- h2). COM may be helpful. |
a)
0.4 ft3/min |
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