Journal of Alloys and Compounds 487 (2009) 744–750
Contents lists available at ScienceDirect
Journal of Alloys and Compounds
journal homepage: www.elsevier.com/locate/jallcom
Low-density TEOS-based silica aerogels prepared at ambient pressure using
isopropanol as the preparative solvent
Askwar Hilonga a , Jong-Kil Kim b , Pradip B. Sarawade a , Hee Taik Kim a,∗
a
b
Department of Chemical Engineering, Hanyang University, 1271 Sa 3-dong, Sangnok-gu, Ansan-si, Gyeonggi-do 426-791, Republic of Korea
E&B Nanotech. Co., Ltd, Republic of Korea
a r t i c l e
i n f o
Article history:
Received 21 April 2009
Received in revised form 7 August 2009
Accepted 14 August 2009
Available online 22 August 2009
Keywords:
Silica aerogels
Ambient pressure drying
Isopropanol
FTIR
TEM
a b s t r a c t
In this paper, we report experimental results on the synthesis of low-density tetraethoxysilane (TEOS)based silica aerogels prepared with different solvents via an ambient pressure drying (APD) route.
Tetraethoxysilane was hydrolyzed and condensed in different solvents (methanol, ethanol, butanol, and
isopropanol) using oxalic acid and NH4 OH as the catalysts. To minimize shrinkage due to drying, the
surfaces of the gels were modified using trimethylchlorosilane (TMCS) before the APD via a one-step solvent exchange/surface modification process. The effects of different solvents on the physical and textural
properties of the resulting aerogels was investigated. It was observed that solvents containing longer
chains of alkyl groups (–CH2 –CH3 ) formed high silica polymerization in the alcogels which enhanced a
distinct “spring-back effect” during APD, and consequently preserved the highly porous silica network by
preventing collapse. Silica aerogels with very low bulk densities (0.041 g/cm3 ), extremely high specific
surface areas (1150 m2 /g), and large cumulative pore volumes (5.2 cm3 /g) were successfully synthesized
using isopropanol as a preparative solvent.
© 2009 Elsevier B.V. All rights reserved.
1. Introduction
Aerogels are nanoscale mesoporous light materials possessing a number of exceptional physical properties that attract the
attention of researchers in various areas of science and technology. They have a large surface area (500–1500 m2 /g), high porosity
(80–99%), low bulk density (∼0.03 g/cm3 ), extremely low thermal conductivities (0.005 W/mk), and unique acoustic properties
(sound velocities as low as 100 m/s) [1,2]. Because of these properties, aerogels lend themselves to potential applications such as
thermal super-insulators in solar energy systems, refrigerators,
thermal flasks [3], internal confinement fusion (ICF) targets for
thermonuclear fusion reactions [4], efficient catalysts and catalytic
supports [5], storage media for liquid for rocket propellants [6], and
radio luminescent devices [7]. Monolithic silica aerogels have been
used extensively in the area of high energy physics in Cherenkov
radiation detectors [8,9]. The extremely low densities and high surface areas of monolithic aerogels provide an opportunity to improve
the performance of various metal-oxide-based devices, including
gas- and bio-sensors, batteries, heterogeneous catalysis devices,
and low dielectric constant materials for integrated circuits (low-k
dielectrics) [10–12].
∗ Corresponding author. Tel.: +82 31 400 5493; fax: +82 31 500 3579.
E-mail address: khtaik@yahoo.co.kr (H.T. Kim).
0925-8388/$ – see front matter © 2009 Elsevier B.V. All rights reserved.
doi:10.1016/j.jallcom.2009.08.055
Silica aerogels are produced by the removal of entrapped solvent
from the wet gel while maintaining the integrity and high porosity
of the gel. Kistler used supercritical organic solvents (ethanol, for
example) for drying [13,14]. In general, supercritical fluids have a
high solvating power and almost zero surface tension. These make
them ideal for the removal of solvents from wet gels while avoiding
the cracking and shrinkage caused by the surface tension force associated with the removal of the solvent. Nevertheless, supercritical
drying requires high pressures and temperatures, is generally risky,
relatively expensive, and greatly hampers large-scale production of
porous silica because of the required labor and use of sophisticated
instruments [13,15].
To enhance the commercial feasibility of aerogels, an important
precondition for large-scale application is to avoid supercritical
drying. Although several attempts have been made to synthesize silica aerogels by drying the gels at ambient pressures, there
are few reports on the synthesis of TEOS-based silica aerogels at
ambient pressure. In addition, the synthesis of monolithic silica
aerogels via APD has not been achieved. For instance, Wei et al.
synthesized monolithic silica aerogels based on a tetraethoxysilane (TEOS) precursor via ambient pressure drying [16]. The
silica aerogel they produced, however, possessed a relatively high
density (0.069 g/cm3 ) and a relatively high thermal conductivity
(0.079 W/mk), a low surface area (777 m2 /g), and a low pore volume (1.13 cm3 /g) compared with aerogels prepared with a TEOS
precursor and supercritical drying [17]. In addition, they employed
A. Hilonga et al. / Journal of Alloys and Compounds 487 (2009) 744–750
745
Table 1
Synthesis conditions and the physical properties of TEOS-based silica aerogels by one-step solvent exchange surface modification.
No.
TEOS/MtOH:H2 O(A):
H2 O (B) molar ratio
(M1 )
EtOH:TMCS molar
ratio (M2 )
Perfluorohexane/TMCS
volume ratio (V1 )
Volume shrinkage (%)
Bulk density
Remarks
1
2
3
4
5
6
7
8
9
1:6.9:3.5:2.2
1:6.9:3.5:2.2
1:6.9:3.5:2.2
1:6.9:3.5:2.2
1:6.9:3.5:2.2
1:6.9:3.5:2.2
1:6.9:3.5:2.2
1:6.9:3.5:2.2
1:6.9:3.5:2.2
0.5
1
1.5
2
1
1
1
1
1
–
–
–
–
10
15
20
25
30
7.2
5.6
5.9
6.3
6.7
6.4
5.4
4.3
5.3
0.67
0.59
0.58
0.57
0.65
0.61
0.59
0.53
0.54
Pieces
Few cracks
Cracks
Pieces
Pieces
Pieces
Cracks
Few cracks
Cracks
a multiple surface modification (MSM) process, which is a complicated and lengthy process (requiring about 6 days), to synthesize
monolithic silica aerogels at ambient pressure.
For the present study, we employed a one-step solvent exchange
and surface modification process that significantly reduced the
time needed to synthesize monolithic aerogels (at ambient pressure) from 6 to 2 days. Moreover, the effects of different preparative
solvents on the physical and textural properties of TEOS-based silica aerogels synthesized at ambient pressure were investigated.
The choice of appropriate solvent is a key factor to consider in
developing aerogels with desirable properties. For instance, isopropanol (which contains more branching alkyl groups) provides
a high degree of polymerization in the two-step acid–base sol–gel
process with a TEOS precursor [18,19]. This high degree of polymerization in the silica network enhances a distinct “spring-back
effect” during APD, and consequently preserves the highly porous
silica network by preventing collapse [20].
In an earlier publication [21] we reported the synthesis of a
high specific surface area TEOS-based silica aerogel with a large
pore volume using an ethanol solvent and a two-step sol–gel
process at ambient pressure. In our continuous program of developing aerogels that are more suitable for industrial application,
we have successfully synthesized monolithic aerogels with more
desirable properties: low density (0.041 g/cm3 ), high surface area
(1150 m2 /g), and large pore volume (5.2 cm3 /g). This was accomplished using an isopropanol solvent and the two-step acid–base
sol–gel polymerization of a TEOS precursor. This paper reports, in
detail, the results obtained.
2. Materials and methods
2.1. Preparation of silica alcogel using a two-step sol–gel process
Silica alcogels were prepared by a two-step acid–base catalyzed sol–gel process
followed by a one-step solvent exchange surface modification and ambient pressure drying, as described elsewhere [22]. The chemicals used for the preparation
of the alcosols were tetraethoxysilane (TEOS), Si–(OC2 H5 )4 (Aldrich), ammonium
hydroxide (NH4 OH, from Duksan Chemical), methanol (MeOH, CH3 OH), ethanol
(EtOH, C2 H5 OH), 1-butanol (C4 H9 OH), isopropanol (C3 H7 OH), oxalic acid (dihydrate,
C2 H5 OH), and perfluorohexane (C6 H14 , from Duksan chemical). Double-distilled
water was used to prepare the desired concentration of hydrochloric acid and
NH4 OH catalysts.
Silica wet gels were prepared using the following two steps. In the first step,
tetraethoxysilane (TEOS) was diluted with a relevant solvent (methanol, ethanol,
butanol, or isopropanol), then mixed with oxalic acid with constant stirring for
30 min. In the second step, after 24 h, the base catalyst (NH4 OH) was added (drop
by drop) into the acid catalyzed silica sol. The molar ratio of TEOS: alcohol: H2 O
(acidic): H2 O (basic) was kept constant at 1:6.9:3.5:2.2 (Table 1). The oxalic acid and
NH4 OH concentrations were kept constant at 0.01 and 0.1 M, respectively. To study
the effects of solvents on the properties of the dried silica aerogels, four alcogel samples were prepared with four different solvents: methanol, ethanol, 1-butanol, and
isopropanol. The as-prepared alcosols were poured into an air-tight 50 ml beaker
and were kept for gelation at room temperature. After gelation of the sols, a small
quantity of the relevant alcohol was added into the targeted gel to prevent the evaporation of the pore solvent which would normally lead to shrinkage and cracking of
the gel.
±
±
±
±
±
±
±
±
±
0.5
0.3
0.4
0.6
0.2
0.5
0.2
0.5
0.4
2.2. One-step solvent exchange surface modification of silica alcogels and the
drying process
To minimize drying-related shrinkage, the surfaces of the gels were modified
using an alcohol/TMCS/perfluorohexane solution via a one-step solvent exchange
surface modification process before the APD. The one-step solvent exchange and
surface modification were carried out by immersing the aged alcogels in the alcohol/TMCS/perfluorohexane solution at room temperature for 24 h. To determine the
optimal conditions for the modification process, the molar ratio of alcohol/TMCS
(M1 ) was varied from 0.5 to 2. Also, the volumetric ratio of perfluorohexane and
TMCS (V2 ) was varied from 10 to 30. In the course of the experiments, we observed
that the alcohol/TMCS molar ratio had no significant effect on the monolithicity of
the dried aerogels in the tested range of ratios. Thus, the molar ratio of alcohol/TMCS
was fixed at 1 in additional experiments. The volumetric ratio of perfluorohexane/TMCS was also fixed at 25 since fewer cracks were observed at this ratio, as
is reported elsewhere [23].
After the surface modification of the alcogels, they were washed with perfluorohexane to remove the unreacted TMCS. The alcogels were dried at 50 ◦ C for 12 h, and
then at 80 ◦ C for 2 h to reduce drying-related shrinkage. For complete evaporation
of the pore liquid, the gels were finally dried at 200 ◦ C for 1 h. The aerogel samples
were allowed to cool to room temperature and were then characterized by various
techniques.
2.3. Characterization methods
The specific surface areas and pore size distributions (PSDs) of the aerogels were
analyzed by Brunauer, Emmett and Teller (BET) and BJH nitrogen gas adsorption and
desorption methods (ASAP 2000, Micromeritics, USA). BET analysis of the amount
of N2 gas adsorbed at various partial pressures (five points 0.05 < p/po < 0.3, nitrogen
molecular cross-sectional area = 0.162 nm2 ) was used to determine the surface area,
and a single condensation point (p/po = 0.99) was used to find the pore size and pore
volume. Before N2 adsorption, the sample was degassed at 200 ◦ C. Pore size distributions were calculated from the desorption isotherms [24]. To study the thermal
stability of the aerogels in terms of the retention of hydrophobicity, the samples were
examined by thermogravimetric and differential thermal analysis (TG-DTA). The
hydrophobic nano-porous silica aerogels with a weight of 6 mg were heat-treated
in air, from room temperature (25 ◦ C) up to 1000 ◦ C, with a controlled heating rate
of 1.5 ◦ C min−1 , using a microprocessor-based Parr temperature controller (Model
4846) connected to a muffle furnace (A.H. JEON Industrial Co. Ltd., Korea). Here,
thermal stability refers to the temperature up to which the silica aerogel retains its
hydrophobicity [25]. The bulk densities of the aerogels were calculated from their
mass to volume ratios. The volume was calculated after measuring the dimensions of
the monolithic aerogels using Vernier calipers. An electronic microbalance (Model
OHAUS EPG214C, USA) was used to measure the masses of the samples. The percents of volume shrinkage and porosity of the prepared aerogels were determined
as follows:
% Volume shrinkage =
% Porosity =
1−
b
s
1−
Va
Vg
× 100
× 100
(1)
(2)
where Va and Vg are the volumes of the aerogel and alcogel, respectively, and s and
b are the skeletal and bulk densities (of silica aerogel), respectively.
Surface modification was confirmed using infrared (IR) spectroscopy
(PerkinElmer, Model No. 783). For this purpose, the as-prepared silica aerogels were
ground into powders and pressed to from a sample pellet for FTIR measurements.
The contact angle () measurements were performed using a contact angle meter
(CAM 200 Automates contact angle analyzer, Finland) to quantify the degree of
hydrophobicity. A 12 l (2 mm) water droplet was placed at three different places on
the surface of the hydrophobic aerogels, and the average measured value was then
taken to be the contact angle (). The optical transmittances of the aerogels (sample
10
15
40
70
Gelation time
(min)
thickness: 10−2 m) were measured at a wavelength of 750 nm (Systronics 119 spectrophotometer). Microstructure studies of the aerogel samples were carried out by
transmission electron microscopy (TEM, JSM 6700 F, JEOL).
3. Results and discussion
Silica alcogels were prepared by two-step hydrolysis and condensation of diluted tetraethoxysilane (TEOS) in the presence
of acid (oxalic acid)–base (ammonium hydroxide) catalysts and
selected solvents, as shown in the following reactions:
Hydrolysis:
Si(O–X)4 + 4H2 O → Si(OH)4 + 4X–OH
(3)
n(Si(OH)4 + (OH)4 Si) → n((OH)3 Si–O–O(OH)3 ) + nH2 O
85
86
89
91
157
159
162
168
0.7
0.4
0.2
0.5
±
±
±
±
87
91
94
96
9
10
11
14
3.1
3.7
4.5
5.2
0.056
0.047
0.044
0.041
Mean pore size
(nm)
Density (g/cm3 )
(4)
3.1. Mechanism of surface modification and hydrophobic
properties of TEOS-based silica aerogels
Pore volume
(cm3 /g)
Porosity (%)
Contact
angle ( ◦ )
Optical
transmittance (%)
Condensation:
The silica network formed due to the polymerization of the TEOS
precursor was weaker than those obtained with the polymerization
of colloidal silica. During the drying process, liquid and vapor coexisted within the pores of the gel. As the liquid began to evaporate,
a meniscus was formed at the liquid–vapor interface. The formation of a liquid–vapor interface within the gel resulted in surface
tension and created concave menisci in the pores of the gel. As
evaporation progressed, the menisci receded into the gel body and
built up a compressive force that acted on the walls of the pores.
This caused considerable shrinkage due to the partial collapse of the
gel network [26]. In addition, the terminal silanol groups (Si–OH)
present on the silica surface underwent a condensation reaction,
forming new siloxane bonds which ultimately resulted in an irreversible shrinkage of the gel [27]. This shrinkage can be reduced by
attaching non-polar alkyl groups to the silica surface by replacing
H by OH. Gel collapse also ceases when the gel structure is strong
enough to withstand the tensile strength of the liquid. Therefore,
to reduce the irreversible shrinkage of the alcogel during the drying process, the surface of the alcogel was organically modified by
tri-methyl groups (found in TMCS). This was done via a one-step
solvent exchange and surface modification processes using an alcohol/TMCS/perfluorohexane solution. The chemical reactions in the
one-step solvent exchange and surface modification are as follows:
CH3 OH + (CH3 )3 –Si–Cl → (CH3 )3 –Si–O–CH3 + HCl
(5)
C2 H5 OH + (CH3 )3 –Si–Cl → (CH3 )3 –Si–O–CH2 CH3 + HCl
(6)
C3 H7 OH + (CH3 )3 –Si–Cl → (CH3 )3 –Si–O–CH(CH3 )2 + HCl
(7)
C4 H9 OH + (CH3 )3 –Si–Cl → (CH3 )3 –Si–O–(CH2 )3 CH3 + HCl
(8)
(CH3 )3 –Si–Cl +
(9)
Si–OH →
Si–O–Si(CH3 )3 + HCl
Surface area
(m2 /g)
978
1044
1080
1150
Methanol (MeOH)
Ethanol (EtOH)
Butanol (BuOH)
Isopropanol (IsoPrOH)
R–OH + (CH3 )3 –SiCl → (CH3 )3 Si–O–R + HCl
Solvent
Table 2
Comparison in physical and textural properties of the TEOS-based silica aerogels prepared with various solvents by one-step solvent exchange surface modification followed by ambient pressure drying.
Pieces
Pieces
Multiple cracks
Monolithic
A. Hilonga et al. / Journal of Alloys and Compounds 487 (2009) 744–750
Remarks
746
(10)
Thus, alcohols reacted with TMCS to form alkoxytrimethylsilane [(CH3 )3 Si–O–R] (Eq. (10)), and consequently, the hydrophilic
surface of the silica network became hydrophobic. As the reaction
proceeded, transferable liquids (HCl/residual alcohol) spontaneously come out of the wet gel [28]. During the one-step solvent
exchange/surface modification process, the reaction between alcohols and TMCS helped to slow down the rate of reaction of
TMCS with the OH groups on the silica surface. This process
spontaneously replaced the pore alcohol with perfluorohexane.
The chemical surface modification of the alcogels by non-polar
alkyl/aryl groups is an indispensable step before the APD as it
prohibits the formation of new siloxane bonds between the adjacent silica cluster, and thereby prevents shrinkage of the gel
A. Hilonga et al. / Journal of Alloys and Compounds 487 (2009) 744–750
747
Fig. 3. TG/DTA curves obtained in an air atmosphere for the TEOS-isopropanolbased silica aerogel.
Fig. 1. A water droplet (2 mm) placed on TEOS-isopropanol-based superhydrophobic silica aerogel surface.
[29,30]. In the present work, the surfaces of the TEOS-based alcogels were organically modified by tri-methyl groups present in
the trimethylchlorosilane using the one-step solvent exchange and
surface modification process explained above. The surface modification of the gels was studied by measuring the contact angle
of water droplets on the silica aerogel surface, and the results are
tabulated in Table 2. The observed hydrophobicity was ascribed to
the attachment of hydrolytically stable –Si–(CH3 )3 groups after the
replacement of H by the –OH groups on the silica surface. There was
a slight increase in the contact angle of the aerogels with the use
of various solvents. The size of the increase occurred in the following order: methanol < ethanol < butanol < isopropanol. The contact
angle was found to be highest (168◦ ) for aerogels prepared with
the isopropanol solvent (Fig. 1). The surface modification of the gels
was also confirmed using Fourier transform infrared spectroscopy
(FTIR) as shown in Fig. 2. In the figure, it is evident that apart from
the; Si–O–Si ( absorption peak at 1060 cm−1 , all aerogel samples
showed Si–CH3 peaks at 850 and 1260 cm−1 [31–33]. The presence of Si–CH3 peaks in the FTIR spectra of all samples confirms
the attachment of –Si–CH3 groups from the TMCS to the silica
aerogel surface, and hence the surface modification of the aerogels was successful. The degree of intensity of the Si–CH3 peaks is
dependent on the solvent used, and occurs in the following order:
methanol < ethanol < butanol < isopropanol. Thus, the most surface
modification occurred in the alcogel prepared with the isopropanol
solvent.
The aerogels were heated in a furnace at a range of temperatures
to investigate the thermal stability of their hydrophobic natures. It
has been observed that aerogels retain their hydrophobic behavior
up to a maximum temperature of 450 ◦ C, above which they become
hydrophilic. This is due to the fact that at this temperature the
surface –CH3 groups, which are the reason for the hydrophobicity, are oxidized. Thermogravimetric (TG) and differential thermal
(DT) analysis of the TMCS-modified silica aerogels were employed
to confirm the thermal stability and oxidation temperature of the
–CH3 groups, respectively. Fig. 3 illustrates the TG/DTA curves
obtained for the isopropanol-based TMCS-modified silica aerogel
in the temperature range of 25–1000 ◦ C, in an air atmosphere. The
weight loss observed up to 200 ◦ C was due to the evaporation of the
residual solvent and water molecules from the aerogel. The sharp
decrease in weight at the temperature of 450 ◦ C can be attributed
to the thermal decomposition of the organic groups (CH3 ) present
in the aerogel. By considering the two sharp exothermic peaks in
the DTA curve for temperatures above 450 ◦ C, the oxidation of surface methyl groups can be confirmed. The results are consistent
with earlier work wherein the thermal stability of TEOS-based silica
aerogels was observed up to 380 ◦ C [21].
3.2. Effects of alcohol/TMCS molar ratio and
perfluorohexane/TMCS volume ratio on the physical properties of
TEOS-alcohol-based silica aerogels
Fig. 2. Fourier transform infrared spectroscopy spectra of the TEOS-based silica
aerogels prepared with various solvent (methanol, ethanol, butanol and isopropanol) and surface modified by alcohol/TMCS/perfluorohexane by one-step
solvent exchange and surface modification process.
Table 1 shows the physical properties of aerogels synthesized
using different alcohols/TMCS molar ratios and perfluorohexane/TMCS volume ratios. The molar ratio of alcohol/TMCS was
varied from 0.5 to 2, and the volumetric ratio of cyclo-hexane
and TMCS was varied from 10 to 30. It was observed that the
alcohol/TMCS ratio had no significant effect on the monolithicity
of the dried aerogels at the tested molar ratios. Thus, in further
experiments the alcohol/TMCS molar ratio was kept constant at
1. However, the volume ratio of perfluorohexane/TMCS strongly
influenced the physical and textural properties of the resulting
aerogels. Fewer cracks were observed when the volumetric ratio
of perfluorohexane/TMCS was 25, as observed in related studies
748
A. Hilonga et al. / Journal of Alloys and Compounds 487 (2009) 744–750
Fig. 4. Photographs of TEOS-based silica aerogels prepared with (a) methanol and (b) isopropanol solvent.
[23,32]. Therefore, in further experiments, the alcohol/TMCS volumetric ratio was fixed at 25.
3.3. Physical properties of TEOS-based silica aerogels
To investigate the effects of different solvents on the physical
properties of the silica aerogels, the molar ratio of alcohol/TMCS
was kept constant at 1, and the volume ratio of perfluorohexane/TMCS was maintained at 25. It was found that the gelation
time was strongly dependant on the type of solvent used. A smaller
gelation time was observed with the methanol solvent, while the
1-butanol solvent induced a higher gelation time. This may be associated with the lengths of the alkyl groups which normally affect the
rates of hydrolysis and condensation. Thus, 1-butanol contains alkyl
groups with longer chains that slow down the hydrolysis and condensation reactions, and extend polymerization, thereby reducing
gelation time (Table 2). Fig. 4 shows the effect of solvent-type on the
monolithicity of the silica aerogel prepared by the two-step sol–gel
process with a TEOS precursor via the one-step solvent exchange
surface modification process. As shown in Fig. 4(a), the cracking
probability during the APD of the alcogels was higher for samples
prepared with the solvents with shorter alkyl chains. On the other
hand, a monolithic silica aerogel was obtained when a solvent with
alkyl groups having longer chains (isopropanol) was used, as shown
in Fig. 4(b). This is due to the fact that the increase in chain-length
in the alkyl group of a solvent extends the degree of polymerization
in the two-step acid–base sol–gel process, consequently decreasing the cracking probability in the alcogel during APD. Hence, the
volume shrinkage seen in the aerogels prepared with short-chain
alkyl group solvents was higher than that seen in alkyl groups with
longer chains (Table 2).
The nanostructures of all aerogels investigated by TEM are presented in Fig. 5. The isopropanol solvent strongly promoted the
formation of a highly branched polymeric structure in the alcogels. The fine polymeric structure is clearly evident in the TEM
images from the aerogels prepared with the isopropanol solvent,
Fig. 5. Transmission electron micrographs of TEOS-based silica aerogels prepared with various solvent (a) methanol (b) ethanol (c) butanol and (d) isopropanol.
A. Hilonga et al. / Journal of Alloys and Compounds 487 (2009) 744–750
Fig. 6. N2 adsorption–desorption isotherms obtained for the TEOS-based silica aerogels prepared with various solvent and drying at ambient pressure.
while the other samples have less polymeric structures. In addition, the aerogels synthesized with the isopropanol solvent showed
a well-developed nano-porous structure consisting of aggregations
of primary particles of about 15 nm in size, as shown in Fig. 5(d).
As shown in Table 2, the bulk density of the aerogels decreased
as the length of alkyl chains in the solvent increased. This is because
the length of alkyl chain in the solvent tends to increase the degree
of polymerization of the TEOS precursor and provide a flexible silica
network. The flexible network can withstand the drying stress, so
the drying shrinkage of the gel and, consequently, the bulk density
of the resulting aerogels is reduced. Moreover, extensive polymerization leads to dense cross-linking which restricts the relative
movement of the polymer chains under the action of an external
force, resulting in the formation of a rigid polymer. A low degree
of polymerization results in a polymer with a low Young’s modulus which can easily be deformed [34]. The optical transmittance
obtained (at 750 nm) was found to be higher (91%) for the aerogels
prepared with the isopropanol solvent than the aerogels prepared
using solvents with shorter alkyl chains (Fig. 4). As shown in Fig. 4
(a and b), multiple cracks existed inside the aerogels prepared with
the methanol solvent. These cracks scattered the incident light,
resulting in a reduction in optical transmittance compared to aerogels prepared using the isopropanol solvent. In addition, optical
transmission decreased with a decrease in the incident wavelength.
This is because the Rayleigh scattering becomes more effective at
shorter wavelengths and thereby reduces the optical transmission
[35].
3.4. Textural properties of the TEOS-alcohol-based silica aerogels
The specific surface areas of the aerogels, as determined by
the standard BET method, are summarized in Table 2. All aerogels
exhibited high specific surface areas in the range of 900–1200 m2 /g.
The specific surface area was found to be higher for the aerogels
prepared using the isopropanol solvent than the aerogels prepared
using the solvents with shorter alkyl chains. This is because efficient surface modification by the tri-methyl groups took place in
the alcogels prepared using the isopropanol solvent via the onestep solvent exchange surface modification process. The average
pore diameters (pd) of the TEOS-based aerogels prepared using different solvents were in the range of 11–14 nm. The increase in pore
diameter (particularly observed in isopropanol-based aerogels) can
be attributed to the fact that more surface modification and polymerization took place. Isopropanol also enhanced the spring-back
effect, resulting in less volume shrinkage and a high pore diameter.
The nitrogen adsorption–desorption isotherms obtained at 77 K
are shown in Fig. 6. The nitrogen physisorption isotherms obtained
749
Fig. 7. BET pore size distribution profiles of the ambient pressure dried silica aerogels prepared with various solvents.
for all samples exhibited Type IV hysteresis loops, which are
generally observed in mesoporous materials [36]. The desorption
cycles of the isotherms showed hysteresis loops in all of the aerogels, which were attributed to capillary condensation occurring
in the mesopores [37]. Fig. 7 shows the pore size distributions
(PSDs) of the aerogels synthesized using four different solvents:
methanol, ethanol, isopropanol, and butanol. The aerogels prepared
with the methanol solvent showed a relatively narrow PSD with
a pronounced peak that corresponds to pores with diameters of
8–10 nm. The aerogels prepared with ethanol, isopropanol, and
butanol exhibited broad PSDs. The peak pore diameter shifted to
a higher value in the aerogels prepared by ethanol, isopropanol,
and butanol solvents. All of the aerogels showed a pronounced
peak in the mesopore region even after drying at ambient pressure.
4. Conclusions
Monolithic silica aerogels with an extremely low density
(0.041 g/cm3 ) and large surface area (1150 m2 /g) were synthesized using a two-step acid–base sol–gel polymerization of
tetraethoxysilane (TEOS) with isopropanol solvent via a one-step
solvent exchange surface modification process and ambient pressure drying (APD). The resulting silica aerogels possessed a low
bulk density and high porosity, similar to those produced by conventional supercritical drying. The success of the approach lies in
the fact that the two-step sol–gel polymerization of TEOS using
the isopropanol solvent promoted formation of a highly branched
polymeric structure in the alcogel that withstood drying stress
during APD, resulting in a monolithic aerogel. Sufficient chemical modification can be achieved by the one-step solvent exchange
surface modification treatment via solvent/TMCS/perfluorohexane.
We propose perfluorohexane as the best solution for the onestep solvent exchange process as it has the lowest surface
tension value (11.91 N/m) which is a significant factor when drying gels at ambient pressure. The new route suggested in this
study is a simple method for the synthesis at ambient pressure
of TEOS-based monolithic silica aerogels with desired properties.
Acknowledgements
We express our gratitude to the Ministry of Commerce and
Industries of the Republic of Korea for financial support under the
R&D Innovation Fund for the Small and Medium Business Administration (Project Application No. S1017370).
750
A. Hilonga et al. / Journal of Alloys and Compounds 487 (2009) 744–750
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