This study deals with numerical modeling of passive autocatalytic hydrogen recombiners (PARs). Such
devices are installed within containments of many nuclear reactors in order to remove hydrogen and convert it
to steam. The main purpose of this work is to develop a numerical model of passive autocatalytic recombiner
(PAR) using the commercial computational fluid dynamics (CFD) software ANSYS-FLUENT and tuning the
model using experimental results. The REKO 3 experiment was used for this purpose. Experiment was made
in the Institute for Safety Research and Reactor Technology in Julich (Germany). It has been performed for different
hydrogen concentrations, different flow rates, the presence of steam, and different initial temperatures
of the inlet mixture. The model of this experimental recombiner was elaborated within the framework of this
work. The influence of mesh, gas thermal conductivity coefficient, mass diffusivity coefficients, and turbulence
model was investigated. The best results with a good agreement with REKO 3 data were received for k-ε model
of turbulence, gas thermal conductivity dependent on the temperature and mass diffusivity coefficients taken
from CHEMKIN program. The validated model of the PAR was next implemented into simple two-dimensional
simulations of hydrogen behavior within a subcompartment of a containment building.
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