9 research outputs found
Adsorption of Estrogen Contaminants by Graphene Nanomaterials under Natural Organic Matter Preloading: Comparison to Carbon Nanotube, Biochar, and Activated Carbon
Adsorption of two estrogen contaminants
(17β-estradiol and
17α-ethynyl estradiol) by graphene nanomaterials was investigated
and compared to those of a multi-walled carbon nanotube (MWCNT), a
single-walled carbon nanotube (SWCNT), two biochars, a powdered activated
carbon (PAC), and a granular activate carbon (GAC) in ultrapure water
and in the competition of natural organic matter (NOM). Graphene nanomaterials
showed comparable or better adsorption ability than carbon nanotubes
(CNTs), biochars (BCs), and activated carbon (ACs) under NOM preloading.
The competition of NOM decreased the estrogen adsorption by all adsorbents.
However, the impact of NOM on the estrogen adsorption was smaller
on graphenes than CNTs, BCs, and ACs. Moreover, the hydrophobicity
of estrogens also affected the uptake of estrogens. These results
suggested that graphene nanomaterials could be used to removal estrogen
contaminants from water as an alternative adsorbent. Nevertheless,
if transferred to the environment, they would also adsorb estrogen
contaminants, leading to great environmental hazards
Stabilized Nanoscale Zerovalent Iron Mediated Cadmium Accumulation and Oxidative Damage of <i>Boehmeria nivea</i> (L.) Gaudich Cultivated in Cadmium Contaminated Sediments
Nanoparticles
can be absorbed by plants, but their impacts on phytoremediation
are not yet well understood. This study was carried out to determine
the impacts of starch stabilized nanoscale zerovalent iron (S-nZVI)
on the cadmium (Cd) accumulation and the oxidative stress in <i>Boehmeria nivea</i> (L.) Gaudich (ramie). Plants were cultivated
in Cd-contaminated sediments amended with S-nZVI at 100, 500, and
1000 mg/kg, respectively. Results showed that S-nZVI promoted Cd accumulation
in ramie seedlings. The subcellular distribution result showed that
Cd content in cell wall of plants reduced, and its concentration in
cell organelle and soluble fractions increased at S-nZVI treatments,
indicating the promotion of Cd entering plant cells by S-nZVI. In
addition, the 100 mg/kg S-nZVI alleviated the oxidative damage to
ramie under Cd-stress, while 500 and 1000 mg/kg S-nZVI inhibited plant
growth and aggravated the oxidative damage to plants. These findings
demonstrate that nanoparticles at low concentration can improve the
efficiency of phytoremediation. This study herein develops a promising
novel technique by the combined use of nanotechnology and phytoremediation
in the remediation of heavy metal contaminated sites
Adsorption of Cu(II), Pb(II), and Cd(II) Ions from Acidic Aqueous Solutions by Diethylenetriaminepentaacetic Acid-Modified Magnetic Graphene Oxide
In
this study, diethylenetriaminepentaacetic acid (DTPA)-modified
magnetic graphene oxide (MGO) was synthesized for removal of CuÂ(II),
PbÂ(II), and CdÂ(II) ions from acidic aqueous solutions. The prepared
DTPA/MGO composites were characterized by scanning electron microscopy,
X-ray diffraction, Fourier transform infrared and X-ray photoelectron
spectroscopies, and zeta potential. The results showed that DTPA successfully
functionalized MGO. Adsorption experiments indicated that DTPA/MGO
composites exhibited excellent adsorption property in acidic aqueous
solutions. The adsorption processes were applicable for the Langmuir
adsorption isotherm and the pseudo-second-order model. The maximum
adsorption capacities at pH 3.0 for CuÂ(II), PbÂ(II), and CdÂ(II) ions
were 131.4, 387.6, and 286.5 mg/g, respectively. The thermodynamic
studies demonstrated that adsorption processes were endothermic and
spontaneous. Moreover, the DTPA/MGO composites could selectively adsorb
PbÂ(II) from multimetal mixed systems. Adsorption–desorption
results showed that the DTPA/MGO composites exhibited excellent reusability.
These results suggested that DTPA/MGO composites have great potential
in removing heavy metals from acidic wastewater, especially for PbÂ(II)
Ethylenediamine grafted to graphene oxide@Fe<sub>3</sub>O<sub>4</sub> for chromium(VI) decontamination: Performance, modelling, and fractional factorial design - Fig 4
<p>(a) Time profiles of Cr(VI) adsorption with GO@Fe<sub>3</sub>O<sub>4</sub> and EDA-GO@Fe<sub>3</sub>O<sub>4</sub>; Kinetics of Cr(VI) adsorption by fitting (b) pseudo-first-order and pseudo-second-order models, and (c) intraparticle diffusion model, respectively (initial Cr(VI) concentration = 10 mg/L; sorbent dose = 2 mL; temperature = 25°C; pH = 2).</p
HRTEM images of EDA-GO@Fe<sub>3</sub>O<sub>4</sub> at different magnification.
<p>HRTEM images of EDA-GO@Fe<sub>3</sub>O<sub>4</sub> at different magnification.</p
Effect of solution pH on Cr(VI) adsorption onto the EDA-GO@Fe<sub>3</sub>O<sub>4</sub>: (initial Cr(VI) concentration = 10 mg/L; sorbent dose = 2 mL; temperature = 25°C; time = 8 h).
<p>Effect of solution pH on Cr(VI) adsorption onto the EDA-GO@Fe<sub>3</sub>O<sub>4</sub>: (initial Cr(VI) concentration = 10 mg/L; sorbent dose = 2 mL; temperature = 25°C; time = 8 h).</p
Isotherm parameters for Cr(VI) ions adsorption onto EDA-GO@Fe<sub>3</sub>O<sub>4</sub>.
<p>Isotherm parameters for Cr(VI) ions adsorption onto EDA-GO@Fe<sub>3</sub>O<sub>4</sub>.</p
Adsorption kinetics parameters for Cr(VI) adsorption onto GO@Fe<sub>3</sub>O<sub>4</sub> and EDA-GO@Fe<sub>3</sub>O<sub>4</sub>.
<p>Adsorption kinetics parameters for Cr(VI) adsorption onto GO@Fe<sub>3</sub>O<sub>4</sub> and EDA-GO@Fe<sub>3</sub>O<sub>4</sub>.</p