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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 359
Comparative Study Between Cross Flow Air To Air Plate Fin Heat
Exchanger With Triangular Fins And Triangular Perforated Fins And
Optimization Using Taguchi Analysis. , Heat recovery and importance of
ventilation.
Mansoor Imtiyaz1, Shilpa Mondkar²
1Student, Dept. of Mechanical Engineering, Pillai College of Engineering, Maharashtra, India
2Asst. Professor, Dept. of Mechanical Engineering, Pillai College of Engineering, Maharashtra, India
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract – Indoor Air Quality (IAQ) is a term which we get
to hear a lot after the commencement of the coronavirus
pandemic. Heat recovery ventilation (HRV) can play a very
important role in this. The fresh air from the ambient is
separated from the stale air exhausted from the indoor
facilities. Due to this the fresh air is not contaminated by the
moisture, dust, pathogens, particulate matters, pollutants,
smoke, smell etc. which is exhausted directly from the
indoors and only heat transfer takes place further
decreasing the load on HVAC systems. Computational fluid
dynamics analysis between conventional plate fin heat
exchanger model with triangular extended surfaces and
proposed perforated model was performed and the
comparative characteristics where studied. In order to
maximize the parameter such as thermal effectiveness,
recovered heat, outlet temperatures, Taguchi analysis was
implemented using the L9 orthogonal array. The design
variables and levels that would maximize the thermal
effectiveness and other factors were plate thickness, velocity
of fluid and plate height.
Keywords-- Plate Fin Heat Exchanger, Taguchi Analysis,
Heat Recovery Ventilation, Computational Fluid
Dynamics, Thermal Effectiveness, Perforations.
1. INTRODUCTION
HRV also known as the heat recovery air exchangers or
Mechanical ventilation heat recovery (MVHR), are
equipped with two continuously running fans. The first
one expels indoor stale air (consisting of - smell, smoke,
pollutants, pathogens etc.), and the second one supplies
fresh filtered air from the outside. The fresh new air and
expelled stale air never come into contact with each other;
the air is not recycled. This technology absorbs heat or
cooled energy and recycles it; it does not generate it. It can
recover heat during winter or cool during summer from
the expelled stale air, and transfers it to the fresh incoming
filtered air. In the article the HRV type to be discussed is a
Fixed plate type heat exchanger with extended surfaces
(fins).Plate heat exchangers are heat exchangers well-
known since the 1940's. They can be used as a sensible
heat or energy recovery, and are characterized by high
effectiveness, compactness, low weight and moderate cost.
They are further divided into cross, counter and parallel
flow. [1]
Figure- 1: Plate fin heat exchanger exploded diagram.
1.1 Working principle of PFHE.
The working principle of a plate fin heat exchanger is quite
simple. Here is an example of cross flow plate finned heat
exchanger. In cross flow the fluids are at an angle of 90°,
the two fluids involved in the heat exchange are separated
by a parting sheet. Which acts as the primary heat transfer
surface. It has side bars which prevents the fluid from
spilling. And extended surfaces or fins which are
sandwiched between the parting sheets. They act as the
secondary heat transfer surfaces.
Figure- 2: Cross flow plate fin heat exchanger meshing
As the fluid enters through the channels of the inlet, due to
the temperature gradient between the two fluids heat
transfer takes place through convection between the fluids
and the primary and secondary heat transfer surfaces.
This type of fixed plate heat exchangers has superiority to
rest of the heat exchangers because of their compactness.
Large heat transfer surface area per unit volume (typically
1000 m²/m³). It produces a high overall heat transfer
coefficient because of the heat transfer associated with the
narrow passages and corrugated surfaces.
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 360
2.TAGHUCHI ANALYSIS
Table 1: Selected 3-level control parameters and their
sub-levels
The Taguchi method is used to determine the main
(important) parameters that have the greatest impact on
the response parameter under study. Instead of changing
one factor, each time with this method, all factors are
changed at once according to the design array and also the
change of response values according to the selected
performance parameter is observed. It is also possible to
evaluate several factors with the minimum number of
experiments or numerical solutions by Taguchi method.
Table 2: 9 different designed numerical PHE models
according to Taguchi
3. CFD details and methodology
3.1 Preprocessing:
Step 1: Construction of Geometry. This problem has three
geometries namely,
1. Fresh fluid section
2. Intermediate plate section
3. Stale fluid section
The geometries of given problem are created by using
Space claim software.
Velocity of the fluid :2 m/s
Fin’s type: plain
Step 2: Meshing the Model
1. Volume mesh with Polyhedral and prism layer
Setting physics of the Problem
Since in this problem consists of three phases, we need to
select three physics, one for gas, second for liquid and
another for SOLID. Physics selected for the fluids
 Three-Dimensional Flow.
 stationary
 Constant density
 Steady Flow.
 Segregated flow model
 TURBULENT FLOW with K-Epsilon model
The Boundary Conditions
In this problem there is inlet one for cool stream and
other for hot steam, through the cross section of core. Both
streams are separated by each other by an intermediate
plate and both are velocity inlet type. Similarly, there are
two outlets in which are pressure outlet type the cross
section is given as symmetry type and remaining are keep
as a wall which are smooth, no slip and adiabatic. The
velocity at both the inlet is 2 m/s. the pressure at the
outlet is one atmosphere.
- Fresh air temperature =305k
- Stale air temperature = 295k.
4. Results
The results of Taguchi obtained are given below.
According to the 9 models made and based on the Taguchi
analysis from MINITAB 2019, the model with the cofactors
which is 0.10mm plate thickness, 2 m/s velocity of fluid
and 3 mm of plate height. And the response table for signal
to noise ratio in which larger is better was considered, the
rank was given in the follo9wing order; A to plate
thickness, B to velocity of the fluid and C to plate height.
LEVELS PLATE
THICKNESS
(mm)
VELOCITY
OF FLUID
(m/s)
PLATE
HEIGHT
(mm)
1 0.1 2 3
2 0.2 2.5 4
3 0.5 3 5
NUMERICAL
RUN
NUMBER
PLATE
THICKNESS
(mm)
VELOCITY
OF FLUID
(m/s)
PLATE
HEIGHT
(mm)
1 0.1 2 3
2 0.1 2.5 4
3 0.1 3 5
4 0.25 2 4
5 0.25 2.5 5
6 0.25 3 3
7 0.50 2 5
8 0.50 2.5 3
9 0.50 3 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 361
Figure 3: Response table for S/N ratios
Figure 4: Signal to noise Ratios Plots
Figure 5: Fresh air outlet temperatures for the 9
Taguchi models.
Therefore, according to the fresh air outlet temperatures
obtained, the effectiveness was calculated and again model
1 resulted in the maximum thermal effectiveness.
Figure 6: Effectiveness curve for 9 Taguchi models.
Figure 7: Temperature Contour for the PFHX
Figure 8:Temperature contour for the intermediate
plate
The fresh air outlet temperatures obtained for 9 different
models are represented below. The maximum decrease in
temperature was for the model 1 and the model 7 , 8 ,9
showed similar decrease pattern.
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 362
Figure 9: Sectional Plane Temperature Contour
Figure 10: Sectional plane Velocity Contour
Figure 11: Fresh side fin Pressure Contour
After obtaining results, from Taguchi analysis the model
which gave the highest thermal effectiveness was designed
and numerically verified. Now in order to further optimize
the design and size , a new model with triangular
perforations was designed and CFD ANALYSIS was carried
on it. The results below were hence obtained.
Figure 12: Perforated Fin Model
Figure 13: Meshing of the model.
Figure 14: Velocity Contour
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 363
Figure 15: Sectional Plane Velocity Contour Of
Perforated Model.
Figure 16: Sectional Plane Velocity Contour Of
Perforated Model.
Figure 17: Temperature Contour
Figure 18: Pressure Contour of the perforated model.
Figure 19: Pressure drop across the Z axis.
CONVENTIONAL
FIN DESIGN
TRIANGULAR
PERFORATED
DESIGN
FRESH AIR
OUTLET TEMP
(K)
302.99K 300.48K
STALE AIR
OUTLET TEMP
(K)
298 K 299.55 K
EFFECTIVENESS
(%)
30.0 - 35 % 45.7264 %
Heat Recovered
(Qrh) (WATTS)
56.455w 87.927W
KW .H/DAY 1.354 2.110
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 364
5.CONCLUSIONS
In this study, a cross-flow plate fin heat exchanger with
fixed plate, and triangular fins with triangular perforations
was designed by using CFD and Taguchi method for
maximum Thermal effectiveness. In Taguchi analysis, 3
control parameters each with 3-levels were selected and
numerical analysis were derived for designed 9 different
3-dimesional CFD models
-When optimal levels of the cofactors were used to create
design for maximum thermal effectiveness, thermal
effectiveness was obtained as 45.73% which is greater
than the conventional model thermal effectiveness by 8 to
10%.
-By using the optimal levels of factors for the maximum
thermal effectiveness, the difference between thermal
effectiveness predicted by the Taguchi method
(45.7264%) and that obtained from the solution of the
new optimum PHE numerical model (53.289%) .the
difference obtained was less than 10%.
-the total heat recovered was which was 56.46w(1.354
KW .H/DAY) in the conventional model was increased to
87.93w (2.110 KW .H/DAY ) in the proposed model.
-Considering the average air flow rate is 19 to to 25 m³/H
per person. the PFHE can easily serve 4 – 5 people
comfortably.
6. FUTURE SCOPE
 Experimental model could be made tested
analyzed and compared with the CFD and
numerical results.
 Perforations for porous media can be used and
analyzed
 Usage of different material such as cellulose,
paper that can retain moisture in the applications
of ERV could be studied.
 Circular perforations could be design for the fins
and its effect could be studied.
7. REFERENCES
1) Gabriela Elena Vlad, Constantin, Horia Necula,
Adrian, Analysis of An Air-To-Air Heat Exchanger
Designed for The Mechanical Ventilation System
of A House| U.P.B. Sci. Bull., Series C, Vol. 76, Iss. 1,
2014
2) Zender–Swiercz, E. A ´ Review of Heat Recovery in
Ventilation. Energies 2021, 14, 1759.
Https://doi.org/10.3390/en14061759 |
3) Room Ventilation & Airborne Disease
Transmission In A Healthcare Setting Energy
University Course Transcript
4) ENERGY RECOVERY VENTILATION
UNDERSTANDING ENERGY WHEELS AND
ENERGY RECOVERY VENTILATION TECHNOLOGY
By: Mark Rabbia, George Dowse Carrier
Corporation Syracuse, New York September 2000
5) ERI CORPORATION
6) Saffa Riffat and Shihao Zhang |Review of Heat
Recovery Technologies for Building Applications |
Energies 2019, 12, 1285;
doi:10.3390/en12071285
7) Grosse-Gorgemann, A., Hahne, W., and Fiebig, M.,
1993, “Influence of Rib Height on Oscillations,
Heat Transfer and Pressure Drop in Laminar
Channel Flow,” Proceedings of Eurotherm 31,
Vortices and Heat Transfer, Bochum, Germany, pp
36-41.
8) Masitah, A.R.S., Mardiana I Ahmad and Y.M. Yatim
| Heat Transfer and Effectiveness Analysis of a
Cross-Flow Heat Exchanger for Potential Energy
Recovery Applications in Hot-Humid Climate |
Masitah, A.R.S. et al. / Energy Research Journal
2015, 6 (1): 7.14 DOI: 10.3844/erjsp.2015.7.14
9) Turk, A.J, and Junklan, G.H., 1986, “Heat Transfer
Enhancement Downstream of Vortex generators
on a Flat Plate,” Proceedings of the Eighth
International Heat Transfer Conference, San
Francisco, Vol. 6, pp. 2903-2908
10) S Premkumar D, D Mangesh M, L Sachin M, K Sunil
V | Design and Study of Triangular Plate and Fin
Heat Exchanger | International Research Journal
of Engineering and Technology (IRJET) e-ISSN:
2395-0056 Volume: 05 Issue: 06 | June-201.

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Comparative Study Between Cross Flow Air To Air Plate Fin Heat Exchanger With Triangular Fins And Triangular Perforated Fins And Optimization Using Taguchi Analysis. , Heat recovery and importance of ventilation

  • 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 359 Comparative Study Between Cross Flow Air To Air Plate Fin Heat Exchanger With Triangular Fins And Triangular Perforated Fins And Optimization Using Taguchi Analysis. , Heat recovery and importance of ventilation. Mansoor Imtiyaz1, Shilpa Mondkar² 1Student, Dept. of Mechanical Engineering, Pillai College of Engineering, Maharashtra, India 2Asst. Professor, Dept. of Mechanical Engineering, Pillai College of Engineering, Maharashtra, India ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract – Indoor Air Quality (IAQ) is a term which we get to hear a lot after the commencement of the coronavirus pandemic. Heat recovery ventilation (HRV) can play a very important role in this. The fresh air from the ambient is separated from the stale air exhausted from the indoor facilities. Due to this the fresh air is not contaminated by the moisture, dust, pathogens, particulate matters, pollutants, smoke, smell etc. which is exhausted directly from the indoors and only heat transfer takes place further decreasing the load on HVAC systems. Computational fluid dynamics analysis between conventional plate fin heat exchanger model with triangular extended surfaces and proposed perforated model was performed and the comparative characteristics where studied. In order to maximize the parameter such as thermal effectiveness, recovered heat, outlet temperatures, Taguchi analysis was implemented using the L9 orthogonal array. The design variables and levels that would maximize the thermal effectiveness and other factors were plate thickness, velocity of fluid and plate height. Keywords-- Plate Fin Heat Exchanger, Taguchi Analysis, Heat Recovery Ventilation, Computational Fluid Dynamics, Thermal Effectiveness, Perforations. 1. INTRODUCTION HRV also known as the heat recovery air exchangers or Mechanical ventilation heat recovery (MVHR), are equipped with two continuously running fans. The first one expels indoor stale air (consisting of - smell, smoke, pollutants, pathogens etc.), and the second one supplies fresh filtered air from the outside. The fresh new air and expelled stale air never come into contact with each other; the air is not recycled. This technology absorbs heat or cooled energy and recycles it; it does not generate it. It can recover heat during winter or cool during summer from the expelled stale air, and transfers it to the fresh incoming filtered air. In the article the HRV type to be discussed is a Fixed plate type heat exchanger with extended surfaces (fins).Plate heat exchangers are heat exchangers well- known since the 1940's. They can be used as a sensible heat or energy recovery, and are characterized by high effectiveness, compactness, low weight and moderate cost. They are further divided into cross, counter and parallel flow. [1] Figure- 1: Plate fin heat exchanger exploded diagram. 1.1 Working principle of PFHE. The working principle of a plate fin heat exchanger is quite simple. Here is an example of cross flow plate finned heat exchanger. In cross flow the fluids are at an angle of 90°, the two fluids involved in the heat exchange are separated by a parting sheet. Which acts as the primary heat transfer surface. It has side bars which prevents the fluid from spilling. And extended surfaces or fins which are sandwiched between the parting sheets. They act as the secondary heat transfer surfaces. Figure- 2: Cross flow plate fin heat exchanger meshing As the fluid enters through the channels of the inlet, due to the temperature gradient between the two fluids heat transfer takes place through convection between the fluids and the primary and secondary heat transfer surfaces. This type of fixed plate heat exchangers has superiority to rest of the heat exchangers because of their compactness. Large heat transfer surface area per unit volume (typically 1000 m²/m³). It produces a high overall heat transfer coefficient because of the heat transfer associated with the narrow passages and corrugated surfaces.
  • 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 360 2.TAGHUCHI ANALYSIS Table 1: Selected 3-level control parameters and their sub-levels The Taguchi method is used to determine the main (important) parameters that have the greatest impact on the response parameter under study. Instead of changing one factor, each time with this method, all factors are changed at once according to the design array and also the change of response values according to the selected performance parameter is observed. It is also possible to evaluate several factors with the minimum number of experiments or numerical solutions by Taguchi method. Table 2: 9 different designed numerical PHE models according to Taguchi 3. CFD details and methodology 3.1 Preprocessing: Step 1: Construction of Geometry. This problem has three geometries namely, 1. Fresh fluid section 2. Intermediate plate section 3. Stale fluid section The geometries of given problem are created by using Space claim software. Velocity of the fluid :2 m/s Fin’s type: plain Step 2: Meshing the Model 1. Volume mesh with Polyhedral and prism layer Setting physics of the Problem Since in this problem consists of three phases, we need to select three physics, one for gas, second for liquid and another for SOLID. Physics selected for the fluids  Three-Dimensional Flow.  stationary  Constant density  Steady Flow.  Segregated flow model  TURBULENT FLOW with K-Epsilon model The Boundary Conditions In this problem there is inlet one for cool stream and other for hot steam, through the cross section of core. Both streams are separated by each other by an intermediate plate and both are velocity inlet type. Similarly, there are two outlets in which are pressure outlet type the cross section is given as symmetry type and remaining are keep as a wall which are smooth, no slip and adiabatic. The velocity at both the inlet is 2 m/s. the pressure at the outlet is one atmosphere. - Fresh air temperature =305k - Stale air temperature = 295k. 4. Results The results of Taguchi obtained are given below. According to the 9 models made and based on the Taguchi analysis from MINITAB 2019, the model with the cofactors which is 0.10mm plate thickness, 2 m/s velocity of fluid and 3 mm of plate height. And the response table for signal to noise ratio in which larger is better was considered, the rank was given in the follo9wing order; A to plate thickness, B to velocity of the fluid and C to plate height. LEVELS PLATE THICKNESS (mm) VELOCITY OF FLUID (m/s) PLATE HEIGHT (mm) 1 0.1 2 3 2 0.2 2.5 4 3 0.5 3 5 NUMERICAL RUN NUMBER PLATE THICKNESS (mm) VELOCITY OF FLUID (m/s) PLATE HEIGHT (mm) 1 0.1 2 3 2 0.1 2.5 4 3 0.1 3 5 4 0.25 2 4 5 0.25 2.5 5 6 0.25 3 3 7 0.50 2 5 8 0.50 2.5 3 9 0.50 3 4
  • 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 361 Figure 3: Response table for S/N ratios Figure 4: Signal to noise Ratios Plots Figure 5: Fresh air outlet temperatures for the 9 Taguchi models. Therefore, according to the fresh air outlet temperatures obtained, the effectiveness was calculated and again model 1 resulted in the maximum thermal effectiveness. Figure 6: Effectiveness curve for 9 Taguchi models. Figure 7: Temperature Contour for the PFHX Figure 8:Temperature contour for the intermediate plate The fresh air outlet temperatures obtained for 9 different models are represented below. The maximum decrease in temperature was for the model 1 and the model 7 , 8 ,9 showed similar decrease pattern.
  • 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 362 Figure 9: Sectional Plane Temperature Contour Figure 10: Sectional plane Velocity Contour Figure 11: Fresh side fin Pressure Contour After obtaining results, from Taguchi analysis the model which gave the highest thermal effectiveness was designed and numerically verified. Now in order to further optimize the design and size , a new model with triangular perforations was designed and CFD ANALYSIS was carried on it. The results below were hence obtained. Figure 12: Perforated Fin Model Figure 13: Meshing of the model. Figure 14: Velocity Contour
  • 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 363 Figure 15: Sectional Plane Velocity Contour Of Perforated Model. Figure 16: Sectional Plane Velocity Contour Of Perforated Model. Figure 17: Temperature Contour Figure 18: Pressure Contour of the perforated model. Figure 19: Pressure drop across the Z axis. CONVENTIONAL FIN DESIGN TRIANGULAR PERFORATED DESIGN FRESH AIR OUTLET TEMP (K) 302.99K 300.48K STALE AIR OUTLET TEMP (K) 298 K 299.55 K EFFECTIVENESS (%) 30.0 - 35 % 45.7264 % Heat Recovered (Qrh) (WATTS) 56.455w 87.927W KW .H/DAY 1.354 2.110
  • 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 364 5.CONCLUSIONS In this study, a cross-flow plate fin heat exchanger with fixed plate, and triangular fins with triangular perforations was designed by using CFD and Taguchi method for maximum Thermal effectiveness. In Taguchi analysis, 3 control parameters each with 3-levels were selected and numerical analysis were derived for designed 9 different 3-dimesional CFD models -When optimal levels of the cofactors were used to create design for maximum thermal effectiveness, thermal effectiveness was obtained as 45.73% which is greater than the conventional model thermal effectiveness by 8 to 10%. -By using the optimal levels of factors for the maximum thermal effectiveness, the difference between thermal effectiveness predicted by the Taguchi method (45.7264%) and that obtained from the solution of the new optimum PHE numerical model (53.289%) .the difference obtained was less than 10%. -the total heat recovered was which was 56.46w(1.354 KW .H/DAY) in the conventional model was increased to 87.93w (2.110 KW .H/DAY ) in the proposed model. -Considering the average air flow rate is 19 to to 25 m³/H per person. the PFHE can easily serve 4 – 5 people comfortably. 6. FUTURE SCOPE  Experimental model could be made tested analyzed and compared with the CFD and numerical results.  Perforations for porous media can be used and analyzed  Usage of different material such as cellulose, paper that can retain moisture in the applications of ERV could be studied.  Circular perforations could be design for the fins and its effect could be studied. 7. REFERENCES 1) Gabriela Elena Vlad, Constantin, Horia Necula, Adrian, Analysis of An Air-To-Air Heat Exchanger Designed for The Mechanical Ventilation System of A House| U.P.B. Sci. Bull., Series C, Vol. 76, Iss. 1, 2014 2) Zender–Swiercz, E. A ´ Review of Heat Recovery in Ventilation. Energies 2021, 14, 1759. Https://doi.org/10.3390/en14061759 | 3) Room Ventilation & Airborne Disease Transmission In A Healthcare Setting Energy University Course Transcript 4) ENERGY RECOVERY VENTILATION UNDERSTANDING ENERGY WHEELS AND ENERGY RECOVERY VENTILATION TECHNOLOGY By: Mark Rabbia, George Dowse Carrier Corporation Syracuse, New York September 2000 5) ERI CORPORATION 6) Saffa Riffat and Shihao Zhang |Review of Heat Recovery Technologies for Building Applications | Energies 2019, 12, 1285; doi:10.3390/en12071285 7) Grosse-Gorgemann, A., Hahne, W., and Fiebig, M., 1993, “Influence of Rib Height on Oscillations, Heat Transfer and Pressure Drop in Laminar Channel Flow,” Proceedings of Eurotherm 31, Vortices and Heat Transfer, Bochum, Germany, pp 36-41. 8) Masitah, A.R.S., Mardiana I Ahmad and Y.M. Yatim | Heat Transfer and Effectiveness Analysis of a Cross-Flow Heat Exchanger for Potential Energy Recovery Applications in Hot-Humid Climate | Masitah, A.R.S. et al. / Energy Research Journal 2015, 6 (1): 7.14 DOI: 10.3844/erjsp.2015.7.14 9) Turk, A.J, and Junklan, G.H., 1986, “Heat Transfer Enhancement Downstream of Vortex generators on a Flat Plate,” Proceedings of the Eighth International Heat Transfer Conference, San Francisco, Vol. 6, pp. 2903-2908 10) S Premkumar D, D Mangesh M, L Sachin M, K Sunil V | Design and Study of Triangular Plate and Fin Heat Exchanger | International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 06 | June-201.