Nanofluid turbulent convective flow in a circular duct with helical turbulators considering CuO nanoparticles

•Nanofluid forced convection heat transfer in a pipe is investigated.•Twisted tape turbulator is selected as passive technique.•Nusselt number decreases with increase of PR.•Nusselt number enhances with increase of Re, BR. Nanofluid heat transfer augmentation in a heat exchanger equipped with helica...

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Bibliographic Details
Published in:International journal of heat and mass transfer Vol. 124; pp. 980 - 989
Main Authors: Sheikholeslami, M., Jafaryar, M., Li, Zhixiong
Format: Journal Article
Language:English
Published: Oxford Elsevier Ltd 01-09-2018
Elsevier BV
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Summary:•Nanofluid forced convection heat transfer in a pipe is investigated.•Twisted tape turbulator is selected as passive technique.•Nusselt number decreases with increase of PR.•Nusselt number enhances with increase of Re, BR. Nanofluid heat transfer augmentation in a heat exchanger equipped with helical twisted tape turbulator is simulated numerically via Finite volume method. Impacts of width ratio, Reynolds number and pitch ratio on nanofluid hydrothermal behavior were illustrated. Related formulas for Nusselt number and Darcy factor are provided according to obtained results. Outputs show that thermal boundary layer thickness decreases with augment of width ratio due to stronger secondary flow. Better nanofluid mixing can be obtained for lower values of pitch ratio.
ISSN:0017-9310
1879-2189
DOI:10.1016/j.ijheatmasstransfer.2018.04.022