Characteristics of Inertial Fibre Suspensions in a Turbulent Pipe Flow Stella Dearing*, Cristian Marchioli, Alfredo Soldati Dipartimento di Energetica.

Slides:



Advertisements
Similar presentations
Using DEM-CFD method to model colloids aggregation and deposition
Advertisements

LARGE-EDDY SIMULATION and LAGRANGIAN TRACKING of a DIFFUSER PRECEDED BY A TURBULENT PIPE Sep 07, 2006 Fabio Sbrizzai a, Roberto Verzicco b and Alfredo.
Measuring Fluid Velocity and Temperature in DSMC Alejandro L. Garcia Lawrence Berkeley National Lab. & San Jose State University Collaborators: J. Bell,
Master’s Dissertation Defense Carlos M. Teixeira Supervisors: Prof. José Carlos Lopes Eng. Matthieu Rolland Direct Numerical Simulation of Fixed-Bed Reactors:
Fluid flow and species transport around a scaffold Centro Interdipartimentale di Fluidodinamica e Idraulica & Department of Energy & Technology, University.
Head loss and velocity profiles Martine RUEFF FP1005 Cost Meeting October 2011 Laboratoire de génie des procédés papetiers Grenoble INP - Pagora.
Fibre suspension flow modelling A key for innovation and competitiveness in the pulp & paper industry FP1005 Start date: 11/05/2011 End date: 10/05/2015.
The effect of raindrop impacted flow on sediment composition.
Introduction to Particle Image Velocimetry (PIV)
Active and hibernating turbulence in channel flow of Newtonian and viscoelastic fluids Li Xi and Michael D. Graham University of Wisconsin-Madison Turbulent.
High-speed holographic measurements of fiber trajectories and orientation in near homogeneous, isotropic turbulence Technion - Israel Institute of Technology.
PTS research activities related to COST FP 1005 Simulation of micro structure mechanics in dynamic fibre networks Timo Kuntzsch, Jan Matheas, Sven Altmann.
Masato Hirota MRI Measurements of Fibre- Suspension Flow in a Sudden Contraction/Expansion FP1005 & SIG43 Workshop NTNU, Trondheim October 2012.
MAE513 Spring 2001 Prof. Hui Meng & Dr. David Song Dept. of Mechanical & Aerospace Engineering Advanced Diagnostics for Thermo- Fluids Laser Flow Diagnostics.
DIAMOND Decommissioning, Immobilisation and Management of Nuclear Wastes for Disposal Physical Modelling of Impinging Jets to aid Nuclear Sludge bed resuspension.
Measuring segregation of inertial particles in turbulent flows by a Full Lagrangian approach E. Meneguz Ph.D. project: Rain in a box of turbulence Supervisor:
PFI, Trondheim, October 24-26, Department of Energy and Process Engineering, NTNU 2 Centro Interdipartimentale di Fluidodinamica e Idraulica, University.
Orientation and distribution of highly elongated and inertial fibres in turbulent flow: a comparison of experimental and numerical data Stella Dearing,
Granular flows under the shear Hisao Hayakawa* & Kuniyasu Saitoh Dept. Phys. Kyoto Univ., JAPAN *
Inertial Confinement Fusion Related Experimental Investigation of a Twice-Shocked Spherical Density Inhomogeneity. Nick Haehn, Chris Weber, Jason Oakley,
Fluid Friction. Outline Bernoulli ’ s Equation The Pressure-Drop Experiment Laminar Flow Turbulent Flow The Three Friction Factor Problems Computer Methods.
1 Lecture #5 of 25 Moment of inertia Retarding forces Stokes Law (viscous drag) Newton’s Law (inertial drag) Reynolds number Plausibility of Stokes law.
Particle Image Velocimeter
Spectra of Gravity Wave Turbulence in a Laboratory Flume S Lukaschuk 1, P Denissenko 1, S Nazarenko 2 1 Fluid Dynamics Laboratory, University of Hull 2.
Suspended Load Above certain critical shear stress conditions, sediment particles are maintained in suspension by the exchange of momentum from the fluid.
1 A combined RANS-LES strategy with arbitrary interface location for near-wall flows Michael Leschziner and Lionel Temmerman Imperial College London.
CHEMICAL REACTION ENGINEERING LABORATORY Characterization of Flow Patterns in Stirred Tank Reactors (STR) Aravind R. Rammohan Chemical Reaction Engineering.
Generation of squeezed states using radiation pressure effects David Ottaway – for Nergis Mavalvala Australia-Italy Workshop October 2005.
Tesi di Laurea Break-up of inertial aggregates in turbulent channel flow Frammentazione di aggregati inerziali in flusso turbolento Relatore: Dott. Ing.
2 nd UK-JAPAN Bilateral and 1 st ERCOFTAC Workshop, Imperial College London.
BREAK-UP OF AGGREGATES IN TURBULENT CHANNEL FLOW 1 Università degli Studi di Udine Centro Interdipartimentale di Fluidodinamica e Idraulica 2 Università.
Volumetric 3-Component Velocimetry (V3V)
Active Flow Control Using Transverse Travelling Waves Speaker: Aki Pakarinen Imperial College.
Characteristics of Fibre Suspensions in a Turbulent Pipe Flow Stella Dearing*, Cristian Marchioli, Alfredo Soldati Dipartimento di Energetica e Macchine,
September, 18-27, 2006, Leiden, The Nederlands Influence of Gravity and Lift on Particle Velocity Statistics and Deposition Rates in Turbulent Upward/Downward.
Pentti Saarenrinne 13th Oct 2011 Experimental fluid dynamics at Department of the Energy and Process Engineering, Tampere University of Technology.
Mechanistic Modeling and CFD Simulations of Oil-Water Dispersions in Separation Components Mechanistic Modeling and CFD Simulations of Oil-Water Dispersions.
Modelling of the particle suspension in turbulent pipe flow
Experimental Study of Mixing at the External Boundary of a Submerged Turbulent Jet A. Eidelman, T. Elperin, N.Kleeorin, G.Hazak, I.Rogachevskii, S.Rudykh,
Statistical Fluctuations of Two-dimensional Turbulence Mike Rivera and Yonggun Jun Department of Physics & Astronomy University of Pittsburgh.
Magnetic Particle Tracking in Spouting and Bubbling Fluidized Beds Jack Halow Separation Design Group Stuart Daw Oak Ridge National Laboratory Presented.
MHD Department Institute of Safety Research 2 nd Sino-German Workshop on EPM (Dresden) Experimental studies of bubble-driven liquid metal flows in a static.
Experimental investigations on secondary structures in a fully developed turbulent jet and extension to fibre-laden case Alessandro Capone, Alfredo Soldati.
Influence of wall roughness on near wall turbulence structure by Haigermoser C.*, Vesely L.*, La Polla M., Onorato M., Politecnico di Torino XIV A.I.VE.LA.
1 LES of Turbulent Flows: Lecture 16 (ME EN ) Prof. Rob Stoll Department of Mechanical Engineering University of Utah Fall 2014.
Department of Aerospace Engineering and Mechanics, Hydrodynamic surface interactions of Escherichia coli at high concentration Harsh Agarwal, Jian Sheng.
Turbulence effects on particle dispersion in a free-surface flow
Simulations of inertial point-particles at NTNU
I m going to talk about my work in last 2 years
IESVic 1 QUANTITATIVE IMAGING OF MULTI-COMPONENT TURBULENT JETS Arash Ash Supervisors: Dr. Djilali Dr. Oshkai Institute for Integrated Energy Systems University.
CFD Modelling of the Flow Inside an LC Refiner COST FP1005 / SIG 43 meeting, X.2012, Trondheim 1 CFD Modelling of the Flow Inside an LC Refiner Dariusz.
STABLY STRATIFIED SHEAR-PRODUCED TURBULENCE AND LARGE-SCALE-WAVES IN A LID DRIVEN CAVITY BEN-GURION UNIVERSITY OF THE NEGEV FACULTY OF ENGINEERING SCIENCES.
Sheared stably stratified turbulence and
Status of Modeling of Damage Effects on Final Optics Mirror Performance T.K. Mau, M.S. Tillack Center for Energy Research Fusion Energy Division University.
Dynamics of Particulate Systems
Chapter 3. Instability of the free plane and near – wall plane jet
CFD Lab 1 Simulation of Turbulent Pipe Flow Seong Mo Yeon, Timur Dogan, and Michael Conger 10/07/2015.
ERMSAR 2012, Cologne, Germany, March 21 – 23, 2012 Aerosol Retention in Containment Leak Paths: Indications for a Code Model in the Light of COLIMA Experimental.
Lavezzo V., Soldati A. Università degli studi di Udine Centro Interdipartimentale di Fluidodinamica e Idraulica and Dipartimento di Energetica e Macchine.
Brookhaven Science Associates U.S. Department of Energy MUTAC Review April , 2004, BNL Target Simulations Roman Samulyak in collaboration with Y.
Behavior of the boundary layer vorticity field as the Reynolds number gets large Joe Klewicki Department of Mechanical Engineering University of New Hampshire.
Presented to: International Aircraft Materials Fire Test Working Group By: Robert Ochs Date: Wednesday, October 21, 2009 Federal Aviation Administration.
Formation of Near-Wall Particle-Streaks in Particle-Laden Wall-Bounded Turbulent Flows Luís M. Portela and Valérie Ferrand Kramers Laboratory Delft University.
Gravity Wave Turbulence in Wave Tanks S Lukaschuk 1, S Nazarenko 2 1 Fluid Dynamics Laboratory, University of Hull 2 Mathematics Institute, University.
Sibley School of Mechanical and Aerospace Engineering
Particles turbulence interactions in boundary layers
Particle (s) motion.
Experimental Characterization of Gas-Liquid Column:
Global Warming Problem
Date of download: 11/30/2018 Copyright © ASME. All rights reserved.
Presentation transcript:

Characteristics of Inertial Fibre Suspensions in a Turbulent Pipe Flow Stella Dearing*, Cristian Marchioli, Alfredo Soldati Dipartimento di Energetica e Macchine, Università di Udine, Italy 1 3rd SIG43 Workshop: Udine, Italy, rd SIG43 Workshop: Dynamics of non-spherical particles in fluid turbulence, Udine, Italy, April 6th - 8th, 2011

Applications: Which industries benefit Inertial fibres suspended in turbulent flows are commonly encountered industry 2 Pulp and paper processing Controlling rheological behaviour and fibre orientation distribution crucial to optimise operations Furniture Industry Pneumatic transport of fibres Fibres as an alternative to polymers as a DRA? Examples include the TAPs, medical application, firehouse Fibres provide more modest reductions but improved shear degradation and filterability Nappy Fabrication Fluff, cellulose fibres, make up 60% of nappy material. Uniform distribution is highly desirable for increased absorption Experimental data is required to validate simulation assumptions, develop and improve current models, provide industry with practical correlations for sizing of industry equipment (aim not to oversize) 3rd SIG43 Workshop: Udine, Italy, 2011

Motivation: Why Study? 3 Fibre suspensions have complicated rheological properties that are quite different than carrier fluid even at low mass fractions. The physical properties f(fibre spatial distribution & orientation) 1.Fibres rotate/align when subject to velocity gradient – hydrodynamic drag of fibres is f(rotational motion)  controls translational motion 2.Strong turbulence tends to randomise orientation (BERNSTEIN &SHAPIRO) 3.BUT coherent structures  interact with fibres causing segregation and accumulation ( MARCHIOLI et al. PHYS. FLUIDS ) y z 3rd SIG43 Workshop: Udine, Italy, 2011 DNS  one way coupling  no fibre-fibre interactions  Re τ =150; Re = 9000  Benchmarking required!

Set-up: Pipe Circuit measurements 4 Pipe length9m31m Pipe materialglassGalvanised steel Pipe diameter ϕ / 0.022m0.1m Re6,000-20,00025, ,000 3rd SIG43 Workshop: Udine, Italy, 2011 Laser Camera z x Mirror ND Yag laser 1000mJ PCO sensicam 1280 x1024 F = 8hz x z Flow Direction ϕ /7 ϕ /5

Experimental Parameters Fibre typeMass fraction, ϕ, % nL 3 Nylon AdditiveLengthDiameterSpecific Density Nylon~0.3mm24 μm rd SIG43 Workshop: Udine, Italy, 2011 Frequency, %

Software development: Phase Discrimination 6 Adjust intensity Dilate Remove noise Erode to orig. size 3rd SIG43 Workshop: Udine, Italy, 2011 zizi Mean orientations Normalised number density 1.Preprocessing 2. Object Identification 3. Discriminate object type based on length & aspect ratio 4.Ellipse fitting 5.Calculate statistics 1.Preprocessing 2. Object Identification 3. Discriminate object type based on length & aspect ratio 4.Ellipse fitting 5.Calculate statistics

Software development: Statistics calculation and validation 7 3rd SIG43 Workshop: Udine, Italy, 2011 Results  mean orientation Green triangles  DNS data (Marchioli et al., 2010) at Re = 9000, Red squares  experimental data Re = 8043 Artificial images Projected fibre onto plane  random distribution tends to 0.64 vs 0.5

Results: Mean orientations 8  Fibres strongly align to the streamwise direction close to wall  Alignment decreases with distance from wall but does not become completely random  Alignment reduction increases with Re for mass fraction of 0.01%  Alignment reductions tends to same value for all Re at mass fraction of 0.02%. 3rd SIG43 Workshop: Udine, Italy, 2011 DNS Re τ =150; Re = 9000

Results: Normalised mean number density 9  Near wall peak; reduction away from wall  Less fibres at near wall cf at higher Re cf to Re=8043  At 0.02% less fibres close to wall, increase in fibres away from wall 3rd SIG43 Workshop: Udine, Italy, 2011 DNS Re τ =150; Re = 9000 Re = 8043

Conclusions 10 Phase discrimination technique and validation has been presented. – Limitations and errors have been quantified. –Phase discrimination technique is appears suitable for the problem ( 3D set-up) First set of experimental data of orientation/distribution close to wall Mean orientation and number density data qualitatively agrees with DNS data  promising. High Re number tests: sensitive to concentrations. –Deposition at higher Re tests. Why? More information required Information on decomposed velocity flow field is required. Study for instantaneous images with high frequency camera We are in the process of doing error analysis of phase discrimination PIV algorithm using a DNS flow field 3rd SIG43 Workshop: Udine, Italy, 2011