A Cu(II)-quinoline complex immobilized on a silica support was prepared to enhance the degradation of dyes. Mesoporous silica functionalized with this Cu(II) complex was turned into a photo-Fenton-like catalyst. Various techniques were used to characterize the resulting material, and the catalytic activity was determined by the degradation of methylene blue (MB) under UV light irradiation. The Cu(II) ion was successfully coordinated to the quinoline ligand on a silica support. The dye degradation investigation has shown that 95% of the dye was degraded in 2.5 h. The active radical species involved in the reaction were OH• and O2 •-, suggesting that a peroxo complex intermediate might be formed during degradation processes.
A Cu(II)-quinoline complex immobilized on a silica support was prepared to enhance the degradation of dyes. Mesoporous silica functionalized with this Cu(II) complex was turned into a photo-Fenton-like catalyst. Various techniques were used to characterize the resulting material, and the catalytic activity was determined by the degradation of methylene blue (MB) under UV light irradiation. The Cu(II) ion was successfully coordinated to the quinoline ligand on a silica support. The dye degradation investigation has shown that 95% of the dye was degraded in 2.5 h. The active radical species involved in the reaction were OH• and O2 •-, suggesting that a peroxo complex intermediate might be formed during degradation processes.
A dye is usually an organic
or inorganic compound giving color
to substrates such as food, fabric, textile cloth, paper, or plastic.[1] The worldwide production of dyes is over 700,000
tons per year.[2−4] About 1–20% of the total world production
of dyes is lost during the dyeing process and is released in the textile
effluents.[5−8] The washed-out dyes can potentially contaminate natural water and
the ecosystem. In recent years, advanced oxidation processes (AOPs)
have been used for wastewater treatment. The in situ generation of
HO• is the basic principle of this process.[9,10] One promising AOP is the Fenton reaction. The Fenton reaction uses
iron ions (Fe2+/Fe3+) as the catalysts in the
presence of H2O2. It was reported that the Fenton
reaction has a high performance and simple method of operation at
room temperature.[11,12] However, a limitation of the
Fenton reaction is the operational pH range of 2–4.[13] To overcome this disadvantage, an improvement
of the Fenton reaction has been investigated. Copper ions have been
reported as an alternative for iron ions in the Fenton reaction having
the advantage of working over a broader pH range (3–7).[14] In addition, the coordination of copper ions
with organic acids, pyridine, amino acids, and chelating agents in
solution systems has been shown to enhance the generation of HO•.[15−17] Furthermore, extra reactions of the Cu-based Fenton
catalyst can occur with photo assistance. For example, light can induce
the decrease of the oxidation number of Cu(II)–Cu(I) through
ligand to metal charge transfer (LMCT), which is followed by the generation
of HO• for the decomposition of substrates.[18] The aim of this research is to investigate a
new photo-Fenton-like catalyst. Inspired by copper complexes with
organic ligands, quinoline was used as a ligand to form a complex
with a Cu(II) ion and immobilized onto a modified silica for the decomposition
of methylene blue (MB). The obtained catalyst was investigated by
spectroscopic techniques and morphology methods. The catalytic performance
of the prepared catalyst was determined from studies of MB degradation
under the selected experimental conditions, including catalyst dosage,
H2O2 concentration, time, and the UV light irradiation
effect.
Results and Discussion
Catalyst Synthesis and Characterization
The SiO2 used in this work was amorphous silica, showing
a broad peak at 22° (Figure S1) in
its X-ray diffraction (XRD) spectra.[19] After
the surface modifications, only characteristic peaks in the infrared
(IR) region of silica were observed (Figure S2) in the FTIR spectra. This is due to the fact that the concentration
of (3-aminopropyl) triethoxysilane (APTES) and the Cu(II)–quinoline
complex was too low when compared with the amount of silica.[20] The SiO2 was spherical with different
degrees of aggregation and dimensions smaller than 100 nm (Figure ) as the reaction
was performed with a high concentration of water (14 mol L–1). In addition, the concentration of ammonia was relatively low (1.4
mol L–1) to inhibit the aggregation of the nascent
silica particles.[21] No change in morphology
of the silica particles was observed as a result of the modifications
and only more extensive aggregation of the silica particles was observed.
Figure 1
SEM images
of (a) SiO2, (b) SiO2–NH2,
and (c) SiO2–Cu(II)–quinoline complexes.
SEM images
of (a) SiO2, (b) SiO2–NH2,
and (c) SiO2–Cu(II)–quinoline complexes.The elemental mapping performed by energy dispersive
X-ray spectroscopy
(EDX) demonstrated that all elements in the catalyst were uniformly
distributed on the silica surface (Figure ). Two peaks of Cu at 0.930 and 8.040 keV
provide key evidence that there is Cu present in the silica (Figure ). The total Cu content
was found to be 0.6 wt % in the selected area.
Figure 2
EDX mapping of the SiO2–Cu(II)–quinoline
complex.
Figure 3
EDX spectra of the SiO2–Cu(II)–quinoline
complex.
EDX mapping of the SiO2–Cu(II)–quinoline
complex.EDX spectra of the SiO2–Cu(II)–quinoline
complex.Adsorption–desorption isotherm for the different
materials
was measured and is shown in Figure . The specific surface area (SBET) was calculated using the Brunauer–Emmett–Teller
(BET) equation. As shown in Table , the SBET of SiO2 (527.3 m2 g–1) decreased to 216.4 and
103.6 m2 g–1 in SiO2–NH2 and SiO2–Cu(II)–quinoline complexes,
respectively. Pore volume (Vpmeso) and
pore size distributions were obtained by the Barrett–Joyner–Halenda
(BJH) model. The values of these parameters also decrease and remain
in the characteristic ranges of mesoporous materials.[22]
Figure 4
N2 adsorption–desorption isotherms of SiO2, SiO2–NH2, and SiO2–Cu(II) complexes.
Table 1
Textural Properties of SiO2, SiO2–NH2, and SiO2–Cu(II)
Complexes
sample
SBET (m2 g–1)
Vpmeso (cm3 g–1)
pore size distribution (nm)
SiO2
527.3
0.41
3.36
SiO2–NH2
216.4
0.16
3.23
SiO2–Cu(II)–quinoline complex
103.6
0.050
2.97
N2 adsorption–desorption isotherms of SiO2, SiO2–NH2, and SiO2–Cu(II) complexes.X-ray photoelectron spectroscopy (XPS) spectra of
SiO2–quinoline before and after loading with Cu(II)
are shown
in Figure a. Peaks
of Si 2p, C 1s, N 1s, and O 1s can be observed at bonding energy (BE)
values of 103, 285, 399, and 532 eV, respectively. The comparison
of the survey spectra of SiO2–quinoline before and
after loading Cu(II) ions indicates the presence of the Cu element.
A new peak of Cu(II) was observed at a binding energy of 935 eV. The
value was assigned to the Cu 2p orbital. The strong Cu 2p1/2 and Cu 2p3/2 peaks at 952.1 and 932.3 eV were in an agreement
with the oxidation state +2 of Cu 2p (Figure b). As shown in Figure c,d, the high-resolution of the N 1s spectrum
fitted with deconvolution peaks of N element reveals peaks at 399.1
eV (primary amines) and 400.1 eV (imines).[23−25] These binding
energies (BEs) of the nitrogen atoms were shifted to 399.2 and 400.4
eV, respectively, due to the electron density of N atoms being donated
to form a shared bond with Cu(II) ions.[26]
Figure 5
(a)
XPS survey spectra of SiO2–quinoline before
and after loading of Cu(II), and the high-resolution XPS for (b) Cu
2p and N 1s (c) before and (d) after loading of Cu(II).
(a)
XPS survey spectra of SiO2–quinoline before
and after loading of Cu(II), and the high-resolution XPS for (b) Cu
2p and N 1s (c) before and (d) after loading of Cu(II).The band gap of SiO2 and SiO2–Cu(II)
complexes was determined through the Kubelka–Munk function. Figure shows the extrapolation
of the linear part of the plot on the energy axis. The observed band
gaps were 5.8 and 2.8 eV, respectively. This result indicates that
the addition of the Cu(II)–quinoline complex to the silica
support decreases the band gap of SiO2.
Figure 6
Kubelka–Munk function
of (a) SiO2 and (b) SiO2–Cu(II)–quinoline
complexes.
Kubelka–Munk function
of (a) SiO2 and (b) SiO2–Cu(II)–quinoline
complexes.
Photo-Fenton-Like Degradation of MB
The catalytic performance of the catalyst was evaluated using the
degradation of MB under UV light irradiation over 150 min as a model
reaction. The control experiments included MB/cat. (UV) and MB/cat./H2O2 (dark), were performed under identical conditions.
The time profile of MB degradation over the catalyst in different
conditions is illustrated in Figure a. The amounts of MB removed after 150 min of experiments
MB/cat. (UV) and MB/cat./H2O2 were 15.8% and
54, respectively. The best MB removal (95%) was obtained for MB/cat./H2O2 (UV). The photocatalytic activity was quantitatively
investigated by the calculation of the apparent rate constant (k) of the catalyst using eq .where C is the
concentration of the MB solution (mg L–1) at the
reaction time t, C30 is
the concentration of the MB solution at 30 min, and k is the apparent reaction rate constant. The slope (k value in min–1) was obtained from the linear plot
of −ln(C/C30) vs t (min). The k value
increased from −0.04 to 0.49 and 2.43 (10–2 min–1) (Figure b). This result also shows that the reaction rate was
enhanced the most in the condition system MB/cat./H2O2 (UV).
Figure 7
(a) Catalytic efficiency and (b) pseudo-first-order kinetic
plot
for the degradation of MB in different reaction systems.
(a) Catalytic efficiency and (b) pseudo-first-order kinetic
plot
for the degradation of MB in different reaction systems.The changes in the UV–vis spectra of MB
of the MB/cat./H2O2 (UV) system are shown in Figure . The characteristic
band of MB (662 nm)
decreased dramatically. Also, no new peak was observed, which suggests
that the chromophore of MB was decomposed during the reaction.[27]
Figure 8
Changes in the spectra of MB.
Changes in the spectra of MB.Further experiments were conducted to determine
the effect of H2O2 concentration. More extensive
degradation with
higher k values was observed when the H2O2 content was increased (Figure a). The degradation efficiency at 2.50 h
increased from 15.8 to 95.0%. In addition, k values
for MB degradation increased with increasing hydrogen peroxide concentration
from −0.07 to 2.35 × 10–2 min–1 (Figure b). This
finding suggests that H2O2 affects the MB degradation.
Figure 9
(a) Catalytic
efficiency and (b) pseudo-first-order kinetic plot
for degradation of MB using different concentrations of H2O2.
(a) Catalytic
efficiency and (b) pseudo-first-order kinetic plot
for degradation of MB using different concentrations of H2O2.There are various radicals involved in the Fenton-based
reaction.
Important active radical species such as HO• and
O2•–/HOO• were
detected. The type of radical species in the MB degradation was determined
using coumarin, isopropyl alcohol (IPA), and p-benzoquinone
(BQ) as probes. Coumarin is a poorly fluorescent molecule that was
used as a probe for the detection of the HO• radical.
It produces the highly fluorescent compound 7-hydroxycoumarin upon
the reaction with HO• radicals. The amount of 7-hydroxycoumarin
reflects the amount of HO• generated in the system.
The fluorescent spectra of the reaction mixture recorded at different
time points (0–150 min) are shown in Figure . After exposing the reaction mixture to
UV light for 30 min (60 min of total reaction time), coumarin was
hydroxylated to 7-hydroxy-coumarin confirmed by the strong emission
band at 460 nm. The band increased continuously with increasing exposure
time. These results suggest that the HO• radical
was generated in the conditions of cat./H2O2 under UV irradiation.
Figure 10
Changes in the fluorescence spectra of coumarin
from 0 to 150 min.
Changes in the fluorescence spectra of coumarin
from 0 to 150 min.Furthermore, results of radical trapping experiments
are shown
in Figure . The
degradation of MB was not interrupted by the addition of HO• radical scavenger isopropyl alcohol (IPA). However, the HO• radical was still involved in MB degradation, as confirmed by the
production of 7-hydroxycoumarin. On the other hand, O2•– trapping by p-benzoquinone
(BQ) shows competitiveness with MB degradation.
Figure 11
(a) Catalytic efficiency
and (b) pseudo-first-order kinetic plot
of the catalyst in the presence of radical active species-trapping
agents.
(a) Catalytic efficiency
and (b) pseudo-first-order kinetic plot
of the catalyst in the presence of radical active species-trapping
agents.The results are in accordance with the radical
generation by the
Cu(II)/organic ligand/H2O2 system, which simultaneously
generates HO• and O2•–/HOO• radicals via a complex mechanism forming
a peroxo complex.[28] Therefore, the mechanism
of the catalyst function in the photo-Fenton-like reaction is proposed
in Scheme .[29] The catalysis takes place on the surface of
the silica particles, where the active site of the [L–Cu2+] complex was immobilized. The unsaturated [L–Cu2+] complex could bind peroxide to form [L–Cu2+(−O2H)] (pathway (1)), which can subsequently
transform into a peroxo complex [L–Cu+(O2H)•] as a result of charge transfer between a hydroperoxide
anion (−O2H) and Cu2+ (pathway
(2)).[30,31] The peroxo complex can then react with H2O2 to produce HO• radicals (pathway
(4)).[30−34] The [L–Cu2+(−O2H)]
can also be regarded as an oxidant based on a complex mechanism, directly
oxidizing substrates through pathway (6).[35,36] In addition, the copper redox cycle with HO• and
the production of dissolved O2 (pathway (4)) are likely
to involve a catalytic cycle (pathways (7) and (8)).[20,37−41] During these processes, the substrate in the reaction can be excited
(pathway (9)), transferring an electron to the metal-centered orbitals
(pathway (10)) with this substrate to the metal charge transfer (SMCT)
process contributing to the decolorization of the substrate via the
loss of conjugation of the double bonds in the molecule.[40] With photo assistance, the photoreduction of
Cu2+ to Cu+ occurs through charge transfer between
the ligand and the metal. This is followed by the production of an
oxidized ligand (L+) (pathway (11)), which could subsequently
oxidize substrate molecules (pathway (13)).
Scheme 1
Proposed Mechanism
of Action of the Heterogeneous Cu–L Complex
Photo-Fenton-Like System
The stability of the catalyst was studied in
consecutive photo-Fenton-like
reactions for MB degradation. The results of this investigation are
shown in Figure S3. A large capacity of
adsorption of the catalyst was found after the first reaction run,
and the degradation efficiency by the photo-Fenton-like reaction decreased.
The apparent rate constants are 3.65 × 10–2 and 1.04 × 10–2 min–1 for
the first and second reaction runs, respectively. These findings suggest
that the catalysis performance could be affected by the leaching of
active sites, which may then be decomposed by self-degradation reactions
during the MB degradation.[37,42]
Conclusions
A new photo-Fenton-like
catalyst was prepared, as evidenced by
the reported characterizations. MB was degraded under UV light irradiation
in the presence of this catalyst in 2.5 h. However, the catalyst was
lost during the catalytic reaction. The development of this type of
catalyst for future use remains a challenge, especially in terms of
protection from self-degradation, which could be achieved by operating
under milder conditions.
Materials and Experimental Section
Materials
All chemicals were used
without further purification. Ammonium hydroxide (NH4OH,
28 wt %), (3-aminopropyl) triethoxysilane (APTES, 99%), 8-aminoquinoline
(C9H8N2, 98%), ethanol (C2H5OH, 99.8%), tetraethyl orthosilicate (TEOS, 98%), isopropanol
(IPA, C3H8O), glutaraldehyde 25 wt % (C5H8O2), glacial acetic acid (CH3COOH), and coumarin (C9H6O2, 99%)
were purchased from Sigma-Aldrich. p-Benzoquinone
(BQ, C6H4O2) and hydrogen peroxide
30 wt % (H2O2) were purchased from MERCK. Copper(Il)
sulfate pentahydrate (CuSO4·5H2O, 98%)
was purchased from Ajax Finechem. Deionized water (DI) was used throughout
the entire experiment.
Synthesis
The synthesis of the Cu(II)–quinoline
complex immobilized on silica is shown in Scheme .
Scheme 2
Synthesis of the Cu(II)–Quinoline
Complex on Silica Support
Preparation of Silica Support
The
silica support was prepared by the hydrolysis of TEOS.[43] A mixture of ethanol (170 mL) and DI water (511
mL) was sonicated for 10 min. This was followed by a dropwise addition
of TEOS (7.0 mL) to the reaction mixture under ultrasonication. After
20 min, 28 wt % NH4OH (12 mL) was added to catalyze the
condensation reaction. The reaction mixture was then stirred at 750
rpm for 60 min. Then, the formation of a white turbid suspension was
observed. The solid was dried at 100 °C for 5 h and obtained
as the silica support (1.8 g). This material was denoted SiO2.
Preparation of Amine-Functionalized Silica
Support
The prepared silica support was dried at 100 °C
for 30 min before further use. The dried solid (1.2 g) was dispersed
in ethanol (10 mL) and continually stirred at 500 rpm. Then, APTES
(3.6 mmol, 0.84 mL) was slowly added to the suspension. After 30 min,
DI water (7.2 mmol, 130 μL) was added to generate the alkoxide
groups of APTES. The amount of DI water was twice the amount for complete
hydrolysis of APTES.[22] The reaction was
continued for further 30 min. The solids (1.1 g) were obtained after
drying at 100 °C for 2 h. The prepared amine-functionalized silica
was denoted SiO2–NH2.
Preparation of the Cu(II)–Quinoline
Complex Immobilized on Silica Support
A total of 1.0 g of
amine-functionalized silica support (SiO2–NH2) was dispersed in DI water (4 mL). Then, the suspension was
sonicated for 10 min. 8-Aminoquinoline (432 mg, 3 mmol) dissolved
in 5 mL of CH3CN was slowly added into the suspension.
After 30 min, the mixture of glutaraldehyde (2.4 mL, 6 mmol) and glacial
acetic acid (0.69 mL, 12 mmol) was added dropwise. The reaction was
carried out at room temperature for 12 h. Afterward, 20 mL of a 0.1
M copper(II) sulfate solution was added to the reaction mixture, which
was then stirred at 60 °C for 5 h.[20] The product (0.8 g) was collected by centrifugation at 9000 rpm,
washed by DI water, and dried at 80 °C for 4 h. The product was
denoted the SiO2–Cu(II)–quinoline complex
or catalyst.
Material Characterization
The surface
of the samples was investigated by Fourier transform infrared spectroscopy-attenuated
total reflectance (FTIR-ATR, Spectrum GX). The structure and composition
were investigated by powder X-ray diffraction (XRD, Panalytical/Expert
2θ: 5–140°). Morphologies were observed by field
emission scanning electron microscopy (FESEM, LEO1455VP) equipped
with energy-dispersive X-ray spectroscopy (EDX). Specific surface
areas of the samples were evaluated by Brunauer, Emmett, and Teller
(BET) surface analysis (TriStar II 3020). The elemental composition
and the surface chemical state were investigated by X-ray photoelectron
spectroscopy (XPS, AXIS Ultra DLD). Characteristic reflectance spectra
were obtained by diffuse reflectance spectroscopy (DRS, Agilent 8453).
The dye concentration was measured by a UV–vis spectrophotometer
(UV-6100 UV/VIS).
Photocatalytic Experiments
Photocatalytic
performance was investigated in a closed chamber with vertical light
irradiation. Ambient temperature inside of the chamber was maintained
at 28 °C with air cooling. The light source was a 30 W UV lamp,
which was placed so that the distance between the level of the solution
and the light source was 13 cm. The reactions were carried out in
a batch experiment setup to avoid the loss of catalyst dosage. In
a typical experiment, 1.0 mg of the catalyst (0.2 g L–1) was added to a 5 ppm solution of MB (5.0 mL) and the mixture was
ultrasonicated for 2 min. The reaction was continually stirred in
the dark for 30 min to reach adsorption equilibrium (Figure S4). Then, one of the reactions was taken out and centrifuged
to obtain a clear supernatant. The MB concentration determined at
this point was labeled as C30. After that,
30 wt % H2O2 was added to the reaction mixture
and the UV lamp was turned on. At predetermined reaction time points
(30, 60, and 120 min), the reaction mixture was centrifuged and analyzed.
The concentrations of MB were determined from its maximum absorption
(664 nm) using a UV–vis spectrometer. Decolorization efficiency
of MB was calculated using eq .where C is the
concentration of the MB solution at the reaction time t, C0 is the initial concentration of
the MB solution at 0 min, and A and A0 are the corresponding absorption values.
Authors: G McMullan; C Meehan; A Conneely; N Kirby; T Robinson; P Nigam; I M Banat; R Marchant; W F Smyth Journal: Appl Microbiol Biotechnol Date: 2001-07 Impact factor: 4.813
Authors: Jessica I Nieto-Juarez; Katarzyna Pierzchła; Andrzej Sienkiewicz; Tamar Kohn Journal: Environ Sci Technol Date: 2010-05-01 Impact factor: 9.028
Authors: Isabel Mesquita; Luís C Matos; Filipa Duarte; F J Maldonado-Hódar; Adélio Mendes; Luis M Madeira Journal: J Hazard Mater Date: 2012-08-24 Impact factor: 10.588