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Next: Downcomer flow path,
Up: Primary coolant circulation loop
Previous: Steam separator assembly,
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In flow path
the highly subcooled feedwater is mixed with the
saturated liquid from the separator
through a so-called sparger.
The pressure change associated with flow path ,
[Pa],
is calculated by the expression
![\begin{displaymath}
\Delta p_{\framebox[1.5ex]{\raisebox{-2.2pt}[0pt][0ex]{\scr...
...5ex]{\raisebox{-2.2pt}[0pt][0ex]{\scriptsize 4}}}}^2}{2\rho_f}
\end{displaymath}](img951.gif) |
(5.17) |
where we have neglected the volume contents of vapor due to carry-under and
is the local loss coefficient of the feedwater inlet flow path
[--]. The mass flux in flow path
is given by
![\begin{displaymath}
\mbox{$<\!{G}\!>$}_{\framebox[1.5ex]{\raisebox{-2.2pt}[0pt]...
...framebox[1.5ex]{\raisebox{-2.2pt}[0pt][0ex]{\scriptsize 4}}}}}
\end{displaymath}](img954.gif) |
(5.18) |
where the mass flow rates
and
are given by the
formulae in section 5.3.
Until the end of the flow path is reached the flow is considered adiabatic. At
the feedwater inlet we assume that thermal equilibrium is reached
instantaneously, ie the equilibrium enthalpy at the outlet of flow path ,
hi [J/kg], can be expressed as
 |
(5.19) |
where hd [J/kg] is the specific enthalpy of the feedwater and
the feedwater mass flow rate,
[kg/s], in steady-state can be stated as
 |
(5.20) |
where the mass flow rates
and
belong to the vapor
outlet of the steam separator (see section 5.3).
Next: Downcomer flow path,
Up: Primary coolant circulation loop
Previous: Steam separator assembly,
  Contents
  Index
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