Evaluation of Performance of both Spiral and Direct Tube Heat Exchanger Using the Hybrid Nano fluid

Authors

1 Department of Mechanical Engineering, University of Kashan, Kashan, Iran

2 Faculty of Engineering, Shahreza Branch, Islamic Azad University, Shahreza, Iran

Abstract

In this study, the comparison of the heat transfer of heat exchanger of the spiral tube and the direct pipe using the hybrid nanofluid in the turbulent flow has been empirically investigated.The nano fluid used in this study consists of a mixture of titanium oxide, silicon oxide and magnesium oxide with a medium diameter (20-30 nm) in a base water fluid at a temperature range of 60 to 30 ° C. Nanoparticles have been used in the volume fractions range of 0.25, 0.5, 0.75 and 1%.The results showed that the Nusselt number increased by increasing the Reynolds number and the concentration in the spiral tube compared to the direct tube by 6.6% on average. Also, the results are reported as temperature difference, the use of nanoparticles in the spiral tube is higher than the direct tube in the volume fraction of 0.25% and the temperature of 60 ° C, 37.6%. The percentage increase in the optimal temperature difference of the hybrid nano fluid in the spiral tube in the volume fraction is 0.25% and 60 ° C, which is 10% higher than the base fluid and in the direct tube in the volume fraction of 0.75% and 60 ° C Compared to the base fluid, the temperature difference is increased by 6%.

Keywords


[1] Kakac S, Bergles AE, Mayinger F, Yuncu H (eds) (2013) Heat transfer enhancement of heat exchangers.  Springer  Science and  Business Media 355.
[2] Choi SUS (1995) Enhancing conductivity of fluids with nanoparticles. ASME Fluid Eng, Division 231: 99-105.
[3] Coronel P, Sandeep KP (2008) Heat transfer coefficient in helical heat exchangers under turbulent flow conditions. Int J Food Eng 4(1).
[4] Jayakumar JS, Mahajani SM, Mandal JC, Iyer KN, Vijayan PK (2010) CFD analysis of single-phase flows inside helically coiled tubes. Comput Chem Eng 34(4): 430-446.
[5] Xie H, Li Y, Yu W (2010) Intriguingly high convective heat transfer enhancement of nanofluid coolants in laminar flows. Phys Lett A 374(25): 2566-2568.
[6] Farajollahi B, Etemad SG, Hojjat M (2010) Heat transfer of nanofluids in a shell and tube heat exchanger. Int J Heat Mass Transf 53(1-3): 12-17.
[7] Narrein K, Mohammed HA (2013) Influence of nanofluids and rotation on helically coiled tube heat exchanger performance. Thermochim Acta 564: 13-23.
 [8] امانی ج، عباسیان آرانی ع ا (1393) مطالعه تجربی انتقال حرارت و افت فشار نانوسیال آب-اکسید تیتانیوم. نشریه علمی پژوهشی امیرکبیر 88-79 :(1)46.
[9] Darzi AR, Farhadi M, Sedighi K (2013) Heat transfer and flow characteristics of AL2O3–water nanofluid in a double tube heat exchanger. Int J Heat Mass Transf 47: 105-112.
[10] Kahani M, Heris SZ, Mousavi SM (2013) Effects of curvature ratio and coil pitch spacing on heat transfer performance of Al2O3/water nanofluid laminar flow through helical coils. J Dispers Sci Technol 34(12): 1704-1712.
[11] Kahani M, Heris SZ, Mousavi SM (2013) Comparative study between metal oxide nanopowders on thermal characteristics of nanofluid flow through helical coils. Powder Technol 246: 82-92.
[12] Aly WI (2014) Numerical study on turbulent heat transfer and pressure drop of nanofluid in coiled tube-in-tube heat exchangers. Energ Convers Manage 79: 304-316.
[13] Rakhsha M, Akbaridoust F, Abbassi A, Majid SA (2015) Experimental and numerical investigations of turbulent forced convection flow of nano-fluid in helical coiled tubes at constant surface temperature. Powder Technol 283: 178-189.
[14] Doshmanziari FI, Zohir AE, Kharvani HR, Jalali-Vahid D, Kadivar MR (2016) Characteristics of heat transfer and flow of Al2O3/water nanofluid in a spiral-coil tube for turbulent pulsating flow. Int J Heat Mass Transf 52(7): 1305-1320.
[15] Mahmoudi M, Tavakoli MR, Mirsoleimani MA, Gholami A, Salimpour MR (2017) Experimental and numerical investigation on forced convection heat transfer and pressure drop in helically coiled pipes using TiO2/water nanofluid. Int J Refrig 74: 627-643.
[16] Nield DA, Kuznetsov AV (2009) The Cheng–Minkowycz problem for natural convective boundary-layer flow in a porous medium saturated by a nanofluid. Int J Heat Mass Transf 52(25-26): 5792-5795.
[17] Pak BC, Cho YI (1998) Hydrodynamic and heat transfer study of dispersed fluids with submicron metallic oxide particles. Exp Heat Transf 11(2): 151-170.
[18] Xuan Y, Roetzel W (2000) Conceptions for heat transfer correlation of nanofluids. Int J Heat Mass Transf 43(19): 3701-3707.
[19] Brinkman HC (1952) The viscosity of concentrated suspensions and solutions. J Chem Phys 20(4): 571-571.
[20] Wasp E,  Kenny J, Gandhi R (1999) S.1.S.P. Transportation, Bulk Materials Handling. Trans Tech Publications, Germany.
[21] Shah RK, Sekulic DP (2003) Fundamentals of heat exchanger design. John Wiley & Sons.
[22] Patil RK, Shende BW, Ghosh PK (1982) Designing a helical-coil heat exchanger. Chem Eng 92(24): 85-88.
[23] Shah RK, Sekulic DP (2003) Fundamentals of heat exchanger design. John Wiley & Sons.
[24] Young Hugh D (1962) Statistical treatment of experimental data.126-132.
[25] Holman JP (1989) Experimental models for engineers. 5th edn. McGraw-Hill, New York.