Toward the Design of a Representative Heater for Boiling Flow Characterization under PWR’s Prototypical Thermalhydraulic Conditions

Author:

Bernadou Louise1,François Fabrice1,Bottin Manon1,Djeridi Henda2,Barre Stephane3

Affiliation:

1. Laboratory for Thermal Hydraulics in Core and Circuits, CEA Cadarache, 13108 Saint-Paul-lez-Durance, France

2. Laboratory of Geophysical Flow, Grenoble INP, 38000 Grenoble, France

3. Laboratory of Geophysical Flow, CNRS, 38000 Grenoble, France

Abstract

In order to improve the understanding of the phenomena underlying the boiling occurrence, CEA Cadarache (France) is designing a new experimental setup, intended to operate for pressures ranging from atmospheric to PWR conditions. This will allow optical access to the convective boiling flow as well as thermal imaging (infrared thermography) of the heated surface. A two-step methodology for designing the heater (particularly its thickness since it directly influences the boiling mechanisms) was developed. This approach is based on solving the heat conduction problem within the heater, considering realistic time-dependent boundary conditions representative of the boiling process. Since those boundary conditions are measured on the external face of the heater, this heat transfer problem is known as an inverse problem that is difficult to solve because of its ill-posedness and high sensitivity to boundary condition uncertainties. In the first stage, we considered one-dimensional modeling to determine the order of magnitude of the heater’s thickness that guaranteed a correct reconstruction of the wet temperature from the measured dry temperature in terms of uncertainties. This value was confirmed in the second stage using a two-dimensional model that accounted for the presence of multiple bubbles on the wet side.

Publisher

MDPI AG

Subject

Fluid Flow and Transfer Processes,Computer Science Applications,Process Chemistry and Technology,General Engineering,Instrumentation,General Materials Science

Reference11 articles.

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3. Maximum bubble diameter, maximum bubble-growth time and bubble-growth rate during the subcooled nucleate flow boiling of water up to 17.7 mn/m2;Unal;Int. J. Heat Mass Tranfer,1976

4. March, P. (1999). Caractérisation et Modélisation de L’environnement thermohydraulique et Chimique des Gaines de Combustible des Réacteurs à eau sous Pression en Présence D’ébullition. [Ph.D. Thesis, Aix-Marseille University].

5. de Munk, P.J. (1973, January 9). Two-phase flow experiments in a 10 m long sodium heated steam generator test section. Proceedings of the International Meeting on Reactor Heat Transfer, Karlsruhe, Germany.

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