Numerical assessment of thermohydraulic performance in pipes with different arrangements of delta winglet pairs via the GEKO turbulence model
Öz
This study systematically investigates the effect of varying the number (N) of Delta Winglet Pairs (DWPs) under both constant (CFPA) and non-constant (NCFPA) total frontal projection areas on the thermal–hydraulic performance of tubular heat exchangers. Prior to these investigations, a detailed evaluation of the GEneralized K-Omega (GEKO) turbulence model is performed to ensure its reliability for the present study. The Nusselt number (Nu) and Darcy friction factor (f) of a tubular domain fitted with delta winglet (DW) type vortex generators (VGs) are numerically investigated within Re=5000-25000. The mean absolute deviations of 4.80%, 1.85% and 4.99% are attained with respect to the NuExp., fExp. and TEFExp. respectively. The free parameters are adjusted to C_SEP=1.75 and the corresponding 〖 C〗_MIXCOR (GEKO-1.75). Besides that, the validation of smooth pipe is also carried out and yields an average absolute deviations of 5.42% and 0.85% in comparison to the Dittus-Boelter and Petukhov correlation equations, respectively, with optimized free parameters are set to C_NW=-1.18-2,C_(NW-SUB)=1.7-2.5,C_SEP=1. Based on the analysis carried out within the scope of the NCFPA approach, Thermal Enhancement Factors (TEF) exceeds unity for most cases, with the highest values of 1.28, 1.26, 1.22, and 1.17 at Re=5000 for N=3-6, respectively, indicating the strong contribution of longitudinal vortices at lower Reynolds numbers. In the CFPA approach, although friction increased notably for N=3S, the heat transfer enhancement outweighs the friction penalty, yielding TEF of 1.18 at Re=5000 and ≈1.00 at Re=25000. Overall, the NCFPA approach showed a more pronounced TEF enhancement compared to CFPA, confirming the strong influence of DWP number and arrangement on thermal performance.
Anahtar Kelimeler
Kaynakça
- [1] Sheikholeslami M, Gorji-Bandpy M, Ganji DD. Review of heat transfer enhancement methods: focus on passive methods using swirl flow devices. Renew Sustain Energy Rev 2015; 49: 444-469.
- [2] Bergles AE. ExHFT for fourth generation heat transfer technology. Exp Therm Fluid Sci 2002; 26: 335-344.
- [3] Liu S, Sakr M. A comprehensive review on passive heat transfer enhancements in pipe exchangers. Renew Sustain Energy Rev 2013; 19: 64-81.
- [4] Bhattacharyya S, Vishwakarma DK, Srinivasan A, Soni MK, Goel V, Sharifpur M, et al. Thermal performance enhancement in heat exchangers using active and passive techniques: a detailed review. J Therm Anal Calorim 2022; 147: 9229-9281.
- [5] Min C, Qi C, Kong X, Dong J. Experimental study of rectangular channel with modified rectangular longitudinal vortex generators. Int J Heat Mass Transf 2010; 53: 3023-3029.
- [6] Xu Z, Han Z, Wang J, Liu Z. The characteristics of heat transfer and flow resistance in a rectangular channel with vortex generators. Int J Heat Mass Transf 2018; 116: 61-72.
- [7] Fiebig M. Vortices, generators and heat transfer. Chem Eng Res Des 1998; 76: 108-123.
- [8] Tian LT, He YL, Lei YG, Tao WQ. Numerical study of fluid flow and heat transfer in a flat-plate channel with longitudinal vortex generators by applying field synergy principle analysis. Int Commun Heat Mass Transf 2009; 36: 111-120.
Ayrıntılar
Birincil Dil
İngilizce
Konular
Makine Mühendisliği (Diğer)
Bölüm
Araştırma Makalesi
Yayımlanma Tarihi
17 Mart 2026
Gönderilme Tarihi
25 Kasım 2025
Kabul Tarihi
11 Şubat 2026
Yayımlandığı Sayı
Yıl 2026 Cilt: 11 Sayı: 1