C O MMU N I C A T I O N S
chains that later segregate into pure PNIPAM and PDEAM. In other
words, early aggregate formation most likely involves the mixing
of PNIPAM and PDEAM. Such mixed aggregates would have
higher entropy than the corresponding structures containing only
one type of polymer. The difference in entropy between the pure
and mixed systems should lead to a lower transition state free
energy, ∆Gq, to precipitation for the mixed complexes. Interestingly,
this initial precipitate then begins to phase segregate into pure
PNIPAM and PDEAM particles presumably on enthalpic grounds.
To verify these assumptions, DSC studies of PNIPAM and PDEAM
were performed as a function of mole fraction of PNIPAM. The
results showed that the onset to the phase transition came at a lower
temperature for mixed systems by amounts that exactly matched
the data in Figure 4. Furthermore, the overall enthalpy for the entire
precipitation process rose continuously as the amount of PNIPAM
was increased. This latter result is consistent with the notion that
the two polymers must ultimately segregate upon undergoing the
phase transition and that PNIPAM has the higher phase transition
enthalpy. The DSC results are provided in the Supporting Informa-
tion.
Figure 3. Kinetic studies of PNIPAM and PDEAM mixtures. PNIPAM
and PDEAM were mixed as 1:1.5 molar ratio in DI water.
The methods and results described above provide a new and rapid
protocol for studying the precipitation/solubilization behavior of
thermoresponsive polymers with minute quantities of materials and
excellent signal-to-noise ratios. Indeed, the high throughput potential
for this method should make it possible in the near future to collect
large amounts of data with great temperature precision quite easily.
Figure 4. Plots of the initial LCST at different mole fractions of PNIPAM
for PNIPAM and PDEAM mixtures. The solid line represents a fit to the
data.
Acknowledgment. We thank the National Science Foundation
(DMR-9977911) (D.E.B.), the Army Research Office (DAAD19-
01-1-0346) (P.S.C.), and the Office of Naval Research (YIP Award
NOOO14-00-1-0664) (P.S.C.). P.S.C. also acknowledges the fol-
lowing: Beckman Young Investigator Award, an Alfred P. Sloan
Fellowship, and a Nontenured Faculty Award from 3M Corporation.
H.M. acknowledges support from a Proctor & Gamble Fellowship.
different polymer solutions with known LCSTs as internal controls
to aid in temperature readout and prevent systematic errors between
experiments.
Since the clouding curves of macromolecules in solution can be
obtained with good temperature resolution over relatively short
times, the time-dependent evolution of the clouding process was
studied simply by recording a series of time-lapse images of a given
sample with a standard CCD camera. When this was done for a
mixed solution of PNIPAM and PDEAM, a series of time-
dependent phenomena were revealed (Figure 3). The first image
was taken immediately after the mixed polymer solution was placed
over the temperature gradient. As can be seen, the original clouding
curve of the mixture appeared to be smooth. After 6 min, however,
a higher temperature kink appeared in the curve. This further
evolved into a pronounced dip after 9 min. At this point, cycling
between the latter two stages occurred; however, the initial sequence
of clouding behavior as well as the migration of the LCST toward
higher temperature were reproducible over many samples and within
a given sample. Reversibility within the same sample was observed
when the TLow and the THigh sides of the tube were switched.
To investigate the significance of the 0 min conditions, experi-
ments for mixtures of PNIPAM and PDEAM were carried out as
a function of mole fraction of PNIPAM. A plot of the nascent LCST
temperature is shown in Figure 4. The results bear a striking
resemblance to the curve obtained for the Gibbs free energy of
mixing of two substances: G ) ø1G1 + ø2G2 + nRT(ø1 ln ø1 + ø2
ln ø2). In this case, G1 and G2 are the Gibbs free energies of pure
substances 1 and 2, respectively. ø1 and ø2 are the mole fractions
of substances 1 and 2, respectively. This correlation implies that
the aggregation process involves the rapid (i.e., kinetically con-
trolled) formation of aggregates of a small number of polymer
Supporting Information Available: Experimental procedures and
characterization data (PDF). This material is available free of charge
References
(1) Mariagnanam, V. M.; Zhang, L.; Bergbreiter, D. E. AdV. Mater. 1995, 7,
69-71.
(2) Huang, X.; Witte, K. L.; Bergbreiter, D. E.; Wong, C.-H. AdV. Synth.
Catal. 2001, 343, 675-681.
(3) Hoffman, A. S. J. Controlled Release 1987, 6, 297-305.
(4) Ito, T.; Hioki, T.; Yamaguchi, T.; Shinbo, T.; Nakao, S.; Kimura, S. J.
Am. Chem. Soc. 2002, 124, 7840-7846.
(5) Rao, G. V. R.; Balamurugan, S.; Meyer, D. E.; Chilkoti, A.; Lopez, G. P.
Langmuir 2002, 18, 1819-1824.
(6) Schild, H. G. Prog. Polym. Sci. 1992, 17, 163-249.
(7) Urry, D. W. J. Phys. Chem. B 1997, 101, 11007-11028.
(8) Urry, D. W.; Starcher, B.; Partridg, S. M. Nature 1969, 222, 795.
(9) Badiger, M. V.; Lele, A. K.; Bhalerao, V. S.; Varghese, S.; Mashelkar,
R. A. J. Chem. Phys. 1998, 109, 1175-1184.
(10) Winnik, F. M. Polymer 1990, 31, 2125.
(11) Boutris, C.; Chatzi, E. G.; Kiparissides, C. Polymer 1997, 38, 2567-
2570.
(12) Taylor, L. D.; Cerankowski, L. D. J. Polym. Sci.: Polym. Chem. Ed. 1975,
13, 2551-2570.
(13) Freitag, R.; Baltes, T.; Eggert, M. J. Polym. Sci.: Part A: Polym. Chem.
1994, 32, 3019-3030.
(14) (a) Mao, H.; Yang, T.; Cremer, P. S. J. Am. Chem. Soc. 2002, 124, 4432-
4435. (b) Mao, H.; Holden, M. A.; You, M.; Cremer, P. S. Anal. Chem.
2002, 74, 5071-5075.
(15) Incropera, F. P.; DeWitt, D. P. Fundamentals of Heat and Mass Transfer,
3rd ed.; John Wiley & Sons: New York, 1990.
JA029691K
9
J. AM. CHEM. SOC. VOL. 125, NO. 10, 2003 2851