j.e. sprittles (university of oxford, u.k.) y.d. shikhmurzaev(university of birmingham, u.k.)...
TRANSCRIPT
J.E. Sprittles (University of Oxford, U.K.)Y.D. Shikhmurzaev (University of Birmingham, U.K.)
Workshop on the Micromechanics of Wetting & Coalescence
Microfluidic TechnologiesOften the key elements are the interaction of:
Drops with a solid - Dynamic WettingDrops with other drops - Coalescence
Dynamic Wetting Phenomena
50nm Channels27mm Radius Tube
1 Million Orders of Magnitude!
Millimetrescale
Microfluidics Nanofluidics
Emerging technologies
Routine experimental measurement
Microdrop Impact Simulations
?
25m water drop impacting at 5m/s. Experiments: Dong et al 06
Coalescence of Liquid DropsHemispheres easier to control
experimentally
Thoroddsen et al 2005Ultra high-speed imaging
Paulsen et al 2011Sub-optical electrical (allowing microfluidic measurements)
r
Thoroddsen et al 2005
A Typical Experiment230cP water-glycerol mixture:
Length scale is chosen to be the radius of dropTime scale is set from so that
Electrical: Paulsen et al, 2011. Optical:Thoroddsen et al, 2005.
(mm)L R O
/U / (ms)T R O
CoalescenceFrenkel 45
Solution for 2D viscous drops using conformal mapping Hopper 84,90,93 & Richardson 92
Scaling laws for viscous-dominated flowEggers et al 99 (shows equivalence of 2D and 3D)
Scaling laws for inertia-dominated flowDuchemin et al 03 (toroidal bubbles, Oguz & Prosperetti 89)
Problem FormulationTwo identical drops coalesce in a dynamically
passive inviscid gas in zero-gravity.
Conventional model has:A smooth free surfaceAn impermeable zero tangential-stress
plane of symmetry
Analogous to wetting a geometric surface with:The equilibrium angle is ninety degreesInfinite ‘slip length’.
90d
d e
Problem Formulation
n P (I nn) = 0
u n = 0
u 0, n P (I nn) = 0, n P n = nf
ft
n P (I nn) = u (I nn)
u n = 0
Bulk
Free Surface
Liquid-Solid Interface Plane of Symmetry
uu 0, u u P, P = - I + u + u
Tp
t
d e 90d
( )r t
( )h t
( )d t
2( )h O r
3( )d O r
Bridge radius:
Undisturbed free surface:
Longitudinal radius of curvature:
( )r t
Conventional Model’s Characteristics
Initial cusp is instantaneously smoothed
dim dim dimln ,visc
r t t RC T
R T T
( )r t
( )h t
( )d t
ln ,viscr C t t
Surface tension driving force when resisted by viscous forces gives (Eggers et al 99):
Conventional Model’s Characteristics
/ ( )d t
0dr
u as tdt
( )r t
( )h t
( )d t
1/2 1/23dim dim ,inert inert
inert
r t RC T
R T
Assumed valid while after which (Eggers et al 99):
2Re / 1r r
Test scaling laws by fitting to experimentsNo guarantee this is the solution to the conventional model
Traditional Use of Scaling Laws
ln
1visc
visc
r C t t
C
ln
0.1visc
visc
r C t t
C
ln
0.2visc
visc
r C t t
C
Computational WorksProblem demands resolution over at least 9 orders of
magnitude.
The result been the study of simplified problems:The local problem – often using the boundary integral method for
Stokes flow (e.g. Eggers et al 99) or inviscid flow.
The global problem - bypassing the details of the initial stages
Our aim is to resolve all scales so that we can:Directly compare models’ predictions to experimentsValidate proposed scaling laws
JES & YDS 2011, Viscous Flows in Domains with Corners, CMAMEJES & YDS 2012, Finite Element Framework for Simulating Dynamic Wetting Flows, Int. J. Num. Meth Fluids.JES & YDS, 2012, The Dynamics of Liquid Drops and their Interaction with Surfaces of Varying Wettabilities, Phy. Fluids.JES & YDS, 2013, Finite Element Simulation of Dynamic Wetting Flows as an Interface Formation Process, J. Comp. Phy.
Resolving Multiscale Phenomena
Arbitrary Lagrangian Eulerian MeshBased on the ‘spine method’ of Scriven and co-workers
Coalescence simulation for 230cP liquid at t=0.01, 0.1, 1.
Microdrop impact and spreading simulation.
Benchmark Simulations‘Benchmark’ code against simulations in Paulsen et al 12 for
identical spheres coalescing in zero-gravity withRadiusDensitySurface tensionViscosities
Giving two limits of Re to investigate:
Hence establish validity of scaling laws for the conventional model
3
1
1mm
970kg m
20mN m
1mPa s & 58000mPa s
R
4 6Re 1.9 10 & 5.8 10
High Viscosity Drops ( )6Re 5.8 10
High Viscosity Drops: BenchmarkingInfluence of minimum radius lasts for time mint O r
Paulsen et al 12
High Viscosity Drops: Scaling Laws
Eggers et al 99
r=3.5t
ln
0.2visc
visc
r C t t
C
Not linear growth
Low Viscosity Drops ( ) 4Re 1.9 10
Low Viscosity Drops: Toroidal Bubbles
Toroidal bubble
As predicted in Oguz & Prosperetti 89 and Duchemin et al 03
Increasing time
Low Viscosity Drops: Benchmarking
Paulsen et al 12
Eggers et al 99
Duchemin et al 03
Low Viscosity Drops: BenchmarkingCrossover atActually nearer
4Re Re 1 10r r r 2 2Re Re 1 10h r r
3
1
4
2mm
1200kg m
65mN m
3.3mPa s , 48mPa s & 230mPa s
Re = 1.4 10 , 68 & 2.9
R
Hemispheres of water-glycerol mixture with:
Qualitative Comparison to Experiment
Coalescence of 2mm radius water drops.
Simulation assumes symmetry about z=0
Experimental images courtesy of Dr J.D. Paulsen
Quantitative Comparison to Experiment
3.3mPas48mPas230mPas
Conventional Modelling: Key PointsAccuracy of simulations is confirmed
Scaling laws approximate conventional model well
Conventional model doesn’t describe experiments
YDS 1993, The moving contact line on a smooth solid surface, Int. J. Mult. Flow
YDS 2007, Capillary flows with forming interfaces, Chapman & Hall.
Interface Formation in Dynamic Wetting
Make a dry solid wet.
Create a new/fresh liquid-solid interface.
Class of flows with forming interfaces.
Forminginterface
Formed interface
Liquid-solidLiquid-solidinterfaceinterface
SolidSolid
Relevance of the Young Equation
U
1 3 2cose e e e 1 3 2cos d
R
σ1e
σ3e - σ2e
Dynamic contact angle results from dynamic surface tensions.
The angle is now determined by the flow field.
Slip created by surface tension gradients (Marangoni effect)
θe θd
Static situation Dynamic wetting
σ1
σ3 - σ2
R
Free surface pressed into solid
Dynamic WettingConventional models: contact angle changes in zero time.
Interface formation: new liquid-solid interface is out of equilibrium and determines angle.
Liquid-solid interface takes a time to form
lgd
ls
180o
Liquid-solid interface forms instantaneously
e
Free surface pressed into solid
CoalescenceStandard models: cusp becomes “rounded” in zero time.
IFM: cusp is rounded in finite time during which surface tension forces act from the newly formed interface.
lglg
Internal interface
d
180o
Infinite velocities as t->0
ll
Interface instantaneously disappears
2u 1u 0, u u up
t
s s1 1 1 2 2 2
1 3 2
v e v e 0
cos
s s
d
s1
*1
*1
s 1 11
s 1 111 1
1 1|| ||
v 0
n [( u) ( u) ] n n
n [( u) ( u) ] (I nn) 0
(u v ) n
( v )
(1 4 ) 4 (v u )
s se
s sss e
s
ff
t
p
t
In the bulk (Navier Stokes):
At contact lines:
On free surfaces:
Interface Formation Model
θd
e2
e1
n
nf (r, t )=0
Interface Formation Modelling
s1
*1
*1
v 0
n [( u) ( u) ] n n
n [( u) ( u) ] (I nn) 0
ff
t
p
Kinematic equation :
Normal stress balance :
Tangential stress balance :
*2
s2
n [ u ( u) ] (I nn) 0
v n 0
Balance of tangential stress :
Normal velocity :
*2
s 2 22
s 2 222 2
2|| || 2
21,2 1,2 1,2
n [ u ( u) ] (I nn) 0
(u v ) n
( v )
4 v u 1 4
( )
s se
s sss e
s
s s
t
A
a b
At the plane of symmery (internal interface):
1 1 2 2
As 0 :
,
90
(conventional model)
e e
d e
T
As 0 :T
Coalescence: Models vs Experiments
Interface Formation
Conventional
Parameters from Blake & Shikhmurzaev 02
1 0.3se apart from
230mPas
Coalescence: Free surface profiles
Interface formation theory
Conventional theory
Water-glycerolmixture of 230cP
Time: 0 < t < 0.1
s is the distance from the contact line.
Disappearance of the Internal Interface
4
2
0 : 0
1: 10
2 : 10
3: 1
t
t
t
t
Free Surface Evolutions is the distance from the contact line.
4
2
0 : 0
1: 10
2 : 10
3: 1
t
t
t
t
Coalescence: Models vs Experiments
Interface Formation
Parameters from Blake & Shikhmurzaev 02
apart from
Conventional
48mPas
1 0.45se
Widergap
Coalescence: Models vs Experiments
3.3mPas
Interface Formation
Conventional Wideninggap
Parameters from Blake & Shikhmurzaev 02
3 3
2
1.2kg m , (10 )
18 Pa s, (10 )
airair
airair
O
O
For the lowest viscosity ( ) liquid: 3.3mPa s
Influence of a Viscous Gas
Eggers et al, 99: gas forms a pocket of radius
3/2br r
Toroidal bubble formation suppressed by viscous gas which forms a pocket in front of the bridge
Influence of a Viscous Gas
Interface Formation
Eggers et al, 99
ConventionalBlack: inviscid passive gasBlue: viscous gas
3.3mPas
Outstanding QuestionsHow does the viscous gas effect the interface formation dynamics?
Can a non-smooth free surface be observed optically?
Can the electrical method be used in wetting experiments?
How do the dynamics scale with drop size?
Are singularities in the conventional model the cause of mesh-dependency in computation of flows with topological changes (Hysing et al 09)?
FundingFunding
This presentation is based on work supported by:
Early-Time Free Surface ShapesHow large is the initial contact?
Eddi, Winkels & Snoeijer (preprint)
Initial PositionsConventional model takes Hopper’s solution:
for and chosen so that .
IFM is simply a truncated sphere:
Notably, as we tend to the shape
2 2 1/2 2 1
2 2 1/2 2 1
( ) 2 (1 )(1 ) (1 2 cos(2 ) ) (1 )cos( ),
( ) 2 (1 )(1 ) (1 2 cos(2 ) ) (1 )sin( )
r m m m m m
z m m m m m
0 u m min(0)r r
min 0r 2 2( 1) 1r z
2 2 2 2min min( ) ( ) , 1 (1 ) / 2c c cr r z z z z r
Influence of GravityOn the predictions of the conventional model.
Benchmark SimulationsConsider a steady meniscus propagating through a capillary.
To validate the asymptotics for take (with ):2 4 3 2 3 4( , ) 1:(5 10 ,5 10 ), 2 :(10 ,2.5 10 ), 3 :(10 ,5 10 )Ca
2 0.1V , 0Ca
Profiles of Interface FormationProfiles along the free surface for:
2 4 3 2 3 4( , ) 1:(5 10 ,5 10 ), 2 :(10 ,2.5 10 ), 3 :(10 ,5 10 )Ca
Profiles of Interface FormationProfiles along the liquid-solid interface for:
2 4 3 2 3 4( , ) 1:(5 10 ,5 10 ), 2 :(10 ,2.5 10 ), 3 :(10 ,5 10 )Ca
Value of the Dynamic Contact AngleFor
we obtain
compared to an asymptotic value of (Shikhmurzaev 07):
Outside region of applicability of asymptotics ( ):
2 4 3 2 3 4( , ) 1:(5 10 ,5 10 ), 2 :(10 ,2.5 10 ), 3 :(10 ,5 10 )Ca
1: 104.1 , 2 : 107.7 , 3 : 102d
102.1d
2 (1)V O
Capillary Rise: Models vs ExperimentsInterface formation & Lucas-Washburn ( ) vs
experiments of Joos et al 90
Silicon oil of viscosity 12000cP for two capillary sizes (0.3mm and 0.7mm)
( )h t
d e
Lucas-Washburn vs Interface Formation
Tube Radius = 0.36mm; Meniscus shape every 100secs
Tube Radius = 0.74mm; Meniscus shape every 50secs
After 100 secs
LW IF
After 50 secs
LW IF
Comparison to Experiment
Full SimulationFull Simulation
Washburn Washburn
JES & YDS 2013, J. Comp. Phy.
Meniscus height h, in cm, as a function of time t, in seconds.
h
tt
h
Microdrop Impact 25 micron water drop impacting at 5m/s on left: wettable substrate right: nonwettable substrate
Microdrop Impact
60e
Velocity Scale
Pressure Scale
-15ms
25m water drop impacting at 5m/s.