Title: Governing Equations for TwoPhase NC T10 Reyes
1Department 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
2Course Roadmap
3Lecture 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.
4Outline
- 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
5Introduction
- 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)
6Introduction(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
7Introduction(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. )
8Two-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
9One-Dimensional, Two-Fluid, Full Non-Equilibrium
(Uniform Density within each Phase,Constant
Axial Cross-Sectional Area)
10One-Dimensional, Two-Fluid, Full Non-Equilibrium
(Uniform Density within each Phase,Constant
Axial Cross-Sectional Area)
11One-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.
12One-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
13One-Dimensional, Two-Phase Mixture Transport
Equations (Uniform Density within each
Phase,Constant Axial Cross-Sectional Area)
Mixture Properties
14One-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
15One-Dimensional, Two-Phase Drift Flux Transport
Equations (Uniform Density within each
Phase,Constant Axial Cross-Sectional Area)
16One-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
17Two-Phase Flow Models for Reactor Analysis
18Equivalent Approaches to Developing Model Balance
Equations
19Two-Phase Flow Models with Equal Phase Pressures
(pv pl p)
20Two-Phase Flow Models with Equal Phase Pressures
(pv pl p)
21Two-Phase Flow Models with Equal Phase Pressures
(pv pl p)
22Advancements 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.
23Advancements 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.
24Advancements in Two-Phase Flow Modeling(Interfaci
al Area Concentration Transport Model)
- 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
25Advancements 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.
26Advancements 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.
27Advancements in Two-Phase Flow Modeling(TRACE
Computer Code) J. Staudenmeier, NRC
28Advancements 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
29Conclusions
- 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.