Numerical study of shell and tube heat exchanger with different cross-section tubes and combined tubes
- Department of Mechanic, Faculty of Engineering, South Tehran Branch, Islamic Azad University, Tehran, IR
- Department of Energy Systems Engineering, Faculty of Engineering, South Tehran Branch, Islamic Azad University, Tehran, IR
- Faculty of Mechanical Engineering, K.N. Toosi University of Technology, Tehran, IR
Published in Issue 2019-02-12
How to Cite
Saffarian, M. R., Fazelpour, F., & Sham, M. (2019). Numerical study of shell and tube heat exchanger with different cross-section tubes and combined tubes. International Journal of Energy and Environmental Engineering, 10(1 (March 2019). https://doi.org/10.1007/s40095-019-0297-9
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Abstract
Abstract Shell and tube heat exchangers are used in various industrial processes, and are one of the most commonly used heat exchangers. A shell and tube heat exchanger with a 25% baffle cut was used in this study. Tubes of different cross-sections (circular, elliptical with an attack angle of 90° and elliptical with an attack angle of 0°) were studied. A combined model of a shell and tube heat exchanger with elliptical tubes with an attack angle of 90° and circular tubes was introduced. A heat exchanger with ellipsoidal tubes near the shell with an attack angle of 90° and circular tubes in the center of the shell showed the highest heat transfer compared with the shell and tube heat exchangers with circular tubes and elliptical tubes with an attack angle of 90° and 0°. The pressure drop in the tube and shell side was also investigated for all five cases in this study. The effect of the location of tubes on heat transfer was investigated. It was shown that tubes located near the shell have a greater impact on heat transfer compared with tubes located in the center of the shell.Keywords
- Shell and tube heat exchanger,
- Elliptical tubes,
- Circular tubes,
- Heat transfer,
- Pressure drop
References
- Yang et al. (2015) Numerical investigation on shell-side performances of combined parallel and serial two shell-pass shell-and-tube heat exchangers with continuous helical baffles (pp. 163-174) https://doi.org/10.1016/j.apenergy.2014.11.029
- Labbadlia et al. (2017) Numerical study of the influence of tube arrangement on the flow distribution in the header of shell and tube heat exchangers (pp. 315-321) https://doi.org/10.1016/j.applthermaleng.2017.07.184
- He et al. (2016) Numerical investigation on performance comparison of non-Newtonian fluid flow in vertical heat exchangers combined helical baffle with elliptic and circular tubes (pp. 84-97) https://doi.org/10.1016/j.applthermaleng.2016.02.033
- Ayub et al. (2018) Performance characteristics of a novel shell and tube heat exchanger with shell side interstitial twisted tapes for viscous fluids application (pp. 248-255) https://doi.org/10.1016/j.applthermaleng.2018.01.054
- Qiu et al. (2018) An experimental study on the heat transfer performance of a prototype molten-salt rod baffle heat exchanger for concentrated solar power (pp. 63-72) https://doi.org/10.1016/j.energy.2018.05.040
- Ibrahim and Gomaa (2009) Thermal performance criteria of elliptic tube bundle in crossflow 48(11) (pp. 2148-2158) https://doi.org/10.1016/j.ijthermalsci.2009.03.011
- Horvat et al. (2006) Comparison of heat transfer conditions in tube bundle cross-flow for different tube shapes 49(5–6) (pp. 1027-1038) https://doi.org/10.1016/j.ijheatmasstransfer.2005.09.030
- Fazelpour, F., Vafaeipour, M., Rahbari, O.: CFD simulation of hydrodynamics of gas-solid two-phase flow for different geometries of solid particles. The 5th International Congress of Energy and Environment Engineering and Management, Lisbon (2013)
- Bonilla et al. (2017) Study on shell-and-tube heat exchanger models with different degree of complexity for process simulation and control design (pp. 1425-1440) https://doi.org/10.1016/j.applthermaleng.2017.06.129
- Skoglund et al. (2006) Dynamic object-oriented heat exchanger models for simulation of fluid property transitions 49(13–14) (pp. 2291-2303) https://doi.org/10.1016/j.ijheatmasstransfer.2005.12.005
- Zaversky et al. (2014) Object-oriented modeling for the transient response simulation of multi-pass shell-and-tube heat exchangers as applied in active indirect thermal energy storage systems for concentrated solar power (pp. 647-664) https://doi.org/10.1016/j.energy.2013.11.070
- Shahdad and Fazelpour (2018) Numerical analysis of the surface and geometry of plate fin heat exchangers for increasing heat transfer rate 9(2) (pp. 155-167) https://doi.org/10.1007/s40095-018-0270-z
- Xie et al. (2018) A numerical study on heat transfer enhancement and flow structure in enhanced tube with cross ellipsoidal dimples (pp. 434-444) https://doi.org/10.1016/j.ijheatmasstransfer.2018.04.106
- Matos et al. (2004) Three-dimensional optimization of staggered finned circular and elliptic tubes in forced convection 43(5) (pp. 477-487) https://doi.org/10.1016/j.ijthermalsci.2003.10.003
- Matos et al. (2004) Optimally staggered finned circular and elliptic tubes in forced convection 47(6–7) (pp. 1347-1359) https://doi.org/10.1016/j.ijheatmasstransfer.2003.08.015
- Matos et al. (2001) Optimization study and heat transfer comparison of staggered circular and elliptic tubes in forced convection 44(20) (pp. 3953-3961) https://doi.org/10.1016/S0017-9310(01)00006-0
- Bouris et al. (2001) Numerical evaluation of alternate tube configurations for particle deposition rate reduction in heat exchanger tube bundles 22(5) (pp. 525-536) https://doi.org/10.1016/S0142-727X(01)00110-2
- Nouri-Borujerdi and Lavasani (2007) Experimental study of forced convection heat transfer from a cam shaped tube in cross flows 50(13–14) (pp. 2605-2611) https://doi.org/10.1016/j.ijheatmasstransfer.2006.11.028
- Nouri-Borujerdi and Lavasani (2008) Pressure loss and heat transfer characterization of a cam-shaped cylinder at different orientations 130(12) https://doi.org/10.1115/1.2969259
- Moawed (2011) Experimental study of forced convection from helical coiled tubes with different parameters 52(2) (pp. 1150-1156) https://doi.org/10.1016/j.enconman.2010.09.009
- Rosen and Dincer (2003) Exergy methods for assessing and comparing thermal storage systems 27(4) (pp. 415-430) https://doi.org/10.1002/er.885
- Mohanty et al. (2018) Thermal performance of mixed tube bundle composed of circular and elliptical tubes (pp. 492-505) https://doi.org/10.1016/j.tsep.2018.02.009
- Harris and Goldschmidt (2002) Measurements of the overall heat transfer from combustion gases confined within elliptical tube heat exchangers 26(1) (pp. 33-37) https://doi.org/10.1016/S0894-1777(02)00105-X
- Khan et al. (2004) An experimental characterization of cross-flow cooling of air via an in-line elliptical tube array 25(4) (pp. 636-648) https://doi.org/10.1016/j.ijheatfluidflow.2004.01.002
- Li, Z., Davidson, J., Mantell, S.: Numerical simulation of flow field and heat transfer of streamlined cylinders in crossflow. In: ASME 2005 Summer Heat Transfer Conference collocated with the ASME 2005 Pacific Rim Technical Conference and Exhibition on Integration and Packaging of MEMS, NEMS, and Electronic Systems 2005, pp. 531–541. American Society of Mechanical Engineers
- Li et al. (2006) Experimental study on friction factor and numerical simulation on flow and heat transfer in an alternating elliptical axis tube 26(17–18) (pp. 2336-2344) https://doi.org/10.1016/j.applthermaleng.2006.03.001
- Tao et al. (2007) Three-dimensional numerical study and field synergy principle analysis of wavy fin heat exchangers with elliptic tubes 28(6) (pp. 1531-1544) https://doi.org/10.1016/j.ijheatfluidflow.2007.02.001
- Pal et al. (2016) CFD simulations of shell-side flow in a shell-and-tube type heat exchanger with and without baffles (pp. 314-340) https://doi.org/10.1016/j.ces.2016.01.011
- Markowski et al. (2013) Identification of the influence of fouling on the heat recovery in a network of shell and tube heat exchangers (pp. 755-764) https://doi.org/10.1016/j.apenergy.2012.08.038
- Yang et al. (2014) Optimization of shell-and-tube heat exchangers conforming to TEMA standards with designs motivated by constructal theory (pp. 468-476) https://doi.org/10.1016/j.enconman.2013.11.008
- Dinçer, İ., Zamfirescu, C.: Appendix B Thermophysical Properties of Water. Drying Phenomena: Theory and Applications, pp. 457–459
- Hilsenrath (1960) Pergamon Press
- Multiphysics, C.: Comsol multiphysics user guide (version 4.3 a). COMSOL, AB, 39-40 (2012)
- Oberg (2012) Industrial Press
- Pepper and Heinrich (2005) Taylor & Francis https://doi.org/10.1201/9780203942352
- Zimmerman (2006) World Scientific Publishing Company https://doi.org/10.1142/6141
- El Maakoul et al. (2016) Numerical comparison of shell-side performance for shell and tube heat exchangers with trefoil-hole, helical and segmental baffles (pp. 175-185) https://doi.org/10.1016/j.applthermaleng.2016.08.067
- Azar et al. (2014) Tube bundle replacement for segmental and helical shell and tube heat exchangers: experimental test and economic analysis 62(2) (pp. 622-632) https://doi.org/10.1016/j.applthermaleng.2013.10.009
- Allen and Gosselin (2008) Optimal geometry and flow arrangement for minimizing the cost of shell-and-tube condensers 32(10) (pp. 958-969) https://doi.org/10.1002/er.1398
- Kumar et al. (2018) Effect of twisted tape inserts on heat transfer, friction factor of Fe3O4 nanofluids flow in a double pipe U-bend heat exchanger (pp. 53-62) https://doi.org/10.1016/j.icheatmasstransfer.2018.03.020
- Gaddis and Gnielinski (1997) Pressure drop on the shell side of shell-and-tube heat exchangers with segmental baffles 36(2) (pp. 149-159) https://doi.org/10.1016/S0255-2701(96)04194-3
- Kakac et al. (2012) CRC Press https://doi.org/10.1201/b11784
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