In this study, we aim to investigate the heat transfer and flow characteristics of diverse hybrid nanofluids (CuO-ZnO-Water, EG-Water, CuO-EG-Water, SiO2-EG-Water, and Al2O3-EG-Water) as coolants across eight discrete inlet velocities in a shell and tube heat exchanger. Various materials (copper, stainless steel, titanium, and carbon steel) have been employed for the tubing to optimize system performance. The impact of Reynolds number concerning hybrid nanofluids on Nusselt number and friction factor was assessed in this research. The results of the numerical simulations are found to agree well with experimental results within an average deviation of 1.8%. The results indicated the superior heat transfer capabilities of the hybrid nanofluid compared to the base fluid across all conditions. The outcomes revealed the superior heat transfer capabilities of the CuO-ZnO-Water hybrid nanofluid under all tested conditions. When employing CuO-ZnO-Water as a coolant, a substantial increase of over 9% in temperature reduction was observed, as opposed to the approximately 6% attained by other hybrid nanofluids at a lower velocity of 0.5 m/s. Notably, higher Reynolds numbers corresponded to increased Nusselt numbers and decreased friction factors. The decline percentage of the friction factor was 43% at Reynolds number ranging between 10,000 to 40,000. We emphasize the imperative need to optimize nanoparticle types for crafting hybrid nanofluids to enhance the performance of industrial heat exchangers and their coolant efficiency. Ultimately, the utilization of hybrid nanofluids in conjunction with shell and tube heat exchanger systems has yielded a notable enhancement in the overall thermal efficiency of these systems.
Citation: Ruaa Al Mezrakchi. Investigation of various hybrid nanofluids to enhance the performance of a shell and tube heat exchanger[J]. AIMS Energy, 2024, 12(1): 235-255. doi: 10.3934/energy.2024011
In this study, we aim to investigate the heat transfer and flow characteristics of diverse hybrid nanofluids (CuO-ZnO-Water, EG-Water, CuO-EG-Water, SiO2-EG-Water, and Al2O3-EG-Water) as coolants across eight discrete inlet velocities in a shell and tube heat exchanger. Various materials (copper, stainless steel, titanium, and carbon steel) have been employed for the tubing to optimize system performance. The impact of Reynolds number concerning hybrid nanofluids on Nusselt number and friction factor was assessed in this research. The results of the numerical simulations are found to agree well with experimental results within an average deviation of 1.8%. The results indicated the superior heat transfer capabilities of the hybrid nanofluid compared to the base fluid across all conditions. The outcomes revealed the superior heat transfer capabilities of the CuO-ZnO-Water hybrid nanofluid under all tested conditions. When employing CuO-ZnO-Water as a coolant, a substantial increase of over 9% in temperature reduction was observed, as opposed to the approximately 6% attained by other hybrid nanofluids at a lower velocity of 0.5 m/s. Notably, higher Reynolds numbers corresponded to increased Nusselt numbers and decreased friction factors. The decline percentage of the friction factor was 43% at Reynolds number ranging between 10,000 to 40,000. We emphasize the imperative need to optimize nanoparticle types for crafting hybrid nanofluids to enhance the performance of industrial heat exchangers and their coolant efficiency. Ultimately, the utilization of hybrid nanofluids in conjunction with shell and tube heat exchanger systems has yielded a notable enhancement in the overall thermal efficiency of these systems.
[1] | Mohammadi MH, Abbasi HR, Yavarinasab A, et al. (2020) Thermal optimization of shell and tube heat exchanger using porous baffles. Appl Therm Eng 170: 115005. https://doi.org/10.1016/j.applthermaleng.2020.115005 doi: 10.1016/j.applthermaleng.2020.115005 |
[2] | Edreis E, Petrov A (2020) Types of heat exchangers in industry, their advantages and disadvantages, and the study of their parameters. IOP Conf Ser: Mater Sci Eng 963: 012027. https://doi.org/10.1088/1757-899X/963/1/012027 doi: 10.1088/1757-899X/963/1/012027 |
[3] | Smith R, Pan M, Bulatov I (2013) 32-Heat transfer enhancement in heat exchanger networks. In: Klemeš, Jiří J., Handbook of Process Integration (PI), Woodhead Publishing Series in Energy, 966–1037. https://doi.org/10.1533/9780857097255.5.966 |
[4] | Di Pretoro A, D'Iglio F, Manenti F (2021) Optimal cleaning cycle scheduling under uncertain conditions: A flexibility analysis on heat exchanger fouling. Processes 9: 93. https://doi.org/10.3390/pr9010093 doi: 10.3390/pr9010093 |
[5] | Arsenyeva O, Orosz Á, Friedler F (2021) Retrofit synthesis of industrial heat exchanger networks with different types of heat exchangers. Chem Eng Trans 88: 613–618. https://doi.org/10.3303/CET2188102 doi: 10.3303/CET2188102 |
[6] | Mehrjardi SAA, Khademi A, Said Z, et al. (2023) Effect of elliptical dimples on heat transfer performance in a shell and tube heat exchanger. Heat Mass Transf 59: 1781–1791. https://doi.org/10.1007/s00231-023-03367-7 doi: 10.1007/s00231-023-03367-7 |
[7] | Bejan A (1982) Entropy generation through heat and fluid flow. 1st Edition, John Wiley & Sons. |
[8] | Bejan A, Tsatsaronis G, Moran MJ (1996) Thermal design and optimization. John Wiley & Sons. |
[9] | Vivekh P, Bui DT, Islam MR, et al. (2020) Experimental performance evaluation of desiccant coated heat exchangers from a combined first and second law of thermodynamics perspective. Energy Convers Manag 207: 112518. https://doi.org/10.1016/j.enconman.2020.112518 doi: 10.1016/j.enconman.2020.112518 |
[10] | Agyenim F, Eames P, Smyth M (2009) A comparison of heat transfer enhancement in a medium temperature thermal energy storage heat exchanger using fins. Sol Energy 83: 1509–1520. https://doi.org/10.1016/j.solener.2009.04.007 doi: 10.1016/j.solener.2009.04.007 |
[11] | Sahin B, Demir A (2008) Performance analysis of a heat exchanger having perforated square fins. Appl Therm Eng 28: 621–632. https://doi.org/10.1016/j.applthermaleng.2007.04.003 doi: 10.1016/j.applthermaleng.2007.04.003 |
[12] | Craig S, Grinham J (2017) Breathing walls: The design of porous materials for heat exchange and decentralized ventilation. Energy Build 149: 246–259. https://doi.org/10.1016/j.enbuild.2017.05.036 doi: 10.1016/j.enbuild.2017.05.036 |
[13] | Dehghan M, Valipour MS, Saedodin S (2016) Microchannels enhanced by porous materials: Heat transfer enhancement or pressure drop increment? Energy Convers Manag 110: 22–32. https://doi.org/10.1016/j.enconman.2015.11.052 doi: 10.1016/j.enconman.2015.11.052 |
[14] | Yang J, Liu W (2015) Numerical investigation on a novel shell-and-tube heat exchanger with plate baffles and experimental validation. Energy Convers Manag 101: 689–696. https://doi.org/10.1016/j.enconman.2015.05.066 doi: 10.1016/j.enconman.2015.05.066 |
[15] | Nanan K, Thianpong C, Pimsarn M, et al. (2017) Flow and thermal mechanisms in a heat exchanger tube inserted with twisted cross-baffle turbulators. Appl Therm Eng 114: 130–147. https://doi.org/10.1016/j.applthermaleng.2016.11.153 doi: 10.1016/j.applthermaleng.2016.11.153 |
[16] | Tawfik MA, Kadhim ZK, Hammoudi RY (2009) Vibration analysis of sudden enlargement pipe conveying fluid with presence of heat flux. Eng Technol 27: 533–557. https://doi.org/10.30684/etj.27.3.10 doi: 10.30684/etj.27.3.10 |
[17] | Geete A, Pathak R (2019) Effect of surface roughness on the performance of heat exchanger. SN Appl Sci 1: 901. https://doi.org/10.1007/s42452-019-0954-x doi: 10.1007/s42452-019-0954-x |
[18] | Attalla M, Maghrabie HM (2020) Investigation of effectiveness and pumping power of plate heat exchanger with rough surface. Chem Eng Sci 211: 115277. https://doi.org/10.1016/j.ces.2019.115277 doi: 10.1016/j.ces.2019.115277 |
[19] | Kumar V, Tiwari AK, Ghosh SK (2015) Application of nanofluids in plate heat exchanger: A review. Energy Convers Manag 105: 1017–1036. https://doi.org/10.1016/j.enconman.2015.08.053 doi: 10.1016/j.enconman.2015.08.053 |
[20] | Tiwari AK, Ghosh P, Sarkar J (2013) Performance comparison of the plate heat exchanger using different nanofluids. Exp Therm Fluid Sci 49: 141–151. https://doi.org/10.1016/j.expthermflusci.2013.04.012 doi: 10.1016/j.expthermflusci.2013.04.012 |
[21] | Sivashanmugam P (2012) Application of nanofluids in heat transfer. In An Overview of Heat Transfer Phenomena, 16. https://doi.org/10.5772/52496 |
[22] | Kumar N, Urkude N, Sonawane SS, et al. (2018) Experimental study on pool boiling and critical heat flux enhancement of metal oxides based nanofluid. Int Commun Heat Mass Transf 96: 37–42. https://doi.org/10.1016/j.icheatmasstransfer.2018.05.018 doi: 10.1016/j.icheatmasstransfer.2018.05.018 |
[23] | Malika M, Sonawane SS (2021) The sono-photocatalytic performance of a novel water based Ti+4 coated Al(OH)3-MWCNT's hybrid nanofluid for dye fragmentation. Int J Chem React Eng 19: 901–912. https://doi.org/10.1515/ijcre-2021-0092 doi: 10.1515/ijcre-2021-0092 |
[24] | Bergman TL, Lavine AS (2017) Fundamentals of heat and mass transfer. 8th ed. John Wiley & Sons. |
[25] | Hibbeler RC (2016) Mechanics of materials. 10th ed. Pearson. |
[26] | Namburu PK, Das DK, Tanguturi KM, et al. (2009) Numerical study of turbulent flow and heat transfer characteristics of nanofluids considering variable properties. Int J Therm Sci 48: 290–302. https://doi.org/10.1016/j.ijthermalsci.2008.01.001 doi: 10.1016/j.ijthermalsci.2008.01.001 |
[27] | Malika M, Bhad R, Sonawane SS (2021) ANSYS simulation study of a low volume fraction CuO-ZnO/Water hybrid nanofluid in a shell and tube heat exchanger. J Indian Chem Soc 98: 100200. https://doi.org/10.1016/j.jics.2021.100200 doi: 10.1016/j.jics.2021.100200 |
[28] | Zhou X, Wang Y, Zheng K, et al. (2019) Comparison of heat transfer performance of ZnO-PG, α-Al2O3-PG, and γ-Al2O3-PG nanofluids in car radiator. Nanomater Nanotechnol 9. https://doi.org/10.1177/1847980419876465 |
[29] | Radkar RN, Bhanvase BA, Barai DP, et al. (2019) Intensified convective heat transfer using ZnO nanofluids in heat exchanger with helical coiled geometry at constant wall temperature. Mater Sci Energy Technol 2: 161–170. https://doi.org/10.1016/j.mset.2019.01.007 doi: 10.1016/j.mset.2019.01.007 |
[30] | Rott N (1990) Note on the history of the Reynolds number. Annual review of fluid mechanics 22: 1–12. https://doi.org/10.1146/annurev.fl.22.010190.000245 doi: 10.1146/annurev.fl.22.010190.000245 |
[31] | White FM (2006) Viscous fluid flow. 3rd ed., McGraw-Hill New York, 629. |
[32] | Gnielinski V (1976) New equations for heat and mass transfer in turbulent pipe and channel flow. Int J Chem Eng 16: 359–367. |
[33] | Duangthongsuk W, Wongwises S (2009) Heat transfer enhancement and pressure drop characteristics of TiO2-water nanofluid in a double-tube counter flow heat exchanger. Int J Heat Mass Transf 52: 2059–2067. https://doi.org/10.1016/j.ijheatmasstransfer.2008.10.023 doi: 10.1016/j.ijheatmasstransfer.2008.10.023 |
[34] | Albadr J (2018) Thermal performance of shell and tube heat exchanger using PG/Water and Al2O3 nanofluid. In Advances in Heat Exchangers. IntechOpen. https://doi.org/10.5772/intechopen.80082 |
[35] | Ahmed HE, Ahmed MI, Yusoff MZ (2015) Heat transfer enhancement in a triangular duct using compound nanofluids and turbulators. Appl Therm Eng 91: 191–201. https://doi.org/10.1016/j.applthermaleng.2015.07.061 doi: 10.1016/j.applthermaleng.2015.07.061 |
[36] | Aminfar H, Motallebzadeh R (2012) Investigation of the velocity field and nanoparticle concentration distribution of nanofluid using Lagrangian-Eulerian approach. J Dispers Sci Technol 33: 155–163. https://doi.org/10.1080/01932691.2010.528336 doi: 10.1080/01932691.2010.528336 |
[37] | Nourafkan E, Karimi G, Moradgholi J (2015) Experimental study of laminar convective heat transfer and pressure drop of cuprous oxide/water nanofluid inside a circular tube. Exp Heat Transf 28: 58–68. https://doi.org/10.1080/08916152.2013.803178 doi: 10.1080/08916152.2013.803178 |