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Next: Nucleate boiling heat transfer
Up: Saturated boiling heat transfer
Previous: Saturated boiling heat transfer
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The convective boiling heat transfer coefficient,
is defined by
 |
(11.44) |
where
l
- single-phase liquid heat transfer coefficient
given by a slightly modified version of (11.37),
![\begin{displaymath}
h_c = C \left[
\frac{\mbox{$<\!{G}\!>$}(1-\mbox{$<\!{x}\!>...
...k_\ell} \right]_m^{0.33} \left(
\frac{k_\ell}{D_H} \right)_m
\end{displaymath}](img1808.gif) |
(11.45) |
where C [--] is defined by (11.34) and
is the flow
quality [--]. Note that the author has exchanged the Dittus-Boelter
correlation originally in the Chen correlation with the correlation by
El-Genk et al (11.37) since it is appropriate in the rod bundle
geometry.
- l
- the so-called Reynolds number factor [--] which
is a hydrodynamic dimensionless parameter to be discussed in the
subsequent.
The F-factor is defined by
![\begin{displaymath}
F \;\hbox{$=$\kern-0.68em\raise1.1ex
\hbox{$\scriptscripts...
... }{\mbox{\bf Re}_{\mbox{\protect\scriptsize f}}} \right]^{0.8}
\end{displaymath}](img1810.gif) |
(11.46) |
where
is an effective Reynolds number for the two-phase flow [--]
and
is the Reynolds number based on the liquid fraction of the
flow [--], ie defined by
 |
(11.47) |
The F-factor being a flow parameter depends only on the turbulent Martinelli
parameter,
[--], defined by
![\begin{displaymath}
\frac{1}{X_{\mbox{\protect\scriptsize tt}}} \;\hbox{$=$\ker...
..._g} \right]^{0.5} \left[ \frac{\mu_g}{\mu_\ell}
\right]^{0.1}
\end{displaymath}](img1815.gif) |
(11.48) |
Values for
originally shown graphically by Chen at some
discrete
values are given in Table 11.1.
Next: Nucleate boiling heat transfer
Up: Saturated boiling heat transfer
Previous: Saturated boiling heat transfer
  Contents
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