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mechanism, the sulfated zirconia particles were also synthesized
without PVP under the same conditions. In contrast, only irregular
sulfated zirconia particles were obtained, and the diameters of these
irregular particles vary greatly from 5 to 20 μm. In fact, highly dis-
persed sulfated zirconia nanoparticles can only be obtained within a
narrow window of the concentration of sulfuric acid. The mechanism
of the formation of the synthesized zirconia nanoparticles is proposed
(Fig. S1). PVP plays key roles in preventing hard agglomerate forma-
tion during glycothermal process. Nanometer-sized particles of
supermicrostructured surfactant-zirconia composite with surface hy-
droxyl groups could form as soon as the Zr precursor is added to the
surfactant solution under given condition. The unconsumed surfac-
tant molecules cover the nanoparticles of the supermicrostructured
surfactant-zirconia composite due to the affinity between the hy-
droxyl groups of the nanoparticles and the carbonyl of the surfactant
molecules. The presence of surfactant PVP molecules surrounding the
surface of the composite improves the size uniformity and promotes
the formation of well-dispersed sulfated zirconia nanoparticles. The
presence of S in sulfated zirconia detected by XPS (Fig. 4) also pro-
motes the formation of the PVP-nanoparticle composite. In the
study, glycothermal process was conducted at 180 °C. Hence, in
order to obtain high dispersion of the sulfated zirconia nanoparticles,
an apropriate temperature, autoclave pressure, the presence of sulfur
and the addition of PVP are indispensable in glycothermal reaction.
Fig. 4. FT-IR spectra of the synthesized sulfated zirconia.
zirconia nanoparticles with narrow size distribution and low aggrega-
tion. However, the reaction mechanisms in nonaqueous solution are
complex, and currently there is very limited information regarding
the reaction thermodynamics, kinetics, and underlying crystallization
mechanisms. Only a few investigations have dealt with the use of
diols to synthesize crystalline zirconia powders under hydrothermal
conditions [13]. In order to get more information about the forming
3.3. Catalytic performances in synthesis of bis(indolyl)methane
derivatives and biodiesel
The catalytic activity of the as-synthesized nanocomposite was eval-
uated by synthesizing bis(indolyl)methanes via electrophilic substitu-
tion reaction of indole with various aldehydes and biodiesel via the
esterification of long-chain free fatty acids. Indoles and their derivatives
are important intermediates in organic synthesis and widely featured in
variety of pharmacologically active compounds [14]. Table 1 lists the
synthesis of bis(indolyl)methane derivatives with the synthesized sul-
fated zirconia nanoparticles as the catalyst. When the molecular frac-
tion of the catalyst was 30%, based on the mole number of indole, the
yield of diindolylphenylmethane was up to 97% in the reaction time of
24 h at room temperature (Table 1, entry 3). Entries 1 and 2 of
Table 1 show the yield of diindolylphenylmethanes under different re-
action conditions. When the amount of sulfated zirconia increased
from 15% to 30%, the yield of diindolylphenylmethane increased from
36% to 57% in the reaction time of 6 h. Under optimized conditions, var-
ious aldehydes smoothly reacted with indole and formed correspond-
ing bis(indolyl)methanes in excellent yields in desired reaction times.
Hence, the synthesized sulfated zirconia is an efficient catalyst for the
synthesis of bis(indolyl)methanes.
As a “green fuel,” biodiesel is gaining much attention in recent
years as a renewable fuel [15]. In the present work, biodiesel was syn-
thesized via the esterification of long-chain free fatty acids in the
presence of the synthesized sulfated zirconia nanoparticles as the cat-
alyst. Table 2 shows the esterification of palmitic acid and methanol
under different conditions. As the palmitic acid:methanol molar
ratio increases, the conversion of palmitic acid increases first then de-
creases. The optimal molar ratio of palmitic acid:methanol was 1:40.
Similar resluts can also be found in the literature [16]. When the alco-
hol concentration increases, the tendency of equilibrium, in principle,
would be to move in favor of products, increasing thereby the yield of
the ester formed. In addition, the increase in the concentration of al-
cohol may be promoting a reduction in the viscosity of the mixture,
leading to better mixing of reagents and catalyst and to an improve-
ment in the rate of mass transfer, resulting thus in a higher conver-
sion. When the molar ratio of palmitic acid:methanol is over 1:40,
there is a competition between methanol and palmitic acid for active
sites of the catalyst and lead to the decrease of catalytic activity. Like-
wise, for entry 8-12, as the catalyst loading increases, the conversion
Fig. 5. SEM images of sulfated zirconia particles synthesized under different synthesis
conditions (a: 0.5 g Zr(OH)4, 2.0 g PVP 1.2 mL H2SO4; b: 1.0 g Zr(OH)4, 2.0 g PVP
1.2 mL H2SO4).