Abstract
Natural convective heat transfer of Fe3O4/ethylene glycol nanofluids around the platinum wire as a heater in the absence and presence of the high electric field was investigated, numerically. The control volume finite element method was employed for the numerical simulation. Effects of the flow model, the volume fraction of nanoparticles, Rayleigh number, and the electric field intensity on the natural heat transfer coefficient (NHTC) of nanofluid were studied. Simulation results of single-phase and two-phase flow models showed that the two-phase model could better predict experimental data than the single-phase model due to take into account the velocity of each phase in the mixture. The two-phase model could predict a particular volume fraction of 0.02 vol%, which enhancement the volume fraction further that deteriorated heat transfer. Streamlines showed that, as the supplied voltage is increased, velocity vectors and buoyant force increase, and NHTC of nanofluid enhances. Isotherms also showed that the thickness of the thermal boundary layer decays for higher voltage of the electric field, and the natural heat transfer rate promotes. Local Nusselt number (Nuθ) changed as a function of angle around the hot wire. Nuθ increased with applying the electric field for all angles, and the highest Nuθ obtained at θ = 180° (below the wire).
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Abbreviations
- \( \vec{u} \) :
-
Velocity vector (m s−1)
- \( \vec{u}_{\text{f}} \) :
-
Continuous phase velocity vector (m s−1)
- \( \vec{u}_{\text{p}} \) :
-
Dispersed phase velocity vector (m s−1)
- \( \vec{u}_{\text{slip}} \) :
-
Relative velocity vector between the two phases (m s−1)
- \( \vec{g} \) :
-
Gravity vector (m s−2)
- P :
-
Hydrodynamic pressure (Pa)
- \( \overrightarrow {{{\text{F}}_{1} }} \) :
-
Volume force (N m−3)
- \( \overrightarrow {{{\text{F}}_{2} }} \) :
-
Electrical force (N m−3)
- m dc :
-
Mass transfer rate from the dispersed to the continuous phase (kg m−3 s−1)
- (C p)nf :
-
Nanofluids specific heat capacity at constant pressure (J kg−1 K−1)
- (C p)f :
-
Base fluids specific heat capacity at constant pressure (J kg−1 K−1)
- (C p)p :
-
Nanoparticle specific heat capacity at constant pressure (J kg−1 K−1)
- k nf :
-
Nanofluids thermal conductivity (W m−1 K−1)
- k f :
-
Base fluids therm2al conductivity (W m−1 K−1)
- k p :
-
Nanoparticle thermal conductivity (W m−1 K−1)
- T :
-
Temperature (K)
- T w :
-
Platinum wire temperature (K)
- A w :
-
Platinum wire surface area (m−2)
- T b :
-
Bulk temperature (K)
- \( \vec{q} \) :
-
Heat flux vector (W m−2)
- Q :
-
Ohmic heating (W m−3)
- S :
-
Strain-rate tensor
- D c :
-
Cylinder diameter (m)
- L :
-
Wall height (m)
- H c :
-
Cylinder height (m)
- d w :
-
Platinum wire diameter (m)
- d p :
-
Particle diameter (m)
- q J :
-
Current sources (A m−3)
- ρ s :
-
Surface charge density (C m−2)
- \( \vec{J} \) :
-
Current density (A m−2)
- \( \overrightarrow {{J_{\text{e}} }} \) :
-
Externally generated current density (A m−2)
- V :
-
Electric potential (V)
- \( \vec{E} \) :
-
Electric field
- σ :
-
Electrical conductivity (S m−1)
- ɛ 0 :
-
Relative permittivity of free space (F m−1)
- ρ nf :
-
Nanofluids density (kg m−3)
- ρ f :
-
Continuous phase density (kg m−3)
- ρ p :
-
Dispersed phase density (kg m−3)
- μ nf :
-
Nanofluids viscosity (Pa s)
- μ f :
-
Continuous phase viscosity (Pa s)
- β :
-
Thermal expansion coefficient (K−1)
- α :
-
Mass fraction of dispersed phase (kg kg−1)
- φ f :
-
Volume fractions of the continuous phase
- φ p :
-
Volume fractions of dispersed phase
- τ :
-
Viscous stress tensor (Pa)
- τ Gm :
-
Sum of the viscous and turbulent stresses (kg m−1 s−2)
- m:
-
Mixture
- p:
-
Nanoparticle
- f:
-
Base fluid
- nf:
-
Nanofluid
- b:
-
Bulk
- Sim:
-
Simulation
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Partial financial support of Isfahan University of Technology is appreciated.
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Etesami, N., Tavakoli, S. & Pishvaie, M.R. Theoretical comparative assessment of single- and two-phase models for natural convection heat transfer of Fe3O4/ethylene glycol nanofluid in the presence of electric field. J Therm Anal Calorim 146, 981–992 (2021). https://doi.org/10.1007/s10973-020-10059-5
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DOI: https://doi.org/10.1007/s10973-020-10059-5