Flow Behavior and Instabilities in Viscoelastic Fluids: Physical and Biological Systems
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Frictional Peeling and Adhesive Shells Suomi Ponce Heredia
Adhesion of thin structures : frictional peeling and adhesive shells Suomi Ponce Heredia To cite this version: Suomi Ponce Heredia. Adhesion of thin structures : frictional peeling and adhesive shells. Physics [physics]. Université Pierre et Marie Curie - Paris VI, 2015. English. NNT : 2015PA066550. tel- 01327267 HAL Id: tel-01327267 https://tel.archives-ouvertes.fr/tel-01327267 Submitted on 6 Jun 2016 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. THÈSE DE DOCTORAT DE L’UNIVERSITÉ PIERRE ET MARIE CURIE Spécialité : Physique École doctorale : «Physique en Île-de-France » réalisée Au Laboratoire de Physique et Mécanique des Milieux Hétérogènes présentée par Suomi PONCE HEREDIA pour obtenir le grade de : DOCTEUR DE L’UNIVERSITÉ PIERRE ET MARIE CURIE Sujet de la thèse : Adhesion of thin structures Frictional peeling and adhesive shells soutenue le 30 Novembre, 2015 devant le jury composé de : M. Etienne Barthel Examinateur M. José Bico Directeur de thèse M. Axel Buguin Examinateur Mme. Liliane Léger Rapporteure M. Benoît Roman Invité M. Loïc Vanel Rapporteur 1 Suomi PONCE HEREDIA 30 Novembre, 2015 Sujet : Adhesion of thin structures Frictional peeling and adhesive shells Résumé : Dans cette thèse, nous nous intéressons à l’adhésion d’élastomères sur des substrats rigides (interactions de van der Waals). -
Monday, July 26
USNCCM16 Technical Program (as of July 27, 2021) To find specific authors, use the search function in the pdf file. All times listed are in Central Daylight Saving Time. Monday, July 26 1 TS 1: MONDAY MORNING, JULY 26 10:00 AM 10:20 AM 10:40 AM 11:00 AM 11:20 AM Symposium Honoring J. Tinsley Oden's Monumental Contributions to Computational #M103 Mechanics, Chair(s): Romesh Batra Keynote presentation: On the Equivalence On the Coupling of Fiber-Reinforced Analysis and Between the Multiplicative Hyper-Elasto-Plasticity Classical and Non- Composites: Interface Application of and the Additive Hypo-Elasto-Plasticity Based on Local Models for Failures, Convergence Peridynamics to the Modified Kinetic Logarithmic Stress Rate Applications in Issues, and Sensitivity Fracture in Solids and Computational Analysis Granular Media Mechanics Jacob Fish*, Yang Jiao Serge Prudhomme*, Maryam Shakiba*, Prashant K Jha*, Patrick Diehl Reza Sepasdar Robert Lipton #M201 Imaging-Based Methods in Computational Medicine, Chair(s): Jessica Zhang Keynote presentation: Image-Based A PDE-Constrained Image-Based Polygonal Cardiac Motion Computational Modeling of Prostate Cancer Optimization Model for Lattices for Mechanical Estimation from Cine Growth to Assist Clinical Decision-Making the Material Transport Modeling of Biological Cardiac MR Images Control in Neurons Materials: 2D Based on Deformable Demonstrations Image Registration and Mesh Warping Guillermo Lorenzo*, Thomas J. R. Hughes, Angran Li*, Yongjie Di Liu, Chao Chen, Brian Wentz, Roshan Alessandro Reali, -
Rheology of Frictional Grains
Rheology of frictional grains Dissertation zur Erlangung des mathematisch-naturwissenschaftlichen Doktorgrades “Doctor rerum naturalium” der Georg-August-Universität Göttingen im Promotionsprogramm ProPhys der Georg-August University School of Science (GAUSS) vorgelegt von Matthias Grob aus Mühlhausen Göttingen, 2016 Betreuungsausschuss: • Prof. Dr. Annette Zippelius, Institut für Theoretische Physik, Georg-August-Universität Göttingen • Dr. Claus Heussinger, Institut für Theoretische Physik, Georg-August-Universität Göttingen Mitglieder der Prüfungskommission: • Referentin: Prof. Dr. Annette Zippelius, Institut für Theoretische Physik, Georg-August-Universität Göttingen • Korreferent: Prof. Dr. Reiner Kree, Institut für Theoretische Physik, Georg-August-Universität Göttingen Weitere Mitglieder der Prüfungskommission: • PD Dr. Timo Aspelmeier, Institut für Mathematische Stochastik, Georg-August-Universität Göttingen • Prof. Dr. Stephan Herminghaus, Dynamik Komplexer Fluide, Max-Planck-Institut für Dynamik und Selbstorganisation • Dr. Claus Heussinger, Institut für Theoretische Physik, Georg-August-Universität Göttingen • Prof. Cynthia A. Volkert, PhD, Institut für Materialphysik, Georg-August-Universität Göttingen Tag der mündlichen Prüfung: 09.08.2016 Zusammenfassung Diese Arbeit behandelt die Beschreibung des Fließens und des Blockierens von granularer Materie. Granulare Materie kann einen Verfestigungsübergang durch- laufen. Dieser wird Jamming genannt und ist maßgeblich durch vorliegende Spannungen sowie die Packungsdichte der Körner, -
Lecture 1: Introduction
Lecture 1: Introduction E. J. Hinch Non-Newtonian fluids occur commonly in our world. These fluids, such as toothpaste, saliva, oils, mud and lava, exhibit a number of behaviors that are different from Newtonian fluids and have a number of additional material properties. In general, these differences arise because the fluid has a microstructure that influences the flow. In section 2, we will present a collection of some of the interesting phenomena arising from flow nonlinearities, the inhibition of stretching, elastic effects and normal stresses. In section 3 we will discuss a variety of devices for measuring material properties, a process known as rheometry. 1 Fluid Mechanical Preliminaries The equations of motion for an incompressible fluid of unit density are (for details and derivation see any text on fluid mechanics, e.g. [1]) @u + (u · r) u = r · S + F (1) @t r · u = 0 (2) where u is the velocity, S is the total stress tensor and F are the body forces. It is customary to divide the total stress into an isotropic part and a deviatoric part as in S = −pI + σ (3) where tr σ = 0. These equations are closed only if we can relate the deviatoric stress to the velocity field (the pressure field satisfies the incompressibility condition). It is common to look for local models where the stress depends only on the local gradients of the flow: σ = σ (E) where E is the rate of strain tensor 1 E = ru + ruT ; (4) 2 the symmetric part of the the velocity gradient tensor. The trace-free requirement on σ and the physical requirement of symmetry σ = σT means that there are only 5 independent components of the deviatoric stress: 3 shear stresses (the off-diagonal elements) and 2 normal stress differences (the diagonal elements constrained to sum to 0). -
Overview of Turbulent Shear Flows
Overview of turbulent shear flows Fabian Waleffe notes by Giulio Mariotti and John Platt revised by FW WHOI GFD Lecture 2 June 21, 2011 A brief review of basic concepts and folklore in shear turbulence. 1 Reynolds decomposition Experimental measurements show that turbulent flows can be decomposed into well-defined averages plus fluctuations, v = v¯ + v0. This is nicely illustrated in the Turbulence film available online at http://web.mit.edu/hml/ncfmf.html that was already mentioned in Lecture 1. In experiments, the average v¯ is often taken to be a time average since it is easier to measure the velocity at the same point for long times, while in theory it is usually an ensemble average | an average over many realizations of the same flow. For numerical simulations and mathematical analysis in simple geometries such as channels and pipes, the average is most easily defined as an average over the homogeneous or periodic directions. Given a velocity field v(x; y; z; t) we define a mean velocity for a shear flow with laminar flow U(y)^x by averaging over the directions (x; z) perpendicular to the shear direction y, 1 Z Lz=2 Z Lx=2 v¯ = lim v(x; y; z; t)dxdz = U(y; t)^x: (1) L ;L !1 x z LxLz −Lz=2 −Lx=2 The mean velocity is in the x direction because of incompressibility and the boundary conditions. In a pipe, the average would be over the streamwise and azimuthal (spanwise) direction and the mean would depend only on the radial distance to the pipe axis, and (possibly) time. -
Rheometry SLIT RHEOMETER
Rheometry SLIT RHEOMETER Figure 1: The Slit Rheometer. L > W h. ∆P Shear Stress σ(y) = y (8-30) L −∆P h Wall Shear Stress σ = −σ(y = h/2) = (8-31) w L 2 NEWTONIAN CASE 6Q Wall Shear Rateγ ˙ = −γ˙ (y = h/2) = (8-32) w h2w σ −∆P h3w Viscosity η = w = (8-33) γ˙ w L 12Q 1 Rheometry SLIT RHEOMETER NON-NEWTONIAN CASE Correction for the real wall shear rate is analogous to the Rabinowitch correction. 6Q 2 + β Wall Shear Rateγ ˙ = (8-34a) w h2w 3 d [log(6Q/h2w)] β = (8-34b) d [log(σw)] σ −∆P h3w Apparent Viscosity η = w = γ˙ w L 4Q(2 + β) NORMAL STRESS DIFFERENCE The normal stress difference N1 can be determined from the exit pressure Pe. dPe N1(γ ˙ w) = Pe + σw (8-45) dσw d(log Pe) N1(γ ˙ w) = Pe 1 + (8-46) d(log σw) These relations were calculated assuming straight parallel streamlines right up to the exit of the die. This assumption is not found to be valid in either experiment or computer simulation. 2 Rheometry SLIT RHEOMETER NORMAL STRESS DIFFERENCE dPe N1(γ ˙ w) = Pe + σw (8-45) dσw d(log Pe) N1(γ ˙ w) = Pe 1 + (8-46) d(log σw) Figure 2: Determination of the Exit Pressure. 3 Rheometry SLIT RHEOMETER NORMAL STRESS DIFFERENCE Figure 3: Comparison of First Normal Stress Difference Values for LDPE from Slit Rheometer Exit Pressure (filled symbols) and Cone&Plate (open symbols). The poor agreement indicates that the more work is needed in order to use exit pressures to measure normal stress differences. -
Guide to Rheological Nomenclature: Measurements in Ceramic Particulate Systems
NfST Nisr National institute of Standards and Technology Technology Administration, U.S. Department of Commerce NIST Special Publication 946 Guide to Rheological Nomenclature: Measurements in Ceramic Particulate Systems Vincent A. Hackley and Chiara F. Ferraris rhe National Institute of Standards and Technology was established in 1988 by Congress to "assist industry in the development of technology . needed to improve product quality, to modernize manufacturing processes, to ensure product reliability . and to facilitate rapid commercialization ... of products based on new scientific discoveries." NIST, originally founded as the National Bureau of Standards in 1901, works to strengthen U.S. industry's competitiveness; advance science and engineering; and improve public health, safety, and the environment. One of the agency's basic functions is to develop, maintain, and retain custody of the national standards of measurement, and provide the means and methods for comparing standards used in science, engineering, manufacturing, commerce, industry, and education with the standards adopted or recognized by the Federal Government. As an agency of the U.S. Commerce Department's Technology Administration, NIST conducts basic and applied research in the physical sciences and engineering, and develops measurement techniques, test methods, standards, and related services. The Institute does generic and precompetitive work on new and advanced technologies. NIST's research facilities are located at Gaithersburg, MD 20899, and at Boulder, CO 80303. -
Vibrating-Wire Rheometry
Western University Scholarship@Western Electronic Thesis and Dissertation Repository 8-20-2018 2:30 PM Vibrating-wire Rheometry Cameron C. Hopkins The University of Western Ontario Supervisor de Bruyn, John R. The University of Western Ontario Graduate Program in Physics A thesis submitted in partial fulfillment of the equirr ements for the degree in Doctor of Philosophy © Cameron C. Hopkins 2018 Follow this and additional works at: https://ir.lib.uwo.ca/etd Part of the Statistical, Nonlinear, and Soft Matter Physics Commons Recommended Citation Hopkins, Cameron C., "Vibrating-wire Rheometry" (2018). Electronic Thesis and Dissertation Repository. 5584. https://ir.lib.uwo.ca/etd/5584 This Dissertation/Thesis is brought to you for free and open access by Scholarship@Western. It has been accepted for inclusion in Electronic Thesis and Dissertation Repository by an authorized administrator of Scholarship@Western. For more information, please contact [email protected]. Abstract This thesis consists of two projects on the behaviour of a novel vibrating-wire rheometer and a third project studying the gelation dynamics of aqueous solutions of Pluronic F127. In the first study, we use COMSOL to perform two-dimensional simulations of the oscillations of a wire in Newtonian and shear-thinning fluids. Our results show that the resonant behaviour of the wire agrees well with the theory of a wire vibrating in Newtonian fluids. In shear-thinning fluids, we find resonant behaviour similar to that in Newtonian fluids. In addition, we find that the shear-rate and viscosity in the fluid vary significantly in both space and time. We find that the resonant behaviour of the wire can be well described by the theory of a wire vibrating in a Newtonian fluid if the viscosity in the theory is set equal to the viscosity averaged over the cir- cumference of the wire and over one period of the wire’s oscillation at the resonant frequency. -
Fluid Mechanics Linear Viscoelasticity
1 Fluid Mechanics Stress Strain Strain rate Shear vs. Extension Apparent Viscosity Oversimplified Models: Maxwell Model Voigt Model Continuity Equation Navier-Stokes Equations Boundary Conditions Volumetric Flow Rate Linear Viscoelasticity Boltzmann Superposition Step Strain: Relaxation Modulus Generalized Maxwell Model Viscosity Creep/Recovery: Creep Compliance Recoverable Compliance Steady State Compliance Terminal Relaxation Time Oscillatory Shear: Storage Modulus Loss Modulus Phase Angle Loss Tangent Time-Temperature Superposition 1 2 Molecular Structure Effects Molecular Models: Rouse Model (Unentangled) Reptation Model (Entangled) Viscosity Recoverable Compliance Diffusion Coefficient Terminal Relaxation Time Terminal Modulus Plateau Modulus Entanglement Molecular Weight Glassy Modulus Transition Zone Apparent Viscosity Polydispersity Effects Branching Effects Die Swell 2 3 Nonlinear Viscoelasticity Stress is an Odd Function of Strain and Strain Rate Viscosity and Normal Stress are Even Functions of Strain and Strain Rate Lodge-Meissner Relation Nonlinear Step Strain Extra Relaxation at Rouse Time Damping Function Steady Shear Apparent Viscosity Power Law Model Cross Model Carreau Model Cox-Merz Empiricism First Normal Stress Coefficient Start-Up and Cessation of Steady Shear Nonlinear Creep and Recovery 3 4 Stress and Strain SHEAR F Shear Stress σ ≡ A l Shear Strain γ ≡ h dγ Shear Rate γ˙ ≡ dt Hooke’s Law σ = Gγ Newton’s Law σ = ηγ˙ EXTENSION F Tensile Stress σ ≡ A ∆l Extensional Strain ε ≡ l dε Extension Rate ε˙ ≡ dt Hooke’s Law σ =3Gε Newton’s Law σ =3ηε˙ 1 5 Viscoelasticity APPARENT VISCOSITY σ η ≡ γ˙ 1.Apparent Viscosity of a Monodisperse Polystyrene. 2 6 Oversimplified Models MAXWELL MODEL Stress Relaxation σ(t)=σ0 exp( t/λ) − G(t)=G0 exp( t/λ) − Creep γ(t)=γ0(1 + t/λ) 0 0 J(t)=Js (1 + t/λ)=Js + t/η 2 G0(ωλ) Oscillatory Shear G (ω)=ωλG”(ω)= 0 1+(ωλ)2 The Maxwell Model is the simplest model of a VISCOELASTIC LIQUID. -
One-Dimensional Differential Newtonian Analysis for Applications in Saliva Rheology
One-dimensional Differential Newtonian Analysis for Applications in Saliva Rheology by Louise Lu McCarroll A dissertation submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy (Mechanical Engineering) in The University of Michigan 2017 Doctoral Committee: Professor William W Schultz, Co-Chair Professor Michael J Solomon, Co-Chair Professor Joseph Bull Dr. Joseph T Murray, Veterans Affairs Hospital Professor Alan S Wineman Louise Lu McCarroll [email protected] ORCID iD: 0000-0003-1471-0655 © Louise Lu McCarroll 2017 For my parents, Yin and Lin Lin ii ACKNOWLEDGEMENTS I think the best phrase that describes this experience for me is \it takes a village" or in my case it should be \it takes a whole metropolitan area and then some." But I'll stick with the \village" analogy for now. The chief villagers I'd like to thank are my advisors, Professor William Schultz and Professor Michael Solomon, for their seemingly unlimited supply of patience with me, especially when I was feeling like the village idiot. Thank you for your guidance these past few years, for teaching me to be resourceful, to a construct logical argument and perform novel analyses, for propping me up when my spirits were low, and last but not least, for being so approachable. I have really enjoyed working on this project with you both. Bill - I am still trying to learn how to \embrace chaos." Mike - I appreciate all the structure you have imposed on this process. I'd also like to extend my gratitude to my committee members, Professor Alan Wineman, Professor Joseph Bull, and Dr. -
Rheometry FLOW in CAPILLARIES, SLITS and DIES DRIVEN by PRESSURE (POISEUILLE DEVICES) CAPILLARY RHEOMETER
Rheometry FLOW IN CAPILLARIES, SLITS AND DIES DRIVEN BY PRESSURE (POISEUILLE DEVICES) CAPILLARY RHEOMETER Figure 1: The Capillary Rheometer. Advantages: (1) Can operate at high shear rates (2) May be closer to real processing situation than a rotational rheometer Disadvantages: (1) Shear rate is not uniform (2) Wall slip (3) Melt fracture (4) Difficult to clean 1 Rheometry CAPILLARY RHEOMETER NEWTONIAN CASE The velocity profile from the Navier-Stokes Equations is: 2Q r 2 v(r) = 1 − (8-9) πR2 R dv Shear Rateγ ˙ = (8-6) dr −4Qr γ˙ (r) = πR4 r γ˙ (r) = γ˙ (R) (8-8) R Wall Shear Rateγ ˙ w ≡ −γ˙ (R) (8-11) 4Q γ˙ = (8-12) w πR3 The shear stress from the Navier-Stokes Equations is: r dP σ(r) = − (8-2) 2 dz R dP σ(R) = − (8-3) 2 dz r σ(r) = σ(R) (8-4) R R dP Wall Shear Stress σ ≡ σ(R) = − (8-5) w 2 dz σ σ (−dP/dz)πR4 Viscosity η = = w = (8-14) γ˙ γ˙ w 8Q 2 Rheometry CAPILLARY RHEOMETER NON-NEWTONIAN CASE 4 σw (−dP/dz)πR Apparent Viscosity ηA = = (8-15) γ˙ A 8Q Since the shear rate varies across the radius of the capillary, a non- Newtonian fluid will have an effective viscosity that depends on radial posi- tion. Figure 2: Dependence of Real Shear Stress σ, Apparent Shear Rateγ ˙ a, and Real Shear Rateγ ˙ on Radial Position for a Non-Newtonian Fluid Flowing in a Capillary. 3 Rheometry CAPILLARY RHEOMETER NON-NEWTONIAN CASE THE RABINOWITCH CORRECTION There is a unique relation between the wall shear stress and the apparent wall shear rate. -
Yield Stress Fluid Flows: a Review of Experimental Data P. Coussot Laboratoire Navier, Univ
Yield stress fluid flows: a review of experimental data P. Coussot Laboratoire Navier, Univ. Paris-Est, Champs-sur-Marne, France Abstract: Yield stress fluids are encountered in a wide range of applications: toothpastes, cement, mortar, foams, muds, mayonnaise, etc. The fundamental character of these fluids is that they are able to flow (i.e. deform indefinitely) only if they are submitted to a stress larger than a critical value, otherwise they deform in a finite way like solids. The flow characteristics of such materials are difficult to predict as they involve permanent or transient solid and liquid regions whose location cannot generally be determined a priori. Here we review the existing knowledge as it appears from experimental data, concerning flows of simple (non-thixotropic) yield stress fluids under various conditions mainly: (i) uniform flows in straight channels or rheometrical geometries, (ii) complex stationary flows in channels of varying cross-section such as extrusion, expansion, flow through porous medium, (iii) transient flows such as flows around obstacles, spreading, spin-coating, squeeze flow, elongation. The effects of surface tension, confinement, and secondary flows are also reviewed. A special emphasis will be laid on the experimental works providing information on the internal flow characteristics which give critical elements for a comparison with numerical predictions. It is in particular shown that (i) the deformations in the solid regime can play a critical role in transient flows; (ii) the yielding character does not play a significant role on the flow field when the boundary conditions impose large deformations; (iii) in secondary flows the yielding character is lost.