hanyang univ. spring 2008 chap 10. non-radical addition polymerization anionic polymerization -the...
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Hanyang Univ.Hanyang Univ.
Spring 2008
Chap 10. Non-Radical Addition PolymerizationAnionic Polymerization -the growing chain end bears a negative charge
The mechanism of cationic polymerization is a kind of repetitive alkylation reaction.
The mechanism of anionic polymerization is a kind of repetitive conjugate addition reaction .(the "Michael reaction" in organic chemistry)
Cationic Polymerization -the growing chain end bears a positive charge
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B-Z + CH2=CHX B-CH2-CH- Z+
X
Initiation:
Propagation:
M- Z+ + M MM- Z+
Termination:
M- Z+ + HT MH + ZT
General Scheme
Anionic Polymerization
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CH LiCH3CH2
CH3
CH2 CH CHCH3CH2
CH3
CH2 CH Li
CH2 CH Li CH2 CH CH2 CH CH2CH Li
CH2 CH Li H OH CH2 CH2 Li OH
Initiation:
Propagation:
Termination:
+
+
+ +
Styrene Polymerization
Anionic Polymerization
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Anionic Polymerization
Characteristics of an Ideal Anionic PolymerizationNegative centers repel one another and thus termination by recombination is not possible. An ideal polymerization is “living”, which does not terminate until a terminator is added. Initiation is normally very fast relative to propagation and all chains grow simultaneously. This leads to polymers with low polydispersity or monodispersity.Theoretically:
The rate of polymerization for methacrylates and styrenes is high even at -78 oC. This is partly for the high concentration of the anion centers.The degree of polymerization
K=1 or 2 depending on initiator used.
nn
w
xM
M 11
0
0
I
MKxn
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Initiation by Electron Transfer
- .
- .
CH2 CH CH2 CH-.
CH2 CH-.
CH2 CHCH2CH--
+ KTHF
-78 oC
K +
K + + +
2
K +
K +K +K
+
0
02
I
Mxn
• Polymerization mostly done in THF and not nonpolar solvents like cyclohexane or benzene for the solubility the complex in THF.
• The degree of polymerization is given by
Anionic Polymerization
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Initiation by Nucleophilic Attack
CH2 CH CH3(CH2)4 CHCH3(CH2)2CH2 Li Li
COOCH3
CH2 C
CH3
N Li N
COOCH3
CH2 C
CH3
Li
THF
-78 oC+
++
THF
-78 oC+ +
0
0
I
Mxn
• Polymerization can be done in both polar and nonpolar solvents.• The degree of polymerization is given by
Anionic Polymerization
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Spring 2008
Initiation by Living Polymer
CH2 CH Li CH2 C
CH3
COOCH3
CH2 CH CH2C
CH3
COOCH3
LiTHF
-78 oC++ +
CH2 CHLiCH2 C
CH3
COOCH3
++
Because the starting anion has to be a stronger Lewis base than the resulting anion.
But not
Anionic Polymerization
0
0
I
Mxn
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Propagation
M Z M M MZ+-Z+-
Z+- +CovalentBond
Contact IonPair
Solvent SeparatedIon Pair
Free ions
Solvent polarity increases
kP increases
Polymer tacticity decreases
• Kp can vary by orders of magnitude.
• The polydispersity remains low because the rate of inter-conversion between the different forms is much faster than the polymerization.
Anionic Polymerization
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Termination
M MH
M MCOO
MCH2Br CH2Br
MM
MCH2Br CH2Br
M Br
Z+-
By proton
H+
Z+ +
By CO2
Z+- CO2
Z+-
By using a limiting amount of 1,2-dibromoethane
Z+-2
K=2
By using a much excess of 1,2-dibromoethane
Z+-
Anionic Polymerization
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Anionic Polymerization (1) proton donor H2O or ethanol Strong base is not enough for initiation.
(2)
Ctr,s=10-3 (small chain transfer constant)
EtOH high MW product
ethoxide no longer living.
C H 2 C
H
: - + H 2 O C H 2 C H 2 + O H
-
H2O Ctr,s=10H2O low MW polymer No living polymer
Strong base is not enough for initiation.
CH2
H
+ C2H5OHC:- CH2 CH2 + C2H5O-
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Anionic Polymerization (3) Termination can occurred by hydride elimination without impurities.
a)
b) anionic species(active center) react with chain ends to form inactive allylic anion.
C H 2 C H C H 2 C H : - N a +
C H 2 C H C H C H
+ N a + H - :
C H C H C H 2 C H + C H 2 C H . . -
C H 2 C H 2 + C H C H C H 2 C H . . - 1,3 diphenylallyl anion is
very unreactive, highly resonance stabilized
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Anionic Polymerization Termination of polar monomer
In this case, although the initiator or active center attacks the monomer, that results the non-polymerization.
C H 2 C
C H 3
C O C H 3
O
+ R - L i + C H 2 C
C H 3
C R
O
+ C H 3 O - L i +
+ CH2 C
CH3
COOCH3
CH2 C:-CH3
COOCH3
Li+
CH2 C
CH3
COOCH3
C
O
C
CH3
CH2 + Li+CH3O-
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Anionic Polymerization Backbiting or intramolecular reaction
4) Hugginson-Wooding System
J.Chem. Soc. 1952
Polymerization of styrene conducted in liq. NH3 at bp -33C
(1) reaction rate ↑ as [I] and [M]2
I=K+NH2- rate ↑ as [NH2
-] ↑ but as [K+] ↓
(2) MW [K+] and [NH2-]
(3) Polymer is formed without unsaturation.
Cyclic trimer at the end of chain
C H 2 C C
O C H 3 O
C C H 3
C O O C H 3
C H 3 C O O C H 3
C H 2 C C
O
C C H 3
C O O C H 3
C H 3 C O O C H 3
+ C H 3 O - - ̈
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Anionic Polymerization
][
]][[]][[ 2
2
K
KNHMKkMHNkR i
ii
][
]][[
2
2
KNH
NHKk
KNH2 K NH2
k
If [K+] , then Ri If [K+] , then Ri
Dissociation of initiatorDissociation of initiator
Initiation step
NH2 + CH CH2 H2N CH2 C:-
Hk1
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Propagation
Anionic Polymerization
]][[ MMkR pp
H 2 N M n - + M H 2 N M n . M
- kp
Termination
][
][][
]][[
][][
3,
22
3,
22
p NHk
NHMkk
NHKk
KNHMkkKR
str
pi
str
pi
][
][][
]][[
3,
2
1
222
1
2
1
22
1
NHk
KNHMkKkR
KNHMKkR
str
pip
ii
H 2 N C H 2 C H C H 2 C : - H
+ N H 3 H 2 N C H 2 C H C H 2 C
H
H
: N H 2 - +
ktr,s
n n
Occurs by chain transfer
Rtr=ktr,s[M-][NH3+]Overall Rate using Steady state assumption. (RiRt).
If KCl is added Rp decreases
[K+]=[NH2-]
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Spring 2008
Anionic Polymerization
][
][
][
][
33, NHC
M
NHk
MkX
sstr
pn
In dehydrate state,
Chain transfer constant for solvent
molekcalEEEE
rateoverall
RateDPtemp
molekcalEEE
trpiR
n
trpnx
/9
/4
Activation energy for Xn
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Anionic Polymerization
1 if 1
1 n
wn
nn
w
M
MX
XM
M
RONa + nCH2 CH2
O
CH2CH2O-Na+RO(CH2CH2O)n- 1
In Flory
If there is no termination rxn, the narrow MW distribution can be obtained.
5) Base Initiated Polymerization - a strong nucleophile is required as the initiator
NO2 > C O > SO2 > CO2
CH CH2 >>> CH3
CN > SO > C2H5
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Anionic Polymerization
6) Practical Comments
If we use metal as an initiator, the propagation rate is fast.
purity import!
7) Propagation Kinetics
]][[ MMkR pp
Comparing to the radical polymerization, the propagation doesn’t occur too fast
For most of the living polymers
[M:-] = [I][M] = is about 10-9 to 10-7 molar[M:-] = 10-3 to 10-2 molar
kp for free radical case is 5103 l/molesec
Kp : depends on solvent and counter ion
Counter ion and active center can be separated by changing the solvent then reaction rate increases
conc. of anion = conc. of initiator
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(1) Evaluation of Individual Propagation Rate Constants
Propagation rate constant for free ion and ion pair. [P-]: conc. of free ion [P-(C+)]: conc. of ion pair
])][([]][[ MCPkMPkR ppp
Anionic Polymerization
2
1
)])([(][
][][
,addedbeen have ions more if
]][[
)]([1
K)( .
]][[][
)]([][
CPKP
CP
CP
CP
K
CPCPEqat
MMkRM
CPkPkk app
pppapp
p
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Spring 2008
Anionic Polymerization* How to measure kp, kp, K ?
][
log 0
MC
C
.apppkslope
appk
2
1
][ M
p
pp
kintercept
Kkkslope 2
1
)(
t
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Spring 2008
Anionic Polymerization
][
][][
C
MKP
][][
][CZ
MKP
the conc. of living and the conc. of free ion
][][
][)]([CZ
MKMCP
A salt that must be soluble in THF with common ion to gegen ion is added to reaction mixture.
[C+][CZ]
The salt was added at high conc.
Conc. of the added salt is [CZ]
][
)(
CZ
Kkkkk pp
pappp
][
)]([][
M
CPkPkk
originally
pappp
apppk
][CZ
p
pp
k
Kkkslope
int
)(
Hence
Then able to get kp-, kp
, K from the two graphs.
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Spring 2008
Anionic Polymerization
Effect of gegen ion on Anionic Polymerization of Styrene
THF Dioxane
kp K107 kp
- kp
Li+ 160 2.2 6.5104 0.94
Na+ 80 1.5 3.4
K+ 60~80 0.8 19.8
Rb+ 50~80 0.1 21.5
CS+ 22 0.02 24.5
- Why kp- is the same value?; kp- is much more larger than kp Thus we can say that reactivity of free ion is much greater than that of ion pairs.
- In the case of dioxane?;In dioxane which is tend not to be solvated, it has reverse tendency comparing to the case of THF. Solvation is not important in dioxane. Cs is too high and there is no difference.
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Anionic Polymerization
]][[
]][:[
MRLikR
MLiMkR
ii
pp
Look at difference.Unassociated species
Li+ genenion in aromatic hydrocarbon
Let’s say we are using the BuLi initiator.
solvation as well as is important!
Although, the 1,2 diethoxyethane reduce the , kp varies 1~1000 fold because of highly
solvating ether . Reactivity of free ion < Reacitivity of ion pair
In aromatic hydrocarbon, unassociated species dominate rate.Depends on the unassociated species in very low conc.
(nC4H9Li)6 C4H9Li6
K1
(R Mn-Li+)2 2C4H9 Mn-Li+K2
CH2 C
H
RLi
LiCH
RCH2 2 CH2 CLi
H
RCovalent character
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Spring 2008
Anionic Polymerization
6
1
6946
1
1 ])[(][ LiHCKRLi
rateinitiationinorder
Rtheinorder
LiMKLiM
R i
6
12
1
2
1
22
1
2
6
1
]):[(]:[
][
Evidence — the viscosity measurement before and after term, we find that living
polymer is associated after termination, viscosity drops.
Because initiators and ion pairs are reduced,
Polymerization reaction in Aliphatic HC is lower than inaromatic HC.
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Effect of solvent and gengenion on Copolymerization of Styrene and isoprene at 25C
Solvent% Styrene in copolymer
Na+ counter ion Li+ counter ion
Nonsolvent 66 15
Benzene 66 15
Triethyl ether 77 59
Ethyl ether 75 68
THF(highly saturating solvent)
80 80
Lenz P.437 Table 13-9
Anionic Polymerization
Generally sodium is more ionic than lithium
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Cationic PolymerizationThe growing chain bears a positive charge. The active sites are either carbenium ions or oxonium ions.
Electron donating groups are needed as the R groups because these can stabilize the propagating species by resonance.
Ex)
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Cationic InitiatorsProton acids with unreactive counterions
Lewis acid + other reactive compound:
* To use Lewis acid effectively as initiators, use the co-initiator.
B
F
F
F
C2H5Cl C2H5 [BF3Cl]+. .
. .: +
cationogen
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Cationic Polymerization
OH
BF3OH H++ C C
C
C
CH3 C+
C
C
B F3OH
isobutylene
BF3 + OH2 BF3OH H+k e
CH3 C C C C+BF3O H + C C
C
C
kp
Typical Initiator Systems Co-initiator Initiator SnCl4 H2O
AlCl3 HCl
H2SO4 H2SO4
Order of reactivity AlCl3 > AlRCl2 > AlR2Cl >AlR3
HCl > CH3COOH > C6H5NO2 > > H2O >> CH3OH > CH3COCH3
Ex)
More acidic initiators are the most effective in initiating polymerization
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Termination
Kinetics
Cationic Polymerization
2 *
3
*
2t
eipp M BFOH
k
KkkR
C C C
C
B F3OH
C
C
C
+ HB-F3OH
H
32ei3ii BF OH MKkHOFBH MkR
OHBF MkR 3pp
S SRR ti 32ei3tt BF OH MKkOHBF kR
32t
ei3 BFOHM
k
KkOHBF
Problem : temination reactions occur randomly.
[ * ] can control rxn
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Cationic Polymerization
MXk
constXk
ntr
nt
0
,. 0
Mkk
MkX
trt
pn
C1
C3
C 6
C7
C8
C15
C16
B17
F3OHk tr
C21
C22
C27
C30 C 32
C33
C34
B F3OH+
M k k
M k
RR
RX
trt
p
trt
pn
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Chain Transfer Reactions -Cationic vinyl polymerization is plagued by numerous side reactions, which lead to chain transfer mostly.
• Difficult to achieve high MW (*initiator can give rise to many separate chains because of chain transfer)
• These side reactions can be minimized But ! not eliminated by running the reaction at low temperature
Ex)
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Cationic Polymerization1) Ring opening polymerization
(1) Mechanism
carbon type polymzn.
Example of ROR : cyclic amides, sulfides, acetals, esters, lactam, alkanes, …
(2) Polymerizability
- unstable ring or the ring which cannot be cyclized easily are very reactive * 3,4 and 7-11 membered ring is the most reactive ring
5,6 membered rings are stable and polymerize slowly, but, it still possible to be polymerized.
**3-membered ring is the most easiest to be polymerized
O R CH2 OCH2
R
O
CH2
ROORCH2ORCH2
CH2
R
++
+. .. .
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Cationic Polymerization(3) polymerization of THF(Polytetrahydrofuran)
PF52 PF4 (PF6)+ -
PF4 (PF6)+ - + O PF4 O
+PF6
-
gegenion
O(CH2)4O(CH2)4 O(CH2)4
(CH2)4
+-
AO
O(CH2)4O(CH2)4O(CH2)4
+O (CH2)4
+
-A
if H2O exist in the co-catalyst, the polymerization rate increases.
If the living polymerization is possible to occur, thus the termination or transfer also could be occurred.
O (CH2)4 O+
-A+ O
(CH2)4
(CH2)4
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Cationic Polymerization(4)Kinetics
I + ZY K Y+(IZ)
-
initiator coinitiator
Y+(IZ)
-+ M
ki YM+(IZ)
-
nM O+
+ O Mn O (CH2)4O
CH2 C+
H
R
[SnCl4OH]- + CH2 CH
Rstrong initiator
CH2CHCH2
R
]][][[]][)([ MZYIKkMIZYkR iii
]][[ MMkR pp
Initiation
ex) styrene, stannic-chloride-H2O System [SnCl4OH-]H+
Propagation – can has a low activation energy and can be polymerized rapidly
or
Simple propagation reaction
The total rate of polymerization may actually increases by decreasing the temperature, which means that the termination has a high activation energy.