The impact of thermal non-equilibrium and large-scale 2D/3D effects on debris bed reflooding and coolability

Abstract During a severe nuclear accident, a part of the molten corium resulting from the core degradation may relocate down to the lower plenum of the reactor vessel. The interaction with residual water in the lower plenum leads to a fragmentation of the corium and formation of particles (characteristic length-scale: 1–5 mm). In order to predict the safety margin of the reactor under such conditions, the coolability of this porous heat-generating medium and the possibility to reflood the particle bed are studied in this paper and compared with other theoretical or experimental results. A quick overview of the existing experimental results and models is provided to identify the remaining uncertainties on some modelling issues and the lack of understanding of some of the physical processes involved. It also justifies the approach chosen by Institut de RadioProtection et de Surete Nucleaire (IRSN) to deal with the issues of debris coolability and reflooding. The detailed description of two-phase flow in a debris bed is addressed in IRSN by a special module of the ICARE/CATHARE code. This thermalhydraulic module is designed to deal with a non-homogeneous debris bed of any shape. The momentum balance equation for each fluid phase is an extension of Darcy's law. This extension takes into account the capillary effects between the two phases, the relative permeabilities and passabilities of each phase, the interfacial drag force between liquid and gas, and the porous bed configuration (porosity, particle diameter, …). The model developed is three-dimensional, which is important to better predict the flow in configurations such as natural convection co-current flows in large beds or to emphasize the impact of preferential paths induced by porous geometry (existence of regions with lower or higher porosity and permeability). The energy balance equations of the three phases (liquid, gas and solid phase) are obtained by a volume averaging process of the local conservation equations. In this method, the local thermal non-equilibrium between the three phases is taken into account and the heat exchange coefficients as well as the thermal dispersion coefficients are calculated as a function of the local geometry of the porous medium and the local phase distribution. Numerical estimations of these thermal properties can be performed, which is quite convenient, on a practical point of view, since they are very difficult to determine experimentally. This feature is a great advantage of this approach. Examples of numerical determination of effective properties are given in the paper, with analytical solutions for a simple geometry. The phase change rate is also naturally determined without additional phenomenological equation. One-dimensional predictions of critical dryout fluxes are presented and compared with results from the literature. Reasonable agreement is obtained. Calculations of one-dimensional reflooding (from top or bottom) are compared with experimental data. The results show the importance of using a non-equilibrium model for temperatures. They also indicate that channeling effects may exist and should be taken into account in the model for further improvements. Two-dimensional calculations are presented and show the influence of the porous medium characteristics. As expected, water circulation is improved considering multi-dimensional flow in the bed and the dryout heat flux is larger than predicted by 1D modelling. Conditions for reflooding are also more favourable if large-scale non-homogeneities exist in the debris bed. This leads to a flow pattern where steam can exit the debris bed in preferential channels and there is less limitation by counter-current flow.

[1]  L. Bova,et al.  Formation of dry pockets during water penetration into a hot particle bed , 1982 .

[2]  R. H. Brooks,et al.  Properties of Porous Media Affecting Fluid Flow , 1966 .

[3]  Vijay K. Dhir,et al.  SUBCOOLED FILM-BOILING HEAT TRANSFER FROM SPHERES , 1978 .

[4]  Stephen Whitaker,et al.  Improved constraints for the principle of local thermal equilibrium , 1991 .

[5]  K. Vafai,et al.  Analysis of Energy and Momentum Transport for Fluid Flow Through a Porous Bed , 1990 .

[6]  A. I. Loboiko,et al.  Critical heat fluxes when boiling occurs in a nonuniform heat-releasing porous medium , 1998 .

[7]  Adrian E. Scheidegger,et al.  The physics of flow through porous media , 1957 .

[8]  Ik Kyu Park,et al.  Multiphase flow modeling of molten material-vapor-liquid mixtures in thermal nonequilibrium , 2000 .

[9]  K. Bang Numerical prediction of forced convection film boiling heat transfer from a sphere , 1994 .

[10]  R. Lenormand,et al.  Inertial Effects in Two-Phase Flow Through Fractures , 2000 .

[11]  Michel Quintard,et al.  Two-medium treatment of heat transfer in porous media: numerical results for effective properties , 1997 .

[12]  T. Schulenberg,et al.  An improved model for two-phase flow through beds of coarse particles , 1987 .

[13]  Michel Quintard,et al.  Heat and Mass Transfer in Tubes: An Analysis Using the Method of Volume Averaging , 2002 .

[14]  Ronald J. Lipinski,et al.  A coolability model for postaccident nuclear reactor debris , 1984 .

[15]  Michel Quintard,et al.  Écoulement diphasique en milieu poreux: modèle à non-équilibre local , 1999 .

[16]  Stephen Whitaker,et al.  Coupled Transport in Multiphase Systems: A Theory of Drying , 1998 .

[17]  Michel Quintard,et al.  Local thermal equilibrium for transient heat conduction: theory and comparison with numerical experiments , 1995 .

[18]  R. Carbonell,et al.  Longitudinal and lateral thermal dispersion in packed beds. Part II: Comparison between theory and experiment , 1985 .

[19]  S. Whitaker,et al.  Heat transfer in packed beds: interpretation of experiments in terms of one- and two-equation models , 1994 .

[20]  Georges Berthoud,et al.  Development of a multidimensional model for the premixing phase of a fuel-coolant interaction , 1994 .

[21]  Kresna Atkhen,et al.  Experimental and Numerical Investigations on Debris Bed Coolability in a Multidimensional and Homogeneous Configuration with Volumetric Heat Source , 2003 .

[22]  David A. Petti,et al.  A Scenario of the Three Mile Island Unit 2 Accident , 1989 .

[23]  Fabien Duval,et al.  Modélisation du renoyage d'un lit de particules : contribution à l'estimation des propriétés de transport macroscopiques , 2002 .

[24]  R. H. Nilson,et al.  Natural Convection in Porous Media with Heat Generation , 1977 .

[25]  Kambiz Vafai,et al.  Analysis of the non-thermal equilibrium condensing flow of a gas through a packed bed , 1990 .

[26]  T. G. Theofanous,et al.  Premixing-related behavior of steam explosions , 1995 .

[27]  Étienne Décossin Ébullition et assèchement dans un lit de particules avec production interne de chaleur : premières expériences et simulations numériques en situation multidimensionnelle , 2000 .

[28]  S. Whitaker,et al.  One- and Two-Equation Models for Transient Diffusion Processes in Two-Phase Systems , 1993 .

[29]  Vijay K. Dhir,et al.  A hydrodynamic model for two-phase flow through porous media , 1988 .

[30]  S. Whitaker,et al.  Transport in ordered and disordered porous media: volume-averaged equations, closure problems, and comparison with experiment , 1993 .

[31]  Michel Quintard,et al.  Convection, dispersion, and interfacial transport of contaminants: Homogeneous porous media , 1994 .

[32]  Ivan Catton,et al.  Dryout of an inductively heated bed of steel particles with subcooled flow from beneath the bed , 1984 .

[33]  T. Ginsberg,et al.  Experimental and analytical investigation of quenching of superheated debris beds under top-reflood conditions. Final report , 1986 .

[34]  R. Lockhart Proposed Correlation of Data for Isothermal Two-Phase, Two-Component Flow in Pipes , 1949 .

[35]  M. Kaviany Principles of heat transfer in porous media , 1991 .

[36]  T. G. Theofanous,et al.  Premixing of steam explosions: a three-fluid model , 1991 .

[37]  Michel Quintard,et al.  A local thermal non-equilibrium model for two-phase flows with phase-change in porous media , 2004 .

[38]  S. Ergun Fluid flow through packed columns , 1952 .

[39]  I. Catton,et al.  The Effect of Pressure on Dryout of a Saturated Bed of Heat-Generating Particles , 1987 .

[40]  Ruben G. Carbonell,et al.  hydrodynamic parameters for gas-liquid cocurrent flow in packed beds , 1985 .