Ethylene-Acrylonitrile Copolymerization with Ni-Dii i ... · Ethylene-Acrylonitrile...
Transcript of Ethylene-Acrylonitrile Copolymerization with Ni-Dii i ... · Ethylene-Acrylonitrile...
Ethylene-Acrylonitrile Copolymerization with Ni Dii i /EASC/Cl C t l t S tNi-Diimine/EASC/Clay Catalyst System
Sang-Young A. Shin, Joao B. P. Soares, Leonardo C. Simon
Department of Chemical Engineering University of Waterloo
111
IPR 20
08
Contents
Motivation
Experimental Results
- Part 1 : Ethylene/Acrylonitrile Copolymer with α-Dimine-[N,N] Nickel
Dichloride/EASC System
- Part 2 : Ethylene In-Situ Polymerization with a Catalyst Supported onPart 2 : Ethylene In Situ Polymerization with a Catalyst Supported on
Clay Modified with Acrylonitrile
ConclusionsConclusions
Contributions and Acknowledgements
222
IPR 20
08
Motivation
Searching for a new surface modifier of clays
Developing high performance thermoplastic elastomers- Product with properties similar to Therban®oduct t p ope t es s a to e ba ®
IPR 20
08
Introduction
C h ld h l h l b h l fi
Polymerization Conditions for Polar Comonomers
- Comonomer should have at least two methylene spacers between the olefin and polar functional groups
- Tolerance to polar groups (approximately 1500 equiv. per metal center)Tolerance to polar groups (approximately 1500 equiv. per metal center)
3° Amines > Halides > Ethers > Ketenes > Esters > Water > Alcohols
Table 1 Amine Monomers Polymerized with Cp* ZrMe /Borate SystemTable 1. Amine Monomers Polymerized with Cp 2ZrMe2 /Borate System
a
Stehling,et al., Macromolecules., 1998, 31,2019
a. Activity = mol of monomer/mol of Zr⋅c[monomer]⋅hIP
R 2008
Part 1: Ethylene/Acrylonitrile Copolymer with α-Diimine-[N,N] Nickel Dichloride/EASC System
Nitrile group of acrylonitrile can coordinate metal active
Nickel Dichloride/EASC System
center in Ethylene/Acrylonitrile copolymerization.
L t t iti t l t l t t l t f lLate transition metal catalysts are tolerant for polar comonomer.
Pretreatment acrylonitrile with alkyl aluminum.
EASC as a co-catalyst for ethylene/acrylonitrile copolymerization.
555
p yIP
R 2008
Catalysts for Ethylene/Acrylonitrile Copolymer
Purging with N2/Solvent
EASC/CAT
TIBA/A l it il
Ethylene
N NNi
Cl Cl
TIBA/Acrylonitrile
1,4-bis(2,6-diisopropylphenyl)-acenaphthenediimine-dichloronickel (II)
Ethylene and acrylate copolymer was reported by Pd-diimine catalyst system by
Brookheart Group.
666
Johnson, L.K.; Mecking, S.; Brookhart, M. J. Am. Chem. Soc., 1996, 118, 267.IP
R 2008
Copolymerization of Ethylene and Acrylonitrile
N M C [C] Ti Yi ld M PDINo. M C [C](mol/L)
Time(hr.)
Yield(g)
Mw (kg/mol)
PDI
1 C2H4 - - 1 2.1 233 3.22 C2H4 C2H3CN 0.06 1 2.0 247 3.43 C2H4 C2H3CN 0.36 1 0.32 364 2.84 C2H4 C2H3CN 0.48 1 0.30 295 2.45 C2H4 C2H3CN 0.60 1 0.32 249 2.26 C2H4 C2H3CN 0.73 1 0.32 277 2.2
Catalyst :(diimine)NiCl2/EASC systemM: monomer(ethylene); C: comonomer (acrylonitrile with tri-isobutilaluminum) Experimental conditions: solvent: 25 mL;[1] = 4.25μmol/L, [Al]/[1] = 43, temperature = 25oC ;
777
[ ] μ , [ ] [ ] , p ;Pethylene = atmospheric. All samples were dried in the oven at 80 °C for 24 hrs.
IPR 20
08
Functional Groups in Ethylene/Acrylonitrile Copolymer,
Xylene Soluble, Xylene Insoluble Fractions
(c) Xylene-soluble fraction- Nitrile groups- Attenuated vinyl groups
(b)
(c)
2214 cm-1
2245 cm-1
(b) Xylene-insoluble fraction- Nitrile groups- vinyl groups- PAN structure an
smitt
ance
(%) ( )
2245 cm-1
2214 cm-1
1250 ~ 1230 cm-1
(a) Ethylene/acrylonitrile copolymer
Tra 2245 cm
1780 ~ 1590 cm-1
copolymer- Nitrile groups
4001000160022002800340040001
(a)2214 cm-1
2245 cm-1
888Figure 1. FT-IR spectra of ethylene/acrylonitrile copolymer sample 3
Wave Number (cm-1)IP
R 2008
1H, 13C NMR spectra ; Xylene insoluble part polymer after 24 hours extraction.
(a)CH3-CH(R)−C≡NR2−CH−C≡N R−CH2−C≡NCH CH(C N) )C N
No. Assignmentc Reference(ppm)
Origin sample(ppm)
CH3−CH(C=N)−)R2−CH−C≡N
3 CH3-CH(R)−C≡N 1.23 1.3 (br)
4 CH3−CH(C=N)−) 0.9 0.9
1 R−CH2−C≡N 2.1 2.1 (br)
2 R2−CH−C≡N 3.1 3.05~3.25 (br)
(b)
R2−CH−C≡N116117118119120121122123124
99
IPR 20
08
Transmission and ATR FT-IR spectra of Ethylene/Acrylonitrile Copolymerof Ethylene/Acrylonitrile Copolymer
Transmission ATR
C≡N C≡N?
C=C (CH )
C-Hrocking
C=CC=N
=N-H
(CH2)bending
C-Hstretching
600110016002100260031003600
Wave Number (cm-1)4001200200028003600
Wave Number
stretching
* ATR :Attenuated total reflection infrared IP
R 2008
1cm1cm
C
NC
N
CN
CN
CN
CN C
NC
N
N
CN
CNC
N
N
CN
CN
CN
C
CN
CN
CN
CN
NN
CN
CN
CN
CNC
NC
N
NN
CN
CN
CN
CN
CN
CN
CC
CN
C
CNC N
CN
CN
CN
CC
CN
CNC NC N
CN
CN
11
Ethylene Acrylonitrile Copolymer (No. 6 in Table 1)TEM, microtomed section of sample (No.6 in Table 1)(80 nm thickness)
500 nmIP
R 2008
Thermal Behavior of Ethylene/Acrylonitrile CopolymerCopolymer
time = 40 min.FT-IR Spectra ;
time = 10 min.
time = 20 min.
time = 30 min. Time increaseethylene/acrylonitrile copolymer(In the heating block at 160 °C)
ansm
ittan
ce (%
)time = 0 min.
Tra
5001000150020002500Wave Number (cm-1)
121212
Wave Number (cm )IP
R 2008
Thermal Behavior of Xylene Insoluble Fraction (PAN Rich Part)
STEP 1STEP 1
( )
0
2
4
282.22°C21 9°C
O N NNNOH
Cyclization220~310 °C
STEP 1O N NNNOHO N NNNOHO N NNNOH
Cyclization220~310 °C
STEP 1
-6
-4
-2
eat F
low
(mW
/g) 100.83 °C
91.17 °C0.42 J/g
217.59°C111.2 J/g
OO N N N NHSTEP 2
OO N N N NHOO N N N NHOO N N N NHSTEP 2
PAN, Jung et al., Material Letters,2002, 53, 18012
-10
-8
-6
He
110.99 °C
OO N N N NH
Aromatization330~350 °C
OO N N N NHOO N N N NHOO N N N NH
Aromatization330~350 °C
-12-100 -50 0 50 100 150 200 250 300 350 400
Temperature (°C)
NNOO N NHX1~2STEP 3
NNOO N NHX1~2NNOO N NHX1~2NNOO N NHX1~2STEP 3
Figure 4 16 Proposed mechanism for cyclization and aromatization of nitrile and acid
131313
Figure 4-16. Proposed mechanism for cyclization and aromatization of nitrile and acid
groups during thermal treatment of ethylene/acrylonitrile copolymers.
IPR 20
08
Stress-Strain Curves of Ethylene/Acrylonitrile Copolymer
8000Stress-Strain Curves ; T il ti i d
6000 No. 5, [AN] = 0.60
No. 6, [AN] = 0.73
Increase of acrylonitrileconcentration
Tensile properties are increased as the increase of initial loading of acrylonitrile concentrations
4000
Str
ess
(Kpa
) No. 4, [AN] = 0.48
2000 No. 1, [AN]1 = 0
•Sample Dimension : width- 6.5 mm, Height - 0.2 mm, Pressed film[AN] l/L
00 300 600 900 1200
Strain (%)
141414
•[AN] ; mol/L IP
R 2008
Conclusion
Successful synthesis of Ethylene/acrylonitrile copolymer.
Presence of PAN structure was confirmed by- FT-IR, 1H-NMR, 13C-NMR
Nano-phase distribution of PAN domains in PE matrix was observed byobserved by- TEM
Improved physical properties were confirmed by- Tensile tests.
151515
IPR 20
08
Part 2: Ethylene In-Situ Polymerization with a Catalyst S t d Cl M difi d ith A l it ilSupported on Clay Modified with Acrylonitrile
Intercalation and exfoliation of clay with acrylonitrile.
I i l i i f h l d l i il h lIn-situ copolymerization of ethylene and acrylonitrile on the clay surface.
Strong interfacial interaction between clay surface and PE matrices through introduction of chemical bonds.
Enhanced mechanical properties with PE-acrylonitrile/clay polymercomposite.
161616
IPR 20
08
Commercial ApplicationsClay Nanocomposites
Timing belt covers of automotive engines– Standard is glass fiber reinforced nylon or PP
Injection molded nylon 6 nanocomposite– Injection molded nylon 6 nanocomposite used in Toyota’s automotive engine parts
– Exhibited good rigidity and excellent thermal stability with a 25% weight reduction
Step- assists on vans/ trucks– Thermoplastic olefin (TPO) nanocomposite
used on 2002 GM mid- size vansNanocomposites are stiffer lighter less brittle– Nanocomposites are stiffer, lighter, less brittle in cold temperatures and more easily recyclable
– Cost the same as conventional TPOs,with no new tooling required
Nylon-clay nanocomposite bottles
171717
IPR 20
08
Morphology of Clays
Clay powder Primary particle Lamella(0.1 ~ 10 μm) (8 ~ 10 nm) (1 nm)
181818
IPR 20
08
In-Situ Polymerization of Ethylene and Clay
In-Situ Polymerization
clay
olefin+
organic clay nanocomposites
olefin+
processing(blending) nanocomposites
catalyst
+
catalyst+
(blending)
1919
IPR 20
08
Modification of Clay with Acrylonitrile
Small angle X-ray
450MMT
MMT/TIBA/An
3.6
8.86
g ydiffraction patterns for MMT and MMT/TIBA/AN.
150
300
Inte
nsity
, A.u
.
7.248.86
0
150
0 2 4 6 8 10 122 d
TGA and DTG(derivative weight loss) curves of MMT, MMT/TIBA and MMT/TIBA/AN samples
98
100
102
0.14
0.19MMT/TIBA/AN
MMT/TIBA
MMT
MMT
2θ degree
and MMT/TIBA/AN samples.
92
94
96
Wei
ght (
%)
0.04
0.09
Der
iv. W
eigh
t (%
/o C)
20202088
90
0 200 400 600 800
Temperature (oC)
-0.01
0.04IP
R 2008
Functional Groups in PE, PE-MMT/TIBA/AN, Clay Residue
Clay Residue(After Soxhlet extraction;
PE-MMT/TIBA/AN )
1742 cm-1(C=O) 1662, 1647 cm-1(C=C)
PE-MMT/TIBA/AN( l 2) sm
ittan
ce (a
.u.)
2244 cm-1(C≡Ν)
Polyethylene
(sample 2)
Tran
Polyethylene(sample 1)
1500180021002400Wavenumber (cm-1)
212121
Figure 5-2. FT-IR spectra for the comparison of functional groups between 1500 cm-1 and 2700 cm-1:IP
R 2008
Thermal Behavior of PE-MMT/TIBA/AN
DSC Curves; PE-MMT/TIBA/AN
(sample 6); 1st DSC thermogram
4
2
117.98 °C313 °C
4
2
117.98 °C313 °C
4
6
116.81°C
4
6
116.81°CDSC Curves; PE-MMT/TIBA/AN
(sample 6); 2nd DSC thermogram
0
(W/g
)
250 280 310 340 370
0
(W/g
)
250 280 310 340 370
2
4
W/g
) 5 15 25 35 45 250 280 310 340 370
118.64°C103.6 J/g
2
4
W/g
) 5 15 25 35 45 250 280 310 340 370
118.64°C103.6 J/g
( p ) g
-2
-4Hea
t Flo
w
313.34 °C128.82 °C140.1J/g-2
-4Hea
t Flo
w
313.34 °C128.82 °C140.1J/g
-2
0H
eat F
low
(W
g
124.96°C103.8 J/g-2
0H
eat F
low
(W
g
124.96°C103.8 J/g
-6
136.15 °C5 15 25 35 45
-6
136.15 °C5 15 25 35 45
-4
H
-4
H
-100 0 100 200 300 400-8
Temperature (°C)-100 0 100 200 300 400
-8
Temperature (°C)
-6-100 0 100 200 300 400
Temperature (°C)
-6-100 0 100 200 300 400
Temperature (°C)
222222
IPR 20
08
Tensile Properties of PE-MMT/TIBA/AN Composite
Stress-strain curves 3500PE 0% MMT
• Tensile properties are increased as MMT content increase
2500
3000
PE_0% MMT
No.3_5.5 wt% MMT
No.4_16.5 wt% MMT
No.2_6.4 wt% MMT
1500
2000St
ress
(KPa
)Increase of MMT/TIBA/AN
500
1000
S
00 50 100 150 200 250 300 350 400 450 500
Strain (%)
PE-Clay dry blending
23232323
( )IP
R 2008
Conclusions
Excellent intercalation and exfoliation of clay particles with acrylonitrileExcellent intercalation and exfoliation of clay particles with acrylonitrilemonomer.
Strong interfacial interaction between polyethylene matrices and clayStrong interfacial interaction between polyethylene matrices and claysurface.
Developed a new synthetic method; in- situ copolymerization of p y p yethylene and acrylonitrile.
Enhanced mechanical properties in polyethylene-acrylonitrile clay composite.
242424
IPR 20
08
Contributions
Scientific
• Synthesized ethylene-acrylonitrile copolymer. • Introduced interfacial interaction between polyethylene matrices and clay surface with acrylonitrile modificationclay surface with acrylonitrile modification.
Industry
• Developed a new synthetic method: in-situ copolymerization of ethylene and modified clay with bifunctional molecules.
Society
• Provided new knowledge for PE-Clay hybrid nanocomposites.
252525
IPR 20
08
Acknowledgements Thank you!
• Prof. Joao Soares and Prof. Leonardo Simon
• Financial support from – NSERC– NSERC
• Collaborators– Prof. Gunter Scholz (X-Ray and TEM)
262626
IPR 20
08
Functional Groups inEthylene/acrylonitrile CopolymerEthylene/acrylonitrile Copolymer
f i i lR−CH2−C N≡
No. Assignmentc Reference
(ppm)Origin sample
(ppm)
1 R−CH2−C≡N 2.0 2.1
2 R−CH2CO−O− 4.1 4.1
3 R−CH2NH− 8.31 8.2
R−CH2NH−
R−CH2CO−O−
012345678910
272727
ppm
1H NMR spectrum of ethylene/acrylonitrile copolymer (No. 6 in Table 1.)
IPR 20
08
Shielding effect
of nitrile group
H
H
H
a
bC N≡
HHC
of nitrile group
Hc HbHa
H
Hb
C N HbHaH
H
a
c
C N≡ Hb
HC
a
Shielding effect
H
H
a
bC N—TIBA≡
HaHb
of vinyl group
Hc
HC
Shielding effect
of vinyl group
55.15.25.35.45.55.65.75.85.966.16.26.36.46.56.66.76.86.97
IPR 20
08
HbC N TIBA
H
H
a
c
C N—TIBA≡
-0.50.51.52.53.54.55.56.57.58.59.5ppmIP
R 2008