S. Bouguerra Neji et al. / C. R. Chimie xxx (2016) 1e7
3
2
.6. TOC removal and leaching-off of Fe ions
that the reaction rate increased (p < 0.05) when adding
acid-activated catalyst clays according to the following
order: K10 < KSF z KSF/0. The enhancement of PAA con-
version is due to the increase in hydroxyl radicals by the
combination of the oxidant hydrogen peroxide and the
redox process in the presence of iron ions.
The total organic carbon TOC of the solution (in mg of
carbon per litre of solution) was measured with a Shimadzu
Model 5050 TOC-analyzer. Iron leaching was evaluated by
measuring iron concentrations at the end of the conversion
reaction using an atomic absorption analyzer,
PerkinElmer 1101 B, with a hollow cathode lamp having
mA current.
a
Acid treatment in commercial-type montmorillonite
KSF/0, KSF and K10 is performed using H SO .This behav-
2 4
8
iour promoted an increase in the number of acid sites of
moderate strength compared to natural clay [15]. The acid
strength of the catalysts can be characterized by the pH
value of their 10% water suspension, while the number of
sites by the intensities of the Brønsted- and Lewis-
characteristic bands in the IR spectra after pyridine
adsorption as previously described (Table 1) [10]. The acid
strength increases from K10 to KSF and KSF/0. Based on the
data shown in Table 1, no correlation was found between
either the surface area or average pore diameter with the
catalytic activity. Indeed, K10, which recorded the highest
2
.7. Antioxidant activity
Evaluation of samples' antioxidant activity withdrawn
at regular intervals was assessed by the DPPH (1,1-
diphenyl-2-picryl hydrazyl) radical scavenging assay [13].
Aliquots (50 mL) were added to 5 mL of methanolic solution
ꢁ
6
ꢁ1
containing DPPH radicals (6 ꢂ 10 mol L ). After 30 min
of incubation period under room temperature and in the
dark, the absorbance was read at 520 nm using a Shimadzu
UV-160 A spectrophotometer. DPPH radical scavenging
activity was calculated as follows:
2
surface area (249 m /g), led to the slowest reaction rate.
The increase of the catalytic conversion could be correlated
to the total acidity surface of the catalyst. Besides, lower pH
clay values resulted in a significant increase (p < 0.05) of
the reaction rate. Both KSF and KSF/0 with initial pH of 1.5
and 1.3, respectively, led to total PAA conversion, where
only 30% PAA conversion yield was observed for the K10
catalyst at initial pH 4.5. KSF/0 and KSF are more active in
the conversion of PAA because of their stronger acidity. So
the catalytic activity of these K-catalysts is controlled by
their acidity.
A
control ꢁ Asample
DPPH radical
scavenging activity ¼
ꢂ 100
A
control
A lower absorbance of the reaction mixture indicates a
higher DPPH radical-scavenging activity. Butylated
hydroxyanisole (BHA) was used as a standard. The test was
carried out in triplicate.
2
.8. Statistical analysis
On the other hand, higher catalytic activity of KSF could
be attributed to its high iron content. As a matter of fact,
hydroxyl radicals can be easily produced through a redox
process known as the Fenton reaction in the presence of
iron ions [16]. They are generally schematized as follows:
Results were expressed as mean ± standard deviation
(
mean ± SD). The whole analysis was carried out with
GraphPad Prism 4.02 for Windows (GraphPad Software,
San Diego, CA). Significant differences for comparison of
the yield of PAA conversion were determined by one-way
ANOVA, followed by Tukey's post-hoc test for multiple
comparisons with a statistical significance of p ꢃ 0.05.
ꢀ
Fe2 þ H
þ
O
/ Fe þ OHꢁ
3þ
þ
OH
2
2
ꢀ
Fe2
þ
þ
OH / Fe þ OHꢁ
3þ
3
. Results and discussion
3
.1. Phenyl acetic acid conversion: preliminary experiments
ꢀ
ꢀ
RH þ OH / H
2
O þ
R
A variety of montmorillonite catalysts KSF, KSF/0 and
K10 were investigated in the PAA acid conversion. Mont-
morillonite is a member of the smectite clay family and has
a 2:1 structure i.e. an octahedral layer of Al is sandwiched
between two tetrahedral layers of silicon coordinated with
oxygen (TOT) exhibiting overall weak acidity. The crystal-
line sheets of negatively charged aluminosilicates are
balanced by hydrated cations (Na , K or Ca ) in the
interlayer spaces of montmorillonite. The most interesting
features of the smectite clay are their intercalation,
swelling and cation exchange capacity which improve the
catalytic properties of smectite clay [14]. Fig. 1 shows the
conversion profiles of the reaction times at the room tem-
perature over the studied catalysts in the presence of
hydrogen peroxide. Blank controls made without the
catalyst were also analysed, and no significant (p > 0.05)
PAA conversion was observed. However, it can be noted
ꢀ
R þ Fe3þ / R þ Fe2þ
þ
Even with its lower iron content compared to KSF's one,
the KSF/0 catalyst yielded high PAA conversion similar to
KSF. This result could be attributed to the high acidic pH
(2.97) of the aqueous phenolic solution mixed with KSF/0
particles (Table 2). Such acidic pH values (around 3) have
been reported to be optimum for homogenous Fenton
processes. The latter corresponds to the maximum con-
þ
þ
2þ
2
þ
centration of the active Fe species and the lowest rate of
parasitic decomposition. By increasing the pH, the
precipitation of the insoluble ferric hydroxides takes place
2 2
H O
and the decomposition of H
[17].
2 2
O becomes preponderant
Please cite this article in press as: S. Bouguerra Neji, et al., Novel mild synthesis of high-added-value p-hydroxyphenyl acetic acid
and 3,4-dihydroxyphenyl acetic acid using the acidic clay/hydrogen peroxide catalytic system, Comptes Rendus Chimie (2016),