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dc.contributor.author | Fahim, Saiyed Tasnim Md. | |
dc.contributor.author | Islam, Rayhanul | |
dc.date.accessioned | 2020-10-31T17:28:25Z | |
dc.date.available | 2020-10-31T17:28:25Z | |
dc.date.issued | 2018-11-15 | |
dc.identifier.citation | [1] R.K. Shah, D.P. Sekulic, Heat exchangers, in: Handbook of Heat Transfer, 1998, p. 3. [2] A. Stankiewicz, J.A. Moulijn, Re-Engineering the Chemical Processing Plant: Process Intensification, CRC Press, 2003. [3] S.A.E. Sayed Ahmed, O.M. Mesalhy, M.A. Abdelatief, Flow and heat transfer enhancement in tube heat exchangers, Heat Mass Transfer 51 (11) (2015) 1607–1630. [4] S. Tiggelbeck, M. Fiebig, Flow structure and heat transfer in a channel with multiple longitudinal vortex generators, Exp. Therm. Fluid Sci. 5 (4) (1992) 425–436. [5] B. Ameel, J. Degroote, C. T’Joen, H. Huisseune, S. De Schampheleire, J. Vierendeels, M. De Paepe, Accounting for the effect of the heat exchanger length in the performance evaluation of compact fin and tube heat exchangers, Appl. Therm. Eng. 65 (1–2) (2014) 544–553. [6] B. Gong, L. Wang, Z. Lin, Heat transfer characteristics of a circular tube bank fin heat exchanger with fins punched curve rectangular vortex generators in the wake regions of the tubes, Appl. Therm. Eng. 75 (2015) 224–238. [7] M. Behfard, A. Sohankar, Numerical investigation for finding the appropriate design parameters of a fin-and-tube heat exchanger with delta-winglet vortex generators, Heat Mass Transfer (2015). [8] B. Gong, L. Wang, Z. Lin, Heat transfer characteristics of a circular tube bank fin heat exchanger with fins punched curve rectangular vortex generators in the wake regions of the tubes, Appl. Therm. Eng. 75 (2015) 224–238. [9] Z.M. Lin, C.P. Liu, M. Lin, L.B. Wang, Numerical study of flow and heat transfer enhancement of circular tube bank fin heat exchanger with curved delta winglet vortex generators, Appl. Therm. Eng. 88 (2015) 198–210. [10] Z.M. Lin, L.B. Wang, Y.H. Zhang, Numerical study on heat transfer enhancement of circular tube bank fin heat exchanger with interrupted annular groove fin, Appl. Therm. Eng. 73 (2) (2014) 1465–1476. [11] Y.L. He, H. Han, W.Q. Tao, Y.W. Zhang, Numerical study of heat- transfer enhancement by punched winglet-type vortex generator arrays in fin- andtube heat exchangers, Int. J. Heat Mass Transfer 55 (21–22) (2012) 5449–5458. [12] ANSYS Inc, ANSYS Fluent Theory Guide, 2013. [13] K.M. Kwak, K. Torii, K. Nishino, Simultaneous heat transfer enhancement and pressure loss reduction for finned-tube bundles with the first or two transverse rows of built-in winglets, Exp. Therm. Fluid Sci. 29 (5) (2005) 625– 632. | en_US |
dc.identifier.uri | http://hdl.handle.net/123456789/629 | |
dc.description | Supervised by Dr. Arafat Ahmed Bhuiyan | en_US |
dc.description.abstract | Compact heat exchanger (CHXs) is one of the top choices in residential and industrial applications for its higher thermal efficiency, lower pressure drop, low cost, light weight characteristics. Among various types of compact thermal devices, fin and tube compact heat exchangers are stimulating enormous interest in thermal engineering field. In the present study, airside performance of CHXs having corrugated fin and oval tube are evaluated using a CFD code ANSYS 12.0. Main motivation of this investigation is to find out the pattern of gradual improvement of thermal-hydraulic performance by showing the comparison between plane and corrugated fin geometry. This study has been performed for Reynolds number ranging from 200 to 1000. Here we have analyzed the performance among plane, one, two & three corrugated fin geometry. Also, the variation of tube shape changing the circular tube geometry to oval shape has also been studied. The significant increase of Nusselt number, Friction factor, Colburn factor has been found for the corrugated compact heat exchangers. Results indicate that incurring a moderate pressure loss the corrugated fin patterns can ensure more thermal efficiency. The pattern of gradual improvement of heat transfer rate and slacken pressure loss with the increase of corrugation in a fin with oval shaped tubes has been experienced. | en_US |
dc.language.iso | en | en_US |
dc.publisher | Department of Mechanical and Production Engineering, Islamic University of Technology, Board Bazar, Gazipur, Bangladesh | en_US |
dc.subject | Compact Heat Exchanger, Corrugated channel, friction factor, Colburn factor, Reynolds Number. | en_US |
dc.title | Improvement of Thermal- Hydraulic Performance of Compact Heat Exchangers with Multi-Corrugated Fin and Oval Tube Arrays | en_US |
dc.type | Thesis | en_US |