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BIRLA VISHVAKARMA MAHAVIDYALAYA,BIRLA VISHVAKARMA MAHAVIDYALAYA,
ENGINEERING COLLAGE.ENGINEERING COLLAGE.
SUBJECT :-ENGINEERING THERMODYNAMICS ANDSUBJECT :-ENGINEERING THERMODYNAMICS AND
HEAT TRANSFER(2132502)HEAT TRANSFER(2132502)
TOPIC :-PRESENTATION ON RADIATIONTOPIC :-PRESENTATION ON RADIATION
GROUP NO.16GROUP NO.16
PREPARED BY :-PREPARED BY :-
 SAHARSH TANDEL -140080125029SAHARSH TANDEL -140080125029
 RUSHABH ZALAWADIAYA -140080125031RUSHABH ZALAWADIAYA -140080125031
 PATELIA KRUNAL -15PES301PATELIA KRUNAL -15PES301
 DHARMIK DAVE -15PES302DHARMIK DAVE -15PES302
SHAPE FACTORSHAPE FACTOR
ALGEBRAALGEBRA
PREPARED BY :- SAHARSH TANDELPREPARED BY :- SAHARSH TANDEL
Shape FactorShape Factor
• The shape factor may be defind as the
fraction of radiative energy that is diffusd from our
surface element and strikes the other surfce
directly with no intervenctions.
•Equation 31is applicable to black surface only and mut
not be used for surfaces having emissivities other than
one.
•For calculation of shape factors/geometry factors for
specific geometries and for the analiys of radiant heat
exchange between surfaces, the following propertis and
factors may be useful :
1) The shape factor is purely funcion of geometry
perameters and it is also known as geometry factor.
2) A1F12=A2F12 (reciprocity theorm)
Above relectionship is useful when one of the shape
factor is unity.
3) For a convex or flat surface, the shape factor with
respect to it self is zero (i.e F1-1=0), because one
Cannot see any other part of same surface.
4) For a concave surface, the shape factor with respect to
itself is not equal to zero because energy coming out from
one part of the surface is intercepted by the another part of
the same surface.
5) For the two infinite parallel surfaces the shape factor
value is unity.
F12=F21=1[A1=A2]
ELECTRICALELECTRICAL
ANALOGYANALOGY
PREPARED BY :- RUSHABH ZALAVADIYAPREPARED BY :- RUSHABH ZALAVADIYA
Electrical networkElectrical network
analogy for thermalanalogy for thermal
radiation systemradiation system
An electrical network analogy is an alternative
approach for analysing radiation heat exchange
between any surface(black or non-black).
Electrical network analogy for two non-Electrical network analogy for two non-
black/gray bodies exchanging heatblack/gray bodies exchanging heat
with each otherwith each other
(Q1-2)Net =Eb1-Eb2/1-ɛ1/A1ɛ1 +1/A1F12+1-ɛ2/A2ɛ2
=σA1(T1
4
-T2
4
) / 1-ɛ1/ɛ1 + 1 / F12 + 1-ɛ2/ɛ2*A1/A2
Q12 = 1 / 1-ɛ1/ɛ1 + 1/F12 + 1-ɛ2/ɛ2
Q12 = (fg)1-2σ*A1*(T1
4
-T2
4
)
(fg)1-2 is known as gray body factor .
Electrical network for two non-Electrical network for two non-
black bodies which are parallel toblack bodies which are parallel to
each othereach other
1)A1=A2,
2)F12=1
So, the intercharge factor or gray body
factor is reduced to,
 f1-2=(F)12=1 / 1-ɛ1/ɛ1 + 1 + 1-ɛ2/ɛ2
 1 / 1/ɛ1 + 1/ɛ2 - 1
Electrical network for concentricElectrical network for concentric
cylinders or spheres:cylinders or spheres:
For concentric cylinders and spheres, F1-2=1
A1 /A2 = πd1L /πd2L = d1 / d2 = r1 /r2
A1 / A2 = 4πr1
2
/ 4πr2
2
= r1
2
/ r2
2
 So,
f1-2 = (Fg)1-2 = 1 / 1-ɛ1/ɛ1 + 1/1 + 1-ɛ2/ɛ2*A1/A2
Radiation shieldsRadiation shields
PREPARED BY :- krunal pateliaPREPARED BY :- krunal patelia
•Radiation heat transfer between two surfaces can be reduced greatly by
inserting a thin, high-reflectivity (low-emissivity) sheet of material between
the two surfaces.
•Such highly reflective thin plates or shells are called radiation shields.
•Multilayer radiation shields constructed of about 20 sheets per cm
thickness separated by evacuated space are commonly used in
cryogenic and space applications.
•Radiation shields are also used in temperature measurements of fluids
to reduce the error caused by the radiation effect when the temperature
sensor is exposed to surfaces that are much hotter or colder than the fluid
itself.
•The role of the radiation shield is to reduce the rate of radiation heat
transfer by placing additional resistances in the path of radiation heat
flow.
•The lower the emissivity of the shield, the higher the resistance.
•Radiation heat
transfer between two
large parallel plates
•Radiation heat transfer between two large parallel plates with one
shield
•The radiation
shield placed
between
•two parallel
plates and the
radiation
network
associated
with it.
•14
IntroductionIntroduction
toto
Gas RadiationGas Radiation
PREPARED BY :- DHARMIK DAVEPREPARED BY :- DHARMIK DAVE
Radiation in absorbing- emitting mediaRadiation in absorbing- emitting media
• When a medium is transparent to radiation,
radiation propagating through such a media
remains unchanged
• However gases such as CO, NO, CO2, SO2,
H2O and various hydrocarbons absorb and emit
radiation over certain wavelength regions called
absorption bands
• We will discuss a very simple analysis of
radiation exchange in an absorbing and emitting
medium, exchange between a body of hot gas
and its black enclosure
Beer’s LawBeer’s Law
• If Io is the intensity of radiation at the source and I is the
observed intensity after a given path, then optical depth τ
is defined by the following equation:
∀β
•s
Characterization of Participating MediaCharacterization of Participating Media :-:-
 Absorption: attenuation of intensity
 Emission: augmentation of intensity
 Scattering →
– In-scattering: augmentation of intensity
– Out-scattering: attenuation of intensity
Equation of Radiative TranferEquation of Radiative Tranfer
• Increase in Intensity of radiation per unit length
along the direction of propagation is
Transmissivity, Absorptivity andTransmissivity, Absorptivity and
EmissivityEmissivity
• Solution of Radaitive Transfer Equation with the
assumption that κ λ and Ibλ(T) are constant
everywhere in the medium, gives
Radiation Exchange between a GasRadiation Exchange between a Gas
Body and its Black EnclosureBody and its Black Enclosure
• Assumption:
– Entire gas body is isothermal
– Enclosure wall is black
• Consider a hemispherical body of gas at uniform
temperature Tg and walls are at temperature Tw
• The intensity of spectral radiation Iλ(L) striking the
surface element dA as a result of the emission of
radiation by the gas along the path L is determined
from
Spectral Emissivity of GasSpectral Emissivity of Gas
Emissivity ChartsEmissivity Charts
• Hottel measured gas emissivity εg and presented
emissivity charts for gases such as CO2, H20,
CO, ammonia, SO2, etc. as a function of
temperature and product term PiL, where Pi is the
partial pressure (in atmospheres) of gas i in the
gas mass and L is the beam length.
Calculation of Radiation exchangeCalculation of Radiation exchange
between a Gas Body and Itsbetween a Gas Body and Its
enclosureenclosure
• The net radiative heat exchange Q between
the gas mass at temperature Tg and its black
surroundings at temperature Tw is
THANK YOUTHANK YOU

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Etht grp 16 (1400080125029,30,31,32)

  • 1. BIRLA VISHVAKARMA MAHAVIDYALAYA,BIRLA VISHVAKARMA MAHAVIDYALAYA, ENGINEERING COLLAGE.ENGINEERING COLLAGE. SUBJECT :-ENGINEERING THERMODYNAMICS ANDSUBJECT :-ENGINEERING THERMODYNAMICS AND HEAT TRANSFER(2132502)HEAT TRANSFER(2132502) TOPIC :-PRESENTATION ON RADIATIONTOPIC :-PRESENTATION ON RADIATION GROUP NO.16GROUP NO.16 PREPARED BY :-PREPARED BY :-  SAHARSH TANDEL -140080125029SAHARSH TANDEL -140080125029  RUSHABH ZALAWADIAYA -140080125031RUSHABH ZALAWADIAYA -140080125031  PATELIA KRUNAL -15PES301PATELIA KRUNAL -15PES301  DHARMIK DAVE -15PES302DHARMIK DAVE -15PES302
  • 2. SHAPE FACTORSHAPE FACTOR ALGEBRAALGEBRA PREPARED BY :- SAHARSH TANDELPREPARED BY :- SAHARSH TANDEL
  • 3. Shape FactorShape Factor • The shape factor may be defind as the fraction of radiative energy that is diffusd from our surface element and strikes the other surfce directly with no intervenctions.
  • 4. •Equation 31is applicable to black surface only and mut not be used for surfaces having emissivities other than one. •For calculation of shape factors/geometry factors for specific geometries and for the analiys of radiant heat exchange between surfaces, the following propertis and factors may be useful : 1) The shape factor is purely funcion of geometry perameters and it is also known as geometry factor. 2) A1F12=A2F12 (reciprocity theorm) Above relectionship is useful when one of the shape factor is unity. 3) For a convex or flat surface, the shape factor with respect to it self is zero (i.e F1-1=0), because one
  • 5. Cannot see any other part of same surface. 4) For a concave surface, the shape factor with respect to itself is not equal to zero because energy coming out from one part of the surface is intercepted by the another part of the same surface. 5) For the two infinite parallel surfaces the shape factor value is unity. F12=F21=1[A1=A2]
  • 6.
  • 7. ELECTRICALELECTRICAL ANALOGYANALOGY PREPARED BY :- RUSHABH ZALAVADIYAPREPARED BY :- RUSHABH ZALAVADIYA
  • 8. Electrical networkElectrical network analogy for thermalanalogy for thermal radiation systemradiation system An electrical network analogy is an alternative approach for analysing radiation heat exchange between any surface(black or non-black).
  • 9. Electrical network analogy for two non-Electrical network analogy for two non- black/gray bodies exchanging heatblack/gray bodies exchanging heat with each otherwith each other (Q1-2)Net =Eb1-Eb2/1-ɛ1/A1ɛ1 +1/A1F12+1-ɛ2/A2ɛ2 =σA1(T1 4 -T2 4 ) / 1-ɛ1/ɛ1 + 1 / F12 + 1-ɛ2/ɛ2*A1/A2 Q12 = 1 / 1-ɛ1/ɛ1 + 1/F12 + 1-ɛ2/ɛ2 Q12 = (fg)1-2σ*A1*(T1 4 -T2 4 ) (fg)1-2 is known as gray body factor .
  • 10. Electrical network for two non-Electrical network for two non- black bodies which are parallel toblack bodies which are parallel to each othereach other 1)A1=A2, 2)F12=1 So, the intercharge factor or gray body factor is reduced to,  f1-2=(F)12=1 / 1-ɛ1/ɛ1 + 1 + 1-ɛ2/ɛ2  1 / 1/ɛ1 + 1/ɛ2 - 1
  • 11. Electrical network for concentricElectrical network for concentric cylinders or spheres:cylinders or spheres: For concentric cylinders and spheres, F1-2=1 A1 /A2 = πd1L /πd2L = d1 / d2 = r1 /r2 A1 / A2 = 4πr1 2 / 4πr2 2 = r1 2 / r2 2  So, f1-2 = (Fg)1-2 = 1 / 1-ɛ1/ɛ1 + 1/1 + 1-ɛ2/ɛ2*A1/A2
  • 12. Radiation shieldsRadiation shields PREPARED BY :- krunal pateliaPREPARED BY :- krunal patelia
  • 13. •Radiation heat transfer between two surfaces can be reduced greatly by inserting a thin, high-reflectivity (low-emissivity) sheet of material between the two surfaces. •Such highly reflective thin plates or shells are called radiation shields. •Multilayer radiation shields constructed of about 20 sheets per cm thickness separated by evacuated space are commonly used in cryogenic and space applications. •Radiation shields are also used in temperature measurements of fluids to reduce the error caused by the radiation effect when the temperature sensor is exposed to surfaces that are much hotter or colder than the fluid itself. •The role of the radiation shield is to reduce the rate of radiation heat transfer by placing additional resistances in the path of radiation heat flow. •The lower the emissivity of the shield, the higher the resistance.
  • 14. •Radiation heat transfer between two large parallel plates •Radiation heat transfer between two large parallel plates with one shield •The radiation shield placed between •two parallel plates and the radiation network associated with it. •14
  • 15.
  • 16.
  • 17. IntroductionIntroduction toto Gas RadiationGas Radiation PREPARED BY :- DHARMIK DAVEPREPARED BY :- DHARMIK DAVE
  • 18. Radiation in absorbing- emitting mediaRadiation in absorbing- emitting media • When a medium is transparent to radiation, radiation propagating through such a media remains unchanged • However gases such as CO, NO, CO2, SO2, H2O and various hydrocarbons absorb and emit radiation over certain wavelength regions called absorption bands • We will discuss a very simple analysis of radiation exchange in an absorbing and emitting medium, exchange between a body of hot gas and its black enclosure
  • 19.
  • 20.
  • 21. Beer’s LawBeer’s Law • If Io is the intensity of radiation at the source and I is the observed intensity after a given path, then optical depth τ is defined by the following equation: ∀β •s
  • 22. Characterization of Participating MediaCharacterization of Participating Media :-:-  Absorption: attenuation of intensity  Emission: augmentation of intensity  Scattering → – In-scattering: augmentation of intensity – Out-scattering: attenuation of intensity
  • 23. Equation of Radiative TranferEquation of Radiative Tranfer • Increase in Intensity of radiation per unit length along the direction of propagation is
  • 24. Transmissivity, Absorptivity andTransmissivity, Absorptivity and EmissivityEmissivity • Solution of Radaitive Transfer Equation with the assumption that κ λ and Ibλ(T) are constant everywhere in the medium, gives
  • 25. Radiation Exchange between a GasRadiation Exchange between a Gas Body and its Black EnclosureBody and its Black Enclosure • Assumption: – Entire gas body is isothermal – Enclosure wall is black • Consider a hemispherical body of gas at uniform temperature Tg and walls are at temperature Tw • The intensity of spectral radiation Iλ(L) striking the surface element dA as a result of the emission of radiation by the gas along the path L is determined from
  • 26. Spectral Emissivity of GasSpectral Emissivity of Gas
  • 27. Emissivity ChartsEmissivity Charts • Hottel measured gas emissivity εg and presented emissivity charts for gases such as CO2, H20, CO, ammonia, SO2, etc. as a function of temperature and product term PiL, where Pi is the partial pressure (in atmospheres) of gas i in the gas mass and L is the beam length.
  • 28.
  • 29. Calculation of Radiation exchangeCalculation of Radiation exchange between a Gas Body and Itsbetween a Gas Body and Its enclosureenclosure • The net radiative heat exchange Q between the gas mass at temperature Tg and its black surroundings at temperature Tw is