Abstract
This paper analyzes the heat transfer for laminar natural convection of a viscous, incompressible, Newtonian fluid between parallel vertical plates, due to a step change in the temperature of one of the two plates. The momentum conservation and energy conservation equations are analytically solved applying the Laplace transform technique. The temperature profile, which is presented as an original solution, is a fast converging series of sinusoidal and exponential functions. It is very easy to be used and highlights that the transient distribution of the temperature tends to the steady-state one when the numerical value of dimensionless time approaches the Prandtl number. The results, obtained for different fluids (liquid sodium, air, water and lubricating oil), show that the thermal transient is always faster than the dynamic transient.
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Abbreviations
- c p :
-
Specific heat at constant pressure (J kg−1 K−1)
- D :
-
Equivalent diameter (2 H, m)
- g :
-
Gravitational acceleration (m s−2)
- Gr :
-
Grashof number (g β Η 3 (T 1 −T 0 ) ν −2)
- h :
-
Heat transfer coefficient (W m−2 K−1)
- H :
-
Distance between two vertical walls (m)
- k :
-
Fluid thermal conductivity (W m−1 K−1)
- Nu :
-
Nusselt number (h D k −1)
- p :
-
Pressure (Pa)
- p s :
-
Hydrostatic pressure (Pa)
- P :
-
Dimensionless pressure
- Pr :
-
Prandtl number (ρ o ν c p k −1)
- R :
-
Buoyancy force distribution parameter
- s :
-
Coordinate of the Laplace transform
- t :
-
Dimensionless time
- t’ :
-
Time (s)
- T :
-
Fluid temperature (K)
- T 0 :
-
Ambient and initial (fluid and wall) temperature (K)
- T 1 :
-
Wall temperature at x = 1, t > 0 (K)
- u :
-
Fluid velocity (m s−1)
- U :
-
Dimensionless fluid velocity
- x, z:
-
Dimensionless Cartesian coordinates
- Y :
-
Function defined in Eq. (18)
- Z :
-
Dimensionless height of the channel
- β 0 :
-
Thermal expansion coefficients at temperature T 0 (K−1)
- μ :
-
Dynamic viscosity (Pa s)
- ν :
-
Kinematic viscosity (m2 s−1)
- θ :
-
Dimensionless temperature
- ρ :
-
Fluid density (kg m−3)
- ρ o :
-
Fluid density at temperature T 0 (kg m−3)
- τ :
-
Dimensionless tangential stress
- ξ, ζ :
-
Cartesian coordinates (m)
- ψ :
-
Integration variable
- b :
-
Fluid bulk
- ss :
-
Steady-state
- w :
-
Wall
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Acknowledgments
The research leading to these results has received the financial support of the Italian MIUR in the PRIN 2009 framework.
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Spiga, M., Vocale, P. Step response for free convection between parallel walls. Heat Mass Transfer 51, 1761–1768 (2015). https://doi.org/10.1007/s00231-015-1539-x
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DOI: https://doi.org/10.1007/s00231-015-1539-x