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Comparison of dissolution and mutual diffusioncoefficients during dissolution of poly(methylmethacrylate) films †
S Ugur and O Pekcan*Istanbul Technical University, Department of Physics, 80626, Maslak Istanbul, Turkey
Abstract: Steady state ¯uorescence measurements have been used for studying the dissolution of
polymer ®lms. These ®lms are formed by free radical polymerization of methyl methacrylate (MMA)
in which pyrene (Py) was introduced as a ¯uorescence probe. Dissolution of poly(methyl methacrylate)
(PMMA) ®lms in chloroform±heptane mixtures were monitored in real-time by the Py ¯uorescence
intensity change. Dissolution coef®cients Dd of Py molecules were measured during dissolution of
PMMA ®lms, and found to be about 10ÿ6cm2sÿ1. After dissolution, ¯uorescence quenching
measurements were performed and the Stern±Volmer equation was employed to measure the mutual
diffusion coef®cients of heptane (Dh) and Py (DPy) molecules; these were found to be about 10ÿ5cm2sÿ1.
# 1999 Society of Chemical Industry
Keywords: ¯uorescence; dissolution; diffusion; Stern±Volmer
INTRODUCTIONDiffusion mechanisms and the determination of diffu-
sion coef®cients (D) of small molecules in polymeric
systems have been of interest over the last two decades.
Veksli and Miller1 investigated non-solvent penetra-
tion into poly(methyl methacrylate) (PMMA) and
polystrene (PS) latex particles using ESR. MacCallum
and Rudkin2 studied the quenching of naphthalene
¯uorescence in PMMA by diffusing oxygen molecules
in thin ®lm samples. Winnik and co-workers3
measured D values in phenanthrene labelled, non-
aqueous dispersions (AND) of poly(vinly acetate)
(PVAc) latex particles, stabilized by poly(2-ethyl-hexyl
methacrylate) PEHMA, using both steady-state and
transient ¯uorescence methods. D =1.91�10ÿ5cm2sÿ1 was obtained for oxygen diffusing in
cyclohexane swollen PEHMA phase by employing
¯uorescence quenching. The ESR method, based on
the scavenging of radicals produced by high energy
g-irradiation of PMMA by oxygen was used for
measurement of the diffusion coef®cient in PMMA.4
D =3.4�10ÿ8cm2sÿ1 was determined for diffusing
oxygen into irradiated PMMA spheres. The oxygen
uptake of g-irradiated spherical PVAc particles was
investigated from changes in the intensity of ESR
signal5 and the value of D for diffusing oxygen so
obtained was 4.5�10ÿ8cm2sÿ1. Diffusion of solvent
molecules into AND of PMMA sterically stabilized by
polyisobutylene (PIB) was studied by ESR, employing
the spin-probe technique.6 Fickian type diffusion of
solvent molecules into PMMA latex particles was
observed and D values were found to be around
10ÿ15cm2sÿ1 in various solvents. Similar D values
were observed when the above technique was applied
to AND of PVAc latex particles sterically stabilized by
PEHMA in various solvents.7
Fluorescence quenching and depolarization
methods have been used for penetration and dissolu-
tion studies in solid polymers.8,9 In situ ¯uoresence
quenching in conjunction with laser interferometry
was used to investigate the dissolution of PMMA ®lms
in various solvents.10 A real-time, non-destructive
method for monitoring small molecule diffusion in
polymer ®lms was developed.11,12 This method is
based on the detection of excited ¯uorescence mol-
ecules desorbing from a polymer ®lm into a solution in
which the ®lm is placed.11±14 Recently, we have
reported a steady state ¯uorescence (SSF) study on
the dissolution of annealed latex ®lms using realtime
monitoring of ¯uorescence probes.15
The penetration of solvent molecules into glassy
polymers often does not proceed according to the
Fickian diffusion model.16,17 Penetration not
described by the Fickian model is called anomalous
diffusion, where the rate of transport is entirely
controlled by polymer relaxation. This transport
mechanism is termed case II, in contrast to Fickian
diffusion which is called case I. In the case II diffusion
model, the second step is the rate limiting step which
predicts a linear dependence of the change in ®lm
thickness with time. The ®rst and third steps, however,
follow a case I diffusion model, where the ®rst one is
Polymer International Polym Int 48:485±490 (1999)
* Correspondence to: O Pekcan, Istanbul Technical University, Department of Physics, 80626, Maslak Istanbul Turkey† This article is dedicated to the 225th anniversary of Istanbul Technical University(Received 19 August 1998; revised version 22 December 1998; accepted 4 February 1998)
# 1999 Society of Chemical Industry. Polym Int 0959±8103/99/$17.50 485
the absorption of solvent molecules by the glassy ®lm
and the third is the dissolution of polymer chains from
the gel layer. The fouth and ®nal step of polymer
dissolution involves diffusion of polymer molecules
throughout the liquid phase. In this work we are
mainly interested in the third and fourth steps of the
dissolution phenomenon.
Polymer dissolution can be affected by various
parameters, including solvent quality, polymer mol-
ecular weight, solvent thermodynamic compatibility,
agitation and temperature. In this work, the effect of
solvent quality on polymer dissolution has been
studied using the SSF method by real-time monitoring
of the (Py) intensity change. Chloroform and heptane
mixtures were used as dissolution agents. In situ SSF
experiments were performed to observe the dissolution
processes. Dissolution experiments were designed so
that Py molecules, dissolving from ®lms, were detected
in real-time monitoring of SSF intensity. Dissolution
coef®cients, Dd were measured using curves of
intensity versus time. Direct illumination of the ®lm
sample was avoided, during the in situ dissolution
experiments. After dissolution experiments were per-
formed, the quenching effect on Py molecules was
detected to measure the mutual diffusion coef®cient,
Dm, using the Stern±Volmer model.
THEORETICAL CONSIDERATIONSFickian DissolutionWe employ the classical diffusion model to interpret
the results of polymer dissolution experiments. This
model includes only case I diffusion kinetics, because
gelation during dissolution was eliminated using
continuous agitation. The case I or Fickian diffusion
model includes the solution of a unidirectional
diffusion equation for a set of boundary conditions
set by Crank and Park.18 For a constant diffusion
coef®cient D and ®xed boundary conditions, the
absorption and dissolution transport in and out of a
thin slab is given by the relation
M1
M1� 1ÿ 8
�2
X1n�0
1
�2n� 1�2 exp�ÿ�2n� 1�2D�2t
d2�
�1�Here, Mt represents the amount of materials absorbed
or dissolved at time t, M? is the equilbrium amount of
material, and d is the thickness of the slab; n comes
from the solution of the diffusion equation in the form
of a trigonometrical series.
Finite concentration fluorescence quenchingThe theories of ¯uorescence quenching with and with-
out diffusion are well established.19 A chromophore A
in its ground state is converted to an electronically
excited state A* by absorption of a photon hnex, i.e.
h�ex � Aÿ!A�
The excited state A* decays to A by producing a
¯uorescence with a lifetime t0, through
A�ÿ!A� h�fl
or the excited state A* can be quenched by collision
with quencher Q at a rate k, described by
A� �Qÿ!A�Q
and, even in the absence of excitation, A and Q are
assumed capable of reacting to form a complex AQ
with a rate kf
A�Q ÿÿ! AQ
and AQ decays with rate kb.
The related rate equations governing the above
processes are solved neglecting diffusion, and the
following equation is obtained:20
I0
I� 1� �k�0 �K��Q� � k�0K �Q�2 �2�
which is known as Stern±Volmer law in the absence of
diffusion control. Here I0 and I present the intensities
of a chromophore with and without quencher and
K =kf/kb.
The Stern±Volmer law in the presence of diffusion
at in®nite concentration can be obtained by solving the
many particle diffusion equation with reactive terms;
Figure 1. Dissolution cell as used in LS-50 Perkin Elmer spectrofluorimeter(a) before and (b) after dissolution. (I0 and Ip are the excitation and emissionintensities at 345nm and 375nm, respectively).
486 Polym Int 48:485±490 (1999)
SË UgÆur, OÈ Pekcan
for the probability densities of A* and Q and equation
(2) it is reproduced20 with
k � 4�NADmpR
1000�Mÿ1sÿ1� �3�
where Dm=DPy�Dh is the sum of the mutual diffusion
coef®cients of chromophore (Py) and quencher (hep-
tane), respectively, R =RPy�Rh is the sum of their
interaction radii, NA is Avagadro's number, and p is a
factor describing the reaction probability per collision.
Here DPy and Dh are the mutual diffusion coef®-
cients and RPy and Rh are the radii of Py and heptane
molecules, respectively. At ®nite concentration, ie
quenchers present in suf®ciently large concentrations
(typically [Q]=0.1M while [A]=10ÿ4M), the com-
plex formation can be neglected and eqn (2) reduces to
the form
I0
I� 1� k�0�Q� �4�
EXPERIMENTALMonomer MMA (Merck) was freed from inhibitor by
shaking with a 1.79M aqueous KOH solution,
washing with water and drying over sodium sulphate.
It was then distilled under reduced pressure over
copper chloride. The initiator, 2,2'-azobisisobutyro-
nitrile (AIBN) (Merck, Detroit), was recrystallized
twice from methanol. The solvents chloroform and
heptane (Merck) were used as received.
The radical polymerization of MMA was performed
in bulk in the presence of AIBN as an initiator. AIBN
(1.59�10ÿ2 M) and Py (4�10ÿ4M) were dissolved in
MMA and this solution was poured into round glass
tubes of 15mm internal diameter. Before polymeriza-
tion, each solution was deoxygenated by bubbling
nitrogen for 10min. Radical polymerization of MMA
was performed at 65�3°C. After polymerization was
complete, the tube was broken. Disc shaped, thin
samples (around 0.2cm) were cut for the swelling and
dissolution experiments.
In situ ¯uorescence experiments were performed
using a Perkin Elmer (London) LS-50 spectro¯uori-
meter. All measurements were made at the 90° posi-
tion and the slit width was kept at 2.5mm. Dissolution
experiments were performed in a 1cm�1cm quartz
cell which was placed in the spectro¯uorimeter. The
¯uorescence emission was monitored so that ®lm
samples were not illuminated by the excitation light.
Disc shaped samples were placed on one side of a
quartz cell ®lled with chloroform±heptane mixture; the
cell was then illuminated with 345nm excitation light.
The pyrene ¯uorescence intensity, IP, was monitored
at 375nm during dissolution using the `time drive'
mode of the spectro¯uorimeter. Py emission was
Figure 2. Pyrene intensity Ip versusdissolution time for film samples dissolvedin various chloroform–heptane mixtures athigh stirring speed. Samples a–g are listedin Table 1.
Polym Int 48:485±490 (1999) 487
Dissolution of poly(methyl methacrylate) ®lms
recorded continuously at 375nm as a function of time.
The cell and the sample position are presented in Fig
1. Here the 1cm�1cm quartz cell was equipped with
a magnetic stirrer at the bottom. The Py ¯uorescence
emission was monitored at a 90° angle as shown in
Fig 1.
RESULTS AND DISCUSSIONDissolution coefficientsPlots of Py intensity Ip versus dissolution time for
various chloroform±heptane mixtures at high stirring
speed are shown in Fig 2. Samples are listed in Table
1. It is seen that as the heptane content increases,
curves reach a plateau at longer times. In other words,
PMMA ®lms dissolve more slowly in solutions with
higher heptane content. After dissolution was com-
plete SSF spectra of Py were taken in various chloro-
form±heptane mixtures. Figure 3 presents the results
for the samples having 10, 30 and 70% heptane
content (mixtures b, d andg, respectively). No shift is
observed at the maximum Py intensity. Smaller
intensity values in Py spectra for high heptane content
mixtures may be explained by collisional quenching in
the low viscous environment (3.8�10ÿ4 Pas) of
heptane, in which excited Py can be quenched more
easily than in a high chloroform content mixture,21
which has relatively high viscosity (5.8�10ÿ4 Pas).
The curves in Fig 2 seem to follow a case I (Fickian)
diffusion model. In processing the dissolution data, it
is assumed that Ip is proportional to the number of Py
molecules dissolving from the PMMA ®lm. The
logarithmic form of eqn (1) is written for n =0, with
Ad=Ddp2/d2 and Bd=ln;(8/p2) as follows
ln�1ÿ Ip
Ip1� � Bd ÿ Adt �5�
Here, Ip? represents the number of Py molecules at
equilibrium, Dd is the dissolution coef®cient and d is
the thickness of the PMMA disc. Figure 4b, d andg
shows the dissolution curves for mixtures having 10,
Figure 3. Emission spectra of pyrene (Py)in 10, 30 and 70% heptane mixtures withchloroform.
Table 1. Film thickness and dissolution coefficients for samples in variouschloroform–heptane mixtures
Samples Heptane (%) Dd�10ÿ6 (cm2/sÿ1) d (cm)
a 0 3.73 0.196
b 10 2.81 0.182
c 20 3.48 0.191
d 30 1.93 0.169
e 40 2.81 0.206
f 50 2.25 0.185
g 70 1.59 0.233
a Dd values were obtained by ®tting eqn (5) to the data in Fig 2. Here,
chloroform±heptane mixtures are used as dissolution agents, and high
speed stirring was employed during experiments; d is the ®lm thickness for
each sample.
488 Polym Int 48:485±490 (1999)
SË UgÆur, OÈ Pekcan
30 and 70% heptane content (b, d andg, respectively)
digitized for numerical treatment according to eqn (5).
All curves in Fig 4 present linear dependence with
time, con®rming our assumption of relationship with a
diffusion model. When these linear curves in Fig 4 are
compared to computations using eqn (5), dissolution
coef®cients Dd for Py molecules are obtained. These
are listed in Table 1 with values for other samples. Dd
values for the PMMA discs dissolved in mixtures
having high heptane content were smaller than those
obtained in low heptane mixtures. These results are
expected for PMMA dissolved in a solvent mixture
which contains a greater amount of non-solvent.
In general, Dd values obtained in these experiments
are three orders of magnitude larger than that found in
our recent work with PMMA latex ®lms.15 In this
study the PMMA discs were 200 times thicker than the
latex ®lms. Thickness effects were observed by
Enscore et al16 where 300-fold larger polystyrene
spheres caused twofold larger dissolution coef®cients
for hexane. This was explained by formation of a
spherical shell during the absorption process. In our
case, however, the gel layer is removed from the
surface of the PMMA discs by stirring. Smaller
dissolution coef®cients in latex ®lms compared to
those of PMMA discs can be explained by the
annealing effect, which resulted in the formation of
mechanically strong ®lms. Most probably, PMMA
discs used in this work have greater free volumes than
annealed latex ®lms. In fact, during latex ®lm
dissolution, a long gelation period (case II diffusion)
was observed at early times. However, the PMMA
discs used here show dissolution by following pure
Fickian (case I) behaviour, or the stirring effect may
prevent us observing case II diffusion. In other words,
the gel layer is immediately removed from the surface
of the PMMA disc by stirring, so that case I diffusion
dominates the dissolution process.
Mutual diffusion coefficientThe results in Fig 3 can be explained by heptane
quenching of excited Py molecules. The Ip of dissolved
samples decreases as the heptane content increases,
indicating effective heptane quenching of the excited
state of Py. These data can be analysed in terms of the
Stern±Volmer model (eqn (4)) by assuming that
collisional quenching of Py becomes very active in
the presence of diffusion at large concentrations of
heptane. I0/Ip is plotted as a function of heptane
(quencher) concentration in Fig 5. In a well behaved
system, such a plot yields a slope equal to kt0 and the
straight line passes through 1.0. When t0 is known, the
magnitude of the collisional quenching rate constant kcan be determined. The linearity of the plot in Fig 5
Figure 4. Plot of digitized data from Fig 2, which obey the relationln(1ÿIp/Ip?)=BdÿAdt, where t is the dissolution time. Curves b, d and grepresent the data for samples containing 10, 30 and 70% heptane,respectively.
Figure 5. Stern–Volmer plot of Io /Ip versus quencher (heptane)concentration [Q] in chloroform.
Polym Int 48:485±490 (1999) 489
Dissolution of poly(methyl methacrylate) ®lms
indicates that the Stern±Volmer law is obeyed and
suggests that unique values of k and t0 exist. When
data in Fig 5 are ®tted to eqn (4), the rate constant for
heptane quenching of Py is found to be
k =1.22�107Mÿ1sÿ1, where t0=20ns was taken as
measured in the presence of oxygen at room tempera-
ture.22 The sum of mutual diffusion coef®cients
calculated with eqn (3) from this k value is found to
be Dm=2.05�10ÿ5cm2sÿ1, where R is taken as
7.86AÊ (ie RPy=3.98AÊ and Rh=3.88 AÊ ) and p is
assumed to be unity. Here it is assumed that heptane
and Py molecules are homogeneously distributed in
chloroform. Because the radii of Py and heptane
molecules are almost equal, it is reasonable to
approximate the mutual diffusion coef®cients (DPy
and Dh) as 1.02�10ÿ5cm2sÿ1 for both molecules.
These observed diffusion coef®cients are typical for a
chromophore in an organic solvent at room tempera-
ture.23±25 If one imagines that the gel layer from the
swollen polymer ®lm is taken away rapidly due to the
effect of vigorous stirring, an order of magnitude
difference between dissolution (Dd) and mutual (DPy
and Dh) diffusion coef®cients seems to be reasonable.
Here the absorption of heptane molecules is immedi-
ately followed by dissolution of Py molecules
(Dd�10ÿ6cm2sÿ1) and it can be assumed that
dissolution of PMMA chains occurs with the same
rate as that of Py.
CONCLUSIONSThis work studied the dynamical parameters of the last
two steps of polymer dissolution, ie dissolution of
polymer chains into a liquid reservoir and diffusion in a
liquid reservoir, respectively. Further suitable work
can be achieved using dye labelled polymer chains and
the ¯uorescence technique.
ACKNOWLEDGEMENTSWe wish to thank the referees for their critical and
constructive reading of our manuscript; we gained a lot
from their comments and objections.
REFERENCES1 Veksli Z and Miller WG, J Polym Sci 54:299 (1976).
2 MacCallum JR and Rudkin AL, Eur Polym J 14:655 (1976).
3 Egan LS, Winnik MA and Croucher MD, Polym Eng Sci 26:15
(1986).
4 Kaptan Y, Pekcan OÈ , Arca E and GuÈven O, J Appl Polym Sci
37:2577 (1992).
5 Kaptan Y, Pekcan OÈ and GuÈven O, J Appl Polym Sci 44:1595
(1992).
6 Pekcan OÈ and Demir Y, J Appl Polym Sci 43:2169 (1991).
7 Pekcan OÈ and Demir Y, J Appl Polym Sci 49:1877 (1993).
8 Nivaggioli T, Wank F and Winnik MA, J Phys Chem 96:7462
(1992).
9 Pascal D, Duhamel J, Wank J, Winnik MA, Napper Dh and
Gilbert R, Polymer 34:1134 (1993).
10 Limm W, Dimnik GD, Stanton D, Winnik MA and Smith B, J
Appl Polym Sci 35:2099 (1988).
11 Lu L and Weiss RG, Macromolecules 27(1):219 (1994).
12 Kronganz VV, Mooney WF III, Palmer JW and Patricia JJ, J
Appl Polym Sci 56(9):1077 (1995).
13 Krongauz VV and Yohannan RM, Polymer 31(9):1130 (1990).
14 He Z, Hammond GS and Weiss RG, Macromolecules 25(1):501
(1992).
15 Pekcan OÈ , Canpolat M and Kaya D, J. Appl Polym Sci 60:2105
(1996).
16 Enscore DJ, Hopfenberg HB and Stannett VT, Polymer 18:793
(1977).
17 Thomas NL and Windle AH, Polymer 23:529 (1982).
18 Crank J and Park GS, Diffusion in Polymers, Academic Press,
London (1968).
19 Birks JB, Photophysics of Aromatic Molecules, Wiley Interscience,
New York (1971).
20 Baird JK, McCaskill JS and Marck NH, J Chem Phys 78:6598
(1983).
21 Pekcan OÈ , J Appl Polym Sci 57(1):25 (1995).
22 Birks JB, Dyson DJ and Munro IH, Proc R Soc London, Sec A
275:575 (1963).
23 Pekcan OÈ , Winnik MA, Egan L and Croucher MD, Macro-
molecules 16:699 (1983).
24 Egan L, Winnik MA and Croucher MD, Polym Eng Sci 26:15
(1986).
25 Birks JB and Salete M, J Phys B At Mol Phys 3:417 (1970).
490 Polym Int 48:485±490 (1999)
SË UgÆur, OÈ Pekcan