Jadavpur University,Saltlake Campus Heat Transfer Laboratory Presentation on Heat Transfer From A Pin Fin Name Roll No Souvik Mondal 06 Kaushik Halder 07 Branch:-Power Engg. , 3rd Year
Oct 27, 2014
Jadavpur University,Saltlake CampusHeat Transfer Laboratory
Presentation on Heat Transfer From A Pin FinName Roll No
Souvik Mondal 06 Kaushik Halder 07
Branch:-Power Engg. , 3rd Year
TITLE :- Heat Transfer From A Pin Fin OBJECT:- (1) To study the temperature distribution along the length of a pin fin under forced convection with tip insulated. (2) To find out the heat transfer co- efficient of the pin fin & pin fin effectiveness.
What is heat transfer ?Heat Transfer is the exchange of thermal energy due to temp diff.This is of mainly 3 types->Conduction is a mode of transfer of energy within and between bodies of matter, due to a temperature gradient. Conduction means collisional and diff usive transfer of kinetic energy of particles of matter. Conduction takes place in all forms of matter, i.e. solids, liquids, gases. Heat tends to flow from a higher temperature body to a lower temperature body.
Convection is the movement of molecules within fluids i.e. liquids, gases.It cannot take place in solids, as neither bulk current flows nor significant diff usion can take place in solids.Convection is one of the major modes of heat transfer and mass transfer. In the context of heat and mass transfer,Convection is used to refer to the sum of Advective and Diff usive transfer.
Radiation is energy emitted by matter as Electromagnetic waves due to the storage of thermal energy that all matter possesses that has a temperature above absolute zero. Thermal radiation propagates through the vacuum of space.
Convection is of two types – (i) Natural Convection & (ii) Forced Convection
Natural convection is a type of heat transfer, in which the fluid motion is not generated by any external source (i.e. a pump, fan, blower etc.) but only by density differences in the fluid occurring due to temperature gradients.
Forced Convection is a type of heat transfer,in which the fluid movement results from external surface forces such as a fan or pump or blower. Forced convection is typically used to increase the rate of heat exchange. Many types of mixing also utilize forced convection to distribute one substance within another.
Application of extended surfaces in Convection:- For both modes of convection heat transfer i.e. Natural &Forced Convection,extended surface known as Fin, is used to increase the rate of heat transfer from a surface to a fluid where heat transfer coeffi cient of the surface and temp. diff. between them is not possible to increase.
How Fin increases the heat transfer rate? Fin increases the surface area available for heat transfer.
Wide application of fins:- Fins are vastly used on the radiator surface,on the boiler water tubes,heat exchanger tubes & sometimes on Electronic equipments.
APPLICATION OF PIN FIN IN PRACTICAL LIFE
pin fin heat sink is used to cool the processer .
The Front view of the experimental setupwhere Heat Transfer From Pin Fin experiment was done.
VoltmeterReadings
AmmeterReadings
TemperatureReadings
DeliveryPipe
Heater
Pump
Rectangular DuctWith Pin Fin
inside it
Manometer
Open Rectangular Channel of the device from where the air is sucked
PinFin Temperature
Point
One Side Opened Rectangular Duct With A Circular Pin Fin At The Center
12 mm
100 mm
150 mm
15mm 15mm30mm 30mm 30mm 30mm
Air is sucked inside
Pin fin
Hot Air
Air Flow Direction is shown here Through the Rectangular Duct
Assumptions:-(i) Steady state Heat Conduction.(ii) Pin Fin Tip insulated i.e. no heat convection from the pin fin tip.
(iii) The shape of pinfin is cylindrical so that perfect fluid and thermal boundary layer can construct.
No Heat Convection
Boundary layer over cylinder
Mathematical Formulae we used for calculation:-
T-Tf =
Where,
m=qfin=
Where,
.
q=(Ts-Tf)(hPAk) tanh mL & qideal=hPL(Ts-Tf)
Ts-Tf
Cosh m(L-x)
Cosh mL
hPkA.
ideal
I
Sl No
HeaterVoltage (V)
HeaterCurrent (Amp)
Manometer readingCm of H2O
Steady
T1
(.c)
State
T2
(.c)
Pin
T3
(.c)
Fin
T4
(.c)
Temp.T5
(.c)
FluidAmbientTemp. T6
(.c)
1. 40 0.17 1.6 74 64 56 51 48 33 2. 60 0.26 1.6 96 82 69 61 56 34 3. 70 0.30 1.6 102 86 72 64 58 34
Observation Table:-
Specifications:-
(i)Width=150 mm, Breadth=100 mm
(ii) Diameter of the Fin=12 mm
(iii) Diameter of the Orifice=20 mm
(iv) Diameter of the Delivery Pipe=40 mm
(v) Length of Fin=150 mm
(vi) Co-efficient of Discharge=0.61
Sample Calculation:-• Volume Flow Rate of Air,Q=Cd A1A2 2g[w/a-1]
A12-A2
2
or,Q=3.199*10-3 m3/sec• Velocity of Flowing Air,V=Q/a=0.242 m/sec
• Reynolds number,Re=VD/=176.322
• Value of Nusselt number using Correlation,Nu=0.683Re0.466Pr1/3
=6.76
now, T-Tf = Cosh m(L-x)
Ts-Tf Cosh mL
let,
Ts=T1, T=T2 & Tf=T6 we get the value of m through iteration
technique,m=10.85
• Theoritical Temperatures are, T2-33
= Cosh 10.85(0.135-0.03)
74-33 Cosh (10.85*0.135)Or,T2= 63.98 .c
Thus the Other Temperatures are, T3= 57.285 .c
T4= 53.179 .c
T5= 51.23 .c
• Fin Effectiveness, qeff= qfin
qwithout fin
= (Ts-Tf)(hPAk) tanh mL
hA(Ts-Tf)
= 27.61
0 20 40 60 80 100 120 140 1600
10
20
30
40
50
60
70
80
Experimental TemperaturesTheoritical Temper-atures
Length of Fin(mm)
Tem
pera
ture
s(. c)
Acknowledgement:-We are sincerely thankful to our teachers->
(i) Prof. Apurba K. Santra
(ii) Prof. Amitava Dutta
(iii) Sri Atish Nandi
(iv) Sri Biraswar paul (v) Sri Prakas Ghosh.
Thank You
Good Afternoon