Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
4990496 | Applied Thermal Engineering | 2017 | 25 Pages |
Abstract
Forced convection across a single tube was investigated numerically for various Reynolds numbers using various numerical models to identify suitable ranges for each model. Direct numerical simulations (DNS), large eddy simulations (LES), and a Reynolds averaged model using the Reynolds stress model (RSM) were compared with experimental date. The calculations used unsteady two-dimensional models with air as the working fluid. For the mesh used here, for Re < 10,000, the DNS method gave good results. For 10,000 < Re < 100,000, the LES is preferred while for Re > 100,000, the RSM is better. Nonlinear phenomena were found for various Reynolds numbers. For Re < 100, the average Nusselt number did not change with time while for 100 â¤Â Re < 1000, the average Nusselt number oscillated with time. The local Nusselt numbers along the entire tube are also discussed.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Fluid Flow and Transfer Processes
Authors
Bonan Zhou, Mo Yang, Zheng Li, Zhiyun Wang, Yuwen Zhang,