13 research outputs found
Bioreactor Performance and Quantitative Analysis of Methanogenic and Bacterial Community Dynamics in Microbial Electrolysis Cells during Large Temperature Fluctuations
The use of microbial electrolysis cells (MECs) for H<sub>2</sub> production generally finds H<sub>2</sub> sink by undesirable
methanogenesis
at mesophilic temperatures. Previously reported approaches failed
to effectively inhibit methanogenesis without the addition of nongreen
chemical inhibitors. Here, we demonstrated that the CH<sub>4</sub> production and the number of methanogens in single-chamber MECs
could be restricted steadily to a negligible level by continuously
operating reactors at the relatively low temperature of 15 °C.
This resulted in a H<sub>2</sub> yield and production rate comparable
to those obtained at 30 °C with less CH<sub>4</sub> production
(CH<sub>4</sub>% < 1%). However, this operation at 15 °C should
be taken from the initial stage of anodic biofilm formation, when
the methanogenic community has not yet been established sufficiently.
Maintaining MECs operating at 20 °C was not effective for controlling
methanogenesis. The varying degrees of methanogenesis observed in
MECs at 30 °C could be completely inhibited at 4 and 9 °C,
and the total number of methanogens (mainly hydrogenotrophic methanogens)
could be reduced by 68–91% during 32–55 days of operation
at the low temperatures. However, methanogens cannot be eliminated
completely at these temperatures. After the temperature is returned
to 30 °C, the CH<sub>4</sub> production and the number of total
methanogens can rapidly rise to the prior levels. Analysis of bacterial
communities using 454 pyrosequencing showed that changes in temperature
had no a substantial impact on composition of dominant electricity-producing
bacteria (Geobacter). The results of
our study provide more information toward understanding the temperature-dependent
control of methanogenesis in MECs
In Situ Photochemical Activation of Sulfate for Enhanced Degradation of Organic Pollutants in Water
The advanced oxidation process (AOP)
based on SO<sub>4</sub><sup>•–</sup> radicals has been
receiving growing attention
in water and wastewater treatment. Producing SO<sub>4</sub><sup>•–</sup> radicals by activation of peroxymonosulfate or persulfate faces
the challenges of high operational cost and potential secondary pollution.
In this study, we report the in situ photochemical activation of sulfate
(<i>i</i>-PCAS) to produce SO<sub>4</sub><sup>•–</sup> radicals with bismuth phosphate (BPO) serving as photocatalyst.
The prepared BPO rod-like material could achieve remarkably enhanced
degradation of 2,4-dichlorophenol (2,4-DCP) in the presence of sulfate,
indicated by the first-order kinetic constant (<i>k</i> =
0.0402 min<sup>–1</sup>) being approximately 2.1 times that
in the absence (<i>k</i> = 0.019 min<sup>–1</sup>) at pH-neutral condition. This presented a marked contrast with
commercial TiO<sub>2</sub> (P25), the performance of which was always
inhibited by sulfate. The impact of radical scavenger and electrolyte,
combined with electron spin resonance (ESR) measurement, verified
the formation of •OH and SO<sub>4</sub><sup>•–</sup> radicals during <i>i</i>-PCAS process. According to theoretical
calculations, BPO has a sufficiently high valence band potential making
it thermodynamically favorable for sulfate oxidation, and weaker interaction
with SO<sub>4</sub><sup>•–</sup> radicals resulting
in higher reactivity toward target organic pollutant. The concept
of <i>i</i>-PCAS appears to be attractive for creating new
photochemical systems where in situ production of SO<sub>4</sub><sup>•–</sup> radicals can be realized by using sulfate
originally existing in aqueous environment. This eliminates the need
for extrinsic chemicals and pH adjustment, which makes water treatment
much easier, more economical, and more sustainable
Data_Sheet_1.pdf
<p>p-Nitrophenol (PNP) is common in the wastewater from many chemical industries. In this study, we investigated the effect of initial concentrations of PNP and glucose and applied voltage on PNP reduction in biocathode BESs and open-circuit biocathode BESs (OC-BES). The PNP degradation efficiency of a biocathode BES with 0.5 V (Bioc-0.5) reached 99.5 ± 0.8%, which was higher than the degradation efficiency of the BES with 0 V (Bioc-0) (62.4 ± 4.5%) and the OC-BES (59.2 ± 12.5%). The PNP degradation rate constant (k<sub>PNP</sub>) of Bioc-0.5 was 0.13 ± 0.01 h<sup>-1</sup>, which was higher than the k<sub>PNP</sub> of Bioc-0 (0.024 ± 0.002 h<sup>-1</sup>) and OC-BES (0.013 ± 0.0005 h<sup>-1</sup>). PNP degradation depended on the initial concentrations of glucose and PNP. A glucose concentration of 0.5 g L<sup>-1</sup> was best for PNP degradation. The initial PNP increased from 50 to 130 mg L<sup>-1</sup> and the k<sub>PNP</sub> decreased from 0.093 ± 0.008 to 0.027 ± 0.001 h<sup>-1</sup>. High-throughput sequencing of 16S rRNA gene amplicons indicated differences in microbial community structure between BESs with different voltages and the OC-BES. The predominant populations were affiliated with Streptococcus (42.7%) and Citrobacter (54.1%) in biocathode biofilms of BESs, and Dysgonomonas were the predominant microorganisms in biocathode biofilms of OC-BESs. The predominant populations were different among the cathode biofilms and the suspensions. These results demonstrated that applied voltage and biocathode biofilms play important roles in PNP degradation.</p
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MOESM1 of Multiple syntrophic interactions drive biohythane production from waste sludge in microbial electrolysis cells
Additional file 1: Table. S1. Similarity-based OTUs and species richness and diversity estimates of bacteria in different systems. Figure. S1. Current density of MEC fed with raw sludge (RS-MEC) and alkali-pretreated waste sludge (AS-MEC). Figure. S2. Variations of SCOD (A), soluble protein (B) and carbohydrates concentration (C) of raw sludge open-circuit MEC (RS-OCMEC), MEC fed with raw sludge (RS-MEC) or alkali-pretreated sludge (AS-MEC)
Biodegradation of Sulfonamide Antibiotics by Microalgae: Mechanistic Insights into Substituent-Induced Effects
Microalgae are a sustainable environmentally friendly
wastewater
treatment technology that has attracted much attention for use in
the purification of antibiotic-containing wastewater. However, research
into the mechanisms involved in microalgal antibiotic degradation
is still in the initial stages, especially concerning the relationship
between pollutant structure and removal rate. This study comprehensively
analyzed the antibiotic biodegradation mechanisms in microalgae from
a molecular structure perspective, examining four sulfonamide antibiotics
(SAs) with different substituents as representative pollutants. Microalgae
exhibited removal efficiencies of 86.15, 74.24, 60.14, and 46.60%
for sulfathiazole, sulfamethazine, sulfadiazine, and sulfamethoxazole,
respectively. It is noteworthy that cytochrome p450 (CYP450) played
a central catalyzing role in their metabolism. Further analysis of
molecular dynamics simulations and density functional theory calculations
revealed that the geometric differences and electronic effect variations
caused by the substituents significantly affected the catalytic activity
of CYP450 as well as the overall reactivity of the SAs, resulting
in different removal rates. Overall, SAs with high binding energy,
low energy gap, and high electrophilicity indices were more readily
catalyzed by CYP450 as evidenced by the degradation pathways. These
results provide valuable insights at the molecular level into how
different substituents affect the degradation rate of SAs in microalgae
Electricity Generation and Pollutant Degradation Using a Novel Biocathode Coupled Photoelectrochemical Cell
The
photoelectrochemical cell (PEC) is a promising tool for the
degradation of organic pollutants and simultaneous electricity recovery,
however, current cathode catalysts suffer from high costs and short
service lives. Herein, we present a novel biocathode coupled PEC (Bio-PEC)
integrating the advantages of photocatalytic anode and biocathode.
Electrochemical anodized TiO<sub>2</sub> nanotube arrays fabricated
on Ti substrate were used as Bio-PEC anodes. Field-emission scanning
electron microscope images revealed that the well-aligned TiO<sub>2</sub> nanotubes had inner diameters of 60–100 nm and wall-thicknesses
of about 5 nm. Linear sweep voltammetry presented the pronounced photocurrent
output (325 μA/cm<sup>2</sup>) under xenon illumination, compared
with that under dark conditions. Comparing studies were carried out
between the Bio-PEC and PECs with Pt/C cathodes. The results showed
that the performance of Pt/C cathodes was closely related with the
structure and Pt/C loading amounts of cathodes, while the Bio-PEC
achieved similar methyl orange (MO) decoloration rate (0.0120 min<sup>–1</sup>) and maximum power density (211.32 mW/m<sup>2</sup>) to the brush cathode PEC with 50 mg Pt/C loading (Brush-PEC, 50
mg). The fill factors of Bio-PEC and Brush-PEC (50 mg) were 39.87%
and 43.06%, respectively. The charge transfer resistance of biocathode
was 13.10 Ω, larger than the brush cathode with 50 mg Pt/C (10.68
Ω), but smaller than the brush cathode with 35 mg Pt/C (18.35
Ω), indicating the comparable catalytic activity with Pt/C catalyst.
The biocathode was more dependent on the nutrient diffusion, such
as nitrogen and inorganic carbon, thus resulting in relatively higher
diffusion resistance compared to the brush cathode with 50 mg Pt/C
loading that yielded similar MO removal and power output. Considering
the performance and cost of PEC system, the biocathode was a promising
alternative for the Pt/C catalyst
Occurrence and Profiles of Phthalates in Foodstuffs from China and Their Implications for Human Exposure
Phthalate esters are used in a wide variety of consumer
products,
and human exposure to this class of compounds is widespread. Nevertheless,
studies on dietary exposure of humans to phthalates are limited. In
this study, nine phthalate esters were analyzed in eight categories
of foodstuffs (<i>n</i> = 78) collected from Harbin and
Shanghai, China, in 2011. Dimethyl phthalate (DMP), diethyl phthalate
(DEP), dibutyl phthalate (DBP), diisobutyl phthalate (DIBP), benzyl
butyl phthalate (BzBP), and diethylhexyl phthalate (DEHP) were frequently
detected in food samples. DEHP was the major compound found in most
of the food samples, with concentrations that ranged from below the
limit of quantification (LOQ) to 762 ng/g wet weight (wt). The concentrations
of phthalates in food samples from China were comparable to concentrations
reported for several other countries, but the profiles were different;
DMP was found more frequently in Chinese foods than in foods from
other countries. The estimated daily dietary intake of phthalates
(EDI<sub>diet</sub>) was calculated based on the concentrations measured
and the daily ingestion rates of food items. The EDI<sub>diet</sub> values for DMP, DEP, DIBP, DBP, BzBP, and DEHP (based on mean concentrations)
were 0.092, 0.051, 0.505, 0.703, 0.022, and 1.60 μg/kg-bw/d,
respectively, for Chinese adults. The EDI<sub>diet</sub> values calculated
for phthalates were below the reference doses suggested by the United
States Environmental Protection Agency (EPA). Comparison of total
daily intakes, reported previously based on a biomonitoring study,
with the current dietary intake estimates suggests that diet is the
main source of DEHP exposure in China. Nevertheless, diet accounted
for only <10% of the total exposure to DMP, DEP, DBP, and DIBP,
which suggested the existence of other sources of exposure to these
phthalates
Biomass-Derived Porous Fe<sub>3</sub>C/Tungsten Carbide/Graphitic Carbon Nanocomposite for Efficient Electrocatalysis of Oxygen Reduction
The
oxygen-reduction reaction (ORR) draws an extensive attention in many
applications, and there is a growing interest to develop effective
ORR electrocatalysts. Iron carbide (Fe<sub>3</sub>C) is a promising
alternative to noble metals (e.g., platinum), but its performances
need further improvement, and the real role of the Fe<sub>3</sub>C
phase remains unclear. In this study, we synthesize Fe<sub>3</sub>C/tungsten carbide/graphitic carbon (Fe<sub>3</sub>C/WC/GC) nanocomposites,
with waste biomass (i.e., pomelo peel) serving as carbon source, using
a facile, one-step carbon thermal-reduction method. The nanocomposite
is characterized by a porous structure consisting of uniform Fe<sub>3</sub>C nanoparticles encased by graphitic carbon (GC) layers with
highly dispersed nanosized WC. The Fe<sub>3</sub>C provides the active
sites for ORR, while the graphitic layers and WC nanoparticles can
stibilize the Fe<sub>3</sub>C surface, preventing it from dissociation
in the electrolyte. The Fe<sub>3</sub>C/WC/GC nanocomposite is highly
active, selective, and stable toward four-electron ORR in pH-neutral
electrolyte, which results in a 67.82% higher power density than that
of commercial Pt/C and negligible voltage decay during a long-term
phase of a 33 cycle (2200 h) operation of a microbial fuel cell (MFC).
The density functional theory (DFT) calculations suggest high activity
for splitting the O–O bond of molecular oxygen on the surface
of Fe<sub>3</sub>C
Forward Osmosis with a Novel Thin-Film Inorganic Membrane
Forward
osmosis (FO) represents a new promising membrane technology
for liquid separation driven by the osmotic pressure of aqueous solution.
Organic polymeric FO membranes are subject to severe internal concentration
polarization due to asymmetric membrane structure, and low stability
due to inherent chemical composition. To address these limitations,
this study focuses on the development of a new kind of thin-film inorganic
(TFI) membrane made of microporous silica xerogels immobilized onto
a stainless steel mesh (SSM) substrate. The FO performances of the
TFI membrane were evaluated upon a lab-scale cell-type FO reactor
using deionized water as feed solution and sodium chloride (NaCl)
as draw solution. The results demonstrated that the TFI membrane could
achieve transmembrane water flux of 60.3 L m<sup>–2</sup> h<sup>–1</sup> driven by 2.0 mol L<sup>–1</sup> NaCl draw
solution at ambient temperature. Meanwhile, its specific solute flux,
i.e. the solute flux normalized by the water flux (0.19 g L<sup>–1</sup>), was 58.7% lower than that obained for a commercial cellulose triacetate
(CTA) membrane (0.46 g L<sup>–1</sup>). The quasi-symmetry
thin-film microporous structure of the silica membrane is responsible
for low-level internal concentration polarization, and thus enhanced
water flux during FO process. Moreover, the TFI membrne demonstrated
a substantially improved stability in terms of mechanical strength,
and resistance to thermal and chemical stimulation. This study not
only provides a new method for fabricating quasi-symmetry thin-film
inorganic silica membrane, but also suggests an effective strategy
using this alternative membrane to achieve improved FO performances
for scale-up applications
How β‑Cyclodextrin-Functionalized Biochar Enhanced Biodenitrification in Low C/N Conditions via Regulating Substrate Metabolism and Electron Utilization
Biodenitrification plays a vital role in the remediation
of nitrogen-contaminated
water. However, influent with a low C/N ratio limits the efficiency
of denitrification and causes the accumulation/emission of noxious
intermediates. In this study, β-cyclodextrin-functionalized
biochar (BC@β-CD) was synthesized and applied to promote the
denitrification performance of Paracoccus denitrificans when the C/N was only 4, accompanied by increased nitrate reduction
efficiency and lower nitrite accumulation and nitrous oxide emission.
Transcriptomic and enzymatic activity analyses showed BC@β-CD
enhanced glucose degradation by promoting the activities of glycolysis
(EMP), the pentose phosphate pathway (PPP), and the tricarboxylic
acid (TCA) cycle. Notably, BC@β-CD drove a great generation
of electron donors by stimulating the TCA cycle, causing a greater
supply of substrate metabolism to denitrification. Meanwhile, the
promotional effect of BC@β-CD on oxidative phosphorylation accelerates
electron transfer and ATP synthesis. Moreover, the presence of BC@β-CD
increased the intracellular iron level, causing further improved electron
utilization in denitrification. BC@β-CD helped to remove metabolites
and induced positive feedback on the metabolism of P. denitrificans. Collectively, these effects elevated the glucose utilization for
supporting denitrification from 36.37% to 51.19%. This study reveals
the great potential of BC@β-CD for enhancing denitrification
under low C/N conditions and illustrates a potential application approach
for β-CD in wastewater bioremediation