Flow Regimes and Mechanistic Predictions of Critical Heat Flux under Subcooled Flow Boiling Conditions - PowerPoint PPT Presentation

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Flow Regimes and Mechanistic Predictions of Critical Heat Flux under Subcooled Flow Boiling Conditions

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Title: Flow Regimes and Mechanistic Predictions of Critical Heat Flux under Subcooled Flow Boiling Conditions


1
Flow Regimes and Mechanistic Predictions of
Critical Heat Flux under Subcooled Flow Boiling
Conditions
  • Jean-Marie Le Corre
  • Westinghouse Electric Sweden AB
  • Carnegie Mellon University, Pittsburgh , USA

2
Outline
  • Introduction
  • Visual experiments, Flow regime types and Flow
    regime map at DNB
  • Postulated mechanistic modeling at DNB
  • Selected DNB model(s)
  • Model validation and applications (1D and 3D)
  • Conclusions and on-going work

3
Introduction
  • Boiling crisis is an important limiting parameter
    in boiling system
  • DNB boiling crisis under subcooled boiling
    conditions
  • Physical modeling of DNB is not well established
  • Mechanistic DNB prediction is useful in
    development of new fuel design
  • Both 1D and 3D applications are desirable

4
Two-phase Flow Regimes at DNB
5
DNB visual experiments flow regime map
  • Review of visual experiments available in the
    literature
  • Various flow regimes were reported
  • Dimensional analysis reveals relevant parameters
  • Consistent calculation of relevant local
    parameters
  • Preliminary map of flow two-phase flow regimes at
    DNB is established
  • Low pressure
  • Limited geometric range
  • X and We as relevant parameters
  • More systematic experimental work is needed

6
DNB visual experiments flow regime map
  • Three main types of flow regime at DNB
  • Type 1 Bubbly flow
  • Type 2 Near-wall vapor clots
  • Type 3 Slug flow

7
DNB visual experiments
8
DNB flow regime map
Type 1
Type 2
Type 3
9
DNB Theoretical Modeling
10
Postulated mechanistic modeling at DNB
  • Various DNB physical modeling can be found in
    literature
  • Most used models relied on near-wall two-phase
    flow hydrodynamics only
  • Experimental evidence show that
  • Various flow pattern can exist at DNB (from
    non-packed bubbly flow to slug flow)
  • No near-wall macroscopic change at DNB
  • Wall effect (e.g. thickness) is important
  • Goal Select model in agreement with experimental
    observations

11
DNB modeling in the literature
  • Theoretical studies
  • Near-wall bubble crowding model (Weisman and Pei,
    1983)
  • Liquid sublayer dryout model (Lee and Mudawar,
    1988)
  • Many others
  • Experimental studies
  • Three main types of flow regime at DNB
  • Dry patch formation quenching prevention has
    been mentioned for Type 1 and 3 (few theoretical
    studies)
  • Bubbly layer lift-off model (Mudawar)
    hypothesized for Type 2

12
Selected DNB model
  • Basic DNB modeling is based on a dry spot created
    under a nucleating bubble (1) or a vapor clots
    (2) or a vapor slug (3)
  • Temperature locally increases under dry area then
    decreases due to quenching
  • Quenching may be prevented in the limiting case
    (Leidenfrost)
  • Resulting dry patch may spread through radial
    conduction

13
DNB physical modeling (Type 1)
  • 2D transient wall thermal response to nucleation
    cycle is calculated (ADI scheme transient heat
    flux boundary conditions)
  • Model consistent with wall boiling model is
    desirable
  • Most needed parameters are in use in wall
    partitioning model (e.g. RPI model)

14
DNB physical modeling (Type 1)
  • A limiting nucleation site is considered
    (stochastic nature)
  • Domain extend to as many averaged nucleation
    sites as necessary

15
DNB physical modeling (Type 1)
  • Needed (optional) constitutive relations
  • Bubble departure diameter ( bubble growth rate)
  • Time of evaporation
  • Bubble departure frequency
  • Nucleation site density
  • Evaporation heat flux (transient form)
  • Quenching heat flux (transient form)
  • Limiting conditions

16
DNB Model Validation
17
Model validation and applications
  • Model validation
  • Limiting nucleation site is the key to the model
  • Use detailed boiling data at DNB (bypass most
    constitutive relations) to show Leidenfrost
    effect can happen
  • Model various CHF points (1D) to study the
    limiting nucleation site
  • Model applications
  • 1D
  • 3D

18
Model validation (Del Valle Kenning data)
  • Detailed boiling information were reported form
    70-95 of DNB (bubble departure diameter, bubble
    departure frequency, nucleation site density,)
  • Parameters from most limiting nucleation site
    calculated from statistical distribution
  • Used for DNB model validations (Type 1)
  • Wall superheat around 100 C can be reached
    allowing for Leidenfrost effect (150 50 C)

19
Model validation (Del Valle data)
  • 2D transient wall thermal response to Nucleation
    cycle
  • DNB occurrence
  • Wall thermal response immediately after DNB (dry
    patch spreading)

20
Model validation (Del Valle data)
  • 2D transient wall thermal response to Nucleation
    cycle
  • DNB occurrence
  • Wall thermal response immediately after DNB (dry
    patch spreading)

L
1
2
3
21
Model validation (Del Valle data)
Hot spot superheat
Dry patch radius
Time
22
Model applications (on going)
  • 1D applications in progress
  • Look-up CHF database
  • Study of limiting nucleation site
  • 3D applications
  • Limited by current advances in the field
  • Prototype CFX-5.7.1 was used in simple geometry
  • Validated at high pressure
  • Validation at low pressure performed in this work
  • Applied to CFD experiments at high pressure
    (DeBortoli, 1958)
  • Approach to complex geometry and fuel assembly
    design

23
3-D CFX-5.7.1 validation (Bartel data)
Volumetric interfacial area
Void fraction
24
3-D DNB Model Applications (on-going)
  • DeBortoli data (1958)
  • Local We 2426 at DNB, local x -0.086
  • Type 2 region but probably Type 1 at high
    pressure
  • Modified Unals model was used
  • Limiting nucleation site 2 averaged bubble
    diameter
  • DNB model application
  • Peak wall superheat 105 C for 0.5 mm SS heater
  • Peak wall superheat 95 C for 1.0 mm SS heater

25
3-D application in complex geometries
  • Not in the scope of the current research program
  • No accurate prediction of CHF is expected
  • Correct parametric trends and correct treatment
    of 3D effects are expected
  • Approach
  • Compute peak wall superheat in each near-wall
    computational cell (CFD post-processing)
  • Show local weak spot relative to DNB
  • Design goal is a low ( uniform) peak wall
    superheat

26
Conclusions
  • Different model of DNB can apply (compete)
    depending on conditions (pressure, We, x)
  • A most likely mechanism is identified for Type
    1 (and Type 3)
  • Model is validated using detailed boiling data
  • Definition of limiting nucleation site is the key
  • Additional validations, 1D and 3D applications
    are on going
  • Accurate prediction of CHF is not expected
  • Help in increasing CHF performance of complex
    systems
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