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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2946
CONTROL OF HYDRAULIC FORCES ON A SQUARE AND CIRCULAR
CYLINDER USING MULTI-ELEMENT SPLITTER PLATE
Alex Jacob1, Arun Abraham2, Arun Omanakuttan3, Ebin V Edison4, Assi. Prof. Arun Jose5
1,2,3,4 Btech students, Department of Mechanical Engineering, Mangalam College Of Engineering, Kerala,
India686631
5,Faculty, Department of Mechanical Engineering, Mangalam College Of Engineering ,Kerala, India-686631
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract- Vortex shedding is an oscillating flow that takes
place when a fluid such as air or water flows past a bluff
body. Von Karman vortex shedding is a repeating pattern
of swirling vortices caused by vortex shedding. The vortex
regime behind the body has a lower pressure in its core
when compared to the freestream velocity which creates a
lift force (FL) and the pressure field at the rear part of the
body creates drag force.
The proposed project involves numerical analysis (two
dimensional) of vortex structure behind the square and
circular cylinder. Splitter plate has considerable effect in
stabilizing the transverse flow behind the body by
rearranging the vortex street. The current works involves
optimizing the splitter plate configuration by using
different values of D/H(0, 1, 1.5,2.0) and employing multi-
element splitter plate. The width of the splitter plate is
taken as 30mm and its thickness as 2mm to minimize flow
interaction. Numerical flow visualization is carried out
using transient simulation and the numerical simulation is
carried out in ANSYS FLUENT with an inlet condition of
Re=1.0×104 taking the gap between the square cylinder
and splitter plate and angle of splitter plate as a variable
geometric parameter. The project is aimed at numerically
investigating the reduction in lift coefficient (CL) in various
splitter plate configurations and using the results to
evaluate the potential benefits of employing multi-element
splitter plate configuration.
1.INTRODUCTION
This project deals with variation of different hydraulic
properties such as pressure, velocity and streamline. These
variations are analyzed in different configurations. These
different configurations are arranged with a ratio of
diameter/side length and distance between cylinder and
splitter plate. The proposed project involves numerical
analysis (two dimensional) of vortex structure behind the
square and circular cylinder. Splitter plate has considerable
effect in stabilizing the transverse flow behind the body by
rearranging the vortex street. The current works involves
optimizing the splitter plate configuration by using
different values of D/H (0, 1, 1.5,2.0) and employing multi-
element splitter plate. The width of the splitter plate is
taken as 30mm and its thickness as 2mm to minimize flow
interaction. The project is aimed at numerically
investigating the reduction in lift coefficient (CL) in various
splitter plate configurations and using the results to
evaluate the potential benefits of employing multi-element
splitter plate configuration.
2. Literature review
2.1 reduction of fluid forces and vortex shedding
frequency of a circular cylinder using rigid splitter
plates.
Rezvan Abdi et.al (2017) conducted a study on reduction of
fluid forces and vortex shedding frequency of a circular
cylinder using rigid splitter plates. A comprehensive
parametric study was performed to identify the optimum
arrangement of the plates using the commercial finite
element software, Comsol Multiphysics. The results show
that the location and the number of the plates have crucial
effects on the wake control.
2.2 Active control of the hydraulic forces of a body by a
splitter plate.
Norio Arai and Masatomo Komatsu (1991) investigated on
active control of the hydraulic forces of a body by a splitter
plate.The two-dimensional incompressible Navier-Stokes
equation is solved numerically. The interaction between
the transverse flow (behind the body) and the splitter has
considerable influence on the rearrangement of the vortex
street. With the splitter plate suitably located, the peak of
the lift coefficient is reduced to 40% of the isolated body
case. Also, the frequency of the variation of the lift
coefficient becomes smaller. It is found that there is an
optimal location for the splitter plate.
2.3 Bifurcation analysis of flow over a rotatable
cylinder with a splitter plate.
J. Xu et.al, (1991) conducted a bifurcation analysis of flow
over a rotatable cylinder with a splitter plate. The two-
dimensional, incompressible, unsteady Navier-Stokes
equations expressed in stream function and vorticity are
solved by using a finite-difference method on a numerically
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2947
generated, boundary-fitted and moving curvilinear
coordinate system. Detailed study of the flow field suggests
that the observed offsetting of the plate are mostly
influenced by the separation process behind the body.
2.4 Suppression of vortex shedding of circular cylinder
in shallow water by a splitter plate.
Huseyin Akilli et.al, (2005) conducted a study on
suppression of vortex shedding of circular cylinder in
shallow water by a splitter plate. The flow behavior around
a vertical circular cylinder placed in shallow water was
controlled by a splitter plate inserted at various locations
downstream of the cylinder. The splitter plate has a
substantial effect on the suppression of the vortex
shedding for the gap ratio (G/D) between 0 and 1.
METHODOLOGY
1. Study of CFD tools.
2. Literature review.
3. Modelling and Meshing of the configuration.
4. Numerical flow visualization of vortex structures
without splitter plate.
5. Numerical flow visualization of vortex structures
with various splitter plate configuration.
6. Theoretical study of vortex structures.
7. Investigating the influence of multi-element
splitter plate.
Ansys tools and taken parameters.
Sl.no Ansys tool Taken as:-
1 Type of flow Transient
2 Step time 0.025s
3 Time steps 600
4 Scheme of
equations
SIMPLE
Table-2.2, Fluid properties taken.
Different configurations used.
Sl.no Diameter
(D)
(mm)
Distance between bluff
body and splitter plate
(H) (mm)
D/H
ratio
1 10 0 0
2 10 20 0.5
3 10 10 1
Table-3, Configurations of bluff body and splitter
plate.
MESH
Square cylinder
Object Name Mesh
State Solved
Display
Display Style Body Color
Defaults
Physics Preference CFD
Solver Preference Fluent
Relevance 0
Export Format Standard
Element Order Linear
Sizing
Size Function Curvature
Relevance Center Coarse
Span Angle Center Fine
Curvature Normal Angle Default (18.0 °)
Min Size Default (1.5958e-004 m)
Max Face Size Default (1.5958e-002 m)
Growth Rate Default (1.20 )
Automatic Mesh Based On
Sl.no Fluid
property
Assigned
value
Unit
1 Fluid density 1000 Kg/m3
2 Fluid velocity 10 m/s
3 Kinematic
viscosity
0.001 Pa.s
4 Reynold’s
number
2 * 105
FLUID PROPERTIES
Table-2.1, Ansys tools and taken parameters.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2948
Defeaturing
Defeature Size Default (7.9789e-005 m)
Minimum Edge Length 1.e-003 m
Quality
Check Mesh Quality Yes, Errors
Target Skewness Default (0.900000)
Smoothing Medium
Mesh Metric None
Inflation
Use Automatic Inflation None
Inflation Option Smooth Transition
Transition Ratio 0.272
Maximum Layers 2
Growth Rate 1.2
Inflation Algorithm Pre
View Advanced Options No
Assembly Meshing
Method None
Advanced
Number of CPUs for
Parallel Part Meshing
Program Controlled
Straight Sided Elements
Number of Retries 0
Rigid Body Behavior Dimensionally Reduced
Mesh Morphing Disabled
Triangle Surface Mesher Program Controlled
Topology Checking No
Use Sheet Thickness for
Pinch
No
Pinch Tolerance Default (1.4362e-004 m)
Generate Pinch on Refresh No
Sheet Loop Removal No
Statistics
Nodes 50137
Elements 49634
Circular cylinder
Object Name Mesh
State Solved
Display
Display Style Body Color
Defaults
Physics Preference CFD
Solver Preference Fluent
Relevance 0
Export Format Standard
Element Order Linear
Sizing
Size Function Curvature
Relevance Center Coarse
Span Angle Center Fine
Curvature Normal Angle Default (18.0 °)
Min Size Default (1.5958e-004
m)
Max Face Size Default (1.5958e-002
m)
Growth Rate Default (1.20 )
Automatic Mesh Based
Defeaturing
On
Defeature Size Default (7.9789e-005
m)
Minimum Edge Length 1.e-003 m
Quality
Check Mesh Quality Yes, Errors
Target Skewness Default (0.900000)
Smoothing Medium
Mesh Metric None
Inflation
Use Automatic Inflation None
Inflation Option Smooth Transition
Transition Ratio 0.272
Maximum Layers 2
Growth Rate 1.2
Inflation Algorithm Pre
View Advanced Options No
Assembly Meshing
Method None
Advanced
Number of CPUs for Parallel
Part Meshing
Program Controlled
Straight Sided Elements
Number of Retries 0
Rigid Body Behavior Dimensionally
Reduced
Mesh Morphing Disabled
Triangle Surface Mesher Program Controlled
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2949
Topology Checking No
Use Sheet Thickness for Pinch No
Pinch Tolerance Default (1.4362e-004
m)
Generate Pinch on Refresh No
Sheet Loop Removal No
Statistics
Nodes 50298
Elements 49812
Simulation
For stimulation activates we are using ANSYS software. The
requirements of the boundary condition will be asked
according to the name information in meshing.
Figure-8.1 Pressure contour in all cases.
Figure-8.2 Streamlines in all cases.
Figure-8.3 Velocity contour in all cases.
Result and Analysis
We use CFD Post for result and post processing. Here we
compare the result of flow of water in a Reynold’s number
of 2 * 105.
9.1Graphical results and result comparison
9.1.1 Graph of pressure on the body
Figure-9.1.1 Graph of pressure on the body.
The graph shown above shows the variation of pressure
with distance from the body to right. The point taken as
zero is the right most point in the body. The colour code is
defined below.
 ______ The red line indicates the pressure exerted on
the circular cylinder with no splitter plate.
 ______ The blue line indicates the pressure exerted
on the circular cylinder with splitter plate in a D/H
ratio of 1.0.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2950
 ______ The green line indicates the pressure exerted
on the square cylinder with no splitter plate.
 ______ The pink line indicates the pressure exerted
on the circular cylinder with splitter plate in a D/H
ratio of 1.0.
9.1.2 Pressure comparison
Table-9.1.2 Pressure comparison.
9.1.3 Graph on transient pressure
Figure-9.1.2 Graph on transient pressure.
The graph shown above shows the variation of pressure
with distance from the body to right. The point taken as
zero is the right most point in the body. The colour code is
defined below.
 ______ The red line indicates the pressure exerted on
the circular cylinder with no splitter plate.
 ______ The blue line indicates the pressure exerted
on the circular cylinder with splitter plate in a D/H
ratio of 1.0.
 ______ The green line indicates the pressure exerted
on the square cylinder with no splitter plate.
 ______ The pink line indicates the pressure exerted
on the circular cylinder with splitter plate in a D/H
ratio of 1.0.
9.1.4 Transient pressure comparison
Sl.
no
Geometry Config
uration
(D/H)
Maximu
m
amplitud
e after 8s
(Pa)
Minimum
amplitude
after 8s
(Pa)
Variati
on
(Pa)
1 Square
cylinder
0 -50,000 -1,40,000 90,000
2 1 -40,000 -30,000 -
10,000
3 Circular
cylinder
0 -15,000 -25,000 10,000
4 1 -15,000 -15,000 0
Table-9.1.4 Transient pressure comparison.
9.1.5 Variation of lift force in circular cylinder with no
splitter plate.
Figure-9.1.5 Variation of lift force in circular cylinder
with no splitter plate.
Sl
no.
Geometr
y
Config
uratio
n
D/H
Pressure
at
reference
point
Y=0
(Pa)
Pressure
at
maximum
of
variation
Y=8 mm
(Pa)
Variation
(Pa)
1
Square
cylinder
0 -55,000 -70,000 15000
2 1 -95,000 -50,000 -45000
3 Circular
cylinder
0 -20,000 -15,000 -5000
4 1 -15,000 -15,000 0
The graph shown above shows the variation of lift force in
circular cylinder with no splitter plate. There is an average
amplitude of -225N and -475N. So a mean variation of
250N is obtained.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2951
Figure-9.1.6 Variation of lift force in circular cylinder with
splitter plate in a D/H ratio of 1.0.
The graph shown above shows the variation of lift force in
circular cylinder with splitter plate in a D/H ratio of 1.0.
There is an average amplitude of -86.75N and -86.75N. So
there is no variation at all.
9.1.7 Variation of lift force in square cylinder with no
splitter plate.
Figure-9.1.7 Variation of lift force in square cylinder with
no splitter plate.
The graph shown above shows the variation of lift force in
square cylinder with no splitter plate. There is an average
amplitude of 225N and -250N. So a mean variation of 475N
is obtained.
9.1.8 Variation of lift force in square cylinder with
splitter plate in a D/H ratio of 1.0.
Figure-9.1.8 Variation of lift force in square cylinder
with splitter plate in a D/H ratio of 1.0.
The graph shown above shows the variation of lift force in
square cylinder with splitter plate in a D/H ratio of 1.0.
There is an average amplitude of 350N and -375N. So a
mean variation of 250N is obtained.
9.1.9 Lift force comparison
Table-9.1.9 Lift force comparison.
Conclusion
Sl.n
o
Geometr
y
Configu
ration
(D/H)
Maximum
amplitude
after first
cycle
(N)
Minimum
amplitude
after first
cycle
(N)
Variati
on
(N)
1 Square
cylinder
0 225 -250 475
2 1 350 -375 725
3 Circular
cylinder
0 -225 -475 250
4 1 -86.75 -86.75 0
In the isolated case, it is observed that the von Karman
vortex street generates alternately and regularly. When the
gap is small, the shed vortex collides with the splitter plate
and is prevented from growing. This causes a reduction in
the peak values of the lift and drag coefficients. It seems
that the reduction in the peak value of the lift coefficient is
caused by the rearrangement of, the vortices due to the
splitter plate. When the gap becomes wider, vortices occur
between the bodies and the wake is reattached.
9.1.6 Variation of lift force in circular cylinder with
splitter plate in a D/H ratio of 1.0.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072
placing a multi-element splitter plate at a distance as same
as the diameter of the circular cylinder. Even though
splitter plates are used, vortex suppression was low for
square cylinder.
When a circular cylinder is placed in a flow of Reynold’s
number of 2*105 with an accompany by a splitter plate
placed in a distance which is equal to the diameter of the
cylinder, the flow is maintained in a stable condition.
Properties like lift, pressure, velocity and streamline has no
changes experienced. It is almost equal to a laminar flow.
But in case of a square cylinder, even splitter plates are
present, changes have been occurred.it was not a negligible
one.
Reference
1. Rezvan Abdi et.al, Reduction of fluid forces and vortex
shedding frequency of a circular cylinder using rigid
splitter plates, European Journal of Computational
Mechanics, volume 26, page 225-244, 2017
2. Norio Arai and Masatomo Komatsu, Active control of
the hydraulic forces of a body by a splitter plate,
Computers Fluids Vol. 21, No. 2, pp. 145-150, 1992.
3. J. Xu et.al, Bifurcation Analysis Of Flow Over A
Rotatable Cylinder With A Splitter Plate, AIAA-1738,
1991.
4. Huseyin Akilli et.al, Suppression of vortex shedding of
circular cylinder in shallow water by a splitter plate,
Flow Measurement and Instrumentation 16, 211–219,
2005.
5. Raghuraman N Go'Vardhan and 0 N Ramesh, A Stroll
down Karman Street, Resonance, Vo1.,S.No.12, 2000.
6. A. Roshko, NACA TN 3169 (1954).
7. J. H. Gerrard, J. Fluid Mech. 25, 401 (1966).
8. S. Hoerner, Fluid Dynamic Drag. Hoerner Fluid
Dynamics, pp. 3-12 (1965)
The variation of different flow properties pressure,
velocity and streamline are analysed. The vortex
suppression for different configurations are considered.
The maximum vortex suppression was obtained from
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page

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CONTROL OF HYDRAULIC FORCES ON A SQUARE AND CIRCULAR CYLINDER USING MULTI-ELEMENT SPLITTER PLATE

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2946 CONTROL OF HYDRAULIC FORCES ON A SQUARE AND CIRCULAR CYLINDER USING MULTI-ELEMENT SPLITTER PLATE Alex Jacob1, Arun Abraham2, Arun Omanakuttan3, Ebin V Edison4, Assi. Prof. Arun Jose5 1,2,3,4 Btech students, Department of Mechanical Engineering, Mangalam College Of Engineering, Kerala, India686631 5,Faculty, Department of Mechanical Engineering, Mangalam College Of Engineering ,Kerala, India-686631 ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract- Vortex shedding is an oscillating flow that takes place when a fluid such as air or water flows past a bluff body. Von Karman vortex shedding is a repeating pattern of swirling vortices caused by vortex shedding. The vortex regime behind the body has a lower pressure in its core when compared to the freestream velocity which creates a lift force (FL) and the pressure field at the rear part of the body creates drag force. The proposed project involves numerical analysis (two dimensional) of vortex structure behind the square and circular cylinder. Splitter plate has considerable effect in stabilizing the transverse flow behind the body by rearranging the vortex street. The current works involves optimizing the splitter plate configuration by using different values of D/H(0, 1, 1.5,2.0) and employing multi- element splitter plate. The width of the splitter plate is taken as 30mm and its thickness as 2mm to minimize flow interaction. Numerical flow visualization is carried out using transient simulation and the numerical simulation is carried out in ANSYS FLUENT with an inlet condition of Re=1.0×104 taking the gap between the square cylinder and splitter plate and angle of splitter plate as a variable geometric parameter. The project is aimed at numerically investigating the reduction in lift coefficient (CL) in various splitter plate configurations and using the results to evaluate the potential benefits of employing multi-element splitter plate configuration. 1.INTRODUCTION This project deals with variation of different hydraulic properties such as pressure, velocity and streamline. These variations are analyzed in different configurations. These different configurations are arranged with a ratio of diameter/side length and distance between cylinder and splitter plate. The proposed project involves numerical analysis (two dimensional) of vortex structure behind the square and circular cylinder. Splitter plate has considerable effect in stabilizing the transverse flow behind the body by rearranging the vortex street. The current works involves optimizing the splitter plate configuration by using different values of D/H (0, 1, 1.5,2.0) and employing multi- element splitter plate. The width of the splitter plate is taken as 30mm and its thickness as 2mm to minimize flow interaction. The project is aimed at numerically investigating the reduction in lift coefficient (CL) in various splitter plate configurations and using the results to evaluate the potential benefits of employing multi-element splitter plate configuration. 2. Literature review 2.1 reduction of fluid forces and vortex shedding frequency of a circular cylinder using rigid splitter plates. Rezvan Abdi et.al (2017) conducted a study on reduction of fluid forces and vortex shedding frequency of a circular cylinder using rigid splitter plates. A comprehensive parametric study was performed to identify the optimum arrangement of the plates using the commercial finite element software, Comsol Multiphysics. The results show that the location and the number of the plates have crucial effects on the wake control. 2.2 Active control of the hydraulic forces of a body by a splitter plate. Norio Arai and Masatomo Komatsu (1991) investigated on active control of the hydraulic forces of a body by a splitter plate.The two-dimensional incompressible Navier-Stokes equation is solved numerically. The interaction between the transverse flow (behind the body) and the splitter has considerable influence on the rearrangement of the vortex street. With the splitter plate suitably located, the peak of the lift coefficient is reduced to 40% of the isolated body case. Also, the frequency of the variation of the lift coefficient becomes smaller. It is found that there is an optimal location for the splitter plate. 2.3 Bifurcation analysis of flow over a rotatable cylinder with a splitter plate. J. Xu et.al, (1991) conducted a bifurcation analysis of flow over a rotatable cylinder with a splitter plate. The two- dimensional, incompressible, unsteady Navier-Stokes equations expressed in stream function and vorticity are solved by using a finite-difference method on a numerically
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2947 generated, boundary-fitted and moving curvilinear coordinate system. Detailed study of the flow field suggests that the observed offsetting of the plate are mostly influenced by the separation process behind the body. 2.4 Suppression of vortex shedding of circular cylinder in shallow water by a splitter plate. Huseyin Akilli et.al, (2005) conducted a study on suppression of vortex shedding of circular cylinder in shallow water by a splitter plate. The flow behavior around a vertical circular cylinder placed in shallow water was controlled by a splitter plate inserted at various locations downstream of the cylinder. The splitter plate has a substantial effect on the suppression of the vortex shedding for the gap ratio (G/D) between 0 and 1. METHODOLOGY 1. Study of CFD tools. 2. Literature review. 3. Modelling and Meshing of the configuration. 4. Numerical flow visualization of vortex structures without splitter plate. 5. Numerical flow visualization of vortex structures with various splitter plate configuration. 6. Theoretical study of vortex structures. 7. Investigating the influence of multi-element splitter plate. Ansys tools and taken parameters. Sl.no Ansys tool Taken as:- 1 Type of flow Transient 2 Step time 0.025s 3 Time steps 600 4 Scheme of equations SIMPLE Table-2.2, Fluid properties taken. Different configurations used. Sl.no Diameter (D) (mm) Distance between bluff body and splitter plate (H) (mm) D/H ratio 1 10 0 0 2 10 20 0.5 3 10 10 1 Table-3, Configurations of bluff body and splitter plate. MESH Square cylinder Object Name Mesh State Solved Display Display Style Body Color Defaults Physics Preference CFD Solver Preference Fluent Relevance 0 Export Format Standard Element Order Linear Sizing Size Function Curvature Relevance Center Coarse Span Angle Center Fine Curvature Normal Angle Default (18.0 °) Min Size Default (1.5958e-004 m) Max Face Size Default (1.5958e-002 m) Growth Rate Default (1.20 ) Automatic Mesh Based On Sl.no Fluid property Assigned value Unit 1 Fluid density 1000 Kg/m3 2 Fluid velocity 10 m/s 3 Kinematic viscosity 0.001 Pa.s 4 Reynold’s number 2 * 105 FLUID PROPERTIES Table-2.1, Ansys tools and taken parameters.
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2948 Defeaturing Defeature Size Default (7.9789e-005 m) Minimum Edge Length 1.e-003 m Quality Check Mesh Quality Yes, Errors Target Skewness Default (0.900000) Smoothing Medium Mesh Metric None Inflation Use Automatic Inflation None Inflation Option Smooth Transition Transition Ratio 0.272 Maximum Layers 2 Growth Rate 1.2 Inflation Algorithm Pre View Advanced Options No Assembly Meshing Method None Advanced Number of CPUs for Parallel Part Meshing Program Controlled Straight Sided Elements Number of Retries 0 Rigid Body Behavior Dimensionally Reduced Mesh Morphing Disabled Triangle Surface Mesher Program Controlled Topology Checking No Use Sheet Thickness for Pinch No Pinch Tolerance Default (1.4362e-004 m) Generate Pinch on Refresh No Sheet Loop Removal No Statistics Nodes 50137 Elements 49634 Circular cylinder Object Name Mesh State Solved Display Display Style Body Color Defaults Physics Preference CFD Solver Preference Fluent Relevance 0 Export Format Standard Element Order Linear Sizing Size Function Curvature Relevance Center Coarse Span Angle Center Fine Curvature Normal Angle Default (18.0 °) Min Size Default (1.5958e-004 m) Max Face Size Default (1.5958e-002 m) Growth Rate Default (1.20 ) Automatic Mesh Based Defeaturing On Defeature Size Default (7.9789e-005 m) Minimum Edge Length 1.e-003 m Quality Check Mesh Quality Yes, Errors Target Skewness Default (0.900000) Smoothing Medium Mesh Metric None Inflation Use Automatic Inflation None Inflation Option Smooth Transition Transition Ratio 0.272 Maximum Layers 2 Growth Rate 1.2 Inflation Algorithm Pre View Advanced Options No Assembly Meshing Method None Advanced Number of CPUs for Parallel Part Meshing Program Controlled Straight Sided Elements Number of Retries 0 Rigid Body Behavior Dimensionally Reduced Mesh Morphing Disabled Triangle Surface Mesher Program Controlled
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2949 Topology Checking No Use Sheet Thickness for Pinch No Pinch Tolerance Default (1.4362e-004 m) Generate Pinch on Refresh No Sheet Loop Removal No Statistics Nodes 50298 Elements 49812 Simulation For stimulation activates we are using ANSYS software. The requirements of the boundary condition will be asked according to the name information in meshing. Figure-8.1 Pressure contour in all cases. Figure-8.2 Streamlines in all cases. Figure-8.3 Velocity contour in all cases. Result and Analysis We use CFD Post for result and post processing. Here we compare the result of flow of water in a Reynold’s number of 2 * 105. 9.1Graphical results and result comparison 9.1.1 Graph of pressure on the body Figure-9.1.1 Graph of pressure on the body. The graph shown above shows the variation of pressure with distance from the body to right. The point taken as zero is the right most point in the body. The colour code is defined below.  ______ The red line indicates the pressure exerted on the circular cylinder with no splitter plate.  ______ The blue line indicates the pressure exerted on the circular cylinder with splitter plate in a D/H ratio of 1.0.
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2950  ______ The green line indicates the pressure exerted on the square cylinder with no splitter plate.  ______ The pink line indicates the pressure exerted on the circular cylinder with splitter plate in a D/H ratio of 1.0. 9.1.2 Pressure comparison Table-9.1.2 Pressure comparison. 9.1.3 Graph on transient pressure Figure-9.1.2 Graph on transient pressure. The graph shown above shows the variation of pressure with distance from the body to right. The point taken as zero is the right most point in the body. The colour code is defined below.  ______ The red line indicates the pressure exerted on the circular cylinder with no splitter plate.  ______ The blue line indicates the pressure exerted on the circular cylinder with splitter plate in a D/H ratio of 1.0.  ______ The green line indicates the pressure exerted on the square cylinder with no splitter plate.  ______ The pink line indicates the pressure exerted on the circular cylinder with splitter plate in a D/H ratio of 1.0. 9.1.4 Transient pressure comparison Sl. no Geometry Config uration (D/H) Maximu m amplitud e after 8s (Pa) Minimum amplitude after 8s (Pa) Variati on (Pa) 1 Square cylinder 0 -50,000 -1,40,000 90,000 2 1 -40,000 -30,000 - 10,000 3 Circular cylinder 0 -15,000 -25,000 10,000 4 1 -15,000 -15,000 0 Table-9.1.4 Transient pressure comparison. 9.1.5 Variation of lift force in circular cylinder with no splitter plate. Figure-9.1.5 Variation of lift force in circular cylinder with no splitter plate. Sl no. Geometr y Config uratio n D/H Pressure at reference point Y=0 (Pa) Pressure at maximum of variation Y=8 mm (Pa) Variation (Pa) 1 Square cylinder 0 -55,000 -70,000 15000 2 1 -95,000 -50,000 -45000 3 Circular cylinder 0 -20,000 -15,000 -5000 4 1 -15,000 -15,000 0 The graph shown above shows the variation of lift force in circular cylinder with no splitter plate. There is an average amplitude of -225N and -475N. So a mean variation of 250N is obtained.
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 2951 Figure-9.1.6 Variation of lift force in circular cylinder with splitter plate in a D/H ratio of 1.0. The graph shown above shows the variation of lift force in circular cylinder with splitter plate in a D/H ratio of 1.0. There is an average amplitude of -86.75N and -86.75N. So there is no variation at all. 9.1.7 Variation of lift force in square cylinder with no splitter plate. Figure-9.1.7 Variation of lift force in square cylinder with no splitter plate. The graph shown above shows the variation of lift force in square cylinder with no splitter plate. There is an average amplitude of 225N and -250N. So a mean variation of 475N is obtained. 9.1.8 Variation of lift force in square cylinder with splitter plate in a D/H ratio of 1.0. Figure-9.1.8 Variation of lift force in square cylinder with splitter plate in a D/H ratio of 1.0. The graph shown above shows the variation of lift force in square cylinder with splitter plate in a D/H ratio of 1.0. There is an average amplitude of 350N and -375N. So a mean variation of 250N is obtained. 9.1.9 Lift force comparison Table-9.1.9 Lift force comparison. Conclusion Sl.n o Geometr y Configu ration (D/H) Maximum amplitude after first cycle (N) Minimum amplitude after first cycle (N) Variati on (N) 1 Square cylinder 0 225 -250 475 2 1 350 -375 725 3 Circular cylinder 0 -225 -475 250 4 1 -86.75 -86.75 0 In the isolated case, it is observed that the von Karman vortex street generates alternately and regularly. When the gap is small, the shed vortex collides with the splitter plate and is prevented from growing. This causes a reduction in the peak values of the lift and drag coefficients. It seems that the reduction in the peak value of the lift coefficient is caused by the rearrangement of, the vortices due to the splitter plate. When the gap becomes wider, vortices occur between the bodies and the wake is reattached. 9.1.6 Variation of lift force in circular cylinder with splitter plate in a D/H ratio of 1.0.
  • 7. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 06 | June 2022 www.irjet.net p-ISSN: 2395-0072 placing a multi-element splitter plate at a distance as same as the diameter of the circular cylinder. Even though splitter plates are used, vortex suppression was low for square cylinder. When a circular cylinder is placed in a flow of Reynold’s number of 2*105 with an accompany by a splitter plate placed in a distance which is equal to the diameter of the cylinder, the flow is maintained in a stable condition. Properties like lift, pressure, velocity and streamline has no changes experienced. It is almost equal to a laminar flow. But in case of a square cylinder, even splitter plates are present, changes have been occurred.it was not a negligible one. Reference 1. Rezvan Abdi et.al, Reduction of fluid forces and vortex shedding frequency of a circular cylinder using rigid splitter plates, European Journal of Computational Mechanics, volume 26, page 225-244, 2017 2. Norio Arai and Masatomo Komatsu, Active control of the hydraulic forces of a body by a splitter plate, Computers Fluids Vol. 21, No. 2, pp. 145-150, 1992. 3. J. Xu et.al, Bifurcation Analysis Of Flow Over A Rotatable Cylinder With A Splitter Plate, AIAA-1738, 1991. 4. Huseyin Akilli et.al, Suppression of vortex shedding of circular cylinder in shallow water by a splitter plate, Flow Measurement and Instrumentation 16, 211–219, 2005. 5. Raghuraman N Go'Vardhan and 0 N Ramesh, A Stroll down Karman Street, Resonance, Vo1.,S.No.12, 2000. 6. A. Roshko, NACA TN 3169 (1954). 7. J. H. Gerrard, J. Fluid Mech. 25, 401 (1966). 8. S. Hoerner, Fluid Dynamic Drag. Hoerner Fluid Dynamics, pp. 3-12 (1965) The variation of different flow properties pressure, velocity and streamline are analysed. The vortex suppression for different configurations are considered. The maximum vortex suppression was obtained from © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page