pdf hw 2
pdf
keyboard_arrow_up
School
University of Alabama *
*We aren’t endorsed by this school
Course
250
Subject
Mechanical Engineering
Date
Apr 3, 2024
Type
Pages
13
Uploaded by KidStarPorpoise32
ME 309 HW 2 (Chapter 2) Question 1 of 5 Consider steady-state conditions for one-dimensional conduction in a plane wall having a thermal conductivity k = 50 W/m-K and a thickness L = 0.4 m, with no internal heat generation. Determine the heat flux, in kW/mZ2, and the unknown quantity for each case. Case Ty (°C) 50 -30 70 T,(°C) -20 -10 20/20 134 40 30 dT/dx (K/m) q; (kW/m?) -175 8.75 50 -2.5 160 -8 -80 4 200 -10 1— 2= = B support
ME 309 HW 2 (Chapter 2) Question 2 of 5 < > 20/20 i= Show Attempt History Consider a plane wall 140 mm thick and of thermal conductivity 120 W/m-K. Steady-state conditions are known to exist with T; = 500K and T, = 700 K. Determine the heat flux g7, in kW/mZ, and the temperature gradient dT/dx, in K/m, for the coordinate systems shown. T(x) T(x) T(x) » X X X (a) (b) (c) Part A @ v Your answer is correct. ’ B support
VNP BT Question 2 of 5 < > 20/20 = Part A ‘ v Your answer is correct. Determine the heat flux g7 ,in kW/mZ2, and the temperature gradient dT/dx, in K/m, for the coordinate system shown. T(x) (a1), = -171.4284 KW/m? dT @ ( — ) = 142857 K/m dx i
Your preview ends here
Eager to read complete document? Join bartleby learn and gain access to the full version
- Access to all documents
- Unlimited textbook solutions
- 24/7 expert homework help
ME 309 HW 2 (Chapter 2) Question 2 of 5 < > 20/20 = Part B ‘ v Your answer is correct. ’ Determine the heat flux g/ , in kW/m?, and the temperature gradient dT/dx, in K/m, for the coordinate system shown. T(x) T, (¢2), = 171.4284 KW/m? R support =) = _ K j (dx )b 1428.57 /m
VNP B Question 2 of 5 < > 20/20 i= Part C ‘ v Your answer is correct. ’ Determine the heat flux g¥ ,in kW/m?2, and the temperature gradient dT/dx, in K/m, for the coordinate system shown. T(x) (a7), = -171.4284 kW/m? dT @ (—) = 1428.57 K/m dx /, B support
ME 309 HW 2 (Chapter 2) Question 3 of 5 < > 20/20 i= Consider a 310 mm x 310 mm window in an aircraft. For a temperature difference of 80°C from the inner to the outer surface of the window, calculate the heat loss through L = 10-mm-thick polycarbonate, soda lime glass, and aerogel windows, respectively. The thermal conductivities of the aerogel and polycarbonate are k,, = 0.014 W/m-Kand k,. = 0.21W/m-K, respectively. Evaluate the thermal conductivity of the soda lime glass at 300 K. If the aircraft has 120 windows and the cost to heat the cabin air is $1/kW-h, compare the costs associated with the heat loss through the windows for an 8-hour intercontinental flight. The thermal conductivity of the soda lime glass, in W/m-K: kgl = 14 W/m-K The heat loss through the soda lime glass, in W: Grg = | 107632 W The heat loss through the polycarbonate, in W: Gy = | 161448 W The heat loss through the aerogel windows, in W: Geq = | 1076 w The costs associated with the heat loss for glass windows, in $: B support Cy = $ | 103327 @ The costs associated with the heat loss for polycarbonate windows, in $:
Your preview ends here
Eager to read complete document? Join bartleby learn and gain access to the full version
- Access to all documents
- Unlimited textbook solutions
- 24/7 expert homework help
ME 309 HW 2 (Chapter 2) Question3of 5 < > 20/20 = = The heat loss through the soda lime glass, in W: Grg = | 107632 W The heat loss through the polycarbonate, in W: Gy = | 161448 W The heat loss through the aerogel windows, in W: Geq = | 1076 W The costs associated with the heat loss for glass windows, in $: Cy = $ | 103327 The costs associated with the heat loss for polycarbonate windows, in $: C, = $ | 15499 The costs associated with the heat loss for aerogel windows, in $: C,=9%] 1033 Physical Properties Mathematical Functions @ eTextbook and Media
ME 309 HW 2 (Chapter 2) Question 4 of 5 < View Policies Show Attempt History 20/20 = Uniform internal heat generationat ¢ = 2.00 x 107 W/m?3is occurring in a cylindrical nuclear reactor fuel rod of 50-mm diameter, and under steady-state conditions the temperature distribution is of the form T' () = a + br?, where T'is in degrees Celsius and r is inmeters, whilea = 800°Cand b = -1.667 x 10°°C/m?2 The fuel rod propertiesare k = 30 W/m-K,p = 1100 kg/m® andc, = 800 J/kg-K. Physical Properties Mathematical Functions Step 1 ‘ v Your answer is correct. Find the steady state temperature gradient at the outer surface of the rod, in °C/m. or = 8335 ar r=r, - - °C/m Attempts: unlimited
VNP BT Question 4 of 5 Step 2 20/20 = v Your answer is correct. What is the steady state rate of heat transfer at the outer surface, in W/m? q (ro) = Step 3 39277.76 W/m Attempts: unlimited v Your answer is correct. What is the steady state rate of heat transfer at the centerline, in W/m? q (0) = W/m Attempts: unlimited
Your preview ends here
Eager to read complete document? Join bartleby learn and gain access to the full version
- Access to all documents
- Unlimited textbook solutions
- 24/7 expert homework help
VNP BT Question 4 of 5 < > 20/20 = Step 4 v Your answer is correct. If the reactor power level is suddenly increased to g, = 1x 108 W/m3 (att = 0 sec),immediately after that what is the temperature at the centerline, in °C? T(0) = | 800 °C Attempts: unlimited Step 5 v Your answer is correct. ’ Immediately after the sudden increase in reactor power level to g, = 1x 108 W/m3(att = 0 sec), what is the time rate of temperature change at the centerline, in °C/s? oT = = 90.9 °C/s ot B support
ME 309 HW 2 (Chapter 2) Question 5 of 5 < 20/20 i= The steady-state temperature distribution in a one-dimensional wall of thermal conductivity 50 W/m-K and thickness 140 mm is observed to be T’ (OC) = a+ bx?,wherea = 200°C,b = -2000 C/m2, and x is in meters. (1) What is the heat generation rate g in the wall? (2) Determine the heat fluxes at the two wall faces. Physical Properties Mathematical Functions Step 1 ‘ v Your answer is correct. What is the temperature gradient evaluated at x = L,in°C/m? dT — = -560 °C/m dx x=L Attempts: unlimited
VNP B Question Step 2 50f 5 < 20/20 = ‘ v Your answer is correct. What is the second derivative of temperature with respect to x evaluated at x = L,in°C/m?%? Step 3 -4000 °C/m? Attempts: unlimited v Your answer is correct. What is the heat generation rate in the wall, in W/m3? q: 200000 W/m?3 Attempts: unlimited R support
Your preview ends here
Eager to read complete document? Join bartleby learn and gain access to the full version
- Access to all documents
- Unlimited textbook solutions
- 24/7 expert homework help
VNP B Question 5 of 5 Step 4 < 20/20 = ‘ v Your answer is correct. What is the heat flux at x = 0, in W/m2? q" (0) = Step 5 W/m? Attempts: unlimited v Your answer is correct. What is the heat flux at x = L,in W/m?? q " X(L) = eTextbook and Media 28000 W/m?2 Attempts: unlimited R support
Related Documents
Related Questions
1- Consider steady- state conduction for one-dimensional conduction in a plane wall
having a thermal conductivity k=50 W/m.K and a thickness L-0.25 m, with no
internal heat generation.
Determine the heat flux and the unknown quantity (blanks) for each case and
sketch the temperature distribution, indicating the direction of heat flux.
Case
TI(°C)
50
T2(°C)
-20
dT/dx(K/m)
1
-30
-10
70
160
40
-80
5
30
200
234n
arrow_forward
Consider steady-state conditions for one-dimensional conduction in a plane wall having a thermal conductivity k = 40 W/m-K and a
thickness L = 0.3 m, with no internal heat generation.
T2
L
Determine the heat flux, in kW/m?, and the unknown quantity for each case.
T1 (°C)
T2(°C)
dT/dx(K/m)
9 (kW/m?)
Case
1
50
-20
i
i
2
-30
-10
i
70
i
160
i
40
-80
i
5
i
30
200
i
arrow_forward
Consider steady-state conditions for one-dimensional conduction in a plane wall having a thermal conductivity k = 40 W/m•K and a
thickness L = 0.3 m, with no internal heat generation.
L
Determine the heat flux, in kW/m2, and the unknown quantity for each case.
Case
T1(°C)
T2(°C)
dT/dx(K/m)
(kW/m²)
1
50
-20
i
i
2
-30
-10
i
3
70
i
160
i
4
i
40
-80
i
i
30
200
i
arrow_forward
Answer correctly and quickly as possible please.
arrow_forward
Solve using the methodology : Known, Find, Schematic Diagram, Assumptions, Properties, Analysis and Comments.
arrow_forward
Consider steady-state conditions for one-dimensional conduction in a plane wall having a thermal conductivity k = 40
W/m-K and a thickness L = 0.4 m, with no internal heat generation.
-T2
L
Determine the heat flux, in kW/m2, and the unknown quantity for each case.
Case
T1(°C)
T2(°C)
dT/dx(K/m)
9% (kW/m²)
1
50
-20
i
i
-30
-10
i
i
3
70
i
160
i
4
i
40
-80
i
i
30
200
i
LO
arrow_forward
Consider a copper plate that has dimensions of 3 cm x 3 cm x 7 cm (length, width, and thickness, respectively). As shown in the following figure, the copper plate is exposed to a thermal
energy source that puts out 126 J every second. The density of copper is 8,900 kg/m³. Assume there is no heat loss to the surrounding block.
126 J
Copper
Insulation
Ⓡ
What is the specific heat of copper (in J/(kg K))?
J/(kg. K)
What is the mass of the copper plate (in kg)?
kg
How much energy (in J) will be consumed during 11 seconds?
J
Determine the temperature rise (in K) in the plate after 11 seconds.
arrow_forward
=
Consider a large plane wall of thickness L=0.3 m, thermal conductivity k = 2.5 W/m.K,
and surface area A = 12 m². The left side of the wall at x=0 is subjected to a net heat
flux of ɖo = 700 W/m² while the temperature at that surface is measured to be T₁ =
80°C. Assuming constant thermal conductivity and no heat generation in the wall, (a)
express the differential equation and the boundary equations for steady one-
dimensional heat conduction through the wall, (b) obtain a relation for the variation of
the temperature in the wall by solving the differential equation, and (c) evaluate the
temperature of the right surface of the wall at x=L.
Ti
до
L
X
arrow_forward
Look at the picture and thank you
arrow_forward
Determine the heat conduction of a boiler if you are given the following data: The thickness of the boiler is 15 cm, the T1 is the temperature of the water is 25°C and the T2 of the steam is 110°C, the thermal conductivity The boiler material is iron (use presentation table), the boiler area is 4.5 m^2
arrow_forward
SEE MORE QUESTIONS
Recommended textbooks for you

Principles of Heat Transfer (Activate Learning wi...
Mechanical Engineering
ISBN:9781305387102
Author:Kreith, Frank; Manglik, Raj M.
Publisher:Cengage Learning
Related Questions
- 1- Consider steady- state conduction for one-dimensional conduction in a plane wall having a thermal conductivity k=50 W/m.K and a thickness L-0.25 m, with no internal heat generation. Determine the heat flux and the unknown quantity (blanks) for each case and sketch the temperature distribution, indicating the direction of heat flux. Case TI(°C) 50 T2(°C) -20 dT/dx(K/m) 1 -30 -10 70 160 40 -80 5 30 200 234narrow_forwardConsider steady-state conditions for one-dimensional conduction in a plane wall having a thermal conductivity k = 40 W/m-K and a thickness L = 0.3 m, with no internal heat generation. T2 L Determine the heat flux, in kW/m?, and the unknown quantity for each case. T1 (°C) T2(°C) dT/dx(K/m) 9 (kW/m?) Case 1 50 -20 i i 2 -30 -10 i 70 i 160 i 40 -80 i 5 i 30 200 iarrow_forwardConsider steady-state conditions for one-dimensional conduction in a plane wall having a thermal conductivity k = 40 W/m•K and a thickness L = 0.3 m, with no internal heat generation. L Determine the heat flux, in kW/m2, and the unknown quantity for each case. Case T1(°C) T2(°C) dT/dx(K/m) (kW/m²) 1 50 -20 i i 2 -30 -10 i 3 70 i 160 i 4 i 40 -80 i i 30 200 iarrow_forward
- Answer correctly and quickly as possible please.arrow_forwardSolve using the methodology : Known, Find, Schematic Diagram, Assumptions, Properties, Analysis and Comments.arrow_forwardConsider steady-state conditions for one-dimensional conduction in a plane wall having a thermal conductivity k = 40 W/m-K and a thickness L = 0.4 m, with no internal heat generation. -T2 L Determine the heat flux, in kW/m2, and the unknown quantity for each case. Case T1(°C) T2(°C) dT/dx(K/m) 9% (kW/m²) 1 50 -20 i i -30 -10 i i 3 70 i 160 i 4 i 40 -80 i i 30 200 i LOarrow_forward
- Consider a copper plate that has dimensions of 3 cm x 3 cm x 7 cm (length, width, and thickness, respectively). As shown in the following figure, the copper plate is exposed to a thermal energy source that puts out 126 J every second. The density of copper is 8,900 kg/m³. Assume there is no heat loss to the surrounding block. 126 J Copper Insulation Ⓡ What is the specific heat of copper (in J/(kg K))? J/(kg. K) What is the mass of the copper plate (in kg)? kg How much energy (in J) will be consumed during 11 seconds? J Determine the temperature rise (in K) in the plate after 11 seconds.arrow_forward= Consider a large plane wall of thickness L=0.3 m, thermal conductivity k = 2.5 W/m.K, and surface area A = 12 m². The left side of the wall at x=0 is subjected to a net heat flux of ɖo = 700 W/m² while the temperature at that surface is measured to be T₁ = 80°C. Assuming constant thermal conductivity and no heat generation in the wall, (a) express the differential equation and the boundary equations for steady one- dimensional heat conduction through the wall, (b) obtain a relation for the variation of the temperature in the wall by solving the differential equation, and (c) evaluate the temperature of the right surface of the wall at x=L. Ti до L Xarrow_forwardLook at the picture and thank youarrow_forward
arrow_back_ios
arrow_forward_ios
Recommended textbooks for you
- Principles of Heat Transfer (Activate Learning wi...Mechanical EngineeringISBN:9781305387102Author:Kreith, Frank; Manglik, Raj M.Publisher:Cengage Learning

Principles of Heat Transfer (Activate Learning wi...
Mechanical Engineering
ISBN:9781305387102
Author:Kreith, Frank; Manglik, Raj M.
Publisher:Cengage Learning