2002
DOI: 10.1016/s0140-7007(01)00049-4
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Empirical correlations for heat transfer and flow friction characteristics of herringbone wavy fin-and-tube heat exchangers

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Cited by 112 publications
(45 citation statements)
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“…For both inline and staggered arrangements, it was observed that the pressure drop increases and the heat transfer coefficient decreases with an increase in the tube diameter. The reason was believed to be the ineffective area behind the tubes as explained by Wang et al (2002). The heat transfer coefficient decreased with an increase in the fin height for both the arrangements; however, the pressure drop was independent of the fin height for the staggered arrangement, whereas it increased with an increase in the fin height for the inline arrangement.…”
Section: Side Viewmentioning
confidence: 90%
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“…For both inline and staggered arrangements, it was observed that the pressure drop increases and the heat transfer coefficient decreases with an increase in the tube diameter. The reason was believed to be the ineffective area behind the tubes as explained by Wang et al (2002). The heat transfer coefficient decreased with an increase in the fin height for both the arrangements; however, the pressure drop was independent of the fin height for the staggered arrangement, whereas it increased with an increase in the fin height for the inline arrangement.…”
Section: Side Viewmentioning
confidence: 90%
“…To validate the selfdeveloped code, the results were compared with Wang et al (2002) and Xin et al (1994). It was observed that, Nu increases and the friction factor and fin efficiency decrease with an increase in the Reynolds number.…”
Section: Plate Finsmentioning
confidence: 99%
“…The wavy fin extended surfaces are recognized by the wavy corrugations which boost the heat transfer performance in contrast to the plain plate surfaces. In last decades, several efforts have been devoted to investigate the fundamentals and performance related issues in different experimental works (Kim, Youn et al 1996, Wang, Fu et al 1997, Wang 1999, Yan and Sheen 2000, Wang, Hwang et al 2002, Pirompugd, Wongwises et al 2006, Junqi, Jiangping et al 2007, Kim, Ham et al 2008, Wang, Liaw et al 2011, Dong, Chen et al 2012, Dong, Su et al 2013, Du, Feng et al 2013, Wu, Wu et al 2014. Also a number of numerical attempts have been accomplished in 2D/3D analysis (Jang and Chen 1997, Bhuiyan, Zaman et al 2010, Bhuiyan, Islam et al 2011, Glazar, Trp et al 2012, Gong, Min et al 2013, Bhuiyan, Amin et al 2014, Lin, Wang et al 2014.…”
Section: Introductionmentioning
confidence: 99%
“…They also gave correlations for use in describing the Colburn factor and friction factor. (Wang et al 2002) proposed the most updated heat transfer coefficient and friction factor correlations wavy fin-and-tube heat exchangers.…”
Section: Introductionmentioning
confidence: 99%