Iranian Journal of Mechanical Engineering Transactions of ISME

Iranian Journal of Mechanical Engineering Transactions of ISME

Numerical Investigation of Double Pipe Heat Exchanger with Nanofluid Inside Helically Corrugated Tube in the Presence of Magnetic Field

Authors
1 Assistant Professor, Mechanical Engineering Department, Faculty of Engineering, Azarbaijan Shahid Madani University, Tabriz, Iran
2 M.Sc., Mechanical Engineering Department, Faculty of Engineering, Azarbaijan Shahid Madani University, Tabriz, Iran
Abstract
In the present work, a special type of concentric two-pipe heat exchangers has been analyzed, in which the inner tube of the heat exchanger is considered as helical grooved. The turbulent flow of water-aluminum oxide nanofluid is used on both sides of the heat exchanger and a constant intensity magnetic field is used to enhance the effect of using the nanofluid. The effect of using this system as well as the use of nanofluid and magnetic field on the total heat transfer coefficient and the total pressure drop of the heat exchanger have been investigated. The results of studies in this field show that the use of nanofluids increases the heat transfer that occurs in the heat exchanger and also decreases the total pressure. While the most suitable volume percentage of nanofluid for the best ratio of heat transfer to pressure drop is also reported to be 15%. The numerical results of this article have also shown that the best optimal conditions in terms of heat transfer enhancement and pressure drop (according to the PEC performance evaluation criteria) are at 15% volume of nanofluid. Applying a magnetic field to the nanofluid current in the transducer also helps to increase the heat transfer in the heat exchanger while also increasing the total pressure drop. The amount of flow velocity has an obvious effect on the displacement heat transfer coefficient of the heat exchanger as well as the amount of total pressure drop. The simulation of the heat exchanger in different values ​​of the turbulent flow Reynolds number shows that the increase in the Reynolds number has a direct effect on the displacement heat transfer and the total pressure drop. The results show that in the intensity of the magnetic field with Hartmann number 40, the best ratio of heat transfer to the pressure drop of the heat exchanger occurs. The best PEC number in Hartmann number 40 is 1.05. However, with further increase of Hartmann number to 60 and 80, the value of PEC number decreases and in Hartmann number 80 decreases to 0.99, which practically makes the use of nanofluid in the presence of magnetic field affectless. The rate of flow velocity has a significant effect on the heat transfer coefficient of the heat exchanger and also the rate of total pressure drop. The value of the PEC number increases from 1.01 to 1.09 in increasing the Reynolds number from 6000 to 10000. However, it seems that with a relatively small increase in the PEC number and increasing costs in increasing the Reynolds number, using a lower Reynolds number scaler is a better choice.
Keywords

Subjects


[1] W. Wang, Y. Zhang, K.-S. Lee, and B. Li, "Optimal Design of a Double Pipe Heat Exchanger Based on the Outward Helically Corrugated Tube," International Journal of Heat and Mass Transfer, Vol. 135, pp. 706-716, 2019, https://doi.org/10.1016/j.ijheatmasstransfer.2019.01.115.
 
[2] X. Zhai, C. Qi, Y. Pan, T. Luo, and L. Liang, "Effects of Screw Pitches and Rotation Angles on Flow and Heat Transfer Characteristics of Nanofluids in Spiral Tubes," International Journal of Heat and Mass Transfer, Vol. 130, pp. 989-1003, 2019, https://doi.org/10.1016/j.ijheatmasstransfer.2018.10.131.
 
[3] A. Asadi, A. H. Nezhad, F. Sarhaddi, and T. Keykha, "Laminar Ferrofluid Heat Transfer in Presence of Non-Uniform Magnetic Field in a Channel with Sinusoidal Wall: A Numerical Study," Journal of Magnetism and Magnetic Materials, Vol. 471, pp. 56-63, 2019, https://doi.org/10.1016/j.jmmm.2018.09.045.
 
[4] M. M. Gabir and D. Alkhafaji, "Comprehensive Review on Double Pipe Heat Exchanger Techniques," in Journal of Physics: Conference Series, 2021, Vol. 1973, No. 1: IOP Publishing, p. 012013, https://doi.org/10.1088/1742-6596/1973/1/012013.
 
[5] Z. Tian et al., "Turbulent Flows in a Spiral Double-Pipe Heat Exchanger: Optimal Performance Conditions Using an Enhanced Genetic Algorithm," International Journal of Numerical Methods for Heat & Fluid Flow, Vol. 30, No. 1, pp. 39-53, 2019, https://doi.org/10.1108/HFF-04-2019-0287.
 
[6] Z. Wu and B. Sundén, "Convective Heat Transfer Performance of Aggregate-Laden Nanofluids," International Journal of Heat and Mass Transfer, Vol. 93, pp. 1107-1115, 2016, https://doi.org/10.1016/j.ijheatmasstransfer.2015.11.032.
 
[7] V. Singh and M. Gupta, "Heat Transfer Augmentation in a Tube Using Nanofluids Under Constant Heat Flux Boundary Condition: A Review," Energy Conversion and Nanagement, Vol. 123, pp. 290-307, 2016, doi: https://doi.org/10.1016/j.enconman.2016.06.035.
 
[8] E. K. Akpinar, "Evaluation of Heat Transfer and Exergy Loss in a Concentric Double Pipe Exchanger Equipped with Helical Wires," Energy Conversion and Management, Vol. 47, No. 18-19, pp. 3473-3486, 2006, doi: https://doi.org/10.1016/j.enconman.2005.12.014.
 
[9] W.-L. Chen and W.-C. Dung, "Numerical Study on Heat Transfer Characteristics of Double Tube Heat Exchangers with Alternating Horizontal or Vertical Oval Cross Section Pipes as Inner Tubes," Energy Conversion and Management, Vol. 49, No. 6, pp. 1574-1583, 2008, https://doi.org/10.1016/j.enconman.2007.12.007.
 
[10] R. Bhadouriya, A. Agrawal, and S. Prabhu, "Experimental and Numerical Study of Fluid Flow and Heat Transfer in an Annulus of Inner Twisted Square Duct and Outer Circular Pipe," International Journal of Thermal Sciences, Vol. 94, pp. 96-109, 2015, https://doi.org/10.1016/j.ijthermalsci.2015.02.019.
 
[11] X. Tang, X. Dai, and D. Zhu, "Experimental and Numerical Investigation of Convective Heat Transfer and Fluid Flow in Twisted Spiral Tube," International Journal of Heat and Mass Transfer, Vol. 90, pp. 523-541, 2015, https://doi.org/10.1016/j.ijheatmasstransfer.2015.06.068.
 
[12] W. Wang, Y. Zhang, B. Li, H. Han, and X. Gao, "Influence of Geometrical Parameters on Turbulent Flow and Heat Transfer Characteristics in Outward Helically Corrugated Tubes," Energy Conversion and Management, Vol. 136, pp. 294-306, 2017, https://doi.org/10.1016/j.enconman.2017.01.029.
 
[13] W. Wang, Y. Zhang, B. Li, and Y. Li, "Numerical Investigation of Tube-Side Fully Developed Turbulent Flow and Heat Transfer in Outward Corrugated Tubes," International Journal of Heat and Mass Transfer, Vol. 116, pp. 115-126, 2018, https://doi.org/10.1016/j.ijheatmasstransfer.2017.09.003.
 
[14] C. Qi, Y.-L. Wan, C.-Y. Li, D.-T. Han, and Z.-H. Rao, "Experimental and Numerical Research on the Flow and Heat Transfer Characteristics of TiO2-Water Nanofluids in a Corrugated Tube," International Journal of Heat and Mass Transfer, Vol. 115, pp. 1072-1084, 2017, https://doi.org/10.1016/j.ijheatmasstransfer.2017.08.098.
 
[15] H. S. Dizaji, S. Jafarmadar, and F. Mobadersani, "Experimental Studies on Heat Transfer and Pressure Drop Characteristics for New Arrangements of Corrugated Tubes in a Double Pipe Heat Exchanger," International Journal of Thermal Sciences, Vol. 96, pp. 211-220, 2015, https://doi.org/10.1016/j.ijthermalsci.2015.05.009.
 
[16] T. N. Verma, P. Nashine, D. V. Singh, T. S. Singh, and D. Panwar, "ANN: Prediction of an Experimental Heat Transfer Analysis of Concentric Tube Heat Exchanger with Corrugated Inner Tubes," Applied Thermal Engineering, Vol. 120, pp. 219-227, 2017, https://doi.org/10.1016/j.applthermaleng.2017.03.126.
 
[17] Z.-j. Jin, B.-z. Liu, F.-q. Chen, Z.-x. Gao, X.-f. Gao, and J.-y. Qian, "CFD Analysis on Flow Resistance Characteristics of Six-Start Spirally Corrugated Tube," International Journal of Heat and Mass Transfer, Vol. 103, pp. 1198-1207, 2016, https://doi.org/10.1016/j.ijheatmasstransfer.2016.08.070.
 
[18] Z.-j. Jin, F.-q. Chen, Z.-x. Gao, X.-f. Gao, and J.-y. Qian, "Effects of Pitch and Corrugation Depth on Heat Transfer Characteristics in Six-Start Spirally Corrugated Tube," International Journal of Heat and Mass Transfer, Vol. 108, pp. 1011-1025, 2017, https://doi.org/10.1016/j.ijheatmasstransfer.2016.12.091.
 
[19] J. Córcoles, J. Moya-Rico, A. Molina, and J. Almendros-Ibáñez, "Numerical and Experimental Study of the Heat Transfer Process in a Double Pipe Heat Exchanger with Inner Corrugated Tubes," International Journal of Thermal Sciences, Vol. 158, p. 106526, 2020, https://doi.org/10.1016/j.ijthermalsci.2020.106526.
 
[20] A. Alamgholilou and E. Esmaeilzadeh, "Experimental Investigation on Hydrodynamics and Heat Transfer of Fluid Flow into Channel for Cooling of Rectangular Ribs by Passive and EHD Active Enhancement Methods," Experimental Thermal and Fluid Science, Vol. 38, pp. 61-73, 2012, https://doi.org/10.1016/j.expthermflusci.2011.11.008.
 
[21] A. Alami nia and A. Campo, "Experimental Study on EHD Heat Transfer Enhancement from Flush-Mounted Ribbons with Different Arrangements of Wire Electrodes in a Channel," Heat and Mass Transfer, Vol. 52, pp. 2823-2831, 2016, https://doi.org/10.1007/s00231-016-1786-5.
 
[22] A. Alami Nia, "Experimental Investigation on Effects of Trapezoidal Ribs on Heat Transfer Enhancement with Electrohydrodynamics Active Method into Duct," AUT Journal of Mechanical Engineering, Vol. 4, No. 4, pp. 493-504, 2020, https://doi.org/10.22060/AJME.2020.16725.5840.
 
[23] M. Khoshvaght-Aliabadi, "Influence of Different Design Parameters and Al2O3-Water Nanofluid Flow on Heat Transfer and Flow Characteristics of Sinusoidal-Corrugated Channels," Energy Conversion and Management, Vol. 88, pp. 96-105, 2014, https://doi.org/10.1016/j.enconman.2014.08.042.
 
[24] A. Fluent, "Ansys Fluent Theory Guide," Ansys Inc., USA, Vol. 15317, pp. 724-746, 2011.
 
[25] D. Choundhury, "Introduction to the Renormalization Group Method and Turbulence Modelling," Fluent Inc., TM-107, 1993.
 
[26] M. Sheikholeslami and K. Vajravelu, "Nanofluid Flow and Heat Transfer in a Cavity with Variable Magnetic Field," Applied Mathematics and Computation, Vol. 298, pp. 272-282, 2017, https://doi.org/10.1016/j.amc.2016.11.025.
 
[27] J. Choi and Y. Zhang, "Numerical Simulation of Laminar Forced Convection Heat Transfer of Al2O3–Water Nanofluid in a Pipe with Return Bend," International Journal of Thermal Sciences, Vol. 55, pp. 90-102, 2012, https://doi.org/10.1016/j.ijthermalsci.2011.12.017.
 
[28] F.-S. Lien and M. Leschziner, "Assessment of Turbulence-transport Models Including Non-Linear RNG Eddy-Viscosity Formulation and Second-Moment Closure for Flow Over a Backward-Facing Step," Computers & Fluids, Vol. 23, No. 8, pp. 983-1004, 1994, https://doi.org/10.1016/0045-7930(94)90001-9.
 
[29] M. Gibson and B. Launder, "Ground Effects on Pressure Fluctuations in the Atmospheric Boundary Layer," Journal of Fluid Mechanics, Vol. 86, No. 3, pp. 491-511, 1978, https://doi.org/10.1017/S0022112078001251.
 
[30] W. Wang, Y. Zhang, J. Liu, B. Li, and B. Sundén, "Numerical Investigation of Entropy Generation of Turbulent Flow in a Novel Outward Corrugated Tube," International Journal of Heat and Mass Transfer, Vol. 126, pp. 836-847, 2018, https://doi.org/10.1016/j.ijheatmasstransfer.2018.06.017.
 
[31] Y. Malmir-Chegini and N. Amanifard, "Heat Transfer Enhancement Inside Semi-Insulated Horizontal Pipe by Controlling the Secondary Flow of Oil-Based Ferro-Fluid in the Presence of Non-Uniform Magnetic Field: A General Correlation for the Nusselt Number," Applied Thermal Engineering, Vol. 159, p. 113839, 2019, https://doi.org/10.1016/j.applthermaleng.2019.113839.
 
[32] T. J. Rennie and V. G. Raghavan, "Numerical Studies of a Double-Pipe Helical Heat Exchanger," Applied Thermal Engineering, Vol. 26, No. 11-12, pp. 1266-1273, 2006, https://doi.org/10.1016/j.applthermaleng.2005.10.030.
 
[33] M. Jagirdar and P. S. Lee, "Mathematical Modeling and Performance Evaluation of a Desiccant Coated Fin-Tube Heat Exchanger," Applied Energy, Vol. 212, pp. 401-415, 2018, https://doi.org/10.1016/j.apenergy.2017.12.038.
 
[34] C.-W. Lu, J.-M. Huang, W. Nien, and C.-C. Wang, "A Numerical Investigation of the Geometric Effects on the Performance of Plate Finned-Tube Heat Exchanger," Energy Conversion and Management, Vol. 52, No. 3, pp. 1638-1643, 2011, https://doi.org/10.1016/j.enconman.2010.10.026.

  • Receive Date 29 April 2022
  • Revise Date 05 August 2022
  • Accept Date 30 January 2023