53 research outputs found
Inter-zonal Tradable Discharge Permit System to Control Water Pollution in Tianjin, China
In recent years, Chinese environmental authorities have
expressed interest in the use of Tradable Discharge Permits
(TDP) as a regulatory instrument to control pollutant
emissions. Environmental professionals still have not had
enough experience, however, in designing and managing
TDP systems, especially for non-uniformly dispersed
pollutants. As an empirical study, this paper proposes an inter-zonal TDP system and analyzes its effectiveness in cost
savings and environmental protection for reducing water
pollutant COD (chemical oxygen demand) in Tianjin, China.
Zonal permit system (ZPS) and emission permit system
(EPS) are discussed for comparison. The inter-zonal TDP
system is demonstrated to improve cost efficiency by allowing
permit trades between zones, as long as water quality
constraints are satisfied. The transactions are assumed to
proceed in a multilateral sequential way and are simulated
with a circularly running linear programming (LP) model. The
simulation of permit transactions among 20 firms shows
that to reach the same COD removal target, ZPS, inter-zonal TDP system, and EPS lowered the total reduction cost
by 12.8%, 14.6%, and 15.8%, respectively. EPS, however,
brought about “hot spots” problem. Finally, the transaction
costs and the sensitivity of the three TDP systems to
changes in both COD reduction rate and the initial permit
allocation are discussed, and policy implications are
addressed
GO–Polymer Modified Anion Exchange Membranes for Antifouling
Organic fouling was one of key issues limiting the application
of electrodialysis in the treatment of industrial wastewater, which
results in degradation of membranes and high energy consumption. In
this study, a novel graphene oxide (GO)–polymer modified anion
exchange membrane (AEM) for antiorganic fouling was first developed
by layer-by-layer interfacial polymerization (IP). The surface of
AEM was alternately contacted with GO and tannic acid (TA) aqueous
as the water phase and an n-hexane solution of trimesoyl
chloride (TMC) as the organic phase; thus, a multilayer GO–polymer
structure was fabricated on the surface of AEM. Results showed that
the aqueous phase was preferred to be the final treatment of layer-by-layer
interfacial polymerization, which was more conducive to enhancing
hydrophilicity and negative charge density of the membrane surface.
Compared with TA-TMC modified AEM, the introduction of GO nanosheets
with carboxyl groups into aqueous solution significantly increased
the negative charge density of the membrane surface and reduced membrane
resistance. The desalination rate of (GOTA-TMC)1.5 was
mostly close to that of pristine AEM without fouling, exhibiting significant
antifouling performance and good stability. The study provides promising
insights into the modification of ion exchange membranes with functional
materials and a polymer composite layer
Selective Production of Jet-Fuel-Range Alkanes from Palmitic Acid over Ni/H-MCM-49 with Two Independent Pore Systems
With
two independent pore systems (intralayer sinusoidal channels
and interlayer supercages) and external 12 membered-ring (MR) cups, H-MCM-49 was selected as the acidic support for upgrading
palmitic acid to jet-fuel-range hydrocarbons via simultaneous hydro-deoxygenation,
hydrocracking, and hydroisomerization. Compared to other zeolites,
H-MCM-49 showed better selectivity toward cracking and isomerizing
products (C12–C14 alkanes). Postsynthesis
of H-MCM-49 could tailor acidity and catalytic performance to produce
more C12–C14 cracking and isoalkane products.
Ni/H-MCM-49 bifunctional catalysts restrained the acid-catalyzed reactions
to some extent because of enhancement in hydro-deoxygenation over
Ni particles, leading to the decrease in appropriate cracking of C12–C14 alkanes’ and isoalkanes’
selectivity. Ni/H-MCM-49 bifunctional catalysts exhibited excellent
catalytic stability on activity and selectivity of target products,
which opened a novel tailoring pathway over zeolites with independent
pore systems
Degradation of Sulfamethoxazole by Manganese(IV) Oxide in the Presence of Humic Acid: Role of Stabilized Semiquinone Radicals
In this work, we demonstrate for the first time the abatement
of
sulfamethoxazole (SMX) induced by stabilized ortho-semiquinone radicals (o-SQ•–) in the MnO2-mediated system in the presence of humic
acid. To evaluate the performance of different MnO2/mediator
systems, 16 mediators are examined for their effects on MnO2 reactions with SMX. The key role of the bidentate Mn(II)-o-SQ• complex and MnO2 surface
in stabilizing SQ•– is revealed. To illustrate
the formation of the Mn(II)-o-SQ• complex, electron spin resonance, cyclic voltammetry, and mass spectra
were used. To demonstrate the presence of o-SQ• on the MnO2 surface, EDTA was used to quench
Mn(II)-o-SQ•. The high stability
of o-SQ•– on the MnO2 surface is attributed to the higher potential of o-SQ•– (0.9643 V) than the MnO2 surface (0.8598 V) at pH 7.0. The SMX removal rate constant
by different stabilized o-SQ• at
pH 7.0 ranges from 0.0098 to 0.2252 min–1. The favorable
model is the rate constant ln (kobs, 7.0) = 6.002EHOMO(o-Qred) + 33.744(ELUMO(o-Q) – EHOMO(o-Qred)) – 32.800, whose parameters represent the
generation and reactivity of o-SQ•, respectively. Moreover, aniline and cystine are competitive substrates
for SMX in coupling o-SQ•–. Due to the abundance of humic constituents in aquatic environments,
this finding sheds light on the low-oxidant-demand, low-carbon, and
highly selective removal of sulfonamide antibiotics
Highly Selective PdCu/Amorphous Silica−Alumina (ASA) Catalysts for Groundwater Denitration
Catalytic nitrate reduction is a promising technology in groundwater purification. In this study, PdCu bimetallic catalysts supported on an industrial amorphous silica−alumina (ASA) were synthesized and used to simulate catalytic removal of nitrate in groundwater. The catalysts exhibited very high activity and the highest catalytic selectivity toward N2O and N2 was 90.2%. The optimal Pd/Cu weight ratio was four. Relatively low reduction temperature was found benefit the catalytic stability and 300 °C was the appropriate reduction temperature during catalyst preparation. With an average particle size 5.4 nm, the metal particles were very uniformly distributed on the catalyst surface prepared with the codeposition method. This kept the catalyst more stable than the PdCu/Al2O3 catalyst with larger metal particles. According to XRD, TEM, and XPS results, the metals maintained zero-valence but aggregated by about 2 nm during the denitration reaction, which caused gradual deactivation of the catalysts. Little leaching of Cu and Pd from the catalyst might also have a slightly negative impact to the stability of the catalysts. A simple treatment was found to redistribute the particles on the deactivated catalysts, and high catalytic activity was recovered after this process
Unexpectedly Enhanced Organics Removal in Persulfate Oxidation with High Concentration of Sulfate: The Origin and the Selectivity
Massive anions in high saline wastewater are primary
factors that
restricted the efficiency of pollutant degradation in advanced oxidation
processes (AOPs). Herein, we reported the influence laws of different
anions at high concentration on the electron-transfer process in the
activation of persulfate, and especially, the sulfate anion exhibited
the excellent promotion effect. Depending on the ionic charge, polarizability,
and size, the anions exerted diverse effects on the dispersed phase
and zeta potential of carbonaceous catalysts, which further embodied
in the removal of pollutants. Based on the differences of reaction
rate constant in water solution and high saline solution, the order
was ClO4– 3– – 42– 32–, obeying the Hofmeister
series. The enhancement of the sulfate anion was widely confirmed
with different carbonaceous catalysts and pollutants with various
structures. It could be attributed to the higher oxidation capacity,
the faster interfacial electron transfer, and the better catalyst
dispersion in the high sulfate environment. On the other hand, the
decrease of zeta potential of the catalyst induced by sulfate reinforced
the electrostatic attraction or repulsion with pollutants, which caused
the selectivity of the sulfate promotion effect. Overall, this study
provides new insights into the mechanism of influence of anions on
AOPs, which refreshed the cognition of the role of sulfate on pollutant
degradation, and helps guide the treatment design of high salinity
wastewater
High-Performance Recovery of Vanadium(V) in Leaching/Aqueous Solution by a Reusable Reagent-Primary Amine N1519
Efficient
extraction and stripping for recovering vanadium(V) from
the leaching/aqueous solution of chromium-bearing vanadium slag (V–Cr
slag) are essential to the reuse of heavy metals. The performance
characteristics of a new reagent, primary amine N1519, were first
reported for extracting vanadium. With a phase ratio of organic to
aqueous up to 1:1, 99.7% of vanadium(V) can be effectively extracted
from the leaching/aqueous solution, and powder of NH<sub>4</sub>VO<sub>3</sub> was obtained through the stripping with ammonia. The new
reagent can be recyclable in use for sustainable reuse after stripping.
Different extraction conditions, e.g., the initial pH of the leaching/aqueous
solution and the molar quantity of N1519 were investigated. The powder
of vanadium-organic compounds (VOC) with N1519 formed in the process
of extraction was obtained and purified through three-steps of solvent-out
crystallizations. The hydrogen bond association mechanism of extraction
was illustrated with the structure of VOC and the enthalpy change
in extraction process. The fast extraction process and slow stripping
procedure for recovering vanadium(V) are suitable for use in annular
centrifugal contactors with very short contact/resident times and
mixed-settler extractors with very good mass transfer, respectively.
The results offer significant advantages over conventional processes
Open-Framework Metal Oxides for Fast and Reversible Hydrated Zinc-Ion Intercalation
The
development of high capacity and stable cathodes is the key
to the successful commercialization of aqueous zinc-ion batteries.
However, significant solvation penalties limit the choice of available
positive electrodes. Herein, hydrated intercalation is proposed to
promote reversible (de)intercalation within host materials by rationally
designing a matching electrode. In contrast to previously reported
works, the as-prepared electrode (NHVO@CC) can achieve fast and reversible
intercalation of hydrated zinc ions in the interlayer gap, leading
to a high capacity of 517 mAh g–1 at 0.1 A g–1 and excellent electrode stability for long-term cycling.
Besides, as a consequence of the flexibility of the NHVO@CC electrode,
a quasi-solid-state battery was achieved with equally advantageous
electrochemical behavior under various bending states. The proposed
hydrated cation direct insertion/extraction sets up an efficient way
of developing high-performance positive electrodes for aqueous batteries
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