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In this study, comparative performance of single-segmental baffle and a newly developed baffle –convex-cut in shell-and-tube heat exchanger were both numerically and experimentally investigated. For the numerical analysis, three working fluids (engine oil, water and air) were successively utilised o...
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2020
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| LEADER | 00000njm a2000000a 4500 | ||
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| 001 | oai:repository.ui.edu.ng:123456789/9586 | ||
| 042 | |a dc | ||
| 720 | |a Petinrin, M. O. |e author | ||
| 720 | |a Dare, A. A. |e author | ||
| 260 | |c 2020 | ||
| 520 | |a In this study, comparative performance of single-segmental baffle and a newly developed baffle –convex-cut in shell-and-tube heat exchanger were both numerically and experimentally investigated. For the numerical analysis, three working fluids (engine oil, water and air) were successively utilised on the shell-side of heat exchangers with 30, 35, 40 and 45% convex-cut (CeC_STHE) and 25% segmental (SS_STHE) baffles, and the resulting models were solved in COMSOL Multiphysics. Experiments were carried out on 30% CeC_STHE and SS_STHE exclusively running on water. The data obtained were used to determine the weighted shell-side heat transfer coefficient and weighted performance factor of each heat exchanger. Hence, the results for all the ranges of Reynolds number indicate that the shell-side heat transfer coefficients of all the CeC_STHEs are lower than that of SS_STHE except for the 30% CeC_STHE. However, the SS_STHE showed greater pressure drop than the CeC_STHEs. The choice of working fluid had more influenced on the weighted shell-side heat transfer coefficient CeC_STHE. Moreover, the weighted performance factors of the CeC_STHEs indicated positive values. Thus, 30% CeC_STHE demonstrated a better performance while the 45% had the lowest performance. | ||
| 024 | 8 | |a 2582-2926 | |
| 024 | 8 | |a ui_art_petinrin_numerical_2020 | |
| 024 | 8 | |a Journal of Engineering Research and Reports 13(3), pp. 8-26 | |
| 024 | 8 | |a http://ir.library.ui.edu.ng/handle/123456789/9586 | |
| 653 | |a Shell-and-tube heat exchangers | ||
| 653 | |a Single-segmental baffle | ||
| 653 | |a Convex-cut baffle | ||
| 653 | |a Weighted performance factor | ||
| 653 | |a Weighted heat transfer coefficient | ||
| 245 | 0 | 0 | |a Numerical and experimental investigation on performance of convex-cut baffles in shell-and tube heat exchanger |