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International Journal of Trend in Scientific Research and Development (IJTSRD)
Volume 6 Issue 2, January-February 2022 Available Online: www.ijtsrd.com e-ISSN: 2456 – 6470
@ IJTSRD | Unique Paper ID – IJTSRD49160 | Volume – 6 | Issue – 2 | Jan-Feb 2022 Page 100
Thermal Analysis of Cooling Tower using
Computational Fluid Dynamics
P Chandra Shekhar1
, Sudhir Singh Rajput2
1
Research Scholar, 2
Assistant Professor,
1,2
Department of Mechanical Engineering, Raipur Institute of Technology, Raipur, Chhattisgarh, India
ABSTRACT
The automotive, chemical and other plants employs use of cooling
tower dissipating heat from water in to the atmosphere. The
performance of cooling tower can be enhanced by various water
modelling and energy consumption analysis. The current research
reviews previous studies conducted in determination of effectiveness
of cooling tower subjected to different operating conditions. The
analytical equations are presented along with experimental data on
evaluation and improvement of cooling tower performance.
KEYWORDS: Cooling tower, thermal analysis
How to cite this paper: P Chandra
Shekhar | Sudhir Singh Rajput "Thermal
Analysis of Cooling Tower using
Computational Fluid Dynamics"
Published in
International Journal
of Trend in
Scientific Research
and Development
(ijtsrd), ISSN: 2456-
6470, Volume-6 |
Issue-2, February
2022, pp.100-103, URL:
www.ijtsrd.com/papers/ijtsrd49160.pdf
Copyright © 2022 by author(s) and
International Journal of Trend in
Scientific Research and Development
Journal. This is an
Open Access article
distributed under the
terms of the Creative Commons
Attribution License (CC BY 4.0)
(http://creativecommons.org/licenses/by/4.0)
1. INTRODUCTION
The cooling tower is one of the key components in
industries such as power generation including
renewable [1] geothermal and solar thermal [2] and
non-renewable [3] power plants, chemical and
petrochemical plants [4], refrigeration and air-
conditioning plants. Thermoelectric generation and its
required cooling are responsible for approx. 10% of
the total water demand in the world. The role of the
cooling tower is dissipating heat from the hot stream
of the process into the air in power plants, district
cooling plants, and cooling systems. To address the
water scarcity for a sustainable future (in smart cities)
cooling towers have to receive special attention.
Replacing the evaporation of water for dissipating the
heat with another method, or capturing the vapor, or
both are the ideas to support water conservation.
Considering several cooling towers that are installed
already highlights the importance of capturing the
vapor and/or reducing evaporation studies. The
design of cooling towers focuses on the water
distribution system, fill, and drift elimination. The
water distribution system introduces and spreads the
process water as evenly over the fill through the use
of water canals and nozzles. The fill is a system of
packing that delays the fall of water and improves
heat transfer, and drift eliminators at the air exit
change the direction of airflow to reduce the volume
of water transported out. Within cooling towers,
water is lost through three main modes. These modes
are drift, blowdown, and evaporation. Drift is the
water losses associated with wind, evaporation loss
occurs due to the heat transfer taking place, and
blowdown is utilized to avoid the buildup of minerals
and sediments within the cooling water that may
damage other components within the system, and.
blowdown is also a byproduct of the evaporation
processes increasing the concentration of the minerals
[5].
IJTSRD49160
International Journal of Trend in Scientific Research and Development @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD49160 | Volume – 6 | Issue – 2 | Jan-Feb 2022 Page 101
Figure 1: The schematic of different types of wet
cooling towers
Wet cooling towers are also categorized by the
movement of water and air inside of the cooling
tower as follows:
1. Crossflow towers: air flows horizontally across
the falling water as it shows in Figure 1 (b) and
(d),
2. Counterflow: the upward airflow that directly
opposes the downward flow of the water
providing which is shown in Figure 1 (a) and (c)
[19].
2. LITERATURE REVIEW
Klopperset al. [6] have worked on development of
empirical equation for determination of efficiency of
cooling tower. When the outlet air from the cooling
tower was saturated, Merkel and e-NTU models were
capable of predicting the temperature of that, while
the Poppe model did not need any assumption for
estimation of the outlet air temperature from the
cooling tower.
Ayoubet al. [7] When the draft in the cooling tower
was the same, the outlet water temperature from the
cooling tower in the three models were the same. A
small difference in the outlet water temperature from
the cooling tower was observed in Merkel and Poppe
models over the outlet air from the cooling tower
since outlet air assumed saturated in the Merkel
model.
M Rothet. al. [8]have worked in development of
water evaporation rate. The water evaporation rate in
the cooling tower was underestimated by the Merkel
model compared to the Poppe model. Since
evaporation was an important factor in designing the
hybrid cooling towers, using the Poppe model was
preferred.
Klopperset. al. [9] have proposed a modelbased on a
reliable equation to determine the Lewis factor value.
While in the Merkel model the Lewis factor was a
constant number of 1. Most researchers believed that
Merkel's assumption was not accurate since the Lewis
factor was between 0.6 to 1.3.
Jaber and Webb [10] put forward the number of heat
transfer unit (ε-NTU) model, which provides another
method for the calculation of the cooling tower. It is
worth noting that the model, like the Merkel enthalpy
model, ignores the effect of water evaporation.
Gan [11, 12] put forward several mathematical
models. These models take into account the mass,
momentum, and energy transfer simultaneously.
These models are based on the Merkel theory and its
modified form, and they can analyse the thermal
processes of different cooling towers. They also
carried out numerical simulation analysis of closed
cooling towers and obtained an earlier relatively
mature simulation experience.
Ronak Shah, TruptiRathore[13] had done thermal
design of industrial cooling tower and determined the
complete performance parameters with given inlet
and outlet conditions and considering several possible
losses. they investigated that cooling tower
performance increases with increasing air flow rate
and cooling tower characteristic decreases with
increase in water to air mass ratio.
Plasencia et al [14] developed a new model which is
based on transfer of heat and mass for IEC; few
simplifications were incorporated to make this model
as user friendly used for analysis of energy as well as
adaption of system.
Camargo et al [15] presented an operational concept
for both type of cooling systems and generated
equations for mass and heat transfer between warm
air and wetted media. Above researches and
mathematical models has been limited up to the
conditioning of air coming out of the coolers, and to
increase the saturation efficiency or effectiveness of
cooler; however, the use of cooled water stored in
tank was not at all explored. This gap of not using the
coolness of cooler water has been identified as a
research gap and thus becomes the main objective of
the present work.
Pushpa B. S, VasantVaze, P. T. Nimbalkar [16] have
evaluated performance of cooling tower in thermal
power plant by varying water inlet temperature, air
inlet temperature and mass flow rate of water. They
found that efficiency of cooling tower increases by
increasing water inlet temp, air inlet temperature and
decreases by increasing mass flow rate.
International Journal of Trend in Scientific Research and Development @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD49160 | Volume – 6 | Issue – 2 | Jan-Feb 2022 Page 102
S. ParimalaMurugaveni, P. Mohamed Shameer[17] in
their research have analyzed a forced draft cooling
tower by varying air inlet parameters and by varying
air inlet angles in horizontal and vertical direction and
both. The cooling tower model has been prepared in
solid works 2013 and it has been meshed using
icemCFD 14.5 software and meshed models have
been analyzed using fluent software. On the basis of
temperature contours obtained, they found that outlet
temperature of water increases as the air inlet angle
increases which will lead to decrease in effectiveness.
Manoj Kumar Chopra, Rahul Kumar[18] in their
research carried out the cfd analysis on a counter flow
cooling tower reference model. the model has been
prepared in Creo and meshed and analyzed through
Ansys 12.1. The analysis is carried out by
simultaneous varying of three parameter inlet water
flow rate, inlet air rate and fills porosity and applied
taguchi method to carry out the optimization. They
investigated that cooling tower gives best
performance at lower mass flow rate of water, high
mass flow rate of air and fill porosity of 50%.
3. CONCLUSION
The performance of cooling towers depends upon
various operational and design parameters. The
empirical equations are presented by various scholars
which can accurately predict the efficiency of cooling
towers under different operating conditions which
includes air inlet temperature, water inlet temperature
and mass flow rate. The present study elaborated the
history of energy-water modeling methods of cooling
towers through the Markel, the Poppe, and the
Effectiveness–(NTU) Models since water and energy
are deeply connected in cooling towers.
REFERENCES
[1] Hooman, K. (2010) ‘Dry cooling towers as
condensers for geothermal power plants’,
International Communications in Heat and
Mass Transfer. Pergamon, 37(9), pp. 1215–
1220. doi:
10.1016/j.icheatmasstransfer.2010.07.011.
[2] Li, X., Gurgenci, H., Guan, Z., Wang, X. and
Duniam, S. (2017) ‘Measurements of crosswind
influence on a natural draft dry cooling tower
for a solar thermal power plant’, Applied
Energy, 206, pp. 1169–1183. doi:
10.1016/j.apenergy.2017.10.038.
[3] Zhai, H. and Rubin, E. S. (2010) ‘Performance
and cost of wet and dry cooling systems for
pulverized coal power plants with and without
carbon capture and storage’, Energy Policy,
38(10), pp. 5653–5660. doi:
10.1016/j.enpol.2010.05.013.
[4] Hansen, E., Rodrigues, M. A. S. and Aquim, P.
M. de (2016) ‘Wastewater reuse in a cascade
based system of a petrochemical industry for
the replacement of losses in cooling towers’,
Journal of Environmental Management.
Academic Press, 181, pp. 157–162. doi:
10.1016/j.jenvman.2016.06.014.
[5] Schlei-Peters, I., Wichmann, M. G., Matthes, I.-
G., Gundlach, F.-W. and Spengler, T. S. (2018)
‘Integrated Material Flow Analysis and Process
Modeling to Increase Energy and Water
Efficiency of Industrial Cooling Water
Systems’, Journal of Industrial Ecology, 22(1),
pp. 41–54. doi: 10.1111/jiec.12540.
[6] Kloppers, J. C. and Kröger, D. G. (2005) ‘The
Lewis factor and its influence on the
performance prediction of wet-cooling towers’,
International Journal of Thermal Sciences.
Elsevier Masson, 44(9), pp. 879–884. doi:
10.1016/j.ijthermalsci.2005.03.006.
[7] Ayoub, A., Gjorgiev, B. and Sansavini, G.
(2018) ‘Cooling towers performance in a
changing climate: Techno-economic modeling
and design optimization’, Energy, 160, pp.
1133–1143. doi: 10.1016/j.energy.2018.07.080.
[8] M Roth (2001) ‘Fundamentals of heat and mass
transfer in wet cooling towers. All well known
or are further developments necessary?’, in
Proceedings of 12th IAHR Cooling Tower and
Heat Exchangers. UTS, Sydney, Australia.
[9] Kloppers, J. C. and KröGer, D. G. (2005)
‘Cooling Tower Performance Evaluation:
Merkel, Poppe, and e-NTU Methods of
Analysis’, asmedigitalcollection.asme.org. doi:
10.1115/1.1787504.
[10] H. Jaber and R. L. Webb, “Design of cooling
towers by the effectiveness-NTU method,”
Journal of Heat Transfer, vol. 111, no. 4, pp.
837–843, 1989.
[11] G. Gan, S. B. Riffat, L. Shao, and P. Doherty,
“Application of CFD to closed-wet cooling
towers,” Applied 5ermal Engineering, vol. 21,
no. 1, pp. 79–92, 2001.
[12] G. Gan and S. B. Riffat, “Numerical simulation
of closed wet cooling towers for chilled ceiling
systems,” Applied 5ermal Engineering, vol. 19,
no. 12, pp. 1279–1296, 1999.
[13] Ronak Shah, TruptiRathod, Thermal Design Of
Cooling Tower, International Journal Of
Advanced Engineering Research And Studies,
E-ISSN: 2249-8974.
International Journal of Trend in Scientific Research and Development @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Paper ID – IJTSRD49160 | Volume – 6 | Issue – 2 | Jan-Feb 2022 Page 103
[14] Alonso JS, Martinez FR, Gomez EV, Plasencia
MA, “Simulation model of an IEC”, Energy
and Buildings, (1998).
[15] Camargo JR and Ebinuma CD, “A
mathematical model for direct and indirect
evaporative cooling AC systems”, Thermal
Engineering and Sciences, Caxambu, Brazil,
(2002).
[16] Pushpa B.S., VasantVaze, P.T.Nimbalkar,
Performance Evaluation Of Cooling Tower In
Thermal Power Plant – A Case Study Of RTPS,
Karnataka, International Journal Of
Engineering And Advanced Technology,,
Volume-4, Issue-2, December 2014, ISSN:
2249 – 8958
[17] S. ParimalaMurugaveni, P. Mohamed Shameer,
Analysis Of Forced Draft Cooling
[18] Tower Performance Using Ansys Fluent
Software, International Journal Of Research In
Engineering And Technology, Eissn: 2319-
1163 Pissn: 2321-7308
[19] Guo, Y., Wang, F., Jia, M. and Zhang, S. (2017)
‘Parallel hybrid model for mechanical draft
counter flow wet-cooling tower Parallel hybrid
model for mechanical draft counter flow wet-
cooling tower’, Applied Thermal Engineering,
125, pp. 1379–1388. doi:
10.1016/j.applthermaleng.2017.07.138.

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Thermal Analysis of Cooling Tower using Computational Fluid Dynamics

  • 1. International Journal of Trend in Scientific Research and Development (IJTSRD) Volume 6 Issue 2, January-February 2022 Available Online: www.ijtsrd.com e-ISSN: 2456 – 6470 @ IJTSRD | Unique Paper ID – IJTSRD49160 | Volume – 6 | Issue – 2 | Jan-Feb 2022 Page 100 Thermal Analysis of Cooling Tower using Computational Fluid Dynamics P Chandra Shekhar1 , Sudhir Singh Rajput2 1 Research Scholar, 2 Assistant Professor, 1,2 Department of Mechanical Engineering, Raipur Institute of Technology, Raipur, Chhattisgarh, India ABSTRACT The automotive, chemical and other plants employs use of cooling tower dissipating heat from water in to the atmosphere. The performance of cooling tower can be enhanced by various water modelling and energy consumption analysis. The current research reviews previous studies conducted in determination of effectiveness of cooling tower subjected to different operating conditions. The analytical equations are presented along with experimental data on evaluation and improvement of cooling tower performance. KEYWORDS: Cooling tower, thermal analysis How to cite this paper: P Chandra Shekhar | Sudhir Singh Rajput "Thermal Analysis of Cooling Tower using Computational Fluid Dynamics" Published in International Journal of Trend in Scientific Research and Development (ijtsrd), ISSN: 2456- 6470, Volume-6 | Issue-2, February 2022, pp.100-103, URL: www.ijtsrd.com/papers/ijtsrd49160.pdf Copyright © 2022 by author(s) and International Journal of Trend in Scientific Research and Development Journal. This is an Open Access article distributed under the terms of the Creative Commons Attribution License (CC BY 4.0) (http://creativecommons.org/licenses/by/4.0) 1. INTRODUCTION The cooling tower is one of the key components in industries such as power generation including renewable [1] geothermal and solar thermal [2] and non-renewable [3] power plants, chemical and petrochemical plants [4], refrigeration and air- conditioning plants. Thermoelectric generation and its required cooling are responsible for approx. 10% of the total water demand in the world. The role of the cooling tower is dissipating heat from the hot stream of the process into the air in power plants, district cooling plants, and cooling systems. To address the water scarcity for a sustainable future (in smart cities) cooling towers have to receive special attention. Replacing the evaporation of water for dissipating the heat with another method, or capturing the vapor, or both are the ideas to support water conservation. Considering several cooling towers that are installed already highlights the importance of capturing the vapor and/or reducing evaporation studies. The design of cooling towers focuses on the water distribution system, fill, and drift elimination. The water distribution system introduces and spreads the process water as evenly over the fill through the use of water canals and nozzles. The fill is a system of packing that delays the fall of water and improves heat transfer, and drift eliminators at the air exit change the direction of airflow to reduce the volume of water transported out. Within cooling towers, water is lost through three main modes. These modes are drift, blowdown, and evaporation. Drift is the water losses associated with wind, evaporation loss occurs due to the heat transfer taking place, and blowdown is utilized to avoid the buildup of minerals and sediments within the cooling water that may damage other components within the system, and. blowdown is also a byproduct of the evaporation processes increasing the concentration of the minerals [5]. IJTSRD49160
  • 2. International Journal of Trend in Scientific Research and Development @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD49160 | Volume – 6 | Issue – 2 | Jan-Feb 2022 Page 101 Figure 1: The schematic of different types of wet cooling towers Wet cooling towers are also categorized by the movement of water and air inside of the cooling tower as follows: 1. Crossflow towers: air flows horizontally across the falling water as it shows in Figure 1 (b) and (d), 2. Counterflow: the upward airflow that directly opposes the downward flow of the water providing which is shown in Figure 1 (a) and (c) [19]. 2. LITERATURE REVIEW Klopperset al. [6] have worked on development of empirical equation for determination of efficiency of cooling tower. When the outlet air from the cooling tower was saturated, Merkel and e-NTU models were capable of predicting the temperature of that, while the Poppe model did not need any assumption for estimation of the outlet air temperature from the cooling tower. Ayoubet al. [7] When the draft in the cooling tower was the same, the outlet water temperature from the cooling tower in the three models were the same. A small difference in the outlet water temperature from the cooling tower was observed in Merkel and Poppe models over the outlet air from the cooling tower since outlet air assumed saturated in the Merkel model. M Rothet. al. [8]have worked in development of water evaporation rate. The water evaporation rate in the cooling tower was underestimated by the Merkel model compared to the Poppe model. Since evaporation was an important factor in designing the hybrid cooling towers, using the Poppe model was preferred. Klopperset. al. [9] have proposed a modelbased on a reliable equation to determine the Lewis factor value. While in the Merkel model the Lewis factor was a constant number of 1. Most researchers believed that Merkel's assumption was not accurate since the Lewis factor was between 0.6 to 1.3. Jaber and Webb [10] put forward the number of heat transfer unit (ε-NTU) model, which provides another method for the calculation of the cooling tower. It is worth noting that the model, like the Merkel enthalpy model, ignores the effect of water evaporation. Gan [11, 12] put forward several mathematical models. These models take into account the mass, momentum, and energy transfer simultaneously. These models are based on the Merkel theory and its modified form, and they can analyse the thermal processes of different cooling towers. They also carried out numerical simulation analysis of closed cooling towers and obtained an earlier relatively mature simulation experience. Ronak Shah, TruptiRathore[13] had done thermal design of industrial cooling tower and determined the complete performance parameters with given inlet and outlet conditions and considering several possible losses. they investigated that cooling tower performance increases with increasing air flow rate and cooling tower characteristic decreases with increase in water to air mass ratio. Plasencia et al [14] developed a new model which is based on transfer of heat and mass for IEC; few simplifications were incorporated to make this model as user friendly used for analysis of energy as well as adaption of system. Camargo et al [15] presented an operational concept for both type of cooling systems and generated equations for mass and heat transfer between warm air and wetted media. Above researches and mathematical models has been limited up to the conditioning of air coming out of the coolers, and to increase the saturation efficiency or effectiveness of cooler; however, the use of cooled water stored in tank was not at all explored. This gap of not using the coolness of cooler water has been identified as a research gap and thus becomes the main objective of the present work. Pushpa B. S, VasantVaze, P. T. Nimbalkar [16] have evaluated performance of cooling tower in thermal power plant by varying water inlet temperature, air inlet temperature and mass flow rate of water. They found that efficiency of cooling tower increases by increasing water inlet temp, air inlet temperature and decreases by increasing mass flow rate.
  • 3. International Journal of Trend in Scientific Research and Development @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD49160 | Volume – 6 | Issue – 2 | Jan-Feb 2022 Page 102 S. ParimalaMurugaveni, P. Mohamed Shameer[17] in their research have analyzed a forced draft cooling tower by varying air inlet parameters and by varying air inlet angles in horizontal and vertical direction and both. The cooling tower model has been prepared in solid works 2013 and it has been meshed using icemCFD 14.5 software and meshed models have been analyzed using fluent software. On the basis of temperature contours obtained, they found that outlet temperature of water increases as the air inlet angle increases which will lead to decrease in effectiveness. Manoj Kumar Chopra, Rahul Kumar[18] in their research carried out the cfd analysis on a counter flow cooling tower reference model. the model has been prepared in Creo and meshed and analyzed through Ansys 12.1. The analysis is carried out by simultaneous varying of three parameter inlet water flow rate, inlet air rate and fills porosity and applied taguchi method to carry out the optimization. They investigated that cooling tower gives best performance at lower mass flow rate of water, high mass flow rate of air and fill porosity of 50%. 3. CONCLUSION The performance of cooling towers depends upon various operational and design parameters. The empirical equations are presented by various scholars which can accurately predict the efficiency of cooling towers under different operating conditions which includes air inlet temperature, water inlet temperature and mass flow rate. The present study elaborated the history of energy-water modeling methods of cooling towers through the Markel, the Poppe, and the Effectiveness–(NTU) Models since water and energy are deeply connected in cooling towers. REFERENCES [1] Hooman, K. (2010) ‘Dry cooling towers as condensers for geothermal power plants’, International Communications in Heat and Mass Transfer. Pergamon, 37(9), pp. 1215– 1220. doi: 10.1016/j.icheatmasstransfer.2010.07.011. [2] Li, X., Gurgenci, H., Guan, Z., Wang, X. and Duniam, S. (2017) ‘Measurements of crosswind influence on a natural draft dry cooling tower for a solar thermal power plant’, Applied Energy, 206, pp. 1169–1183. doi: 10.1016/j.apenergy.2017.10.038. [3] Zhai, H. and Rubin, E. S. (2010) ‘Performance and cost of wet and dry cooling systems for pulverized coal power plants with and without carbon capture and storage’, Energy Policy, 38(10), pp. 5653–5660. doi: 10.1016/j.enpol.2010.05.013. [4] Hansen, E., Rodrigues, M. A. S. and Aquim, P. M. de (2016) ‘Wastewater reuse in a cascade based system of a petrochemical industry for the replacement of losses in cooling towers’, Journal of Environmental Management. Academic Press, 181, pp. 157–162. doi: 10.1016/j.jenvman.2016.06.014. [5] Schlei-Peters, I., Wichmann, M. G., Matthes, I.- G., Gundlach, F.-W. and Spengler, T. S. (2018) ‘Integrated Material Flow Analysis and Process Modeling to Increase Energy and Water Efficiency of Industrial Cooling Water Systems’, Journal of Industrial Ecology, 22(1), pp. 41–54. doi: 10.1111/jiec.12540. [6] Kloppers, J. C. and Kröger, D. G. (2005) ‘The Lewis factor and its influence on the performance prediction of wet-cooling towers’, International Journal of Thermal Sciences. Elsevier Masson, 44(9), pp. 879–884. doi: 10.1016/j.ijthermalsci.2005.03.006. [7] Ayoub, A., Gjorgiev, B. and Sansavini, G. (2018) ‘Cooling towers performance in a changing climate: Techno-economic modeling and design optimization’, Energy, 160, pp. 1133–1143. doi: 10.1016/j.energy.2018.07.080. [8] M Roth (2001) ‘Fundamentals of heat and mass transfer in wet cooling towers. All well known or are further developments necessary?’, in Proceedings of 12th IAHR Cooling Tower and Heat Exchangers. UTS, Sydney, Australia. [9] Kloppers, J. C. and KröGer, D. G. (2005) ‘Cooling Tower Performance Evaluation: Merkel, Poppe, and e-NTU Methods of Analysis’, asmedigitalcollection.asme.org. doi: 10.1115/1.1787504. [10] H. Jaber and R. L. Webb, “Design of cooling towers by the effectiveness-NTU method,” Journal of Heat Transfer, vol. 111, no. 4, pp. 837–843, 1989. [11] G. Gan, S. B. Riffat, L. Shao, and P. Doherty, “Application of CFD to closed-wet cooling towers,” Applied 5ermal Engineering, vol. 21, no. 1, pp. 79–92, 2001. [12] G. Gan and S. B. Riffat, “Numerical simulation of closed wet cooling towers for chilled ceiling systems,” Applied 5ermal Engineering, vol. 19, no. 12, pp. 1279–1296, 1999. [13] Ronak Shah, TruptiRathod, Thermal Design Of Cooling Tower, International Journal Of Advanced Engineering Research And Studies, E-ISSN: 2249-8974.
  • 4. International Journal of Trend in Scientific Research and Development @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Paper ID – IJTSRD49160 | Volume – 6 | Issue – 2 | Jan-Feb 2022 Page 103 [14] Alonso JS, Martinez FR, Gomez EV, Plasencia MA, “Simulation model of an IEC”, Energy and Buildings, (1998). [15] Camargo JR and Ebinuma CD, “A mathematical model for direct and indirect evaporative cooling AC systems”, Thermal Engineering and Sciences, Caxambu, Brazil, (2002). [16] Pushpa B.S., VasantVaze, P.T.Nimbalkar, Performance Evaluation Of Cooling Tower In Thermal Power Plant – A Case Study Of RTPS, Karnataka, International Journal Of Engineering And Advanced Technology,, Volume-4, Issue-2, December 2014, ISSN: 2249 – 8958 [17] S. ParimalaMurugaveni, P. Mohamed Shameer, Analysis Of Forced Draft Cooling [18] Tower Performance Using Ansys Fluent Software, International Journal Of Research In Engineering And Technology, Eissn: 2319- 1163 Pissn: 2321-7308 [19] Guo, Y., Wang, F., Jia, M. and Zhang, S. (2017) ‘Parallel hybrid model for mechanical draft counter flow wet-cooling tower Parallel hybrid model for mechanical draft counter flow wet- cooling tower’, Applied Thermal Engineering, 125, pp. 1379–1388. doi: 10.1016/j.applthermaleng.2017.07.138.