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School of something

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School of something FACULTY OF OTHER School of Mechanical Engineering FACULTY OF ENGINEERING Flow Simulation for Improved Engineering Design Dr Harvey Thompson – PowerPoint PPT presentation

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Title: School of something


1
School of something FACULTY OF OTHER
School of Mechanical Engineering FACULTY OF
ENGINEERING
Flow Simulation for Improved Engineering
Design Dr Harvey Thompson Institute of
Engineering Thermofluids, Surfaces Interfaces
(iETSI) (With particular thanks to Dr Nik
Kapur, Dr Jon Summers, Dr Mark Wilson, Dr Sergii
Veremieiev, Dr Yeawchu Lee, Prof. Phil Gaskell)
2
Summary
School of something FACULTY OF OTHER
  • Applications of Computational Fluid Dynamics
    (CFD) Design and Analysis in Free Surface Film
    Flows
  • 2D Simulations Industrial Coating
  • 3D Simulations Flows over real surfaces
  • Bio-pesticide
    application methods

3
2D Simulations Industrial Coating Flows
Slot Coating
  • Several different precision coating processes
  • produce a range of important products,
  • including
  • Polymer films and packaging materials
  • Ink-jet printing and imaging media
  • Large Area Printed Electronic Devices
  • etc...

Roll Coating
4
2D Simulations Industrial Coating Flows
Key Problem for Coating Engineers avoid
formation of streak-lines which destroy product
quality caused by eddies in the flow
Coating web direction
Thin streak-line destroys product quality
5
2D Simulations Industrial Coating Flows
  • Industrial Coating Flows Difficult to Simulate
  • (even in 2D!)
  • Surface-tension dominated, free surface flows
  • Static and dynamic wetting lines where
  • coating is formed
  • Highly curved flow domains
  • Finite Element (FE) Methods suitable
  • for such problems

6
2D Simulations Industrial Coating Flows
Avoidance of Streak-lines (1) Classic Moffatt
1964 JFM paper strong effect of static contact
line on eddy size and strength Increase static
angle to reduce streak-lines Practical solution
coat cascade surface with PTFE reduced product
wastage by 4M over three years!
7
2D Simulations Industrial Coating Flows
Avoidance of Streak-lines (2) Slot exit
flow. Slot exits often used to supply pre-metered
coatings such as slide and curtain
8
2D Simulations Industrial Coating Flows
Avoidance of Streak-lines (2) Slot exit
flow. Back-wetting of uppermost slot may occur
during start-up can lead to defect-causing
solids deposits due to degradation in
recirculation regions. Back wetting at the upper
slot (a) experimental, (b) CFD prediction
9
2D Simulations Industrial Coating Flows
Avoidance of Streak-lines (2) Slot exit
flow Merging flow out of slot exits effect of
chamfering lower corner Chamfer can remove
eddies in both liquid layers simultaneously!
10
2D Simulations Industrial Coating Flows
Stirring and Mass Transfer in Continuously
Modulated Forward Roll Coating, M.C.T. Wilson et
al, JFM, 2006.
11
2D Simulations Industrial Coating Flows
Tracer particle trajectories Runge-Kutta
scheme trigonometric interpolation of nodal and
spinal data allows evaluation of u,v at arbitrary
t
12
2D Simulations Industrial Coating Flows
Stirring and Mass Transfer in Continuously
Modulated Forward Roll Coating, M.C.T. Wilson et
al, JFM, 2006. Enables residence times and
effects of time-dependent forcing to be analysed,
e.g. Roll eccentricity or variable roll speeds.
Experiment
CFD
13
3-D Film and Droplet Flows over Topography
Several important practical applications e.g.
film flow in the eye, electronics cooling, heat
exchangers, combustion chambers, etc... Focus
on precision coating of micro-scale displays
and sensors, Tourovskaia et al, Nature
Protocols, 3, 2006. Pesticide flow over
leaves, Glass et al, Pest Management Science,
2010.
Plant disease control
14
3D Film Flow over Topography
For displays and sensors, coat liquid layers over
functional topography light-emitting species on
a screen Key goal ensure surfaces are as planar
as possible ensures product quality and
functionality BUT free surface disturbances are
persistent!
Stillwagon, Larson and Taylor, J. Electrochem.
Soc. 1987
15
3D Film Flow over Topography
  • Key Modelling Challenges
  • 3-D surface tension dominated free surface flows
    are very complex Commercial CFD codes are
    limited and Navier-Stokes solvers at early stage
    of development (see later)
  • Surface topography often very small (100s nm)
    but influential need highly resolved grids?
  • No universal wetting models exist
  • Large computational problems adaptive
    multigrid, parallel computing?
  • Very little experimental data for realistic 3D
    flows.

16
3D Film Flow over Topography
Finite Element methods not as well-established
for 3-D free surface flow. Promising alternatives
include Level-Set, Volume of Fluid (VoF), Lattice
Boltzmann etc but still issues for 3D surface
tension dominated flows grid resolution
etc... Fortunately thin film lubrication low
assumptions often valid provided eH0/L0 ltlt1 and
capillary number Caltlt1 Enables 3D flow to be
modelled by 2D systems of pdes.
gravity
H0
inflow
y
s(x,y)
h(x,y)
L0
x
outflow
a
17
3D Film Flow over Topography
Decre Baret, JFM, 2003 Flow of Water Film over
a Trench Topography
Comparison between experimental free surface
profiles and those predicted by solution of the
full Navier-Stokes and Lubrication
equations. Agreement is very good Lubrication
theory is accurate for thin film flows with small
topography and inertia. Unfortunately not always
the case!
18
3D Film Flow over Topography
Thin Film Flows with Significant Inertia Free
surfaces can be strongly influenced by inertia
e.g. free surface instability, droplet
coalescence,... standard lubrication theory can
be extended to account for significant inertia
Depth Averaged Formulation of Veremieiev et al,
Computer Fluids, 2010. Film Flows of Arbitrary
Thickness over Arbitrary Topography Need full
numerical solutions of 3D Navier-Stokes
equations!
19
Depth-Averaged Formulation for Inertial Film Flows
  1. Reduction of the Navier-Stokes equations by the
    long-wave approximation

Restrictions
2. Depth-averaging stage to decrease
dimensionality of unknown functions by one

,

Restrictions no internal recirculations
3. Assumption of Nusselt velocity profile to
estimate unknown friction and dispersion terms
20
Depth-Averaged Formulation for Inertial Film Flows
DAF system of equations
For Re 0 DAF LUB
  • Boundary conditions
  • Inflow b.c.
  • Outflow (fully developed flow)

21
Flow over 3D trench Effect of Inertia
Gravity-driven flow of thin water film 130µm
H0 275µm over trench topography sides 1.2mm,
depth 25µm
surge
bow wave
comet tail
22
Accuracy of DAF approach
Gravity-driven flow of thin water film 130µm
H0 275µm over 2D step-down topography sides
1.2mm Max Error vs
Navier-Stokes (FE)
Error 1-2 for Re50 and s0 0.2
s0step size/H0
23
Free Surface Planarisation
  • Noted above many manufactured products require
    free surface disturbances to be minimised
    planarisation
  • Very difficult since comet-tail disturbances
    persist over length scales much larger than the
    source of disturbances
  • Possible methods for achieving planarisation
    include
  • thermal heating of the substrate, Gramlich et al
    (2002)
  • use of electric fields

24
Electrified Film Flow
  • Gravity-driven, 3D Electrified film flow over a
    trench topography
  • Assumptions
  • Liquid is a perfect conductor
  • Air above liquid is a perfect dielectric
  • Film flow modelled by Depth Averaged Form
  • Fourier series separable solution of Laplaces
    equation
  • for electric potential above the film is coupled
    to film flow
  • by Maxwell free surface stresses.

25
Electrified Film Flow
  • Effect of Electric Field Strength on Film Free
    Surface
  • No Electric Field
    With Electric Field
  • Note Maxwell stresses can planarise the
    persistent, comet-tail disturbances very
    effectively.

26
Computational Issues
  • Real and functional surfaces are often extremely
    complex.

Multiply-connected circuit topography
Lee, Thompson and Gaskell, International Journal
for Numerical Methods in Fluids, 2008
Need highly resolved grids for 3D flows
Flow over a maple leaf topography
Glass et al, Pest Management Science, 2010
27
Adaptive Multigrid Methods
  • Full Approximation Storage (FAS) Multigrid
    methods very efficient.
  • Spatial and temporal adaptivity enables fine
    grids to be used only where they are needed.
  • E.g. Film flow over a substrate with isolated
    square, circular and diamond-shaped topographies
  • Free Surface
    Plan View of Adaptive Grid

28
Parallel Multigrid Methods
  • Parallel Implementation of Temporally Adaptive
    Algorithm using
  • Message Passing Interface (MPI)
  • Geometric Grid Partitioning
  • Combination of Multigrid O(N) efficiency and
    parallel speed up very powerful!
  • BUT Parallelisation of spatially adaptive
    algorithm very challenging!

29
3D FE Navier-Stokes Solutions
Remember Lubrication and Depth Averaged
Formulations invalid for flow over arbitrary
topography and unable to predict recirculating
flow regions As seen earlier important to
predict eddies in many applications E.g. In
industrial coating
30
3D FE Navier-Stokes Solutions
Mixing phenomena E.g. Heat transfer enhancement
due to thermal mixing, Scholle et al, Int. J.
Heat Fluid Flow, 2009.
31
3D FE Navier-Stokes Solutions
  • Commercial CFD codes still rather limited for
    these type of problems
  • Finite Element methods are still the most
    accurate for surface tension dominated free
    surface flows grids based on Arbitrary
    Lagrangian Eulerian Spine methods
  • Spine Method for 2D Flow
    Generalisation to 3D flow

32
3D FE Navier-Stokes vs DAF Solutions
Gravity-driven flow of a water film over a trench
topography comparison between free surface
predictions
33
3D FE Navier-Stokes Solutions
  • Gravity-driven flow of a water film over a trench
    topography particle trajectories in the trench
  • 3D FE solutions can predict how fluid residence
    times and volumes of
  • fluid trapped in the trench depend
    on trench dimensions
  • Will be extended to analyse thermal mixing in
    3D flows

34
Droplet Flows Bio-pesticides
  • Droplet Flow Modelling and Analysis

35
Application of Bio-pesticides
Changing EU legislation is limiting use of
chemically active pesticides for pest control in
crops. Bio-pesticides using living organisms
(nematodes, bacteria etc...) to kill pests are
increasing in popularity but little is known
about pesticide motion over leaves Working with
Food Environment Research Agency in York and
Becker Underwood Ltd to understand the dominant
flow mechanisms
36
Nematodes
  • Nematodes are a popular bio-pesticide control
  • method - natural organisms present in soil
  • typically up to 500 microns in length.
  • Aggressive organisms that attack the pest by
    entering body openings
  • Release bacteria that stops pest feeding kills
    the pest quickly
  • Mixed with water and adjuvants and sprayed onto
    leaves

37
What do we want to understand?
  • Why do adjuvants improve effectiveness reduced
  • evaporation rate?
  • How do nematodes affect droplet size
    distribution?
  • How can we model flow over leaves?
  • How does impact speed, droplet size and
    orientation affect droplet motion?

38
Droplet spray evaporation time effect of adjuvant
Size of droplets Concentration () Initial mass (mg) Mass fraction left after 10 min () Evaporation time (min)
large 0 130.3 36.3 26.3
large 0.01 138.0 36.6 24.0
large 0.1 161.0 48.7 36.0
small 0 87.3 13.3 16.3
small 0.01 92.5 9.7 16.0
small 0.1 138.3 33.3 25.7
39
Droplet size distribution for bio-pesticides
Teejet XR110 05 nozzle with 0.8bar
Matabi 12Ltr Elegance18 knapsack sprayer
Malvern Spraytec Laser Diffraction System
40
VMD of the bio-pesticide spray depending on the
concentration of adjuvant
addition of bio-pesticide does not affect Volume
Mean Diameter of the spray
Substance Dv50 (µm) Dv50 (µm) Dv50 (µm) Dv50 (µm) Dv50 (µm)
Substance c 0 c 0.01 c 0.03 c 0.1 c 0.3
wateradjuvant 273.3 275.1 269.4 330.5 352.9
watercarrier material 285.9 276.1 297.3 329.2 360.8
watercommercial product (biopesticide) 271.0 272.8 282.6 307.5 360.6
41
Droplet flow over a leaf simple theory
2nd Newtons law in x direction
theoretical expressions from Dussan (1985)
Stokes drag
Contact angle hysteresis
Velocity
Relaxation time
Terminal velocity
Volume of smallest droplet that can move
42
Droplet flow over a leaf simple theory vs.
experiments



47V10 silicon oil drops flowing over a
fluoro-polymer FC725 surface


Dussan (1985) theory
Podgorski, Flesselles, Limat (2001) experiments
Linearity of graph gt droplet flow is governed by
this law (until pearling!)
Le Grand, Daerr Limat (2005), experiments
43
Droplet flow over a leaf (?60º) effect of
inertia
For V10mm3, R1.3mm, terminal
velocity0.22m/s Lubrication theory
Depth averaged formulation
44
Droplet flow over a leaf (?60º) effect of
inertia
For V20mm3 R1.7mm terminal velocity0.45m/s Lu
brication theory Depth
averaged formulation
45
Droplet flow over a leaf (?60º) summary of
computations
Grid density has a big influence on accuracy of
predictions need at least 512x512 nodes Koh et
al, Eur. Phys. J., 166, 2009 4millionx4million!
V, mm3 R, mm Bosin? Ca a, m/s Ca a, m/s Ca a, m/s
V, mm3 R, mm Bosin? Experiment Experiment Computation Re0 Computation Re0 Computation Re10 Computation Re10
0.27 0.4 0.06 0 0 0.0003 0.02 0.0001 0.007
10 1.3 0.62 0.003 0.13 0.005 0.21 0.005 0.22
20 1.7 0.99 0.006 0.24 0.010 0.42 0.009 0.40
30 1.9 1.30 0.008 0.33 0.012 0.54 0.011 0.48
40 2.1 1.57 0.011 0.48 0.014 0.62 0.012 0.55
46
Droplet flow over a leaf theory shows small
effect of initial velocity
Velocity
Initial velocity
Relaxation time
47
Droplet flow over a leaf computation of
influence of initial condition
V10mm3 R1.3mm a0.22m/s Bosin?0.61 v00.69m/s B
osin? init 1.57
V10mm3 R1.3mm a0.22m/s Bosin?0.61 v01.04m/s B
osin? init 2.49
this is due to the relaxation of the droplets
shape
48
Droplet flow over (?60º) vs. under (?120º) a
leaf computation
V20mm3 R1.7mm a0.45m/s Bosin?0.99 ?60º
V20mm3 R1.7mm a0.45m/s Bosin?0.99 ?120º
49
Bio-pesticides initial conclusions
  • Addition of carrier material or commercial
    product (bio-pesticide) does not affect the
    Volume Mean Diameter of the spray.
  • Dynamics of the droplet over a leaf are governed
    by gravity, Stokes drag and contact angle
    hysteresis these are verified by experiments.
  • Droplets shape can be adequately predicted by
    lubrication theory, while inertia and initial
    condition have minor effect.
  • Simulating realistically small bio-pesticide
    droplets is extremely computationally intensive
    efficient parallelisation is needed ( see e.g.
    Lee et al (2011), Advances in Engineering
    Software) BUT probably does not add much extra
    physical understanding!

50
General Conclusions
  • Free surface film and droplet flows are
    everywhere! Lots of important industrial
    applications.
  • They are very difficult to model surface
    tension-dominated, complex geometry and governing
    physics. Commercial CFD still quite primitive.
  • Simplifications such as lubrication theory can be
    very useful but must be careful about validity.
    Methods for 3D Navier-Stokes beginning to emerge.
  • Simulating realistic 3D flows requires highly
    efficient numerical methods and access to High
    Performance Computing
  • Finally desperate need to more experimental data!
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