Investigation of heat transfer performance within annular geometries with swirl-inducing fins using clove-treated graphene nanoplatelet colloidal suspension

• Published in: Journal of thermal analysis and calorimetry Vol. 147; no. 24; pp. 14873 - 14890
• Main Authors: Nair, S. R., Oon, C. S., Tan, M. K., Mahalingam, Savisha, Manap, Abreeza, Kazi, S. N.
• Format: Journal Article
• Language: English
• Published: Cham Springer International Publishing 01.12.2022; Springer; Springer Nature B.V
• Subjects: Analytical Chemistry; Angles (geometry); Chemistry; Chemistry and Materials Science; Colloids; Domains; Fins; Flow velocity; Fluid flow; Graphene; Graphite; Heat transfer; Heat transfer coefficients; Inorganic Chemistry; Investigations; Measurement Science and Instrumentation; Physical Chemistry; Polymer Sciences; Pressure drop; Swirling; Thermal boundary layer; CFD; CGNP; Colloidal suspension; Annular flow; Swirl-inducing fins; Heat transfer
• ISSN: 1388-6150; 1588-2926
• DOI: 10.1007/s10973-022-11733-6

The paper investigated the benefits of having fins that induce swirling flow within an annular passage. The importance of the vortical structures produced using different fin angles and flow velocities in heat transfer was studied. The combination of swirling fluid with recirculation on heat transfer within an annular domain was not fully understood, and this paper aims to address that gap. The 10°, 20°, 30° and 40° angled fins were investigated to understand the changes in heat transfer performance as fluid recirculation becomes more dominant as angles become steeper. The usage of CGNP colloidal suspension was investigated for its potential benefits in heat transfer in a domain with angled fins. The CGNP concentrations of 0.025, 0.075 and 0.1 mass % were used as part of this investigation. Higher concentrations of CGNP increased the overall heat transfer coefficient. A more compact fin spacing improved heat transfer performance at the expense of increased pressure drop. Fin angles of 20° and 30° yielded poor heat transfer performance in the transitional flow regime (2000 < Re < 3000) due to the smaller swirling longitudinal vortices being insufficient in promoting fluid mixing from the thermal boundary layer into the freestream.