Convective heat transfer of micropolar fluid in a horizontal wavy channel under the local heating; International Journal of Mechanical Sciences; Vol. 128-129

書目詳細資料
Parent link:International Journal of Mechanical Sciences
Vol. 128-129.— 2017.— [P. 541–549]
企業作者: Национальный исследовательский Томский политехнический университет (ТПУ) Энергетический институт (ЭНИН) Кафедра атомных и тепловых электростанций (АТЭС)
其他作者: Miroshnichenko I. V. Igor V., Sheremet M. A. Mikhail Aleksandrovich, Pop I. Ioan, Ishak A. Anuar
總結:Title screen
A numerical analysis of laminar mixed convection of micropolar fluid in a horizontal wavy channel with a local heater has been carried out. Governing equations formulated in dimensionless stream function, vorticity and temperature have been solved by finite difference method. Effects of Rayleigh number, Reynolds number, Prandtl number, vortex viscosity parameter and undulation number on streamlines, isotherms, vorticity isolines as well as horizontal velocity and temperature profiles with average Nusselt number at the heater have been studied. It has been found that the average Nusselt number is an increasing function of Rayleigh, Reynolds and Prandtl numbers and a decreasing function of undulation number while an influence of vortex viscosity parameter is non-monotonic.
Режим доступа: по договору с организацией-держателем ресурса
語言:英语
出版: 2017
主題:
在線閱讀:https://doi.org/10.1016/j.ijmecsci.2017.05.013
格式: 電子 Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=656710
實物特徵
總結:Title screen
A numerical analysis of laminar mixed convection of micropolar fluid in a horizontal wavy channel with a local heater has been carried out. Governing equations formulated in dimensionless stream function, vorticity and temperature have been solved by finite difference method. Effects of Rayleigh number, Reynolds number, Prandtl number, vortex viscosity parameter and undulation number on streamlines, isotherms, vorticity isolines as well as horizontal velocity and temperature profiles with average Nusselt number at the heater have been studied. It has been found that the average Nusselt number is an increasing function of Rayleigh, Reynolds and Prandtl numbers and a decreasing function of undulation number while an influence of vortex viscosity parameter is non-monotonic.
Режим доступа: по договору с организацией-держателем ресурса
DOI:10.1016/j.ijmecsci.2017.05.013