Numerical Simulation of Spontaneous Capillary Penetration PennState Tony Fick Comprehensive Exam Oct. 27, 2004 Goal: Develop a first principle simulation.

Slides:



Advertisements
Similar presentations
Charles A. Ward Thermodynamics and Kinetics Laboratory, University of Toronto Fluid Behavior In Absence Of Gravity: Confined Fluids and Phase Change Second.
Advertisements

Impact of Microdrops on Solids James Sprittles & Yulii Shikhmurzaev Failure of conventional models All existing models are based on the contact angle being.
Outline Overview of Pipe Flow CFD Process ANSYS Workbench
Dominic Hudson, Simon Lewis, Stephen Turnock
Hongjie Zhang Purge gas flow impact on tritium permeation Integrated simulation on tritium permeation in the solid breeder unit FNST, August 18-20, 2009.
Lecture 15: Capillary motion
Chapter 2 Introduction to Heat Transfer
Basic Governing Differential Equations
Advanced Artificial Lift Methods Electrical Submersible Pump Advanced Artificial Lift Methods – PE 571 Chapter 1 - Electrical Submersible Pump Centrifugal.
DEBRIS FLOWS & MUD SLIDES: A Lagrangian method for two- phase flow simulation Matthias Preisig and Thomas Zimmermann, Swiss Federal Institute of Technology.
Introduction: Gravitational forces resulting from microgravity, take off and landing of spacecraft are experienced by individual cells in the living organism.
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,
Free Convection: General Considerations and Results for Vertical and Horizontal Plates Chapter 9 Sections 9.1 through 9.6.2, 9.9.
2003 International Congress of Refrigeration, Washington, D.C., August 17-22, 2003 CFD Modeling of Heat and Moisture Transfer on a 2-D Model of a Beef.
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.
Heat transfer to fluids without phase change
Basic Governing Differential Equations
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)
James Sprittles ECS 2007 Viscous Flow Over a Chemically Patterned Surface J.E. Sprittles Y.D. Shikhmurzaev.
Fluid Mechanics Wrap Up CEE 331 June 27, 2015 CEE 331 June 27, 2015 
Paradoxes in Capillary Flows James Sprittles Yulii Shikhmurzaev.
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.
ABSTRACT Many new devices and applications are being created that involve transporting droplets from one place to another. A common method of achieving.
Forces Acting on a Control Volume Body forces: Act through the entire body of the control volume: gravity, electric, and magnetic forces. Surface forces:
Monroe L. Weber-Shirk S chool of Civil and Environmental Engineering Basic Governing Differential Equations CEE 331 July 14, 2015 CEE 331 July 14, 2015.
Chapter:1 Fluids & Properties
In the analysis of a tilting pad thrust bearing, the following dimensions were measured: h1 = 10 mm, h2 = 5mm, L = 10 cm, B = 24 cm The shaft rotates.
Flow and Thermal Considerations
Convection Prepared by: Nimesh Gajjar. CONVECTIVE HEAT TRANSFER Convection heat transfer involves fluid motion heat conduction The fluid motion enhances.
Hydraulic Routing in Rivers
Simulation of Droplet Drawback in Inkjet Printing
Dynamics of Capillary Surfaces Lucero Carmona Professor John Pelesko and Anson Carter Department of Mathematics University of Delaware.
James Sprittles BAMC 2007 Viscous Flow Over a Chemically Patterned Surface J.E Sprittles Y.D. Shikhmurzaev.
A Hybrid Particle-Mesh Method for Viscous, Incompressible, Multiphase Flows Jie LIU, Seiichi KOSHIZUKA Yoshiaki OKA The University of Tokyo,
Proceedings of the 18 th International Conference on Nuclear Engineering ICONE18 May , 2010, Xi’an, China Hannam University Fluid-elastic Instability.
KINEMATICS OF PARTICLES Kinematics of Particles This lecture introduces Newtonian (or classical) Mechanics. It concentrates on a body that can be considered.
Unit: IV-Fluid Dynamic
Viscous Flow.
The Rayleigh-Taylor Instability By: Paul Canepa and Mike Cromer Team Leftovers.

NUMERICAL SIMULATION OF AIR POLLUTION TRANSFER IN URBAN AREAS P. I. Kudinov, V. A. Ericheva Dnepropetrovsk National University, Dnepropetrovsk, Ukraine.
Basic Fluid Dynamics.
Mass Transfer Coefficient
Chapter 03: Macroscopic interface dynamics Xiangyu Hu Technical University of Munich Part A: physical and mathematical modeling of interface.
One-Dimensional Steady-State Conduction
Order of Magnitude Scaling of Complex Engineering Problems Patricio F. Mendez Thomas W. Eagar May 14 th, 1999.
Unit 1: Fluid Dynamics An Introduction to Mechanical Engineering: Part Two Fluid dynamics Learning summary By the end of this chapter you should have learnt.
Hydraulic Routing in Rivers Reference: HEC-RAS Hydraulic Reference Manual, Version 4.1, Chapters 1 and 2 Reading: HEC-RAS Manual pp. 2-1 to 2-12 Applied.
200 Physics Concepts from Delores Gende Website
Heat Transfer/Heat Exchanger How is the heat transfer? Mechanism of Convection Applications. Mean fluid Velocity and Boundary and their effect on the rate.
The Generalized Interpolation Material Point Method.
Governing Equations Conservation of Mass Conservation of Momentum Velocity Stress tensor Force Pressure Surface normal Computation Flowsheet Grid values.
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
PRESENTATION OF CFD ACTIVITIES IN CV GROUP Daniel Gasser.
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.
Chapter 4 & 5 Dynamics: Newton's Laws and Its Application.
Combustor modeling Webinar
Engineering Modeling: Mathematical and Computer. What is Engineering Modeling? Model: A representation of a real object or system of objects for purposes.
APPLICATION TO EXTERNAL FLOW
Pipe flow analysis.
Engineering Mechanics: Statics
SIGGRAPH 2005 신 승 호 신 승 호. Water Drops on Surfaces Huamin Wang Peter J. Mucha Greg Turk Georgia Institute of Technology.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 7 External flow.
Chapter 1: Basic Concepts
Chapter 8: Internal Forced Convection
Chapter 8: Internal Flow
Modeling and experimental study of coupled porous/channel flow
Fluid Flow Regularization of Navier-Stokes Equations
Subject Name: FLUID MECHANICS
Anthony D. Fick & Dr. Ali Borhan Governing Equations
Presentation transcript:

Numerical Simulation of Spontaneous Capillary Penetration PennState Tony Fick Comprehensive Exam Oct. 27, 2004 Goal: Develop a first principle simulation to explore fluid uptake in capillaries h(r,t) r

Motivation NASA Advanced Human Support Technology Capillarity critical in water recovery systems, thermal systems, and phase change processes Halliburton studying capillary flow Prevent losses in oil well drilling Paper products work by capillary motion Improved paper product fluid uptake New multi layered film with capillary gradient

Project Objectives Proposed research to identify geometric effects on capillary rate 1) Compute equilibrium height/shape in cylindrical, conical, wedge shaped, elliptical cross sections, and periodic walled capillaries 2) Numerical simulation of capillary penetration in cylindrical, conical, and wedge shaped capillaries from infinite reservoir 3) Modeling kinetics of capillary penetration in cylindrical, conical, and wedge shaped capillaries from finite reservoir 4) Repeat steps 2 and 3 for elliptical cross section capillaries 5) Repeat step 2 for periodically corrugated capillaries

Literature Experimental Results Region IRegion IIRegion III t*t* h*h* t I* t II* h I* h II* M. Stange, M. E. Dreyer, and H. J. Rath, “Capillary driven flow in circular cylindrical tubes,” Physics of Fluids 15, 2587 (2003) Inertial force domain Force from pressure drop at entrance Friction force domain

System to Test Algorithm Interface modeled as function h(r,t) Dynamic contact angle  Need to transform system into simulation box R r z z=h(r,t)  0 0 r z Co-ordinate Transformation Use cylindrical capillary: easy system experimental results

Developing The Model Governing equations for the transformed system: Conservation of Mass Conservation of momentum  direction  direction

Boundary Conditions Velocity Pressure Normal stress condition Update height Tangential stress condition Kinematic condition Contact line velocity constitutive equation L. H. Tanner, “The spreading of silicone oil on horizontal surfaces,” J. Phys. D: Appl. Phys. 12, 1473 (1979). Dimensionless parameters

Numerical Method Initial values for h, P, U, and V Use h for factors in equations Solve for U*Obtain P from div U* Use P to get U from U* Use U to get new h Repeat until convergence Convective terms Viscous terms Pressure terms

Preliminary Results Static case - test geometric effect on meniscus - determine improvement of conical capillary Dynamic simulation of dodecane rise - test model against earthbound experiment - match equilibrium height/shape Dynamic simulation of microgravity rise - match early time-height behavior - test effect of exponent in contact line velocity

Dynamic Rise of Dodecane Region I Region II Region III Data matches within 97.5% confidence interval B. V. Zhmud, F. Tiberg, and K. Hallstensson, “Dynamics of capillary rise,” J. Colloid Interface Sci. 228, 263 (2000) Simulation shows behavior of all three regions

Dodecane Equilibrium 0.1% error Equilibrium shape calculated from static equations Simulation end shape within 0.1% of equilibrium shape Simulation matches dynamic and equilibrium behavior

Dynamic Simulation of Microgravity Use microgravity rise of Dow Corning Silicon fluid “SF 0.65” to match initial height behavior Test effect of exponent in contact line equation Previous work values 1.01, 2.73, 3.00, 3.76 Test values 1.00, 3.00 Experiments carried out in jet producing free fall environment

Time (s) Height (mm) Stange Paper (7) Microgravity run m=3 Microgravity run m=1 m=1 simulation m=3 simulation Dynamic Simulation of Microgravity M. Stange, M. E. Dreyer, and H. J. Rath, “Capillary driven flow in circular cylindrical tubes,” Physics of Fluids 15, 2587 (2003) Simulations match experimental behavior

Static Case Test geometric effect Model reduces to solving single height equation Two different capillaries: cylinder and cone

Static Case Radius (mm) Height (mm) Cone Cylinder Centerline Wall Cone wall Same contact angle  h Increased height for cone, also increased curvature

Conclusions Static Case height increase for conical capillary over cylindrical Dynamic Dodecane Rise end results within 0.1% of equilibrium dynamic data within 97.5% confidence of experimental Dynamic Microgravity Rise simulation matched experimental results exponent in constitutive equation only effects behavior in Region II Model for capillary flow developed based on first principle equations Algorithm able to predict previous experimental results

Future Work Dynamic simulation for capillaries with different geometries to determine geometric effect on capillary penetration (conical, wedge, ellipsoidal, periodic corrugated walls) Experimental results for capillaries with different geometries Develop constitutive equation for contact line for multi phase systems (e.g. surfactants)

Acknowledgements Funding Penn State Academic Computing Fellowship Academic Dr. Ali Borhan Dr. Kit Yan Chan Personal Dr. Kimberly Wain Rory Stine Michael Rogers PennState

Expanded microgravity graph

Constitutive contact line velocity plotted against contact angle aa rr