3524
S.-d. Mun et al. / Journal of Organometallic Chemistry 692 (2007) 3519–3525
Table 2
graphic Data Centre, 12 Union Road, Cambridge CB2
1EZ, UK; fax: (+44) 1223-336-033; or e-mail: deposit@
ccdc.cam.ac.uk.
Ring opening polymerization of l-LA using 5–8
Entry
Catalyst
Yield (%)c Tm (ꢁC)d Men
Mwe
PDIe
1a
2b
3a
4b
5a
6b
7a
8b
a
5
95.8
95.1
96.2
93.8
93.8
91.0
90.3
89.6
166.8
167.3
161.1
163.9
161.2
163.0
161.0
164.5
10600 23800 2.25
14800 24100 1.63
8300 15300 1.84
7300 13000 1.80
6200 11700 1.90
6900 11900 1.72
6200 12000 1.93
7200 12200 1.69
6
7
8
Acknowledgements
This work was supported by the research grant of the
Chungbuk National University in 2005. The authors
acknowledge PAL for beam line use (Grant 2006-3041-10).
Bulk polymerization condition: Tp = 130 ꢁC, [LA]/[Ti] = 200, cata-
lysts = 0.05 mmol, time = 10 h.
b
References
Solution polymerization condition: Tp = 100 ꢁC, [LA]/[Ti] = 200, cat-
alysts = 0.05 mmol, time = 10 h, toluene 1 ml.
c
Isolated yield.
Determined by DSC.
Determined by GPC.
[1] (a) J.G. Verkade, Acc. Chem. Res. 26 (1993) 483;
(b) J.G. Verkade, Coord. Chem. Rev. 137 (1994) 233;
(c) R.R. Holmes, Chem. Rev. 96 (1996) 927.
d
e
[2] (a) C.L. Frye, G.E. Vogel, J.A. Hall, J. Am. Chem. Soc. 83 (1961) 996;
(b) B. de Ruiter, R.A. Jacobson, J.G. Verkade, Inorg. Chem. 29 (1990)
1065;
by bulk and solution polymerization using 5–8 are in the
range Mw = 11700–23800 with Mw/Mn = 1.84–2.25 and
Mw = 11900–24100 with Mw/Mn = 1.63–1.80, respec-
tively. Not unexpectedly, the polydispersity index (PDI)
values of PLA obtained by the solution polymerization
are narrower than that prepared by the bulk polymeriza-
tion. Interestingly, Mn values for PLA obtained from solu-
tion polymerization are even higher than that from bulk
polymerization except for 6. Furthermore, catalysts 5–8
yield polymers with somewhat large polydispersities and
low molecular weights. This may be attributed to a rate
of initiation that is slower than the rate of polymer propa-
gation, thus allowing more time for the occurrence of
transesterification reactions during propagation. Although
the polymerizations were carried out at an elevated temper-
ature, the PLA polydispersity indices are in an acceptable
range (1.63–2.25 in Table 2). In addition, all catalytic sys-
tems afford PLA with Tm values of greater than 161.0 ꢁC,
even at a high polymerization temperature. Interestingly,
Tm of PLA obtained from the solution polymerization is
higher than Tm from the bulk polymerization. It appears
that the initiating group is the highly bulky di-i-Pr-pheno-
(c) M.A.H. Laramay, J.G. Verkade, J. Am. Chem. Soc. 112 (1990)
9421;
(d) S.K. Xi, H. Schmidt, C. Lensink, S. Kim, D. Wintergrass, L.M.
Daniels, R.A. Jacobson, J.G. Verkade, Inorg. Chem. 29 (1990) 2214;
(e) J. Woning, J.G. Verkade, J. Am. Chem. Soc. 113 (1991) 944.
[3] (a) H.J. Cohen, J. Organomet. Chem. 9 (1967) 177;
(b) R.L. Harlow, Acta Crystallogr., Sect. C 39 (1983) 1344;
(c) R. Taube, P. Knoth, Z. Anorg. Allg. Chem. 581 (1990) 89;
(d) W.M.B.P. Menge, J.G. Verkade, Inorg. Chem. 30 (1991) 4628;
(e) A.A. Naiini, W.M.B.P. Menge, J.G. Verkade, Inorg. Chem. 30
(1991) 5009;
(f) A.A. Naiini, S.L. Ringrose, Y. Su, R.A. Jacobson, J.G. Verkade,
Inorg. Chem. 32 (1993) 1290;
(g) W.A. Nugent, T.V. RajanBabu, M.J. Burk, Science 259 (1993)
479;
(h) W.A. Nugent, R.L. Harlow, J. Am. Chem. Soc. 116 (1994) 6142;
(i) Y. Kim, E. Hong, M.H. Lee, J. Kim, Y. Han, Y. Do,
Organometallics 18 (1999) 36;
(j) T. Kemmitt, N.I. Al-Salim, G.J. Gainsford, Inorg. Chem. 39
(2000) 6067;
(k) Y. Kim, Y. Han, J.W. Hwang, M.W. Kim, Y. Do, Organomet-
allics 21 (2002) 1127;
(l) Y. Kim, G.K. Jnaneshwara, J.G. Verkade, Inorg. Chem. 42 (2003)
1437;
(m) A.G. Maestri, S.N. Brown, Inorg. Chem. 43 (2004) 6995;
(n) Y. Kim, Y. Do, J. Organomet. Chem. 655 (2002) 186;
(o) M.G. Voronkov, Z.A. Ovchinnikova, V.P. Baryshok, Zhurnal
Obshchei Khimii 57 (1987) 2643;
(p) G. Boche, K. Mobus, K. Harms, M. Marsch, J. Am. Chem. Soc.
118 (1996) 2770;
1
late group, which was shown by H NMR spectra of the
isolated PLA samples. However, no dependence of poly-
mer yield on the degree of polymerization or molecular
weight support that not-simple ROP mechanism with com-
plicated transesterification for our catalytic system is
involved.
(q) S.-d. Mun, Y. Hong, Y. Kim, Bull. Korean Chem. Soc. 28 (2007)
698.
In summary, we have synthesized a novel series of four
titanatranes with controlled steric hindrance in a stepwise
fashion. These complexes function, with a trend in effi-
ciency roughly decreasing the number of methyl groups
in tetradentate ligand they possess, as single-site initiators
for the ring opening polymerization of l-LA.
[4] D.F. Shriver, The Manipulation of Air-Sensitive Compounds,
McGraw-Hill, New York, 1969.
[5] W.L.F. Armarego, C.L.L. Chai, In Purification of Laboratory
Chemicals, 5th ed., Elsevier, New York, 2003.
[6] Y. Kim, J.G. Verkade, Organometallics 21 (2002) 2395.
[7] All software and sources of the scattering factors are contained in the
SHELXTL (version 5.1) program library (G. Sheldrick, Bruker Analyt-
ical X-Ray Systems, Madison, WI).
[8] (a) C.C. Cummins, R.R. Schrock, W.M. Davis, Organometallics 11
(1992) 1452;
5. Supplementary material
(b) C.C. Cummins, J. Lee, R.R. Schrock, W.D. Davis, Angew.
Chem., Int. Ed. Engl. 31 (1992) 1501;
(c) M. Schubart, L. O’Dwyer, L.H. Gade, W.-S. Li, M. McPartlin,
Inorg. Chem. 33 (1994) 3893;
CCDC 638141 and 638142 contain the supplementary
crystallographic data for this 6 and 7. These data can be