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Governing Equations for TwoPhase NC T10 Reyes

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One-Dimensional Two-Fluid Full Non-Equilibrium Transport Equations ... A variety of methods have been used to model two-phase natural circulation in loops. ... – PowerPoint PPT presentation

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Title: Governing Equations for TwoPhase NC T10 Reyes


1
Department of Nuclear Engineering Radiation
Health Physics
GOVERNING EQUATIONS IN TWO-PHASE FLUIDNATURAL
CIRCULATION FLOWS(Lecture T10)
José N. Reyes, Jr. June 25 June 29,
2007 International Centre for Theoretical Physics
(ICTP) Trieste, Italy
2
Course Roadmap
3
Lecture Objectives
  • Describe the various models used to describe
    mass, momentum and energy transport processes in
    two-phase fluid flows related to natural
    circulation.
  • Provide an overview of new models being
    considered for nuclear reactor safety computer
    codes.

4
Outline
  • Introduction
  • Brief History of U.S. Nuclear Reactor Safety
    Computer Codes
  • Two-Phase Flow Transport Equations
  • One-Dimensional Two-Fluid Full Non-Equilibrium
    Transport Equations
  • Two-Phase Mixture Transport Equations
  • Two-Phase Drift Flux Transport Equations
  • Two-Phase Flow Models for Reactor Analysis
  • Advancements in Two-Phase Flow Modelling
  • Conclusions

5
Introduction
  • The complexity of nuclear reactor geometry (e.g.,
    multiple parallel paths and systems) coupled with
    transient two-phase fluid interactions make
    predictions of two-phase natural circulation
    behavior quite challenging
  • A variety of methods have been used to model
    two-phase natural circulation in loops.
  • Analytical Models (Solutions to Integration of
    transport equations around the loop).
  • Systems codes (3,4,5 and 6 Equation Models)

6
Introduction(Brief History)
  • The FLASH computer code, developed by
    Westinghouse-Bettis, 1950s.
  • Simple"node and branch" approach to modeling
    suitable for some studies of single-phase flow in
    PWRs.
  • Predecessor to the RELAP Series

7
Introduction(Brief History)
  • 1955 to 1975, Reactor Safety Research led to
    major advancements in boiling heat transfer and
    two-phase flow. Mid-1960s, Zubers development of
    the drift flux model.
  • From the early 1970s to the present, the U.S.
    Nuclear Regulatory Commission supported the
    development of a number of computer codes to
    predict Loss-of-Coolant-Accident (LOCA)
    phenomenon.
  • Idaho National Engineering Laboratory (RELAP2,
    RELAP3, RELAP3B (BNL), RELAP4, RELAP5, TRAC-BF1)
  • Los Alamos National Laboratory (TRAC-PF1,
    TRAC-PD1)
  • Brookhaven National Laboratory (RAMONA-3B, THOR,
    RAMONA-3B, RAMONA-4B,HIPA-PWR and HIPA-BWR)
  • In 1996, the NRC decided to produce the
    TRAC/RELAP Advanced Computational Engine or
    TRACE. (Combines the capabilities of RELAP5,
    TRAC-PWR, TRAC-BWR, and RAMONA. )

8
Two-Phase Flow Transport Equations
  • One-Dimensional, Two-Fluid, Full Non-Equilibrium
  • One-Dimensional, Two-Phase Fluid Mixture
  • One-Dimensional, Homogeneous Equilibrium
    Mixture(HEM) Transport Equations
  • One-Dimensional, Two-Phase Drift Flux Transport
    Equations

9
One-Dimensional, Two-Fluid, Full Non-Equilibrium
(Uniform Density within each Phase,Constant
Axial Cross-Sectional Area)
10
One-Dimensional, Two-Fluid, Full Non-Equilibrium
(Uniform Density within each Phase,Constant
Axial Cross-Sectional Area)
11
One-Dimensional, Two-Fluid, Full Non-Equilibrium
(Uniform Density within each Phase,Constant
Axial Cross-Sectional Area)(Neglecting Axial
Heat Conduction and Axial Shear Effect)
Phase k Energy Conservation
  • STAGNATION ENERGY Thermodynamic internal energy
    and the kinetic energy of the fluid phase.
  • STAGNATION ENTAHLPY Usual definition, however,
    it is expressed in terms of the stagnation energy.

12
One-Dimensional, Two-Phase Mixture Transport
Equations (Uniform Density within each
Phase,Constant Axial Cross-Sectional Area)
Mixture Mass Conservation
Mixture Momentum Conservation
Mixture Enthalpy Conservation
13
One-Dimensional, Two-Phase Mixture Transport
Equations (Uniform Density within each
Phase,Constant Axial Cross-Sectional Area)
Mixture Properties
14
One-Dimensional, HEM Transport Equations
(Uniform Density within each Phase,Constant
Axial Cross-Sectional Area)
  • Restrictions Imposed on Two-Phase Mixture
    Equations
  • Thermal Equilibrium (Tl Tv TSAT), or
    Saturated Enthalpies (hl hf and hv hg)
  • Equal Phase Pressures (pl pv p)
  • Equal Velocities (vl vv vm).

Mixture Mass Conservation
Mixture Properties
Mixture Momentum Conservation
Mixture Energy Conservation
15
One-Dimensional, Two-Phase Drift Flux Transport
Equations (Uniform Density within each
Phase,Constant Axial Cross-Sectional Area)
16
One-Dimensional, Two-Phase Drift Flux Transport
Equations (Uniform Density within each
Phase,Constant Axial Cross-Sectional Area)
Mixture Mass Conservation
Drift-Flux Momentum Conservation
Drift-Flux Internal Energy Conservation
17
Two-Phase Flow Models for Reactor Analysis
18
Equivalent Approaches to Developing Model Balance
Equations
19
Two-Phase Flow Models with Equal Phase Pressures
(pv pl p)
20
Two-Phase Flow Models with Equal Phase Pressures
(pv pl p)
21
Two-Phase Flow Models with Equal Phase Pressures
(pv pl p)
22
Advancements in Two-Phase Flow Modeling(Interfaci
al Area Concentration Transport Model)
  • Constitutive laws for interfacial transport are
    currently based on static flow regime maps.
  • Efforts are underway to develop an interfacial
    area concentration transport model for dynamic
    flow regime modeling.
  • Two-Group Interfacial Area Transport Model
    similar to Multi-Group neutron transport model.
  • Group I consists of the spherical/distorted
    bubble group
  • Group II consists of the cap/slug bubble group.

23
Advancements in Two-Phase Flow Modeling(Interfaci
al Area Concentration Transport Model)
  • Two-group bubble number density transport
    equations

Group I
Group II
  • Sj is the net rate of change in the number
    density function due to the particle breakup and
    coalescence processes
  • Sph is the net rate of change in the number
    density function due to phase change
  • Sj,12 and Sj, 21 are the inter-group particle
    exchange terms.

24
Advancements in Two-Phase Flow Modeling(Interfaci
al Area Concentration Transport Model)
  • Number Density Relation
  • ai,k is the interfacial area concentration
  • ? is the void fraction
  • ?k is the bubble shape factor.
  • Subscript k represents the bubble group.
  • Two-group Interfacial Area Transport Equations

Group I
Group II
25
Advancements in Two-Phase Flow Modeling(TRACE
Computer Code)
  • The U.S. Nuclear Regulatory Commission (USNRC) is
    in the process of developing a modern code for
    reactor analysis.
  • It is an evolutionary code that merges RAMONA,
    RELAP5, TRAC-PWR and TRAC-BWR into a single code.
  • The reason for merging the codes, as opposed to
    starting new, is to maintain the sizable
    investment that exists in the development of
    input models for each of the codes.
  • The consolidated code is called the TRAC/RELAP
    Advanced Computational Engine or TRACE.

26
Advancements in Two-Phase Flow Modeling(TRACE
Computer Code)
  • TRACE is a component-oriented code designed to
    analyze reactor transients and accidents up to
    the point of fuel failure.
  • It is a finite-volume, two-fluid, compressible
    flow code with 3-D capability.
  • It can model heat structures and control systems
    that interact with the component models and the
    fluid solution.
  • TRACE can be run in a coupled mode with the PARCS
    three dimensional reactor kinetics code.
  • TRACE has been coupled to CONTAIN through its
    exterior communications interface (ECI) and can
    be coupled to detailed fuel models or CFD codes
    in the future using the ECI.
  • TRACE has been coupled to as user-friendly front
    end, SNAP, that supports input model development
    and accepts existing RELAP5 and TRAC-P input
    models.

27
Advancements in Two-Phase Flow Modeling(TRACE
Computer Code) J. Staudenmeier, NRC
28
Advancements in Two-Phase Flow Modeling(TRACE
Computer Code)
  • Conservation Equations
  • (1) Mixture Mass
  • (1) Vapor Mass
  • (1) Liquid Momentum
  • (1) Vapor Momentum
  • (1) Mixture Energy
  • (1) Vapor Energy
  • Constitutive Equations
  • Equations of State
  • Wall Drag
  • Interfacial Drag
  • Wall Heat Transfer
  • Interfacial Heat Transfer
  • Static Flow Regime Maps
  • Additional Equations
  • Non-condensable Gas
  • Dissolved Boron
  • Control Systems
  • Reactor Power
  • Calculated Parameters
  • Vapor Void Fraction
  • Steam Pressure
  • Non-condensable Gas Pressure
  • Liquid Velocity and Temperature
  • Vapor Velocity and Temperature
  • Boron Concentration
  • Heat Structure Temperatures

29
Conclusions
  • A Description of Two-Phase Flow Transport
    Equations has been provided
  • One-Dimensional, Two-Fluid, Full Non-Equilibrium
  • One-Dimensional, Two-Phase Fluid Mixture
  • One-Dimensional, Homogeneous Equilibrium
    Mixture(HEM) Transport Equations
  • One-Dimensional, Two-Phase Drift Flux Transport
    Equations
  • The 6, 5, 4, and 3 Equation Models have been
    discussed.
  • A brief overview of new models being considered
    in the U.S. for nuclear reactor safety computer
    codes has been presented.
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