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UNIVERSITEIT TWENTE. Physics of Complex Fluids
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Dispersion Rheology
Dirk van den Ende
Dept. of Science and Technology
University of Twente
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Outline Dispersions of non-interacting hard spheres • Volume fraction dependence • Brownian particles and Péclet number • Shear induced diffusion
Soft particle dispersions Weakly aggregating dispersions
microstructure in relation to • flowcurve • linear viscoelasticity
Dispersions out of thermodynamic equilibrium
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Sphere in liquid • goes with the flow • has to rotate, additional friction
NVp
V φ =
Einstein calculated: η = ηo (1+2.5φ )
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At higher concentrations • particles collide with each other • excluded volume effects
Dispersions
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φ
η/ηs
η(φ)/ηs Phan and Russel; 1996
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Einstein’s result
In terms of number of added particles, ΔN:
Mean field approach: starting with N particles, call that your “solvent” and add again ΔN particles:
Vfree: volume available to the added particles
α slightly larger than 1 due to interstitial solvent.
[η]=2.5, φ = NVp/V
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rewriting this equation
or
Krieger Dougerhty equation:
α = 1/φm
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φ
η/ηs φm = 0.53
φm = 0.65
Einstein
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ηr
Pe = γ’a2/D0
colloidal particles competition between diffusion and convection
tflow ~ 1/γ’ tdiff ~ a2/D0
polystyrene particles a = 400 nm
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Viscoelastic effects: HS dispersions show visco-elasticity. What is the origine of the elasticity?
J. van de Werf et al.; 1989
log(ωa2/D0)
silica particles, a = 50 nm
η’’ r
η’
r
Entropy and distorsion of the pair distribution fuction g(r)
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Non colloidal particles shear-induced self-diffusion in simple shear flow
D = a2’ D ()
a particle radius
’ rate of shear
volume fraction y
x
Dxx Dxy 0
Dyx Dyy 0
0 0 Dzz
Tensor character:
UNIVERSITEIT TWENTE. Physics of Complex Fluids
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Simple model • Particles follow flow lines
if not prohibited by excluded volume • While colliding they role over each other • Collisions are not completed due
to interaction with a third particle
Δz
z
x
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Taking an average collision time tc(φ), we calculate the displacement vector s(θ,φ) per collision.
Diffusion tensor:
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UNIVERSITEIT TWENTE. Physics of Complex Fluids
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φ
Dij /γ’ a
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Soft particle rheology
P.A. Nommensen; 1999
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φeff
ηr, D’Haene, thesis Leuven; 1992
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The mystery of the missing factor 3
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Weakly aggregating colloidal dispersions
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depletion interaction
Parameters: • particle concentration • polymer concentration and size • structure of the aggregates
Fint
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Flow curve
γ/γ#
η/η o
Silica particles (a = 38nm) in Polystyrene (5970 g/mole)
φ = 8%
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R volume fraction of aggregates:
Fint ≥ Fhyd :
mean field approximation
viscosity curve:
fractal aggregate
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γ/γ#
η/η o
df = 2.3±0.2
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measuring cylinder
and sampleholder
spring, K
air bearing, D
exciter
measuring elasticity in a shear flow: G' (',) G'' (',)
Steady rotation in the r,φ plane, Oscillation in the r,z plane
Zeegers et al. ; 1995
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10|-‐2 10|-‐1 10|0 10|1 10|2
‘ [rad/s]
10|-‐2
10|-‐1
10|0
10|1
10|2
G' [P
a]
10|-‐2 10|-‐1 10|0 10|1 10|2
‘ [rad/s]
10|-‐2
10|-‐1
10|0
10|1
10|2
G'' [Pa] Fmax
Fmax
R h
Ábreak = ‡/…
Áescape
.
tescape
increasing γ’
ω [rad/s]
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Shear cell on Confocal Scanning Laser Microscope
Silica particles (1 m) and poly(ethylene glycol) in a methanol-bromoform mixture
100 x
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Different cross sections through an aggregate
V. Tolpekin, thesis UT; 2004
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0.4 1 10 40
r/a
1
10
100
N(r)
df = 2.0 ± 0.1
z = +5 um z = 0 um z =-5 um
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Aggregate growth
t [s] 0 1000 2000 3000 0
5
10
15
20
25 <D
>/a
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Modeling the aggregate growth
adjustable: Ko(' ), Q
dni /dt = ½ Ai-j,j ni-j nj - Aij ni nj + Bj pji nj - Bi ni
Aggregation: Aij =4/3 ' (Ri+ Rj)3
Break-up: Bi = Ko(' ) (Ri /a)Q
d Rdf /dt = C [R3 +3 R2 R ] - Ko(' ) RQ Rdf
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Results of the modeling
t [s] 0 1000 2000 3000 0
5
10
15
20
25 <D
>/a
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Aging of soft colloidal suspensions studied by macro- and micro-Rheology
40 °C
20 °C
E.H. Purnomo et al.; 2008
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(micro-) rheology probes the aging
Structural relaxation time: ts ~ tc
log w
G’
G” increasing Age
log G
Aging in soft glassy materials
* relaxation processes slow down with age of the sample… * equilibrium is never reached…
tc
log t
log <x2>
increasing Age
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Thermosensitive polyNipam-polyNipmam particles
40 °C
20 °C
10 20 30 40 50 60
50
75
100
T [oC]
R g [n
m]
light scattering data
liquid glass
40 oC
20 oC
with fluorescent ( ) tracer particles eff = V0 n
V0 (T)
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Experiment To obtain reproducible results… …rejuvenate the sample
quench > yield 0 < yield
stre
ss
qu
ench
tw t
1: macro-rheology (HAAKE RS 600)
2: particle tracking (Confocal Scanning Laser Microscopy)
quench > yield stre
ss
qu
ench
tw t <
x2>
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0 100 200 300 400 500 600 700 800
time [s]
0
1
2
…(t) [-‐]
0
2
4
Â(t) / Â
y
t w
t
/y
t [s]
tw [s]
Creep measurements
T = 24 oC c = 7 %w/w
J(t-tw,tw) = ( (t)- (tw))/0
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10 - 2 10 - 1 10 0 10 1 10 2 10 1
10 2
10 3
G'
G"
10 - 2 10 - 1 10 0 10 1 10 2 10 1
10 2
10 3
10 - 2 10 - 1 10 0 10 1 10 2 10 1
10 2
10 3
G’
G"
(rad/s)
G’’,
G’
(Pa)
tw= 30, 600, 3000, 10000s
• Brownian motion (~√) • local viscosity (~ ) (Mason, Weitz 1995)
age dependence at low frequencies
particle-liquid interaction at high frequencies
Linear rheology, age dependence
T = 25 oC c = 7 %w/w
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Soft Glassy Rheology model
P. Sollich et al., Phys. Rev. Lett. 78, 2020 (1997); S.M. Fielding et al., J. Rheol. 44, 323 (2000)
• Dissipation due to internal yielding of the particles • Activated rate process with effective noise temperature x x > 1: liquid, G* = fnc (), J = fnc (t-tw) x < 1: glass, G* = fnc (t), J = fnc ((t-tw)/tw)
102
G',
G" (
Pa)
101
102 104
t Elastic response
10-1 100 10+1
ω [1/s]
G’’ tw
Microscopic picture
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glass aging
liquid non aging
100
101
102
G',
G" (
Pa) (a)
T=35 oCx=0.67±0.03
100 101 102 10310 0
10 1
ωtG
', G
" (Pa
) (b)
T=37 oCx=0.87±0.03
100 10110-4
10-3
10-2
10-1
100
ω(rad/s)
G',G
" (Pa
) (d)
T=40 oCx>3
10-1 100 10110-2
10-1
100 101 102 103ωt
(c)
T=38 oCx=2.2±0.3
ω(rad/s)
G',G
" (Pa
)
100
100
101
102
G',
G" (
Pa) (a)
T=35 oCx=0.67±0.03
100 101 102 10310 0
10 1
ωtG
', G
" (Pa
) (b)
T=37 oCx=0.87±0.03
100 10110-4
10-3
10-2
10-1
100
ω(rad/s)
G',G
" (Pa
) (d)
T=40 oCx>3
100 10110-4
10-3
10-2
10-1
100
ω(rad/s)
G',G
" (Pa
) (d)
T=40 oCx>3
10-1 100 10110-2
10-1
100 101 102 103ωt
(c)
T=38 oCx=2.2±0.3
ω(rad/s)
G',G
" (Pa
)
100
10-1 100 10110-2
10-1
100 101 102 103ωt
(c)
T=38 oCx=2.2±0.3
ω(rad/s)
G',G
" (Pa
)
100
Macro-rheology (curves: SGR model)
mass concentr. c: 7 %w/w tw: 3, 30, 300 s
T= 35oC
T= 38oC
T= 37oC
T= 40oC
t
t
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+: micro-rheology 0 5 10 15
0.50
1.00
1.50
2.00
φ
G p [Pa]
li quid
glas s
hard s pher e limit
(b)
liquid
glass
eff = V0 n
φeff
E.H. Purnomo et al., 2008
3 5 7 9
20
30
40
c [%]
li quid
glas s
T [
o C]
(a)
Phase diagrams
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10 1 10 2 10 3 10 4 10 5 10 6 10 1
10 2
10 3
G'
G"
10 1 10 2 10 3 10 4 10 5 10 6 10 1
10 2
10 3
10 1 10 2 10 3 10 4 10 5 10 6 10 1
10 2
10 3
t
G'
G"
The structural relaxation time is not observable How to measure the structural relaxation time ?
T = 25 oC c = 7 %w/w
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5 m
rn(t)
rn(t+s)
particle tracking µ-rheology
<>: ensemble averaging
Stokes Einstein Relation (Newtonian fluid):
Generalized Stokes Einstein Relation:
: fluoresent tracer observed by CSLM
rn = (xn,yn)
Bursac et al; Nature materials 2005
J(t): retardation function
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<r2> polyNipam, 4%
liquid
glass
32oC
30oC
27oC
detection limit
eff = 1.2
eff = 1.3
eff = 1.5
eff = 1.4
31oC
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Glass transition at c = 4%
tw
300 s (o) 3000 s (●)
eff = 1.3
eff = 1.4 30 <Tg< 31 oC 1.3 <g< 1.4
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tw [s]
300 800
1300 1800 3000 3500 4000 4500
10|0 10|1 10 |2 10 |3 10 |4
10 |-‐3
10 |-‐2
t-tw [s]
<r2 >
[m
2 ]
polyNipam-polyNipmam, 4%, 27 °C Age dependence
10|-‐2 10 |-‐1 10 |0 10 |1
10 |0
10 |1
(t-tw)/
<r2 >
/<
r2 >p
0.0 2.5 5.00.00
0.25
0.50
[ks]
tw [ks]
= (0.09 ± 0.01) tw
polyNipam-polyNipmam, 4%, 27 °C scaling with tw
UNIVERSITEIT TWENTE. Physics of Complex Fluids
48/50 10 |-‐1 10 |0 10 |1 10 |2
10 |-‐1
10 |0
G’/G’
G’’/G’
micro-rheology viscoelastic moduli
T.G. Mason, 2000
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Macro- vs µ-rheology
10|-‐3 10 |-‐2 10|-‐1 10 |0 10|110|-‐1
10|0
10|1
10|2
ω [1/s]
G',G'' [Pa]
Experimental observation:
G'macro / G'micro 2
tcmacro / tcmicro 5
T = 27 °C c = 4 % w/w tw = 1300 s
Mean field calculation of the frequency dependent drag on a
stationary particle in a low viscous cell surrounded by a viscoelastic bulk
= [G”/] =
UNIVERSITEIT TWENTE. Physics of Complex Fluids
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G’
G’’
[P
a]
micro- vs macro T = 27 °C c = 4 % w/w tw = 1300 s
10 |-‐3 10|-‐2 10|-‐1 10 |0 10 |110|-‐1
10 |0
10 |1
b/a =1.05
G*
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