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Ammonia electrosynthesis in a palladium membrane flow cell

Fertilizer granules

Ammonia (NH₃) is a crucial raw material for fertilizer production and a potential renewable, carbon-free energy storage solution. It is produced in the Haber-Bosch process using natural gas (CH4). During this process, natural gas is converted into hydrogen (H₂) and CO₂ by steam reforming. The Haber-Bosch process accounts for approximately 1-3% of global CO₂ emissions. This method requires stable energy supply and CAPEX intensive facilities, leading to highly centralized ammonia production. In contrast, alternative electrochemical pathways for ammonia production represent sustainable and decentralized solutions.

Electrochemical ammonia production is not a new process and is based on hydrogen electrolysis. In a subsequent step, hydrogen is used for catalytic nitrogen reduction. Experimentally, lithium and calcium have been used as electrocatalysts. Ammonia has been produced in continuous flow cells with efficiencies of up to 76%, as well as in other electrochemical cells. However, stable ammonia production in flow cells requires dry and purified hydrogen.

The primary issue with moist hydrogen is the excessive formation of lithium hydroxide (LiOH):

2 Li + 2 H₂O → 2 LiOH + H₂

However, water electrolysis could be completely eliminated if the protons (H+) generated from water oxidation were directly supplied to the lithium-coated cathode. This would further simplify systems and lower investment costs.

Researchers at Imperial College London followed exactly that approach. They coupled continuous water oxidation directly to lithium-mediated nitrogen reduction under non-aqueous conditions in a two-chamber flow cell. They recently published their results in the journal ACS Energy Letters.

The coupling was achieved through an electrically isolated, hydrogen-permeable palladium membrane between the chambers. On the anodic side (aqueous), water was oxidized at an iridium oxide-coated titanium anode to produce protons, meaning adsorbed H. This form of hydrogen permeated the palladium membrane. It then entered the dry, non-aqueous cathodic chamber, where N₂ was reduced on lithium.

Schematic palladium membrane ammonia synthesis

The palladium membrane was not integrated into the external circuit during nitrogen reduction. It simultaneously served as both a proton source and sink, made possible by its electrical conductivity and hydrogen permeability.

The scientists first validated proton transport through the palladium membrane while preventing water crossover through symmetric cell tests and ¹H-NMR isotopic exchange using water (H₂O) and deuterium oxide (D₂O, heavy water).

Real-time mass spectrometry of D₂O at the anode confirmed that deuterons supplied through the palladium membrane were incorporated into ammonia (ND₂H). This demonstrates that the protons in NH₃ originated from water oxidation and not solely from the ethanol used as well. It was evidence for linear charge transfer while maintaining negligible water transport.

As a control, an experiment was conducted using a Nafion™ membrane to demonstrate that membranes allowing water crossover prevented lithium-mediated ammonia synthesis. Nafion™ permits proton transfer while being permeable to water.

The researchers showed that the electrical conductivity of the palladium membrane enabled it to operate simultaneously as both an anode and a cathode. This allowed for continuous conversion of nitrogen and water into ammonia without producing molecular hydrogen as an intermediate. The Nafion™ control proved that the transport of protons while preventing water crossover allowed for lithium-mediated ammonia synthesis.

The necessity for pre-hydration of the membrane and the gradual increase in membrane potential during pulsed operation indicated that the kinetics of hydrogen transfer and membrane stability were key factors for performance. This was because the system was optimized for the neutral aqueous electrolyte with isotopic labeling. The researchers proposed ways to improve efficiency in their article, including the exploration of alternative hydrogen-permeable metals and alloys.

The presented membrane could find applications beyond ammonia synthesis, in other electrochemical transformations where anhydrous conditions and controlled proton release are required. These include CO₂ reduction and non-aqueous redox flow batteries.

For further research, the authors suggested:

  • Increase proton flow and reduce membrane transition resistance,
  • Test alternative hydrogen-permeable metals or alloys to reduce costs, and
  • Conduct pulse and idle protocols to monitor lithium loss.

At Frontis Energy, we are eager to see how individual monolithic palladium membranes will enter in the market. Continuous ammonia electrosynthesis represents a conceptual advancement towards simpler, more robust green fertilizer production and energy storage.

Ye et al. 2026, Continuous ammonia electrosynthesis from nitrogen and water in a monolithic Pd membrane-based flow cell, ACS Energy Letters, DOI: 10.1021/acsenergylett.5c03617

Image: Pixabay

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Polyelectrolyte coatings for ion-exchange membranes in electrodialysis

Reverse electrodialysis water purification

Ion exchange membranes are key components for various electrochemical technologies in water treatment and energy storage, such as electrodialysis, membrane electrolysis, and flow batteries. These membranes are characterized by a high concentration of charged groups, which can be either cationic (positively charged) or anionic (negatively charged). The function of an ion exchange membrane is to facilitate the transport of counterions while limiting the loss of water and co-ions.

The efficiency of cation exchange membranes is affected by unwanted co-ion and water transport. The transport of hydroxide ions (OH) through cation exchange membranes is of particular interest. Depending on the application, cation exchange membranes are designed either to selectively facilitate hydroxide transport or to minimize hydroxide loss. Therefore, improved ion exchange membranes must support such additional functionalities.

Researchers at Wageningen University have characterized ion exchange and water transport through both coated and uncoated cation exchange membranes. The scientists published their findings in the Journal of Membrane Science. In their study, they examined cation exchange membrane coating with polyelectrolytes made of polyallylamine and polystyrene sulfonic acid.

The researchers coated one side of commercial cation exchange membranes with double layers of these two polymers. They then studied ion and water transport in diffusion dialysis and electrodialysis. Diffusion dialysis involves passive ion transport driven by concentration gradients, while in electrodialysis, ion transport occurs actively and is powered by an applied current.

The coatings were evaluated for their selectivity for monovalent and divalent ions. This selectivity affects hydroxide transport and water permeability. Both are key factors for the efficiency of bipolar membrane electrodialysis, where solutions containing multivalent cations such as magnesium and calcium are treated.

Magnesium and calcium transport was significantly limited by the coatings, while sodium ion transport remained largely unaffected. This selectivity was attributed to the Donnan exclusion mechanism and differences in hydration shells, as multivalent ions have a higher resistance within the cation exchange membrane.

Orientation is crucial in this context. Coating alignment affected performance. Resistance increased in the direction of multivalent ion flow, which reduced the flow of magnesium ions. This finding is impotant for the design of devices for bipolar membrane electrodialysis.

Surprisingly, the coatings did not reduce water crossover. Denser layers remained the bottleneck. The hydroxide flow was somewhat higher in coated membranes exposed to extreme pH values. This was likely due to structural changes during the coating process.

The combination of a low-water-content cation exchange membrane with a coating could enable the direct use of untreated salt solutions in bipolar membrane electrodialysis. This would reduce pretreatment costs and improve sustainability. The Fuji CEM-12 proved to be a promising candidate for future designs with coatings.

Salt diffusion through uncoated cation exchange membranes was mainly determined by the type of anion, such as chloride, sulfate, or hydroxide. In addition, membrane properties, including water content and ionic charge density, had a significant influence. The ionic charge density determined the anion distribution within the cation exchange membranes.

In summary, the researchers coated various commercial cation exchange membranes multiple times on one side with polyelectrolytes. For uncoated cation exchange membranes, water permeability correlated well with  ionic membrane resistance. This correlation was due to both parameters being dependent on the water content of the membrane. Moreover, permeability for co-ions increased with a higher volume fraction of water in the membranes.

Osmotic water transport in cation exchange membranes was not affected by the multiple layers of polyallylamine and polystyrene sulfonic acid. The researchers recommended single layer coating of low-water-content cation exchange membranes to minimize the transport of hydroxides and problematic multivalent cations.

This work demonstrates that surface modification using polyelectrolyte layers can enhance the functionality of conventional membranes without significant trade-offs. Water transport remained a challenge but the ability to block multivalent ions while maintaining conductivity for sodium ions represented a major step toward more efficient and cost-effective dialysis systems.

At Frontis Energy, we are excited about the future application of multilayered membranes on an industrial scale.

Elozeiri et al. 2026, Water and co-ion transport across ion-exchange membranes coated with PAH/PSS polyelectrolyte multilayer in electrodialysis and diffusion dialysis, Journal of Membrane Science,741, 125072, DOI: 10.1016/j.memsci.2025.125072

Image: Getty Images

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Transforming water systems with scalable membrane solutions

Fresh water from a faucet

In a world increasingly defined by the need for cleaner processes, sustainable production, and advanced materials, membrane technology has emerged as a key enabler across multiple industries from water purification and energy generation to chemical separation and bioprocessing. Its high selectivity, compact footprint, and low energy requirements make it indispensable in meeting both environmental and performance demands.

At the heart of membrane fabrication lies a well-established method known as non-solvent-induced phase separation. This technique involves casting a polymer solution into a thin layer and exposing it to a non-solvent, typically through immersion or vapor contact, which triggers phase separation, forming a porous matrix with fine-tuned filtration properties. Due to its simplicity and scalability, this method has become a mainstay in industrial membrane production, offering reliable performance across many applications.­

However, as industries demand more specialized and high-efficiency membranes, researchers are continuously pushing the boundaries of conventional fabrication techniques. One of the most promising advancements is the spray-modified non-solvent-induced phase separation method, which swaps immersion for targeted non-solvent spraying. This subtle yet powerful modification enables patterned surface architectures, improved permeability, and reduced fouling, all while maintaining the advantages of scalable continuous production. Such innovation is instrumental in tailoring membranes to meet the complex needs of modern filtration systems.

Building on this progress, a recent study conducted by the Catholic University Leuven in Belgium successfully adapted the spray-modified non-solvent-induced phase separation technique to a roll-to-roll, 12-inch pilot-scale platform. This represents a meaningful advancement from laboratory concept to industrial feasibility. The findings were recently published in the Membranes. Through strategic variations in polymer concentration, molecular weight, and the inclusion of hydrophilic additives such as polyethylene glycol and polyvinylpyrrolidone, researchers fabricated defect-free, uniformly patterned polysulfone ultrafiltration membranes with remarkable performance gains. Notably, these membranes delivered up to 350% higher water flux compared to traditional flat membranes, attributed to their deep surface patterns—reaching 825 µm—and a porous, finger-like internal structure that enhances throughput without sacrificing rejection efficiency.

Among the additives tested, polyethylene glycol emerged as the standout, yielding membranes with high pure water permeance (over 1000 Liters/m²/hour/bar) and consistent protein rejection levels (around 90%). These membranes also demonstrated excellent structural fidelity and homogeneity, which are critical for ensuring long-term durability and process reliability. The study further identified operational parameters, such as optimal casting speed, non-solvent spray rate, and solution viscosity control, as essential contributors to reproducible membrane quality and process scalability.

This leap from bench to pilot scale carries profound industrial implications. The ability to continuously produce high-flux, anti-fouling membranes with precise structural characteristics offers industries a robust and scalable filtration solution. Applications span from municipal and industrial wastewater treatment to biopharmaceutical production and food processing—sectors where membrane performance can directly influence both environmental outcomes and operational costs.

In essence, the optimized spray-modified non-solvent-induced phase separation approach does more than enhance membrane metrics; it embodies the transition from research novelty to commercial readiness. By bridging the gap between design and deployment, this work lays a foundational blueprint for mass-producing advanced membranes that are not only efficient, but also economically and environmentally viable. It is a compelling example of how thoughtful engineering and process innovation can move technologies from promising prototypes to real-world solutions, thus shaping the future of filtration in a world that urgently needs it.

Frontis Energy envisions a world transformed by sustainable membrane innovations, where clean water, resource efficiency, and resilient infrastructure are accessible to all.

Ilyas, et al., 2025, Pilot-scale polysulfone ultrafiltrationpPatterned membranes: phase-inversion parametric optimization on a roll-to-roll casting system, Membranes 15, 8, 228, DOI: 10.3390/membranes15080228

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Sulfonated clay and carbon nanotubes Nafion™-based proton exchange membranes

Toyota fuel cell concept car

The demand for sustainable energy has accelerated the development of electrochemical systems for energy conversion. This includes, in particular, proton exchange membrane fuel cells (PEMFCs). PEMFCs offer numerous advantages, including high energy density, low operating temperatures, fast start-up times, and compact design. These characteristics make them especially suitable for mobile and decentralized energy applications. The development of high-performance proton exchange membranes is crucial for the advancement of fuel cell technology, particularly under demanding operating conditions.

The central component, the proton exchange membrane, is characterized by high proton conductivity, excellent chemical and physical stability, low gas permeability, and adequate water uptake under a variety of conditions. Nafion™, a perfluorosulfonic acid (PFSA) ionomer, is considered the gold standard for proton exchange membranes due to its outstanding proton conductivity and chemical resistance.

However, its performance degrades significantly at elevated temperatures (>80 °C) and low relative humidity due to excessive water loss. These limitations restrict its applicability in next-generation high-temperature fuel cells. To overcome these limitations, extensive efforts have been made to develop PFSA-based composite membranes. For this purpose, inorganic or organic fillers such as silica, metal oxides, and carbon-based nanomaterials have been used. These additives aim to improve water retention, mechanical strength, and thermal stability.

Italian researchers from the University of Calabria have developed Nafion™ membranes reinforced with sulfonated clay and carbon nanotubes to address issues with water retention and proton transport. They recently published their results in the journal Materials for Renewable and Sustainable Energy. The hybrid fillers created a synergistic effect. The clay improved the hydrophilic properties, while carbon nanotubes enhanced the structural integrity and conductivity.

In tests with hydrogen fuel cells at 120 °C and 20% relative humidity—conditions that typically severely impair normal PFSA membranes—the new composition achieved a peak power of 443 mW/cm². This was four times that of Nafion™ membranes. This breakthrough suggested that integrating nanofillers could yield further improvements in durability and efficiency of proton exchange membranes. At the same time, the experiments paved the way for robust fuel cells in the automotive and stationary energy sectors, where such performance improvements are particularly needed.

The incorporation of sulfonated clay and carbon nanotubes not only improved the ion exchange capacity and hydrolytic stability but also critically modulated the water dynamics. The result was superior water retention and sustained proton diffusion, particularly at elevated temperatures. The significantly higher proton conductivity under low humidity conditions was a crucial factor for the operation of high-temperature fuel cells in the study presented.

This study successfully demonstrated the significant potential of sulfonated clay and carbon nanotubes to enhance the performance and durability of Nafion-based proton exchange membranes for fuel cell applications. The incorporation of the additives also increased the structural integrity of the membrane. Dynamic mechanical analysis showed a significant reinforcement effect from the inclusion of the additives, with a consistent increase in storage modulus and a shift of the glass transition temperature to higher temperatures. For the improved membrane, the glass transition temperature increased from 120 °C for conventional Nafion to approximately 150 °C.

Moreover, the nanocomposite membrane exhibited a remarkable conductivity of 42.3 mS/cm at low humidity. This represented a significant improvement compared to pure Nafion™.

In summary, the nanohybrid membrane consistently overcame significant limitations of conventional PFSA membranes, particularly their susceptibility to drying out and mechanical degradation under demanding operating conditions.

At Frontis Energy, we are convinced that the synergistic interplay of enhanced proton transport pathways, improved water retention, and superior thermomechanical stability makes this composite membrane a promising candidate for robust and efficient next-generation fuel cells.

Nicotera, et al. 2025 Enhanced electrochemical performance and thermomechanical stability of nafion/sulfonated clay-carbon nanotube nanocomposite membranes for high-performance fuel cells under challenging conditions. Materials for Renewable and Sustainable Energy 14, 48, DOI: 10.1007/s40243-025-00325-7.

Image: Pixabay

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Advancing wastewater sustainability: Nafion-powered ammonium recovery

Wastewater treatment plant Bern

DOI: 10.13140/RG.2.2.24268.68488

With global population growth and the resulting increase in environmental stress, the need for sustainable wastewater treatment is becoming ever more urgent. Traditional methods focus on removing pollutants but often overlook the opportunity to recover valuable resources. One such resource is ammonium. This nitrogen-containing molecule promotes growth and is a key component of fertilizers. When mishandled, such as through over-fertilization, ammonium becomes one of the main contributors to nitrogen pollution.

A promising solution lies in bioelectrical systems. This umbrella term refers to innovative technologies that not only purify wastewater but also recover resources like ammonium. At the same time, bioelectrical systems generate clean energy such as electricity or biogas. The technology is based on galvanic cells, where the two cell chambers are often separated by a membrane. High-performance cation exchange membranes enable precise ion transport and system stability. The premium product among cation exchange membranes is Nafion, such as our Nafion 115 membrane.

At Frontis Energy, we have demonstrated that bioelectrochemical systems can remove ammonium from wastewater, offering an energy-efficient alternative to the energy-intensive Haber-Bosch process. To validate this concept, we developed microbiological electrolysis cells populated with microorganisms from oxygen-deprived marine sediments off the coast of Namibia. These sediments are naturally rich in ammonia and low in organic carbon, ideal conditions for microbes capable of anaerobic ammonium oxidation. For comparison, we also used conventional municipal wastewater to populate the electrodes.

Maintaining anoxic conditions was crucial to avoid nitrification, a process that transfers electrons directly to oxygen, bypassing the anode and resulting in energy loss and reduced hydrogen production. Instead, we regulated the anode potential between +150 mV and +550 mV, well below the redox potential required for water oxidation (+820 mV). This configuration enabled the oxidation of ammonium to nitrogen gas (N₂) at the anode, while hydrogen (H₂) or methane gas was produced at the cathode.

Central to this process is Nafion 115, a membrane made of perfluorosulfonic acid polymers (PFSA polymers). Its exceptional proton conductivity, chemical resistance, and mechanical robustness make it ideal for demanding wastewater environments. Nafion 115 acts like a selective gate, allowing ammonium ions (NH₄⁺) to migrate from the anode to the cathode while blocking competing ions and maintaining anoxic conditions. This selective transport, driven by electric field gradients and concentration differences, ensures efficient nutrient recovery and stable performance of the bioelectrical system.

A practical validation of this technology comes from our earlier report, in which researchers developed a two-chamber, anoxic bioelectrical reactor that continuously removed ammonium at a rate of about 5 g/m³/day. Their system converted over 97% of the ammonium directly into nitrogen gas. This transformation occurred without the formation of harmful byproducts like nitrite or NOx gases. Particularly impressive was the energy consumption, just 0.13 kWh per kilogram of nitrogen removed. That is a 35-fold reduction compared to conventional aeration, which typically requires around 5 kWh/kg.

These results highlight the transformative potential of bioelectrical systems. As mentioned earlier, significant energy is used to remove nitrogen from wastewater, only to make it available again via the Haber-Bosch process, accounting for 1–2% of global energy consumption. Bioelectrical systems offer a circular alternative: by coupling ammonium oxidation with hydrogen production, wastewater treatment plants could become net energy producers. The generated hydrogen and biogas can be used directly for electricity generation and ultimately to reduce greenhouse gas emissions.

With the right biofilms, well-controlled electrode potentials, and robust membranes like Nafion 115, ammonium can serve as a clean, resource-efficient alternative to water electrolysis. This underscores the potential of bioelectrical systems to build a circular water economy, where waste is treated as a resource.

This technology reflects Frontis Energy’s commitment to promoting clean, efficient, and circular solutions that turn ecological challenges into sustainable opportunities.

Siegert and Tan, 2019, Electric stimulation of ammonotrophic methanogenesis, Frontiers in Energy Research 7:17, DOI: 10.3389/fenrg.2019.00017

Image: Wastewater treatment plant Bern

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Stability of anion exchange membranes for electrolysis

Electrolyzer in China

DOI: 10.13140/RG.2.2.18396.65927

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, et al., 2025, Photochemical methods to study the radical-induced degradation of anion-exchange membranes. Membranes, 15, 305. DOI: 10.3390/membranes15100305

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Complex interaction between nitrogen emissions and global warming

Nitrogen compounds are essential for life on Earth. The use of fossil fuels and artificial fertilizers have led to a significant increase in reactive nitrogen available to the biosphere. This increase has far-reaching and well-researched effects on ecosystems, biodiversity and health. Air pollution can lead to premature deaths and nitrogen compounds may play an important role. Previous studies have only inadequately researched the effects of reactive nitrogen on the global climate system since industrialization.

A new study by the Max Planck Institute for Biogeochemistry in Jena is now closing this knowledge gap. The researchers modeled the terrestrial biosphere and global atmospheric distribution of nitrogen. They then combined the results with findings from atmospheric chemistry. This combination enabled them to come up with a new and comprehensive assessment of the climate impact of anthropogenic reactive nitrogen. The results were recently published in the renown scientific journal Nature.

Man emits a number of nitrogen compounds. Some of these, such as nitrous oxide (N2O, laughing gas), are greenhouse gases. Others, such as fine dust particles that reflect solar radiation, have a cooling effect on the climate. These effects were also described in the present the study. Significant warming due to increasing concentrations of the greenhouse gases nitrous oxide  and ozone (O3) were reported. In contrast, several processes that contribute to the cooling effect of nitrogen were also described. In addition to particulate matter, these processes include chemical reactions that lead to a shorter residence time of the greenhouse gas methane in the atmosphere, as well as an increased uptake of carbon dioxide (CO2) by the terrestrial biosphere due to the fertilizing effect of nitrogen.

If all global warming and cooling processes caused by the reactive nitrogen are combined, a net cooling effect is the result. This new result suggests that nitrogen emissions have compensated for about one sixth of the global warming to date caused by the increase in CO2 over the industrial period.

The new results are also important for future strategies for nitrogen regulation in the context of climate protection policy. In most scenarios, nitrous oxide emissions from farming remained high due to the continued use of fertilizers in agriculture and thus the warming influence of this gas. Scenarios that are compatible with the climate goals of the Paris Agreement require an end to CO2 emissions from fossil fuels. This also reduces the release of reactive nitrogen from fossil sources and its harmful effects on health and biodiversity, but also eliminates its cooling effect. The researchers therefore expect a slightly warming contribution from total nitrogen for these climate protection scenarios, but this is far less than the warming from the unchecked consumption of fossil fuels.

The study underlines the urgency of finally stopping emissions from fossil fuels and using fertilizers more specifically. This would not only slow down global warming, but also reduce the burden of harmful ozone and particulate matter concentrations for all of us in rural areas and in cities. New technologies are needed to reduce harmful nitrogen emissions while making good use of beneficial nitrogen. At Frontis Energy we have developed such a technology. Our patented process removes ammonia from wastewater while producing useful carbon neutral biogas. Using this technology, harmful nitrous oxide emissions can be reduced.

Picture: Smog over Guangzhou, China

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Terrestrial vegetation and soils absorb up to 30% more CO2

A significant part of the scientific community is investigating in impact of GHG emissions, and in particular CO2, on our past, present, and future climate. To model our future climate, researchers use CO2 emissions to estimate the future climate of our planet. They predict how much CO2 industry and households can emit to remain within the set 1.5°C target. The central question therefore is: How much of the emitted CO2 actually remains in the atmosphere? How much is metabolized or otherwise bound?

It seems the models have so far underestimated the capacity of biomass to incorporate CO2. That is because the models have now received a major upgrade from an analysis of radiocarbon data from nuclear bomb testing in the 1960s, which suggests that terrestrial ecosystems are capable of absorbing more CO2 than previously thought. Does that mean that the earth copes with more emissions?

Researchers  at the Worcester Polytechnic Institute in Massachusetts found that plants are currently absorbing 80 million tons of CO2 each year. They published their finding in a recent article in the renown magazine Science. That is 30% more than previously assumed.

The initial idea was to take a closer look at the remnants of the nuclear tests in the 1950s and 1960s. Carbon dioxide molecules are made of carbon and oxygen. The radioactive substances that atomic bombs have left all over the world is also a radioactive carbon (14C). Like ordinary carbon (12C), the radioactive version is a possible component in CO2. After the atomic bombing tests, 14C got into the terrestrial biosphere through the photosynthesis of plants along with 12C. So one studies how 14C was enriched, the rates of the CO2 uptake in plants reveal how much carbon is captured.

Animals that feed on plants take in the same CO2 into their organism, as well as fungi and soil bacteria. Through decaying biomass in soil, carbon is then again released into the atmosphere in the form of CO2 and the cycle closes.

However, the question of is how much CO2 from the air goes into the ground and in is bound in biomass long term is anything but trivial. The analyzes of radioactive carbon now show slightly less 14CO2 in the atmosphere shortly after the nuclear tests. That is, plants worldwide would bind 80 gigatons carbon per year. So far, climate researchers assumed that storage performance was 43 to 76 gigatons.

The current assumptions were wrong due to the fact that mainly tree trunks were used for the calculation. Carbon stored in wood has been bound for many decades or centuries. The new study looked at non-wood biomass such as leaves, which also store a large proportion of carbon. Plus, extensive  underground plant biomass received hitherto too little attention. As a rule, underground biomass is comparable to what’s found above ground. In particular, only the woody roots were taken into account, but not the fine rhizosphere which has even more mass and accordingly binds more carbon.

Eighty gigatons are not only significantly more than is used in the common climate change forecasts. It is also twice as much as the annual man-made CO2 emissions (37.2 billion tons).

Unfortunately, this does not mean that there is nothing to worry about. Living creatures also use biomass as a fuel. Almost the same amount of CO₂ is released again when plants lose their leaves in autumn, which then serve soil creatures as a source of food. These natural CO2 emissions from the biosphere have accelerated more since the 1960s.

Overall, photosynthesis can get only 30% of the total man-made CO2 emissions from the atmosphere and can therefore not make up for fossil fuel consumption. With large natural areas available for photosynthesis more CO2 could be extracted from air. In consequence, more and not fewer forests and meadows need to be re-naturalized.

Some climate models are based on wrong assumptions. And yet, the more important carbon storage is not on land, but in the water. CO2 dissolves better there and countless micro-algae in the oceans also carry out photosynthesis. Carbon is very popular as building material for shells. In total, the oceans 16 times more carbon than the biosphere on land.

The key findings include:

  • Terrestrial vegetation and soils might absorb up to 30% more CO2 than what was estimated by earlier models.
  • The carbon storage in these ecosystems is more temporary than once believed, implying that man-made CO2 may not remain in the terrestrial biosphere as long as current models suggest.
  • The discrepancy in the models is due to underestimating the carbon stored in short-lived or non-woody plant tissues, as well as the extensive underground parts of plants, like fine roots.

The implications of these findings are significant for climate predictions and crafting effective climate policies. It highlights the need for more accurate representation of the global carbon cycle in climate models. While this increased uptake of CO2 by vegetation is a positive sign, it does not negate the urgency of reducing carbon emissions to combat climate change.

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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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Poly-electrolyte layers determine the efficiency of desalination membranes

Increasing water scarcity and pollution with micropollutants are responsible for the increasing cost of drinking water. Desalination of sea water and better wastewater treatment are necessary to counter this trend. Membranes can desalinate and remove most wastewater pollution. However, a lot of energy is required. Therefore, modern membranes must be more efficient in order to achieve satisfactory results.

Nano-filtration membranes consisting of poly-electrolytic layers are a promising approach to treat water more efficiently. Accordingly, the composition of poly-electrolytic layers has stirred up much interest in the production of nano-filtration membranes. Such membranes are manufactured layer by layer, which enables a good tuning of membrane properties for different purposes.

Commercially available nano-filtration membranes are usually a trade-off between high water permeability and good salt retention (desalination). This trade-off impacts either the quality or the volume of the cleaned water. Nano-filtration membranes that are produced in layer by layer can have a positive impact on this trade-off balance due to the formation of nano scaled layers. It is important to know which component plays a crucial role in the layer forming process.

A research group of the Technical University Eindhoven in the Netherlands had therefore undertaken the task of examining these layer components more closely. They specifically investigated the poly-electrolyte concentration. It is known that a higher poly-electrolyte concentration produces thicker layers. However, their impact on the membrane performance has so far been unknown. They now published their work, in which the researchers used two well-known strong poly-electrolytes: PDADMAC and PSS (polydiallyldimethylammonium chloride and poly(sodium-4-styrene sulfonate)). The membrane output was examined with regard to water permeability, the molecular weight cutoff and salt retention.

In the first double layer, the membranes made with a 50 mM saline solution showed a lower water permeability and molecular weight cutoff, as well as better salt retention (magnesium sulfate) due to the higher poly-electrolyt concentration. After a certain number of double layers, the molecular weight cutoff and the salt retention efficiency for all poly-electrolyte concentration leveled off. The higher the poly-electrolyte concentration, the sooner the plateau value was reached.

The membranes prepared with a 1 M salt concentration had a lower or comparable salt retention efficiency with one exception. The scientists concluded that the poly-electrolyte concentration significantly changed the membrane properties. A plateau was reached with seven or more double layers. The thicker layers showed a lower water permeability than those that were coated with poly-electrolyte solutions using a 50 mM salt concentration. Due to the reduced swelling of these membranes, they all had better salt retention efficiency, with the exception of magnesium chloride.

The results showed that increasing the poly-electrolyte concentration also increased the amount of poly-electrolyte adsorption. Due to a higher coating thickness, this led to lower permeability with pure water. However, this did not lead to a lower molecular weight cutoff or salt retention. The additional poly-electrolyte adsorption resulted in fewer links between the individual layers. The higher diffusivity of PDADMAC compared to PSS resulted in highly positively charged membranes, which in turn led to a better salt retention of magnesium and sodium chloride.

Overall, increased poly-electrolyte concentration and the salt concentration influenced the membrane charge exclusion significantly due to a higher charged surface, which led to better salt retention. However, the membrane size exclusion has not changed, which led to the same plateau values. The study presented here will allow chemists to produce better tuned desalination membranes, which will reduce the energy requirement and raw material requirements during production.

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