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International Journal of Trend in Scientific Research and Development (IJTSRD)
Volume 4 Issue 4, June 2020 Available Online: www.ijtsrd.com e-ISSN: 2456 – 6470
@ IJTSRD | Unique Paper ID – IJTSRD31613 | Volume – 4 | Issue – 4 | May-June 2020 Page 1562
Effect of Different Fin Geometries on Heat Transfer Coefficient
Rohit, Kuldeep
UG Student, Department of Mechanical Engineering,
Dronacharya College of Engineering, Gurugram, Haryana, India
ABSTRACT
High rate of heat flow is the demand of number of engineering applications,
heat exchangers used in process industries, economizersusedtoheat waterto
boiler or activities like cooling of IC engines. Also, the removal of heat from
integral circuit or exchange of heat between two fluids as in nuclear power
plants many researchers contributed inenhancementofheattransferthrough
various approaches. Increase in heat transfer rate and to derive is being done
by using different techniques or by performing experiments as well previous
literature mentioned the theory regarding heat transfer in such a way that it
will increased by increasing area and heat transfer coefficient. In case of
natural convection there is only scope for increasing heat transfer area, there
extended surfaces i.e. fins are better option to it.Otheradvantageisincreasing
turbulence with pitch therefore it enhances heat transfer. Study of heat
transfer is possible through numerical experimental analysis. In case of
numerical analysis, the results give’s heat flow pattern and but less accurate.
Whereas experimental analysis gives accurate results but require setup,time
and valid conditions.
KEYWORDS: Conduction, Fins, Geometry, Heat Transfer Co-efficient, Natural
Convection, Steady State Heat Transfer, Temperature
How to cite this paper: Rohit | Kuldeep
"Effect of Different Fin Geometries on
Heat Transfer Coefficient" Published in
International Journal
of Trend in Scientific
Research and
Development(ijtsrd),
ISSN: 2456-6470,
Volume-4 | Issue-4,
June 2020, pp.1562-
1565, URL:
www.ijtsrd.com/papers/ijtsrd31613.pdf
Copyright © 2020 by author(s) and
International Journal ofTrendinScientific
Research and Development Journal. This
is an Open Access article distributed
under the terms of
the Creative
CommonsAttribution
License (CC BY 4.0)
(http://creativecommons.org/licenses/by
/4.0)
1. INTRODUCTION
Actual convection heat transfer in a fluid layer confined in a
closed enclosure with partitions like fins is encountered in a
wide variety of engineering applications. Such as in power
and automotive sectorswhereheatexchangers,economizers
used to heat the feed water to boiler and the activities like
cooling of internal combustion engine, also removal of heat
from integrated circuitsintheelectroniccircuitsorexchange
of heat between two fluids as inn nuclear power plants,
passive cooling of electronic equipment such as compact
power supplies, portable computers and
telecommunications enclosures. In the design of electronic
packages, there are strong incentives to mount as much
electronic components as possible in a given enclosure. This
leads to high power generation density and this may raise
the temperature of the packages above the allowable limit.
Therefore, there is need to increase heat transfer rate for
working a device at designed at efficiency.Manyresearchers
have been mentioned through their literature, heat transfer
rate is increased by increasing heat transfer coefficientor by
heat transfer area. In case of natural convection thereisonly
scope for increasing heat transfer area by providing finned
surfaces. The enhancement ratio ofheattransferdepends on
the fin’s orientations and the geometric parameters of fin
arrays. The most common configurations of using fin arrays
in heat sinks involve horizontal or vertical surface plate to
which fin arrays are attached. Specially designed finned
surfaces called heat sink, which are commonly used in the
cooling of electronic equipment and stationary engines
needs optimized design with minimum material and
maximum heat transfer from them. In the natural cooling of
fins, the temperature drops along the fins exponentially and
reaches the environment temperature at some length. But
heat transfer from the area near the tip is low. It results in
wastage of material for small heat transfer rate. Cutting this
portion of fins, results in the complete elimination of heat
transfer from that region. Also, the central portion of the fin
flat becomes ineffective due to the fact that, already heated
air comes in its contact. In this project the fin modified by
removing the central fin portion by cutting a notch of
different geometrical shapes and adding it at the arrays
entrance on the two sides, where it is more effective and
thereby keeping fin surface area same.
2. MATERIALS AND METHODOLGY
2.1. Materials The most important elements of the
experimental set-up are the set of fins and a Base Plate on
which these fins are mounted. Base plate and fins with
different notch geometries are made up of aluminum.
Selection criteria for a aluminum is based on thermal
conductivity, density, cost and from manufacturing point of
view. The used Aluminium has thermal conductivityof237.4
w/mk and density 2712 kg/m3.
S.NO. Tests Actual Specified UOM
1. SUCON 0.3728 0 %
2. MAGANESE 0.1982 0 %
3. NICKEL 0.0104 0 %
4. CROMIUM 0.0176 0 %
5. COPPER 0.2201 0 %
6. TITANUM 0.0092 0 %
7. ALUMINIUM 97.450 0 %
8. FE 1.3023 0 %
9. MG 0.0926 0 %
Fig.No.1: Composition of Aluminium used for Baseplate and
Fins
IJTSRD31613
International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD31613 | Volume – 4 | Issue – 4 | May-June 2020 Page 1563
Fig.No.2 Aluminium Base Plate
Fig.No.3 Fins with different Geometry
Fig.No.4 Apparatus of the Experiment
2.2 Fabrication Sheets of Aluminum are purchased
directly from the shops available in the market. The sheets
required for this purpose are of thickness 2mm which are
available in that thickness. All the sets of fins and the base
plate are cut and machined in the workshop. Fins with
rectangular notch are cut very easilywiththehacksawasthe
machining of aluminum is very easy. The fins with circular
notches are cut with the help of milling machine. Fins with
triangular and trapezoidal notches are also cut withthehelp
of hacksaw manually. One set of fins include five number of
fin flats. There are five such sets of fins, for the fins without
notch, fins with circular notch, fins with rectangular notch,
fins with triangular notch, and fins with trapezoidal notch.
The dimensions the notches selectedastomaintaina surface
area in and the depth of notch constant for all notched fins.
These three fin flats are mounted on one base. Thus a total
number of fin flats fabricated are 18. Only a single base plate
is fabricated with notches and thesamebaseplateisused for
all the sets of fins. The dimensions of base plate are
[200x200] mm the three fins are placed on the base plate in
the slots made on the base plate at equal intervals. The
distance between the slots thus obtained is 20 mm. Base
plates and the set of three fins were assembled.
2.3 Method The Apparatus consisted of Base frame to
inscribe various equipments such as Dimmerstattoregulate
the voltage supply. Multi-point temperature indicator with
digital display in terms of degree Celsius. J-type
thermocouple were used to measure the temperature at tip
of the fins. A heater of 600 Watt capacity was used to heat
the Aluminium base plate to a required temperature.Firstly,
the Apparatus was assembled and calibrated to room
temperature. The fins of required geometries were fixed on
the base plate and the base plate was heated to temperature
of 100°C and 120°C for two different set of readings for each
fin geometry. There were total of five different geometries
that were heated and tested. Thebaseplateandfinsattached
to it was placed within a box made outof WoodandAsbestos
to attain Steady State Heat Transfer. The Baseplate along
with the fins was then heated to 100°C for the first set of
readings. After the readings were noted down,theBaseplate
along with the fins was cooled through natural Convection.
The base plate along with the fins was again heated to 120°C
for the next set of readings. A correspondig reading was
taken for each fin with respect to the base plate temperature
at five different locations and the mean was taken. The
corresponding readings, for each fin geometry are
represented in the following tables
Table 1 Fin temperature Readings
S. NO. Fin Geometry
Base plate temperature
(Tb)
Mean fin temperature
(Tf)
Chamber temperature
(Tchamber)
1 Without Notch
101.45°C
120.8°C
92.32°C
108.34°C
51.2°C
58.8°C
2 Circular Notch
100°C
120.3°C
96.36°C
116.2°C
52.7°C
62.9°C
3 Triangular Notch
99.85°C
120.3°C
93.32°C
11.88°C
52.8°C
63.6°C
4 Square Notch
100.1°C
120°C
91.81°C
108.8°C
54.1°C
66.7°C
5 Rectangular Notch
100.05°C
119.95°C
92.06°C
109.1°C
52.9°C
60.8°C
6 Comb Profile
99.85°C
119.85°C
91.16°C
110.68°C
52.2°C
59.7°C
International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD31613 | Volume – 4 | Issue – 4 | May-June 2020 Page 1564
2.3.1. Various Parameters required to calculate Heat
Transfer Coefficient
2.3.1.1. Temperature of the whole body
T(body)=Tb+Tf /2 ,°C
2.3.1.2. Temperature of body and surrounding
temperature
∆ T= Tbody−Tchamber ,°C
2.3.1.3. Mean film temperature
Tmf=Tbody+Tchamber 2 ,°C
2.3.1.4. Coefficient of volume expansion
β=1/ Tmf
2.3.1.5. Grashof Number
Gr = gβ∆TL3
c/ Y2
L c= characteristic length of geometry,
m ߛߛ = kinematic viscosity of fluid,m2/s
g= Acceleration dure to gravity, m/s2
∆T= Temperature of the Body and surroundingtemperature
β = Grashof’s Number
2.3.1.6. Rayleigh number
Ra=GrPr
Pr=Prandtl number
2.3.1.7. Nusselt number
If 104<GrPr<109 then, Nu =0.59(GrPr)(1/4)
If 109<GrPr<1012 then, Nu =0.59(GrPr)(1/3)
2.3.1.8 Heat Transfer Coefficient
H= Nuk/Lc, W/m2k
3. RESULTS AND DISCUSSION
3.1. Graphical Representation of Results
h(w/m2k)
8
8.2
8.4
8.6
8.8
9
9.2
9.4
9.6
9.8
notch profile
Fig.No.5 Comparison of Heat Transfer Coefficient at 100 ℃℃℃℃ base temperature for various notch profiles
h(w/m2k)
8
8.5
9
9.5
10
10.5
notch profile
Fig.No.6 Comparison of Heat Transfer Coefficient at 120 ℃℃℃℃ base temperature for various notch profiles
International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD31613 | Volume – 4 | Issue – 4 | May-June 2020 Page 1565
Discussion
It is clearly visible from the above results table that the
geometry of the fin can have a considerable amount of
difference in the Heat Transfer Coefficient. We can say that
as the fin geometry changes, the Heat Transfer Coefficient
also changes. From various geometries which were put
under the test, the Comb shaped notch profile in the fin
tends to have maximum Heat Transfer Coefficient among all
the other geometrics of the fin.
4. CONCLUSIONS
It is proved that the heat transfer coefficient is highest for
the set of fins with comb profile (9.6290 W/m2K) at base
temperature 100℃ and (10.2232W/m2K) at base
temperature 120℃. This has been shown by the
experimental analysis. FromtheExperimental analysisithas
been observed that temperaturedistributionforthenotched
fins is more uniform than the fins without notch. It is
observed that the heat transfer coefficient varies with notch
geometry. As area removed from the fin at the air entry ends
of the fin, it provides chance to get greater amount of fresh
air in contact. From, economical point of view, along with
increasing Heat Transfer Coefficient. it saves thefinmaterial
and indirectly cost of the production. Along, with
Experimental analysis, numerical simulationmaybedefined
through CFD tool for predicting heat transfer phenomena
and temperature gradient along the finned area. Study can
be extended by analysis to be carried out with forced
convection and results can be predicted for different
Reynolds numbers. Further analysis can be carried out on
the basis of surface roughness and orientation of fins.
5. REFERENCES
[1] S. A. Nada, ‘Natural convection heat transfer in
horizontal and vertical closed narrow enclosures with
heated rectangular finned base plate’, J. Heat transfer
Vol. 116, pp 75-81.
[2] H. G. Yalcinet. Al, ‘Study of effect of clearance
parameters on the steady-state heat transfer’, ASEM
journal of heat transfer, Vol. 103, pp.616.623.
[3] S. S. Sane1, N. K. Sane2, G. V. Parishwad3,
‘Computational analysis of horizontal rectangular
notched fins arrays dissipating heat by natural
convection.’
[4] P. K. Nag, 2006, ‘Heat and mass transfer’, 2nd Edition,
Tata McGraw Hill Co. Page No.: 86-108 and 425-449.
[5] J. P. Holman, 2004, ‘Heat transfer- A particleapproach.’
SI units 2nd Edition, Tata McGraw Hill Co., Page
No.:156-168, 333352, and 459-500.
[6] El Hassan Ridouane and Antonio Campo, ‘Heattransfer
and pressure drop characteristics of laminar air flows
moving in parallel plate channel with transversehemi-
cylindrical cavities’, International journal of heat and
mass transfer, Vol. 50, September 2007.
[7] W. W. Lin and D. J. Lee, ‘second law analysis on a flat
plate fin array under cross-flow’, International
communications in heat and mass transfer, Vol. 27,
issue 2, February 2000.
[8] Gutavo Ledezma and Adrian Bejan, ‘heat sinks with
sloped plate fins in natural and forced convection’,
International Journal of heat and masstransfer,vol.39,
issue 9, June 1996.

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Effect of Different Fin Geometries on Heat Transfer Coefficient

  • 1. International Journal of Trend in Scientific Research and Development (IJTSRD) Volume 4 Issue 4, June 2020 Available Online: www.ijtsrd.com e-ISSN: 2456 – 6470 @ IJTSRD | Unique Paper ID – IJTSRD31613 | Volume – 4 | Issue – 4 | May-June 2020 Page 1562 Effect of Different Fin Geometries on Heat Transfer Coefficient Rohit, Kuldeep UG Student, Department of Mechanical Engineering, Dronacharya College of Engineering, Gurugram, Haryana, India ABSTRACT High rate of heat flow is the demand of number of engineering applications, heat exchangers used in process industries, economizersusedtoheat waterto boiler or activities like cooling of IC engines. Also, the removal of heat from integral circuit or exchange of heat between two fluids as in nuclear power plants many researchers contributed inenhancementofheattransferthrough various approaches. Increase in heat transfer rate and to derive is being done by using different techniques or by performing experiments as well previous literature mentioned the theory regarding heat transfer in such a way that it will increased by increasing area and heat transfer coefficient. In case of natural convection there is only scope for increasing heat transfer area, there extended surfaces i.e. fins are better option to it.Otheradvantageisincreasing turbulence with pitch therefore it enhances heat transfer. Study of heat transfer is possible through numerical experimental analysis. In case of numerical analysis, the results give’s heat flow pattern and but less accurate. Whereas experimental analysis gives accurate results but require setup,time and valid conditions. KEYWORDS: Conduction, Fins, Geometry, Heat Transfer Co-efficient, Natural Convection, Steady State Heat Transfer, Temperature How to cite this paper: Rohit | Kuldeep "Effect of Different Fin Geometries on Heat Transfer Coefficient" Published in International Journal of Trend in Scientific Research and Development(ijtsrd), ISSN: 2456-6470, Volume-4 | Issue-4, June 2020, pp.1562- 1565, URL: www.ijtsrd.com/papers/ijtsrd31613.pdf Copyright © 2020 by author(s) and International Journal ofTrendinScientific Research and Development Journal. This is an Open Access article distributed under the terms of the Creative CommonsAttribution License (CC BY 4.0) (http://creativecommons.org/licenses/by /4.0) 1. INTRODUCTION Actual convection heat transfer in a fluid layer confined in a closed enclosure with partitions like fins is encountered in a wide variety of engineering applications. Such as in power and automotive sectorswhereheatexchangers,economizers used to heat the feed water to boiler and the activities like cooling of internal combustion engine, also removal of heat from integrated circuitsintheelectroniccircuitsorexchange of heat between two fluids as inn nuclear power plants, passive cooling of electronic equipment such as compact power supplies, portable computers and telecommunications enclosures. In the design of electronic packages, there are strong incentives to mount as much electronic components as possible in a given enclosure. This leads to high power generation density and this may raise the temperature of the packages above the allowable limit. Therefore, there is need to increase heat transfer rate for working a device at designed at efficiency.Manyresearchers have been mentioned through their literature, heat transfer rate is increased by increasing heat transfer coefficientor by heat transfer area. In case of natural convection thereisonly scope for increasing heat transfer area by providing finned surfaces. The enhancement ratio ofheattransferdepends on the fin’s orientations and the geometric parameters of fin arrays. The most common configurations of using fin arrays in heat sinks involve horizontal or vertical surface plate to which fin arrays are attached. Specially designed finned surfaces called heat sink, which are commonly used in the cooling of electronic equipment and stationary engines needs optimized design with minimum material and maximum heat transfer from them. In the natural cooling of fins, the temperature drops along the fins exponentially and reaches the environment temperature at some length. But heat transfer from the area near the tip is low. It results in wastage of material for small heat transfer rate. Cutting this portion of fins, results in the complete elimination of heat transfer from that region. Also, the central portion of the fin flat becomes ineffective due to the fact that, already heated air comes in its contact. In this project the fin modified by removing the central fin portion by cutting a notch of different geometrical shapes and adding it at the arrays entrance on the two sides, where it is more effective and thereby keeping fin surface area same. 2. MATERIALS AND METHODOLGY 2.1. Materials The most important elements of the experimental set-up are the set of fins and a Base Plate on which these fins are mounted. Base plate and fins with different notch geometries are made up of aluminum. Selection criteria for a aluminum is based on thermal conductivity, density, cost and from manufacturing point of view. The used Aluminium has thermal conductivityof237.4 w/mk and density 2712 kg/m3. S.NO. Tests Actual Specified UOM 1. SUCON 0.3728 0 % 2. MAGANESE 0.1982 0 % 3. NICKEL 0.0104 0 % 4. CROMIUM 0.0176 0 % 5. COPPER 0.2201 0 % 6. TITANUM 0.0092 0 % 7. ALUMINIUM 97.450 0 % 8. FE 1.3023 0 % 9. MG 0.0926 0 % Fig.No.1: Composition of Aluminium used for Baseplate and Fins IJTSRD31613
  • 2. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD31613 | Volume – 4 | Issue – 4 | May-June 2020 Page 1563 Fig.No.2 Aluminium Base Plate Fig.No.3 Fins with different Geometry Fig.No.4 Apparatus of the Experiment 2.2 Fabrication Sheets of Aluminum are purchased directly from the shops available in the market. The sheets required for this purpose are of thickness 2mm which are available in that thickness. All the sets of fins and the base plate are cut and machined in the workshop. Fins with rectangular notch are cut very easilywiththehacksawasthe machining of aluminum is very easy. The fins with circular notches are cut with the help of milling machine. Fins with triangular and trapezoidal notches are also cut withthehelp of hacksaw manually. One set of fins include five number of fin flats. There are five such sets of fins, for the fins without notch, fins with circular notch, fins with rectangular notch, fins with triangular notch, and fins with trapezoidal notch. The dimensions the notches selectedastomaintaina surface area in and the depth of notch constant for all notched fins. These three fin flats are mounted on one base. Thus a total number of fin flats fabricated are 18. Only a single base plate is fabricated with notches and thesamebaseplateisused for all the sets of fins. The dimensions of base plate are [200x200] mm the three fins are placed on the base plate in the slots made on the base plate at equal intervals. The distance between the slots thus obtained is 20 mm. Base plates and the set of three fins were assembled. 2.3 Method The Apparatus consisted of Base frame to inscribe various equipments such as Dimmerstattoregulate the voltage supply. Multi-point temperature indicator with digital display in terms of degree Celsius. J-type thermocouple were used to measure the temperature at tip of the fins. A heater of 600 Watt capacity was used to heat the Aluminium base plate to a required temperature.Firstly, the Apparatus was assembled and calibrated to room temperature. The fins of required geometries were fixed on the base plate and the base plate was heated to temperature of 100°C and 120°C for two different set of readings for each fin geometry. There were total of five different geometries that were heated and tested. Thebaseplateandfinsattached to it was placed within a box made outof WoodandAsbestos to attain Steady State Heat Transfer. The Baseplate along with the fins was then heated to 100°C for the first set of readings. After the readings were noted down,theBaseplate along with the fins was cooled through natural Convection. The base plate along with the fins was again heated to 120°C for the next set of readings. A correspondig reading was taken for each fin with respect to the base plate temperature at five different locations and the mean was taken. The corresponding readings, for each fin geometry are represented in the following tables Table 1 Fin temperature Readings S. NO. Fin Geometry Base plate temperature (Tb) Mean fin temperature (Tf) Chamber temperature (Tchamber) 1 Without Notch 101.45°C 120.8°C 92.32°C 108.34°C 51.2°C 58.8°C 2 Circular Notch 100°C 120.3°C 96.36°C 116.2°C 52.7°C 62.9°C 3 Triangular Notch 99.85°C 120.3°C 93.32°C 11.88°C 52.8°C 63.6°C 4 Square Notch 100.1°C 120°C 91.81°C 108.8°C 54.1°C 66.7°C 5 Rectangular Notch 100.05°C 119.95°C 92.06°C 109.1°C 52.9°C 60.8°C 6 Comb Profile 99.85°C 119.85°C 91.16°C 110.68°C 52.2°C 59.7°C
  • 3. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD31613 | Volume – 4 | Issue – 4 | May-June 2020 Page 1564 2.3.1. Various Parameters required to calculate Heat Transfer Coefficient 2.3.1.1. Temperature of the whole body T(body)=Tb+Tf /2 ,°C 2.3.1.2. Temperature of body and surrounding temperature ∆ T= Tbody−Tchamber ,°C 2.3.1.3. Mean film temperature Tmf=Tbody+Tchamber 2 ,°C 2.3.1.4. Coefficient of volume expansion β=1/ Tmf 2.3.1.5. Grashof Number Gr = gβ∆TL3 c/ Y2 L c= characteristic length of geometry, m ߛߛ = kinematic viscosity of fluid,m2/s g= Acceleration dure to gravity, m/s2 ∆T= Temperature of the Body and surroundingtemperature β = Grashof’s Number 2.3.1.6. Rayleigh number Ra=GrPr Pr=Prandtl number 2.3.1.7. Nusselt number If 104<GrPr<109 then, Nu =0.59(GrPr)(1/4) If 109<GrPr<1012 then, Nu =0.59(GrPr)(1/3) 2.3.1.8 Heat Transfer Coefficient H= Nuk/Lc, W/m2k 3. RESULTS AND DISCUSSION 3.1. Graphical Representation of Results h(w/m2k) 8 8.2 8.4 8.6 8.8 9 9.2 9.4 9.6 9.8 notch profile Fig.No.5 Comparison of Heat Transfer Coefficient at 100 ℃℃℃℃ base temperature for various notch profiles h(w/m2k) 8 8.5 9 9.5 10 10.5 notch profile Fig.No.6 Comparison of Heat Transfer Coefficient at 120 ℃℃℃℃ base temperature for various notch profiles
  • 4. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD31613 | Volume – 4 | Issue – 4 | May-June 2020 Page 1565 Discussion It is clearly visible from the above results table that the geometry of the fin can have a considerable amount of difference in the Heat Transfer Coefficient. We can say that as the fin geometry changes, the Heat Transfer Coefficient also changes. From various geometries which were put under the test, the Comb shaped notch profile in the fin tends to have maximum Heat Transfer Coefficient among all the other geometrics of the fin. 4. CONCLUSIONS It is proved that the heat transfer coefficient is highest for the set of fins with comb profile (9.6290 W/m2K) at base temperature 100℃ and (10.2232W/m2K) at base temperature 120℃. This has been shown by the experimental analysis. FromtheExperimental analysisithas been observed that temperaturedistributionforthenotched fins is more uniform than the fins without notch. It is observed that the heat transfer coefficient varies with notch geometry. As area removed from the fin at the air entry ends of the fin, it provides chance to get greater amount of fresh air in contact. From, economical point of view, along with increasing Heat Transfer Coefficient. it saves thefinmaterial and indirectly cost of the production. Along, with Experimental analysis, numerical simulationmaybedefined through CFD tool for predicting heat transfer phenomena and temperature gradient along the finned area. Study can be extended by analysis to be carried out with forced convection and results can be predicted for different Reynolds numbers. Further analysis can be carried out on the basis of surface roughness and orientation of fins. 5. REFERENCES [1] S. A. Nada, ‘Natural convection heat transfer in horizontal and vertical closed narrow enclosures with heated rectangular finned base plate’, J. Heat transfer Vol. 116, pp 75-81. [2] H. G. Yalcinet. Al, ‘Study of effect of clearance parameters on the steady-state heat transfer’, ASEM journal of heat transfer, Vol. 103, pp.616.623. [3] S. S. Sane1, N. K. Sane2, G. V. Parishwad3, ‘Computational analysis of horizontal rectangular notched fins arrays dissipating heat by natural convection.’ [4] P. K. Nag, 2006, ‘Heat and mass transfer’, 2nd Edition, Tata McGraw Hill Co. Page No.: 86-108 and 425-449. [5] J. P. Holman, 2004, ‘Heat transfer- A particleapproach.’ SI units 2nd Edition, Tata McGraw Hill Co., Page No.:156-168, 333352, and 459-500. [6] El Hassan Ridouane and Antonio Campo, ‘Heattransfer and pressure drop characteristics of laminar air flows moving in parallel plate channel with transversehemi- cylindrical cavities’, International journal of heat and mass transfer, Vol. 50, September 2007. [7] W. W. Lin and D. J. Lee, ‘second law analysis on a flat plate fin array under cross-flow’, International communications in heat and mass transfer, Vol. 27, issue 2, February 2000. [8] Gutavo Ledezma and Adrian Bejan, ‘heat sinks with sloped plate fins in natural and forced convection’, International Journal of heat and masstransfer,vol.39, issue 9, June 1996.