1 lesson 1&2- general law of conduction i
TRANSCRIPT
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ME 306 HEAT TRANSFER
Dr. Y. Mukkamala
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1) Boiling water
(fotosearch.com)
2) Condensing steam
(Purdue University)
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1. Heat Transfer : is the rate of energytransfer (i.e., J/s or Watts) from a hightemperature source to a low temperature
sink.
2. Heat transfer deals with the rate of
energy transfer, while thermodynamics :deals with magnitude of energy and itsconversion.
3. An insulated object at a certaintemperature possesses a magnitude of
internal energy, with no attendant heattransfer.
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1. Conduction : Heat transfer mode thatoccurs mainly in solids, liquids andstationary gases due to molecular
vibration and electron transport.
2. Convection : Heat transfer mechanismobserved in liquids and vapors due tobulk movement of a fluid.
3. Radiation : Heat transfer phenomenain which heat can be transferred in the
form of photons and electromagneticrays, across a temperature differentialwithout any participating media.
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Tgas
Twall
Tbead qconv
qrad
Hot FlueGases
Thermocouple
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Cartesian Coordinates.
xdTq kAc dX
(1)
.
xq : Heat Transfer Rate (W/m)
k : Thermal conductivity (W/ m K)
Ac : Cross Section Area (m2)
dT
dx: Temperature Gradient (C/m)
Radial Coordinates (Radial Conduction)
. dTq kAr r dr (2)
Ar = 2rL (Cylindrical Area)
dT
dr: Radial Temperature Gradient
Spherical Coordinates. dTq kAr r dr
. dTq kA d
(3)
. dTq kAd
dT
dr: Radial Temperature Gradient
dT
d,
dT
d: Circumferential Temperature Gradients
Ar = A = A = 4r2
(Spherical Surface Area : Solid Sphere)
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Energy Balance (Cartesian Coordinates)
. . .( )dq q q c VT x x dx gen pdt (4)
Using Taylors expansion theorem (neglecting higher order terms)
. '''. . .( ) ( )
q dxq q dx q dV c VT x x px dt
(5)
. '''.. ( . )
q dx dx q dx A c dx AT px dt
(6)
'''.( ) . ( . )
T dkA dx q dx A c dx AT pdtx x
(7)
If variation in physical properties and cross-section are assumed to be negligible
2
2
'''.. . ( )
p
T dkA dx q dx A A dx c T dtx
2
2
.2 '''
2
'''.
p
p
T dT
k q c dtx
cT q dT
k k dt x
(8)
.2 '''
21T q dT
k dtx
(9)
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nergy Balance (Cylindrical Coordinates)
. . . . . . '''( ) ( ) ( ) [ ]dq q q q q q q dV c VT r r dr z z dz pt
(14)
Where
. . .
. . .
( ) ; ( ) ; ( )
( . ); ( . ); ( . )r zr z
T T T
q kA q kA q kAr r r
q k rd dz q k dr dz q k rd dr
Hence Eqn. 14 can be re-written as
.. . '''[ . . . ] ( . . ) [ ( . . ). ]qq qr zdr d dz q dr dz rd c dr dz rd T pr z t
'''[ ( ) ( ) ( ) ] ( . . . ) [ . . ]k rd dzT dr k rdrdzT d k rd drT dz q dr dz r d T c dr dz rd zr pr z t
'''[ ( ) ( ) ( )] (. . ) [ ]k rT k rT k rT q r T c rT zr pr z t
(15)
The above equation simplifies as (for isotropic solid)
'''2 2 21 1 12 2 2 2 qT T T T T r r tkr r z
(16)
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STEADY STATE HEAT DIFFUSION EQUATIONS (No Source Term)
Cartesian Coordinates (1-D):
20
2d T
dx
2-D :
2
2
20
2
TT
yx
Cylindrical Coordinates (Ignoring Axial Diffusion)
2 10
2
dTd T
r drdr
Spherical Coordinates
'''2 21 1 1 1( ) ( ) ( )2 2 2 2 2
qT T TrT Sinr tkr r Sin r Sin
(17)
Equation 17 is the general heat diffusion equation in spherical coordinates with a
volumetric source term.
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k : Constant of proportionality fromFourier law.
Solids : Conduction in solids is due to
lattice vibrations (phonon transport),and electron transport. Phonon vibration contributes
insignificantly. Good electrical conductors are hence,
good heat conductors as well. Exs:Copper, Aluminum, and most other
metals, and some alloys. Similarly insulators are also poor heat
conductors.
Exceptions : Semi conductors; somealloys.
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Combined Heat Transfer Eqn :