<?xml version="1.0"?>
<rdf:RDF xmlns:rdf="http://www.w3.org/1999/02/22-rdf-syntax-ns#" xmlns:dc="http://purl.org/dc/elements/1.1/"><rdf:Description rdf:about="https://repozitorij.uni-lj.si/IzpisGradiva.php?id=134748"><dc:title>Numerical modeling of non-condensable gases transport in two-phase flow</dc:title><dc:creator>Murad,	Afeef	(Avtor)
	</dc:creator><dc:creator>Kljenak,	Ivo	(Mentor)
	</dc:creator><dc:creator>Patel,	Giteshkumar	(Komentor)
	</dc:creator><dc:subject>Apros</dc:subject><dc:subject>non-condensable gases</dc:subject><dc:subject>two-phase flow</dc:subject><dc:subject>thermal hydraulics system codes.</dc:subject><dc:description>The presence of non-condensable gases at the gas-liquid interface significantly decreases
the heat and mass transfer, and disturbs the fluid flow. Thus, modeling the transport of
non-condensable gases in two-phase flow is of great importance in nuclear reactor safety.
Non-condensable gases transport in two-phase flow is considered as a multi-component
flow, where the non-condensable gases are assumed to be homogeneously mixed with
steam in the gas phase. Modeling of non-condensable gases transport has been already
done by Computational Fluid Dynamics, system thermal-hydraulics codes, and numerical
simulations. This work is dedicated to the Apros thermal-hydraulics system code. Some
stability and convergence issues can show up when modeling non-condensable gases in
the the current version of the code Apros 6; for example, when the gas phase consists
of a high mass fraction of non-condensable gas with a very low mass fraction of steam.
In the present work, a new procedure is proposed to integrate the non-condensable gases
transport equation solution in the two-fluid six equations solution algorithm to develop a
new thermal-hydraulic solver. A new pressure equation is derived based on considering
the non-condensable gas transport equation solution from the beginning of the numerical
algorithm formulation. This is expected to improve the stability and convergence by ma-
king the non-condensable gas transport equation solution more tightly coupled with the
pressure equation. The oscillating U-tube numerical benchmark test case was simulated
to verify and validate the new implementation of the new pressure equation. The results
of the oscillating U-tube show good agreement with the analytical solution when using a
dense nodalization. The second test performed was the simulation of experiments on con-
densation in the presence of non-condensable gases in the separate test facility CONAN.
Experiments were simulated with a constant heat transfer coefficient and a heat transfer
coefficient, obtained from the Uchida correlation. The simulation results were quantita-
tively reasonable. Moreover, the results showed qualitatively the same behavior as the
experimental data. In addition, a hypothetical case with a varying velocity behavior was
also simulated (with a constant heat transfer coefficient).</dc:description><dc:date>2021</dc:date><dc:date>2022-01-29 08:15:02</dc:date><dc:type>Magistrsko delo/naloga</dc:type><dc:identifier>134748</dc:identifier><dc:language>sl</dc:language></rdf:Description></rdf:RDF>
