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International Journal of Scientific & Engineering Research, Volume 6, Issue 6, June-2015 260
ISSN 2229-5518
IJSER © 2015
http://www.ijser.org
Computational Fluid Dynamics Modelling and
Simulation of Laminar Convective Fluid and Heat
Flow of a portable air-conditioning Unit
Part I
Ashaju Abimbola
Abstract— This work deals with a study on the laminar convective heat flow of a homemade air condition ing unit through a computational
fluid dynamics simulation. With adoption of chilled water as the working fluid within a tube section of the evaporative compartment of the
homemade air conditioner whose radius is 5mm and Height 20mm .The numerical analysis was carried out using COMSOL
MULTIPHYSICS.Simulation was carried out, using (276𝐾 (3°
𝑆) as the inlet temperature and 293𝐾 (20°
𝑆) as the outlet temperature
with a flow rate of 0.15 𝑚3
𝑠⁄ . The result showed the velocity profile of the working fluid and the temperature distribution before, during
and after heat exchange, helping to achieve a Visual understanding of the Laminar convective fluid and heat flow phenomena within the
cooling coil.
Index Terms—Compuational Fluid Dynamics, Convection, Modelling, Simulation, Heat transfer, Comsol, Air-conditioning
——————————  ——————————
1 INTRODUCTION
The home made air conditioner was designed and con-
structed by a Canadian Geoffrey Milburn in 2006, during the
course of an extreme hot weather condition in Canada. [1]
Figure 1 Home made portable air conditioner
The evaporator unit consists basically of cooling coil prima-
ry copper
1
4
"
wounded around a fan as shown in figure 1.The
working principle, Design and construction was given de-
tailed out in [1]
The evaporative compartment remains one of the most im-
portant parts of any cooling system unit.
The study of combined fluid flow and heat transfer inside
tubes is a Fundamental problem in convective heat transfer.
Laminar convective heat transfer has found application in
many works by several authors [2] [3] [4] [5] [6] [7].
Baron et al. [2] investigated the phenomenon of fully devel-
oped and developing laminar flows of a Newtonian fluid be-
tween parallel plates and through circular tubes. Sarma et al.
[3]Suggested a method, to estimate the heat transfer coeffi-
cients in the entry region, of a short length of tube under de-
veloping laminar flow conditions. Zhuo et al [4].performed 3D
numerical simulations of the laminar flow and heat transfer in
silicon microchannels of non-circular cross sections. Edalati et
al.[8] Obtained a 41% enhancement in the convective heat
transfer coefficient for a 0.8% 𝐶𝐶𝐶/𝑊𝑊𝑊𝑊𝑊 nanofluid after
studying the heat transfer of an equilateral triangular duct.
The aim of this study is to apply numerical computation in
understanding the laminar convective heat flow phenomena
within the coiling coil of the home made air conditioner, with
the simulation and modelling through the application of
COMSOL MULTIPHYSICS.
2 GOVERNING EQUATIONS
2.1 Laminar Convective Fluid and Heat Flow
The governing equations for the laminar flow within the
cooling coil are
1. Conservation of mass [continuity equation]
2. Conservation of momentum [Navier-stokes equation]
3. Conservation of Energy.
————————————————
• Ashaju Abimbola is currently pursuing masters degree program in me-
chanical engineering in Universityof ibadan , Nigeria,
• PH-+234(0)8062302107.
• E-mail: samuelashaju@gmail.com
IJSER
International Journal of Scientific & Engineering Research, Volume 6, Issue 6, June-2015 261
ISSN 2229-5518
IJSER © 2015
http://www.ijser.org
These equations are summarized below as;
2.2 Continuity equation
𝜕𝜌
𝜕𝑡
+ 𝜌(∇. 𝑣⃗)=0 (2.2.1)
𝜕𝜌
𝜕𝑡
+ ∇(𝜌𝑣⃗) = 0 (2.2.2)
𝜕𝜌
𝜕𝑡
+
𝜕(𝜌𝑢)
𝜕𝑥
+
𝜕(𝜌𝑣)
𝜕𝑦
+
𝜕(𝜌𝑤)
𝜕𝑧
= 0 (2.2.3)
2.3 Navier-Stoke’s Equation
𝜕
𝜕𝑡
[𝜌𝑣⃗] + ∇. (𝜌𝑣⃗𝑣⃗) = −∇𝑝 − ∇𝜏̿ + 𝜌𝑔⃗ (2.3.1)
𝜌 �
𝜕𝑣�⃗
𝜕𝑡
+ (𝑣⃗.∇)𝑣⃗� = −∇𝑝 − ∇𝜏̿ + 𝜌𝑔⃗ (2.3.2)
𝜌
𝜕𝑣�⃗
𝜕𝑡
= −∇𝑝 − ∇𝜏̿ + 𝜌𝑔⃗ (2.3.3)
2.4 Energy Equation
𝜌 𝐶𝑝
𝑑𝑇
𝑑𝑡
= −∇𝑞⃗ +
𝑑𝑝
𝑑𝑡
+ 𝜏̿. ∇𝑣⃗ (2.4.1)
𝜌 𝐶𝑝 �
𝜕𝜕
𝜕𝜕
+ (𝑢. ∇) 𝑇
� = −(∇. 𝑞) + 𝜏. 𝑠 −
𝑇
𝜌
𝜕𝜕
𝜕𝜕
�
𝜕𝜕
𝜕𝜕
+ (𝜇.∇)ρ�
(2.4.2)
The major mode of heat transfer under study is convection.
2.5 Newton’s law of cooling
𝑞̇ 𝑐𝑜𝑛𝑣 = ℎ[𝑇𝑠 − 𝑇∞ ] 𝑊/𝑚2
(2.5.1)
𝑇𝑠 = 𝑆𝑆𝑆𝑆𝑆𝑆𝑆 𝑡𝑡𝑡𝑡𝑡𝑡𝑡𝑡𝑡𝑡𝑡
𝑇∞ = Temperature of the fluid
Fourier's Law of conduction
𝑞 = −𝑘
𝜕𝑇
𝜕𝑥
2.6 Nusselt Number 𝐍 𝐮
𝒒̇ 𝒄𝒐𝒏𝒗
𝒒̇ 𝒄𝒐𝒏𝒅
=
𝒉∆𝑻
𝒌
∆𝑻
𝒉
=
𝒉𝒉
𝑲
(2.5.2)
𝑁𝑢 =
ℎ𝐿
𝑘
(2.6.3)
3 NUMERICAL MODELS
A 3D domain which was a section of the cooling coil was cre-
ated, with height 20𝑚𝑚 and radius5𝑚𝑚 as shown in Figure 2
below
Figure 3 Schematic of the Tube section from the cooling coil
The material used for the cooling coil was copper, while the
working fluid was chilled water which was considered New-
tonian and incompressible.
The physics considered was conjugate Heat transfer, which
was a mixture of convective heat and Laminar fluid flow.
No-slip condition was imposed at the walls of the tube.
At the inlet of the tube section, a Laminar inflow boundary
condition was adopted, with a flow rate of 0.15m3
s⁄ .At the
outlet of the tube section, zero pressure condition was im-
posed.
An external fan was imposed at the outer of the cooling
coils, to provide forced convection effect, whose static pres-
sure curve was linear, with a free delivery flow rate of
0.01 m3
s⁄ .
3.1 Meshing
This was done using coarse free tetrahedral shape with el-
ement size ranging from 0.0014 − 0.01, refinements were done
at corners with an element scale sizing factor of 0.35 .
The features of the meshing are:
Number of vertex elements: 8
Number of edge elements: 36
Number of boundary elements: 128
Number of elements: 150.
The meshed tube section is shown below in Figure 3
————————————————
• Ashaju Abimbola is currently pursuing masters degree program in me-
chanical engineering in Universityof ibadan , Nigeria, PH-
+234(0)8062302107. E-mail: samuelashaju@gmail.com
IJSER
International Journal of Scientific & Engineering Research, Volume 6, Issue 6, June-2015 262
ISSN 2229-5518
IJSER © 2015
http://www.ijser.org
Figure 4 Meshed Tube section
4 RESULTS AND DISCUSSION
The Laminar Convective heat effect within the cooling coil is
discussed. As mentioned previously the flow inside the pipe is
laminar.The Velocity and Temperature profile for the fluid
within the tube section was computed as shown in Figure four
and Figure five below.
Figure four shows the computed velocity plot for the flow of
chilled water within the tube section, as heat exchange takes
place between the fluid and the ambient air with channel wall
acting as an intermediary
Figure 5 Velocity profile for the flow within the tube section
The temperature field obtained from the simulation ,is pre-
sented in Figure 5.
A cold zone is observed at the inlet of the tube section where
chilled water enters.This is followed by a reduction in the
temperature of the fluid at the warm zone. This happens as a
temperature gradient is established between the chilled water
and the ambient air surrounding the cooling coils. The ex-
change of heat takes place and the temperature of the working
fluid increases from 276𝐾 (3°
𝐶) 𝑡𝑡 292𝐾 (19°
𝐶).
Figure 6 Temperature profile within the tube section
5 CONCLUSION
Numerical investigation of laminar convective heat and fluid
flow has been investigated within a tube section, with the aid
of COMSOL MULTIPHYSICS.
The inlet showed the temperature of the chilled water before
heat exchange and the outlet temperature showed the temper-
ature of the chilled water after heat exchange and energy
transport.
More work still needs to be done to investigate the fluid flow
and heat transfer process within the cooling coil of the evapo-
rator. As a perspective, it would be interesting to investigate
further, the pressure drop and heat transfer rate of the cooling
coils, likewise also the effects of the flow rate on the heat trans-
fer rate.
ACKNOWLEDGMENT
The author wish to thank Geoffrey Milburn, who provided the
platform to work on his portable air-conditioing unit
REFERENCES
1. Prediction of flow pattern and velocity distribution in pipe
lines,using COMSOL MULTIPHYSICS simulator. Nasser,
Saghatoleslami and Okhovat, Ahmad. Kermanshah : s.n.
Iranian National Chemical Engineering Congress. pp. 1-10.
2. Jakob, Munch Jensen. Dynamic modelling of Thermo-fluid
systems with focus on evaporators for refrigeration. Department of
Mechanical Engineering, Technical University of Denmark.
2003. Ph.D Thesis.
3. Computational fluid Dynamics [CFD] simulation to analyse the
performance of tube-in-tube helically coiled of a heat exchanger.
Chaves, C. A, et al. 7, s.l. : Scientific Research and Essays,
2014, academic journals, Vol. 9, pp. 181-188.
IJSER
International Journal of Scientific & Engineering Research, Volume 6, Issue 6, June-2015 263
ISSN 2229-5518
IJSER © 2015
http://www.ijser.org
4. CFD Investigation of Heat Transfer and Flow Patterns in Tube
Side Laminar Flow and the Potential for Enhancement. Osley, G.
William, Droegemueller, Peter and Ellerby, Peter. s.l. : The
Italian Association of Chemical Engineering, 2013,
CHEMICAL ENGINEERING TRANSACTIONS, Vol. 35.
5. Modelling and Optimization of Heat Transfer in Smooth Circular
Tube Used in the Shell and Tube Evaporator. RANJ, SIRWAN, et
al. Recent Advances in Fluid Mechanics, Heat & Mass Transfer
and Biology.
6. Modeling Convective Heat Transfer under Laminar Flow of a
Newtonian Fluid in Simple Geometries. Baron, B. and Gutierrez,
E. Miravete. Boston : s.n., 2007. Excerpt from the Proceedings
of the COMSOL Conference.
7. A novel method to determine laminar convective heat transfer in
the entry region of a tube. Sarma, P. k, et al. s.l. : Elsevier, 2003,
International Journal of Thermal Sciences, Vol. 43, pp. 555–559.
8. A numerical study of laminar convective heat transfer in
microchannel with non-circular cross-section. Zhuo, Li, Wen-
Quan, Tao and Ya-Ling, He. s.l. : ELSEVIER, 2006,
International Journal of Thermal Sciences, Vol. 45, pp. 1140–
1148.
9. Laminar convective heat transfer and pressure drop in the
corrugated channels. Paisarn, Naphon. s.l. : ELSEVIER,
International Communications in Heat and Mass Transfer,
Vol. 34, pp. 62–71.
10. The Study of Laminar Convective Heat Transfer of CuO/Water
Nanofluid Through an Equilateral Triangular Duct at Constant wall
heat flux. Edalati, Z., Heris, S. Zeinal and Noie, S. H. 5, s.l. :
Wiley Periodicals, Inc., 2012, Heat Transfer—Asian Research, Vol.
41, pp. 1-12.
NOMENCLATURE
CFD – Computational Fluid Dynamics
CuO – Copper(II) Oxide
𝜌 - Density (𝐾𝐾 𝑚3
)⁄
U - Velocity Vector (𝑚 𝑠⁄ )
T - Absolute temperature (𝑘)
𝐶 𝑝 - Specific Heat Capacity ( 𝐽 (𝑘𝑘. 𝑘)⁄ )
𝑣 - Viscous Stress Tensor (𝑃𝑃)
Q - Heat Source [ 𝑊 𝑚3
⁄ ]
IJSER

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Computational fluid-dynamics-modelling-and-simulation-of-laminar-convective-fluid

  • 1. International Journal of Scientific & Engineering Research, Volume 6, Issue 6, June-2015 260 ISSN 2229-5518 IJSER © 2015 http://www.ijser.org Computational Fluid Dynamics Modelling and Simulation of Laminar Convective Fluid and Heat Flow of a portable air-conditioning Unit Part I Ashaju Abimbola Abstract— This work deals with a study on the laminar convective heat flow of a homemade air condition ing unit through a computational fluid dynamics simulation. With adoption of chilled water as the working fluid within a tube section of the evaporative compartment of the homemade air conditioner whose radius is 5mm and Height 20mm .The numerical analysis was carried out using COMSOL MULTIPHYSICS.Simulation was carried out, using (276𝐾 (3° 𝑆) as the inlet temperature and 293𝐾 (20° 𝑆) as the outlet temperature with a flow rate of 0.15 𝑚3 𝑠⁄ . The result showed the velocity profile of the working fluid and the temperature distribution before, during and after heat exchange, helping to achieve a Visual understanding of the Laminar convective fluid and heat flow phenomena within the cooling coil. Index Terms—Compuational Fluid Dynamics, Convection, Modelling, Simulation, Heat transfer, Comsol, Air-conditioning ——————————  —————————— 1 INTRODUCTION The home made air conditioner was designed and con- structed by a Canadian Geoffrey Milburn in 2006, during the course of an extreme hot weather condition in Canada. [1] Figure 1 Home made portable air conditioner The evaporator unit consists basically of cooling coil prima- ry copper 1 4 " wounded around a fan as shown in figure 1.The working principle, Design and construction was given de- tailed out in [1] The evaporative compartment remains one of the most im- portant parts of any cooling system unit. The study of combined fluid flow and heat transfer inside tubes is a Fundamental problem in convective heat transfer. Laminar convective heat transfer has found application in many works by several authors [2] [3] [4] [5] [6] [7]. Baron et al. [2] investigated the phenomenon of fully devel- oped and developing laminar flows of a Newtonian fluid be- tween parallel plates and through circular tubes. Sarma et al. [3]Suggested a method, to estimate the heat transfer coeffi- cients in the entry region, of a short length of tube under de- veloping laminar flow conditions. Zhuo et al [4].performed 3D numerical simulations of the laminar flow and heat transfer in silicon microchannels of non-circular cross sections. Edalati et al.[8] Obtained a 41% enhancement in the convective heat transfer coefficient for a 0.8% 𝐶𝐶𝐶/𝑊𝑊𝑊𝑊𝑊 nanofluid after studying the heat transfer of an equilateral triangular duct. The aim of this study is to apply numerical computation in understanding the laminar convective heat flow phenomena within the coiling coil of the home made air conditioner, with the simulation and modelling through the application of COMSOL MULTIPHYSICS. 2 GOVERNING EQUATIONS 2.1 Laminar Convective Fluid and Heat Flow The governing equations for the laminar flow within the cooling coil are 1. Conservation of mass [continuity equation] 2. Conservation of momentum [Navier-stokes equation] 3. Conservation of Energy. ———————————————— • Ashaju Abimbola is currently pursuing masters degree program in me- chanical engineering in Universityof ibadan , Nigeria, • PH-+234(0)8062302107. • E-mail: samuelashaju@gmail.com IJSER
  • 2. International Journal of Scientific & Engineering Research, Volume 6, Issue 6, June-2015 261 ISSN 2229-5518 IJSER © 2015 http://www.ijser.org These equations are summarized below as; 2.2 Continuity equation 𝜕𝜌 𝜕𝑡 + 𝜌(∇. 𝑣⃗)=0 (2.2.1) 𝜕𝜌 𝜕𝑡 + ∇(𝜌𝑣⃗) = 0 (2.2.2) 𝜕𝜌 𝜕𝑡 + 𝜕(𝜌𝑢) 𝜕𝑥 + 𝜕(𝜌𝑣) 𝜕𝑦 + 𝜕(𝜌𝑤) 𝜕𝑧 = 0 (2.2.3) 2.3 Navier-Stoke’s Equation 𝜕 𝜕𝑡 [𝜌𝑣⃗] + ∇. (𝜌𝑣⃗𝑣⃗) = −∇𝑝 − ∇𝜏̿ + 𝜌𝑔⃗ (2.3.1) 𝜌 � 𝜕𝑣�⃗ 𝜕𝑡 + (𝑣⃗.∇)𝑣⃗� = −∇𝑝 − ∇𝜏̿ + 𝜌𝑔⃗ (2.3.2) 𝜌 𝜕𝑣�⃗ 𝜕𝑡 = −∇𝑝 − ∇𝜏̿ + 𝜌𝑔⃗ (2.3.3) 2.4 Energy Equation 𝜌 𝐶𝑝 𝑑𝑇 𝑑𝑡 = −∇𝑞⃗ + 𝑑𝑝 𝑑𝑡 + 𝜏̿. ∇𝑣⃗ (2.4.1) 𝜌 𝐶𝑝 � 𝜕𝜕 𝜕𝜕 + (𝑢. ∇) 𝑇 � = −(∇. 𝑞) + 𝜏. 𝑠 − 𝑇 𝜌 𝜕𝜕 𝜕𝜕 � 𝜕𝜕 𝜕𝜕 + (𝜇.∇)ρ� (2.4.2) The major mode of heat transfer under study is convection. 2.5 Newton’s law of cooling 𝑞̇ 𝑐𝑜𝑛𝑣 = ℎ[𝑇𝑠 − 𝑇∞ ] 𝑊/𝑚2 (2.5.1) 𝑇𝑠 = 𝑆𝑆𝑆𝑆𝑆𝑆𝑆 𝑡𝑡𝑡𝑡𝑡𝑡𝑡𝑡𝑡𝑡𝑡 𝑇∞ = Temperature of the fluid Fourier's Law of conduction 𝑞 = −𝑘 𝜕𝑇 𝜕𝑥 2.6 Nusselt Number 𝐍 𝐮 𝒒̇ 𝒄𝒐𝒏𝒗 𝒒̇ 𝒄𝒐𝒏𝒅 = 𝒉∆𝑻 𝒌 ∆𝑻 𝒉 = 𝒉𝒉 𝑲 (2.5.2) 𝑁𝑢 = ℎ𝐿 𝑘 (2.6.3) 3 NUMERICAL MODELS A 3D domain which was a section of the cooling coil was cre- ated, with height 20𝑚𝑚 and radius5𝑚𝑚 as shown in Figure 2 below Figure 3 Schematic of the Tube section from the cooling coil The material used for the cooling coil was copper, while the working fluid was chilled water which was considered New- tonian and incompressible. The physics considered was conjugate Heat transfer, which was a mixture of convective heat and Laminar fluid flow. No-slip condition was imposed at the walls of the tube. At the inlet of the tube section, a Laminar inflow boundary condition was adopted, with a flow rate of 0.15m3 s⁄ .At the outlet of the tube section, zero pressure condition was im- posed. An external fan was imposed at the outer of the cooling coils, to provide forced convection effect, whose static pres- sure curve was linear, with a free delivery flow rate of 0.01 m3 s⁄ . 3.1 Meshing This was done using coarse free tetrahedral shape with el- ement size ranging from 0.0014 − 0.01, refinements were done at corners with an element scale sizing factor of 0.35 . The features of the meshing are: Number of vertex elements: 8 Number of edge elements: 36 Number of boundary elements: 128 Number of elements: 150. The meshed tube section is shown below in Figure 3 ———————————————— • Ashaju Abimbola is currently pursuing masters degree program in me- chanical engineering in Universityof ibadan , Nigeria, PH- +234(0)8062302107. E-mail: samuelashaju@gmail.com IJSER
  • 3. International Journal of Scientific & Engineering Research, Volume 6, Issue 6, June-2015 262 ISSN 2229-5518 IJSER © 2015 http://www.ijser.org Figure 4 Meshed Tube section 4 RESULTS AND DISCUSSION The Laminar Convective heat effect within the cooling coil is discussed. As mentioned previously the flow inside the pipe is laminar.The Velocity and Temperature profile for the fluid within the tube section was computed as shown in Figure four and Figure five below. Figure four shows the computed velocity plot for the flow of chilled water within the tube section, as heat exchange takes place between the fluid and the ambient air with channel wall acting as an intermediary Figure 5 Velocity profile for the flow within the tube section The temperature field obtained from the simulation ,is pre- sented in Figure 5. A cold zone is observed at the inlet of the tube section where chilled water enters.This is followed by a reduction in the temperature of the fluid at the warm zone. This happens as a temperature gradient is established between the chilled water and the ambient air surrounding the cooling coils. The ex- change of heat takes place and the temperature of the working fluid increases from 276𝐾 (3° 𝐶) 𝑡𝑡 292𝐾 (19° 𝐶). Figure 6 Temperature profile within the tube section 5 CONCLUSION Numerical investigation of laminar convective heat and fluid flow has been investigated within a tube section, with the aid of COMSOL MULTIPHYSICS. The inlet showed the temperature of the chilled water before heat exchange and the outlet temperature showed the temper- ature of the chilled water after heat exchange and energy transport. More work still needs to be done to investigate the fluid flow and heat transfer process within the cooling coil of the evapo- rator. As a perspective, it would be interesting to investigate further, the pressure drop and heat transfer rate of the cooling coils, likewise also the effects of the flow rate on the heat trans- fer rate. ACKNOWLEDGMENT The author wish to thank Geoffrey Milburn, who provided the platform to work on his portable air-conditioing unit REFERENCES 1. Prediction of flow pattern and velocity distribution in pipe lines,using COMSOL MULTIPHYSICS simulator. Nasser, Saghatoleslami and Okhovat, Ahmad. Kermanshah : s.n. Iranian National Chemical Engineering Congress. pp. 1-10. 2. Jakob, Munch Jensen. Dynamic modelling of Thermo-fluid systems with focus on evaporators for refrigeration. Department of Mechanical Engineering, Technical University of Denmark. 2003. Ph.D Thesis. 3. Computational fluid Dynamics [CFD] simulation to analyse the performance of tube-in-tube helically coiled of a heat exchanger. Chaves, C. A, et al. 7, s.l. : Scientific Research and Essays, 2014, academic journals, Vol. 9, pp. 181-188. IJSER
  • 4. International Journal of Scientific & Engineering Research, Volume 6, Issue 6, June-2015 263 ISSN 2229-5518 IJSER © 2015 http://www.ijser.org 4. CFD Investigation of Heat Transfer and Flow Patterns in Tube Side Laminar Flow and the Potential for Enhancement. Osley, G. William, Droegemueller, Peter and Ellerby, Peter. s.l. : The Italian Association of Chemical Engineering, 2013, CHEMICAL ENGINEERING TRANSACTIONS, Vol. 35. 5. Modelling and Optimization of Heat Transfer in Smooth Circular Tube Used in the Shell and Tube Evaporator. RANJ, SIRWAN, et al. Recent Advances in Fluid Mechanics, Heat & Mass Transfer and Biology. 6. Modeling Convective Heat Transfer under Laminar Flow of a Newtonian Fluid in Simple Geometries. Baron, B. and Gutierrez, E. Miravete. Boston : s.n., 2007. Excerpt from the Proceedings of the COMSOL Conference. 7. A novel method to determine laminar convective heat transfer in the entry region of a tube. Sarma, P. k, et al. s.l. : Elsevier, 2003, International Journal of Thermal Sciences, Vol. 43, pp. 555–559. 8. A numerical study of laminar convective heat transfer in microchannel with non-circular cross-section. Zhuo, Li, Wen- Quan, Tao and Ya-Ling, He. s.l. : ELSEVIER, 2006, International Journal of Thermal Sciences, Vol. 45, pp. 1140– 1148. 9. Laminar convective heat transfer and pressure drop in the corrugated channels. Paisarn, Naphon. s.l. : ELSEVIER, International Communications in Heat and Mass Transfer, Vol. 34, pp. 62–71. 10. The Study of Laminar Convective Heat Transfer of CuO/Water Nanofluid Through an Equilateral Triangular Duct at Constant wall heat flux. Edalati, Z., Heris, S. Zeinal and Noie, S. H. 5, s.l. : Wiley Periodicals, Inc., 2012, Heat Transfer—Asian Research, Vol. 41, pp. 1-12. NOMENCLATURE CFD – Computational Fluid Dynamics CuO – Copper(II) Oxide 𝜌 - Density (𝐾𝐾 𝑚3 )⁄ U - Velocity Vector (𝑚 𝑠⁄ ) T - Absolute temperature (𝑘) 𝐶 𝑝 - Specific Heat Capacity ( 𝐽 (𝑘𝑘. 𝑘)⁄ ) 𝑣 - Viscous Stress Tensor (𝑃𝑃) Q - Heat Source [ 𝑊 𝑚3 ⁄ ] IJSER