19 research outputs found
Microbial Electrolytic Carbon Capture for Carbon Negative and Energy Positive Wastewater Treatment
Energy
and carbon neutral wastewater management is a major goal
for environmental sustainability, but current progress has only reduced
emission rather than using wastewater for active CO<sub>2</sub> capture
and utilization. We present here a new microbial electrolytic carbon
capture (MECC) approach to potentially transform wastewater treatment
to a carbon negative and energy positive process. Wastewater was used
as an electrolyte for microbially assisted electrolytic production
of H<sub>2</sub> and OH<sup>–</sup> at the cathode and protons
at the anode. The acidity dissolved silicate and liberated metal ions
that balanced OH<sup>–</sup>, producing metal hydroxide, which
transformed CO<sub>2</sub> in situ into (bi)Âcarbonate. Results using
both artificial and industrial wastewater show 80–93% of the
CO<sub>2</sub> was recovered from both CO<sub>2</sub> derived from
organic oxidation and additional CO<sub>2</sub> injected into the
headspace, making the process carbon-negative. High rates and yields
of H<sub>2</sub> were produced with 91–95% recovery efficiency,
resulting in a net energy gain of 57–62 kJ/mol-CO<sub>2</sub> captured. The pH remained stable without buffer addition and no
toxic chlorine-containing compounds were detected. The produced (bi)Âcarbonate
alkalinity is valuable for wastewater treatment and long-term carbon
storage in the ocean. Preliminary evaluation shows promising economic
and environmental benefits for different industries
Microbial Metabolism and Community Structure in Response to Bioelectrochemically Enhanced Remediation of Petroleum Hydrocarbon-Contaminated Soil
This
study demonstrates that electrodes in a bioelectrochemical
system (BES) can potentially serve as a nonexhaustible electron acceptor
for <i>in situ</i> bioremediation of hydrocarbon contaminated
soil. The deployment of BES not only eliminates aeration or supplement
of electron acceptors as in contemporary bioremediation but also significantly
shortens the remediation period and produces sustainable electricity.
More interestingly, the study reveals that microbial metabolism and
community structure distinctively respond to the bioelectrochemically
enhanced remediation. Tubular BESs with carbon cloth anode (CCA) or
biochar anode (BCA) were inserted into raw water saturated soils containing
petroleum hydrocarbons for enhancing <i>in situ</i> remediation.
Results show that total petroleum hydrocarbon (TPH) removal rate almost
doubled in soils close to the anode (63.5–78.7%) than that
in the open circuit positive controls (37.6–43.4%) during a
period of 64 days. The maximum current density from the BESs ranged
from 73 to 86 mA/m<sup>2</sup>. Comprehensive microbial and chemical
characterizations and statistical analyses show that the residual
TPH has a strongly positive correlation with hydrocarbon-degrading
microorganisms (HDM) numbers, dehydrogenase activity, and lipase activity
and a negative correlation with soil pH, conductivity, and catalase
activity. Distinctive microbial communities were identified at the
anode, in soil with electrodes, and soil without electrodes. Uncommon
electrochemically active bacteria capable of hydrocarbon degradation
such as <i>Comamonas testosteroni, Pseudomonas putida, and Ochrobactrum
anthropi</i> were selectively enriched on the anode, while hydrocarbon
oxidizing bacteria were dominant in soil samples. Results from genus
or phylum level characterizations well agree with the data from cluster
analysis. Data from this study suggests that a unique constitution
of microbial communities may play a key role in BES enhancement of
petroleum hydrocarbons biodegradation in soils
Active H<sub>2</sub> Harvesting Prevents Methanogenesis in Microbial Electrolysis Cells
Undesired
H<sub>2</sub> sinks, including methanogenesis, are a
serious issue faced by microbial electrolysis cells (MECs) for high-rate
H<sub>2</sub> production. Different from current top-down approaches
to methanogenesis inhibition that showed limited success, this study
found active harvesting can eliminate the source (H<sub>2</sub>) from
all H<sub>2</sub> consumption mechanisms via rapid H<sub>2</sub> extraction
using a gas-permeable hydrophobic membrane and vacuum. Active harvesting
completely prevented CH<sub>4</sub> production and led to H<sub>2</sub> yields (2.62–3.39 mol of H<sub>2</sub>/mol of acetate) much
higher than that of the control using traditional spontaneous release
(0.79 mol of H<sub>2</sub>/mol of acetate). In addition, existing
CH<sub>4</sub> production in the control MEC was stopped once the
switch to active H<sub>2</sub> harvesting was made. Active harvesting
also increased current density by 36%, which increased operation efficiency
and facilitated organic removal. Energy quantification shows the process
was energy-positive, as the H<sub>2</sub> energy produced via active
harvesting was 220 ± 10% of external energy consumption, and
a high purity of H<sub>2</sub> can be obtained
Microbial Photoelectrosynthesis for Self-Sustaining Hydrogen Generation
Current
artificial photosynthesis (APS) systems are promising for
the storage of solar energy via transportable and storable fuels,
but the anodic half-reaction of water oxidation is an energy intensive
process which in many cases poorly couples with the cathodic half-reaction.
Here we demonstrate a self-sustaining microbial photoelectrosynthesis
(MPES) system that pairs microbial electrochemical oxidation with
photoelectrochemical water reduction for energy efficient H<sub>2</sub> generation. MPES reduces the overall energy requirements thereby
greatly expanding the range of semiconductors that can be utilized
in APS. Due to the recovery of chemical energy from waste organics
by the mild microbial process and utilization of cost-effective and
stable catalyst/electrode materials, our MPES system produced a stable
current of 0.4 mA/cm<sup>2</sup> for 24 h without any external bias
and ∼10 mA/cm<sup>2</sup> with a modest bias under one sun
illumination. This system also showed other merits, such as creating
benefits of wastewater treatment and facile preparation and scalability
Brönsted Catalyzed Hydrolysis of Microcystin-LR by Siderite
Six naturally occurring minerals
were employed to catalyze the
hydrolysis of microcystin-LR (MC-LR) in water. After preliminary screening
experiments, siderite stood out among these minerals due to its higher
activity and selectivity. In comparison with kaolinite, which is known
to act as a Lewis acid catalyst, siderite was found to act primarily
as a Brönsted acid catalyst in the hydrolysis of MC-LR. More
interestingly, we found that the presence of humic acid significantly
inhibited catalytic efficiency of kaolinite, while the efficiency
of siderite remained high (∼98%). Reaction intermediates detected
by LC-ESI/MS were used to indicate cleavage points in the macrocyclic
ring of MC-LR, and XPS was used to characterize siderite interaction
with MC-LR. Detailed analysis of the <i>in situ</i> ATR-FTIR
absorption spectra of MC-LR indicated hydrogen bonding at the siderite–water–MC-LR
interface. A metastable ring, involving hydrogen bonding, between
surface bicarbonate of siderite and an amide of MC-LR was proposed
to explain the higher activity and selectivity toward MC-LR. Furthermore,
siderite was found to reduce the toxicity of MC-LR to mice by hydrolyzing
MC-LR peptide bonds. The study demonstrates the potential of siderite,
an earth-abundant and biocompatible mineral, for removing MC-LR from
water
Demethanation Trend of Hydrochar Induced by Organic Solvent Washing and Its Influence on Hydrochar Activation
Hydrochar derived
from hydrothermal carbonization (HTC) has been
recognized as a promising carbonaceous material for environmental
remediation. Organic solvents are widely used to extract bio-oil from
hydrochar after HTC, but the effects of solvent extraction on hydrochar
characteristics have not been investigated. This study comprehensively
analyzed the effects of different washing times and solvent types
on the hydrochar properties. The results indicate that the mass loss
of hydrochar by tetrahydrofuran washing occurred mainly in the first
90 min, and the loss ratios of elements followed a descending order
of H > C > O, resulting in a decrease in the H/C atomic ratio
and
an increase in the O/C atomic ratio. The use of various solvents for
washing brought about hydrochar loss ratios in a descending order
of petroleum ether < dichloromethane < acetone < tetrahydrofuran.
The results from the Van Krevelen diagram and Fourier transform infrared, <sup>13</sup>C nuclear magnetic resonance, and X-ray photoelectron spectroscopies
further confirmed that demethanation controlled this washing process.
Most importantly, the surface area of hydrochar increased after bio-oil
removal via washing, which promoted the surface area development for
hydrochar-derived magnetic carbon composites, but to some extent decreased
the microporosity. Additionally, hydrochar washing by organic solvent
has important implications for the global carbon cycle and its remediation
application
Nickel-Based Membrane Electrodes Enable High-Rate Electrochemical Ammonia Recovery
Wastewater
contains significant amounts of nitrogen that can be
recovered and valorized as fertilizers and chemicals. This study presents
a new membrane electrode coupled with microbial electrolysis that
demonstrates very efficient ammonia recovery from synthetic centrate.
The process utilizes the electrical potential across electrodes to
drive NH<sub>4</sub><sup>+</sup> ions toward the hydrophilic nickel
top layer on a gas-stripping membrane cathode, which takes advantage
of surface pH increase to realize spontaneous NH<sub>3</sub>Â production
and separation. Compared with a control configuration with conventionally
separated electrode and hydrophobic membrane, the integrated membrane
electrode showed 40% higher NH<sub>3</sub>–N recovery rate
(36.2 ± 1.2 gNH<sub>3</sub>–N/m<sup>2</sup>/d) and 11%
higher current density. The energy consumption was 1.61 ± 0.03
kWh/kgNH<sub>3</sub>–N, which was 20% lower than the control
and 70–90% more efficient than competing electrochemical nitrogen
recovery processes (5–12 kWh/kgNH<sub>3</sub>–N). Besides,
the negative potential on membrane electrode repelled negatively charged
organics and microbes thus reduced fouling. In addition to describing
the system’s performance, we explored the underlying mechanisms
governing the reactions, which confirmed the viability of this process
for efficient wastewater–ammonia recovery. Furthermore, the
nickel-based membrane electrode showed excellent water entry pressure
(∼41 kPa) without leakage, which was much higher than that
of PTFE/PDMS-based cathodes (∼1.8 kPa). The membrane electrode
also showed superb flexibility (180° bend) and can be easily
fabricated at low cost (<20 $/m<sup>2</sup>)
Alternating Current Influences Anaerobic Electroactive Biofilm Activity
Alternating current
(AC) is known to inactivate microbial growth
in suspension, but how AC influences anaerobic biofilm activities
has not been systematically investigated. Using a <i>Geobacter</i> dominated anaerobic biofilm growing on the electrodes of microbial
electrochemical reactors, we found that high frequency AC ranging
from 1 MHz to 1 kHz (amplitude of 5 V, 30 min) showed only temporary
inhibition to the biofilm activity. However, lower frequency (100
Hz, 1.2 or 5 V) treatment led to 47 ± 19% permanent decrease
in limiting current on the same biofilm, which is attributed to the
action of electrohydrodynamic force that caused biofilm damage and
loss of intercellular electron transfer network. Confocal microscopy
images show such inactivation mainly occurred at the interface between
the biofilm and the electrode. Reducing the frequency further to 1
Hz led to water electrolysis, which generated gas bubbles that flushed
all attached cells out of the electrode. These findings provide new
references on understanding and regulating biofilm growth, which has
broader implications in biofouling control, anaerobic waste treatment,
energy and product recovery, and general understanding of microbial
ecology and physiology
Influences of Temperature and Metal on Subcritical Hydrothermal Liquefaction of Hyperaccumulator: Implications for the Recycling of Hazardous Hyperaccumulators
Waste <i>Sedum plumbizincicola</i>, a zinc (Zn) hyperaccumulator
during phytoremediation, was recycled via a subcritical hydrothermal
liquefaction (HTL) reaction into multiple streams of products, including
hydrochar, bio-oil, and carboxylic acids. Results show approximately
90% of Zn was released from the <i>S. plumbizincicola</i> biomass during HTL at an optimized temperature of 220 °C, and
the release risk was mitigated via HTL reaction for hydrochar production.
The low-Zn hydrochar (∼200 mg/kg compared to original plant
of 1558 mg/kg) was further upgraded into porous carbon (PC) with high
porosity (930 m<sup>2</sup>/g) and excellent capability of carbon
dioxide (CO<sub>2</sub>) capture (3 mmol/g). The porosity, micropore
structure, and graphitization degree of PCs were manipulated by the
thermal recalcitrance of hydrochar. More importantly, results showed
that the released Zn<sup>2+</sup> could effectively promote the production
of acetic acid via the oxidation of furfural (FF) and 5-(hydroxymethyl)-furfural
(HMF). Fourier transform ion cyclotron resonance mass spectrometry
(FT-ICR MS) with negative electrospray ionization analysis confirmed
the deoxygenation and depolymerization reactions and the production
of long chain fatty acids during HTL reaction of <i>S. plumbizincicola</i>. This work provides a new path for the recycling of waste hyperaccumulator
biomass into value-added products