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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 30
Review of Convection and Magnetohydrodynamic Mixed Convection
Heat Transfer Enhancement
Mayur Sakhare1, Rohit Yadav2
1,2Vellore Institute of Technology
Dept. of Mechanical Engineering, Vellore Institute of Technology, Tamil Nadu, India
---------------------------------------------------------------------***----------------------------------------------------------------------
Abstract – In this paper, we discuss about the recent research
trends in heat transfer enhancement in convection mode by
using two kinds of techniques: killing thermal boundary layer
and using magnetohydrodynamic (MHD) mixed convection.
We first give a glance of various techniques utilized by the
researchers to properly utilize energy and heat in varying
applications. Then we focus our study in heat transfer
enhancement only. The entire discussion is divided into two
categories based on the kinds of heat transferenhancementas
mentioned. We have presented the comparative study of
related investigations along with the conclusion from them in
the most understandable manner. This articleopensapathfor
inclusive understanding of the phenomenon for future study,
design and development of devices inconvectionheattransfer.
Key Words: heat transfer, convection,
magnetohydrodynamics
1. INTRODUCTION
Heat transfer is required for the exchangeofthermal energy.
Heat exchangers are used in several applications including
cooling the engines of automobiles, in refrigerationcycle, air
conditioning as well as in power plants. All of these utilize
the phenomenon of heat transfer to take heatfromonepoint
to other. Sometimes, a hotter body is required to be cooled
for its efficient operation while in some other application,
one needs to transfer heat to generate power and transmit
electricity, and efficient heat transfer is crucial to all those
fields. However, there lies always a limit of heat transfer
between two bodies. The limit exists due to the material
properties, design as well as fluid flow parameters of the
heat exchanger or transfer device. So, in the recent decade,
many researchers around the world are concerned about
this limit and are trying to eliminate this limit so that
maximum amount of heat transfer is possible. If there is an
infinite limit to the heat transferphenomenonina device, we
can achieve greater thermal efficiency, optimize the
geometry of heat exchanger and ultimately save energy.
In the scenario of present innovation in thermo-fluids
engineering we can find a lot of researchers who have
contributed to design, develop and test the devices related
energy/thermal management and clean energy. Various
techniques to attain efficient heat exchange [1-3], effective
combustion [4-6], alternative fuels [7-10], efficient power
generation [11-13] have been explored. And, all these have
helped the present-day technology in thermo-fluids and
energy sector to march ahead. In this paper, we concentrate
on the heat transfer enhancement portion of the energy
management technique. We have discussedabouttherecent
advances in convection heat transfer enhancement which is
required in various fields as discussed above. We have
presented a review of those articles in the most
understandable way. Based on our knowledge, this is one of
the first articles in literature, to encompass a clear and
understandable review in convection heat transfer
enhancement and mixed magnetohydrodynamic (MHD)
convection in a single paper.
2. DISCUSSION
We divide the discussion in the present article into two
categories based on two different kinds of convection heat
transfer enhancement: extrasurfacetokillthermalboundary
layer and MHD mixed convection.
2.1 Extra surface to kill thermal boundary layer
In this technique, people thesurfaceofheattransferdeviceor
heat exchanger is modified. The modification can be done by
using rough surface to increase friction for the flow or by
using an extra device like coil or tape inside the exchanger
which are typically called as insertions. Table -1 shows the
comparative illustration of various researches carried out in
this field. It alsoshowsthefinaloutcome/conclusionfromthe
corresponding studies. The reason behind this insertion isto
kill the thermal boundary layer which ultimately increases
the limit of heat transfer.
Table -1: Various studies illustrating heat transfer
enhancement using extra surface to kill thermal boundary
layer
S.
No.
Author(s) Investigation Conclusion
1 Sheikholeslami
et al. [14]
Passive
methods of
heat transfer
enhancement
using swirl
flow
Swirl device
induce
turbulence and
vortex motion
ultimately
inducing a
thinner
boundary layer
2 Kareem et al.
[15]
Review in
corrugation
for heat
Helically coiled
corrugation has
compound
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 31
transfer
enhancement
effect of
curvatures as
well as
corrugation
3 Pethkool et al.
[16]
Helical
corrugation in
heat
exchanger
Heat transfer
enhancement
along with
friction factor
was studied
experimentally
and an
empirical
relation was
established
4 García et al.
[17]
Corrugated
tubes,
dimpled tubes
and wire coils
in heat
transfer
Core flow
rotation causes
transition from
laminar to
tubulent flow,
coil causes
smooth
transition to
turbulent
5 Zimparov [18] Combined
single-start
spirally
corrugated
tubes with a
twisted tape
Benefits of
using combined
structures over
smooth tubes,
reduction in
entropy
generation
6 Elshafei et al.
[19]
Heat transfer
& pressure
drop
Heat transfer
enhancement
achieved along
with rise in
pressure drop,
channel spacing
also affects
pressure drop
7 Rainieri et al.
[20]
Helically
coiled wall
corrugated
tubes
In a given range
of Re, both the
curvature as
well as the
combination of
curvature &
corrugation
enhance heat
transfer
8 Naphon [21] Channel with
V corrugated
upper and
lower plates
Such design
provides higher
compactness
9 Gradeck et al.
[22]
Local heat
transfer
analysis in
corrugated
channel
Heat transfer
coefficient has
strong
sensitivity to
convective
effects at top of
the corrugation
only
10 Saha & Saha
[23]
Integral
helical rib
roughness &
fitted wavy
strip
Up to a certain
amount of wavy
strip centre-
clearance, the
integral design
performs better
than individual
11 Bhattacharyya
et al. [24]
Heat transfer
enhancement
& entropy
generation of
flow through
a wavy
channel
Combination of
the low wave
ratio and low
diameter ratio
shows
promising heat
transfer effect
12 Deb & Poudel
[25]
Combined
wire coil and
wavy strip in
a tube
Combined effect
augments the
heat transfer
enhancement
13 Sharma et al.
[26]
Twisted tape
inserts in a
tube
A new method
to predict heat
transfer
coefficient with
twisted tape
inserts
considering
heat transfer
augmentation
due modified
wall shear and
temperature
gradient
14 Agarwal & Rao
[27]
Circular tubes
with twisted
tape inserts
Developed a
correlation to
predict
isothermal
friction factors
and Nusselt
number
2.2 Magnetohydrodynamic (MHD) mixed convection
In this type of procedure, magnetic field with certain
strength is also applied in the heat transfer device with an
aim of enhancing the heat transfer capability. Many of the
research works in this area arecarriedoutnumericallyusing
computational fluid dynamics rather than experimentally
due to the ease of parametric variation and cost
effectiveness. Generally, a lid-driven square cavity is
considered with liquid filled inside it. Magnetic field is
supplied across the cavity and the variation of heat transfer
coefficient in terms of Nusselt number (Nu) is studied.Table
-2 demonstrate various kinds of heat transfer enhancement
techniques within MHD mixed convection using lid-driven
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 32
cavity. Each kind of innovation has helped to understandthe
fundamental behind the phenomenon and to draw a strong
conclusion for applying in the practical field.
Table -2: Studies associated with heat transfer
enhancement technique using magnetohydrodynamic
(MHD) mixed convection in a lid-driven cavity
S.
No.
Author(s) Investigation Conclusion
1 Malleswaran
&
Sivasankaran
[28]
MHD Mixed
Convection in
a Lid-driven
Cavity with
Corner
Heaters
The magnetic
field has greater
effect on heat
transfer rate
with vertical
heater than
with horizontal
one
2 Oztop et al.
[29]
MHD mixed
convection in
a lid-driven
cavity with
corner heater
Size of heater
and the
magnetic field
strength has a
great effect on
boundary layer
thus dictates
heat transfer
rate
3 Selimefendigil
& Oztop [30]
MHD mixed
convection in
a nanofluid
filled lid-
driven
enclosure with
a rotating
cylinder
Presence of
magnitic field
minimizes the
velocity field
and thus
convection;
solid volume
fraction of
nanoparticle
increases heat
transfer
4 Deb et al. [31] MHD
convection in
a lid-driven
cavity with a
heat
conduction
elliptical
obstacle
Magnetic field
offers damping
effect on
transport
(convection)
and suppress
natural
convection of
heat
5 Pekmen &
Tezer-Sezgin
[32]
MHD flow in a
lid-driven
porous
enclosure
Decrease in
permeability of
porous medium
slows down the
fluid flow
6 Hussain et al.
[33]
MHD mixed
convection
and entropy
generation in
Total entropy
generation adds
up with rise in
Reynolds
a lid-driven
cavity with
nanofluid flow
number
7 Rashad et al.
[34]
MHD mixed
convection in
a nanofluid-
filled lid-
driven cavity
with partial-
slip
Shortest length
of source/sink
give the
maximum
convective heat
transfer; partial
slip on walls
alters the
streamlines and
isotherms
ultimately
decreases the
convective heat
transfer
8 Chatterjee
[35]
MHD mixed
convection in
a lid-driven
cavity with a
heated source
Contribution of
straight and
semicircular
sources
towards heat
transfer is more
than towards
the bulk fluid
temperature
9 Rahman et al.
[36]
MHD mixed
convection in
a lid-driven
cavity with a
heated semi-
circular source
Direction of the
moving lid has a
great effect on
flow field; lower
Joule parameter
decreases heat
transfer
10 Sivasankaran
et al. [37]
MHD mixed
convection of
Cu-water
nanofluid in a
lid-driven
porous cavity
with a partial
slip
Nanoparticles
properties as
well as porosity
of the medium
affects the flow
thus the
convection heat
transfer
11 Rahman &
Alim [38]
MHD mixed
convection in
a lid-driven
enclosure with
a heat
conducting
circular
cylinder with
Joule heating
Hartmann
number,
Reynolds
number and
Richardson
number have
strong effects
on the
streamline and
isotherm plots
12 Deb et al. [39] MHD
convection in
a lid-driven
cavity
containing a
Size and
orientation of
the obstacle
dictates
isotherms as
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 33
obstacle with
different
inclination
well as
orientation thus
alters heat
transfer
13 Sajjadi et al.
[40]
Lattice
Boltzmann
simulation of
MHD mixed
convection
Established a
new lattice
Boltzmann
method to
replicate the
results of CFD;
growth of
magnetic field
induces
circulation and
vortices on
streamlines
14 Hasanpour et
al. [41]
Prandtl effect
on MHD flow
in a lid-driven
porous cavity
Rise in average
Nusselt number
by increasing
Prandtl
number; up to
28% increment
in heat transfer
enhancement
by increasing
Prandtl number
3. CONCLUSION
In this work, we show a comparative study of two different
kinds of convection heat transfer enhancement techniques
carried out with an aim of better thermal/energy/power
management. We explored and presented therecentarticles
in the field of passive heat transfer enhancement using extra
surface to kill the thermal boundarylayeraswell astheMHD
mixed convection in a lid-driven cavity. Hereby, we are
confident enough that this review article will help in
planning for future design and development of heat
exchangers in plethora of applications.
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Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 34
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IRJET- Review of Convection and Magnetohydrodynamic Mixed Convection Heat Transfer Enhancement

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 30 Review of Convection and Magnetohydrodynamic Mixed Convection Heat Transfer Enhancement Mayur Sakhare1, Rohit Yadav2 1,2Vellore Institute of Technology Dept. of Mechanical Engineering, Vellore Institute of Technology, Tamil Nadu, India ---------------------------------------------------------------------***---------------------------------------------------------------------- Abstract – In this paper, we discuss about the recent research trends in heat transfer enhancement in convection mode by using two kinds of techniques: killing thermal boundary layer and using magnetohydrodynamic (MHD) mixed convection. We first give a glance of various techniques utilized by the researchers to properly utilize energy and heat in varying applications. Then we focus our study in heat transfer enhancement only. The entire discussion is divided into two categories based on the kinds of heat transferenhancementas mentioned. We have presented the comparative study of related investigations along with the conclusion from them in the most understandable manner. This articleopensapathfor inclusive understanding of the phenomenon for future study, design and development of devices inconvectionheattransfer. Key Words: heat transfer, convection, magnetohydrodynamics 1. INTRODUCTION Heat transfer is required for the exchangeofthermal energy. Heat exchangers are used in several applications including cooling the engines of automobiles, in refrigerationcycle, air conditioning as well as in power plants. All of these utilize the phenomenon of heat transfer to take heatfromonepoint to other. Sometimes, a hotter body is required to be cooled for its efficient operation while in some other application, one needs to transfer heat to generate power and transmit electricity, and efficient heat transfer is crucial to all those fields. However, there lies always a limit of heat transfer between two bodies. The limit exists due to the material properties, design as well as fluid flow parameters of the heat exchanger or transfer device. So, in the recent decade, many researchers around the world are concerned about this limit and are trying to eliminate this limit so that maximum amount of heat transfer is possible. If there is an infinite limit to the heat transferphenomenonina device, we can achieve greater thermal efficiency, optimize the geometry of heat exchanger and ultimately save energy. In the scenario of present innovation in thermo-fluids engineering we can find a lot of researchers who have contributed to design, develop and test the devices related energy/thermal management and clean energy. Various techniques to attain efficient heat exchange [1-3], effective combustion [4-6], alternative fuels [7-10], efficient power generation [11-13] have been explored. And, all these have helped the present-day technology in thermo-fluids and energy sector to march ahead. In this paper, we concentrate on the heat transfer enhancement portion of the energy management technique. We have discussedabouttherecent advances in convection heat transfer enhancement which is required in various fields as discussed above. We have presented a review of those articles in the most understandable way. Based on our knowledge, this is one of the first articles in literature, to encompass a clear and understandable review in convection heat transfer enhancement and mixed magnetohydrodynamic (MHD) convection in a single paper. 2. DISCUSSION We divide the discussion in the present article into two categories based on two different kinds of convection heat transfer enhancement: extrasurfacetokillthermalboundary layer and MHD mixed convection. 2.1 Extra surface to kill thermal boundary layer In this technique, people thesurfaceofheattransferdeviceor heat exchanger is modified. The modification can be done by using rough surface to increase friction for the flow or by using an extra device like coil or tape inside the exchanger which are typically called as insertions. Table -1 shows the comparative illustration of various researches carried out in this field. It alsoshowsthefinaloutcome/conclusionfromthe corresponding studies. The reason behind this insertion isto kill the thermal boundary layer which ultimately increases the limit of heat transfer. Table -1: Various studies illustrating heat transfer enhancement using extra surface to kill thermal boundary layer S. No. Author(s) Investigation Conclusion 1 Sheikholeslami et al. [14] Passive methods of heat transfer enhancement using swirl flow Swirl device induce turbulence and vortex motion ultimately inducing a thinner boundary layer 2 Kareem et al. [15] Review in corrugation for heat Helically coiled corrugation has compound
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 31 transfer enhancement effect of curvatures as well as corrugation 3 Pethkool et al. [16] Helical corrugation in heat exchanger Heat transfer enhancement along with friction factor was studied experimentally and an empirical relation was established 4 García et al. [17] Corrugated tubes, dimpled tubes and wire coils in heat transfer Core flow rotation causes transition from laminar to tubulent flow, coil causes smooth transition to turbulent 5 Zimparov [18] Combined single-start spirally corrugated tubes with a twisted tape Benefits of using combined structures over smooth tubes, reduction in entropy generation 6 Elshafei et al. [19] Heat transfer & pressure drop Heat transfer enhancement achieved along with rise in pressure drop, channel spacing also affects pressure drop 7 Rainieri et al. [20] Helically coiled wall corrugated tubes In a given range of Re, both the curvature as well as the combination of curvature & corrugation enhance heat transfer 8 Naphon [21] Channel with V corrugated upper and lower plates Such design provides higher compactness 9 Gradeck et al. [22] Local heat transfer analysis in corrugated channel Heat transfer coefficient has strong sensitivity to convective effects at top of the corrugation only 10 Saha & Saha [23] Integral helical rib roughness & fitted wavy strip Up to a certain amount of wavy strip centre- clearance, the integral design performs better than individual 11 Bhattacharyya et al. [24] Heat transfer enhancement & entropy generation of flow through a wavy channel Combination of the low wave ratio and low diameter ratio shows promising heat transfer effect 12 Deb & Poudel [25] Combined wire coil and wavy strip in a tube Combined effect augments the heat transfer enhancement 13 Sharma et al. [26] Twisted tape inserts in a tube A new method to predict heat transfer coefficient with twisted tape inserts considering heat transfer augmentation due modified wall shear and temperature gradient 14 Agarwal & Rao [27] Circular tubes with twisted tape inserts Developed a correlation to predict isothermal friction factors and Nusselt number 2.2 Magnetohydrodynamic (MHD) mixed convection In this type of procedure, magnetic field with certain strength is also applied in the heat transfer device with an aim of enhancing the heat transfer capability. Many of the research works in this area arecarriedoutnumericallyusing computational fluid dynamics rather than experimentally due to the ease of parametric variation and cost effectiveness. Generally, a lid-driven square cavity is considered with liquid filled inside it. Magnetic field is supplied across the cavity and the variation of heat transfer coefficient in terms of Nusselt number (Nu) is studied.Table -2 demonstrate various kinds of heat transfer enhancement techniques within MHD mixed convection using lid-driven
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 32 cavity. Each kind of innovation has helped to understandthe fundamental behind the phenomenon and to draw a strong conclusion for applying in the practical field. Table -2: Studies associated with heat transfer enhancement technique using magnetohydrodynamic (MHD) mixed convection in a lid-driven cavity S. No. Author(s) Investigation Conclusion 1 Malleswaran & Sivasankaran [28] MHD Mixed Convection in a Lid-driven Cavity with Corner Heaters The magnetic field has greater effect on heat transfer rate with vertical heater than with horizontal one 2 Oztop et al. [29] MHD mixed convection in a lid-driven cavity with corner heater Size of heater and the magnetic field strength has a great effect on boundary layer thus dictates heat transfer rate 3 Selimefendigil & Oztop [30] MHD mixed convection in a nanofluid filled lid- driven enclosure with a rotating cylinder Presence of magnitic field minimizes the velocity field and thus convection; solid volume fraction of nanoparticle increases heat transfer 4 Deb et al. [31] MHD convection in a lid-driven cavity with a heat conduction elliptical obstacle Magnetic field offers damping effect on transport (convection) and suppress natural convection of heat 5 Pekmen & Tezer-Sezgin [32] MHD flow in a lid-driven porous enclosure Decrease in permeability of porous medium slows down the fluid flow 6 Hussain et al. [33] MHD mixed convection and entropy generation in Total entropy generation adds up with rise in Reynolds a lid-driven cavity with nanofluid flow number 7 Rashad et al. [34] MHD mixed convection in a nanofluid- filled lid- driven cavity with partial- slip Shortest length of source/sink give the maximum convective heat transfer; partial slip on walls alters the streamlines and isotherms ultimately decreases the convective heat transfer 8 Chatterjee [35] MHD mixed convection in a lid-driven cavity with a heated source Contribution of straight and semicircular sources towards heat transfer is more than towards the bulk fluid temperature 9 Rahman et al. [36] MHD mixed convection in a lid-driven cavity with a heated semi- circular source Direction of the moving lid has a great effect on flow field; lower Joule parameter decreases heat transfer 10 Sivasankaran et al. [37] MHD mixed convection of Cu-water nanofluid in a lid-driven porous cavity with a partial slip Nanoparticles properties as well as porosity of the medium affects the flow thus the convection heat transfer 11 Rahman & Alim [38] MHD mixed convection in a lid-driven enclosure with a heat conducting circular cylinder with Joule heating Hartmann number, Reynolds number and Richardson number have strong effects on the streamline and isotherm plots 12 Deb et al. [39] MHD convection in a lid-driven cavity containing a Size and orientation of the obstacle dictates isotherms as
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 12 | Dec 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 33 obstacle with different inclination well as orientation thus alters heat transfer 13 Sajjadi et al. [40] Lattice Boltzmann simulation of MHD mixed convection Established a new lattice Boltzmann method to replicate the results of CFD; growth of magnetic field induces circulation and vortices on streamlines 14 Hasanpour et al. [41] Prandtl effect on MHD flow in a lid-driven porous cavity Rise in average Nusselt number by increasing Prandtl number; up to 28% increment in heat transfer enhancement by increasing Prandtl number 3. CONCLUSION In this work, we show a comparative study of two different kinds of convection heat transfer enhancement techniques carried out with an aim of better thermal/energy/power management. We explored and presented therecentarticles in the field of passive heat transfer enhancement using extra surface to kill the thermal boundarylayeraswell astheMHD mixed convection in a lid-driven cavity. Hereby, we are confident enough that this review article will help in planning for future design and development of heat exchangers in plethora of applications. REFERENCES [1] Arsenyeva, O. P., Tovazhnyansky, L.L.,Kapustenko,P.O., & Khavin, G. L. (2011). Optimal design of plate-and- frame heat exchangers for efficient heat recovery in process industries. Energy, 36(8), 4588-4598. [2] Vasiliev, L. L. (2005). Heat pipes in modern heat exchangers. Applied thermal engineering, 25(1), 1-19. [3] Sunden, B. (2005, September). High temperature heat exchangers (HTHE). In Proceedings of the 5th International Conference on Science, Engineering and Technology, VIT University, Vellore, India. [4] Babrauskas, V. (2006). Effective heat of combustion for flaming combustion of conifers. Canadian Journal of Forest Research, 36(3), 659-663. [5] Cartellieri, W., Chmela, F. G., Kapus, P. E., & Tatschl, R. M. (1994). Mechanisms leading to stable and efficient combustion in lean burn gas engines. In Proceedings of International Symposium COMODIA. [6] Singh, S. (2001). U.S. Patent No. 6,237,579. Washington, DC: U.S. Patent and Trademark Office. [7] Balat, M. (2005).Currentalternativeenginefuels.Energy Sources, 27(6), 569-577. [8] Murugesan, A., Umarani, C., Subramanian, R., & Nedunchezhian, N. (2009). Bio-diesel as an alternative fuel for diesel engines—a review. Renewable and sustainable energy reviews, 13(3), 653-662. [9] Poudel, S., & Deb, D. Study of Modified Internal Combustion Engine to Run with Ethanol. International Journal of Engineering and Applied Sciences, 4(8). [10] Gupta, K. K., Rehman, A., & Sarviya, R. M. (2010). Bio- fuels for the gas turbine: A review. Renewable and Sustainable Energy Reviews, 14(9), 2946-2955. [11] Farooque, M., & Maru, H. C. (2001). Fuel cells-the clean and efficient power generators. Proceedings of the IEEE, 89(12), 1819-1829. [12] Wang, J., Anthony, E. J., & Abanades, J. C. (2004). Clean and efficient use of petroleum coke for combustion and power generation. Fuel, 83(10), 1341-1348. [13] Andreycak, W. M. (2008). U.S. Patent No. 7,375,994. Washington, DC: U.S. Patent and Trademark Office. [14] Sheikholeslami, M., Gorji-Bandpy, M., & Ganji, D. D. (2015). Review of heat transfer enhancement methods: Focus on passive methods using swirl flow devices. Renewable and Sustainable Energy Reviews, 49, 444-469. [15] Kareem, Z. S., Jaafar, M. M., Lazim, T. M., Abdullah, S., & Abdulwahid, A. F. (2015). Passive heat transfer enhancement review in corrugation. Experimental Thermal and Fluid Science, 68, 22-38. [16] Pethkool, S., Eiamsa-Ard, S., Kwankaomeng, S., & Promvonge, P. (2011). Turbulent heat transfer enhancement in a heat exchanger using helically corrugated tube. International Communications in Heat and Mass Transfer, 38(3), 340-347. [17] García, A., Solano, J. P., Vicente, P. G., & Viedma, A. (2012). The influence of artificial roughness shape on heat transfer enhancement: Corrugated tubes, dimpled tubes and wire coils. Applied Thermal Engineering, 35, 196-201. [18] Zimparov, V. (2002). Enhancement of heat transfer by a combination of a single-start spirally corrugated tubes with a twisted tape. Experimental Thermal and Fluid Science, 25(7), 535-546. [19] Elshafei, E. A. M., Awad, M. M., El-Negiry, E., & Ali, A. G. (2010). Heat transfer and pressure drop in corrugated channels. Energy, 35(1), 101-110. [20] Rainieri, S., Bozzoli, F., Cattani, L., & Pagliarini,G.(2013). Compound convective heat transfer enhancement in helically coiled wall corrugated tubes. International Journal of Heat and Mass Transfer, 59, 353-362. [21] Naphon, P. (2007). Heat transfer characteristics and pressure drop in channel with V corrugated upper and lower plates. Energy conversionandmanagement, 48(5), 1516-1524.
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