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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 399
FORCED CONVECTIVE HEAT TRANSFER IN A LID-DRIVEN CAVITY
Anjan Bhunia1, Souvik Maity1, Anupam Santra1, Sribas Samanta1
1Dept. of Mechanical Engineering, College of Engineering & Management, Kolaghat, India
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract - This work deals with the processes of forced
convective heat transfer within a lid-driven cavity, using
numerical simulations to assess the thermal behavior under
varied flow conditions. The lid-driven cavity is a traditional
structure with several technical and industrial uses. The goal
is to comprehend the complex interplay between fluid flow
patterns and heat transmission within the hollow. The
numerical simulations are carried out using a proven
computational fluid dynamics (CFD) model, with the effects of
Reynolds number and aspect ratio taken into account.
Basically, this work consists Reynolds number (Re), Nusselt
number (Nu) and Prandtl number (Pr). We are taking a
rectangular channel whose top wall is moving and the
working fluid of Prandtl number (Pr) equal to 0.71 and 5.83 is
utilized for this study.
Key Words: Forced convection; Rectangular
channel; Heat generation; Lid-driven cavity;
Reynolds number; Prandtl number
NOMENCLATURE
Nu Nusselt number
Pr Prandtl Number
Re Reynolds number
1. INTRODUCTION
Forced convection within rectangular channel holds a great
relevance in engineering applications such as heat
exchangers,coolingsystems, andotherthermal management
equipment. The practical ramifications of this research
include the design and optimization of rectangular channel
heat exchangers, cooling systems, and other thermal
management equipment. By utilizing forced convection
inside rectangular geometries, the findingsofthisstudyhelp
to the creation of efficient and sustainable engineering
solutions. Prior studies have looked into heat transfer
enhancement in an inclined square cavity filled with
nanofluid, heat transfer in a two-sided Lid-driven cavity
filled with volumetrically heat-generatingporousmedia,etc.
Basically, this work deals with Nusselt number (Nu) and
Prandtl number (Pr). Nusselt number (Nu) is the ratio of
heat flow rate by convection and heat flow rate by
conduction.
For forced convection, NuisindependentofGrashofnumber.
And the Prandtl number (Pr) is the ratio of kinematic and
dynamic viscosity.
For air, Pr =0.71
For water, Pr =5.83
2. PROBLEM FORMULATION
This study deals into captivating domain of computational
fluid dynamics (CFD) within a rectangular channel. A
rectangular channel with the dimension of height (H) 1m
and length (L) of 1m. The top wall of the channel is
maintaining the no slip condition while traveling
continuously in the positive x-direction. The other walls are
stationary. The upper and lower wall of the rectangular
channel is insulated and other two side wall is one heating
wall and another is cooling wall.TheworkingfluidofPrandtl
number (Pr) equals to 0.71 and 5.83 are utilized for this
investigation.
The walls are filled with water and air, and the walls are at a
specified reference temperature. Except for the mass
density, which varies according to the Boussinesq
approximation, the thermo-physical parameters of the
working fluid are considered to remain constant.Thefluid is
taken to be Newtonian and incompressible.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 400
Fig. 1: Problem Formulation
3. MATHEMATICAL FORMULATION
Assumptions are two – dimensional steady incompressible
Newtonian laminar flow. The gravity force is neglected.
Applying the conservations principles of mass, momentum
and energy, the continuity,momentumandenergyequations
are written as,
(1)
(2)
(3)
(4)
The above – mentioneddimensional governing equations are
transformed into the non – dimensional equations as
expressed below,
(5)
(6)
(7)
(8)
Here, the transformation of primitive variables (u, v, p, T)
is made on the basis of certain scales as given by,
,
, (9)
,
4. NUMERICAL ASPECTS
The acronym for computational fluid dynamics is CFD. This
area of fluid mechanics uses numerical techniques and
algorithms to investigate and solve problems involvingfluid
flows. CFD has evolved into a strong tool in engineering and
scientific research for modeling fluid (liquids and gases)
behavior in a variety of applications. Here we are using the
CFD domain for fluid flow and heat transfer enhancement in
a rectangular channel.
Fig. 2: Meshing Model
For analysis purpose we are using the COMSOLMultiphysics
5.6 version and choosing the domain of computational fluid
dynamics. The model we are using has a physics-controlled
mesh sequence with fine element sizes.
5. RESULTS AND DISCUSSION
Under the result section the color filled magnitude plot,
absolute velocity & streamlines contour plot are given.
L
H
x, u
y, v
Adiabatic
Adiabatic
Fluid – filled
LID – DRIVEN CAVITY
(u, v, p)
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 401
Fig.3: Color filled magnitude plot: Absolute velocity (Pr=0.71, 5.83)
Re=10 Re=100 Re=500
Fig.4: Absolute velocity contour plot
Re=10 Re=100 Re=500
Fig.5: Streamlines contour plot
Re=10 Re=100 Re=500
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 402
Re=10 Re=100 Re=500
Pr
=
0.71
Pr
=
5.83
Re=10 Re=100 Re=500
Pr
=
0.71
Fig.6: Temperature surface plot
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 403
Fig.7: Isotherm plot (Pr =0.71, 5.83)
Figure 3 shows the color filled magnitude plot of absolute
velocity where the plot of absolute velocity is same for both
air (Pr= 0.71) and water (Pr= 5.83) Prandtl number. For the
whole study we are taking basically three types of Reynolds
number (Re= 10, 100 & 500). In the figure 4, it shows the
absolute velocity contour plot and figure 5 shows the
Streamlines contour plot. In figure 6 and 7 it shows the
temperature surface plot and isotherm plot. In figure 6, we
fixed the Reynolds number but for Prandtl numbervariation
it shows the different contour.
Fig.8: Trend of average Nusselt number (Nu) at the hot
wall
6. CONCLUSIONS
We investigate the forced convection and heat transfer in a
rectangular channel using computational fluid dynamics.
Analyzing laminar fluid flow and transient results provides
valuable insights into CFD phenomena. The results shows
that fluid flow patterns are independent of Prandtl number
(as Pr is absence in the momentum equations). And the
thermal aspects significantly affected by Re as well as Pr.
Enhance convective flow has profound impact on the
enhancement of heat transfer and nonlinear static
temperature distribution.
7. REFERENCES
[1] J. V. Indukuri and R. Maniyeri, “Numerical study of
forced convection heat transfer in an oscillating lid
driven cavity with heated top wall,” Int. J. Heat
Technol., vol. 36, no. 4, pp. 1378–1387, 2018, doi:
10.18280/ijht.360429.
[2] A. Boutra, K. Ragui, N. Labsi, and Y. K. Benkahla, “Lid-
driven and inclined square cavity filled with a
nanofluid: Optimum heat transfer,” Open Eng., vol. 5,
no. 1, pp. 248–255, 2015, doi: 10.1515/eng-2015-
0028.
[3] M. Manchanda and K. M. Gangawane, “Mixed
convection in a two-sided lid-driven cavity
containing heated triangular block for non-
Newtonian power-law fluids,” Int. J. Mech. Sci., vol.
144, no. June, pp. 235–248, 2018, doi:
10.1016/j.ijmecsci.2018.06.005.
[4] Heat and Mass Transfer, R.K. Rajput, year 2008
[5] Heat and Mass Transfer, P.K. Nag, year 2018
BIOGRAPHIES
Anjan Bhunia
B. Tech (Pursuing)
Dept. of Mechanical Engineering
College of Engineering &
Management, Kolaghat
Pr
=
5.83
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072
© 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 404
Souvik Maity
B. Tech (Pursuing)
Dept. of Mechanical Engineering
College of Engineering &
Management, Kolaghat
Anupam Santra
B. Tech (Pursuing)
Dept. of Mechanical Engineering
College of Engineering &
Management, Kolaghat
Sribas Samanta
B. Tech (Pursuing)
Dept. of Mechanical Engineering
College of Engineering &
Management, Kolaghat

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FORCED CONVECTIVE HEAT TRANSFER IN A LID-DRIVEN CAVITY

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 399 FORCED CONVECTIVE HEAT TRANSFER IN A LID-DRIVEN CAVITY Anjan Bhunia1, Souvik Maity1, Anupam Santra1, Sribas Samanta1 1Dept. of Mechanical Engineering, College of Engineering & Management, Kolaghat, India ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - This work deals with the processes of forced convective heat transfer within a lid-driven cavity, using numerical simulations to assess the thermal behavior under varied flow conditions. The lid-driven cavity is a traditional structure with several technical and industrial uses. The goal is to comprehend the complex interplay between fluid flow patterns and heat transmission within the hollow. The numerical simulations are carried out using a proven computational fluid dynamics (CFD) model, with the effects of Reynolds number and aspect ratio taken into account. Basically, this work consists Reynolds number (Re), Nusselt number (Nu) and Prandtl number (Pr). We are taking a rectangular channel whose top wall is moving and the working fluid of Prandtl number (Pr) equal to 0.71 and 5.83 is utilized for this study. Key Words: Forced convection; Rectangular channel; Heat generation; Lid-driven cavity; Reynolds number; Prandtl number NOMENCLATURE Nu Nusselt number Pr Prandtl Number Re Reynolds number 1. INTRODUCTION Forced convection within rectangular channel holds a great relevance in engineering applications such as heat exchangers,coolingsystems, andotherthermal management equipment. The practical ramifications of this research include the design and optimization of rectangular channel heat exchangers, cooling systems, and other thermal management equipment. By utilizing forced convection inside rectangular geometries, the findingsofthisstudyhelp to the creation of efficient and sustainable engineering solutions. Prior studies have looked into heat transfer enhancement in an inclined square cavity filled with nanofluid, heat transfer in a two-sided Lid-driven cavity filled with volumetrically heat-generatingporousmedia,etc. Basically, this work deals with Nusselt number (Nu) and Prandtl number (Pr). Nusselt number (Nu) is the ratio of heat flow rate by convection and heat flow rate by conduction. For forced convection, NuisindependentofGrashofnumber. And the Prandtl number (Pr) is the ratio of kinematic and dynamic viscosity. For air, Pr =0.71 For water, Pr =5.83 2. PROBLEM FORMULATION This study deals into captivating domain of computational fluid dynamics (CFD) within a rectangular channel. A rectangular channel with the dimension of height (H) 1m and length (L) of 1m. The top wall of the channel is maintaining the no slip condition while traveling continuously in the positive x-direction. The other walls are stationary. The upper and lower wall of the rectangular channel is insulated and other two side wall is one heating wall and another is cooling wall.TheworkingfluidofPrandtl number (Pr) equals to 0.71 and 5.83 are utilized for this investigation. The walls are filled with water and air, and the walls are at a specified reference temperature. Except for the mass density, which varies according to the Boussinesq approximation, the thermo-physical parameters of the working fluid are considered to remain constant.Thefluid is taken to be Newtonian and incompressible.
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 400 Fig. 1: Problem Formulation 3. MATHEMATICAL FORMULATION Assumptions are two – dimensional steady incompressible Newtonian laminar flow. The gravity force is neglected. Applying the conservations principles of mass, momentum and energy, the continuity,momentumandenergyequations are written as, (1) (2) (3) (4) The above – mentioneddimensional governing equations are transformed into the non – dimensional equations as expressed below, (5) (6) (7) (8) Here, the transformation of primitive variables (u, v, p, T) is made on the basis of certain scales as given by, , , (9) , 4. NUMERICAL ASPECTS The acronym for computational fluid dynamics is CFD. This area of fluid mechanics uses numerical techniques and algorithms to investigate and solve problems involvingfluid flows. CFD has evolved into a strong tool in engineering and scientific research for modeling fluid (liquids and gases) behavior in a variety of applications. Here we are using the CFD domain for fluid flow and heat transfer enhancement in a rectangular channel. Fig. 2: Meshing Model For analysis purpose we are using the COMSOLMultiphysics 5.6 version and choosing the domain of computational fluid dynamics. The model we are using has a physics-controlled mesh sequence with fine element sizes. 5. RESULTS AND DISCUSSION Under the result section the color filled magnitude plot, absolute velocity & streamlines contour plot are given. L H x, u y, v Adiabatic Adiabatic Fluid – filled LID – DRIVEN CAVITY (u, v, p)
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 401 Fig.3: Color filled magnitude plot: Absolute velocity (Pr=0.71, 5.83) Re=10 Re=100 Re=500 Fig.4: Absolute velocity contour plot Re=10 Re=100 Re=500 Fig.5: Streamlines contour plot Re=10 Re=100 Re=500
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 402 Re=10 Re=100 Re=500 Pr = 0.71 Pr = 5.83 Re=10 Re=100 Re=500 Pr = 0.71 Fig.6: Temperature surface plot
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 403 Fig.7: Isotherm plot (Pr =0.71, 5.83) Figure 3 shows the color filled magnitude plot of absolute velocity where the plot of absolute velocity is same for both air (Pr= 0.71) and water (Pr= 5.83) Prandtl number. For the whole study we are taking basically three types of Reynolds number (Re= 10, 100 & 500). In the figure 4, it shows the absolute velocity contour plot and figure 5 shows the Streamlines contour plot. In figure 6 and 7 it shows the temperature surface plot and isotherm plot. In figure 6, we fixed the Reynolds number but for Prandtl numbervariation it shows the different contour. Fig.8: Trend of average Nusselt number (Nu) at the hot wall 6. CONCLUSIONS We investigate the forced convection and heat transfer in a rectangular channel using computational fluid dynamics. Analyzing laminar fluid flow and transient results provides valuable insights into CFD phenomena. The results shows that fluid flow patterns are independent of Prandtl number (as Pr is absence in the momentum equations). And the thermal aspects significantly affected by Re as well as Pr. Enhance convective flow has profound impact on the enhancement of heat transfer and nonlinear static temperature distribution. 7. REFERENCES [1] J. V. Indukuri and R. Maniyeri, “Numerical study of forced convection heat transfer in an oscillating lid driven cavity with heated top wall,” Int. J. Heat Technol., vol. 36, no. 4, pp. 1378–1387, 2018, doi: 10.18280/ijht.360429. [2] A. Boutra, K. Ragui, N. Labsi, and Y. K. Benkahla, “Lid- driven and inclined square cavity filled with a nanofluid: Optimum heat transfer,” Open Eng., vol. 5, no. 1, pp. 248–255, 2015, doi: 10.1515/eng-2015- 0028. [3] M. Manchanda and K. M. Gangawane, “Mixed convection in a two-sided lid-driven cavity containing heated triangular block for non- Newtonian power-law fluids,” Int. J. Mech. Sci., vol. 144, no. June, pp. 235–248, 2018, doi: 10.1016/j.ijmecsci.2018.06.005. [4] Heat and Mass Transfer, R.K. Rajput, year 2008 [5] Heat and Mass Transfer, P.K. Nag, year 2018 BIOGRAPHIES Anjan Bhunia B. Tech (Pursuing) Dept. of Mechanical Engineering College of Engineering & Management, Kolaghat Pr = 5.83
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 10 Issue: 11 | Nov 2023 www.irjet.net p-ISSN: 2395-0072 © 2023, IRJET | Impact Factor value: 8.226 | ISO 9001:2008 Certified Journal | Page 404 Souvik Maity B. Tech (Pursuing) Dept. of Mechanical Engineering College of Engineering & Management, Kolaghat Anupam Santra B. Tech (Pursuing) Dept. of Mechanical Engineering College of Engineering & Management, Kolaghat Sribas Samanta B. Tech (Pursuing) Dept. of Mechanical Engineering College of Engineering & Management, Kolaghat