Abstract
This work presents a numerical study addressing the hydrodynamic and thermal behaviour of a new trapezoidal tube bank arrangement composed of nine circular cylinders subjected to forced convection. The pressure drop and Nusselt numbers are evaluated aiming to assess the influences of the following parameters: the new trapezoidal factor, the longitudinal and transverse pitches and the free stream velocity (Reynolds number). The second law analysis was also performed by computing the entropy production as function of the trapezoidal factor. The validation of the results obtained with the present methodology was conducted by comparing against empirical correlations available in the literature. The main results indicate that entropy production in the tube bank is very sensitive to the trapezoidal factor. Finally, all results for the global Nusselt number for the new geometry were condensed in an empirical correlation for practical applications with good accuracy (maximum error around ±1.15%).
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callMore From: International Communications in Heat and Mass Transfer
Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
