All material properties are evaluated at (T + Text) ⁄ 2, except
ρs, which is evaluated at the wall temperature,
T, and
g is the acceleration of gravity equal to 9.81 m/s
2. This correlation is valid for
104≤ RaL ≤ 1013. The laminar-turbulent transition at
RaL = 109 is handled by the use of a smoothed Heaviside function with a transition of size
108, which corresponds to 10% of the threshold value.
where the length of the wall, L, is a correlation input and
is the tilt angle (the angle between the wall and the vertical direction;
for vertical walls). These correlations are valid for
−60°
< < 60° and
104≤ RaL ≤ 1013.
The definition of the Raleigh number, RaL, is analogous to the one for vertical walls and is given by the following:
g denotes the gravitational acceleration, equal to 9.81 m/s
2.
For turbulent flow, 1 is used instead of
cos in the expression for
h, because this gives better accuracy (see
Ref. 41).
The laminar-turbulent transition depends on (see
Ref. 41). Unfortunately, little data is available about transition. There is some data available in
Ref. 41 but this data is only approximate, according to the authors. In addition, data is only provided for water (
Pr around 6). For this reason, the flow is defined as turbulent, independently of the
value, when
All material properties are evaluated at (T + Text) ⁄ 2, except
ρswhich is evaluated at the wall temperature,
T. The laminar-turbulent transition at
RaL = 109 is handled by the use of a smoothed Heaviside function with a transition of size
108, which corresponds to 10% of the threshold value.
RaL is given by
Equation 4-175 or
Equation 4-176, and
L, the characteristic length (defined as area/perimeter, see
Ref. 41) is a correlation input. The material data are evaluated at
(T + Text) ⁄ 2, except
ρswhich is evaluated at the wall temperature,
T.
The laminar-turbulent transition at RaL = 107 is handled by the use of a smoothed Heaviside function with a transition of size
106, which corresponds to 10% of the threshold value.
Equation 4-180 is used when
ρ ≥ ρext (or
T ≤ Text) and
Equation 4-181 is used when
ρ < ρext (or
T > Text). Otherwise it is the same implementation as for
Horizontal Plate, Upside.
Here D is the cylinder diameter and
RaD is given by
The material data are evaluated at (T + Text) ⁄ 2, except
ρswhich is evaluated at the wall temperature,
T.
Here D is the cylinder diameter and
RaD is given by
The material data are evaluated at (T + Text) ⁄ 2, except
ρswhich is evaluated at the wall temperature,
T.
The following correlation corresponds to equation 7.83 in Ref. 41. It evaluates the heat transfer coefficient on the lateral surface of the thin cylinder. The horizontal disks (top and bottom) should be treated as horizontal plates.
where D is the cylinder diameter,
H is the cylinder height, and
RaH is given by
The material data are evaluated at (T + Text) ⁄ 2, except
ρswhich is evaluated at the wall temperature,
T.
If the thermal boundary layer thickness δT is much smaller than the cylinder diameter
D, the curvature does not play any significant role, and vertical wall correlations should be used. In practice, the (
δT < D) criterion requires