RHEOLOGY OF BRANCHED POLYMERS - Leibniz … of... · RHEOLOGY OF BRANCHED POLYMERS Overview: The...
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RHEOLOGY OF BRANCHED POLYMERS
Overview: The Tube Model
Shear and elongational viscosity
Albena Lederer
Leibniz-Institute of Polymer Research Dresden
Member of Gottfried Wilhelm Leibniz Society WGL
Hohe Strasse 6, D-01069 Dresden, Germany
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Rheology of branching
Flow visualisation of molten PE into a contraction - different flow fields when driven from a
larger to a smaller cylinder
HDPE (linear) LDPE (branched)
Newtonian
fluid
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The tube model Monodispers linear polymers
Many chain system Tube model
Tube model of de Gennes, Doi and Edwards (1986)
Tube width a
Primitive lenght N.b
(N number of segments, b Kuhn lenght)
Monomer friction coef. x Perpendicular motions are confined
Curvilinear motions are permitted
Determination of stress relaxation modulus G(t) , e.g. G*(t)
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The tube model Monodispers linear polymers
PS, PB and PI with similar degrees of entanglement
G‘(w) elastic modulus
G‘‘(w) dissipative modulus
in phase and out of phase stresses – structure information!
reptation
Tube distance
Diff constant of the chain
DP of enanglement
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The tube model Monodispers star polymers
Broad range of relaxation times in the
branched polymer!
Reptation is suppresed
Fluctuations on the primitive length of the star arms
Unentangled loops
Number of entanglements of the arms Ma/Me
Linear PI
3-star PI
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The tube model Monodisperse Comb polymers
Arm
retractions
Unentangled
backbones
H-shaped PI
(arm molecular weight 20 kg/mol, backbone 110kg/mol)
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Model blends Star-star blends
PI 3-arm stars
M1=28 kg/mol
M2=114 kg/mol
Fast relaxation
Slow relaxation
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Model blends Star-linear blends
PI star-linear
blend
fstar=0
0.4
0.65
0.9
1.0
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Branched polymer melts Viscosity
Prediction of extension and shear viscosity of a branched polymer
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Branched polymer melts Viscosity
extension viscosity
shear viscosity
LDPE
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Hypebranched polymers Mechanical properties
a) b)a) b)
Storage modulus G’ and loss modulus G’’ vs. angular
frequency at 60°C for polyethylene
(chain walking mechanism with Pd-diimine catalyst)
highly branched topology nearly linear chain topology
Ye, Z.B.; Al Obaidi, F.; Zu, S.P. Macromol. Chem. Phys. 2004, 205, 897.
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Hypebranched polymers Complex viscosity
0,1 1 10 100
102
103
104
105
co
mp
lex
vis
co
sit
y
[Pa
s]
frequency [rad/s]
OH terminated hb polyester
C12 terminated hb polyester
0,1 1 10 100
102
103
104
105
co
mp
lex
vis
co
sit
y
[Pa
s]
frequency [rad/s]
OH terminated hb polyester
C12 terminated hb polyester
Complex viscosity versus frequency of
OH- and C12- terminated aromatic hb
polyester
Schmaljohann, D.; Häußler, L; Pötschke, P.; Voit, B.I.; Loontjens, T.J.A. Macromol. Chem. Phys. 2000, 201, 49
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Electron beam irradiation of linear PP
Formation of long chain branching-PP Advantageous property:
strain hardening / HMS behaviour
LCB Polypropylene Generation of LCB
CH3
CHCH2+
CH2 CH2
CH3
C CH
CH3
CH
CH3
CH2 CH
CH3
CH2
CH2
CH3CH
CH2 CH2
CH3
C CH
CH3
CH
CH3
CH2+
CH2 C
CH3 CH3
CHCH2
CH3
CHCH2 CH
CH3
CH2
Molar mass degradation by
ß-scission Molar mass increasing by
Branching reaction
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Influence of the irradiation temperature
Faster decrease of the concentration of radicals induced by irradiation,
decrease of the addition reaction frequency,
increase of the rate of ß-scission reaction,
increase of the chain diffusion to the amorphous phase,
partial melting of pellets.
Rätzsch, M.; Arnold, M.; Borsig, E.; Bucka, H.; Reichelt, N. Progr. Polym. Sci. 2002, 27, 1195-1282.
LCB Polypropylene
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ß-scission
low temperature
~25 °C
high temperature
up to 190 °C
Increasing of
ß-scission rate
e-beam
radiation
low branched PP
with large arms
high branched PP
with short arms
Speculation about
the structure of
modified products
Influence of the irradiation temperature LCB Polypropylene
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Modification
Electron beam 1.5 MeV
sample
Heating Turbo molecular Pump
Inert gas
Experimental set-up
• isotactic polypropylene (iPP)
homopolymer Novolen PPH2150
(Basell Polyolefins)
• electron accelerator ELV-2
(Budker Institute of Nuclear Physics,
Novosibirsk, Russia)
• dose: 20 kGy, 100 kGy
(1.5 MeV; 2 mA)
• atmosphere: nitrogen
• temperature: 25 –190 °C
LCB Polypropylene
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Characterization methods
Molecular Characterization by HT-SEC
at 150°C in 1,2,4-trichlorobenzene coupled with MALLS-detector
Molar mass M; radius of gyration <r2>
Principle of separation: hydrodynamic volume of molecules
branchlinear rr 22
branchlinear rr 22
branchlinear MM
branchlinear MM
LCB Polypropylene
<r2
> [
nm
2]
M [g/mol]
Linear iPP
Branched PP
linear
branch
r
rg
2
2
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SEC-MALLS characterization
Auhl et al. Macromolecules 2004, 37 (25), 9465-9472
Increase of the
Irradiation dose
Decrease of the
molar mass
and
Increase of
the LCB
0,2
0,4
0,6
0,8
1,0
0 20 40 60 80 100 120 140 160
1x105
2x105
3x105
4x105
5x105
6x105
7x105
8x105
Nu
mb
er
of
LC
B p
er
100
0 m
ono
me
rs
Mw
irradiation dose d [kGy]
Mw
[g
/mo
l]
NLCB
LCB Polypropylene
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5x105
106
2x106
3x106
103
104
virgin iPP
20 kGy: 100 kGy:
25°C 25°C
me
an
sq
ua
re r
adiu
s o
f g
yra
tio
n <
r2>
[n
m2]
molar mass M [g/mol]
Increase of the
Irradiation dose
Decrease of <r2>
Increase of
the LCB
Auhl et al. Macromolecules 2004, 37 (25), 9465-9472
SEC-MALLS characterization LCB Polypropylene
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5x105
106
2x106
3x106
103
104
virgin iPP
20 kGy: 100 kGy:
25°C 25°C
80°C 80°C
mean s
quare
radiu
s o
f gyra
tion <
s2>
[nm
2]
molar mass M [g/mol]
SEC-MALLS characterization LCB Polypropylene
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5x105
106
2x106
3x106
103
104
virgin iPP
20 kGy: 100 kGy:
25°C 25°C
80°C 80°C
110°C 110°C
mean s
quare
radiu
s o
f gyra
tion <
s2>
[nm
2]
molar mass M [g/mol]
SEC-MALLS characterization LCB Polypropylene
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5x105
106
2x106
3x106
103
104
virgin iPP
20 kGy: 100 kGy:
25°C 25°C
80°C 80°C
110°C 110°C
150°C 150°C
mean s
quare
radiu
s o
f gyra
tion <
s2>
[nm
2]
molar mass M [g/mol]
SEC-MALLS characterization LCB Polypropylene
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5x105
106
2x106
3x106
103
104
virgin iPP
20 kGy: 100 kGy:
25°C 25°C
80°C 80°C
110°C 110°C
150°C 150°C
190°C
mean s
quare
radiu
s o
f gyra
tion <
r2>
[nm
2]
molar mass M [g/mol]
Increase of the
Irradiation
temperature
Decrease of <r2>
SEC-MALLS characterization LCB Polypropylene
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5,05,0
9
4
71
mmg
Assumption: trifunctional
randomly branched polymer
12
mm
MM S
Molar mass of the segments Ms:
(m+2) - number of the pieces between the branching points and the chain ends
(m-1) - number of the pieces between the branching points
Sugimoto et al. J. Appl. Polym. Sci.
1999, 73, 1493.;
Zimm et al. J. Chem. Phys. 1949, 17, 1301.
m - number of branching points
SEC-MALLS characterization LCB Polypropylene
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105
106
107
3x103
104
105
7x105
20 kGy: 100 kGy:
25°C 25°C
190°C 130°Cmola
r m
ass o
f seg
ments
MS [
g/m
ol]
molar mass M [g/mol]
Ms is nearly
constant in the
range between
5x105 - 3x106 g/mol
SEC-MALLS characterization LCB Polypropylene
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1x104
2x104
3x104
1,0x105
1,5x105
2,0x105
20 40 60 80 100 120 140 160 180 200
20 kGy
100 kGy
irradiation temperature T [°C]
mo
lar
ma
ss o
f se
gm
ent
MS [
g/m
ol]
Increase of the
Irradiation
temperature
Decrease of Ms
shorter chain
segments
SEC-MALLS characterization LCB Polypropylene
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1x104
2x104
3x104
1,0x105
1,5x105
2,0x105
20 40 60 80 100 120 140 160 180 200
20 kGy
100 kGy
irradiation temperature T [°C]
mo
lar
ma
ss o
f se
gm
ent
MS [
g/m
ol]
norm
aliz
ed h
ea
t flo
w [
W/g
]
exo
partial melt melt solid
SEC-MALLS characterization LCB Polypropylene
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Shear Flow Rheology by Plate-Plate rheometer
at 180°C, in nitrogen, cylindrical samples of 2 mm thickness and 25 mm diameter
Zero shear-rate viscosity 0
0
0
t
tJtJ
0lim
tJ
t
t
Qualitative determination of the branching topology
0 in dependence on Mw
J. Janzen, R. H. Colby J. Mol. Struct. 1999, 485-486, 569.
e
a
e
a
M
M
M
M
exp0
Rheology characterization LCB Polypropylene
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105
2x105
4x105
6x105
8x105
106
102
103
104
105
106
3x106
T= 180°C
lg -15.4 + 3,5 x lg M
w
0 [P
a s
]
Mw [g/mol]
Low
branching
High
branching
Linear iPP
polyethylene:
Decrease of 0
Decrease of the
molar mass of LCB
and
Increase of the
number of LCB
(Mw~constant)
Inkson et al. Proc. XIVth Int. Congr. on Rheology, August 22-27, 2004, Seoul, Korea.
Shear Flow Rheology LCB Polypropylene
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105
106
5x102
103
104
105
106
190°C170°C150°C
110°C 80°C25°C
150°C130°C
110°C80°C50°C
25°C
virgin iPP
linear iPP, T=180°C
lg -15,4 + 3,5 * lgM
W
ze
ro s
he
ar
vis
co
sity
0 [
Pa
s]
linear iPP
20 kGy & irrad. temp.
100 kGy & irrad. temp.
weight average molar mass Mw [g/mol]
Increase of the
Irradiation
temperature
Decrease of 0 (Mw~const.)
lower molar mass
and higher
number of LCB
More and shorter long chain branches (arms)
LCB Polypropylene Shear Flow Rheology
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SEC-MALLS vs. Rheology LCB Polypropylene
Auhl et al. Macromolecules 2004, 37 (25), 9465-9472
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SEC-MALLS vs. Rheology LCB Polypropylene
Auhl et al. Macromolecules 2004, 37 (25), 9465-9472
Increase of the
Irradiation dose
Decrease of 0
At low LCB amounts
Increase of 0
At high LCB amounts
lower molar mass
and higher
number of LCB
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SEC-MALLS vs. Rheology LCB Polypropylene
Auhl et al. Macromolecules 2004, 37 (25), 9465-9472
Transient elongational viscosity vs. time
at different Henky strain rates Strain hardening factor:
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SEC-MALLS vs. Rheology LCB Polypropylene
Auhl et al. Macromolecules 2004, 37 (25), 9465-9472
•High sensitivity of detecting low amounts of branches in polymers of rheology measurements (strain
hardening/elongational viscosity and shear viscosity)
•Lower sensitivity of detection in solution (SEC) but qualitative calculations possible
Strain hardening factor: