Photocatalytic Degradation of a Herbicide Namely Glyphosate and
Hexazinone from the Surface Water which will be Used as Drinking
Water via Polyaniline/ZnWO4/WO3 and Evaluation of Acute Toxicity
Assays
RUKİYE ÖZTEKİN a , DELİA TERESA SPONZA a , *
a Department of Environmental Engineering
Dokuz Eylül University
Tınaztepe Campus, 35160 Buca/Izmir,
TURKEY
* Corresponding Author
Abstract: - Polyaniline/Zinc tungsten oxide/Tungsten trioxide nanocomposites (PANI/ZnWO4/WO3 NCs) was
prepared to remove glyphosate (GLP) and Hexazinone (HZN) herbicides from the surface water. The properties
of PANI/ZnWO4/WO3 NCs was investigated using XRD, FTIR, FESEM, HRTEM, XPS analyses. The toxicity
of NCs and treated wastewater were investigated using Microtox and Daphnia magna acute toxicity tests. The
effects of increasing values of PANI/ZnWO4/WO3 NCs concentrations (0.1, 0.4, 0.6, 1.0 and 1.5 mg/l),
PANI/ZnWO4/WO3 mass ratios (1:1:3, 1:2:3, 3:1:1 and 3:2:1), GLP concentrations (1, 2, 3 and 4 mg/l),
photodegradation times (2, 10, 15 and 20 min), and solar light powers (20, 40, 60, 80 and 100 W/m2) on the GLP
and HZN removals in the surface were examined. The results of the acute toxicity analysis performed showed
that the acute toxicity in the surface water decreased significantly after photooxidation. The maximum removal
conditions for 3 mg/l GLP (99.90%) were 1 mg/l PANI/ZnWO4/WO3 NCs with a PANI/ZnWO4/WO3 ratio of
1:2:3 after 15 min photodegradation time at 80 W/m2 sun light power while the maximum HZN removal was
obtained as 96% after 15 min photodegradation, under 300 W solar light, at pH=7.0 and at 25oC. The crystalline
monoclinic ZnWO4 and WO3 was detected from XRD analysis while PANI exhibited characteristic broad peak
at 28.91° with an amorphous nature. FTIR spectra showed that pure ZnWO4 has the Zn–O–W vibrational bands.
XPS analysis, exhibited reactive oxygen species. The charge/discharge analysis indicated that WO3 has a larger
particle size that decreases surface density increasing the interplanar spacing between atoms. The introduction of
ZnWO4 and WO3 nanoparticles into the PANI matrix enhanced the surface of the PANI/ZnWO4/WO3 NC.
Key-Words: - Glyphosate; Hexazinone; Daphnia magna acute toxicity test; Herbicie; Microtox acute toxicity
assay; Photocatalytic degradation process; Polyaniline/Zinc tungsten oxide/Tungsten trioxide nanocomposites;
Surface water.
Received: March 22, 2024. Revised: August 14, 2024. Accepted: September 18, 2024. Published: November 29, 2024.
1 Introduction
The increasing of population and industrial
discharges to the environment elevated the limits
required for drinking water supply and large-scale
food production,[1]. Under these conditions in order
to decrease the primary productivity at an
economically steady-state level, some of
agrochemicals has been extensively used to remove
the pesticides and herbicides, [2]. With the excess
utilization of some anthropogenic compounds and as
a result of excess industrialization, water pollution
was elevated, [3]. Synthetic pesticides and herbicides
are usually utilized in agricultural lands to protect the
plants. The herbicides were resistant to biological
degradation, and has high bio-accumulative capacity
consisting from their physicochemical properties
with long half-life of 10–20 years. Their bio
magnification increasing in the ecosystems and in the
humans, [4, 5]. Due to recalcitrant structure of
pesticides their persistence in soil, wastewater, and
surface water elevated excessively and cause to an
environmental problem. They can contaminate the
food chain, and can cause toxicity to human health,
[6]. Due to their high stability, these compounds
cannot be biodegraded. The recent studies showed
that exposure to the aforementioned compounds
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cause to hormonal changes in the immune system and
as a results some neurological and cardiac disease
and some neoplasms occurred, [7, 8]. In order to
remove these organics adsorption and advanced
oxidation processes (AOPs), including Fenton,
photo-Fenton, heterogeneous photocatalysis,
ozonation systems…etc, were used, [9-11]. AOPs are
based on the generation of free radicals, e.g.,
hydroxyl (OH) and superoxide (O2 - ), having high
oxidizing activities in aquatic systems and pollutants
can be converted into lower molecular weight
metabolites and inorganic compounds, [12, 13].
Heterogeneous photocatalysis is an advanced process
through the photoactivation of a semiconductor via
redox reactions under sun and UV ligths, [14]. This
process is very efficient and promising for the
degradation of organic pollutants including dyes,
antibiotics, drugs and pesticides, [9, 15, 16]. Among
the nanocomposites used, metallic nano-oxides; Zinc
oxide (ZnO) and titanium dioxide (TiO2) have been
excesively employed due to their low toxicity, good
availability, chemical stability, large surface
area/porosity, and photo-corrosion, [17, 18]. Nano-
adsorbents and nanocomposites were used for
pesticide removal from wastewater for their
simplicity of operation, relatively low cost and low
energy requirements, [19], Furthermore they have
high specific surface area, chemical/thermal stability,
and affinity to organic pollutants, [20].
Glyphosate herbicide (GLP; N-
phosphomethyl[glycine] or C3H8NO5P), is
metabolized by microorganisms into
aminomethylphosphonic acid (AMPA, known as its
most active metabolite) and methylphosphonic acid
(MPA), [21-23]. After more than 40 years of global
use, GLP has been classified as “probably
carcinogenic” in humans by the International Agency
for Research on Cancer (IARC). In 2019, United
States federal health agency, the Agency for Toxic
Substances and Disease Registry, [24], part of the
Centers for Disease Control and Prevention, [25],
determined that both cancer and non-cancer hazards
derive from exposure to GLP and GLP-based
herbicides.
Hexazinone (HZN) is an example of an atypical
triazine herbicide used for control of woody plants in
reforestation areas and for selective weed control in
sugarcane, pineapple, and alfalfa. The degradation of
HZN in the rat, alfalfa, and sugarcane was reported
by Holt, [26]. The mass spectral identification of
HZN metabolites isolated from rat urine and from
sugarcane extracts was reported by Reiser et al., [26].
Established sugarcane plants grown in the
greenhouse were treated by soil drench with 14C-
HZN and harvested at plant maturity 6 months later.
The total radioactive residues in mature sugarcane
were less than 0.1 ppm, and the intact parent was not
detected, [26].
No more studies were found in the recent
literature about the removal of GLP: For the
degradation of GLP, ultimate and intermediate
metabolites such as AMPA, sarcosine, formaldehyde
and CO2 was produced during microbial
transformation. During abiotic degradation, the
amounts of GLP degraded by non-microbial forms
and biological transformation were negligible, [27].
Low GLP yields was detected in the biodegradability
studies performed by microorganisms. The
biodegradation of GLP in soils by microorganisms is
also rapid, [28]. During the photodegradation of GLP
by sunlight no GLP removals was detected in soils,
[29]. Other some chemical and physicochemical
methods are used with nanocomposites to degrade
the GLP. TiO2 photocatalyst with H2O2 under UV
ligth provided 65-70% GLP removals. TiO2 particles
doped with Mn, Ce or La under visible light provided
79-83% GLP removals. A nanocomposite namely
BiOBr/Fe3O4 consisting from TiO2 nanotubes and
photocatalytic Ce and Fe3O4 was used in GLP
photooxidation. MnO2 and BiVO4 was used as
nanocomposite for the removal of GLP, [30]. In
addition, in the removal of GLP adsorption on a
MnFe2O4-graphene hybrid compound and an
oxidative degradation process assisted with MnO2
has been used, [31]. However, in the aforementioned
studies low GLP yields (79-82%) was detected. In
recent years nnotechnology recently began to used to
photodegrade the GLP with high yields. In the studies
performed by MnO2/C nanocomposite high GLP
yields was detected (87%) due to high specific
surface and high dispersion of the aforementioned
nanocomposite, [28]. An efficient GLP removal was
further achieved using a nanosized resin (D201Cu)
modified with Cu(OH)2), [32]. However, the GLP
yields found in the study given above were not
effectively high and remained between 76% and
81%, [32]. Degradation of HZN has been
investigated by means of photocatalysis of mixed-
phase crystal nano-TiO2. Influences of adsorption,
amount of nano-TiO2, pH and irradiation time on the
photocatalytic process are studied. Results show that
hexazinone is totally degraded within 140 min of
irradiation under pH neutral conditions, [33].
More than 98% degradation of HZN was observed
under 3 J/cm2 UVC (ultraviolet C) fluence in the
presence of 0.5 mM H2O2 at pH 7.0, [34]. Moreover,
the degradation rate enhanced significantly with an
increase in the initial dosage of H2O2, UV fluence,
and contact time in the UV/H2O2 process. The rate of
degradation was lower using secondary effluent than
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that of Milli-Q water due to the presence of dissolved
organics in wastewater. However, the reactions in
bothmatrices obeyed pseudo-first-order kinetics.
Photocatalytic kinetic information of HZN
degradation exhibited first order kinetics from the fit
in the Langmuir–Hinshelwood model with high
yields (96%), [33].
Electrochemical degradation of HZN in aqueous
solution was performed by using Bi-doped PbO2
electrodes as anodes. The main influencing
parameters on the electrocatalytic degradation of
HZN were initial HZN concentration, current
density, initial pH and Na2SO4 concentration. The
electrochemical oxidization reaction of HZN fitted
pseudo-first-order kinetics model with a yield of
95.9%, [35].
Polyaniline (PANI) is a conducting polymer and
organic semiconductor of the semi-flexible rod
polymer family, [36, 37]. PANI has low-cost and
environment-friendly conjugated semiconductor for
the fabrication and is effective under visible light
photocatalysis, [38]. It is a conducting polymer with
an extensive conjugated π-system and high
absorption coefficient under visible light during
charge carrier production. It has a simple processing
with high conductivity during production of
heterojunction nano catalysts. In recent studies many
effective data were detected during photodegradation
of organics when contacting with its interfaces and
individual pollutant components. PAI exhibited high
separation efficiency during photocatalysis for
photogenerated electron–hole pairs, [39].
Zinc tungsten oxide or zinc tungstate (ZnWO4) is
extensively used during photodegradation due to its
high UV light response, tunable band edges, optical
transparency, chemical stability, and suitable
strength, [40]. The band edge tuning of ZnWO4-
centered nanostructures can be organized through
appropriate changes such as heterostructure
construction, doped/combining with transition metal
ions, and noble metals, [41, 42]. By deposition of O2-
ions around the tungsten (W), ZnWO4 forms an
insulated trioxide-oxo-tungsten [WO6] octahedron
with an asymmetric shape showing a local atomic
structure with a wolframite-type space group of P2/c,
[43]. This is an essential inorganic ternary oxide
material with crystalle properties and exhibited
scheelite structure depending on the ionic radius,
[44]. W clusters formed a network since they are
more stable, leading to form the covalent nature of
W–O bonds. During generation of electron-hole
pairs a charge separation process was performed with
dipoles when WO6 clusters act as electron receptors.
Thus, the oxygen vacancies in the Zn/W clusters can
transfer electrons to the W cluster and permanent
dipoles were generated, [45]. The Zn and W
vacancies act as electron capture in the holes since
they are charged negatively, [46].
Tungsten trioxide (WO3) is an n-type
semiconductor photocatalyst having a wide range of
bandgap values (2.7–3.4 eV) providing a better
extension into the visible range, [47]. WO3 as alone
photocatalyst suffers from the limitation of fast
recombination of charge carriers, thereby restricting
its potential during photocatalytic applications, [48].
Several studies suggest that constructing a
heterojunction between two metal oxides with
suitable band arrangements can improve the charge
carrier separation by suppressing the fast
recombination, [49, 50]. Binary heterojunctions like
WO3/Bi2WO6, [51], WO3/ZnO, [52], and WO3/TiO2,
[53], have been constructed to achieve superior
charge separation and high photocatalytic yields.
Bimetallic W has always been very significance for
its chemical inertness structure with low toxicity,
exhibited corrosion-resisstant properties with large
magnetic properties, and economic feasibility, [54].
ZnWO4 possesses wolframite (WO4) structures with
six-fold coordination sites for W exhibited superior
activities under UV light, [55].
The interaction of WO3 with ZnWO4 also
provides high photocatalytic activity by changing the
electronic properties in the material. WO3 it can be
recombinated fastly providing low charge carrier
properties and leading to a lower photocatalytic
degradation efficiency compared to other metal
oxides such as TiO2 or ZnO, [56]. Conversely,
ZnWO4 presents a high ionic conductivity and long
lifetime of photogenerated carriers under sun ligth
irradiation, [56].
PANI has received increasing attention due to its
electron and hole transferring properties. It can be
easily prepared with high chemical stability, [57].
Furthermore, many studies showed that combination
of PANI with semiconductors impoved the interfacial
charge carrier's separation due to the excellent charge
carrier mobility and thus enhance the photo-
electrocatalytic activity, [58]. With g-C3N4/PANI
composite enhanced photocatalytic yields was
detected for degradation of methylene blue (MB)
dye, [59]. Wang et al., [60], synthesized ZnWO4
modified by polyaniline (PANI/ZnWO4) and found
that the photocatalytic activity of PANI/ZnWO4
composites was higher than ZnWO4. This was
attributed to the synergistic effect between PANI and
ZnWO4. ZnWO4 nanosheets were homogenously
grown on the surface of the WO3 resulting in a large
active surface area. The charge carriers separation
can be improved because of the energy band structure
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match between WO3 and ZnWO4, This improve
significantly the photoelectrochemical activity, [60].
Barık et al., [61], investigated the degradation of
the toxic GLP herbicide (Kapp = 0.0707 min−1). In this
study, radical trapping experiment, and reactive
oxygen species (ROS) quantification (OH and O2 -
) suggested a possible double electron transfer type
Z-scheme mechanism, which accounts for superior
solar light-assisted N–C bond cleavage of GLP
herbicide. Barık et al., [61], a ternary PANI–ZnWO4
WO3 photocatalyst was synthesized via in situ
polymerization method exhibiting double Z-scheme
channelization towards photodegradation of GLP
with superior minimization of toxicity of degraded
metabolites.
Based on the assumptions and references given
above, in other to improve the removals of GLP and
HZN herbicides from the surface water via
photooxidation, in this study, PANI/ZnWO4/WO3
NCs were prepared under laboratory conditions. The
influence of different PANI/ZnWO4/WO3 NCs
concentrations (0.1, 0.4, 0.6, 1.0 and 1.5 mg/l),
PANI/ZnWO4/WO3 mass ratios (1:1:3, 1:2:3, 3:1:1
and 3:2:1), GLP and HZN concentrations (1, 2, 3 and
4 mg/l), photodegradation times (2, 10, 15 and 20
min), and solar light powers (20, 40, 60, 80 and 100
W/m2) on the photodegradation yields of GLP and
HZN was examined. The characteristics of the
synthesized NCs were assessed using XRD, FTIR,
FESEM, HRTEM and XPS analyses, respectively.
The ecotoxicities of NCs and treated wastewater
were investigated using Microtox (Aliivibrio fischeri)
and Daphnia magna acute toxicity tests.
2 Materials and Methods
2.1 Synthesis of ZnWO4 Nanoparticles (NPs)
ZnWO4 was prepared by 1-butyl-3-
methylimidazolium chloride (BMIMCl) ionic liquid
(IL)-assisted solvothermal method. In a typical
procedure, 0.005 mole of Zn(NO3)2.6H2O and the
same amount of Na2WO4 was added to a 50 ml of
deionized water and BMIMCl IL mixture solution.
The whole reaction mixture was kept under
mechanical stirring for 30 min. The pH of the
solution was balanced at 3.0 before transferring the
whole solution to the Teflon-lined stainless-steel
autoclave. The reaction was kept at 180ºC for 18 h.
After, the reaction was cooled at room temperature
naturally. The white precipitates were washed with
ethanol and deionized water followed by drying at
70ºC for 8 h before further characterization
2.2 Synthesis of WO3 NPs
WO3 was also prepared by BMIMCl IL-assisted
solvothermal method. 0.005 mole of Na2WO4 was
added to 50 ml of deionized water and BMIMCl IL
mixture solution. The resultant reaction mixture was
kept under mechanical stirring for 30 min. The pH of
the solution was adjusted to 3.0 with 0.1 M HCl
solution. The resultant mixture was transferred to the
autoclave and it was kept at 180ºC for 18 h. Then, the
reaction was cooled naturally. The final solid residue
was washed with ethanol and deionized water
followed by drying at 70ºC for 8 h before further
characterization.
2.3 Synthesis of PANI
In chemical oxidation polymerization, PANI is
synthesized by using hydrochloric acid (HCl) or
sulfuric acid (H2SO4) as a dopant and ammonium
persulfate [(NH4)2S2O8] as an oxidant in an aqueous
environment, [62, 63]. At this time, a proton can be
removed by the oxidant from the monomer of aniline
without either creating a heavy bond, or with the
absolute product.
In chemical synthesis, there are three reactants of
PANI that require aniline, oxidant, and acidic
medium. HCl and H2SO4 are common acids used in
the synthesis of PANI, whereas [(NH4)2S2O8,
hydrogen peroxide (H2O2), sodium vanadate
(NaVO3), cerium sulfate [Ce(SO4)2], potassium
dichromate (K2Cr2O7), potassium iodate (KIO3), and
potassium free cyanide {K3[Fe(CN)6]} can be used as
oxidizers. The oxidant polymerization method is the
most communal mechanism used to synthesize
PANI, while aniline reacts with an acidic substance
as a neutralizing agent and polymerizes by adding
one drop of an oxidizing agent such as [(NH4)2S2O8
at dissimilar temperatures. After realization, the
polymerization mechanism (3 h) was an aqueous
solution separated by filtration. Pure PANI can be
obtained by rinsing the above solution 5–6 times with
deionized water. Alcohol and acetone are then added
to make the filter colourless and ensure that non-
reactive materials are completely removed. The
product is slime green and is well-known as PANI
polymer aldine salt, which is unstable due to the
existence of swords. Therefore, the polymer aldine
salt converts to the PANI-EB structure, which is
naturally stable at 25oC, allowing this precipitate to
equilibrate with and ensure that non-reactive
materials, [64].
2.4 Synthesis of PANI/ZnWO4/WO3 NCs
The ternary PANI/ZnWO4/WO3 NCs was
synthesized by an ionic liquid-assisted in situ
oxidative polymerization process. In this process,
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BMIMCI used in the polymerization of aniline using
[(NH4)2S2O8]. At the beginning, 0.8 ml of aniline
was added to the aqueous solution of BMIMCI to
determine three different PANI solutions. Then, in
every PANI mixture, 0.2 mg/l [(NH4)2S2O8] was
added at an [(NH4)2S2O8] to aniline ratio of 1/1.
Furthermore, 0.31 g of ZnWO4 and 0.21 g of WO3
were dispersed in 50 ml of 0.15 M HCl solution
during ultra sonication for 50 min. Then, the particle
mixtures were transferred into the PANI mixtures
and mixed at 21oC. The dark green products were
separated by centrifugation and washed with ethanol
to remove the residual ionic part. The three
composites (PANI/ZnWO4/WO3 NCs) obtained were
dried in a vacuum oven at 60oC.
2.5 Photocatalytic Degradation Reactor
A 2 liters cylinder quartz glass reactor was used for
the photodegradation experiments of GLP and HZN
aqueous solution at different operational conditions.
1000 ml of GLP and HZN aqueous solution was
filled into a cylindrical quartz glass reactor,
separately. Then, the photocatalyst was added into
the cylindrical quartz glass reactors. The
photocatalytic reactor was operated with constant
stirring (1.5 rpm) during the photocatalytic
degradation process. 10 ml of the reacting solution
were sampled and centrifugated (at 10000 rpm) at
different time intervals. Sunlight was used at hours
11.00, 12.30, 14.30 and 15.30 corresponding to
increasing light powers of 20, 40, 60, 80 and 100
W/m2, respectively.
2.6 GLP and HZN Photocatalytic
Degradation Experiments
The photocatalytic degradation efficiencies of PANI,
ZnWO4 NPs, WO3 NPs and PANI/ZnWO4/WO3 NCs
were investigated with a cylinder quartz glass
photocatalytic reactor under solar light irradiation.
The series of GLP and HZN photodegradation
studies were performed in aqueous solutions. The
temperature of the photocatalytic system was
maintained using a continuously circulating aqueous
solution. Typically, 20 mg/l catalysts were used for
the batch degradation study with 100 ml of 10 mg/l
GLP and HZN nder continuous magnetic stirring in
separate reactors. From 10 mg/l GLP and HZN stock
solution, dilutions were performed for GLP and HZN
concentrations of 1 mg/l, 2 mg/l, 3 mg/l and 4 mg/l in
separate reactors. The pollutant solutions were
maintained throughout the degradation process at
pH=7.0 ± 0.1 by dropwise addition of 1.2 M H2SO4
and 1.2 M NaOH solutions as necessary. Initially, the
reaction mixtures were kept in dark to check the
adsorption properties of GLP and HZN to attain
adsorption–desorption equilibrium. Next, the whole
setup was exposed to solar light for the photocatalytic
degradation study. In 20 min time gap, a 4 ml aliquot
of the pollutant solution was withdrawn and
centrifuged to separate the PANI/ZnWO4/WO3 NCs.
The initial experimental conditions are given in Table
1.
* Table 1 can be found in the Appendix section.
The percentage degradation was calculated by the
following Eq. (1):
󰇛󰇜󰇡
󰇢 (1)
where; Co: is the pollutant concentration before
illumination, (mg/l) and Ct is the final concentration,
(mg/l) of the pollutant at time t (min).
2.7 Determination of GLP and HZN
The quantification of GLP and HZN was determined
with a gas chromatography (Agilent 8890N GC)
equipped with a mass selective detector (Agilent
MSD) Gas Chromatography-Mass Spectrometry
(GC-MS) (Agilent 8890GC/Agilent MSD). A
capillary column (HP5-MS, 30 m, 0.25 mm, 0.25 μm)
was used. The injection volume was 1 μl. The initial
oven temperature was kept at 50oC for 1 min, then
raised to 200oC at 25oC/min. Then the temperature
was elevated from 200oC to 300oC at 8oC/min for 6.5
min. High purity He(g) was used as the carrier gas at
constant flow mode (1.8 ml/min, 48 cm/s linear
velocity). The method involves the addition of 6%
borate buffer to the aqueous sample to adjust the
pH=9.3 and then mixing with 9-fluorenylmethyl
chloroformate (FMOC) in acetonitrile (C2H3N) prior
to analysis. The derivatization process was continued
for 13 h at 23°C and the process was stopped by drop-
wise addition of 7 M HCl solution where the resulting
pH was measured to be pH=1.3. Chromatographic
separation was performed with a C18 column where
the mobile phase was 4 mM acetic acid/ammonium
acetate (HAc/NH4Ac) (pH=4.5) acetonitrile. The
percentage of acetonitrile was changed from 75%
(between 0th min and 40nd min) to 100% (between
40.1st min and 46th min) and then to 5% (between
46.1st min and 53th min). For each sample the
separation process was completed in 30 min.
2.8 Photodegradation Mechanism of
PANI/ZnWO4/WO3 NCs
Under the illumination of sunlight, the electrons in
the valence band of PANI, ZnWO4, and WO3 are
excited to their respective conduction bands leaving
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the photo-generated holes (h+) behind (Fig. 1). If the
ternary composite follows photodegradation
mechanism, the holes (h+) in the higher positive EVB
of ZnWO4 and WO3 migrate to the EVB of PANI. On
the other hand, the electrons (e-) migrate in reverse
direction to the CB of ZnWO4 and WO3. The
conduction band edge of ZnWO4 and WO3 located at
- 0.23 and 0.45 eV which is insufficient to reduce O2
into O2 - [E0 (O2/O2) = - 0.33 eV vs. NHE] (Fig. 1).
Again, the photo-generated holes on the valence band
of ZnWO4 and WO3 cannot lead to formation of OH
from the OH- ions/H2O molecules [E0 (OH-/OH) =
1.99 eV vs. NHE, E0 (H2O/OH) = 2.72 eV vs. NHE]
(Fig. 1). This clearly banishes the formation O2 -
from O2 and the formation OH from the OH-
ions/H2O molecules. But the radical trapping test and
ROS quantification have already confirmed O2 - ● and
OH as the major active species behind the
photocatalytic degradation (Fig. 1). For this reason,
the possibility of photodegradation mechanism has
ruled out. These results were also supported by GC-
MS analysis.
* Fig. 1 can be found in the Appendix section.
2.9 Characterization of Photocatalyst
2.9.1 X-Ray Diffraction (XRD) Analysis
Powder XRD patterns were recorded on a Shimadzu
XRD-7000, Japan diffractometer using Cu
radiation (λ=1.5418 Å, 40 kV, 40 mA) at a scanning
speed of 1o min-1 at a 10-80o range. Raman
spectrum was collected with a Horiba Jobin Yvon-
Labram HR UV-Visible NIR (200-1600 nm) Raman
microscope spectrometer, using a laser with a λ=512
nm. The spectrum was collected from 10 scans at a
resolution of 2 cm-1.
2.9.2 Fourier Transform Infrared Spectroscopy
(FTIR) Analysis
The FTIR spectra of samples was recorded using a
FT-NIR spectroscope (RAYLEIGH, WQF-510).
Experimental samples were scanned using infrared
light and their chemical properties were observed in
FTIR spectra.
2.9.3 Field Emission Scanning Electron
Microscopy (FESEM) Analysis
The morphological features and structure of the
synthesized catalyst were investigated by FESEM
(FESEM, Hitachi S-4700), to investigate the
composition of the elements present in the
synthesized catalyst.
2.9.4 High Resolution Transmission Electron
Microscopy (HRTEM) Analysis
The structure of the samples was analyzed by
HRTEM data. HRTEM analysis was recorded in a
Technai G2 20 X-TWIN TEM (FEI, USA) under 200
kV accelerating voltage. Samples were prepared by
applying one drop of the suspended material in
ethanol onto a carbon-coated copper HRTEM grid
and allowing them to dry at 25oC.
2.9.5 X-Ray Photoelectron Spectroscopy (XPS)
Analysis
The valence state of the samples was investigated and
was analyzed using XPS (ESCALAB 250Xi,
England). In XPS analysis it was used an Al Kα
source and surface chemical composition and
reduction state analyses was done by the core levels
recorded using a pass energy of 30 eV
(resolution≈0.10 eV). The peak fitting of the
individual core-levels was done using XPS-peak 41
software, achieving better fitting and component
identification. All binding energies were calibrated to
the C 1s peak originating from C–H or C–C groups
at 284.6 eV.
2.9.6 N2-Adsorption-Desorption Curves
Micromeritics ASAP 2020 M porosimeter was used
to measure the N2-adsorption-desorption curves of
the material. The supercapacitive behavior of the
synthesized samples was investigated using
Princeton Applied Research Center.
2.9.7 Band gap from the UV−vis absorbance
Detailed bandgap calculations were performed along
with the proposal of an accelerated double electron
transfer Z-scheme type channelization mechanism in
the ternary heterojunction system.
The UV-DRS and photoluminescence (PL)
spectra of the synthesized materials were recorded
using Jasco V-650 spectrophotometer and Jasco FP-
8200 Fluorescence spectrometer respectively.
2.9.8 AC Impedance Spectra and Electrochemical
Impedance Spectroscopy (EIS) Analyses
The analysis of impedance data for reduction of
ferricyanide [Fe(CN)6]3− in a potassium chloride
(KCl) supporting electrolyte is used to demonstrate
the error structure for impedance measurements, the
use of measurement and the sensitivity of impedance
to the evolution of nanocomposite properties.
2.9.9 Cyclic Voltammogram Records
Cyclic voltammetry is an electrochemical technique
used to measure the current response of a redox active
solution to a linearly cycled potential sweep using a
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Henken potentiostat. It is a useful method if you need
to quickly find information about the
thermodynamics of redox processes and the energy
levels of the nanocomposite.
2.9.10 Galvanostatic Charge/Discharge Curves
All electrochemical characterization was done using
the Metrohm 128 N AUTOLAB Potentiostat from
the Netherlands in 1 M KOH electrolyte.
2.10 Acute Toxicity Assays
Acute toxicity tests were applied to the raw surface
water containing GLP and HZN, and to
photodegraded surface water at maximum GLP and
HZN removals was taken after treatment.
2.10.1 Microtox Acute Toxicity Test
Ecotoxicity to the bioluminescent organism
Aliivibrio fischeri (also called Vibrio fischeri) was
assayed using the Microtox measuring system
according to DIN 38412L34, L341, (EPS 1/ RM/24
1992). Microtox testing was performed according to
the standard procedure recommended by the
manufacture, [65]. A specific strain of the marine
bacterium, V. fischeri-Microtox LCK 491 Kit, [65],
was used for the Microtox acute toxicity assay. Dr.
LANGE LUMIX-mini type luminometer was used
for the Microtox toxicity assay, [66].
2.10.2 Daphnia magna Acute Toxicity Test
To test ecotoxicity, 24-h born Daphnia magna were
used as described in Standard Methods, [67], sections
8711A, 8711B, 8711C, 8711D and 8711E,
respectively, [68]. After preparing the test solution,
experiments were carried out using 5 or 10 Daphnia
magna introduced into the test vessels. These vessels
had 100 ml of effective volume at 7.0–8.0 pH,
providing a minimum dissolved oxygen (DO)
concentration of 6 mg/l at an ambient temperature of
20–25°C. Young Daphnia magna was used in the test
( ≤ 24 h old); 24–48 h exposure is generally accepted
as standard for a Daphnia magna acute toxicity test.
The results were expressed as mortality percentage of
the Daphnia magna. Immobile animals were reported
as dead Daphnia magna.
All experiments were carried out three times and
the results are given as the means of triplicate
samplings. The data relevant to the individual
pollutant parameters are given as the mean with
standard deviation (SD) values.
2.11 Statistical Analysis
Regression analysis between variables was
performed using the EXCELL in Microsoft
WindowsTM (HP, USA), [69]. The linear correlation
was assessed with r2. The r2 value is the correlation
coefficient and reflects statistical significance
between dependent and independent variables.
Analysis of variance (ANOVA) (SAS ANOVA
procedure) test was used to assess the data obtained
in reactors using the EXCELL in Microsoft
WindowsTM (HP, USA), [69].
3 Results and Discussions
3.1 XRD Analysis Results
The results of XRD analysis for PANI, WO3 NPs,
ZnWO4 NPs, PANI-WO3 NCs, PANI-ZnWO4 NCs
and PANI/ZnWO4/WO3 NCs after photocatalytic
degradation process during GLP removal was
illustrated in Fig. 2. The characterization peaks were
observed at a value of 27.88°, corresponding to the
(002) for PANI (Fig. 2a). The characterization peaks
were obtained at values of 22.17o, 39.97o, 53.25o
and 55.11o, respectively, corresponding to the (001),
(131), (100) and (112), respectively, for WO3 NPs
(Fig. 2b). The characterization peaks were found at
values of 35.10o, 41.34o and 51.04o, respectively,
corresponding to (110), (220) and (132),
respectively, for ZnWO4 NPs (Fig. 2c). The
characterization peaks were observed at 2θ values of
25.61o, 40.36o, 55.47o and 58.79o, respectively,
corresponding to (111), (033), (022) and (202),
respectively, for PANI-WO3 NCs (Fig. 2d). The
characterization peaks were obtained at values of
28.75o, 30.11o, 40.42o and 51.65o, respectively,
corresponding to the (124), (312), (021) and (121),
respectively, for PANI-ZnWO4 NCs (Fig. 2e). The
characterization peaks were measured at 2θ values of
29.11o, 32.40o, 40.02o, 55.09o and 59.78o,
respectively, corresponding to the (010), (225),
(130), (103) and (211), respectively, for
PANI/ZnWO4/WO3 NCs (Fig. 2f).
* Fig. 2 can be found in the Appendix section.
All the reflection peaks from the crystal planes are
exhibited highly crystalline nature. The monoclinic
crystal structure exhibited an agreement with the
reported values in JCPDS file no.: 88-0251, with
space group of ZnWO4, [65]. From Fig. 2 it is seen
that the monoclinic structural peak of ZnWO4
indicates the crystalline nature in the whole
composite. The bi-metal oxide ZnWO4 also exhibited
also a crystalline monoclinic-structure in the PANI
matrix during chemical polymerization reaction.
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3.2 FTIR Analysis Results
The FTIR spectrum of PANI, ZnWO4 NPs and WO3
NPs were determined after photocatalytic
degradation process during GLP removal (Fig. 3).
The main peaks of FTIR spectrum for PANI was
observed at a wavenumber of 850 cm-1 (Fig. 3a). The
main peaks of FTIR spectrum for ZnWO4 NPs was
obtained at 458 cm-1, 570 cm-1 and 785 cm-1
wavenumbers, respectively (Fig. 3b) while the main
peaks of FTIR spectrum for WO3 NPs was
determined at wavenumber of 740 cm-1 (Fig. 3c).
* Fig. 3 can be found in the Appendix section.
Prominent peaks and their assignment are found
at 3434 cm-1 originated from NH bond-stretching
while the maximum abundaces at 520 and 639 cm-1
are defined as Benzenoid and Quinoid ring bond
stretching. The maximal disturbances at 725 cm-1 is
N=H and + C-C bond-stretching. In the region of 631
cm-1, 750 cm-1 and 1700 cm-1 the characteristic
stretching maximums were defined as pure PANI and
PANI/ZnWO4 composites. Comparison of stretching
frequencies of PANI and composites confirms that,
frequencies of bond-stretching of the composites are
sligtly elevated in the nano structure. This indicates a
weak bond interaction between ZnWO4 and PANI
moeities. The peaks at 621 cm−1 and 629 cm−1 are
stretching frequencies of metal and oxygen bond in
pure ZnWO4 composite. This strongly indicates the
formation of PANI/ZnWO4. The intensity of metal
oxygen stretching peaks of FTIR spectra grows with
increase in weight percent of ZnWO4 in PANI.
3.3 FESEM Analysis Results
The morphological features of PANI, ZnWO4 NPs,
WO3 NPs and PANI/ZnWO4/WO3 NCs were
characterized through FESEM images (Fig. 4). The
FESEM images of PANI, ZnWO4 NPs, WO3 NPs and
PANI/ZnWO4/WO3 NCs were illustrated in Fig. 4a,
4b, 4c and 4d, respectively, after photocatalytic
degradation of GLP and HZN.
* Fig. 4 can be found in the Appendix section.
Although, a spherical morphology was detected
the nanocomposite particles exhibited cubic shapes.
The average sizes of the NPs were 25 nm and 27 nm,
respectively. Moreover, all metal oxide particles
were well dispersed in the PANI matrix. In addition,
the general morphology of all hybrid materials was
found to be spherical.
3.4 HRTEM Analysis Results
The HRTEM images of PANI/ZnWO4/WO3 ternary
NCs was performed to detect the
micromorphological structure level after
photocatalytic degradation process of GLP and HZN
(HRTEM image scale: 220 nm) (Fig. 5).
* Fig. 5 can be found in the Appendix section.
High-resolution HRTEM images indicated the
monocrystalline structure of the NCs. The HRTEM
images demonstrate the polycrystalline structure of
the investigated NCs, with average diameter of
21.9±10 nm. The lattice distance of the NCs was
0.9±0.03 nm corresponding to the (002) crystal
planes. HRTEM images exhibited that a compact
interface is formed between WO3 nanorods and
ZnWO4 nanosheets. The lattice fringes was measured
as 0.489 nm and 0.359 nm corresponding to the
crystal planes (101) and (012) of the ZnWO4 phase,
respectively (data not shown). The lattice space of
0.379 nm is corresponded to the (003) planes of
monoclinic WO3. This indicates that WO3 and Zn2+
were transformed into ZnWO4 during in situ reaction.
Such surface/interface are beneficial for the
formation of oxygen vacancy, and also helpful for
improving the electronic transmission. WO3 nanorod
indicates that the WO3 have a single-crystalline
structure with a diameter of 0.386 nm and can be
attributed to the (002) plane defining the monoclinic
WO3. The pattern of the WO3 confirmed the single-
crystalline structure of WO3.The data shows that
(002) and (020) facets with an angle of 90o indicates
the crystal structure of WO3. This component is
growing along the (100) direction (data not shown).
3.5 XPS Analysis Results
The XPS analysis of PANI, ZnWO4 NPs, WO3 NPs
and PANI/ZnWO4/WO3 NCs were perforned during
photo catalytic oxidation of GLP and HZN (Fig. 6).
Absorption peaks were observed at binding energy of
396.14 eV for PANI (red line) (Fig. 6a), at 399.63 eV
for ZnWO4 NPs (green line) (Fig. 6b), at 402.91 eV
for WO3 NPs (blue line) (Fig. 6c) and at 398.36 eV
for PANI/ZnWO4/WO3 NCs (black line) (Fig. 6d),
respectively, after photocatalytic degradation of
GLP.
* Fig. 6 can be found in the Appendix section.
The survey spectra of PANI, ZnWO4 NPs, WO3
NPs and PANI/ZnWO4/WO3 NCs exhibiting four
peaks at 411, 399, 398.9, and 399 eV shows the
existence of W, Zn, O, and C elements. Pristine
ZnWO4 surface absorbed only to carbon species Fig.
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6b exhibits the binding energy peaks of ZnWO4 at
1021.4 and 1044.5 eV, which are indicating the Zn
2p3/2 and the Zn 2p1/2 respectively. This confirm the
presence of Zn2+ ions in the ZnWO4.
3.6 N2 AdsorptionDesorption Isotherms
Fig. 7 presents the N2 adsorption–desorption
isotherms of the ZnWO4, WO3–PANI, PANI–
ZnWO4 samples to analyze their respective surface
area, pore size, and pore volume. The surface areas
of the ZnWO4, WO3, WO3–PANI and
PANI/ZnWO4/WO3 NCs samples were found to be
194, 214, 264, and 248, m2/g, respectively. Notably,
the introduction of ZnWO4 and WO3 NPs into the
PANI matrix enhanced the surface area of the binary
nanocomposites, which was further increased for the
ternary nanocomposite. The nanostructures can act as
spacers increasing the pore size distribution and pore
volume of the ternary nanocomposite as determined
from Barrett–Joyner–Halenda (BJH) analysis.
* Fig. 7 can be found in the Appendix section.
The pore size and pore volume of the
PANI/ZnWO4/WO3 NCs was found to be 5.6 nm and
0.43 cm3/g, respectively, which were much higher
than those of the single nanostructures and binary
nanocomposites. Typicaly, the samples exhibit an
H3-hysteresis loop suggesting a type-IV isotherm
plot. The surface analysis demonstrated about a 28%
surface area increase due to the incorporation of the
ZnWO4 and WO3. Besides, the “cation–π” and
electrostatic interactions established by these
compounds considerably affect the pore structure of
the ternary nanocomposite. This can provide more
adsorption sites and can act as a better charge carrier
for light harvesting.
3.7 Band Gap from the UV−vis Absorbance
The band gap can also be estimated from the onset of
UV−vis absorbance. Fig 8a shows the UV−vis
absorbance divided by film thickness for WO3, 8%
Zn/WO3, and ZnWO4 samples of approximately the
same thickness (0.20, 0.22, and 0.27 μm,
respectively). Using the absorbance data, Tauc plots
were created for each of the three samples (Fig. 8b).
* Fig. 8 can be found in the Appendix section.
A Tauc plot can be used to estimate the band gap
of a semiconductor because, near the absorption
edge, a direct band gap is governed by Eq. 2:
󰇛󰇜
󰇜  (2)
where; h is the Planck constant, ν is the photon’s
frequency, Eg is the band gap energy, and B is a
constant. The γ factor depends on the nature of the
electron transition and is equal to 1/2 or 2 for the
direct and indirect transition band gaps, respectively.
The band gap energy of PANI/ZnWO4/WO3 NC was
calculated as 3.22 eV.
3.8 Cyclic Voltammogram Records
Cyclic voltammogram (CV) records of WO3, PANI
and WO3/PANI was detected in 0.7 M LiClO4-PC
electrolyte at the scanning rate of 100 mV/s. The inset
represents CV of PANI sample. Fig. 9 compares the
cyclic voltammetric changes of the films recorded in
0.7 M LiClO4-PC electrolyte in a potential window
of -0.8 to 0.6 V, -0.5 to +0.6 V and -1.1 to +0.8 V for
WO3, PANI and WO3/PANI films. PANI displayed
oxidation peak at approximately +0.6 V in orwarding
scan, though the oxidation of aniline was not clearly
seen in the forward scan, the reverse scan shows a
small shoulder at +0.3 and -0.1 V, which was due to
the reduction of PANI formed on the electrode. The
WO3 thin film showed a small oxidation and
reduction peak at -0.6 and -0.3V vs SCE.
* Fig. 9 can be found in the Appendix section.
However, WO3/PANI film illustrated a large
difference among the CV of PANI and WO3. The
enhancement of the peak current density of about
0.16 A/cm2 could be observed in WO3/PANI
composite film with respect to pure PANI and WO3
films and is comparable to the earlier reports. This
could be due to the anoporous structure of
WO3/PANI which provided more reactive centers on
the film to contact with the electrolyte and so assist
the charge transfer process with improved charge
density. This also indicated the catalytic behavior of
PANI in WO3. The capacitance from CV curve of all
the film calculated using following relation in Eq. 3:

(3)
where, Imax is the maximum current (in Ampere) and
ds is the potential scan rate in V/s. Mass of WO3,
PANI and WO3/PANI films were measured using a
high precision weight balance and is evaluated as
0.0117, 0.0117 and 0.0138 g respectively.
3.9 AC Impedance Spectra (EIS)
AC impedance spectra (EIS) of PANI, WO3, and
WO3/PANI were measured to substantiate our
approach of injecting PANI over WO3 nanotablets
using a hydrothermal method that contributed
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superior strength in electricity, ion diffusion process,
and structural cyclability]. Fig. 10 displayed the
impedance spectra of a WO3, PANI, and WO3/PANI
measured at +0.38V, +0.07V, and -0.4V respectively.
* Fig. 10 can be found in the Appendix section.
Strikingly, the diffusion layer resistance of
WO3/PANI was lower than their sole performance.
An impedance spectrum in the Nyquist plot possesses
a straight line inclined by 45º at a higher frequency
and a semicircle at a lower frequency. However, the
compressed semicircle indicated irregular electrode
surface that compensates double layer capacitance by
a constant phase element. Particularly, the Nyquist
plot of WO3/PANI exemplified small straight line at
higher frequencies as a result of the diffusion process
and a broad semicircle in the smaller frequency
attributed to fast electron transfer and its prolonged
existence in the film.
3.10 Galvanostatic Charge/Discharge Curves
The galvanostatic charge-discharge is a trustworthy
technique to measure the electrochemical behavior of
the material under controlled conditions using three
electrode systems with 0.5 M LiClO4-PC electrolyte.
Fig. 11(a) exhibited charge/discharge curves of
PANI, WO3, and WO3/PANI for initial cycles at
constant current density of 0.05, 0.5 and 0.05
mA/cm2 respectively, while Fig. 11(b) represents
charge-discharge cycles for initial 10 cycles of
WO3/PANI films.
* Fig. 11 can be found in the Appendix section.
The potential responses of the composite film
during charge-discharge were more symmetrical than
the sole performance of WO3 and the working
potential could be extended to 0.8 V. The discharge
curve represented the characteristic profile of a
pseudocapacitance showing the potential dependent
nature of faradic reaction. When we correlated
charge/discharge with the morphological study, it
indicated that WO3 has a larger particle size that
decreases surface density increasing the interplanar
spacing between atoms. Thus, during the charging
process, it utilizes less coulombic force that
accumulates large charges in a short time.
Subsequently, the capacity of WO3 increases with
less charge-discharge time n PANI, the charge-
discharge time increases because it is highly
conductive consisting of many electrons that
enhances displacement of the electron cloud.
Accordingly, it utilizes more coulombic force with
the increase in charge-discharge time. However,
when PANI coated over WO3, it enhances the surface
area of WO3 with the reduction in the distance.
Ultimately the resistance decreases intrinsically with
the improved charge transport process. Owing to this,
WO3/PANI uses more coulombic force with more
time for charging and discharging process. Therefore,
the charge storing capacity of the system enhances.
The capacitance from charge/discharge curves
evaluated using following relation in Eq. 4:

 (4)
where; I and td are the in applied current density and
time discharge, ΔV is the potential range, m is the
mass of deposited film mentioned above.
3.11 The Effect of Increasing
PANI/ZnWO4/WO3 NCs Concentrations on
GLP and HZN Removals
Maximum 99% GLP removal was observed at 1.0
mg/l PANI/ZnWO4/WO3 NCs, after 180 min
photodegradation, under 300 W solar light at pH=7.0
and at a temperature of 25 oC (Table 2). The cost of a
nanocomposite in practical application depends to a
large extent on its specific dosage to achieve the
wastewater treatment standards. In this work, the
correlation of the NCs dosage and the removal
efficiency of GLP was explored. It can be clearly
observed that the removal efficiency of GLP
increases from about 68% to almost 99% as the
PANI/ZnWO4/WO3 NCs dosage increases from 0.1
to 1.5 mg/l. However, there is no evident growth
anymore when the dosage exceeds 1.5 mg/l. The
reason for this might be that more available binding
sites are provided to capture GLP molecules in
solution with the increased content of the
nanocomposite. To reduce the expense of GLP
disposal, an optimal PANI/ZnWO4/WO3 NCs dosage
of 1 mg/l is suggested for the efficient elimination of
GLP.
* Table 2 can be found in the Appendix section.
The maximum HZN removal was 96% at 1.0 mg/l
PANI/ZnWO4/WO3 NCs, after 180 min
photodegradation, under 300 W solar lights at
pH=7.0 and at a temperature of 25oC (data not
shown). A significant linear correlation between
nanocomposite concentration and herbicide yields
was observed up to a nanocomposite concentration of
15 mg/l (r2 = 0.91, p = 0.07, F = 0.76). ANOVA test
indicated that there were significant differences
between nanocomposite concentration and herbicide
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removals for PANI/ZnWO4/WO3 NCs concentration
> 1.00 (p = 1.87, F =9.14, d.f. = 2).
3.12 The Effect of Different
PANI/ZnWO4/WO3 Mass Ratios on GLP and
HZN Removals
Maximum 99% GLP removal was measured at 1:2:3
mass ratio of PANI to ZnWO and to /WO3 NCs after
180 min photodegradation, under 300 W solar light,
at pH=7.0 and and at 25oC temperature (Table 3). It
could be seen from this table that the increase in
ZnWO4 and WO3 percentages in the whole NCs
resulted in an increase from 68 to 99.7% in the
photooxidation yields of GLPs(V). This may be due
to the greater availability of the exchangeable sites or
surface area at higher concentrations of the ZnWO4
and WO3 percentages.
* Table 3 can be found in the Appendix section.
The Maximum HZN removal yield was 95% at
1:2:3 mass ratio of PANI/ZnWO4/WO3 NCs after 180
min photodegradation, under 300 W solar lights, at
pH=7.0 and and at 25oC temperature (data not
shown). A significant linear correlation between
mass ratio of PANI to ZnWO and to WO3 in the
nanocomposite and herbicide yields was observed up
to a mass ratio of 3:1:1 and 3:2:1 (r2 = 0.91, p = 0.07,
F = 0.76). ANOVA test indicated that there were
significant differences between mass ratio of PANI
to ZnWO4 and to /WO3 and herbicide yields at ratios
> 1:2:3 (p = 1.87, F =9.14, d.f. = 2).
3.13 The Effect of Different GLP and HZN
Concentrations on GLP and HZN Removals
Maximum 99% GLP removal was found at 3 mg/l
GLP, after 180 min photodegradation, under 300 W
solar lights at pH=7.0 and at 25 oC (Table 4). An
increase in the GLP concentration from 1 mg/l up to
4 mg/l increased the photodegradation yields of GLP.
This may be due to the almost all GLP
photocatalyzed by PANI/ZnWO4/WO3 NCs and the
establishment of equilibrium between the NCs and
GLP and none of a GLP photocatalyst was not
remained in the solution. At 3 mg/l GLP more NCs
surface or more adsorption spots were available for
the solute to be photocatalyzed. A further increase in
photocatalyst dosage (4 mg/l) did not cause a
significant improvement in GLP adsorption. This
may be due to the adsorption of almost all GLP to the
photocatalyst and the establishment of equilibrium
between the GLP adsorbed to the NCs and those
remaining unabsorbed and unphotocatalyzed in the
solution. The loading amount of catalyst is a
significant factor in the photocatalytic degradation
process, because the efficiency could be strongly
affected by the number of active sites and photo-
adsorption ability of the catalyst used. However, it
was observed that above a certain optimum catalyst
mass, the reaction rate decreases and becomes
independent of the catalyst concentration.
* Table 4 can be found in the Appendix section.
The maximum HZN removals was 96% at 3 mg/l
GLP, after 180 min photodegradation, under 300 W
solar light at pH=7.0 and at 25oC (data not shown). A
significant linear correlation between GLP and HZN
concentrations and herbicide yields was observed up
to a nanocomposite concentration of 4 mg/l (r2 = 0.91,
p = 0.07, F = 0.76). ANOVA test indicated that there
were significant differences between nanocomposite
concentration and herbicide removals for
PANI/ZnWO4/WO3 NC concentration > 4.00 mg/l (p
= 1.87, F =9.14, d.f. = 2).
3.14 The Effect of Increasing
Photodegradation Time on GLP and HZN
Removals
Maximum 99% GLP removal was obtained after 15
min photodegradation, under 300 W solar lights, at
pH=7.0 and at 25oC (Table 5). As the photooxidation
times were increased from 2 min up to 15 min the
GLP yields increased from 68% up to 99% under sun
light. Further increase of time did not affect the GLP
removals. Data obtained from this study showed that
the GLP yields at longer retention time was low. In
an elevated ratio of contact at long contact times; no
hydroxyl radicals production was achieved for GLR
reduction. As a result, low conversion rates were
observed at shorter residence times. The optimum
illumination time for maximum removal of GLP was
obtained as 15 min.
* Table 5 can be found in the Appendix section.
The maximum HZN removal was obtained as
97% after 15 min photodegradation, under 300 W
solar light, at pH=7.0 and at 25oC (data not shown).
A significant linear correlation between
photodegradation time and herbicide yields was
observed up to a time of 20 min (r2 = 0.91, p = 0.07,
F = 0.76). ANOVA test indicated that there were
significant differences between photodegradation
time and herbicide removals for time > 15 min (p =
1.87, F =9.14, d.f. = 2).
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3.15 The Effect of Increasing Solar Light
Power on GLP and HZN Removals
Maximum 99% GLP removal was measured at 80
W/m2 solar light power after 180 min
photodegradation, under 300 W solar lights at
pH=7.0 and at 25oC (Table 6). Photocatalytic
reaction rate depends largely on the radiation
absorption of the photocatalyst, where the increase in
light intensity enhances the degradation rate and the
yield in photocatalytic degradation. At low light
intensities (20–60 W/m2), the rate would increase
linearly with increasing light intensity, whereas at
intermediate light intensities, above 14 W/m2, the rate
would depend on the square root of the light intensity.
This is likely, because at low light intensity, reactions
involving electron–hole formation are predominant,
and electron–hole recombination is negligible.
However, at increased light intensity, electron–hole
pair separation competes with recombination,
thereby causing lower effect on the reaction rate like
a solar light power of 100 W/m2. The enhancement
of the photodegradation of GLP increased as the light
intensity increased up to 100 W/m2.
* Table 6 can be found in the Appendix section.
Maximum 96% HZN removal was measured at 80
W/m2 solar light power after 180 min
photodegradation, under 300 W solar lights at
pH=7.0 and at 25oC (data not shown). A significant
linear correlation between sunligth power and
herbicide yields was observed up to a sunligth power
of 350 W/m2 (r2 = 0.91, p = 0.07, F = 0.76). ANOVA
test indicated that there were significant differences
between sunligth power and herbicide removals for
sun ligth power > 300 W/m2 (p = 1.87, F =9.14, d.f.
= 2).
3.16 Acute Toxicity Assays
3.16.1 Effect of Increasing GLP and HZN
Concentrations on the Microtox Acute Toxicity at
Increasing Photocatalytic Degradation Time and
Temperature
It was found a high toxicity in raw surface water
based on Microtox bacteria (Aliivibrio fischeri also
called Vibrio fischeri). In Microtox with Aliivibrio
fischeri acute toxicity test, the initial EC90 =825 mg/l
was found at pH=7.0, at 25oC (Table 7: SET 1). The
EC90 values decreased to EC57=414 mg/l to EC22=236
mg/l and to EC12=165 mg/l at GLP=3 mg/l, after 60,
120 and 180 min photocatalytic degradation time, at
30oC (Table 7: SET 3). The Microtox acute toxicity
removal efficiencies were 40.86%, 79.75% and
90.86% after 60, 120 and 180 min photocatalytic
degradation time, respectively, at GLP=3 mg/l, and a
temperature of 30oC (Table 7: SET 3).
* Table 7 can be found in the Appendix section.
The EC90 values decreased to EC51=550 mg/l,
EC17=214 mg/l and EC7=5 mg/l after 60, 120 and 180
min photocatalytic degradation time, respectively, at
GLP=3 mg/l at 60oC (Table 7: SET 3). The toxicity
removal efficiencies were 46.41%, 85.30% and
96.41% after 60, 120 and 180 min photocatalytic
degradation time, respectively, at GLP=3 mg/l, and a
temperature of 60oC (Table 7: SET 3). 96.41%
maximum Microtox acute toxicity removal was
found in GLP=3 mg/l after 180 min photocatalytic
degradation time, at 60oC (Table 7: SET 3).
The EC90 values decreased to EC62=422 mg/l, to
EC21=241 mg/l and to EC17=168 mg/l after 60, 120
and 180 min photocatalytic degradation time,
respectively, at GLP=1 mg/l at 30oC (Table 7: SET
3). The EC90 values decreased to EC62=421 mg/l, to
EC27=239 mg/l and to EC11=167 mg/l after 60, 120
and 180 min photocatalytic degradation time,
respectively, at GLP=2 mg/l at 30oC. The EC90 values
decreased to EC67=408 mg/l, to EC32=230 mg/l and to
EC22=162 mg/l after 60, 120 and 180 min
photocatalytic degradation time, respectively, at
GLP=4 mg/l at 30oC. The Microtox acute toxicity
removals were 85.30%, 85.28% and 79.75% in 1
mg/l, 2 mg/l and 4 mg/l GLP, respectively, after 180
min photocatalytic degradation time, at 30oC. It was
obtained an inhibition effect of GLP=4 mg/l to Vibrio
fischeri after 180 min photocatalytic degradation
time, at 30oC (Table 7: SET 3).
The EC90 values decreased to EC57=419 mg/l, to
EC22=266 mg/l and to EC12=150 mg/l after 60, 120
and 180 min photocatalytic degradation time,
respectively, at GLP=1 mg/l at 60oC (Table 7: SET
3). The EC90 values decreased to EC57=414 mg/l, to
EC22=232 mg/l and to EC12=161 mg/l after 60, 120
and 180 min photocatalytic degradation time,
respectively, in GLP=2 mg/l, at 60oC. The EC90
values decreased to EC62=403 mg/l, to EC27=218
mg/l and to EC17=148 mg/l after 60, 120 and 180 min
photocatalytic degradation time, respectively, in
GLP=4 mg/l at 60oC. The Microtox acute toxicity
removals were 90.86%, 90.83% and 85.30% in 1
mg/l, 2 mg/l and 4 mg/l GLP, respectively, after 180
min photocatalytic degradation time, at 60oC. It was
observed an inhibition effect of GLP=4 mg/l to
Vibrio fischeri after 180 min photocatalytic
degradation time, at 60oC (Table 7: SET 3). The
Microtox acute toxicity removals were 88.80%,
86.83% and 80.38% in 1 mg/l, 2 mg/l and 4 mg/l
International Journal of Chemical Engineering and Materials
DOI: 10.37394/232031.2024.3.9
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HZN, respectively, after 180 min photocatalytic
degradation time, at 60oC (data not shown).
3.16.2 Effect of Increasing GLP and HZN
Concentrations on the Daphnia magna Acute
Toxicity at Increasing Photocatalytic Degradation
Time and Temperature in the Raw Surface Water
A high toxicity was found for raw surface water
before photooxidation in the acute toxicity tests
performed by Daphnia magna. The initial EC50=850
mg/l was observed at 25oC (Table 8: SET 1). After
60, 120 and 180 min photocatalytic degradation time,
the EC50 values decreased to EC31=350 mg/l, to
EC17=240 mg/l and to EC12=90 mg/l in GLP=3 mg/l,
at 30oC (Table 8: SET 3). The Daphnia magna acute
toxicity removals were 42.96%, 72.87% and 82.65%
after 60, 120 and 180 min photocatalytic degradation
time, respectively, in GLP=3 mg/l, at 30oC (Table 8:
SET 3).
* Table 8 can be found in the Appendix section.
The EC50 values decreased to EC27 =150 mg/l, to
EC12=60 mg/l and to EC7=6 mg/l after 60, 120 and
180 min photocatalytic degradation time,
respectively, in GLP=3 mg/l, at 60oC (Table 8: SET
3). The toxicity removal efficiencies were 52.94%,
82.62% and 92.36% after 60, 120 and 180 min
photocatalytic degradation time, respectively, in
GLP=3 mg/l, at 60oC (Table 8: SET 3). 92.38%
maximum Daphnia magna acute toxicity removal
was obtained in GLP=3 mg/l after 180 min
photocatalytic degradation time, at 60oC,
respectively (Table 8: SET 3).
The EC50 values decreased to EC37=450 mg/l, to
EC22=145 mg/l and to EC17=260 mg/l after 60, 120
and 180 min photocatalytic degradation time,
respectively, in GLP=1 mg/l at 30oC (Table 8: SET
3). The EC50 values decreased to EC37=450 mg/l, to
EC22=175 mg/l and to EC17=100 mg/l after 60, 120
and 180 min photocatalytic degradation time,
respectively, in GLP=2 mg/l and at 30oC. The EC50
values decreased to EC42=300 mg/l, to EC27=170
mg/l and to EC22=52 mg/l after 60, 120 and 180 min
photocatalytic degradation time, respectively, in
GLP=4 mg/l, at 30oC. The Daphnia magna acute
toxicity removals were 72.22%, 72.56% and 63.21%
in 1 mg/l, 2 mg/l and 4 mg/l GLP, respectively, after
180 min photocatalytic degradation time, at 30oC. It
was observed an inhibition effect of GLP=4 mg/l to
Daphnia magna after 180 min photocatalytic
degradation time, at 30oC (Table 8: SET 3).
The EC50 values decreased to EC32=130 mg/l, to
EC17=425 mg/l and to EC12=340 mg/l after 60, 120
and 180 min photocatalytic degradation time,
respectively, in GLP=1 mg/l, at 60oC (Table 8: SET
3). The EC50 values decreased to EC32=425 mg/l, to
EC17=140 mg/l and to EC7=90 mg/l after 60, 120 and
180 min photocatalytic degradation time,
respectively, in GLP=2 mg/l, at 60oC. The EC50
values decreased to EC37=250 mg/l, to EC22=110
mg/l and to EC17=10 mg/l after 60, 120 and 180 min
photocatalytic degradation time, respectively, in
GLP=4 mg/l, at 60oC. The Daphnia magna acute
toxicity removals were 83.06%, 92.65% and 73.11%
in 1 mg/l, 2 mg/l and 4 mg/l GLP, respectively, after
180 min photocatalytic degradation time, at 60oC. It
was observed an inhibition effect of GLP=4 mg/l to
Daphnia magna after 180 min photocatalytic
degradation time, at 60oC (Table 8: SET 3).
Increasing the GLP concentrations from 1 mg/l to
3 mg/l did not have a positive effect on the decrease
of EC50 values as shown in Table 8 at SET 3. GLP
concentrations > 3 mg/l decreased the acute toxicity
removals by hindering the photocatalytic degradation
process. Similarly, a significant contribution of
increasing GLP concentration to acute toxicity
removal at 60oC after 180 min photocatalytic
degradation time was not observed. Low toxicity
removals found at high GLP concentrations could be
attributed to their detrimental effect on the Daphnia
magna (Table 8: SET 3). The Daphnia magna acute
toxicity removals were 78.09%, 88.60% and 70.14%
in 1 mg/l, 2 mg/l and 4 mg/l HZN, respectively (data
not shown).
3.17 Aplication of PANI/ZnWO4/WO3 NCs to
the Surface Water which is Going to be Used
as Drinking Water
Water treatment and purification in environmental
protection are the worldwide issues to relieve the
water shortage. At present, various treatment
technologies for drinking water or wastewater have
been developed. Firstly, the purification processes for
drinking water are introduced including the
efficiency and mechanism of filtration and
sedimentation, flocculation and disinfection. In order
to remove the GLP and HZN herbicides with
maximum yields of 99% and 96%, respectively, 3 mg
PANI/ZnWO4/WO3 NCs should be added to 1 liter of
surface water to the sedimentation tank of the
drinking water treatment process. The retention time
should be 180 min, at 300 W solar light at pH=7.0
and at 25 oC.
International Journal of Chemical Engineering and Materials
DOI: 10.37394/232031.2024.3.9
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E-ISSN: 2945-0519
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4 Conclusion
PANI/ZnWO4/WO3 NCs was produced under
laboratory conditions to remove GLP and HZN
herbicides from the surface water via photooxidation.
In order to detect the maximum GLP and HZN
photodegradation yields for optimum operational
conditions (the effects of increasing
PANI/ZnWO4/WO3 NCs concentrations,
PANI/ZnWO4/WO3 mass ratios, GLP and HZN
concentrations, photocatalytic degradation times and
solar light powers on GLP and HZN removals) was
investigated. The maximum removal conditions for
GLP (99.90%) and HZN (96.00%) were 3 mg/l
PANI/ZnWO4/WO3 NCs with a mass ratio of 1:2:3
of PANI to ZnWO4 and to WO3, after 15 min
photocatalytic degradation time at 80 W/m2 power, at
25oC.
The toxicity of raw and photodegraded surface
water was examined using Microtox (with Aliivibrio
fischeri) and Daphnia magna acute toxicity tests. The
acute toxicity decreased significantly in
photodegraded surface water. The acute toxicity
analysis showed that the surface water was toxic and
the toxicity decreased after photocatalytic treatment.
PANI/ZnWO4/WO3 NCs exhibited slightly toxicity
after a concentration of 5 mg/l and 6 mg/l for
Microthox and Daphnia magna acute toxicity,
respectively.
The crystalline structure of monoclinic ZnWO4
and WO3 was detected from XRD analysis while
PANI exhibited a broad characteristic maximum
peak at 28.91° with an amorphous structure. FTIR
spectra showed that pure ZnWO4 has the Zn–O–W
vibrational bands. For WO3 nanostructures, the
vibrational band at 740 cm−1 represent the presence
of W–O–W stretching while PANI was observed at
850 cm−1 describing the C/-C vibrational mode of the
quinoid and benzenoid rings. Therefore, in the XPS
the radical trapping and ROS quantification (OH
and O2˙−●) analysis explained the double electron
transfer type of Z-scheme mechanism ending with
the cleavage of N–C bonds in the GLP and HZN
herbicides. The survey spectra of PANI, ZnWO4
NPs, WO3 NPs and PANI/ZnWO4/WO3 NCs, which
displays four peaks at 410 eV, 397 eV, 398.9 eV, and
399 eV, shows the existence of W, Zn, O, and C
elements. Pristine ZnWO4 shows the adsorption of
carbon species by ZnWO4 surface.
A novel, efficient, and non-toxic
PANI/ZnWO4/WO3 NCs, synthesized following an
IL-assisted in situ oxidative polymerization method.
The prepared nanocomposite was utilized towards
improved photocatalytic wastewater treatment and
acute toxicity removal. Comprehensive analysis of
the structural and morphological properties of the
nanocomposite revealed high structural integrity and
close contact between the individual components.
Very high photocatalytic degradation efficiencies
were obtained with the effect of sunlight irradiation
in the use of PANI/ZnWO4/WO3 NCs to remove the
GLP and HZN herbicides from surface water.
PANI/ZNWO4/WO3 NCs are non-toxic, costly-
effective, easy to apply and can be successfully
applied in the removal of different toxic and
refractory pollutants from surface waters.
Abbreviations
Al: Aluminum
(NH4)2S2O8: Ammonium persulfate
AMPA: Aminomethylphosphonic acid
AOPs: Advanced oxidation processes
ATSDR: Agency for Toxic Substances and Disease
Registry
BiOBr: Bismuth oxobromide
BiVO4: Bismuth vanadate
Bi2WO6: Bismuth tungstate
C: Carbon
Co: the pollutant concentration before illumination
CDC: the Centers for Disease Control and
Prevention
Ce: Cerium
CO2: Carbon dioxide
Ct : the final concentration of the pollutant at time t.
C2H3N: Acetonitrile
Cu: Copper
Cu(OH)2: Copper hydroxide
CV: Cyclic voltammogram
DIN: “Deutsches Institut für Normung”, meaning
"German institute for standardization"
DO: Dissolved oxygen
D201Cu: Nanosized copper hydroxide modified
resin
EC: Effective concentration in toxicity measurement
EC50: 50% Effective concentration in toxicity
measurement
Fe3O4: Iron (II, III) oxide or Magnetite
FESEM: Field emission scanning electron
microscopy
FMOC: 9-fluorenylmethyl chloroformate
FTIR: Fourier transform infrared spectroscopy
GC-MS: Gas Chromatography Mass Spectrometry
GLP: Glyphosate
g-C3N4: Graphitic carbon nitride
He: Helium
H2O: Water
H2O2: Hydrogen peroxide
H2SO4: Sulfuric acid
HAc: Acetic acid
HCl: Hydrogen chloride
International Journal of Chemical Engineering and Materials
DOI: 10.37394/232031.2024.3.9
Ruki
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a Teresa Sponza
E-ISSN: 2945-0519
79
Volume 3, 2024
HRTEM: High resolution transmission electron
microscopy
IARC: International Agency for Research on Cancer
IR: Infrared
La: Lanthanum
MB: Methylene blue
Mn: Manganese
MnFe2O4: Manganese iron oxide
MnO2: Manganese dioxide
MPA: Methylphosphonic acid
MSD: Mass selective detector
NaOH: Sodium hydroxide
NBT: Nitro blue tetrazolium dichloride
NCs: Nanocomposites
NH4Ac: Ammonium ethanoate
NPs: Nanoparticles
O: Oxygen
O2- : Oxygen ion
O2- ●: Superoxide radicals
OH: hydroxyl radicals
PANI: Polyaniline
PO4-P: Orthophosphate
ROS: Reactive oxygen species
SD: Standard deviation
TiO2: Titanium dioxide
US: United States
UV: Ultraviolet
W: Tungsten
WO3: Tungsten trioxide
WO4: Wolframite
WO6: Trioxido-oxo-tungsten
XPS: X-Ray photoelectron spectroscopy
XRD: X-Ray diffraction
Zn: Zinc
Zn2+: Zinc ions
ZnO: Zinc oxide
ZnWO4: Zinc tungsten oxide or Zinc tungstate
Acknowledgement:
Experimental analyzes in this study were performed
at the Laboratories of the Canada Research Center,
Ottawa, Canada. The authors would like to thank this
body for providing financial support.
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Contribution of Individual Authors to the
Creation of a Scientific Article (Ghostwriting
Policy)
Prof. Dr. Delia Teresa Sponza and Post-Dr. Rukiye
Öztekin took an active role in every stage of the
preparation of this article.
The authors equally contributed in the present
research, at all stages from the formulation of the
problem to the final findings and solution.
Sources of Funding for Research Presented in a
Scientific Article or Scientific Article Itself
This research study was undertaken in the
Environmental Microbiology Laboratories at Dokuz
Eylül University Engineering Faculty Environmental
Engineering Department, İzmir, Turkey. The authors
would like to thank this body for providing financial
support.
Conflict of Interest
The authors have no conflicts of interest to declare
that are relevant to the content of this article.
Creative Commons Attribution License 4.0
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APPENDIX
Table 1. The initial experimental conditions for this study.
PANI/ZnWO4/WO3 NCs
Concentrations (mg/l)
PANI/ZnWO4/WO3
Mass Ratios
GLP
Concentrations
(mg/l)
Solar Light
Powers
(W/m2)
0.1
1:1:3
1
20
0.4
1:2:3
2
40
0.6
3:1:1
3
60
1.0
3:2:1
4
80
1.5
100
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Fig. 1. Photodegradation Mechanism of PANI/ZnWO4/WO3 NCs
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Fig. 2. The XRD patterns of (a) PANI, (b) WO3 NPs, (c) ZnWO4 NPs, (d) PANI-WO3 NCs, (e) PANI-ZnWO4
NCs and (f) PANI/ZnWO4/WO3 NCs, respectively, in surface water after photocatalytic degradation process for
GLP removal.
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Fig. 3. FTIR spectrum of (a) PANI, (b) ZnWO4 NPs and (c) WO3 NPs, respectively, in surface water after
photocatalytic degradation process for GLP removal.
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(a)
(b)
(c)
(d)
Fig. 4. FESEM images of (a) PANI, (b) ZnWO4 NPs, (c) WO3 NPs and (d) PANI//ZnWO4/WO3 NCs,
respectively, in surface water after photocatalytic degradation process for GLP removal (FESEM images scale:
200 nm).
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Fig. 5. HRTEM images of PANI/ZnWO4/WO3 NCs in micromorphological structure level in surface water after
photocatalytic degradation process for GLP removal (HRTEM image scale: 200 nm).
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Fig. 6. The XPS spectra of (a) PANI (red) (b) ZnWO4 NPs (green), (c) WO3 (blue) and (d) PANI/ZnWO4/WO3
NCs (black), respectively, in surface water after photocatalytic degradation process for GLP removal.
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Fig 7. N2 adsorption desorption isoterm of PANI, ZnWO4, WO3 and PANI/ZnWO4/WO3 NCs
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Fig 8a. UV−vis absorbance for WO3, 8% Zn/WO3, and ZnWO4
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Fig 8b. Tauc plots for WO3, ZnWO4 and 8% WO3
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Fig 9. Cyclic voltammogram data of WO3, PANI, ZnWO4 and PANI/ZnWO4/WO3 NCs in 0.7 M LiClO4-PC
electrolyte.
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Fig. 10. Nyquist plots of WO3, PANI, and PANI/ZnWO4/ WO3 NCs in 0.7 M LiClO4-PC electrolyte
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Fig. 11a. Galvanostatic charge/discharge curve of PANI/WO3 and PANI/ZnWO4/WO3 NCs
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Fig. 11b. Galvanostatic charge/discharge curve of PANI/WO3 NCs
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Table 2. The effect of increasing PANI/ZnWO4/WO3 NCs concentrations for GLP removal
PANI/ZnWO4/WO3 NCs Concentrations (mg/l)
GLP Removal Efficiency (%)
0.1
68
0.4
74
0.6
80
1.0
99
1.5
91
Table 3. The effect of different PANI/ZnWO4/WO3 mass ratios for GLP removal
PANI/ZnWO4/WO3 Mass Ratios
GLP Removal Efficiency (%)
1:1:3
67
1:2:3
99
3:1:1
86
3:2:1
79
Table 4. The effect of different GLP concentrations for GLP removal
GLP Concentrations (mg/l)
GLP Removal Efficiency (%)
1
65
2
82
3
99
4
84
Table 5. The effect of increasing photodegradation time for GLP removal
Photodegradation Time (min)
GLP Removal Efficiency (%)
2
68
10
81
15
99
20
73
Table 6. The effect of increasing solar light power for GLP removal
Solar Light Power (W/m2)
GLP Removal Efficiency (%)
20
58
40
71
60
86
80
99
100
92
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Table 7. Effect of increasing GLP concentrations on Microtox acute toxicity in surface water after
photocatalytic degradation process, at 30oC and at 60oC.
No
Parameters
Microtox Acute Toxicity Values, * EC (mg/l)
25oC
0. min
60. min
120. min
180. min
*EC90
*EC
*EC
*EC
1
Control
825
EC70=510
EC60=650
EC49=638
30oC
60oC
0.
min
60.
min
120.
min
180.
min
0.
min
60.
min
120.
min
180.
min
*EC90
*EC
*EC
*EC
*EC90
*EC
*EC
*EC
2
Control
825
EC70=
580
EC50=
580
EC39=
548
825
EC55=
550
EC40=
590
EC29=
688
3
GLP=1 mg/l
825
EC62=
422
EC27=
242
EC17=
168
825
EC57=
419
EC22=
266
EC12=
150
GLP=2 mg/l
825
EC62=
421
EC27=
239
EC17=
167
825
EC57=
414
EC22=
232
EC12=
161
GLP=3 mg/l
825
EC57
=414
EC22=
236
EC12=
16.5
825
EC52=
550
EC17=
214
EC7=
5
GLP=4 mg/l
825
EC67=
408
EC32=
230
EC22=
162
825
EC62=
403
EC27=
218
EC17=
148
* EC values were calculated based on CODdis (mg/l). Control: raw ww.
Table 8. Effect of increasing GLP concentrations on Daphnia magna acute toxicity in surface water after
photocatalytic degradation process, at 30oC and at 60oC.
No
Parameters
Daphnia magna Acute Toxicity Values, * EC (mg/l)
25oC
0. min
60. min
120. min
180. min
*EC50
*EC
*EC
*EC
1
Control
850
EC45=625
EC40=370
EC29=153
30oC
60oC
0.
min
60.
min
120.
min
180.
min
0.
min
60. min
120.
min
180.
min
*EC50
*EC
*EC
*EC
*EC50
*EC
*EC
*EC
2
Control
850
EC39=
468
EC34=
228
EC23=
111
850
EC34=
373
EC29=
210
EC18=
71
3
GLP=1 mg/l
850
EC32=
450
EC22=
145
EC17=
260
850
EC32=
130
EC17=
425
EC12=
340
GLP=2 mg/l
850
EC37=
450
EC22=
175
EC17=
100
850
EC32=
425
EC17=
140
EC7=
90
GLP=3 mg/l
850
EC32=
350
EC17=
240
EC12=
90
850
EC27=
150
EC12=
60
EC7=
6
GLP=4 mg/l
850
EC42=
300
EC27=
170
EC22=
52
850
EC37=
250
EC22=
110
EC17=
11
* EC values were calculated based on CODdis (mg/l). Control: Raw ww
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