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Stratified Flow Phenomena, Graphite Oxidation, and Mitigation Strategies of Air Ingress Accident INL / Chang Oh, U.S. PI.

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Presentation on theme: "Stratified Flow Phenomena, Graphite Oxidation, and Mitigation Strategies of Air Ingress Accident INL / Chang Oh, U.S. PI."— Presentation transcript:

1 Stratified Flow Phenomena, Graphite Oxidation, and Mitigation Strategies of Air Ingress Accident
INL / Chang Oh, U.S. PI

2 Background and Motivation
What happens following LOCA ? Depressurization Stratified Flow Diffusion Natural Convection T/H Safety Issues Core maximum temperature Potential core collapse Technical Requirements Accurate stratified flow modeling Accurate graphite oxidation and collapse modeling Accurate power distribution with neutronics model

3 Objectives To conduct experiments to supply information to model important phenomena in air-ingress accident, and code V&V. Effect of density-driven stratified flow on the air-ingress Oxidation and density variation of the graphite structures Internal pore area density of the graphite structures Effect of burn-off on the structural integrity of the graphite structures To develop a coupled neutronics and thermal-hydraulic capability in the GAMMA code Development of core neutronics model Coupling neutronic-thermal hydraulic tools Coupled core model V&V To evaluate various methods for the mitigation of air-ingress

4 Project Organization Schematic diagram of all tasks involved GAMMA
Stratified Flow Study Task 1 (INL) Validation Task 2 (INL) Stratified Flow Analysis (CFD & GAMMA) Stratified Flow Experiment Advanced Graphite Oxidation Study Models and Parameters Core Neutronic Model Models and Parameters Task 7 (KAIST) Task 3 (INL) Coupling Neutronic Thermal Hydraulic Tool Advanced Graphite Oxidation Study GAMMA Code Models and Parameters Task 8 (KAIST) Task 5 (KAIST) Experiment of Burn-off In the Bottom Reflector Analysis Core Neutronic Model Task 9 (KAIST) Task 6 (KAIST) Task 4 (INL) Coupled Core Model V&V Structural Test of Burn- off Bottom Reflector Full Air-ingress Analysis Air-ingress Mitigation Study

5 New Assumption on the Air-ingress Analysis
Stratified Flow in Air-ingress Previous air-ingress analyses are all based on the assumption that the main air-ingress is dominated by molecular diffusion. Previous analyses were performed using 1-D and a vertical geometry A new issue has been raised for the possibility of a convective flow driven by local density gradient. After depressurization, there is large density differences between inside(Helium) and outside(Air) of vessel. The density driven stratified flow can highly accelerate the whole air-ingress scenarios. Diffusion Assumption (40000 sec) Stratified Flow Assumption (60 sec)

6 Density-Gradient Driven Stratified Flow
(1) Depressurization (2) Onset-of Flow (3) Density-driven Flow Air ingress velocities by density driven flow Volumetric flowrates of air and helium are the same. At the interface, the shear stresses are the same between Air and Helium.

7 Density Driven Stratified Flow
Water and Salted Water Experiment Helium Air Salted Water Water

8 New Scenario for Air Ingress
Helium

9 CFD Analysis on the Stratified Flow in VHTR
51,566 nodes Mesh (GAMBIT / FLUENT)

10 Porous Media Parameters
Porous Media Approach Core and Plenum were assumed to be porous media. Porosity and Permeability should be determined. Porous Zones Additional Momentum Source permeability Inertia resistance

11 Porous Media Parameters
Porosity In the Core Core Hole Pattern (d = 1.58 cm, p = 3.27 cm) In the Lower Plenum Geometry of Lower Plenum (d = m, p = 0.36 m)

12 Porous Media Parameters
Flow Resistance Parameters in the Core Empirically determined based on the friction correlations Flow resistance in the radial was assumed to be infinitely large. In the Core Friction Factor in the Circular Channel

13 Porous Media Parameters
Flow Resistance Parameters in the Lower Plenum Flow resistance in the radial direction was calculated based on the friction data in the staggered array. Flow resistance in the axial direction was calculated based on the friction data in the circular pipe flow. For axial direction In the Lower Plenum For radial direction Friction Factor in the Staggered Array

14 Simulation of Stratified Flow
Stratified Flow Simulation (by FLUENT 6.3) Initial Conditions Temperature Air-Mole Fraction Natural convection started about 160 sec after simulation.

15 Turbulence Models

16 Multi-step Approach for Air-ingress Analysis
Stratified flow phase was solved by CFD code (FLUENT). Depressurization and Diffusion/natural convection phase were solved by GAMMA code. CFD Code System Code 1. Depressurization Analysis Data Transfer 2. Stratified Flow Analysis Data Transfer 3. Natural Convection Analysis FLUENT Simulation GAMMA Simulation

17 Air Ingress Analysis - Results
Temperature (Bottom Reflector) Temperature (Core) Corrosion (Lower Plenum) DDA-1 Diffusion Dominated Air-Ingress In the Infinite Vault (1X1010 m3) DDA-2 In the Finite Vault (25,000 m3) SFDA-1 Stratified Flow Dominated Air-Intress SFDA-2 In the finite Vault (25,000 m3) Stratified Flow Assumption Diffusion Assumption

18 Isothermal Experiment in the Horizontal Circular Pipe (TEST-1)
Experimental Plan - 1 Isothermal Experiment in the Horizontal Circular Pipe (TEST-1) Focused on the separate effect of stratified flow phenomena A simple scaling method used for pipe sizing and test conditions. 1~1.5 m 1m 0.5~1.0 m Tube diameter = 20 cm

19 Scaling Analysis of Stratified Flow in a Simple Channel
Experimental Plan - 1 Scaling Analysis of Stratified Flow in a Simple Channel Summary of Scaling Results (ratio = scaled down/full-scale) Countercurrent stratified flow behavior in the VHTR hot duct (Turner(1973)) By Reynolds number similitude By gas law

20 Non-isothermal Test (TEST-2)
Experimental Plan - 2 Non-isothermal Test (TEST-2) Focused on the coupling effect of stratified flow and natural convection. On-set of natural convection is the main measuring parameter. 0.8~1.0 m Pipe diameter 5 cm

21 Onset of natural convection occurred at around 400 sec.
Experimental Plan - 2 Fluent Simulation for Density Driven Air-ingress Experiment 10 sec 20 sec 40 sec 80 sec 300 sec 400 sec 410 sec 420 sec Onset of natural convection occurred at around 400 sec.

22 Experimental Plan - 2 FLUENT Results for Density Driven Air-ingress Experiment (at Valve-3) Time vs. Flow-rate Time vs. Temperature onset of natural convection onset of natural convection Flow rate and Temperature can be used as signals for onset-natural-circulation.

23 Experimental Plan – 3 and 4
Non-isothermal Test (TEST-3, TEST-4) Focused on the coupling effects Stratified Flow + Natural Convection + Porous Media + Chemical Reaction Basic Experimental Procedures are the same as TEST 2 Metal (TEST-3) or Graphite (TEST-4) Non-isothermal test with Pebbles Non-isothermal test with Structures

24 Experiment on the Oxidized Graphite Fracture
Experimental Set-up The experiment was performed at 650 oC for uniform oxidation. The test procedure and set-up is based on ASTM standard test method. IG-110 and H451 graphite was used for testing. Sample load and holder

25 Experiment on the Oxidized Graphite Fracture
Normal Compressive Stress vs. Burn-off old data old data H-451 IG-110 New data New data

26 Graphite Surface Area Density
Graphite Surface Area Density (Unoxidized Initial Value) The graphite surface area density was calculated from the BET surface area measured by previous investigations. Density [g/m3] Specific Surface Area [m2/g] Surface Area Density [m2/m3] NBG-18 (Contescu (2008)) 1790 0.21 375.9 NGB-10 0.29 519.1 PCEA 20-20 0.46 823.4 IG-11 (Eto and Growcock (1981)) 1750 2.8 4900 IG-110 (Nakano et al. (1997)) 1780 0.5 890 H451 (Pawelko et al. (2001)) 1760 0.75 1320 PGX 1730 0.7 1211

27 Effect of Graphite Burn-off on the Oxidation Rate
Graphite Oxidation Rate and Burn-off The reaction rate increases with the increasing burn-off in the beginning because of the increase of pore size and porosity open. The reaction rate decreases at high burn-off because the pores join together, decreasing the reaction surface area.

28 Modeling of Graphite Oxidation and Fracture in Air-ingress
Reference Reactors (GT-MHR 600 MWt) Core Graphite Structure

29 Estimation of Corrosion Depth by GAMMA code
Burn-off refers to the oxidation of the graphite’s internal body, causing reduction of density, leading to reduction of stiffness and mechanical strength. Corrosion refers to oxidation taking place on the outer surface exposed to airflow. The corrosion decreases the cross-sectional area available to support the weight leading to stress concentration. Most Seriously Damaged!

30 Detailed Geometry of the Supporting Block
Coolant channels from core Lower reflector blocks

31 Oxidized State Results
Compressive stress distribution on plenum head, 6.5 days after ONC Corrosion Progression 1/6 cyclic symmetry unit of the modified plenum head for each day * The specified time is the elapsed time after natural convection.

32 Oxidized State Results
Failure occurs 5.5 to 6 days after the start of natural convection

33 Experimental facility
Task 5 - Experimental facility Task Progress Kinetics Completed activity Planned activity Activation energy Order of reaction Graphite selection Experimental facility Bottom reflector Burn-off model IG-110 IG-430 NBG-18 NBG-25 Mass transfer Design Installation Heat/mass analogy Other effects Geometry Burn-off Moisture IG-110, IG-430, NBG-18, NBG-25 were selected sample graphite. The test facility was installed. This facility was designed to test kinetics, mass transfer, combined-effect, effect of burn-off and effect of moisture. Kinetics of IG-110 and IG-430 was studied this year. Schematics of Experimental Facility 33

34 Task 5 - Test Condition Graphite Temperature (oC) Flow rate (SLPM)
First Kinetics of IG-110 and IG-430 was measured. Temperature range is 540~800 degree C. oxygen fraction was maximum 32%. Picture of the Test Section Temperature (oC) 540 ~ 800 Flow rate (SLPM) ~ 10 SLPM (0.04 m/s) Oxygen fraction (%) ~ 34 % Graphite 34

35 Task 5 – Kinetics (I) IG-110 IG-430 Activation energy (kJ/mol) 218 ± 4
Activation energy and order of reaction of IG-110 and IG-430 were measured. Figure show the data of IG-430 Effect of Temperature on Oxidation Rate Effect of Oxygen Concentration on Oxidation Rate IG-110 IG-430 Activation energy (kJ/mol) 218 ± 4 158.5 ± 1.5 Order of reaction, n 0.75 ± 0.15 0.37 ± 0.04 35

36 Task 5 – Kinetics (II) IG-110 IG-430 Material Author T (℃)
Oxygen Mole Fraction Flow rate (SLPM) Ea (kJ/mol) n Method IG-110 Fuller 450~750 0.2 0.496 201 - TGA Kawakami 550~650 210 Gas Analysis Ogawa 700~1500 0.05~0.19 0.2~4.5 200 KAIST 540~630 0.03~0.32 7~18 218 0.75 IG-430 KAERI 608~808 10 161.5 540~800 0~0.34 8~10 158.5 0.37 36

37 Task 6 - Task Progress Task Progress Fresh graphite Failure test
Completed activity Planned activity Fresh graphite Failure test Oxidized graphite Mechanical test Structural analysis Uniform oxidation Non-uniform oxidation Structure Support column Support block Other components GAMMA Failure Model Development Data collection Estimation of burn-off 37

38 Task 6 - Bottom structures
Bottom reflector components and condition Components Condition Relative temperature Support column A graphite column encounters oxygen first when an air-ingress event occurs Low (cooling effect) Support block A support block has a lot of channels. External surface is relatively large. High (close to core) There are two bottom structures mainly issued. One is support column and another is support block. Support column was historically considered that it is the weakest structure. A support block also is easy to be oxidized because a support block has a lot of channels; large external surface. This year, the study was focused about failure of graphite column. (simplified graphite column figure) Oxidized graphite column is to be decreased in bulk density and to be slender. Long column is easy to fail under axial load. Schematics of oxidation trend in graphite support columns Graphite support columns, GT-MHR 600MWth 38

39 Task 6 - Test facility Picture of the electric furnace
Hardened steel plate Machine cross head Air outlet Vent Thermocouple Clear Plastic safety shield Test specimen Graphite specimen Insulating material Compression block Spherical block Support plate Air inlet Distributor Picture of the electric furnace Picture of the failure test facility 39

40 Task 6 – Compressive and buckling strength of
fresh IG-110 column Compressive strength of IG-110 IG-110 Φ15mm ×30mm 80.16 ± 1.97MPa Φ25mm ×50mm 78.75 ± 2.48 MPa Average 79.46 MPa Buckling point: Measured compressive strength was listed in table. The measured bucking strength versus slenderness ratio was showed in figure . It shows that the critical strength of graphite columns is reduced with an increase of the slenderness ratio. buckling point is estimated by the calculating the intersection point of compressive strength and buckling strength correlation. Buckling strength 40

41 Task 6 - Compressive and buckling strength of oxidized IG-110 column
Normalized compressive strength of oxidized graphite Normalized compressive and buckling strength of oxidized graphite columns. Samples of graphite were oxidized in the electric furnace. Furnace temperature was 600 degree C and air is sufficiently supplied. Figure shows that normalized compressive strength of oxidized graphite. The relation between the compressive strength and bulk density can be estimated by the Knudsen relation. Another figure shows the degradation of oxidized graphite which have various geometry. The relation between the strength and bulk density also can be estimated by the Knudsen relation; there is no remarkable trend. The strength of oxidized graphite column under axial load: 41

42 Average fracture load (Unit: Kgf)
Task 6 - Fracture load changes of oxidized complicated-shape samples Table of complicated-shape sample test Sample 1 Sample 2 Sample 3 Geometry (Unit: mm) Top: Φ10 × 10 Bottom: Φ20 × 10 Top: Φ10 × 20 Bottom: Φ20 × 20 Cylindrical column: Φ15 × 60 Cap: 15.1 × 10 (7 in depth) Average fracture load (Unit: Kgf) 590.1 531.3 1297.3 Complicated-shape sample were tested for applicability of the correlation. The correlation can be applied for the complicated-shape samples. It turns out that the strength degradation trend of oxidized graphite structure is independent of geometry while the strength degradation of a uniformly oxidized graphite structure is dependent on the initial strength of structure and the bulk density change. Fracture load changes of oxidized complicated-shape samples 42


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