9 research outputs found
Degradation of Cationic Red GTL by Catalytic Wet Air Oxidation over Mo–Zn–Al–O Catalyst under Room Temperature and Atmospheric pressure
To overcome the drawback of catalytic wet air oxidation
(CWAO)
with high temperature and high pressure, the catalytic activity of
Mo–Zn–Al–O catalyst for degradation of cationic
red GTL under room temperature and atmospheric pressure was investigated.
Mo–Zn–Al–O catalyst was prepared by coprecipitation
and impregnation. XRD, TG-DTG, and XPS were used to characterize the
resulting sample. Central composition design using response surface
methodology was employed to optimize correlation of factors on the
decolorization of cationic red GTL. The results show that the optimal
conditions of pH value, initial concentration of dye and catalyst
dosage were found to be 4.0, 85 mg/L and 2.72 g/L, respectively, for
maximum decolorization of 80.1% and TOC removal of 50.9%. Furthermore,
the reaction on the Mo–Zn–Al–O catalyst and degradation
mechanism of cationic red GTL was studied by Electron spin resonance
(ESR) and GC-MS technique. The possible reaction mechanism was that
the Mo–Zn–Al–O catalyst can efficiently react
with adsorbed oxygen/H<sub>2</sub>O to produce ·OH and <sup>1</sup>O<sub>2</sub> and finally induce the degradation of cationic red
GTL. GC-MS analysis of the degradation products indicates that cationic
red GTL was initiated by the cleavage of î—¸Nî—»Nî—¸
and the intermediates were further oxidized by ·OH or <sup>1</sup>O<sub>2</sub>
Volumetric, Viscometric, and Refractive Index Behavior of 7‑Hydroxy-4-methylcoumarin in Aqueous Ethanol or 1‑Propanol Solutions in the Temperature Range of (293.15 to 313.15) K
Densities
and viscosities of the pseudo binary system 7-hydroxy-4-methylcoumarin
+ (ethanol or 1-propanol) + water at temperatures of (293.15, 298.15,
303.15, 308.15, and 313.15) K and refractive indices of this system
at <i>T</i> = 298.15 K have been measured as a function
of the molality of 7-hydroxy-4-methylcoumarin. The density data have
been used to compute the apparent molar volume and limiting partial
molar volume. The viscosity <i>B</i>-coefficients and variation
of <i>B</i> with temperature have been calculated from the
viscosity data according to the Jones–Dole equation. Molar
refractions of the investigated system have been obtained from the
refractive index data. These parameters and their variation tendencies
have been expounded in terms of the interactions between solutes and
solvents. The results have shown that 7-hydroxy-4-methylcoumarin plays
a structure-making role in the given solution
Extracellular Polymeric Substances Induced Porous Polyaniline for Enhanced Cr(VI) Removal from Wastewater
Extracellular
polymeric substances (EPS) of bacteria were used
as templates for synthesizing unique polyaniline nanocomposites, i.e.,
porous EPS-modified polyaniline (EPS@PANI). The proteins were responsible
for forming porous structure, while polysaccharides for the fiber
morphology of EPS@PANI. The specific surface area (53.2 m<sup>2</sup>/g) of these unique EPS@PANI with an optimal EPS loading of 2 wt
% was ∼2 times larger than that of pristine PANI. The PANI
in EPS@PANI stayed as the emeraldine form and acted as the electron
donor for reduction of CrÂ(VI) to CrÂ(III). Herein, 1.0 mg/L CrÂ(VI)
was completely reduced to CrÂ(III) by 600 mg/L of EPS@PANI within 10
min, which was much faster than the pristine PANI (1 h). A maximum
CrÂ(VI) removal capacity of 913.2 mg/g was achieved by these unique
EPS@PANI nanocomposites and was ∼4.7 times higher than the
pristine PANI (193.8 mg/g). Moreover, the isoelectric point (pI) was
decreased from pH 7.5 for pure PANI to ∼4.5 for these porous
EPS@PANI nanocomposites due to the low pI of polysaccharides remained
in the composites. This lowered pI facilitated further CrÂ(III) removal
on the surface of EPS@PANI from the wastewater
Additional file 1: Figures S1–S6. of Facile Fabrication of Bi2WO6/Ag2S Heterostructure with Enhanced Visible-Light-Driven Photocatalytic Performances
The EDS, BET surface area, and Zeta potential analysis for the as-formed heterostructures, the XRD pattern of Ag2S, and the temporal evolution of Rh B absorption spectra over Bi2WO6/Ag2S heterostructure at different pH values. Figure S1. Elemental mapping and EDX spectra of the Bi2WO6/Ag2S heterostructure. Figure S2. EDS spectra of the composite photocatalysts Bi2WO6/Ag2S. Figure S3. Nitrogen adsorption-desorption isotherms and the pore size distribution curve (inset) of sample (a) Bi2WO6 and (b) Bi2WO6/Ag2S. Figure S4. XRD pattern of Ag2S. Figure S5. Zeta potential for a suspension containing 1 g L of sample Bi2WO6/Ag2S in the presence of KCl (10−3 M) at different pH values. Figure S6. The temporal evolution of Rh B absorption spectra over Bi2WO6/Ag2S heterostructure at different pH values
Ultrasonic Pretreated Sludge Derived Stable Magnetic Active Carbon for Cr(VI) Removal from Wastewater
A stable
magnetic carbon was synthesized using activated sludge
as the carbon precursor. The ultrasonic pretreatment was used to destroy
the cells in the activated sludge and to release the soluble carbon
source, which was responsible for the improved stability of the synthesized
magnetic carbon. 800 W was demonstrated as the optimized ultrasonication
power for the pretreatment of activated sludge. Then, the carbonization
parameters, such as pyrolysis temperature, heating rate, and dwell
time were optimized as 800 °C, 10 °C/min, and 60 min, respectively.
To be more specific, this activated sludge derived magnetic carbon
can reduce almost all the hexavalent chromium (CrÂ(VI)) (2.0 mg/L)
in 10 min and has a maximum capacity as high as 203 mg/g. The iron
release rate of the synthesized activated sludge derived magnetic
carbon was decreased, which improved the electron utilization of zerovalent
iron (ZVI). This composite was demonstrated to have a good stability
and recyclability as well. Finally, the CrÂ(VI) removal mechanisms
were clarified under the acidic and the natural conditions
Rheological Behavior of Aqueous Solutions of An Ionic Liquid As A Surfactant
<div><p>The rheological properties of aqueous solutions of an ionic liquid as a surfactant, 1-tetradecyl-3-methylimidazolium bromide (C<sub>14</sub>mimBr), in the presence of sodium salicylate (NaSal), have been studied by rheological measurements. For these C<sub>14</sub>mimBr/NaSal systems, zero-shear viscosity as a function of NaSal concentration shows the maxima behavior. The effect of the concentration ratio, C<sub>NaSal</sub>/C<sub>C14mimBr</sub>, on the maximum was determined, and the scaling relations were obtained. Network structures could be formed in the aqueous C<sub>14</sub>mimBr solutions containing NaSal. <sup>1</sup>H NMR spectra analysis indicates that the main interaction between C<sub>14</sub>mimBr and NaSal molecules is electrostatic attraction, which leads to the formation of an ion pair.</p></div
DataSheet1_Granular activated carbon enhances volatile fatty acid production in the anaerobic fermentation of garden wastes.docx
Garden waste, one type of lignocellulosic biomass, holds significant potential for the production of volatile fatty acids (VFAs) through anaerobic fermentation. However, the hydrolysis efficiency of garden waste is limited by the inherent recalcitrance, which further influences VFA production. Granular activated carbon (GAC) could promote hydrolysis and acidogenesis efficiency during anaerobic fermentation. This study developed a strategy to use GAC to enhance the anaerobic fermentation of garden waste without any complex pretreatments and extra enzymes. The results showed that GAC addition could improve VFA production, especially acetate, and reach the maximum total VFA yield of 191.55Â mg/g VSadded, which increased by 27.35% compared to the control group. The highest VFA/sCOD value of 70.01% was attained in the GAC-amended group, whereas the control group only reached 49.35%, indicating a better hydrolysis and acidogenesis capacity attributed to the addition of GAC. Microbial community results revealed that GAC addition promoted the enrichment of Caproiciproducens and Clostridium, which are crucial for anaerobic VFA production. In addition, only the GAC-amended group showed the presence of Sphaerochaeta and Oscillibacter genera, which are associated with electron transfer processes. Metagenomics analysis indicated that GAC addition improved the abundance of glycoside hydrolases (GHs) and key functional enzymes related to hydrolysis and acidogenesis. Furthermore, the assessment of major genera influencing functional genes in both groups indicated that Sphaerochaeta, Clostridium, and Caproicibacter were the primary contributors to upregulated genes. These findings underscored the significance of employing GAC to enhance the anaerobic fermentation of garden waste, offering a promising approach for sustainable biomass conversion and VFA production.</p
Solvent and pH Dependences of Mixing Enthalpies of <i>N</i>‑Glycylglycine with Protocatechuic Acid
Protocatechuic
acid (PA) is a natural phenolic compound which has
been proven to have chemopreventive property against chemically induced
carcinogenesis. The mixing enthalpies of PA with <i>N</i>-glycylglycine in sodium phosphate and potassium phosphate buffer
solutions with different pH values have been investigated by mixing-flow
isothermal microcalorimetry at <i>T</i> = 298.15 K. The
heterotactic enthalpic interaction coefficients (<i>h</i><sub><i>xy</i></sub>) in the pH range of phosphate buffer
solution from 3.0 to 8.0 have been calculated according to the McMillan–Mayer
theory. Trends of the enthalpic pairwise interaction coefficients
(<i>h</i><sub><i>xy</i></sub>) with increasing
pH in both phosphate buffer solutions were obtained. The solvent and
pH dependence of the <i>h</i><sub><i>xy</i></sub> were discussed in terms of molecular interactions between solvated
solute molecules
Polyaniline Coated Ethyl Cellulose with Improved Hexavalent Chromium Removal
The ethyl celluloses (ECs) modified
with 5.0, 10.0, and 20.0 wt
% polyaniline (PANI) (PANI/ECs) prepared by homogeneously mixing the
EC and PANI formic acid solutions have demonstrated a superior hexavalent
chromium (CrÂ(VI)) removal performance to that of pure EC. Having an
increased CrÂ(VI) removal percentage with increased PANI loading, the
PANI/ECs with 20.0% PANI loading were noticed to remove 2.0 mg/L CrÂ(VI)
completely within 5 min, much faster than the pristine EC (>1 h).
A chemical redox of CrÂ(VI) to CrÂ(III) by the active functional groups
of PANI/ECs was revealed from the kinetic study. Meanwhile, isothermal
study demonstrated a monolayer adsorption behavior following the Langmuir
model with a calculated maximum absorption capacity of 19.49, 26.11,
and 38.76 mg/g for the 5.0, 10.0, and 20.0 wt % PANI/ECs, much higher
than that of EC (12.2 mg/g). The CrÂ(VI) removal mechanisms were interpreted
considering the functional groups of both PANI and EC, the valence
state fates of CrÂ(VI), and the variation of solution acidity