Design Constraints for Liquid-Protected Divertors S. Shin, S. I. Abdel-Khalik, M. Yoda and ARIES Team G. W. Woodruff School of Mechanical Engineering Atlanta,

Slides:



Advertisements
Similar presentations
Introduction to Plasma-Surface Interactions Lecture 6 Divertors.
Advertisements

Lecture 15: Capillary motion
Ss Hefei, China July 19, 2011 Nuclear, Plasma, and Radiological Engineering Center for Plasma-Material Interactions Contact: Flowing.
CHAPTER 2 DIFFERENTIAL FORMULATION OF THE BASIC LAWS 2.1 Introduction  Solutions must satisfy 3 fundamental laws: conservation of mass conservation of.
Self-propelled motion of a fluid droplet under chemical reaction Shunsuke Yabunaka 1, Takao Ohta 1, Natsuhiko Yoshinaga 2 1)Department of physics, Kyoto.
DIFFUSION MODELS OF A FLUIDIZED BED REACTOR Chr. Bojadjiev Bulgarian Academy of Sciences, Institute of Chemical Engineering, “Acad. G.Bontchev” str.,
Results It was found that variations in wettability disturb the flow of adjacent liquid (Fig. 3). Our results suggest that for a given liquid the normal.
Analysis of Simple Cases in Heat Transfer P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Gaining Experience !!!
1 MECH 221 FLUID MECHANICS (Fall 06/07) Tutorial 6 FLUID KINETMATICS.
Thermal Analysis of Helium- Cooled T-tube Divertor S. Shin, S. I. Abdel-Khalik, and M. Yoda ARIES Meeting, Madison (June 14-15, 2005) G. W. Woodruff School.
Fluid Mechanics Research Laboratory Vibration Induced Droplet Ejection Ashley James Department of Aerospace Engineering and Mechanics University of Minnesota.
Preliminary Assessment of Porous Gas-Cooled and Thin- Liquid-Protected Divertors S. I. Abdel-Khalik, S. Shin, and M. Yoda ARIES Meeting, UCSD (March 2004)
Experimental Verification of Gas- Cooled T-Tube Divertor Performance L. Crosatti, D. Sadowski, S. Abdel-Khalik, and M. Yoda ARIES Meeting, UCSD (June 14-15,
Jordanian-German Winter Academy 2006 NATURAL CONVECTION Prepared by : FAHED ABU-DHAIM Ph.D student UNIVERSITY OF JORDAN MECHANICAL ENGINEERING DEPARTMENT.
James Sprittles ECS 2007 Viscous Flow Over a Chemically Patterned Surface J.E. Sprittles Y.D. Shikhmurzaev.
CHE/ME 109 Heat Transfer in Electronics
An Overview of the Fluid Dynamics Aspects of Liquid Protection Schemes for Fusion Reactors S. I. Abdel-Khalik and M. Yoda TOFE-16 Meeting - Madison (September.
Temperature Gradient Limits for Liquid-Protected Divertors S. I. Abdel-Khalik, S. Shin, and M. Yoda ARIES Meeting (June 2004) G. W. Woodruff School of.
CE 1501 CE 150 Fluid Mechanics G.A. Kallio Dept. of Mechanical Engineering, Mechatronic Engineering & Manufacturing Technology California State University,
Introduction to Convection: Flow and Thermal Considerations
Heat Flux Gradient Limits for Liquid-Protected Divertors S. I. Abdel-Khalik, S. Shin, and M. Yoda ARIES Meeting, San Diego (Nov 4-5, 2004) G. W. Woodruff.
Computation of FREE CONVECTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Quantification of Free …….
M. Yoda, S. I. Abdel-Khalik, D. L. Sadowski and M. D. Hageman Woodruff School of Mechanical Engineering Extrapolating Experimental Results for Model Divertor.
1 NUMERICAL AND EXPERIMENTAL STUDIES OF THIN-LIQUID-FILM WALL PROTECTION SCHEMES S.I. ABDEL-KHALIK AND M. YODA G. W. Woodruff School of Mechanical Engineering.
Fluid Dynamics: Boundary Layers
Flow and Thermal Considerations
General Formulation - A Turbojet Engine
Introduction to Convection: Flow and Thermal Considerations
Heat Transfer in Structures
T HE C OOLING E FFECTS OF V ARYING W ATER D ROPLET V OLUME AND S URFACE C ONTACT A NGLE W ITH A M ETAL S URFACE I N A S TEADY S TATE, H IGH T EMPERATURE.
1 CHAPTER 5 POROUS MEDIA Examples of Conduction in Porous Media component electronic micro channels coolant (d) coolant porous material (e) Fig.
M. Yoda, S. I. Abdel-Khalik, D. L. Sadowski, B. H. Mills, and J. D. Rader G. W. Woodruff School of Mechanical Engineering Updated Thermal Performance of.
A Hybrid Particle-Mesh Method for Viscous, Incompressible, Multiphase Flows Jie LIU, Seiichi KOSHIZUKA Yoshiaki OKA The University of Tokyo,
PTT 204/3 APPLIED FLUID MECHANICS SEM 2 (2012/2013)
Multiscale analysis of gas absorption in liquids Wylock, Dehaeck, Mikaelian, Larcy, Talbot, Colinet, Haut Transfers, Interfaces and Processes (TIPs) Université.
M. Yoda, S. I. Abdel-Khalik, D. L. Sadowski, B. H. Mills, and J. D. Rader G. W. Woodruff School of Mechanical Engineering Correlations for the Plate Divertor.
Mass Transfer Coefficient
The Governing Equations The hydrodynamic model adopted here is the one based on the hydrostatic pressure approximation and the boussinesq approximation,
Stirling-type pulse-tube refrigerator for 4 K M. Ali Etaati CASA-Day April 24 th 2008.
Chapter 6 Introduction to Forced Convection:
Free Convection: General Considerations and Results for Vertical and Horizontal Plates 1.
J.-Ph. Braeunig CEA DAM Ile-de-FrancePage 1 Jean-Philippe Braeunig CEA DAM Île-de-France, Bruyères-le-Châtel, LRC CEA-ENS Cachan
Nazaruddin Sinaga Laboratorium Efisiensi dan Konservasi Energi Fakultas Teknik Universitas Diponegoro.
HEAT TRANSFER FINITE ELEMENT FORMULATION
T HE E VAPORATIVE C OOLING E FFECTS OF V ARYING W ATER D ROPLET C HARACTERISTICS ON A M ETAL S URFACE I N A S TEADY S TATE, H IGH T EMPERATURE A IR F LOW.
FREE CONVECTION 7.1 Introduction Solar collectors Pipes Ducts Electronic packages Walls and windows 7.2 Features and Parameters of Free Convection (1)
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
Compressible Frictional Flow Past Wings P M V Subbarao Professor Mechanical Engineering Department I I T Delhi A Small and Significant Region of Curse.
Chapter 9: Natural Convection
CONDUCTION WITH PHASE CHANGE: MOVING BOUNDARY PROBLEMS
1 NUMERICAL AND EXPERIMENTAL STUDIES OF THIN-LIQUID-FILM WALL PROTECTION SCHEMES S.I. ABDEL-KHALIK AND M. YODA G. W. Woodruff School of Mechanical Engineering.
Two-phase hydrodynamic model for air entrainment at moving contact line Tak Shing Chan and Jacco Snoeijer Physics of Fluids Group Faculty of Science and.
M. Yoda, S. I. Abdel-Khalik, D. L. Sadowski, B. H. Mills and M. D. Hageman G. W. Woodruff School of Mechanical Engineering Correlations for Divertor Thermal-Hydraulic.
Nelson Applied Research, Inc – N. 88 th St. Seattle, WA USA aol.com Study of Heat Flux in a Thin Silicon MEMS Wafer.
1 CASE 2: Modeling of a synthetic jet in a cross flow Williamsburg, Virginia, USA March 29 th -31 th 2004 C. Marongiu 1, G. Iaccarino 2 1 CIRA Italian.
CAD and Finite Element Analysis Most ME CAD applications require a FEA in one or more areas: –Stress Analysis –Thermal Analysis –Structural Dynamics –Computational.
Convection Heat Transfer in Manufacturing Processes P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Mode of Heat Transfer due to.
CONVECTION : An Activity at Solid Boundary P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Identify and Compute Gradients.
T HE C OOLING E FFECTS OF V ARYING W ATER D ROPLET V OLUME AND S URFACE C ONTACT A NGLE W ITH A M ETAL S URFACE I N A S TEADY S TATE, H IGH T EMPERATURE.
CHAPTER 6 Introduction to convection
Transient Analysis of Heat Transfer and Fluid Flow in a Polymer-based Micro Flat Heat Pipe with Hybrid Wicks Mehdi Famouria, Gerardo Carbajalb, Chen Lia.
Design of Port Injection Systems for SI Engines
Fourier’s Law and the Heat Equation
Fourier’s Law and the Heat Equation
CAD and Finite Element Analysis
Extended Surface Heat Transfer
Finite difference code for 3D edge modelling
topic8_NS_vectorForm_F02
topic8_NS_vectorForm_F02
A. Vertkov et al., SC “Red Star”, Moscow, Russia
Presentation transcript:

Design Constraints for Liquid-Protected Divertors S. Shin, S. I. Abdel-Khalik, M. Yoda and ARIES Team G. W. Woodruff School of Mechanical Engineering Atlanta, GA 30332–0405 USA

2 Work on Liquid Surface Plasma Facing Components and Plasma Surface Interactions has been performed by the ALPS and APEX Programs Operating Temperature Windows have been established for different liquids based on allowable limits for Plasma impurities and Power Cycle efficiency requirements This work is aimed at establishing limits for the maximum allowable temperature gradients (i.e. heat flux gradients) to prevent film rupture due to thermocapillary effects Spatial Variations in the wall and Liquid Surface Temperatures are expected due to variations in the wall loading Thermocapillary forces created by such temperature gradients can lead to film rupture and dry spot formation in regions of elevated local temperatures Initial Attention focused on Plasma Facing Components protected by a “non- flowing” thin liquid film (e.g. porous wetted wall) Problem Definition

3 open B.C. at top, y l >>h o periodic B.C. in x direction Specified Non-uniform Wall Temperature Two Dimensional Cartesian (x-y) Model (assume no variations in toroidal direction) Two Dimensional Cylindrical (r-z) Model has also been developed (local “hot spot” modeling) L Gas Liquid y Wall h o initial film thickness x Convective cooling Non-uniform heat flux L Gas Liquid y Wall h o initial film thickness x Non-uniform wall temperature Specified Non-uniform Surface Heat flux Initially, quiescent liquid and gas (u=0, v=0, T=T m at t=0)

4 Energy Momentum Conservation of Mass Governing Equations Non-dimensional variables Specified Non-uniform Wall Temperature Specified Non-uniform Surface Heat flux

5 Asymptotic Solution ( Low Aspect Ratio Cases) Asymptotic solution used to analyze cases for Lithium, Lithium-lead, Flibe, Tin, and Gallium with different mean temperature and film thickness Asymptotic solution produces conservative (i.e. low) temperature gradient limits Limits for “High Aspect Ratio” cases analyzed by numerically solving the full set of conservation equations using Level Contour Reconstruction Method Long wave theory with surface tension effect (a<<1). Govering Equations reduce to : Specified Non-uniform Wall Temperature *Specified Non-uniform Surface Heat flux * [Bankoff, et al. Phys. Fluids (1990)]

6 Similar Plots have been obtained for other aspect ratios In the limit of zero aspect ratio Asymptotic Solution ( Low Aspect Ratio Cases) 1/Fr (  T s /L)/(  L 2 /  L  o h o 2 ) Maximum Non-dimensional Temperature Gradient 1/We=10 7 1/We=10 6 1/We=10 5 1/We=10 4 1/We=10 3 1/We=10 2 a=0.02 aNu=10 0 aNu=10 -1 aNu=10 -2 aNu=10 -3 aNu=10 -4 ( Q /L)/( a  L g k/  o ) o/LgL2o/LgL2 Maximum Non-dimensional Heat Flux Gradient Specified Non-uniform Wall Temperature Specified Non-uniform Surface Heat flux

7 Parameter LithiumLithium-LeadFlibeTinGallium 573K773K573K773K573K773K1073K1473K873K1273K Pr /Fr 1.2           /We 7.8           10 7 [K/m] * 1/We  h o, 1/Fr  h o 3 Asymptotic Solution ( Low Aspect Ratio Cases) – Specified Non-uniform Wall Temp (h o =1mm) Property ranges Coolant Mean Temperature [K] Max. Temp. Gradient : (  T s /L) max [K/cm] Asymptotic SolutionNumerical Solution Lithium Lithium-Lead Flibe Tin Ga

8 Coolant Mean Temperature [K]  o /  L gL 2 Max. Heat Flux. Gradient : (Q  /L) max [(MW/m 2 )/cm] aNu=1.0aNu=0.1aNu=0.01 Lithium    Lithium-Lead   Flibe     Tin   Ga   h o =10 mm, a=0.02 Coolant Mean Temperature [K] Max. Heat Flux. Gradient : (Q  /L) max [(MW/m 2 )/cm] a=0.05a=0.02a=0.01a=0.005a=0.002 Lithium      Lithium-Lead      Flibe      Tin      Ga      10 0 h o =1 mm, aNu=1.0 Asymptotic Solution ( Low Aspect Ratio Cases) – Specified Non-uniform Surface Heat Flux

9 Evolution of the free surface is modeled using the Level Contour Reconstruction Method Two Grid Structures  Volume - entire computational domain (both phases) discretized by a standard, uniform, stationary, finite difference grid.  Phase Interface - discretized by Lagrangian points or elements whose motions are explicitly tracked. Phase 2 Phase 1 F Numerical Solution ( High Aspect Ratio Cases) A single field formulation Constant but unequal material properties Surface tension included as local delta function sources  Force on a line element  Variable surface tension : thermocapillar y force normal surface tension force AtAAtA -BtB-BtB n BtBBtB e -CtC-CtC A B ss n : unit vector in normal direction t : unit vector in tangential direction  : curvature

10 Two-dimensional simulation with 1[cm]  0.1[cm] box size, 250  50 resolution, and h o =0.2 mm Numerical Solution ( High Aspect Ratio Cases) - Specified Non-uniform Wall Temperature case using Lithium x [m] y [m] time [sec] y [m] maximum y location minimum y location black : blue : red : a=0.02 velocity vector plot temperature plot

11 1/We (  T s /L)/(  L 2 /  L  o h o 2 ) Pr=40 Pr=0.4 Pr=0.004 Asymptotic Solution Maximum Non-dimensional Temperature Gradient 1/We 1/Fr=10 3 1/Fr=10 5 1/Fr=10 1 Numerical Solution ( High Aspect Ratio Cases) - Specified Non-uniform Wall Temperature case a=0.02

12 Limiting values for the temperature gradients (or heat flux gradients) to prevent film rupture can be determined Generalized charts have been developed to determine the temperature (or heat flux) gradient limits for different fluids, operating temperatures (i.e. properties), and film thickness values For thin liquid films, limits may be more restrictive than surface temperature limits based on Plasma impurities (evaporation) constraint Experimental Validation of Theoretical Model has been initiated Preliminary results for Axisymmetric geometry (hot spot model) produce more restrictive limits for temperature gradients Conclusions