Understanding Atom Transfer Radical Polymerization
A R T I C L E S
Scheme 1. Proposed Mechanism for Atom Transfer Radical
Polymerization
Equation 4 must be used when C0 ) I0:
2
C0
C0
1
F(Y) )
+
+
)
3(C0 - Y)3 (C0 - Y)2
C0 - Y
1
3C0
2ktKATRP2t +
(4)
crucial for deeper understanding of this catalytic system and for
optimal catalyst selection, especially for newly developed ATRP
systems that use low concentrations of the catalyst CuIY/Ln (i.e.,
[CuI] on the order of ppm).26,27 Small values of KATRP (∼10-9 to
∼10-4) are required in order to maintain a low radical concentra-
In either case, a plot of F(Y) versus t should give a straight
line, and the equilibrium constant for the reaction can be
calculated from the slope (m) using the formula KATRP ) (m/
2kt)1/2. In our calculations, a kt value of ) 2.5 × 109 M-1 s-1
(obtained for model small radicals in acetonitrile at 22 °C) was
used.33 UV-vis spectrometry and gas chromatography were
used to follow the evolution of the CuII species and the initiator
concentration, respectively, for several catalysts and alkyl halide
initiators, from which the corresponding values of KATRP were
determined.30
In this work, we present a large set of KATRP values
determined for ATRP using various alkyl halide initiators and
Cu catalysts with nitrogen-based ligands, and we discuss how
the structures of the ligands and initiators affect the KATRP
values. Values of KATRP that were not readily available were
extrapolated by assuming similar selectivities of alkyl halides
for various complexes.
tion and minimize termination reactions. The apparent KATRP
app
(K
) KATRP/[CuII]) can be estimated from the kinetic plot
ATRP
of ln([M]0/[M]) versus time for an ATRP experiment;28
however, precise values for KATRP are difficult to measure during
polymerization because CuII concentrations continuously change
as a result of the persistent radical effect (PRE), which is
described in the Results and Discussion.29
[M]0
[M]t
kpKATRP[PmX][CuI]
[CuII]
ln
)
t
(1)
(2)
(
)
M
kp([RX]0 - [RX])
w ) 1 +
+
- 1
1
DPn
2
p
(
)
kdeact[CuII]
(
)
Mn
Our group recently modified Fischer’s original equations for
the PRE and successfully applied the new equations to determine
KATRP values for various ATRP catalytic systems by monitoring
the amount of accumulated deactivator as a function of time.30,31
Fischer’s original equations, which assume constant values of
the catalyst and initiator concentrations, correctly describe the
PRE up to only ∼10% conversion of CuI to CuII, and
Experimental Section
Materials. N-(n-Propyl)pyridylmethanimine (NPPMI) and N-(n-
octyl)pyridylmethanimine (NOPMI) were synthesized by condensa-
tion of n-propylamine and n-octylamine, respectively, with pyridine-
2-carboxaldehyde.34 Tris(2-(dimethylamino)ethyl)amine (Me6TREN)
was synthesized by methylation of tris(2-aminoethyl)amine (TREN).35
Tris(2-(diethylamino)ethyl)amine (Et6TREN) was synthesized accord-
ing to the literature.36 Tris(2-(di-(2-cyanoethyl)amino)ethyl)amine
(AN6TREN), tris(2-(di-(2-(methoxycarbonyl)ethyl)amino)ethyl)amine
(MA6TREN), and tris(2-(di-(2-(n-butoxycarbonyl)ethyl)amino)ethyl)-
amine (BA6TREN) were synthesized by Michael addition of TREN
to acrylonitrile, methyl acrylate, and n-butyl acrylate, respectively.37
2,5,9,12-Tetramethyl-2,5,9,12-tetraazatridecane (N4[2,3,2]),38 2,6,9,13-
tetramethyl-2,6,9,13-tetraazatetradecane (N4[3,2,3]),38 4,11-dimethyl-
1,4,8,11-tetraazabicyclo[6.6.2]hexadecane (Cyclam-B),39,40 N′,N′′-
dimethyl-N′,N′′-bis((pyridin-2-yl)methyl)ethane-1,2-diamine (BPED),41
4,4′-di-(5-nonyl)-2,2′-bipyridine (dNbpy),42 and tris[(2-pyridyl)methyl]-
amine (TPMA)43 were synthesized according to the literature. 2,5,8,12-
Tetramethyl-2,5,8,12-tetraazatridecane (N4[2,2,3]) was synthesized by
a similar methylation of 2,5,8,12-tetraazatridecane tetrahydrochloride
salt with formaldehyde and formic acid and distilled under reduced
consequently, they can only be used in the determination of
32
relatively small values of KATRP
.
For greater conversion of
CuI to CuII (>10%) and larger values of KATRP (>10-7),
modified equations that take into account the changes in catalyst
and initiator concentrations should be used, as shown in eqs 3
and 4, in which I0 ) [RX]0, C0 ) [CuI]0, and Y ) [CuII].30
Equation 3 applies when C0 * I0:
2
I0C0
I0 - Y
C0 - Y
1
2
F(Y) )
+
ln
+
(
)
2
(
)
C0 - I0
I0C0(C0 - I0)
[
C0 (I0 - Y)
1
) 2ktKATRP2t + c′ (3)
2
]
I0 (C0 - Y)
where kt is the termination rate constant and c′ is given by the
(33) Fischer, H.; Radom, L. Angew. Chem., Int. Ed. 2001, 40, 1340–1371.
(34) Haddleton, D. M.; Clark, A. J.; Crossman, M. C.; Duncalf, D. J.;
Heming, A. M.; Morsley, S. R.; Shooter, A. J. Chem. Commun 1997,
1173.
(35) Queffelec, J.; Gaynor, S. G.; Matyjaszewski, K. Macromolecules 2000,
33, 8629–8639.
(36) Inoue, Y.; Matyjaszewski, K. Macromolecules 2004, 37, 4014–4021.
(37) Zeng, F.; Shen, Y.; Zhu, S.; Pelton, R. Macromolecules 2000, 33,
1628–1635.
expression
2
I0C0
I0
1
2
1
c′ )
+
ln
I0C0(C0 - I0) C0
+
(
)
2
2
C0 - I0
[
]
C0 I0
I0 C0
(26) Matyjaszewski, K.; Jakubowski, W.; Min, K.; Tang, W.; Huang, J.;
Braunecker, W. A.; Tsarevsky, N. V. Proc. Natl. Acad. Sci. U.S.A.
2006, 103, 15309–15314.
(38) Golub, G.; Cohen, H.; Paoletti, P.; Bencini, A.; Messori, L.; Bertini,
I.; Meyerstein, D. J. Am. Chem. Soc. 1995, 117, 8353–8361.
(39) Wong, E. H.; Weisman, G. R.; Hill, D. C.; Reed, D. P.; Rogers, M. E.;
Condon, J. S.; Fagan, M. A.; Calabrese, J. C.; Lam, K.-C.; Guzei,
I. A.; Rheingold, A. L. J. Am. Chem. Soc. 2000, 122, 10561–10572.
(40) Tsarevsky, N. V.; Braunecker, W. A.; Tang, W.; Brooks, S. J.;
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(29) Fischer, H. Chem. ReV. 2001, 101, 3581–3610.
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J. AM. CHEM. SOC. VOL. 130, NO. 32, 2008 10703