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DIPARTIMENTO DI INGEGNERIA CIVILE E INDUSTRIALE

TESIDILAUREASPECIALISTICAININGEGNERIA NUCLEARE EDELLASICUREZZAINDUSTRIALE

“SIMMER Code Improvements and Applications in Safety Analysis of MYRRHA Reactor”

RELATORI IL CANDIDATO

Prof. Ing. Walter Ambrosini Simone Gianfelici

DICI

Dott. Ing. Nicola Forgione DICI

Anno Accademico 2012-2013

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Abstract

As a part of collaboration between the Dipartimento di Ingegneria Civile ed Industriale (DICI) of the University of Pisa and the Institut für Kern- und Energietechnik (IKET) of the Karlsruher Institut für Technologie, a FORTRAN program, for the restarting of calculations for SIMMER III code was developed. The “SIMMER-to-SIMMER coupling program” gives great flexibility in comparison with the default RESTART capability of the code and allows modifying any option in the input file.

The first part of this thesis work describes the SIMMER-III code and the ADS reactors, in particular the MYRRHA-FASTEF reactor.

In the fourth chapter a description of the coupling program and the 2D domain adopted in the description of the MYRRHA reactor is presented. The results of a 500 s steady-state calculation are compared with those of a standard RESTART and of a restart carried out with the coupling program, both from 200 s of simulation. For both restarts, pressure and velocities are in good agreement with the steady-state analysis, while the temperatures show small differences during the two transients.

The coupling program was used to start transients of fuel release, equivalent to the mass of fuel present in a single pin, in natural and forced circulation. The results are then compared to those already obtained by DICI, started with velocity and temperature fields chosen by the user and with radius of fuel particles equal to 1 mm. Due to the different velocity and temperature fields at the beginning of the transients, a higher amount of fuel particles was calculated in proximity of the baffle in forced circulation conditions. Furthermore, for natural circulation calculations, the fuel particles released tend to concentrate more in proximity of the free level of the hot pool. According to the results of the SEARCH meetings, the radius was then set to 75 micrometers and a comparison with the previous simulation is reported. The smaller fuel particles tend to float and accumulate more, in particular in the regions where the coolant has low velocities.

Finally, to check the coherence of the geometry approximations of the 2D mesh, the results of the last analysis are compared with those of the analyses of fuel pin release performed with the 3D model of MYRRHA developed by DICI and ENEA. Differently from the 2D one, the 3D domain shows high concentration of fuel particles between the diaphragm and the vessel, and a lower amount in the pumps and the cold pool A certain amount of fuel near the baffle is anyhow predicted.

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I

List of Contents

LIST OF CONTENTS ... I LIST OF FIGURES ... V LIST OF TABLES ... X NOMENCLATURE ... XI Acronyms ... XI Roman Letters ... XIV Greek letters ... XVI Subscripts ... XVI Superscripts ... XVIII 1. INTRODUCTION ... 1-1 References ... 1-5 2. SIMMER-III CODE ... 2-1 2.1 Introduction ... 2-1 2.2 Models and Methods of SIMMER-III ... 2-2 2.2.1. Code Framework and Geometry ... 2-2 2.3 Structure (fuel pin) model ... 2-6 2.4 Fluid-Dynamics Model ... 2-10 2.4.1 Fundamental Differential Equations ... 2-10 2.4.2 Overall Solution Procedure ... 2-11 2.4.3. Fluid Convection Algorithm ... 2-12 2.4.4 Flow regimes and Interfacial Area Model... 2-14 2.4.5 Momentum Exchange Functions ... 2-18 2.4.6 Heat-Transfer Coefficients ... 2-19 2.4.7 Heat and Mass Transfer Model ... 2-20 2.4.8 Inter-cell Heat Transfer ... 2-24

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II

2.4.9 Equations-of-State Model ... 2-25 2.5 Neutronics Model ... 2-27 References ... 2-28 3. THE ADSS SYSTEMS AND THE MYRRHA-FASTEF REACTOR ... 3-1 3.1 ADS systems ... 3-1 3.1.1 Introduction ... 3-1 3.1.2 Minor Actinides and transuranic elements as nuclear fuel ... 3-2 3.1.3 THORIUM as nuclear fuel ... 3-6 3.1.4 ADSs neutron source ... 3-8 3.1.5 Sub-critical reactor in ADS ... 3-11 3.2 The MYRRHA reactor ... 3-13 3.2.1 Introduction ... 3-13 3.2.2 Historical evolution of MYRRHA: from ADONIS to FASTEF... 3-14 3.2.3 Current MYRRHA-FASTEF design ... 3-16 3.2.4 Main components ... 3-17 References ... 3-26 4. SIMMER-TO-SIMMER COUPLING PROGRAM ... 4-1 4.1 Introduction ... 4-1 4.2 Description of the program ... 4-2 4.3 Description of the 2D mesh for the MYRRHA reactor ... 4-9 4.3.1 Vessel ... 4-10 4.3.2 Diaphragm ... 4-10 4.3.3 Core Support Structure ... 4-12 4.3.4 Pump... 4-13 4.3.5 Primary heat exchangers ... 4-13 4.3.6 Core ... 4-14 4.4 Steady-state analysis of the model ... 4-18 4.4.1 Mass flow rate ... 4-18

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III

4.4.2 Temperature in the structures ... 4-19 4.4.3 Temperature in the LBE ... 4-20 4.4.4 LBE velocities ... 4-23 4.5 Default RESTART and coupling program comparison ... 4-25 4.5.1 Temperatures ... 4-25 4.5.2 Pressure ... 4-26 4.5.3 Velocities ... 4-26 4.6 Final considerations ... 4-27 References ... 4-28 5. FUEL DISPERSION ANALYSIS IN MYRRHA REACTOR ... 5-1 5.1 Generalities ... 5-1 5.2 Initial conditions and time evolution of the flow conditions ... 5-3 5.2.1 Forced circulation in the primary loop ... 5-3 5.2.2 Natural circulation in the primary loop ... 5-5 5.3 Fuel dispersion: 1 mm particle radius ... 5-8 5.3.1 Test 1 ... 5-8 5.3.2 Test 2 ... 5-14 5.3.3 Natural Circulation, comparison between 5% and 10% porosity ... 5-18 5.3.4 Test 3 ... 5-19 5.3.5 Test 4 ... 5-25 5.3.6 Forced Circulation, comparison between 5% and 10% porosity ... 5-29 5.4 Fuel dispersion: 75 µm particle radius ... 5-30 5.4.1 Test 5 and Test 6 ... 5-30 5.4.2 Test 7 ... 5-34 5.4.3 Test 8 ... 5-37 References ... 5-39 6. COMPARISON BETWEEN SIMMER-III AND SIMMER-IV RESULTS ... 6-1 6.1 Description of the 3D model ... 6-1

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IV

6.2 Fuel porosity 5%, particles radius 75 µm ... 6-6 6.3 Fuel porosity 10%, particles radius 75 µm ... 6-12 References ... 6-18 7. CONCLUSIONS ... 7-1

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V

List of Figures

Figure 2.1: SIMMER-III Overall Code Structure ... 2-2 Figure 2.2: SIMMER-III geometry ... 2-3 Figure 2.3: Fluid-dynamics mesh cell configuration ... 2-3 Figure 2.4: Axial fuel pin representation in SIMMER-III... 2-6 Figure 2.5: Radial fuel pin representation in SIMMER-III ... 2-7 Figure 2.6: Fuel pin and can wall configuration in a mesh cell ... 2-9 Figure 2.7: Schematic Diagram of the Four-Step Method ... 2-11 Figure 2.8: Pool Flow Regime Map ... 2-15 Figure 2.9: Schematic Concept of Separating Bubbly and Dispersed Regions... 2-15 Figure 2.10: Channel Flow Regimes ... 2-16 Figure 2.11: Non-equilibrium mass transfer model in SIMMER-III ... 2-21 Figure 2.12: Basis of non-equilibrium heat-transfer limited process ... 2-22 Figure 3.1: Main trajectories of nuclear transformations in the U-Pu fuel cycle ... 3-4 Figure 3.2: Main trajectories of nuclear transformations in the Th-U fuel cycle ... 3-6 Figure 3.3: Schematics of Spallation reaction ... 3-10 Figure 3.4: Neutron emission from tungsten (W) target – estimates reported for

various energy of primary protons ... 3-10 Figure 3.5: Schematic ADS configuration ... 3-12 Figure 3.6: Overview of the MYRRHA-FASTEF reactor ... 3-17 Figure 3.7: General lay-out of the pump ... 3-18 Figure 3.8: FASTEF heat exchanger, ver. 1.2 ... 3-19 Figure 3.9: FASTEF heat exchanger, ver. 1.4 ... 3-19 Figure 3.10: Overall configuration of the RVACS system ... 3-21 Figure 3.11: In-vessel fuel handling machine ... 3-21 Figure 3.12: Overview of the diaphragm ... 3-22 Figure 3.13: LBE cold and hot pools divided by the diaphragm ... 3-22 Figure 3.14: MYRRHA-FASTEF core assemblies ... 3-23 Figure 4.1: First step: name of the base file and problem time ... 4-4 Figure 4.2: Variables that the code can elaborate ... 4-5 Figure 4.3: Example of a case with missing variables ... 4-5 Figure 4.4: Variables routine ... 4-5 Figure 4.5: Variables selected (read from the variables.dat file) ... 4-6

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VI

Figure 4.6: Routine to skip cells ... 4-6 Figure 4.7: Concept of the square exclusion ... 4-7 Figure 4.8: Pause to edit the skipped.dat file ... 4-7 Figure 4.9: Summary of selected cells (0 = excluded, 1 = included) ... 4-8 Figure 4.10: Section of MYRRHA-FASTEF reactor ... 4-9 Figure 4.11: SIMMER-III 2D mesh for MYRRHA ... 4-10 Figure 4.12: IVFHM and baffle in 2D mesh ... 4-11 Figure 4.13: In-vessel fuel storage and pump-PHX volumes ... 4-11 Figure 4.14: Core Support Structure... 4-12 Figure 4.15: Particular of the model of the pump... 4-13 Figure 4.16: Scheme of the PHX model ... 4-14 Figure 4.17: FA design ... 4-14 Figure 4.18: Radial power profile used in SIMMER-III calculations ... 4-15 Figure 4.19: Axial power profile used in SIMMER-III calculations ... 4-16 Figure 4.20: Modeling of the core with the related rings for SIMMER-III ... 4-17 Figure 4.21: Mass Flow rate ... 4-19 Figure 4.22: Structure temperatures in the core ... 4-20 Figure 4.23: Radial profile of structures temperature in FA ... 4-21 Figure 4.24: Radial profile of LBE temperature in the core ... 4-22 Figure 4.25: Axial LBE temperature in the PHX ... 4-22 Figure 4.26: LBE velocity in the core ... 4-23 Figure 4.27: Cells with high velocity that cause convergence problem ... 4-24 Figure 4.28: Comparison between LBE temperatures in the core for the steady-state

calculation and the two restars ... 4-25 Figure 4.29: Comparison between pressures in the gas zone ... 4-26 Figure 4.30: Comparison between velocities in the core... 4-27 Figure 5.1: Densities of LBE and MOX fuel, theoretical and with 5% and 10% of

porosity ... 5-1 Figure 5.2: LBE velocity vectors from 2D steady-state calculation, with stagnation

regions indicated in red and recirculation zones in yellow... 5-4 Figure 5.3: LBE temperature profile from steady-state analysis [°K] ... 5-5 Figure 5.4: LBE mass flow rate trend in the core for natural circulation tests ... 5-6 Figure 5.5: Time evolution of LBE velocity vectors and LBE temperature profile

[°K]: natural circulation tests, pumps trip and reactor scram at 10 s ... 5-7

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VII

Figure 5.6: Comparison between LBE velocity field at 10 s in the old (left) and in the new calculation (right) ... 5-8 Figure 5.7: Time evolution of fuel particles concentration in the primary loop for test

1 (first 150 s of transient)... 5-9 Figure 5.8: Time evolution of fuel particles concentration in the primary loop for test

1 (200, 250 and 300 s of transient) ... 5-10 Figure 5.9: Input Zones for BFCAL: natural circulation ... 5-11 Figure 5.10: Test 1: BFCAL results from old calculation, 5% fuel porosity, natural

circulation ... 5-12 Figure 5.11: Test 1: BFCAL results from new calculation, 5% fuel porosity, natural

circulation ... 5-12 Figure 5.12: LBE temperature in the hot pool at 300 s, old (left) and new (right)

calculations ... 5-13 Figure 5.13: Test 2: BFCAL results from old calculation, 10% fuel porosity, natural

circulation ... 5-14 Figure 5.14: Test 2: BFCAL results from new calculation, 10% fuel porosity, natural

circulation ... 5-15 Figure 5.15: Time evolution of fuel particle concentration in the primary loop for test

2 (first 150 s of transient) ... 5-16 Figure 5.16: Time evolution of fuel particle concentration in the primary loop for test

2 (200, 250 and 300 s of transient) ... 5-17 Figure 5.17: Comparison between fuel particles volume fractions of test 1 (5% fuel

porosity, left) and test 2 (10% fuel porosity, right) at the end of transient . 5-18 Figure 5.18: Time evolution of fuel particle concentration in the primary loop for test

3 (first 150 s of transient) ... 5-20 Figure 5.19: Time evolution of fuel particle concentration in the primary loop for test

3 (200, 250 and 300 s of transient) ... 5-21 Figure 5.20: Input Zones for BFCAL for the tests in forced circulation ... 5-22 Figure 5.21: Test 3: BFCAL results from old calculation, 5% fuel porosity, forced

circulation ... 5-24 Figure 5.22: Test 3: BFCAL results from new calculation, 5% fuel porosity, forced

circulation ... 5-24 Figure 5.23: Time evolution of fuel particle concentration in the primary loop for test

4 (first 150 s of transient) ... 5-26

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VIII

Figure 5.24: Time evolution of fuel particle concentration in the primary loop for test 4 (200, 250 and 300 s of transient) ... 5-27 Figure 5.25: Test 4: BFCAL results from old calculation, 10% fuel porosity, forced

circulation ... 5-28 Figure 5.26: Test 4: BFCAL results from new calculation, 10% fuel porosity, forced

circulation ... 5-28 Figure 5.27: Comparison between fuel particles volume fractions of test 3 (5% fuel

porosity, left) and test 4 (10% fuel porosity, right) at the end of transient . 5-29 Figure 5.28: Time evolution of fuel particles concentration in the primary loop for

test 5 ... 5-31 Figure 5.29: Time evolution of fuel particles concentration in the primary loop for

test 6 ... 5-32 Figure 5.30: Test 5: BFCAL results, 5% fuel porosity, particles radius 75 µm, natural

circulation ... 5-33 Figure 5.31: Test 6: BFCAL results, 10% fuel porosity, particles radius 75 µm,

natural circulation ... 5-34 Figure 5.32: Time evolution of fuel particles concentration in the primary loop for

test 7 ... 5-35 Figure 5.33: Test 7: BFCAL results, 5% fuel porosity, particles radius 75 µm, forced

circulation ... 5-36 Figure 5.34: Test 8: BFCAL results, 10% fuel porosity, particles radius 75 µm,

forced circulation ... 5-37 Figure 5.35: Time evolution of fuel particles concentration in the primary loop for

test 8 ... 5-38 Figure 6.1: Horizontal section of the 3D mesh for SIMMER-IV ... 6-2 Figure 6.2: Overall view of 3D mesh for SIMMER-IV ... 6-2 Figure 6.3: View of velocities in proximity of the baffle ... 6-3 Figure 6.4: Comparison between 2D and 3D meshes ... 6-4 Figure 6.5: Position of the release in the core ... 6-5 Figure 6.6: View of the PHX-pump volume ... 6-5 Figure 6.7: Comparison between time evolutions of fuel dispersion in 2D and 3D

domains, fuel porosity 5% and particles radius 75 µm (first 150 s of calculation) ... 6-7

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IX

Figure 6.8: Comparison between time evolutions of fuel dispersion in 2D and 3D domains, fuel porosity 5% and particles radius 75 µm (200, 250 and 300 s of calculation)... 6-8 Figure 6.9: Stagnation regions (in yellow) in 3D calculation, vertical section. LBE

coolant velocity vectors in black. ... 6-9 Figure 6.10: Horizontal view of the fuel particles volume fraction ... 6-10 Figure 6.11: Stagnation regions (in yellow) in 3D calculation, horizontal section.

LBE Coolant velocity vectors in black. ... 6-11 Figure 6.12: Comparison between time evolutions of fuel dispersion in 2D and 3D

domains, fuel porosity 10% and particles radius 75 µm (first 150 s of calculation) ... 6-13 Figure 6.13: Comparison between time evolutions of fuel dispersion in 2D and 3D

domains, fuel porosity 10% and particles radius 75 µm (200, 250 and 300 s of calculation) ... 6-14 Figure 6.14: LBE temperature distribution in 3D simulation [°K] ... 6-15 Figure 6.15: Fuel particles dispersion at the free level for 3D domain with 10% fuel

porosity ... 6-16

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X

List of Tables

Table 2.1: SIMMER-III Fluid Dynamics Structure Field Components ... 2-4 Table 2.2: SIMMER-III Fluid Dynamics Liquid Field Components ... 2-5 Table 2.3: SIMMER-III Fluid Dynamics Vapor Field Components ... 2-5 Table 2.4: SIMMER-III Fuel-Pin Components ... 2-5 Table 3.1: Values of the fission parameters of selected actinides ... 3-4 Table 3.2: Average composition of spent nuclear fuel (main radionuclides/1GWe*year .. 3-5 Table 3.3: Actinides content in PWR fuel [g/t] (BU 30 GWd/t) ... 3-7 Table 3.4: Energy cost of neutrons from various accelerator-based sources ... 3-9 Table 3.5: MYRRHA pump updated parameters ... 3-18 Table 4.1: Input and Output variables in SIMMER-III; correlation between region-

wise input options XRGN, cell-wise input options XCWD and output variables in SIMBF ... 4-3 Table 4.2: Main characteristics of the MYRRHA reactor ... 4-18 Table 5.1: Simulation matrix ... 5-2

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XI

Nomenclature Acronyms

ADS Accelerator Driven System

AFDM Advanced Fluid-Dynamics Model

BoC Beginning of Cycle

BoL Beginning of Life

CAD Computer-Aided Design

CDA Core Disruptive Accident

CDT Central Design Team

CEA Commissariat A L'energie Atomique

CFD Computational Fluid-Dynamic

CP Continuous Phase

CPU Central Processor Unit

CR Control Rod

CRGT Control Rod Guide Tube

CSS Core Support Structure

DA Dummy Assembly

DBC Design Basis Condition

DHR Decay Heat Removal

DICI Dipartimento di Ingegneria Civile ed Industriale of University of Pisa

DPIN Detailed Fuel-Pin Model

EFIT European Facility for Industrial Transmutation

ENEA Agenzia nazionale per le nuove tecnologie, l’energia e lo sviluppo economico sostenibile

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XII

EoC End of Cycle

EoL End of Life

EOS Equation Of State

ETD European Transmutation Demonstration

FA Fuel Assembly

FASTEF Fast Spectrum Transmutation Experimental Facility

FC Forced Circulation

FZK Forschungszentrum Karlsruhe

GFR Gas Fast Reactor

GIF Generation IV International Forum

HLM High Liquid Metal

HMT Heat and Mass Transfer model

HTC Heat Transfer Coefficient

IAEA International Atomic Energy Agency

IFA InterFacial Area model

IKET Institut für Kern- und Energietechnik

IPS In-Pile Section

IVFHM In-Vessel Fuel Handling Machine

IVFS In-Vessel Fuel Storage

JNC Japan Nuclear Cycle Development Institute KIT Karlsruhe Institute of Technology

LANL Los Alamos National Laboratory

LBE Lead-Bismuth Eutectic

LFR Lead Fast Reactor

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XIII

LMFR Liquid Metal Fast Reactor

LWR Light Water Reactor

M/F Melting/Freezing

MA Minor Actinide

MFBT Minimum Film Boiling Temperature

MFC Multi-Functional Channel

MOX Mixed OXide fuel

MRK Modified Redlich-Kwong

MSR Molten Salt Reactor

MWC Melt Water Contact

MYRRHA Multi-purpose hYbrid Research Reactor for High-tech Applications

NC Natural Circulation

P&T Partitioning & Transmutation

PBA Protected Blockage Accident

PDS-XADS Preliminary Design Studies of an eXperimental Accelerator Driven System

PHX Primary Heat eXchanger

PNC Power Reactor and Nuclear Fuel Development Corp

PTOP Protected Transient OverPower

RVACS Reactor Vault Air Cooling System R&D Research & Development

RIA Reactivity Induced Accident

RV Reactor Vessel

SA Sub-Assembly

SAEOS Simplified Analytic EOS

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XIV

SCARA Selective Compliant Assembly (Articulated) Robot Arm

SCRAM Safety Control Rod Axe Man

SCWR Super Critical Water Reactor

SEARCH Safe ExploitAtion Related CHemistry for HLM reactors

SFR Sodium Fast Reactor

SG Steam Generator

S-S Steady-State

SR Safety Rod

SS Stainless Steel

SPIN Simplified Fuel-Pin Model

TRU TRansUranium element

V/C Vaporization/Condensation

VHTR Very High Temperature Reactor

VF Volume Fraction

WP WorkPackage

XS eXtenSion (SIMMER)

XT-ADS eXperimental Transmuter and irradiation facility based on ADS concept

Roman Letters

A interfacial area (m-1)

a binary-contact area per unit volume (m-1) ALPGK volume fraction of gas

ALPLK4 volume fraction of fuel particles ALPLK5 volume fraction of clad particles

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XV CORF orifice coefficient

c heat capacity (J/kg/K)

Dh hydraulic diameter (m)

E entrainment

e specific internal energy (J/kg)

f volume fraction

g gravity (m/s2)

Gr Grashof number

H heaviside unit function

h heat transfer coefficient (W/m2/K)

i specific enthalpy (J/kg)

K inter-field momentum exchange function (kg/m3/s)

L characteristic length (m)

Nu Nusselt number

p pressure (Pa)

Pr Prandtl number

Q heat transfer rate (W/m3) q heat transfer rate (W/m3)

R gas constant (J/kg/K)

r radius (m)

Ra Rayleigh number

Re Reynolds number

S interfacial area source term (1/m/s)

T temperature (K)

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XVI

TLK3 LBE temperature (°C)

TIPINK center pin temperature (°C) TSK1 surface pin temperature (°C) TSK4 clad temperature (°C) TSK8 can wall temperature (°C

v specific volume of the structure V

ur velocity (m/s)

v

r velocity (m/s)

VM

uuur virtual mass (kg/m2/s2)

We Weber number

Greek letters

α volume fraction or void fraction

δ thermal penetration length (m)

Γ mass-transfer rate per unit volume (kg/s/m3)

κ thermal conductivity (W/m/K)

µ dynamic viscosity (Pa·s)

ρ density (kg/m3)

ρ macroscopic density (kg/m3)

σ surface tension (N/m)

τ time constant (s)

Subscripts

a fuel pin interior node

B bubbly flow regime

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XVII

b fuel pin surface node

c cladding or continuous phase

CP continuous phase

Crt critical (temperature)

D dispersed flow regime

d dispersed phase

f fuel

film film region

FS liquid film

G vapour mixture

GL Terms existing at interface between vapour and liquid velocity

Gm energy component m in a vapour field

hb fluid and fuel pellet surface (rate of energy interchange between) hc fluid and cladding (rate of energy interchange between)

HT heat transfer

int fuel pin interior node

L liquid component

LCW left can wall

Lm energy component m in a liquid field

M material number or energy component

m density component

MF melting/freezing (rate of energy interchange due to)

N nuclear (heating rate)

nf non-flow volume

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XVIII

P particle component

PIN fuel pin

pool pool flow regime q, 'q velocity fields

qq ' terms existing at interface between two velocity fields

RCW right can wall

S Structure component

slug slug flow regime

Sm energy component m in a structure

str structure

VC vaporization/condensation (rate of energy interchange due to)

VS vapour structure

Superscripts

I interface quantity

Riferimenti

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