Time-Resolved SAXS Study of Nucleation and Growth of Silica Colloids
Time-Resolved SAXS Study of Nucleation and Growth of Silica Colloids
Time-Resolved SAXS Study of Nucleation and Growth of Silica Colloids
This paper reports a time-resolved small-angle X-ray scattering study of in situ Stöber silica synthesis.
The hydrolysis reaction is initiated by rapidly mixing equal amounts of alcoholic solutions of ammonia
and tetraethyl orthosilicate, using a stopped-flow device coupled to a flow-through capillary cell.
Measurements covered the scattering wave vector (q) range of 0.02 e q e 6 nm-1 and time (t) range of
0.1 e t e 1000 s. The combination of high sensitivity, low background, and high dynamic range of the
experimental setup permitted observation of the primary particles of nucleation. During the entire growth
process, the measured scattered intensity can be adequately described by a sphere scattering function
weighted by a Schultz size distribution function. At the early stages of growth, the fitted radius increased
linearly with time, subsequently crossing over to a smaller exponent of between 1/3 and 1/2. The observed
behavior is consistent with an aggregation process involving primary particles of a few nanometers in size.
Experimental Section
The chemicals, TEOS (Fluka), 25% ammonia solution
(Prolabo), and absolute alcohol (Prolabo), were used as purchased.
The growth process was initiated by mixing two stock solutions
of ammonia and TEOS in ethanol in equal volumes. The resulting
concentrations of the reacting mixtures were [TEOS] ) 0.09 mol/
L, [NH3] ) 1.45 mol/L, and [H2O] ) 4.15 mol/L. These concen-
trations were chosen as an intermediate between those used in
earlier studies2-4,7,8 and to complete the whole growth process Figure 1. Typical 3-d representation of the time evolution of
within a short period when the sedimentation effect is not the SAXS intensity during the Stöber synthesis of silica
significant. particles. Measurements covered over 20 min corresponding to
The stopped-flow apparatus consisted of two pneumatically a sample-to-detector distance of 10 m.
driven syringes and a mixing chamber that is coupled to a thin-
walled flow-through capillary (2 mm diameter and wall thickness analytical form:
10 µm). To reduce the parasitic background, the capillary was
mounted in vacuum without any windows in the entire flight P(q) ) [3 (sin(qRS) - qRS cos(qRS))/q3RS3]2 (2)
path of the incident and transmitted beams. The combined mixing
and transfer dead times were less than 10 ms. The data
acquisition is hardware triggered at the end of the movement of Equations 1 and 2 imply that the intensity at q ) 0 is I0
the pneumatically driven piston. ) N(4/3πRS3)2(Fc - Fs)2. If the particle number and mass
SAXS is a powerful technique to probe the size, shape, and densities were conserved during the growth process, then
polydispersity of colloidal particles.10 The scattered intensity, I0/RS6 should remain constant. However, in real systems
I(q), is measured as a function of scattering wave vector, q ) there is a finite distribution of particle sizes and eq 1 has
(4π/λ) sin(θ/2), where λ is the wavelength of incident radiation to be weighted over the entire size distribution P(R).
and θ is the scattering angle. SAXS measurements were Experimentally, it has been found that the size distribution
performed on the ID2 beamline at the European Synchrotron of many colloidal systems can be adequately described by
Radiation Facility, Grenoble, France.11 The incident X-ray
wavelength was 0.1 nm. To cover a wide q-range (0.02 nm-1 e
the Schultz distribution function,13
[ ] [ ]
q e 6 nm-1) with sufficient intensity statistics, several different
sample-to-detector distances were used (1.5, 3, and 10 m). The (Z + 1)Z+1 (Z + 1)R
two-dimensional SAXS patterns were recorded with an image- P(R) ) RZ exp - /Γ(Z+1) (3)
intensified CCD camera.11 The incident and the transmitted
h
R h
R
fluxes were also simultaneously registered with each SAXS
pattern. Typically, a sequence of 120 frames was acquired after where Rh is the mean radius; Z is related to σR, the root-
each mixing. The dead time between the frames was varied in mean-square deviation of the radius, by σR ) R h /xZ+1;
a geometric progression. and Γ(Z) is the gamma function.
The standard data treatment involved various detector cor- In addition, for noninteracting systems the intensity at
rections for flat field response, spatial distortion, and dark current small q values (qRS < 1) is given by the Guinier
of the CCD, and normalization by the incident flux, sample approximation,10
transmission, exposure time and the angular acceptance of the
detector pixel elements.11 Further corrections, described else-
where,12 were necessary to account for the long tail of the point I(q) ) N(Fc - Fs)2V2 exp(-q2RS2/5) (4)
spread function of the image intensifier. The resulting normalized
two-dimensional images were azimuthally averaged to obtain From the limiting slope and the intercept of ln(I) versus
I(q) which essentially refers to the differential scattering cross q2, the radius and the molecular mass can be estimated.
section dΣ/dΩ per unit length in mm-1 sterad-1. However, slight interactions between particles can affect
The beam intensity was optimized in order to reduce the beam- I(q) in the small q region; thus, a more reliable method
induced degassing of the dissolved ammonia. During the early of estimating the radius and molecular weight is by fitting
stages, the measured I(q) at small q was dominated by this
the measured scattered intensity to the polydisperse
microbubble scattering if the full beam intensity (typically 1013
photons/s) was used. As a result, for the low q measurements spherical form factor over the whole measured q-range.
(sample-to-detector distance of 10 m) the beam intensity was For the Schultz distribution, there exists an analytical
reduced by a factor of 20 and the exposure time varied from 0.05 expression13 for the scattered intensity and this expression
to a few seconds. was used to fit the experimental data. In the following
sections, the fitted mean radius is represented as R.
Data Analysis
In the small-angle region, I(q) of a suspension of uniform Results
noninteracting spherical particles is given by10 Typical time evolution of SAXS intensity during the
Stöber growth process is depicted in Figure 1 as a 3-d plot
I(q) ) N(Fc - Fs)2V2 P(q) (1) of I versus q and time. Similar features were observed in
data sets acquired under different conditions. The oscil-
where N is the particle number density, Fc and Fs are the lations in the intensity at the later stages of the growth
average electron densities of the particle and the solvent, process readily indicate the development of the form factor
respectively, V ) 4/3πRS3 is the volume, and P(q) is the of spherical particles as given by eq 2. The maxima and
form factor of a sphere of radius RS. P(q) has the following the minima progressively shifted to the low-q region
signifying the growth of the particles. During the so-called
(10) Modern Aspects of Small-Angle Scattering; Brumberger, H., Ed.; induction time, the intensity evolved marginally only in
NATO ASI Series; Kluwer Academic Publishers: Dordrecht, 1995. the intermediate q-range. Figure 2 shows the evolution
(11) Narayanan, T.; Diat, O.; Boesecke, P. Nucl. Instrum. Methods
Phys. Res., Sect. A 2001, 467, 1005. of intensity over this q-range. The continuous lines depict
(12) Pontoni, D.; Narayanan, T.; Rennie, A. R. J. Appl. Crystallogr.,
submitted. (13) Kotlarchyk, M.; Chen, S.-H. J. Chem. Phys. 1983, 79, 2461.
58 Langmuir, Vol. 18, No. 1, 2002 Pontoni et al.
density. This is in contrast to the fractally rough colloids14 fresh nuclei cannot be ruled out since the measured
found in slow growth. For the reaction conditions used in intensity is completely dominated by the larger growing
this study, the induction time associated with the nucle- particles. In fact, the deduced morphology of the particles
ation of particles is fairly short (<60 s). Presumably, during suggests that the growth is likely to have proceeded by
this time sufficient hydrolyzed monomers were formed the addition of the primary nuclei onto these larger
but SAXS is not sensitive to this first step. Subsequently, particles. At this stage, the size distribution approaches
I(q) in the intermediate q-range (0.1 < q < 0.5 nm-1) began an invariant form as indicated in Figure 5. The decrease
to evolve, and it is attributed to the formation of primary in growth rate at later stages can be attributed to the
nuclei. At the same time, there was not any observable depletion of the primary nuclei in the reservoir.3 The
change in the intensity over the high q-range, typically observed behavior is in agreement with previous studies
1-6 nm-1. Within the statistical uncertainties, the scat- which concluded that the rate-limiting step is the hy-
tering from these primary nuclei is better described by a drolysis reaction and the growth proceeds by an aggrega-
polydisperse sphere form factor of radius ∼3 nm (see the tion mechanism involving primary particles.2,6,7
fitted curve for t ) 65 s in Figure 2) than by a fractal After the initial nucleation stage, the growth is pre-
structure function, indicating that they have droplet-like sumably accomplished by the coalescence/coagulation of
form. These small nuclei rapidly coalesced to form larger primary nuclei with colloidally stable larger particles.
particles, and in this process their number density sharply Therefore, the Smoluchowski rate equation16,18,19 can be
decreased as is evident in the inset of Figure 3. In the used to rationalize the observed growth laws. This rate
subsequent stages of growth, presumably freshly formed equation can describe both gelling and nongelling growth
primary nuclei coalesced with larger particles, thus processes.18 In the nongelling case, typically R ∼ tz/D, where
resulting in dense compact particles. z ) 1/(1 - λ) with λ being the homogeneity exponent of the
After the initial nucleation stage, the radius of the reaction kernel.18 Nongelling systems pertain to λ e 1,
particles increased linearly with time. The polydispersity with λ ) 0 and 1 for diffusion-limited and reaction-limited
of the system decreased until it reached a steady value of aggregation, respectively.19 The observed linear regime
about 10%. In the classical Lifshitz-Slyozov15 nucleation corresponds to λ ) 2/3, implying compact particles and
and growth process, one would expect a power law of either straight-line ballistic motion between aggregating par-
1
/2 or 1/3 during the early stage of nucleation depending on ticles.20 This is consistent with a scenario where particles
the degree of supersaturation (high or low, respectively). attract each other without an intervening repulsive
This suggests that the early stage growth of silica particles barrier. The later behavior refers to λ between 0.33 and
is faster than a purely diffusion-controlled process and 0 and the growth mechanism crossover toward a diffusion
cannot be readily explained by classical theory of nucle- type behavior. The colloidal stability is attained in this
ation and growth. Faster growth rates are usually seen crossover region when the electrostatic repulsive barrier
in the presence of gravity-induced hydrodynamic flows,16 is developed.
which is very unlikely in this case. A faster growth than Conclusion
the Brownian diffusion limit is possible if the initial nuclei
are attracted together by long-ranged dispersion forces. Stopped-flow time-resolved SAXS is used to follow the
The cumulative effect of interactions and local hydrody- nucleation and growth process in Stöber silica synthesis.
namics can be expressed in terms of the stability factor The high brilliance of the X-ray beam combined with the
(W).17 The Brownian diffusion limit corresponds to W ) high-sensitivity detection permitted monitoring of the
1, and in general W > 1. However, with a vanishing complete process of nucleation to the formation of final
repulsive barrier, the long-ranged dispersion forces can stable particles. The classical theory of heterogeneous
bring down W to <1 resulting in a faster growth than the nucleation is not adequate to fully describe the nucleation
Brownian limit. At the later stages of growth, particles and growth process in Stöber silica synthesis. The observed
acquire sufficient electric charges to overcome the strong growth laws are consistent with an aggregation mecha-
dispersion forces. The Stöber silica is stabilized by the nism involving primary particles. The exponent describing
electric double layer formed by the surface silanol groups the power law growth depends on the interparticle
(SiO- Η+). The onset of repulsive interaction between the interactions. A crossover in the power law exponent
particles is evident in the inset of Figure 4. However, the demarcates the limiting stability of the suspension where
signature of initial attractive interactions in the small-q the electrostatic repulsion overcomes the long-ranged
data may have been camouflaged by the scattering from dispersion forces. The first observable nuclei seem to have
the unavoidable gas microbubbles present in the mixture. a dropletlike form. This morphology is consistent with a
scenario where one of the reaction intermediates is phase
The observed power law at the late stage approaches separating from the solution.6,7 The mass and the number
that of a diffusive type growth. This is in sharp contrast densities of dominantly growing particles remained
to that observed near a first-order phase transition with constant after the initial stage of growth suggesting that
a conserved order parameter, where the early stage is freshly formed nuclei coagulate with existing colloidally
usually diffusion limited and in the later stage the growth stable larger particles.
is accelerated by hydrodynamic flows.16 Throughout the
growth process, the deduced I0, which is proportional to Acknowledgment. We are grateful to S. Finet and J.
the square of the molecular mass, remained proportional Gorini for fabricating and extensively testing the stopped-
to R6 indicating that the particles are dense (dimension- flow device. The European Synchrotron Radiation Facility
ality D ) 3) and the number density of the dominantly is acknowledged for the provision of beam time and the
growing spheres is constant. However, the formation of financial support.
LA015503C
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(15) Lifshitz, I. M.; Slyozov, V. V. J. Phys. Chem. Solids 1961, 19, 35. (18) van Dongen, P. G. J.; Ernst, M. H. Phys. Rev. Lett. 1985, 54,
(16) Gunton, J. D.; San Miguel, M.; Sahni, P. S. In Phase Transitions 1396.
and Critical Phenomena; Domb, C., Lebowitz, J. L., Eds.; Academic (19) Ball, R. C.; Weitz, D. A.; Witten, T. A.; Leyvraz, F. Phys. Rev.
Press: London, 1983; Vol. 8, p 267. Lett. 1987, 58, 274. Broide, M. L.; Cohen, R. J. J. Colloid Interface Sci.
(17) Spielman, L. A. J. Colloid Interface Sci. 1970, 33, 562. Law, B. 1992, 153, 493.
M.; Petit, J.-M.; Beysens, D. Phys. Rev. E 1998, 57, 5782. (20) Oh, C.; Sorensen, C. M. J. Aerosol Sci. 1997, 28, 937.