Category: Green Energy

Interesting news around wind and solar energy, bioenergy, like biogas, biomass, biofuel, hydro power, geothermal energy, and much more.

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Stability of anion exchange membranes for electrolysis

Electrolyzer in China

Energy security and climate change are among the greatest challenges of our time. To reduce dependence on fossil fuels, renewable energy sources are emerging as key solutions for sustainable energy production. To this end, scalable solutions are essential for storing and transporting renewable energy. Hydrogen produced in water electrolyzers and reconverted into electricity in fuel cells can help balance the seasonal variability of renewable energy.

Fuel cells have the potential to significantly contribute to the decarbonization of the transport sector. Transport of people and goods accounts for almost one‑third of global greenhouse gas emissions. Despite this potential, the widespread adoption of modern fuel cells and electrolyzers remains limited due to high investment costs. This is mainly due to expensive noble‑metal catalysts and perfluorinated proton exchange membranes.

This challenge has sparked growing interest in anion exchange membranes. Under alkaline conditions, they offer several advantages:

  • Use of non‑noble metal catalysts thanks to non‑corrosive conditions
  • More sustainable membrane materials

However, there are hurdles to their introduction, particularly their short lifetime under alkaline conditions and oxidative stress. The formation of hydrogen peroxide and hydroxyl radicals under alkaline conditions is responsible for the accelerated degradation of polymer membranes. Investigation radical‑induced degradation of anion exchange membranes is therefore of central importance.

Hence, efficient radical generation in the laboratory is required. Current methods such as thermal decomposition or UV activation of hydrogen peroxide are inefficient and prone to side reactions, limiting their relevance to real operating conditions. Immersion in oxygen‑saturated alkaline solutions has provided useful insights, but cannot distinguish between natural membrane degradation and radical‑accelerated breakdown.

Radioactivity and electromagnetic pulse radiation allow precise control of radical formation but require expensive, specialized infrastructure. Affordable and practical solutions are needed to study radicals under realistic laboratory conditions.

Researchers from SINTEF in Norway and ETH Zurich have addressed this challenge. They introduced adapted photochemical methods to generate radicals and study their influence on the stability of anion exchange membranes independently of other degradation processes. The results were recently published in Membranes.

By irradiating aqueous potassium nitrite solutions or titanium oxide suspensions with UV light at 365 nm, hydroxyl radicals or a combination of hydroxyl and superoxide radicals were successfully generated. Tests on three commercial anion exchange membranes – PiperION®‑40 (PiperION), FM‑FAA‑3‑PK‑75 (Fumasep), and PNB‑R45 (Polynorbornene) – showed clear differences in durability. As expected, thinner, non‑reinforced membranes degraded faster than thicker, reinforced ones, likely due to the limited penetration depth of highly reactive radicals.

Both methods proved to be practical, affordable, and accessible tools for evaluating the stability of anion exchange membranes against radical attack. Photochemical radical generation was thus a viable way to study radical‑induced degradation under controlled conditions. The nitrite‑based approach selectively generated hydroxyl radicals, while titanium oxide suspensions produced both hydroxyl and superoxide radicals. Longer irradiation intensified membrane damage, clearly demonstrating the critical role of radicals in membrane decomposition. Experiments at pH 10 enabled differentiation between natural and radical‑driven causes.

Beyond laboratory use, both methods are also of industrial relevance. Combined with low‑cost laboratory equipment, they provide widely applicable and reproducible tools for evaluating commercial and prototype anion exchange membranes. By reducing costs and extending durability tests under realistic conditions, the development of robust anion exchange membranes for fuel cells and electrolyzers can be accelerated.

Frontis Energy is part of the mission to provide cost‑effective solutions for the development of efficient energy conversion technologies. In doing so, we strengthen the global transition to clean, resilient, and sustainable energy systems.

Solyom, P.; Nauser, T.; Nemeth, T. Photochemical Methods to Study the Radical-Induced Degradation of Anion-Exchange Membranes. Membranes 2025, 15, 305. https://doi.org/10.3390/membranes15100305

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Electrolytic water splitting for binders in building material

DOI: 10.13140/RG.2.2.27780.18562

The oceans are rich in magnesium resources, which that could be used in the production of construction materials. Sorel cement (magnesium cement), for example, can be used in interior building applications as an alternative to screed. Extracting magnesium from seawater traditionally requires a highly energy-intensive calcination process to isolate magnesium oxide (magnesia). The innovative method of electrolysis-controlled water splitting can bypass this process, significantly reducing CO₂ emissions.

To obtain the precursor of magnesia, magnesium hydroxide (Mg[OH]₂), an alkaline solution must be produced. While previous research has investigated electrochemical methods for hydroxide production, few studies have combined efficient alkali synthesis with the direct precipitation of magnesium hydroxide to make magnesia for low-carbon cement. This critical knowledge gap in optimizing energy and material efficiency has now been addressed.

A new study led by a research team at Columbia University used electrochemical water splitting at low voltages (1.6–2.0 V). Hydroxide ions (OH⁻) were generated from seawater through hydrogen production. This led to the direct precipitation of magnesium hydroxide. The findings were recently published in the journal Desalination. This new approach reduces energy intensity by 52–78%. Normally, the energy consumption per ton of MgO is 0.56 MWh. With the new method, carbon emissions per ton of magnesia can be reduced by up to 0.41 tons of CO₂.

To further improve production efficiency, the nanostructure of magnesium hydroxide was optimized using urea as a crosslinker. This enhanced its reactivity, porosity, and specific surface area. At an optimal urea concentration of 0.2 mol/L, magnesia particles exhibited excellent binding properties. The researchers attributed this to the sealing effects of rosette-shaped dypingite and rod-shaped nesquehonite. According to the authors, the formation of these minerals facilitates CO₂ incorporation and enhances carbonate hardening.

Advances in symmetric electrochemical systems, as demonstrated in this study, result in up to a 78% reduction in energy demand for the production of alkaline solutions. This gives these methods the potential to serve as viable alternatives to traditional processes. The further optimization of electrodes and electrolytes represents a pioneering approach to the carbon-neutral production of building materials and alkalis. Additionally, this method highlights how construction material manufacturing can efficiently lead to large-scale CO₂ mineralization. As a result, the greenhouse gas can be permanently removed from the atmosphere.

The industrial scaling of electrochemical alkali production can reduce operating costs, minimize environmental impact, and improve the properties of low-carbon building materials. The economic aspects of this manufacturing process are particularly noteworthy, as the demand for efficient binding materials continues to grow.

At Frontis Energy, we are committed to promoting sustainable and economically viable energy solutions. Research like this provides valuable insights and innovations to support such sustainable advancements.

Chu. Yang, Unluer, 2025, Energy-efficient calcination-free Mg cement recovered from desalination brine, Desalination, Volume 610, 118928, 10.1016/j.desal.2025.118928.

Image: Pixabay

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From waste heat to ultrapure water: A new technology transforming renewable hydrogen

DOI: 10.13140/RG.2.2.34925.24809

Hydrogen (H₂), produced using renewable energy, has emerged as a possible alternative to fossil fuel. This versatile molecule can serve as an energy carrier, an efficient storage solution, and a sustainable feedstock for transportation, chemical processing, and energy systems worldwide.

Unlike fossil fuels, hydrogen produces no harmful emissions when used. It can be generated using electrolyzers running on renewable energy and abundant water as feedstock. It then becomes a renewable and sustainable energy source, reducing reliance on depleting fossil fuel reserves, helping combat climate change. Consequently, hydrogen production has become a key priority on the political agenda of numerous countries.

However, the water used in electrolyzers must be ultrapure in order to protect the electrodes of electrolyzers from poisoning and avoid chloride oxidation to chlorine. Abundant seawater adds several challenges when directly fed to electrolyzer plants for hydrogen production, making highly pure water, specifically ultrapure water, an expensive necessity. Ultrapure water is produced in a series of steps, including pretreatment to remove suspended solids and desalination to eliminate salts, organics, and colloidal particles. Polishing techniques such as deionization, degasification, and ultraviolet treatment are then used to achieve the required quality. Among these processes, desalination is particularly critical for removing most impurities.

Reverse osmosis, especially seawater reverse osmosis, is a widely used desalination technology but has notable drawbacks, such as requiring high-pressure operation (high energy consumption), intensive pretreatment, and producing concentrated brine, which can harm marine ecosystems when discharged. Membrane distillation has gained attention as an alternative for producing high-quality water and supporting recovery applications. It operates at lower temperatures and has the ability to utilize waste heat.

Membrane distillation is a thermal separation process where a vapor pressure difference across a hydrophobic membrane causes liquid particles to phase change and pass through as gas. Operating at ambient pressure and utilizing low-temperature heat sources (<90 °C), membrane distillation offers significant advantages. However, research on membrane distillation as a viable alternative to reverse osmosis for ultrapure water production remains limited, particularly in areas such as module design and techno-economic analysis.

A group of researchers at the Fraunhofer Institute for Solar Energy Systems (ISE) in Freiburg, Germany, has explored the potential of membrane distillation as a cost- and energy-efficient alternative to reverse osmosis for producing ultrapure water for proton exchange membrane (PEM) electrolyzers. The findings were recently published in the Desalination Journal. They introduced membrane distillation as a possible alternative to reverse osmosis for ultrapure water production. But here is the twist: the membrane distillation system ingeniously taps into waste heat from a 5 MW proton exchange membrane electrolyzer, transforming what would typically be an efficiency liability into an asset for sustainability. So far, their results are impressive—membrane distillation not only produces exceptional distillate (<3 μS/cm) but does so at a cost ranging from €2.33 to €2.85 per ton of distillate, compared to reverse osmosis’s €2.80 to €5.51. Using membrane distillation, seawater desalination could be 50% or more cheaper.

Economic analyses highlight that membrane distillation’s cost-effectiveness is driven by its low electrical energy requirements and optimized short-channel module design. Its impressive energy efficiency, enabled using low-grade thermal energy, establishes membrane distillation as a highly versatile and environmentally friendly solution that aligns seamlessly with the vision for renewable hydrogen production. This study positions membrane distillation as more than just an alternative to reverse osmosis: it is a smarter and greener approach to ultrapure water production.

Their findings have the potential to reshape the industrial approach to ultrapure water production. By demonstrating an efficient use of waste heat and providing a more economical solution, it offers industries a pathway to lower operational costs while advancing sustainability. This aligns particularly well with sectors striving for greener operations, such as renewable hydrogen production and other energy-intensive applications. Moreover, the adoption of membrane distillation could catalyze innovation in system design and integration, encouraging industries to optimize processes and reduce dependence on traditional, energy-intensive methods. This shift can contribute to broader sustainability goals and improve the economic feasibility of renewable energy initiatives.

At Frontis Energy, we are committed to advancing sustainable and green energy solutions by embracing innovative technologies like membrane distillation, bringing us closer to a sustainable future.

Schwantes et al. 2025 Thermally driven ultrapure water production for water electrolysis – A techno-economic analysis of membrane distillation, Desalination, Volume 608, 118848, DOI: 10.1016/j.desal.2025.118848.

Image: Pixabay

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Unlocking the potential of conducting polymers for sustainable water treatment and energy solutions

DOI: 10.13140/RG.2.2.24586.94404

Carbon based materials have a broad range of applications such as energy storage and conversion, electronics, nanotechnology, water purification, and catalysis. They are made of an element which is available everywhere.

In recent times, the electrochemical features of carbon-based electrodes are being enhanced by using conducting polymers. Carbon cloth, woven from carbon microfibers, serves as a promising carbon-based electrode, which acts as a durable and cost-effective medium for facilitating electrochemical reactions that degrade pollutants and improve water quality. These electrodes, notable for their mechanical flexibility, strength, and cost-effectiveness, are employed in processes such as electrochemical oxidation, microbial fuel cells, and other advanced wastewater treatment technologies.

Due to a few limitations of pristine carbon cloth electrodes such as low specific capacitance and limited wettability associated with its inherent hydrophobicity, scientists conduct research to improve the modern electrodes. For instance, since wettability is crucial for for immersing the electrode surface in liquid and ensuring interaction with contaminants, enhancing it is always beneficial for the process. Improving the performance of carbon cloth electrodes could lead to more efficient treatment, faster reaction times, and better overall performance.

A research group at San Diego State University undertook the task of addressing these limitations by making conformal conducting polymer films on carbon fibers via oxidative chemical vapor deposition (oCVD) method. They recently published their results in the Advanced Material Interface Journal. With antimony pentachloride (SbCl5) as the oxidant, they developed a highly uniform coating of poly(3,4-ethylenedioxythiophene) (PEDOT) on three-dimensional porous fibers. The oCVD technique ensures uniform coatings while preserving the geometric and functional properties of the carbon cloth, making it a promising approach for enhancing electrochemical performance.

The PEDOT-coated carbon cloth electrodes achieved a remarkable improvement in specific capacitance and pseudocapacitance compared to pristine carbon cloth. Depending on the deposition temperature, the oCVD PEDOT-coated electrodes showed a 1.5- to 2.3-fold enhancement in specific capacitance. Notably, the electrode fabricated at a deposition temperature of 80 °C exhibited the highest specific capacitance and superior electrochemical performance. Adjusting the deposition temperature to optimize performance can help tailor carbon cloth electrodes for specific wastewater treatment needs.

The investigation underscores the effectiveness of the oCVD method in addressing the limitations of carbon cloth electrodes and expanding their potential applications in wastewater treatment and electrochemical energy storage devices. Furthermore, the researchers showed that PEDOT-coated carbon cloth can be applied as supercapacitors, where flexibility and high capacitance are critical. It should be noted that the study not only showcases significant advancements in material design but also open new avenues for optimizing electrode performance for diverse applications.

Overall, the findings emphasize the growing potential of advanced electrode technologies in addressing industrial challenges. By improving the functionality of carbon-based electrodes through novel material coatings, industries can achieve more efficient and tailored solutions for both wastewater treatment and energy storage. The ability to fine-tune electrode properties to meet specific requirements offers a pathway toward the development of highly efective and cost-efficient technologies, which could be a game-changer for sectors focused on sustainability and resource management. As these innovations continue to evolve, they have the potential to significantly improve operational efficiency and environmental impact across various industries. For example, in wastewater treatment, electrochemical processes such as electrocoagulation, electrooxidation, or electroreduction are often used to remove contaminants.

At Frontis Energy, we believe that improvements and customization can aid in designing electrodes tailored to specific contaminants or types of wastewater.

Heydari Gharahcheshmeh and Chowdhury, 2024, Enhancing Capacitance of Carbon Cloth Electrodes via Highly Conformal PEDOT Coating Fabricated by the OCVD Method Utilizing SbCl5 Oxidant, Advanced Materials Interfaces, 11, 2400118. DOI: 10.1002/admi.202400118.

Image: Pixabay

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Producing liquid bio-electrically engineered fuels from CO2

At Frontis Energy we have spent much thought on how to recycle CO2. While high value products such as polymers for medical applications are more profitable, customer demand for such products is too low to recycle CO2 in volumes required to decarbonize our atmosphere to pre-industrial levels. Biofuel, for example from field crops or algae has long been thought to be the solution. Unfortunately, they require too much arable land. On top of their land use, biochemical pathways are too complex to understand by the human brain. Therefore, we propose a different way to quickly reach the target of decarbonizing our planet. The proce­dure begins with a desired target fuel and suggests a mi­crobial consortium to produce this fuel. In a second step, the consortium will be examined in a bio-electrical system (BES).

CO2 can be used for liquid fuel production via multiple pathways. The end product, long-chain alcohols, can be used either directly as fuel or reduced to hydrocarbons. Shown are examples of high level BEEF pathways using CO2 and electricity as input and methane, acetate, or butanol as output. Subsequent processes are 1, aerobic methane oxida­tion, 2, direct use of methane, 3 heterotrophic phototrophs, 4, acetone-butanol fermentation, 5, heterotrophs, 6, butanol di­rect use, 7, further processing by yeasts

Today’s atmospheric CO2 imbalance is a consequence of fossil carbon combus­tion. This real­ity requires quick and pragmatic solutions if further CO2 accu­mulation is to be prevented. Direct air capture of CO2 is moving closer to economic feasibility, avoid­ing the use of arable land to grow fuel crops. Producing combustible fuel from CO2 is the most promis­ing inter­mediate solution because such fuel integrates seamlessly into existing ur­ban in­frastructure. Biofuels have been ex­plored inten­sively in re­cent years, in particular within the emerging field of syn­thetic biol­ogy. How­ever tempt­ing the application of genetically modified or­ganisms (GMOs) ap­pears, non-GMO technology is easier and faster to im­plement as the re­quired microbial strains al­ready exist. Avoiding GMOs, CO2 can be used in BES to produce C1 fu­els like methane and precursors like formic acid or syngas, as well as C1+ com­pounds like ac­etate, 2-oxybut­yrate, bu­tyrate, ethanol, and butanol. At the same time, BES inte­grate well into urban in­frastructure without the need for arable land. However, except for meth­ane, none of these fuels are readily com­bustible in their pure form. While elec­tromethane is a com­mercially avail­able al­ternative to fossil natu­ral gas, its volumetric energy den­sity of 40-80 MJ/m3 is lower than that of gasoline with 35-45 GJ/m3. This, the necessary technical modifications, and the psychological barrier of tanking a gaseous fuel make methane hard to sell to automobilists. To pro­duce liq­uid fuel, carbon chains need to be elongated with al­cohols or better, hy­drocarbons as fi­nal prod­ucts. To this end, syngas (CO + H2) is theoreti­cally a viable option in the Fischer-Tropsch process. In reality, syngas pre­cursors are ei­ther fossil fu­els (e.g. coal, natural gas, methanol) or biomass. While the for­mer is ob­viously not CO2-neu­tral, the latter com­petes for arable land. The di­rect con­version of CO2 and electrolytic H2 to C1+ fuels, in turn, is catalyzed out by elec­troactive microbes in the dark (see title figure), avoid­ing food crop com­petition for sun-lit land. Unfortunately, little re­search has been under­taken beyond proof of con­cept of few electroactive strains. In stark con­trast, a plethora of metabolic studies in non-BES is avail­able. These studies often pro­pose the use of GMOs or complex or­ganic sub­strates as precur­sors. We propose to systemati­cally identify metabolic strategies for liquid bio-electrically engineered fuel (BEEF) production. The fastest approach should start by screening meta­bolic data­bases using es­tablished methods of metabolic modeling, fol­lowed by high throughput hypothesis testing in BES. Since H2 is the intermediate in bio-electrosynthesis, the most efficient strategy is to focus on CO2 and H2 as di­rect pre­cursors with as few in­termediate steps as pos­sible. Scala­bility and energy effi­ciency, eco­nomic feasibil­ity that is, are pivotal elements.

First, an electrotrophic acetogen produces acetate, which then used by heterotrophic algae in a consecutive step.

The biggest obstacle for BEEF production is lacking knowledge about pathways that use CO2 and electrolytic H2. This gap exists despite metabolic data­bases like KEGG and more recently KBase, making metabolic design and adequate BEEF strain selection a guessing game rather than an educated ap­proach. Nonetheless, metabolic tools were used to model fuel pro­duction in single cell yeasts and various prokaryotes. In spite of their shortcomings, metabolic data­bases were also employed to model species interactions, for example in a photo-het­erotroph consor­tium using software like ModelSEED / KBase (http://mod­elseed.org/), RAVEN / KEGG and COBRA. A first sys­tematic at­tempt for BEEF cul­tures produci­ng acetate demonstrated the usability of KBase for BES. This research was a bottom-up study which mapped ex­isting genomes onto existing BEEF consor­tia. The same tool can also be em­ployed in a top-down ap­proach, starting with the desired fuel to find the re­quired or­ganisms. Some possi­ble BEEF organisms are the following.

Possible pathways for BEEF production involving Clostridium, 3, or heterotrophic phototrophs, 7, further processing by yeasts

Yeasts are among the microorganisms with the greatest potential for liquid biofuel production. Baker’s yeast, (Saccha­romyces cerevisiae) is the most promi­nent exam­ple. While known for ethanol fermentat­ion, yeasts also produce fusel oils such as bu­tane, phenyl, and amyl derivate aldehy­des and alco­hols. Unlike ethanol, which is formed via sugar fer­mentation, fusel oil is syn­thesized in branched-off amino acid pathways followed by alde­hyde reduction. Many en­zymes involved in the re­duction of aldehydes have been identified, with al­cohol dehydro­genases be­ing the most commonly ob­served. The corre­sponding reduc­tion reactions require reduced NADH⁠ but it is not known whether H2 pro­duced on cathodes of BES can be in­volved.
Clostridia, for example Clostridium acetobutylicum and C. carboxidivo­rans, can pro­duce alcohols like butanol, isopropanol, hexanol, and ketones like acetone from complex sub­strates (starch, whey, cel­lulose, etc. ) or from syngas. Clostridial me­tabolism has been clarified some time ago and is dif­ferent from yeast. It does not necessar­ily require com­plex precursors for NAD+ reduction and it was shown that H2, CO, and cath­odes can donate elec­trons for alcohol production. CO2 and H2 were used in a GMO clostridium to produce high titers of isobu­tanol. Typi­cal representa­tives for acetate produc­tion from CO2 and H2 are C. ljungdahlii, C. aceticum, and Butyribac­terium methy­lotrophicum. Sporo­musa sphaeroides pro­duces acetate in BES. Clostridia also dominated mixed cul­ture BESs converting CO2 to butyrate. They are therefore prime targets for low cost biofuel production. Alcohols in clostridia are produced from acetyl-CoA. This reaction is re­versible, al­lowing ac­etate to serve as substrate for biofuel production with extra­cellular en­ergy sup­ply. Then, en­ergy con­servation, ATP syn­thesis that is, can be achieved from ethanol electron bifurca­tion or H2 oxida­tion via respi­ration. While pos­sible in anaero­bic clostridia, it is hitherto unknown whether elec­tron bifurca­tion or res­piration are linked to alcohols or ke­tone synthesis.
Phototrophs like Botryococcus produce C1+ biofuels as well. They synthesize a number of different hydro­carbons including high value alkanes and alkenes as well as terpenes. However, high titers were achieved by only means of ge­netic engineering, which is economically not feasible in many countries due to regulatory constrains. Moreover, aldehyde dehy­dration/deformylation to alkanes or alkenes requires molecular oxygen to be present. Also the olefin path­way of Syne­chococcus depends on molecular oxygen with the cytochrome P450 involved in fatty acid de­carboxylation. The presence of molecular oxygen affects BES performance due to immediate product degrada­tion and unwanted cathodic oxygen reduction. In contrast, our own preliminary experi­ments (see title photo) and a corrosion experi­ment show that algae can live in the dark using electrons from a cath­ode. While the en­zymes in­volved in the production of some algal biofuels are known (such as olefin and alde­hyde de­formylation), it is not known whether these pathways are connected to H2 utilization (perhaps via ferredox­ins). Such a con­nection would be a promising indicator for the possibility of growing hydrocar­bon produc­ing cyanobacteria on cathodes of BES and should be examined in future research.
At Frontis Energy we believe that a number of other microorganisms show potential for BEEF production and these deserve further investi­gation. To avoid GMOs, BES compatible co-cultures must be identified via in silico meta­bolic reconstruc­tion from existing databases. Possible inter-species intermediates are unknown but are prerequisite for suc­cessful BES operation. Finally, a techno-economical assessment of BEEF pro­duction, with and with­out car­bon taxes, and compared with chemical methods, will direct future research.

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Alternating catholyte flow improves microbial electrosynthesis start-up

Microbial electrolysis is a technology that uses living microorganisms as electro-catalysts in electrolysis cells. The technology can be used for wastewater treatment. Earlier, we proposed that microbial electrolysis be used to decentralize wastewater treatment and biogas production. Since this is a process that converts CO2 into organic compounds using electricity it can also be used for CO2 valorization. Besides methane, such electrolysis cells produce compounds such as acetic acid (vinegar), caproic acid, and others. It is then called microbial electrosynthesis.

However, the main problem with microbial electrolysis and electrosynthesis is the long start-up time. The start-up time is the time required for the microorganisms to form a biofilm on the electrode surface and to start producing the desired products. It can range from several weeks to several months, depending on the operating conditions and the type of microorganisms. This long start-up time limits the feasibility and the scalability of microbial electrosynthesis, as well as its economic and environmental benefits.

Now, scientists of the Wageningen University in the Netherlands presented new research, which aimed to reduce the start-up time of microbial electrosynthesis. By using a novel technique that involves alternating the direction of the catholyte flow through a three-dimensional electrode they were able to reduce the startup time to only ten days. They hypothesized that this technique enhances mass transfer and biofilm formation, and thus accelerates the CO2 reduction and the product formation. This was a start-up time reduction of 50%, compared to a conventional flow-through electrode.

 

The alternating electrolyte flow also reduced the power consumption to 136 kWh per kg of hydrogen. After 60 days, the local hydrogen concentration at the cathode was at a maximum of 600 μM, which indicates a better mass transport and thus a more active biofilm. The researchers speculated that the alternating catholyte flow improved mass transport, because the hydrogen could be better distributed over the cathode layers. In addition, the researchers think that alternating the flow refreshed potential “dead zones” in the cathode chamber.

The pH in the catholyte was 5.8–6.8 and in optimal range for electrosynthetic microorganisms. Production of short and medium chain fatty acids was linked to the presence of microorganisms identified as Peptococcaceae and Clostridium sensu stricto 12 species. Hydrogenotrophic methanogenesis was also observed and was linked to Methanobrevibacter. The latter is a typical constituent of microbial electrolysis cells that use higher intermediate hydrogen concentrations for electrosynthesis at the cathode.

However, there are limitations of the technique, such as the energy efficiency, the product selectivity, and the scalability of microbial electrosynthesis. Such limitations are typical for bench top experiments. We are therefore looking forward to see an industrial application of this new method.

 

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Trace metals accelerate hydrogen evolution reaction of biocathodes in microbial electrolysis cells

It has been known that microbial biofilms on biocathodes improve the productions rates of hydrogen evolution reaction (HER). This is the process of producing hydrogen gas from water using electricity. The hydrogen evolution was even accelerated when the biofilm colonizing a biocathode was killed. Different types of bacteria, such as exoelectrogenic (Geobacter sulfurreducens), non-exoelectrogenic (Escherichia coli), and a hydrogenotrophic methanogen (Methanosarcina barkeri) accomplished the feat but Geobacter was the fastest. Even cell debris and metalloproteins catalyzed HER. Therefore, living cells are not required for enhanced HER, and biocathodes could be a cheap and environmentally friendly alternative to precious metal catalysts. While the authors back then speculated on the role of metalloproteins, a new publication in Electrochimica Acta by researchers of Wageningen University shows that indeed trace metals in the growth medium are responsible for the observed rate acceleration.

The authors used a mixture of metal compounds present in the microbial medium such as cobalt, copper, iron, manganese, molybdenum, nickel and zinc salts as well as the metal chelating agent ethylenediaminetetraacetic acid (EDTA) as the catalyst for the HER under microbial compatible conditions (near-neutral pH, mesophilic temperature, aquous electrolyte).

They performed a series of experiments to investigate the effect of different parameters on the catalytic activity and stability of the trace metal mix medium. These parameters included the concentration of the metal compounds, the presence or absence of EDTA, the type of electrode material, and the type of electrolyte. Various techniques to measure the cathodic current, the hydrogen production rate, the overpotential, and the exchange current density of the HER were used.

The results show that the trace metal mix medium increased the cathodic current and the electron recovery into hydrogen significantly, and that copper and molybdenum were the most active compounds in the mix. This is surprising because the previous publication found mostly cobalt and iron compounds on the surface of the biocathodes. Both of which are good hydrogen catalysts as well, whereas molybdenum sulfide for example, did not increase production rates in methanogenic microbial electrolysis cells. HER is the rate determining reaction in methanogenic electrolysis cells because it is the intermediate:

4 H2 + CO2 → CH4 + 2 H2O

The results also showed that removing EDTA from the mix improved the catalyst performance further, as EDTA acted as a complexing (chelating) agent that reduced the availability of metal ions for HER. The results also showed that carbon-based electrodes were more suitable than metal-based electrodes for HER, possibly because they have a higher surface area. This is an interesting result because it was previously thought that the mechanism behind the better performance of carbon electrodes was the microbial preference to adhere to carbon than to metal surfaces. The results also showed that using microbial growth medium as the electrolyte did not affect the catalyst performance significantly, as compared to using phosphate buffer solution.

The authors concluded that their method was a simple, cheap, and environmentally friendly way to prepare effective catalysts for HER using trace metals from microbial growth media. They suggested that these catalysts could be integrated in biological systems for in situ hydrogen production in bio-electrochemical and fermentation processes. Indeed, it is inevitable not to use trace metals in microbial electrolysis cells as they are essential to sustain growth.

Both articles demonstrate that trace metals can play an important role in the HER, and that they can be derived from biological sources. However, they also have some limitations and challenges, such as the stability, selectivity, and scalability of the catalysts. Therefore, further research is needed to optimize the performance and applicability of trace metal-based catalysts for HER.

(Image: US National Science Foundation)

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Decentralized waste energy systems produce biogas where it is needed

Among others, the current European energy crisis was caused by a surge in demand after the pandemic, the embargo on Russia, the reluctance of investors to finance fossil energy projects and the throttling of production by the OPEC countries. In this complex situation, European countries are forced to develop alternatives and renewable energy sources. At the same time, however, natural gas is difficult to replace in many industries. One exception is the food and beverage industry, which sits enormous untapped resources of biogas in their wastewater.

Wastewater is a resource of which 380 billion m³ are produced worldwide. It contains valuable nutrients and energy. Global production is projected to increase by 51% by 2050. Wastewater treatment consumes about 3-4% of the energy generated globally. The full reeovery of the energy that is contained in this wastewater would completely offset the energy consumption of its treatment and in many cases even produce a surplus. In addition, the entire global water treatment is estimated to account for up to 5% of man-made CO2 production. Unfortunately, many businesses and municipalities do not invest in complex and expensive wastewater treatment technologies and continue to waste this valuable resource. The European Biogas Association estimates that by 2050, a maximum of 65% of gas requirements (~167 billion m³) could be covered by biogas.

Europe is the largest cheese maker in the world. More than 9 million tons of cheese are produced annually. With every ton of cheese, 9 m³ of cheese whey remain. Despite its high nutritional value, whey is often treated like wastewater for various reasons. Yet, the very high organic load in the whey makes it difficult to treat. Wasted whey can also be used for biogas production. In addition to whey, regular wastewater is also produced by cheese makers. For example, a medium-sized cheese factory pays 1.5 million euros a year for its waste water. Reducing these costs by producing biogas would turn dairy industry wastewater into a valuable resource.

This situation is similar in many other food and beverage sectors such as breweries, distilleries, winemakers, bakeries etc. All of these sectors have high energy requirements. Renewable electrical energy cannot meet this need. The market for wastewater treatment in Europe and the US is around 12 billion euros.

Traditional wastewater treatment is a cascaded process including aeration and anaerobic sludge digestion followed by incineration. These methods often consume more than 70% of the energy in a wastewater treatment plant. If contaminants such as high-energy total organic carbon or ammonia were converted into biogas before the process, at least 80% of the energy needed for wastewater treatment could be saved. It is absurd that this energy is removed from the wastewater using even more energy.

An ever-increasing number of sewage treatment plants already recover the resources contained in their wastewater, apart from the water itself. The oldest recivered products are biogas and fertilizers made from sewage sludge. Due to its heavy metal content such as copper and mercury, sewage sludge is no longer used as fertilizer but incinerated.

Biogas is particularly popular in Europe as the produced volumes and prices are high enough to compete with natural gas. Biogas is also a green alternative to natural gas as no additional CO2 is emitted. (Hence, it is often called Renewable Natural Gas in North America.) A disadvantage of classic biogas is the CO2 and sulfide content. Another disadvantage is that anaerobic digestion is the terminal treatment step, wasting valuable wastewater resources in the preceding treatment. Finally, the size and complexity of current digestion requires significant commitment from users when it comes to capital expenditures. Most food manufacturers prefer to focus on making food rather than cleaning their wastewater.

Novel high-performance biogas reactors solve these problems through miniaturization. A 20-fold size reduction is achieved compared to conventional systems. The new technology used was developed in Japan in the early 1990s and is called microbial electrolysis. The electrolysis of wastewater is catalyzed by electroactive microorganisms on the anode (the positive electrode). The reaction products are CO2 (from organic matter) and nitrogen gas (N2 from ammonia).

Principle of a microbial electrolysis reactor. On the left anode, the organic material is oxidized to CO2. The free electrons are absorbed by the anode and transported to the cathode. Hydrogen gas (H2) is released there. CO2 and hydrogen form methane, the final microbial reaction product.

At the same time, hydrogen gas (H2) is generated at the cathode (the negative electrode). This hydrogen reacts with CO2 to form methane. The final methanation step completes the biocatalytic treatment of the wastewater. Gas grid injection is one possible use. But for cheese makers, the gas would be used on site to generate electricity and/or heat.

The reaction is accelerated using an applied voltage and is based on the laws of thermodynamics. As a result, the reactor volume can be reduced. The size reduction has several advantages. First, it makes biogas accessible in markets where it was previously not possible due to the high investment costs. Second, it enables higher throughput at a lower cost. Smaller units are mobile and can be shared, moved or rented. After all, food manufacturers want to do what they do best, which is to make food.

 

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Nanostructured membranes improve the gas separation of carbon dioxide

To reduce greenhouse gas emissions, various technologies are in development requiring the separation of mixed gases, such as  CO2 and methane or CO2 and nitrogen gas (CO2/CH4 and CO2/N2). Compared to other separation technologies, polymer membranes are  good candidates for industrial use. This is due to their low operating costs, high energy efficiency and simple scalability.

The gas permeability and selectivity, as well as the cost of these polymer membranes are the crucial criteria for their industrial use. These criteria are influenced by molecular order processes during polymerization at nano- and micrometer levels. However, the processes regulating the molecular order of most common membranes do not occur on these levels. Hence, there is little control over them during manufacturing. Not much is known about materials with self organizing properties and their influence on molecular order and gas separation.

Chemists at the Technical University of Eindhoven in the Netherlands examined the effects of the layer distance within the membrane and its halogenation on the gastrunge and published their results in the MDPI Membranes journal. They focused on the separation of helium, CO2 and nitrogen. The researchers used liquid crystal membranes for their investigation. Liquid crystal molecules can align in various nanostructures. These structures vary depending on the manufacturing process and can therefore be controlled. As a result, liquid crystal membranes are ideal in order to investigate the influence of nanostructures on gas separation.

A frequently used manufacturing method is to commence the self organization of the reactive liquid crystal molecules in a cell with spacers. This helps to better control the membrane thickness and alignment and ultimately control the molecular orientation. The final network of the liquid crystal molecules and their fixation in nanostructures is required to achieve mechanical strength. For example, high ordered crystal membranes (i.e. not liquid crystals) have a lower gas permeability. Nonetheless, they also are characterized by a higher selectivity for helium and CO2 compared to nitrogen.

A lamellar morphology and the flow direction of the gas also have a great influence on selectivity and permeability of the membrane. It is also known that halogen atoms such as chlorine or fluorine improve CO2 permeability and selectivity by affecting both gas solubility and diffusion.

In the presented experiments, all liquid crystal membranes with similar chemical compositions, but different halogenated alkyl chains, were aligned. The CO2 sorption and the entire gas permeation were better if their layers were further apart. The gas solubility itself had no impact. This was confirmed by the increased gas diffusion coefficients, which were also determined in the experiments.

Bulky halogens had only limited influence on gas permeability and selectivity. The CO2 permeability of all halogenated liquid crystal membranes increased due to a slightly higher CO2 solubility and diffusion coefficients, which led to improved selectivity for CO2. The layer distance in particular was a crucial factor that directly influenced the diffusion coefficient. The researchers recommended that future investigations should focus on improving separation performance, for example by reducing the membrane thickness.

At Frontis Energy, we are looking forward to a good commercial product that can separate CO2 from gas mixtures, such as biogas, effectively and cheap.

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Transition between double-layer and Faradaic charge storage in porous carbon nano-material

In electrochemical cells, such as fuel cells or electrolyzers, electric double-layer (EDL) formation occurs on their electrode surfaces. These EDL act as both, capacitors and resistors and impact therefore the performance of electrochemical cells. Understanding the structure and dynamics of EDL formation could significantly improve the performance of, electrochemical systems, for example in energy storage and conversion, including supercapacitors, water desalination, sensors and so forth.

On a planar electrode, electrolyte ions and the solvent are adsorbed at the electrode surface. The resulting capacitance depends on charge, solvation state and concentration. Traditionally, the capacitance of electrochemical interfaces can be divided into two types:

  1. Double-layer capacitance: ions are adsorbed based on their charge. Ion adsorption is non-specific.
  2. Faradaic pseudocapacitance: specific ions are adsorbed, for example through chemical interactions the electrode surface. This may involve charge transfer.

The electrode interface in the most energy application-based technology is, however, not planar but porous. Layer materials in such situations have various degrees of electrolyte confinement and thus different capacitive adsorption mechanisms. Understanding electrosorption in such materials requires a refined view of electrochemical capacitance and charge storage.

A team of researchers from the North Carolina State University, the Paul Sabatier University in Toulouse and the Karlsruhe Institute of Technology reported new insights in electrolyte confinement at the non-planar interfaces in the journal Nature Energy.

Electric double-layer at planar electrodes

The degree of ion solvation (the process of reorganizing solvent and solute molecules) at ideal (planar) electrochemical interfaces determines the ions interaction with the electrodes. There are two distinct cases:

  1. Ions are non-specifically adsorbed: this is the case with strong ion solvation. The electrode’s interactions are primarily electrostatic. This type of interactions can be considered as the induction – charge is induced but not transferred.
  2. Ions are specifically adsorbed: in this case, ions are not solvated and can undergo specific adsorption and chemical bonding to the electrode. This process can be described as charge transfer reaction between the electrode and the adsorbed ion. However, the charge transfer reaction depends on the bonding between the ion and the electrode. This correlates with the state of ion solvation.  Thus, it can be expected that the ion solvation is crucial for understanding the ion-electrode interactions in a nano-confined environment such as porous materials.

Carbon based EDL capacitor – the confinement effect

There is a great interest for understanding the relationship between the porosity of carbon nano-materials and their specific capacitance.

When electric double-layer formation occurs in a nano-confined micro-environment, the EDL capacitor in porous carbon materials deviates from the classic EDL model on flat interfaces. The degree of the ion solvation under confinement is determined by the pore size in nano-porous materials and by the inter-layer distance in layered materials that is, 2D-layer materials.

Confinement of ions in sub-nanometer pores results in their desolvation, leading to the capacitance increase and deviation from the typical linear behavior on the surface area. During negative polarization of porous carbon materials with the pore sizes <1 nm, a decrease of capacitance  is observed. This is due to the ion selection limiting ion transport.

These insights are important for effectively tailoring carbon pore structures and for increasing their specific capacitance. Since carbon material is not an ideal conductor, it is important to consider its specific electric structure. For graphite materials, the availability of the charge carriers increases during the polarization which leads to increased conductivity.

Unified model of electrochemical charge storage under confinement

Since the electrochemical interface in the most technological application is non-planar, the researchers proposed a detailed evaluation and different concept of electrochemical capacitance on such non-ideal interfaces. The team evaluated electrosorption on 2D surfaces and 3D porous carbon surfaces with a continuous reduction in pore size in a step-by-step approach of increasing complexity.

The example provided relates to the charge storage characteristics of lithium ions (Li+) in the graphene sheets of organic lithium-containing electrolytes depending on the number of graphene layers. In a single graphene layer, the capacitive response is potential independent due to the absence of specific adsorption. However, with an increase of graphene sheets, redox peaks emerged that are associated with the intercalation of desolvated lithium ions. Lithium intercalation is responsible for battery wear. The team’s hypothesis was that the transition of solvated lithium ion adsorption on a single graphene sheet into subsequent intercalation of desolvated lithium ions occurs with a continuous charge storage behavior. There can be a seamless transition based on the increased charge transfer between an electrolyte ion and host associated with the extent of desolvation and confinement.

In the presented research, a unified approach was proposed that involves the continuous transition between double-layer capacitance and Faradaic intercalation under confinement. This approach excludes the traditional “single” view of electrochemical charge storage in nano-materials regarded as purely electrostatic or purely Faradaic phenomenon.

The increasing degree of ion confinement is followed by decreasing degree of ion solvation thus the increase ion-host intercalation. This results in a continuum from EDL formation through transitioning state to Faradaic intercalation, typical for EDLC nanomaterial.

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