Heat Transfer Augmentation of Compact Heat Exchangers Using Modern Innovative Techniques, A review and Parametric study

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dc.contributor.author Awais, Muhammad
dc.date.accessioned 2021-10-07T06:23:18Z
dc.date.available 2021-10-07T06:23:18Z
dc.date.issued 2017-11-15
dc.identifier.citation [1] Giovannoni, F., and Mattarlo, L., Experimental Researches on the Finned Tube Heat Exchangers with Corrugated Fins, Proc. XVIth Int. Congress of Refrigeration, Paris, paper B.1-493, pp. 215±220, 1983. [2] Beecher, D. T., and Fagan, T. J., Effects of Fin Pattern on the Air-Side Heat Transfer Coefficient in Plate Finned-Tube [3] M. Fiebig, N. Mitra, Y. Dong, Simultaneous heat transfer enhancement and flow loss reduction of fin-tubes, in: Proceedings of the 9th International Heat Transfer Conference 4, Jerusalem, 1990, pp. 51–55. [4] M. Fiebig, Vortex generators for compact heat exchangers, Journal of Enhanced Heat Transfer 2 (1995) 43–61.eat Exchangers, ASHRAE Trans., vol. 93, no. 2, pp. 1961±1984, 1987. [5]: J. Zhang, J. Kundu, R.M. Manglik, Effect of fin waviness and spacing on the lateral vortex structure and laminar heat transfer in wavyplate-fin cores, Int. J. Heat Mass Transfer 47 (2004) 1719–1730. [6]: Y. Asako, M. Faghri, Finite-volume solutions for laminar flow and heat transfer in a corrugated duct, J. Heat Transfer 109 (3) (1987) 627–634. [7]: Y. Asako, H. Nakamura, Heat transfer and pressure drop characteristic in a corrugated duct with rounded corners, Int. J. Heat Mass Transfer 31 (1988) 1237–1245. [8] H.M. Metwally, R.M. Manglik, Enhanced heat transfer due to curvature-induced lateral vortices in laminar flows in sinusoidal corrugated-plate channels, Int. J. Heat Mass Transfer 47 (2004) 2283– 2292. [9] D.R. Sawyers, M. Sen, H.C. Chang, Heat transfer enhancement in three-dimensional corrugated channel flow, Int. J. Heat Mass Transfer 41 (1998) 3559–3573. [10]: M. Fiebig, N. Mitra, Y. Dong, Simultaneous heat transfer enhancement and flow loss reduction of fin-tubes, in: G. Hetsroni (Ed.), Heat Transfer, vol. 3, Hemisphere, Washington, 1990, pp. 51–55. [11] R.L. Manglik, J. Zhang, Low Reynolds number forced convection in three-dimensional wavy-plate-fin compact channels: fin density effects, Int. J. Heat Mass Transfer 48 (2005) 1439–1449. [12] J.L. Goldstein, E.M. Sparrow, Heat mass transfer characteristics for flow in a corrugated wall channel, J. Heat Transfer 99 (1977) 187–195. [13] T.A. Rush, A.M. Newell, A.M. Jacobi, An experimental study of flow and heat transfer in sinusoidal wavy passages, Int. J. Heat Mass Transfer 42 (1999) 1541–1553. [14]: Jacobi, A. M., and Shah, R. K., 1995, ‘‘Heat Transfer Surface Enhancement Through the Use of Longitudinal Vortices: A Review of Recent Progress,’’ Exp. Therm. Fluid Sci., 11, pp. 295–309. [15]: Fiebig, M., Kallweit, P., and Mitra, N. K., 1986, ‘‘Wing Type Vortex Generators for Heat Transfer Enhancement,’’ Heat Transfer 1986, Proc. of 8 Int. Heat Transfer Conf., Hemisphere, New York, Vol. 6, pp. 2903–2908. en_US
dc.identifier.uri http://hdl.handle.net/123456789/1129
dc.description Supervised by Dr. Arafat Ahmed Bhuiyan, Lecturer, Department of Mechanical and Chemical Engineering (MCE), Islamic University of Technology (IUT), Board Bazar, Gazipur-1704, Bangladesh. en_US
dc.description.abstract This project presents a comprehensive review and numerical study on different ways of enhancing heat transfer rate and pressure loss reduction in compact heat exchangers (CHXs). The sole objective of this study is to gather major thermodynamic features of CHXs presented by researchers through both experimental and numerical investigation for innovative designing purpose of heat exchangers. The influence of fins and tubes spacing, geometry and shape on heat transfer performance is widely discussed. The effectuality of different fins types and their pattern, height, pitch/spacing on heat transfer augmentation and pressure drop reduction were considered. It is seen that convex louver fin yields better heat transfer performance than plane and louver fins. The influence of fin spacing on heat transfer performance varied with Reynolds number but their impact on pressure drop is negligible. The impact of elliptical and circular tubes with inline and staggered alignment on heat transfer enhancement and pressure loss is also widely discussed. Staggered alignment as compared to inline alignment of tubes in HXs leads to the higher heat transfer performance at the expense of larger pressure drop and also the optimal position for tubes is at downstream region instead of upstream region due to the significant enhancement of heat transfer performance because of horseshoe vortex formation. A numerical study was performed to acknowledge the influence of vortex generators on heat transfer augmentation and pressure drop reduction. The impact of VGs row numbers with different configuration is widely discussed. The effect of tubes arrangement i.e. inline and staggered on heat transfer performance and pressure drop of compact heat exchanger is also elucidated. It was found that CHXs with vortex generators yield better heat transfer rate as compare to compact heat exchanger without VGs. However, this arrangement yields higher pressure drop. Moreover, it was found that staggered tube arrangement tends to give higher heat transfer performance than inline arrangement of tubes. en_US
dc.language.iso en en_US
dc.publisher Department of Mechanical and Production Engineering (MPE),Islamic University of Technology(IUT), Board Bazar, Gazipur, Bangladesh en_US
dc.title Heat Transfer Augmentation of Compact Heat Exchangers Using Modern Innovative Techniques, A review and Parametric study en_US
dc.type Thesis en_US


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