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Air-side performance of herringbone wavy fin-and-tube heat exchangers under dehumidifying condition – Data with larger diameter tube
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Under dehumidifying conditions, heat transfer coefficient first remained constant for N=2, then increased for N=4 and decreased for N=8 and 12.
“Under dehumidifying conditions, the heat transfer coefficient first remained constant for N = 2, then increased for N = 4 and decreased for N = 8 and 12.”
For herringbone wavy fins, heat transfer performance under dehumidifying conditions is better than dry, whereas opposite for plane fin geometry.
“for herringbone wavy fins, the heat transfer performance under dehumidifying conditions was better than that under dry conditions, whereas this was opposite for a plane fin geometry.”
Pressure drop under dry and dehumidifying conditions for wavy fin structure is less significant than plain fin configuration.
“the pressure drop under dry and dehumidifying conditions for a wavy fin structure was less significant as compared to that with a plain fin configuration.”
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Research works printed but not linked: 21
- Liu, 2008, Sensible airside performance of fin-and-tube heat exchangers – Data with larger diameter tube, ASHRAE Trans., 114, 379
- Liu, 2010, Airside performance of fin-and-tube heat exchangers in dehumidifying conditions – Data with larger diameter, Int. J. Heat Mass Transfer, 53, 1603, 10.1016/j.ijheatmasstransfer.2009.12.015 · DOI
- Beecher, 1987, Effects of fin pattern on the air-side heat transfer coefficient in plate finned-tube heat exchangers, ASHRAE Trans., 93, 1961
- Webb, 1990, Air-side heat transfer correlations for flat and wavy plate fin-and-tube geometries, ASHRAE Trans., 96, 445
- Wang, 1997, Heat transfer and friction characteristics of typical wavy fin-and-tube heat exchangers, Exp. Thermal Fluid Sci., 14, 174, 10.1016/S0894-1777(96)00056-8 · DOI
- Wang, 1998, A comprehensive study of convex-louver and wavy fin-and-tube heat exchangers, AIAA J. Thermophys. Heat Transfer, 12, 423, 10.2514/2.6354 · DOI
- Wang, 1999, Effect of waffle height on the air-side performance of wavy fin-and-tube heat exchangers, Heat Transfer Eng., 20, 45, 10.1080/014576399271411 · DOI
- Wang, 1999, A heat transfer and friction correlation for wavy fin-and-tube heat exchangers, Int. J. Heat Mass Transfer, 42, 1919, 10.1016/S0017-9310(98)00288-9 · DOI
- Wang, 2002, Empirical correlations for heat transfer and flow friction characteristics of herringbone wavy fin-and-tube heat exchangers, Int. J. Refrigeration, 25, 653, 10.1016/S0140-7007(01)00049-4 · DOI
- Chokeman, 2005, Effect of fin pattern on the air-side performance of herringbone wavy fin-and-tube heat exchangers, Int. J. Heat Mass Transfer, 41, 642, 10.1007/s00231-004-0578-5 · DOI
- Wongwises, 2005, Effect of fin pitch and number of tube rows on the air side performance of herringbone wavy fin and tube heat exchangers, Energy Convers. Manage., 46, 2216, 10.1016/j.enconman.2004.09.011 · DOI
- Wang, 1999, An investigation of wavy fin-and-tube heat exchangers; A contribution to databank, Exp. Heat Transfer, 12, 73, 10.1080/089161599269825 · DOI · Paper page
- Wang, 2011, Air-side performance of herringbone wavy fin-and-tube heat exchangers – Data with larger diameter tube, Int. J. Heat Mass Transfer, 54, 1024, 10.1016/j.ijheatmasstransfer.2010.11.038 · DOI
- Wang, 1997, Performance of plate finned tube heat exchangers under dehumidifying conditions, J. Heat Transfer, 119, 109, 10.1115/1.2824075 · DOI
- Moffat, 1988, Describing the uncertainties in experimental results, Exp. Thermal Fluid Sci., 1, 3, 10.1016/0894-1777(88)90043-X · DOI · Paper page
- McNab, 1998, Numerical modeling of heat transfer and fluid flow over herringbone corrugated fins, Heat transfer, 6, 119
- Hwang, 2006, Experimental study on flow and local heat/mass transfer characteristics inside corrugated duct, Int. J. Heat Fluid Flow, 27, 21, 10.1016/j.ijheatfluidflow.2005.07.001 · DOI
- Lin, 2002, Performance of the herringbone wavy fin under dehumidifying conditions, Int. J. Heat Mass Transfer, 45, 5035, 10.1016/S0017-9310(02)00193-X · DOI
- Wang, 1996, Sensible heat and friction characteristics of plate fin-and-tube heat exchangers having plane fins, Int. J. Refrigeration, 19, 223, 10.1016/0140-7007(96)00021-7 · DOI · Paper page
- Sparrow, 1984, Effect of rounding protruding edges on heat transfer and pressure drop in a duct, Int. J. Heat Mass Transfer, 27, 1715, 10.1016/0017-9310(84)90154-6 · DOI
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Cited by
Sorted by citations
Patil, M. S., Seo, J.-H., & Lee, M.-Y. (2017) · Applied Thermal Engineering · doi:10.1016/j.applthermaleng.2016.11.107 · Cited by 86
Metadata
- Authors
- Wang, C.-C., & Liaw, J.-S.
- Affiliations
- National Yang Ming Chiao Tung University (TW)
- Industrial Technology Research Institute (TW)
- Corresponding author
- Wang, Chi-Chuan
- ORCID
- Wang, Chi-Chuan
- Venue
- International Journal of Heat and Mass Transfer
- Publisher
- Elsevier BV
- Published
- 2012-05
- Volume
- 55
- Issue
- 11-12
- Pages
- 3054-3060
- ISSN
- 0017-9310 (ISSN-L)
- OpenAlex
- W2048346991
- Cited by
- 45
- References
- 0
- Citations by year
- 2026: 1 · 2025: 1 · 2024: 4 · 2023: 1 · 2022: 4 · 2021: 1 · 2020: 1 · 2019: 1 · 2018: 5 · 2017: 6 · 2016: 6 · 2015: 6 · 2014: 5 · 2013: 3
- FWCI
- 6.85
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- International Journal of Heat and Mass Transfer (publishedVersion)
- Funders
- National Science Council
- Topics
- Physical Sciences › Engineering › Mechanical Engineering › Heat Transfer and Optimization
- Physical Sciences › Engineering › Mechanical Engineering › Heat Transfer Mechanisms
- Physical Sciences › Engineering › Mechanical Engineering › Adsorption and Cooling Systems
- Keywords
- finned tube heat exchanger, heat transfer coefficient, pressure drop, fin spacing, plain fins, large-diameter pipes
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