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Balram Deokar.et. al. Int. Journal of Engineering Research and Applications www.ijera.com
ISSN: 2248-9622, Vol. 6, Issue 3, (Part - 4) March 2016, pp.01-04
www.ijera.com 1|P a g e
Analytical and Experimental analysis ofthermal characteristics
throughTriangular microchannel heat sink
Balram Deokar*, Dattatraya Nalawade **,Mahesh Jagadale***
*(M.E. Student, Department of Mechanical Engineering, G. S. Moze College of Engineering, Balewadi, Pune
(M.S.) India).
** (Assistant Professor, Department of Mechanical Engineering, Vishwakarma Institute of Information
Technology , Kondwa (BK), Pune (M.S.) India ).
*** (Assistant Professor, Department of Mechanical Engineering, G. S. Moze College of Engineering,
Balewadi, Pune (M.S.) India).
ABSTRACT
Microscale heat transfer technique is widely intended for best cooling applications in electronic devices as high
heat transfer coefficients are achieved in microscale convection. In present study, analysis of thermal
characteristics has been carried out by analytical calculations along with experimental investigation for a straight
microchannel heat sink of equilateral triangular cross section of 173.21 μm hydraulic diameter with distilled
water as the working fluid. Designed Heater input watts and Reynolds number based on flow rate are varied for
optimized microchannel geometry. Experimental analysis is carried out under constant heat flux condition. The
microchannels are produced on highly accurate micro wire cut EDM. The Reynolds number is varied from 100
to 700. The major intension for this work is to enhance heat transfer coefficient and minimize pressure drop
across microchannel. The Reynolds number, temperature distribution, pressure distribution, heat transfer
coefficient, hydrodynamic entrance length, thermal entrance length, equivalent thermal resistances parameters
are calculated for microchannel heat sink performance analysis. The results of analytical calculations are verified
with experimental investigation. It is found that heat transfer coefficient and pressure drop increases with
increase in Reynolds numbers and decrease in microchannel heat sink hydraulic diameter. Also channel length is
directly proportional to temperature rise.
Keywords-Heat transfer coefficient, Laminar flow, Pressure drop,Reynolds number&Triangular Micro channel
Heat sink
I. INTRODUCTION
Most of thermally operated equipments are
designed for high heat transfer rates. The heat
transfer enhancement with minimum pressure drop,
minimum pumping power are goals of best heat
transfer equipment design. The microchannel heat
exchangers are used for heat recovery and energy
interactions. The first innovation for microchannel is
studied by Tuckerman and Pease [1]. They are
considered as father of microchannel heat sink
which is used for high heat transfer applications in
electronics devices cooling.They have achieved high
heat transfer coefficient in single and two phase
flows field. Also they observed that heat transfer
coefficient is inversely proportional to hydraulic
diameter.
The microchannel heat sinks are capable for
disposing high heat flux. It is become popular
within fewer time frames for cooling applications for
electronics devices. The high surface to volume ratio
has proven the use for high heat transfer
applications. The microchannel heat sink geometries
which are widely used for research and applications
are rectangular, circular, triangular and trapezoidal.
Triangular microchannels are become popular
because for equal heat transfer coefficient they
require less volume corresponds to rectangular
channel and they are easy to analysis than
trapezoidal cross section. The geometrical
parameters are affecting on performance of heat
sink.
P. Wibulswas [2] has implemented
numerical solution method for rectangular duct,
right-angled isosceles and equilateral triangular
geometry with thermally developed and developing
boundary conditions. He has demonstrated method
for various aspect ratio having constant wall
temperature and constant heat flux conditions. He
used 1*2 in2
straight rectangular duct with 3ft. length
for analysis. Nusselt numbers which is obtained in
this analysis was depends on channel aspect ratio
and dimensionless axial position. The
simultaneously developing velocity profile gives
higher Nusselt number as compared with developed
velocity profile. In order to design best microchannel
heat exchanger increase number of channel of short
length rather than few number of channels with more
length .He has developed no of relations for Nusselt
numbers which are good agreement with other
RESEARCH ARTICLE OPEN ACCESS
Balram Deokar.et. al. Int. Journal of Engineering Research and Applications www.ijera.com
ISSN: 2248-9622, Vol. 6, Issue 3, (Part - 4) March 2016, pp.01-04
www.ijera.com 2|P a g e
equivalent researches.Kandlikar and Upadhye [3]
has done investigation on optimization of heat sink
geometry for constant heat flux and constant wall
temperature conditions in order minimizes pressure
drop across the channel. They have presented
numerical calculations for single phase flow for
laminar and turbulent boundary conditions. They
have worked for optimization of cooling system for
silicon microchannels with water. The plain
rectangular microchannels with 300 μm width single
pass arrangement which are engraved on 10 mm*10
mm silicon chip are used for analysis with high heat
flux 3 MW/m2
with maximum chip temperature 360
K. They have investigated that number of channels
for optimized geometry are from 68 to 90. They
have used split flow arrangement for analysis
because the pressure drop which we get for loner
channel is higher as compared to short length
channels and large mass flow rate is required to
maintain designed temperature rise across the
microchannel Thus it is concluded that roadmap of
microchannels heat sink investigation can be useful
for high heat dissipation in short area in
applicationsaircraft, automotive sector.Konstantinos,
Yannis, Steryios, Dimitris [4] have done numerical
investigation on triangular andtrapezoidal cross
section geometry with long channels having acute
angle 54.74° which is produced from chemical
etching of silicon wafers. They have evaluated
linearized shakhov model with impartment of
Maxwell boundary conditions for combined gas
flow. It is found out dimensionless flow rate due to
pressure drop and temperature drop which is used
for experimental analysis for validation.
Lee, Garimella and Liu [5] have conducted
experimental analysis in single phase flow on
rectangular microchannels. Straight parallel 10 no’s
of rectangular microchannels width 194 μm to 534
μm having depth 5 times for respective width are
tested with deionized water for experimental
investigation. The Reynolds numbers is varied from
300 to 3500 for carrying out experimentation. They
have used predictive and fluid continuum approach
for their analysis. Also they have collectively put
conventional correlations from literature for
microchannel heat transfer investigation. They
compared their numerical predicted calculated
results with experimental analysis results and it is
within 5% limit. Jiann Cherng [6] has
experimentally investigated pressure drop and heat
transfer coefficient for silicon triangular
microchannels in laminar flow with Reynolds
number less than 100. As per experimental
investigation Nusselt number is nearly directly
proportional to Reynolds number and high
temperature gradient is observed between input and
output plenum. The empirical correlations obtained
results are compared with experimental results and
they are with 15%.
The major core about this research is to optimize
number of microchannels for maximize heat transfer
coefficient and minimize pressure drop across the
channel. The laminar flow is best suitable for
required results. The analytical calculations along
with same designed experimental analysis which
system is best useful for practical implementation.
II. THEROTICAL ANALYSIS
The Hydraulic diameter through
microchannel will decide Nano and microchannel.
The heattransfer coefficient is depends on Nusselt
number.As microchannel are defined as per 10 to
200 μm hydraulic diameter. The microchannel chip
having dimension 27.5*19.5 mm is used for analysis
in this study. Since equilateral section is having
maximum surface to volume ratio in comparison of
triangular section so geometry is chosen as
equilateral section. Standard manufacturing process
capability Constrains will useful for sectional area
determination. The best optimum tooling and heat
transfer area constrain channel width is obtained as
300 μm. The hydraulic diameter for optimum width
and cross section is 173.2 μm. The number of
channels is varied from 0-50. The cross functional
design is created as variation of number of channel
and flow rate. The Reynolds number is varied from
0-2000 which is equivalent to laminar flow range.
The best results for lowest pressure drop and
maximum heat transfer is obtained from 100-700
Reynolds number. So it is taken as golden mean for
optimum results. The effect of thermal resistance is
decrease the convective heat transfer. The genetic
algorithm is used with two objective functions as
maximization of heat transfer coefficient and
minimization of thermal resistance across the
channel. The optimum numbers of channels are
obtained as 21. This is optimum for heat transfer rate
maximization along with minimization of pressure
drop across the channel and minimization of thermal
resistance for convective heat transfer. The same
designed problem is experimentally investigated and
results are compared and they are in good agreement
with some reference study.
III. EXPERIMENTAL SET UP
The schematic of experimental facility used
for analysis is shown in figure 1. The core section is
microchannel heat sink test module. The data logger
system consists of pressure transducer, thermocouple
and input watts for accurate measurement. Peristaltic
pump with different tubing will provide accurate
flow rate along with sufficient pressure. The
cartridge heater is used for uniform heating of
copper microchannel heat test section.
Balram Deokar.et. al. Int. Journal of Engineering Research and Applications www.ijera.com
ISSN: 2248-9622, Vol. 6, Issue 3, (Part - 4) March 2016, pp.01-04
www.ijera.com 3|P a g e
Water tank at bottom Stores distilled water is used
for microchannel experimental investigation. The
micro filter removes contaminations and other
particles from water through microporous
membrane. The pore size of membrane used by us
ranged from 1-10 μm. It is used prior to pump and
microchannel system because it will saves pump
tubing and system along with it will avoids clogging
of flow in microchannel manifold due to
contaminations
Figure1-Schematic of experimental facility
The pump provides require water as per
required flow rate. The digital peristaltic pump
provides different flow by adjusting speed and
tubing sizes. We have used peristaltic digital
variable speed provides flow rate from 0.06-3400
ml/min having speed control accuracy ± 0.25 %. The
water flows through microchannel heat sink test
module. The base core section of PTFE material will
ensure leak proof and high temperature
sustainability. The microchannels are engraved on
chip 27.5*19.5 mm chip of electrolytic copper which
is having maximum thermal conductivity. The
optimized 21 number of microchannels are straight
manufactured with highly accurate wire cut EDM
with triangular micro wire with 0.3 mm length with
equilateral section. Transparent acrylic cover at top
will show water flow through manifold and
microchannels.
Figure 2 - Test section manifold
Micro plate heater is mounted at bottom of
microchannel chip for uniform heating. The
thermocouple sensors are used to measure the
temperature at various locations at Inlet and outlet
along with heater base. The accurate positioning and
sensor length will decide accurate reading. The K
type thermocouples are used for measurement of
temperature 0.02resolution over -200 to 1200 ° C
range. Pressure sensor measures 0-1000 Psi
differential Pressure. The sensors get connected with
data logger for accurate measurement. The logger
system is USB portable and having digital display.
The readings are taken when steady state is
achieved. The heater thermocouple will create void,
thermal grease can be used for perfect ensure of
contacts. The voltage current supplied to heater can
be recorded on same data logger. The readings are
taken for constant heat flux also the Reynolds
number is varied by equivalent varying flow rate.
The theoretical designed conditions are taken for
experimental analysis.
IV. RESULT AND DISCUSSION
The experimental analysis is conducted and
graphs are plotted for variation of heat transfer
coefficient with respect to variation of Reynolds
number along with pressure difference across
channel with respect to variations of same Reynolds
number. The friction factor and thermal resistance
across channel are theoretically calculated.
Figure 3 - Reynolds number versus Heat transfer
coefficient.
It can be observed thatconvective heat
transfer coefficient increases with increase in
Reynolds numbers. The radioactive heat losses and
conduction through grease surface will leads to
difference in experimental investigation and
theoretical calculations. We have compared
theoretical results with Wibulswaswhich is draw by
using correlation given in journal paper.
Balram Deokar.et. al. Int. Journal of Engineering Research and Applications www.ijera.com
ISSN: 2248-9622, Vol. 6, Issue 3, (Part - 4) March 2016, pp.01-04
www.ijera.com 4|P a g e
Figure 4 - Reynolds number versus Pressure Drop
Also it can be observed that with increase
in Reynolds number,friction factor across the
channel increases. It will affect cumulatively to
increase the pressure drop across the channel. Since
the entrance effect and other sudden expansion
losses the effective pressure drop across channel
increases as compared to theoretical pressure drop.
We have compared theoretical results with
Wibulswaswhich is draw by using correlation given
in journal paper.
V. CONCLUSIONS
1. It is concluded that microchannel heat Sink
are media which is best useful to dissipate
large amount of heat within small surface
area.
2. The optimum results for heat transfer
enhancement with minimum pressure drop are
observed in Reynolds number 300-650.
3. It is found that experimentally investigated
pressure drop across microchannel is higher
than theoretically predicted calculation
4. Heat transfer coefficient and Reynolds
number which is investigated experimentally
are slightly less than theoretically predicated
analysis but they are in good agreement with
correlations in Journal paper.
5. The flow rate and temperature drop across the
microchannel are inversely proportional to
each other for constant input watts.
6. In order to maximize heat transfer
coefficient, minimize pumping power,
minimize pressure drop, minimize friction
factor, minimize entropy generation, there is a
need to analyse simultaneous effects of
geometry dimension, number of micro
channels, aspect ratio, fluid properties, and
hydrodynamic parameters along with thermal
properties of sink material.
REFERENCES
[1] Tuckerman, David B., and R. F. W. Pease.
"High-performance heat sinking for VLSI."
Electron Device Letters, IEEE 2, no. 5
(1981): 126-129.
[2] Wibulswas, P. "Laminar-flow heat-transfer
in non-circular ducts." PhD diss.,
University of London, 1966.
[3] Kandlikar, Satish G., and Harshal R.
Upadhye. "Extending the heat flux limit
with enhanced microchannels in direct
single-phase cooling of computer chips." In
Semiconductor Thermal Measurement and
Management Symposium, 2005 IEEE
Twenty First Annual IEEE, pp. 8-15. IEEE,
2005.
[4] Ritos, Konstantinos, Yiannis
Lihnaropoulos, Stergios Naris, and
Dimitris Valougeorgis. "Pressure-and
temperature-driven flow through triangular
and trapezoidal microchannels." Heat
Transfer Engineering 32, no. 13-14 (2011):
1101-1107.
[5] Lee, Poh-Seng, Suresh V. Garimella, and
Dong Liu. "Investigation of heat transfer in
rectangular microchannels." International
Journal of Heat and Mass Transfer 48, no. 9
(2005): 1688-1704.
[6] Chu, Jiann-Cherng, Jyh-Tong Teng, and
Ralph Greif. "Heat transfer for water flow
in triangular silicon microchannels."
Journal of Thermal science and Technology
3, no. 3 (2008): 410-420.

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Analytical and Experimental analysis ofthermal characteristics throughTriangular microchannel heat sink

  • 1. Balram Deokar.et. al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN: 2248-9622, Vol. 6, Issue 3, (Part - 4) March 2016, pp.01-04 www.ijera.com 1|P a g e Analytical and Experimental analysis ofthermal characteristics throughTriangular microchannel heat sink Balram Deokar*, Dattatraya Nalawade **,Mahesh Jagadale*** *(M.E. Student, Department of Mechanical Engineering, G. S. Moze College of Engineering, Balewadi, Pune (M.S.) India). ** (Assistant Professor, Department of Mechanical Engineering, Vishwakarma Institute of Information Technology , Kondwa (BK), Pune (M.S.) India ). *** (Assistant Professor, Department of Mechanical Engineering, G. S. Moze College of Engineering, Balewadi, Pune (M.S.) India). ABSTRACT Microscale heat transfer technique is widely intended for best cooling applications in electronic devices as high heat transfer coefficients are achieved in microscale convection. In present study, analysis of thermal characteristics has been carried out by analytical calculations along with experimental investigation for a straight microchannel heat sink of equilateral triangular cross section of 173.21 μm hydraulic diameter with distilled water as the working fluid. Designed Heater input watts and Reynolds number based on flow rate are varied for optimized microchannel geometry. Experimental analysis is carried out under constant heat flux condition. The microchannels are produced on highly accurate micro wire cut EDM. The Reynolds number is varied from 100 to 700. The major intension for this work is to enhance heat transfer coefficient and minimize pressure drop across microchannel. The Reynolds number, temperature distribution, pressure distribution, heat transfer coefficient, hydrodynamic entrance length, thermal entrance length, equivalent thermal resistances parameters are calculated for microchannel heat sink performance analysis. The results of analytical calculations are verified with experimental investigation. It is found that heat transfer coefficient and pressure drop increases with increase in Reynolds numbers and decrease in microchannel heat sink hydraulic diameter. Also channel length is directly proportional to temperature rise. Keywords-Heat transfer coefficient, Laminar flow, Pressure drop,Reynolds number&Triangular Micro channel Heat sink I. INTRODUCTION Most of thermally operated equipments are designed for high heat transfer rates. The heat transfer enhancement with minimum pressure drop, minimum pumping power are goals of best heat transfer equipment design. The microchannel heat exchangers are used for heat recovery and energy interactions. The first innovation for microchannel is studied by Tuckerman and Pease [1]. They are considered as father of microchannel heat sink which is used for high heat transfer applications in electronics devices cooling.They have achieved high heat transfer coefficient in single and two phase flows field. Also they observed that heat transfer coefficient is inversely proportional to hydraulic diameter. The microchannel heat sinks are capable for disposing high heat flux. It is become popular within fewer time frames for cooling applications for electronics devices. The high surface to volume ratio has proven the use for high heat transfer applications. The microchannel heat sink geometries which are widely used for research and applications are rectangular, circular, triangular and trapezoidal. Triangular microchannels are become popular because for equal heat transfer coefficient they require less volume corresponds to rectangular channel and they are easy to analysis than trapezoidal cross section. The geometrical parameters are affecting on performance of heat sink. P. Wibulswas [2] has implemented numerical solution method for rectangular duct, right-angled isosceles and equilateral triangular geometry with thermally developed and developing boundary conditions. He has demonstrated method for various aspect ratio having constant wall temperature and constant heat flux conditions. He used 1*2 in2 straight rectangular duct with 3ft. length for analysis. Nusselt numbers which is obtained in this analysis was depends on channel aspect ratio and dimensionless axial position. The simultaneously developing velocity profile gives higher Nusselt number as compared with developed velocity profile. In order to design best microchannel heat exchanger increase number of channel of short length rather than few number of channels with more length .He has developed no of relations for Nusselt numbers which are good agreement with other RESEARCH ARTICLE OPEN ACCESS
  • 2. Balram Deokar.et. al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN: 2248-9622, Vol. 6, Issue 3, (Part - 4) March 2016, pp.01-04 www.ijera.com 2|P a g e equivalent researches.Kandlikar and Upadhye [3] has done investigation on optimization of heat sink geometry for constant heat flux and constant wall temperature conditions in order minimizes pressure drop across the channel. They have presented numerical calculations for single phase flow for laminar and turbulent boundary conditions. They have worked for optimization of cooling system for silicon microchannels with water. The plain rectangular microchannels with 300 μm width single pass arrangement which are engraved on 10 mm*10 mm silicon chip are used for analysis with high heat flux 3 MW/m2 with maximum chip temperature 360 K. They have investigated that number of channels for optimized geometry are from 68 to 90. They have used split flow arrangement for analysis because the pressure drop which we get for loner channel is higher as compared to short length channels and large mass flow rate is required to maintain designed temperature rise across the microchannel Thus it is concluded that roadmap of microchannels heat sink investigation can be useful for high heat dissipation in short area in applicationsaircraft, automotive sector.Konstantinos, Yannis, Steryios, Dimitris [4] have done numerical investigation on triangular andtrapezoidal cross section geometry with long channels having acute angle 54.74° which is produced from chemical etching of silicon wafers. They have evaluated linearized shakhov model with impartment of Maxwell boundary conditions for combined gas flow. It is found out dimensionless flow rate due to pressure drop and temperature drop which is used for experimental analysis for validation. Lee, Garimella and Liu [5] have conducted experimental analysis in single phase flow on rectangular microchannels. Straight parallel 10 no’s of rectangular microchannels width 194 μm to 534 μm having depth 5 times for respective width are tested with deionized water for experimental investigation. The Reynolds numbers is varied from 300 to 3500 for carrying out experimentation. They have used predictive and fluid continuum approach for their analysis. Also they have collectively put conventional correlations from literature for microchannel heat transfer investigation. They compared their numerical predicted calculated results with experimental analysis results and it is within 5% limit. Jiann Cherng [6] has experimentally investigated pressure drop and heat transfer coefficient for silicon triangular microchannels in laminar flow with Reynolds number less than 100. As per experimental investigation Nusselt number is nearly directly proportional to Reynolds number and high temperature gradient is observed between input and output plenum. The empirical correlations obtained results are compared with experimental results and they are with 15%. The major core about this research is to optimize number of microchannels for maximize heat transfer coefficient and minimize pressure drop across the channel. The laminar flow is best suitable for required results. The analytical calculations along with same designed experimental analysis which system is best useful for practical implementation. II. THEROTICAL ANALYSIS The Hydraulic diameter through microchannel will decide Nano and microchannel. The heattransfer coefficient is depends on Nusselt number.As microchannel are defined as per 10 to 200 μm hydraulic diameter. The microchannel chip having dimension 27.5*19.5 mm is used for analysis in this study. Since equilateral section is having maximum surface to volume ratio in comparison of triangular section so geometry is chosen as equilateral section. Standard manufacturing process capability Constrains will useful for sectional area determination. The best optimum tooling and heat transfer area constrain channel width is obtained as 300 μm. The hydraulic diameter for optimum width and cross section is 173.2 μm. The number of channels is varied from 0-50. The cross functional design is created as variation of number of channel and flow rate. The Reynolds number is varied from 0-2000 which is equivalent to laminar flow range. The best results for lowest pressure drop and maximum heat transfer is obtained from 100-700 Reynolds number. So it is taken as golden mean for optimum results. The effect of thermal resistance is decrease the convective heat transfer. The genetic algorithm is used with two objective functions as maximization of heat transfer coefficient and minimization of thermal resistance across the channel. The optimum numbers of channels are obtained as 21. This is optimum for heat transfer rate maximization along with minimization of pressure drop across the channel and minimization of thermal resistance for convective heat transfer. The same designed problem is experimentally investigated and results are compared and they are in good agreement with some reference study. III. EXPERIMENTAL SET UP The schematic of experimental facility used for analysis is shown in figure 1. The core section is microchannel heat sink test module. The data logger system consists of pressure transducer, thermocouple and input watts for accurate measurement. Peristaltic pump with different tubing will provide accurate flow rate along with sufficient pressure. The cartridge heater is used for uniform heating of copper microchannel heat test section.
  • 3. Balram Deokar.et. al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN: 2248-9622, Vol. 6, Issue 3, (Part - 4) March 2016, pp.01-04 www.ijera.com 3|P a g e Water tank at bottom Stores distilled water is used for microchannel experimental investigation. The micro filter removes contaminations and other particles from water through microporous membrane. The pore size of membrane used by us ranged from 1-10 μm. It is used prior to pump and microchannel system because it will saves pump tubing and system along with it will avoids clogging of flow in microchannel manifold due to contaminations Figure1-Schematic of experimental facility The pump provides require water as per required flow rate. The digital peristaltic pump provides different flow by adjusting speed and tubing sizes. We have used peristaltic digital variable speed provides flow rate from 0.06-3400 ml/min having speed control accuracy ± 0.25 %. The water flows through microchannel heat sink test module. The base core section of PTFE material will ensure leak proof and high temperature sustainability. The microchannels are engraved on chip 27.5*19.5 mm chip of electrolytic copper which is having maximum thermal conductivity. The optimized 21 number of microchannels are straight manufactured with highly accurate wire cut EDM with triangular micro wire with 0.3 mm length with equilateral section. Transparent acrylic cover at top will show water flow through manifold and microchannels. Figure 2 - Test section manifold Micro plate heater is mounted at bottom of microchannel chip for uniform heating. The thermocouple sensors are used to measure the temperature at various locations at Inlet and outlet along with heater base. The accurate positioning and sensor length will decide accurate reading. The K type thermocouples are used for measurement of temperature 0.02resolution over -200 to 1200 ° C range. Pressure sensor measures 0-1000 Psi differential Pressure. The sensors get connected with data logger for accurate measurement. The logger system is USB portable and having digital display. The readings are taken when steady state is achieved. The heater thermocouple will create void, thermal grease can be used for perfect ensure of contacts. The voltage current supplied to heater can be recorded on same data logger. The readings are taken for constant heat flux also the Reynolds number is varied by equivalent varying flow rate. The theoretical designed conditions are taken for experimental analysis. IV. RESULT AND DISCUSSION The experimental analysis is conducted and graphs are plotted for variation of heat transfer coefficient with respect to variation of Reynolds number along with pressure difference across channel with respect to variations of same Reynolds number. The friction factor and thermal resistance across channel are theoretically calculated. Figure 3 - Reynolds number versus Heat transfer coefficient. It can be observed thatconvective heat transfer coefficient increases with increase in Reynolds numbers. The radioactive heat losses and conduction through grease surface will leads to difference in experimental investigation and theoretical calculations. We have compared theoretical results with Wibulswaswhich is draw by using correlation given in journal paper.
  • 4. Balram Deokar.et. al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN: 2248-9622, Vol. 6, Issue 3, (Part - 4) March 2016, pp.01-04 www.ijera.com 4|P a g e Figure 4 - Reynolds number versus Pressure Drop Also it can be observed that with increase in Reynolds number,friction factor across the channel increases. It will affect cumulatively to increase the pressure drop across the channel. Since the entrance effect and other sudden expansion losses the effective pressure drop across channel increases as compared to theoretical pressure drop. We have compared theoretical results with Wibulswaswhich is draw by using correlation given in journal paper. V. CONCLUSIONS 1. It is concluded that microchannel heat Sink are media which is best useful to dissipate large amount of heat within small surface area. 2. The optimum results for heat transfer enhancement with minimum pressure drop are observed in Reynolds number 300-650. 3. It is found that experimentally investigated pressure drop across microchannel is higher than theoretically predicted calculation 4. Heat transfer coefficient and Reynolds number which is investigated experimentally are slightly less than theoretically predicated analysis but they are in good agreement with correlations in Journal paper. 5. The flow rate and temperature drop across the microchannel are inversely proportional to each other for constant input watts. 6. In order to maximize heat transfer coefficient, minimize pumping power, minimize pressure drop, minimize friction factor, minimize entropy generation, there is a need to analyse simultaneous effects of geometry dimension, number of micro channels, aspect ratio, fluid properties, and hydrodynamic parameters along with thermal properties of sink material. REFERENCES [1] Tuckerman, David B., and R. F. W. Pease. "High-performance heat sinking for VLSI." Electron Device Letters, IEEE 2, no. 5 (1981): 126-129. [2] Wibulswas, P. "Laminar-flow heat-transfer in non-circular ducts." PhD diss., University of London, 1966. [3] Kandlikar, Satish G., and Harshal R. Upadhye. "Extending the heat flux limit with enhanced microchannels in direct single-phase cooling of computer chips." In Semiconductor Thermal Measurement and Management Symposium, 2005 IEEE Twenty First Annual IEEE, pp. 8-15. IEEE, 2005. [4] Ritos, Konstantinos, Yiannis Lihnaropoulos, Stergios Naris, and Dimitris Valougeorgis. "Pressure-and temperature-driven flow through triangular and trapezoidal microchannels." Heat Transfer Engineering 32, no. 13-14 (2011): 1101-1107. [5] Lee, Poh-Seng, Suresh V. Garimella, and Dong Liu. "Investigation of heat transfer in rectangular microchannels." International Journal of Heat and Mass Transfer 48, no. 9 (2005): 1688-1704. [6] Chu, Jiann-Cherng, Jyh-Tong Teng, and Ralph Greif. "Heat transfer for water flow in triangular silicon microchannels." Journal of Thermal science and Technology 3, no. 3 (2008): 410-420.