Heat transfer and friction correlation for compact louvered fin-and-tube heat exchangers
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The e-NTU relations depend on the circuitry arrangement, and reduced data are only meaningful if investigators use correct e-NTU relations.
“As pointed out by Wang et al. [13], e -NTU relations depend on the circuitry arrangement, the reduced data are only meaningful if the investigators use correct e -NTU relations to reduce their test results.”
From Heat transfer and friction characteristics of plain fin-and-tube heat exchangers, part II: Correlation (2000) · cites this paper as [13]
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“In modern heat exchangers this is done through a transition of the angled louvers to a flat fin surface (the so called landing), which is then connected to the tubes through mechanical or hydraulic expansion [9].”
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“[17]) as well as some highly interrupted fin-and-tube heat exchangers like louver, slit, and convex louver [5,18–19] did not reveal this kind of behaviour.”
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“The consistency of the ηoho experimental values obtained through Equations 11 and 12 was evaluated by comparison with the (ηoho)calc values calculated according to the Wang et al. (1999) model.”
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“[16]).”
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“For example in studies by Yashar et al. (2008) and AbdelAziz et al.”
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“The effect of the number of tube row on the heat transfer performance of louver fin geometry surface is negligible either for a flat tube geometry [1–7] or for a round tube configuration [11,12].”
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“(12) is calculated according to the following formulation [17] and using appropriate correlation [25,27,24] to estimate the friction factor parameter depending on fin shape and tube arrangement: ⎡ ⎣ ⎢⎢ ⎛ ⎝⎜ ⎞ ⎠⎟ ⎤ ⎦ ⎥⎥ p G f A A 2 1 1 13 AIR FRIC IN TOT MIN IN AVE IN OUT , 2 2 Δ ρ ρ ρ σ ρ ρ = + ( + ) − ( )”
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“As shown in Figure 8, according to the design parameters of the heat exchanger, variations in the heat transfer coefficient and fin efficiency are predicted using the heat transfer model of Wang et al. (1999).”
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“…heat exchanger are defined with different heat transfer coefficients and pressure Air-side forced convection heat transfer and pressure drop (dry) Wang et al. (1999) Air-side forced convection heat transfer and pressure drop (wet) Wang et al. (2000) Refrigerant-side single-phase heat…”
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- Authors
- Wang, C.-C., Lee, C.-J., Chang, C.-T., & Lin, S.-P.
- Affiliations
- Industrial Technology Research Institute (TW)
- Yuan Ze University (TW)
- Corresponding author
- Wang, C.-C.
- Venue
- International Journal of Heat and Mass Transfer
- Publisher
- Elsevier BV
- Published
- 1999-06
- Volume
- 42
- Issue
- 11
- Pages
- 1945-1956
- ISSN
- 0017-9310 (ISSN-L)
- OpenAlex
- W2004327662
- Cited by
- 265
- References
- 0
- Citations by year
- 2026: 8 · 2025: 10 · 2024: 11 · 2023: 11 · 2022: 9 · 2021: 5 · 2020: 12 · 2019: 19 · 2018: 15 · 2017: 14 · 2016: 19 · 2015: 16 · 2014: 17 · 2013: 10 · 2012: 28
- FWCI
- 12.82
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- International Journal of Heat and Mass Transfer (publishedVersion)
- Funders
- Industrial Technology Research Institute
- Topics
- Physical Sciences › Engineering › Mechanical Engineering › Heat Transfer and Optimization
- Physical Sciences › Engineering › Mechanical Engineering › Heat Transfer Mechanisms
- Physical Sciences › Engineering › Mechanical Engineering › Heat Transfer and Boiling Studies
- Keywords
- louvered fins, finned tube heat exchanger, heat transfer correlations, friction factor correlation, round tubes, fin spacing, tube pitch, compact heat exchangers
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