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33 pages, 3673 KiB  
Review
Addressing Challenges for Eco-Friendly and Sustainable Wastewater Treatment Solutions Using Extremophile Microorganisms
by Hassan Mohamad Anabtawi, Amir Ikhlaq, Sandeep Kumar, Safa Rafique and Ashraf Aly Hassan
Sustainability 2025, 17(6), 2339; https://doi.org/10.3390/su17062339 - 7 Mar 2025
Viewed by 186
Abstract
The pressure on the environment from wastewater has been increasing in line with industrialization and urbanization, thus calling for better and eco-friendly solutions for wastewater treatment. Extremophilic microorganisms, which can grow in extreme conditions including high salinity, acidity, and temperature, can be applied [...] Read more.
The pressure on the environment from wastewater has been increasing in line with industrialization and urbanization, thus calling for better and eco-friendly solutions for wastewater treatment. Extremophilic microorganisms, which can grow in extreme conditions including high salinity, acidity, and temperature, can be applied in wastewater bioremediation. This review assesses the various functions of extremophiles, halophiles, thermophiles, alkaliphiles, and acidophiles in the treatment of organic and inorganic pollutants. They are capable of catabolizing a wide range of hazardous chemicals, such as polycyclic aromatic hydrocarbons, phenolic compounds, and heavy metals. Moreover, extremophilic microalgae, like Galdieria sulphuraria, have been effective in nutrient removal, biosorption of heavy metals, and pollutant conversion into valuable biomass. This dual-functioning, therefore, helps not only in wastewater treatment but also in the production of biofuel and biofertilizer, making the process cost-effective. The use of extremophiles in biofilm reactors improves pollutant removal, with less energy input. Extremophilic microorganisms can, therefore, be used to revolutionize wastewater management by providing green solutions to current treatment approaches. This review discusses the existing drawbacks of wastewater treatment along with the additional requirements needed to enhance the capability of bioremediation and potential future research. Full article
(This article belongs to the Special Issue Water Treatment, Waste Valorization and Environment Sustainability)
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<p>Keyword Co-occurrence Network Map for Extremophilic Wastewater Treatment and Similar Research.</p>
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<p>Top 10 academic institutions by number of relevant research articles.</p>
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<p>Map illustrating the global distribution of scientific production.</p>
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<p>Line chart of the most cited countries for scientific research.</p>
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<p>Line graph showing related author’s publishing distribution by nation.</p>
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<p>Line graph illustrating the rise in scientific article output per nation over time.</p>
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<p>Adaptation mechanism of acidophilic substances for survival at acidic pH.</p>
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<p>Alkaliphiles’ role in wastewater treatment.</p>
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<p>Halophilic mechanisms in saline environment.</p>
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<p>Use of extremophilic microalgae in wastewater treatment.</p>
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22 pages, 2346 KiB  
Article
A Green Chemistry and Energy- and Cost-Effective Approach in Innovative Advanced Oxidation Processes Through Photoactive Microgels for Sustainable Applications
by Víctor Fabregat and Juana María Pagán
Sustainability 2025, 17(5), 2331; https://doi.org/10.3390/su17052331 - 6 Mar 2025
Viewed by 106
Abstract
Current sustainability challenges for the chemical industry include developing advanced wastewater treatment technologies and transitioning to renewable biomass for more sustainable processes. This study aims to design and develop photoactive colloidal microgels for environmental applications, focusing on the removal of pollutants and the [...] Read more.
Current sustainability challenges for the chemical industry include developing advanced wastewater treatment technologies and transitioning to renewable biomass for more sustainable processes. This study aims to design and develop photoactive colloidal microgels for environmental applications, focusing on the removal of pollutants and the green synthesis of sustainable materials. PNIPAM-based microgels with covalently integrated Rose Bengal as a photosensitizer was synthesized and characterized. The stimuli-responsive colloidal structure of the microgels enhances substrate adsorption and reaction kinetics, surpassing free Rose Bengal due to the local concentration effect provided by the polymeric matrix at the reaction temperature and pH. These materials, designed according to green chemistry principles, enable the sustainable synthesis of 5-hydroxy-2(5H)-furanone, a C4 building block intermediate, achieving over 99% conversion in aqueous media, which is a novel aspect compared to the literature. The removal of Diclofenac from wastewater has been highly efficient, reaching degradation rates of over 99% in 160 min. The photoactive microgels act as efficient photocatalysts, validated under direct solar irradiation, capable of generating singlet oxygen (O2(1Δg)) with full recoverability and reusability over multiple cycles. This approach provides a cost-effective eco-friendly solution to economic and environmental challenges in water treatment, as shown by scale-up economic simulations. Full article
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<p>(<b>Left</b>) Chemical structure of NIPAM, AEMA, and MBAM. Centre: Illustration of colloidal microgels without RB (left vial, NIPAM-co-AEMA) and with covalently anchored Rose Bengal (NIPAM-co-AEMA-RB). (<b>Right</b>) Chemical structure of Rose Bengal in basic media RB<sup>−2</sup>.</p>
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<p>Scheme of the carbodiimide coupling reaction in MeOH medium using EDC and Rose Bengal with the carboxylate group protonated (HOOC-RB, previously adjusted to pH = 2).</p>
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<p>Graphics of substrate adsorption in the microgel NIPAM-co-AEMA-RB (Diclofenac, (<b>left</b>) and furoic acid, (<b>right</b>)) in µmol substrate/g microgel as a function of the equilibrium substrate concentration at 25 °C and pH = 6.45.</p>
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<p>(<b>a</b>) Comparison of first-order kinetic parameters for singlet oxygen production between microgel-anchored RB and free RB. (<b>b</b>) Evolution graph of reaction rates of the microgel NIPAM-co-AEMA-RB vs. substrate (ADPA) adsorption onto the microgel. Comparison with free Rose Bengal, which remains constant.</p>
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<p>(<b>a</b>) Degradation ratio of Diclofenac over time (C) relative to the initial concentration (C<sub>0</sub>) for free RB and NIPAM-co-AEMA-RB in triplicate-performed experiments carried out in June. (<b>b</b>) Evolution graph of Diclofenac adsorption onto the NIPAM-co-AEMA-RB microgel vs. reaction rates of the microgel. Comparison with free Rose Bengal and TiO<sub>2</sub>, both at a concentration of 2.2 × 10<sup>−4</sup> M and remaining constant.</p>
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<p>Quenching of singlet molecular oxygen O<sub>2</sub>(<sup>1</sup>Δ<sub>g</sub>) by Diclofenac.</p>
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<p>Reaction pathway for the photo-oxidation of 2-furoic acid to 5-hydroxy-2(5H)-furanone via singlet oxygen. Photosensitizer (Sens) transitions to its excited singlet state (Sens*) after sun irradiation (hʋ), generating singlet oxygen (<sup>1</sup>O<sub>2</sub>) from ground-state molecular oxygen (<sup>3</sup>O<sub>2</sub>.). The process involves the formation of an endoperoxide intermediate.</p>
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<p>(<b>Left</b>) Conversion ratio of 5-hydroxy-2(5H)-furanone as a function of time under different irradiation scenarios. (<b>Right</b>) Evolution of the absorption band (λ = 246 nm) of furoic acid as a function of time under the December solar irradiation scenario, in both cases for NIPAM-co-AEMA-RB.</p>
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23 pages, 2660 KiB  
Article
Transitioning Hochschule Geisenheim University: A Shift from NET Source to NET Sink Regarding Its CO2 Emissions
by Georg Ardissone-Krauss, Moritz Wagner and Claudia Kammann
Sustainability 2025, 17(5), 2316; https://doi.org/10.3390/su17052316 - 6 Mar 2025
Viewed by 202
Abstract
Various Higher Education Institutions (HEIs) set themselves goals to become carbon neutral through the implementation of different reduction strategies such as the replacement of fossil-fueled vehicles with electric cars. However, even if all reduction measures are taken, residual GHG emissions will still remain. [...] Read more.
Various Higher Education Institutions (HEIs) set themselves goals to become carbon neutral through the implementation of different reduction strategies such as the replacement of fossil-fueled vehicles with electric cars. However, even if all reduction measures are taken, residual GHG emissions will still remain. Therefore, most HEIs have to compensate for the remaining emissions by, for example, buying carbon credits. However, due to growing criticism of carbon credit purchases, HEIs need to explore options for establishing carbon sinks on their own premises to offset their remaining, unavoidable emissions. This study aimed to assess the CO2 footprint of Hochschule Geisenheim University (HGU) as an exemplary HEI, identify emission hot-spots, and investigate the potential of biomass utilization for achieving carbon neutrality or even negative emissions. The analysis found that HGU’s main emissions were scope 1 emissions, primarily caused by on-site heat supply. The research determined that conversion to a wood chip-based heating system alone was insufficient to achieve climate neutrality, but this goal could be achieved through additional carbon dioxide removal (CDR). By operating a pyrolysis-based bivalent heating system, the study demonstrated that heat demand could be covered while producing sufficient C-sink certificates to transform HGU into the first carbon-negative HEI, at a comparable price to conventional combustion systems. Surplus C-sink certificates could be made available to other authorities or ministries. The results showed that bivalent heating systems can play an important role in HEI transitions to CO2 neutrality by contributing significantly to the most urgent challenge of the coming decades: removing CO2 from the atmosphere to limit global warming to as far below 2 °C as possible at nearly no extra costs. Full article
(This article belongs to the Special Issue Energy Efficiency: The Key to Sustainable Development)
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<p>Methodological framework for assessing the transition of Hochschule Geisenheim University from CO<sub>2</sub> source to sink. The flowchart illustrates the three-stage analytical approach: (1) GHG emissions analysis, (2) biomass potential assessment, and (3) technical-economic feasibility evaluation of heating systems. Green boxes indicate the identified optimal pathway.</p>
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<p>Spatial distribution of energy supply clusters at Hochschule Geisenheim University campus. The three main clusters are: central campus (CC) with primary energy demand, viticulture/oenology (VO) in the east, and Plant Breeding (PB) in the west. Colored areas represent distinct heating networks with current fossil (also known as natural) gas supply infrastructure.</p>
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<p>Annual heat load duration curve for the central campus cluster in 2019. The curve demonstrates that 90.55% of the annual heating demand occurs below 1.5 MW capacity, with peak loads reaching a maximum of 2.87 MW. This load distribution pattern supports the design rationale for a hybrid heating system.</p>
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<p>Sensitivity analysis results visualized as a tornado diagram showing the impact of key parameters on the Levelized Cost of Energy (LCOE) for the PY20/WC25 scenario. Parameters are ranked by their influence on LCOE, with locally sourced biomass share and heat production emerging as the most significant factors. (*) CO<sub>2</sub> credit price applies only to the wood chip (WC) system.</p>
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<p>Three-dimensional surface plot illustrating the combined effects of heat production capacity and locally sourced biomass percentage on the Levelized Cost of Energy (LCOE). The plot reveals a clear gradient with optimal economic performance (lowest LCOE) achieved at maximum heat production and 100% local biomass utilization.</p>
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<p>Projected carbon balance trajectory for Hochschule Geisenheim University following implementation of strategic emission reduction measures. The graph shows the transition from current emissions (2019 baseline) through various intervention stages, demonstrating the potential pathway to achieve carbon negativity through hybrid pyrolysis–wood chip heating system implementation.</p>
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16 pages, 15608 KiB  
Article
Financial Feasibility of Bioenergy Products Based on Forest Residues: Case of Costa Rica Northern
by Juan Carlos Valverde, Dagoberto Arias-Aguilar and Rooel Campos-Rodríguez
Clean Technol. 2025, 7(1), 21; https://doi.org/10.3390/cleantechnol7010021 - 6 Mar 2025
Viewed by 119
Abstract
This research identified the optimal scenarios to produce three bioenergy outputs: dual generation (electricity and heat), electricity, and heat in two regions located in the northern part of Costa Rica. Two biomass conversion technologies—boilers and gasification—with 2, 5, and 10 MW production capacities [...] Read more.
This research identified the optimal scenarios to produce three bioenergy outputs: dual generation (electricity and heat), electricity, and heat in two regions located in the northern part of Costa Rica. Two biomass conversion technologies—boilers and gasification—with 2, 5, and 10 MW production capacities were assessed to ascertain the most suitable technology-capacity pairing for each bioproduct. To this end, a comprehensive financial model was developed to maximize the net present value. Following this, the equilibrium point for biomass supply and demand was ascertained, alongside estimations of the associated costs and energy utility. The findings indicated that the three bioenergy products could be completed within the local energy market at prices below 0.14 USD/kWh, with maximum supply distances of 90 km. The boiler and turbine technology proved most suitable for dual and electricity generation, with capacities ranging between 2 MW and 5 MW, where differentiation was influenced by biomass transportation. Furthermore, heat generation demonstrated financial viability at a capacity of 2 MW. In the evaluation of supply-demand break-even points, a maximum benefit of 26% was observed, with dual production yielding the highest benefits and heat production being the least favorable option due to the costs linked to biomass transportation and the low efficiency of energy transformation. Full article
(This article belongs to the Collection Bioenergy Technologies)
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<p>Spatial distribution of areas with forest crops and locations considered for the installation of bioenergy processing plants in northern Costa Rica.</p>
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<p>Supply distances and maximum annual biomass demand are required to generate bioenergy products in the location 1 (<b>a</b>) and location 2 (<b>b</b>) in northern Costa Rica.</p>
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<p>Supply-demand production curves function of biomass price (<b>a</b>) and distribution of biomass costs with the biomass equilibrium price (<b>b</b>) for dual-energy generation in two locations in northern Costa Rica.</p>
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<p>Supply-demand production curves function of biomass price (<b>a</b>) and distribution of biomass costs with the biomass equilibrium price (<b>b</b>) for electricity generation in two locations in northern Costa Rica.</p>
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<p>Supply-demand production curves as a function of biomass price (<b>a</b>) and distribution of biomass costs with the biomass equilibrium price (<b>b</b>) for heat generation in two locations in northern Costa Rica.</p>
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16 pages, 772 KiB  
Article
Influence of Supplementary Blue and Far-Red Light on the Morphology and Texture of Ocimum basilicum L. Grown in Controlled Environments
by Madison A. Oehler, Nathan Kelly, Jorge M. Fonseca, Ella Evensen, Eunhee Park, Ganyu Gu, Zi Teng and Yaguang Luo
Horticulturae 2025, 11(3), 287; https://doi.org/10.3390/horticulturae11030287 - 6 Mar 2025
Viewed by 117
Abstract
Basil (Ocimum basilicum L.) is highly sensitive to environmental conditions and is an ideal candidate for cultivation in controlled environment agriculture (CEA). Light-emitting diode technology has become essential in CEA, offering precise control over light intensity, spectrum, and duration. This study investigated [...] Read more.
Basil (Ocimum basilicum L.) is highly sensitive to environmental conditions and is an ideal candidate for cultivation in controlled environment agriculture (CEA). Light-emitting diode technology has become essential in CEA, offering precise control over light intensity, spectrum, and duration. This study investigated how supplemental blue light, far-red light, or their combination influences basil biomass, morphology, texture, and color when added to a white + red light spectrum. Basil ’Prospera’ and ’Amethyst’ were exposed to five light treatments for 14–28 days: white + red at 180 µmol∙m−2∙s−1 (W) as the control, and four treatments with an additional 60 µmol∙m−2∙s−1 of either white + red (+W60), blue (+B60), far-red (+FR60), or a combination of B and FR (+B30+FR30), for a total photon flux density of 240 µmol∙m−2∙s−1. The results demonstrated that +B60 and +W60 light treatments increased leaf thickness by 17–20% compared to the +FR60 treatment. Conversely, texture analysis revealed that +FR60-treated leaves had higher puncture resistance, with ’Amethyst’ and ’Prospera’ requiring 1.57 ± 0.43 N and 1.45 ± 0.35 N of force, respectively, compared to 1.19 ± 0.32 N and 1.1 ± 0.21 N under +B60. These findings suggest that tailored light recipes in CEA can optimize basil quality, allowing growers to modify traits like leaf color, thickness, and toughness. Full article
(This article belongs to the Section Protected Culture)
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<p>Emission spectra for light treatments. Low white light control (W), high white light control (+W<sub>60</sub>), blue light treatment (+B<sub>60</sub>), far-red light treatment (+FR<sub>60</sub>), and blue and far-red light combined treatment (+B<sub>30</sub>+FR<sub>30</sub>).</p>
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<p>Average peak force, toughness, leaf thickness, and specific leaf area (SLA) of ‘Prospera’ and ‘Amethyst’ basil. Different letters denote significant differences among means based on Tukey’s honestly significant difference test (α = 0.05).</p>
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17 pages, 3998 KiB  
Article
Contributions of Oxide Support Reducibility for Selective Oxidation of 5-Hydroxymethylfurfural over Ag-Based Catalysts
by Haichen Lai, Gaolei Shi, Liuwei Shen and Xingguang Zhang
Catalysts 2025, 15(3), 248; https://doi.org/10.3390/catal15030248 - 5 Mar 2025
Viewed by 203
Abstract
As a type of sustainable and renewable natural source, biomass-derived 5-hydroxymethyl furfural (HMF) can be converted into high-value chemicals. This study investigated the interactions between silver (Ag) and oxide supports with varied reducibility and their contributions to tuning catalytic performance in the selective [...] Read more.
As a type of sustainable and renewable natural source, biomass-derived 5-hydroxymethyl furfural (HMF) can be converted into high-value chemicals. This study investigated the interactions between silver (Ag) and oxide supports with varied reducibility and their contributions to tuning catalytic performance in the selective oxidation of HMF. Three representatives of manganese dioxide (MnO2), zirconium dioxide (ZrO2), and silicon dioxide (SiO2) were selected to support the Ag active sites. The catalysts were characterized by techniques such as STEM (TEM), Raman, XPS, H2-TPR, and FT-IR spectroscopy to explore the morphology, Ag dispersion, surface properties, and electronic states. The catalytic results demonstrated that MnO2 with the highest reducibility exhibited superior catalytic performance, achieving 75.4% of HMF conversion and 41.6% of selectivity for 2,5-furandicarboxylic acid (FDCA) at 120 °C. In contrast, ZrO2 and SiO2 exhibited limited oxidation capabilities, mainly producing intermediate products like FFCA and/or HMFCA. The oxidation ability of these catalysts was governed by support reducibility, because it determined the density of oxygen vacancies (Ov) and surface hydroxyl groups (OOH), and eventually influenced the catalytic activity, as demonstrated by the reaction rate: Ag/MnO2 (3214.5 molHMF·gAg−1·h−1), Ag/ZrO2 (2062.3 molHMF·gAg−1·h−1), and Ag/SiO2 (1394.4 molHMF·gAg−1·h−1). These findings provide valuable insights into the rational design of high-performance catalysts for biomass-derived chemical conversion. Full article
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<p>XRD patterns of the three representative Ag catalysts and their corresponding supports: (<b>a</b>) Ag/MnO<sub>2</sub> and MnO<sub>2</sub>, (<b>b</b>) Ag/ZrO<sub>2</sub> and ZrO<sub>2</sub>, and (<b>c</b>) Ag/SiO<sub>2</sub> and SiO<sub>2</sub>.</p>
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<p>TEM images and HAADF-STEM images with corresponding elemental mapping of (<b>a</b>–<b>c</b>) Ag/MnO<sub>2</sub>, (<b>d</b>–<b>f</b>) Ag/ZrO<sub>2</sub>, and (<b>g</b>–<b>i</b>) Ag/SiO<sub>2</sub>.</p>
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<p>Raman spectra of the three representative Ag catalysts and their corresponding supports: (<b>a</b>) Ag/MnO<sub>2</sub> and MnO<sub>2</sub>, (<b>b</b>) Ag/ZrO<sub>2</sub> and ZrO<sub>2</sub>, and (<b>c</b>) Ag/SiO<sub>2</sub> and SiO<sub>2</sub>.</p>
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<p>High-resolution XPS spectra of (<b>a</b>) Ag 3d over three catalysts of Ag/MnO<sub>2</sub>, Ag/ZrO<sub>2</sub>, and Ag/SiO<sub>2</sub>, and (<b>b</b>) O 1s over MnO<sub>2</sub>, Ag/MnO<sub>2</sub>, ZrO<sub>2</sub>, Ag/ZrO<sub>2</sub>, SiO<sub>2</sub>, and Ag/SiO<sub>2</sub>.</p>
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<p>High-resolution XPS spectra of (<b>a</b>) Mn 2p over MnO<sub>2</sub> and Ag/MnO<sub>2</sub>, (<b>b</b>) Zr 3d over ZrO<sub>2</sub> and Ag/ZrO<sub>2</sub>, and (<b>c</b>) Si 2p over SiO<sub>2</sub> and Ag/SiO<sub>2</sub>.</p>
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<p>H<sub>2</sub>-TPR profiles of the three representative Ag catalysts and their corresponding supports: (<b>a</b>) Ag/MnO<sub>2</sub> and MnO<sub>2</sub>, (<b>b</b>) Ag/ZrO<sub>2</sub> and ZrO<sub>2</sub>, and (<b>c</b>) Ag/SiO<sub>2</sub> and SiO<sub>2</sub>.</p>
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<p>(<b>a</b>) Possible reaction routes for the selective oxidation of HMF via intermediates and FDCA. Catalytic performance of (<b>b</b>) MnO<sub>2</sub> and Ag/MnO<sub>2</sub>, (<b>c</b>) ZrO<sub>2</sub> and Ag/ZrO<sub>2</sub>, and (<b>d</b>) SiO<sub>2</sub> and Ag/SiO<sub>2</sub> for the oxidation of HMF. Reaction conditions: catalyst (0.05 g), reactant (0.1 mmol), NaHCO<sub>3</sub> (0.2 mmol), solvent: H<sub>2</sub>O (10 mL), 0.5 MPa O<sub>2</sub>, 120 °C, 5 h, 600 rpm.</p>
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<p>FTIR spectra of (<b>a</b>) MnO<sub>2</sub> and Ag/MnO<sub>2</sub>, (<b>b</b>) ZrO<sub>2</sub> and Ag/ZrO<sub>2</sub>, and (<b>c</b>) SiO<sub>2</sub> and Ag/SiO<sub>2</sub>. (<b>d</b>) The OH content of the different oxides as quantified by FTIR spectroscopy based on the peak area (3600–3300 cm<sup>−1</sup>). Correlation between Ag loading with (<b>e</b>) OH group content and (<b>f</b>) OH group consumption (the net OH content before and after Ag loading, calculated based on the aforementioned peak area). The Ag loading values were obtained from ICP-OES results.</p>
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<p>Catalytic performance of (<b>a</b>) Ag/MnO<sub>2</sub> and Ag/MnO<sub>2</sub>-1h, (<b>b</b>) Ag/ZrO<sub>2</sub> and Ag/ZrO<sub>2</sub>-1h, and (<b>c</b>) Ag/SiO<sub>2</sub> and Ag/SiO<sub>2</sub>-1h for the selective oxidation of HMF. Reaction conditions: catalyst (0.05 g), reactant (0.1 mmol), NaHCO<sub>3</sub> (0.2 mmol), solvent: H<sub>2</sub>O (10 mL), 0.5 MPa O<sub>2</sub>, 120 °C, 5 h, 600 rpm.</p>
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28 pages, 7947 KiB  
Article
Evaluation of Kabuli Chickpea Genotypes for Terminal Drought Tolerance in Tropical Growing Environment
by Megha Subedi, Mani Naiker, Ryan du Preez, Dante L. Adorada and Surya Bhattarai
Plants 2025, 14(5), 806; https://doi.org/10.3390/plants14050806 - 5 Mar 2025
Viewed by 133
Abstract
Terminal drought is the major constraint for chickpea production, leading to yield losses of up to 90% in tropical environments. Understanding the morphological, phenological, and physiological traits underlying drought tolerance is crucial for developing resilient chickpea genotypes. This study elucidates the drought-tolerant traits [...] Read more.
Terminal drought is the major constraint for chickpea production, leading to yield losses of up to 90% in tropical environments. Understanding the morphological, phenological, and physiological traits underlying drought tolerance is crucial for developing resilient chickpea genotypes. This study elucidates the drought-tolerant traits of eight kabuli chickpea genotypes under a controlled environment using polyvinyl chloride (PVC) lysimeters. Terminal drought was imposed after the flowering stage, and the response was assessed against non-stress (well-watered) treatment. Drought stress significantly impacted gas-exchange parameters, reducing the stomatal conductance (16–35%), chlorophyll content (10–22%), carbon assimilation rate (21–40%) and internal carbon concentration (7–14%). Principal component analysis (PCA) indicated three groups among these eight genotypes. The drought-tolerant group included two genotypes (AVTCPK#6 and AVTCPK#19) with higher water use efficiency (WUE), deep-rooted plants, longer maturity, and seed yield stability under drought stress. In contrast, the drought-susceptible group included two genotypes (AVTCPK#1 and AVTCPK#12) that were early-maturing and low-yielding with poor assimilation rates. The intermediate group included four genotypes (AVTCPK#3, AVTCPK8, AVTCPK#24, and AVTCPK#25) that exhibited medium maturity and medium yield, conferring intermediate tolerance to terminal drought. A significantly strong positive correlation was observed between seed yield and key physiological traits (stomatal conductance (gsw), leaf chlorophyll content (SPAD) and carbon assimilation rate (Asat)) and morphological traits (plant height, number of pods, and root biomass). Conversely, carbon discrimination (Δ13C) and intrinsic WUE (iWUE) showed a strong negative correlation with seed yield, supporting Δ13C as a surrogate for WUE and drought tolerance and a trait suitable for the selection of kabuli chickpea genotypes for drought resilience. Full article
(This article belongs to the Section Horticultural Science and Ornamental Plants)
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<p>Total water applied to the plant in well-watered (WW) and water-stress (WS) treatments in eight chickpea genotypes. Each vertical bar represents the least significant difference.</p>
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<p>Total water transpired by the plant in well-watered (WW) and water-stress (WS) treatments in eight chickpea genotypes. Each vertical bar represents the least significant difference.</p>
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<p>Water use efficiency in well-watered (WW) and water-stress (WS) treatments for eight chickpea genotypes. Each vertical bar represents the least significant difference.</p>
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<p>Carbon assimilation rate (Asat; mmol<sup>−2</sup>s<sup>−1</sup>) at 10 DAT (<b>A</b>) and 20 DAT (<b>B</b>) in eight chickpea genotypes. Same letters indicate, no significance, while different letters indicate a significant effect.</p>
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<p>Stomatal conductance (gsw; molm<sup>−2</sup>s<sup>−1</sup>) at 10 DAT (<b>A</b>) and 20 DAT (<b>B</b>) in eight chickpea genotypes. Same letters indicate no significance, while different letters indicate a significant effect.</p>
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<p>Internal CO<sub>2</sub> concentration (vpm) at 10 DAT (<b>A</b>) and 20 DAT (<b>B</b>) in eight chickpea genotypes. Same letters indicate no significance, while different letters indicate a significant effect.</p>
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<p>Internal water use efficiency (iWUE: (µmolmol<sup>−1</sup>)) at 10 DAT (<b>A</b>) and 20 DAT (<b>B</b>) in eight chickpea genotypes. Same letters indicate no significance, while different letters indicate a significant effect.</p>
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<p>SPAD chlorophyll content (SPDA unit) at 10 DAT (<b>A</b>) and 20 DAT (<b>B</b>) in eight chickpea genotypes. Same letters indicate no significance, while different letters indicate a significant effect.</p>
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<p>Interaction between genotype and treatment graph, presenting number of pods/plants of eight chickpea genotypes. Each vertical bar represents the least significant difference.</p>
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<p>Interaction between genotype and treatment graph presenting pod weight/plant (g) of eight chickpea genotypes. Each vertical bar represents the least significant difference.</p>
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<p>Interaction between genotypes and treatment graph presenting numbers of seeds/plants in eight chickpea genotypes. Each vertical bar represents the least significant difference.</p>
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<p>Interaction between genotypes and treatment graph presenting seed yield/plant (g) in eight chickpeas. Each vertical bar represents the least significant difference.</p>
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<p>Interaction between genotypes and treatment graph presenting harvest index in eight chickpeas. Each vertical bar represents the least significant difference.</p>
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<p>Standard PCA biplot of all traits with their loading vectors. Note: Biplot display of two principal components of all studied traits in chickpea genotypes. Correlogram showing the relationships among studied traits for water-stressed plants. SPAD10 (SPAD chlorophyll content at 10 DAT), SPAD20 (SPAD chlorophyll content at 20 DAT), Asat10 (carbon assimilation rate at 10 DAT, µmol m<sup>−</sup><sup>2</sup> s<sup>−</sup><sup>1</sup>), Asat20 (carbon assimilation rate at 20 DAT, µmol m<sup>−</sup><sup>2</sup> s<sup>−</sup><sup>1</sup>), gsw10 (stomata conductance at 10 DAT, mol m<sup>−</sup><sup>2</sup> s<sup>−</sup><sup>1</sup>), gsw20 (stomata conductance at 20 DAT, mol m<sup>−</sup><sup>2</sup> s<sup>−</sup><sup>1</sup>), Ci10 (internal carbon concentration at 10 DAT, vpm), Ci20 (internal carbon concentration at 20 DAT, vpm), iWUE10 (intrinsic water use efficiency at 10 DAT, µmol mol<sup>−1</sup>, iwue20 (intrinsic water use efficiency at 20 DAT, µmolmol<sup>−1</sup>), ∆<sup>13</sup>C (<sup>13/14</sup>carbon discrimination ratio), SY (seed yield, g plant<sup>−1</sup>), AGB (aboveground biomass, g plant<sup>−1</sup>), HI (harvest index), N.seed (number of seeds per plant), PW (pod weight, g plant<sup>−1</sup>), N.pod (number of pods per plant), PH (plant height at harvest, cm), PS (primary shoots at harvest), leaves (number of leaves at 60 DAS), DTF (days to flowering), DTP (days to podding), DTM (days to maturity), RL (root length, cm), RW (root dry weight, g), R:S (root–shoot ratio), WUE (water use efficiency at plant level, g/L plant) Dendrogram for eight genotypes in k-means clustering analysis is presented in <a href="#plants-14-00806-f016" class="html-fig">Figure 16</a>.</p>
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<p>PCA scores for genotypes with grouping based on cluster analysis.</p>
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<p>Dendrogram for eight genotypes in k-means clustering analysis.</p>
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<p>Correlogram showing the relationships between studied traits for water-stressed plants. Note: SPAD10 (SPAD chlorophyll content at 10 DAT), SPAD20 (SPAD chlorophyll content at 20 DAT), Asat10 (carbon assimilation rate at 10 DAT, µmol m<sup>−</sup><sup>2</sup> s<sup>−</sup><sup>1</sup>), Asat20 (carbon assimilation rate at 20 DAT, µmol m<sup>−</sup><sup>2</sup> s<sup>−</sup><sup>1</sup>), gsw10 (stomatal conductance at 10 DAT, mol m<sup>−</sup><sup>2</sup> s<sup>−</sup><sup>1</sup>), gsw20 (stomata conductance at 20 DAT, mol m<sup>−</sup><sup>2</sup> s<sup>−</sup><sup>1</sup>), Ci10 (internal carbon concentration at 10 DAT, vpm), Ci20 (internal carbon concentration at 20 DAT, vpm), iWUE10 (intrinsic water use efficiency at 10 DAT, µmolmol<sup>−1</sup>), iwue20 (intrinsic water use efficiency at 20 DAT, µmolmol<sup>−1</sup>), ∆13C (13/14 carbon discrimination ratio), SY (seed yield, g plant<sup>−1</sup>), AGB (aboveground biomass, g plant<sup>−1</sup>), HI (harvest index), N.seed (number of seeds per plant), PW (pod weight, g plant<sup>−1</sup>), N.pod (number of total pods per plant), PH (plant height at harvest, cm), PS (primary shoot at harvest), leaves (number of leaves at 60 DAS), DTF (days to flowering), DTP (days to podding), DTM (days to maturity), RL (root length, cm), RW (root dry weight, g), R:S (root–shoot ratio), WUE (water use efficiency at plant level, g/L plant).</p>
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<p>Percentage (%) decline in seed yield (g plant <sup>−1</sup>) under water stress treatment relative to well-watered plant.</p>
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<p>Trial setup of eight AgriVentis chickpea genotypes under well-watered (WW) and water-stressed (WS) conditions in glasshouse.</p>
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16 pages, 6354 KiB  
Article
From Cellulose to Highly Aromatic Hydrochar: Catalytic Carbonization and Catalytic Aromatization Mechanism of Lanthanide (III) Ions
by Shuaijie Han, Mingshu Chi, Xiuling Xu, Li Bai, Junquan Wu and Yizhuo Guo
Catalysts 2025, 15(3), 245; https://doi.org/10.3390/catal15030245 - 5 Mar 2025
Viewed by 79
Abstract
Hydrothermal carbonization (HTC) is an efficient method for converting lignocellulosic biomass into biofuels. However, traditional Brønsted acid-catalyzed HTC processes face challenges such as high costs and limited catalytic efficiency. In this study, the catalytic carbonization mechanism was investigated within the temperature range of [...] Read more.
Hydrothermal carbonization (HTC) is an efficient method for converting lignocellulosic biomass into biofuels. However, traditional Brønsted acid-catalyzed HTC processes face challenges such as high costs and limited catalytic efficiency. In this study, the catalytic carbonization mechanism was investigated within the temperature range of 180–220 °C by analyzing the evolution of functional groups in hydrochar under lanthanide (III)-catalyzed and non-catalyzed conditions. The results indicate that compared to acid catalysis, lanthanide (III) exhibits superior catalytic performance during the low-temperature HTC of cellulose. At 200 °C, lanthanide (III) accelerates the conversion of cellulose into char microparticles, while at 220 °C, it promotes the complete hydrolysis of cellulose into char microparticles enriched with furan structures. Characterization analyses revealed that lanthanide (III) enhances the formation of HMF (5-hydroxymethylfurfural), suppresses its conversion to LA (levulinic acid), promotes the polymerization of HMF into char microparticles, and indirectly accelerates the hydrolysis of cellulose into oligosaccharides. Full article
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<p>The proximate analysis and HHV of hydrochars.</p>
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<p>SEM images of (<b>a</b>) C-220, (<b>b</b>) LC-220, (<b>c</b>) C-250, and (<b>d</b>) C-280.</p>
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<p>FTIR spectra of hydrothermal carbon catalyzed by Lacl<sub>3</sub> (<b>a</b>) and acetic acid (<b>b</b>) between 180 and 220 °C.</p>
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<p>The <sup>13</sup>C NMR spectra of the hydrochars: (<b>a</b>) hydrochars at 180 °C; (<b>b</b>) hydrochars at 200 °C; (<b>c</b>) hydrochars at 220 °C; (<b>d</b>) hydrochars at different temperatures.</p>
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<p><sup>13</sup>C NMR labeling schemes for cellulose (<b>a</b>) and aromatic rings (furan and phenol) (<b>b</b>).</p>
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<p>Distribution of the C-containing functional groups (<b>a</b>) and the proposed structures (<b>b</b>) of hydrochars formed from raw materials of a high degree of intermediate dissolution and the subsequent hydrolyzed part through polymerization.</p>
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<p>Potential polymerization pathways of HMF: (<b>A</b>) aldol condensation reaction of HMF with HMF; (<b>B</b>) aldol condensation reaction of HMF with DHH; (<b>C</b>) polymerization reactions between furan molecules and between furan and phenolic compounds.</p>
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<p>The evolution of pH and TOC of liquid-phase products.</p>
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<p>The catalytic HTC mechanism of cellulose to form hydrochar with highly aromatic structures on account of lanthanide (III) ion catalysis.</p>
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25 pages, 3293 KiB  
Article
Design of a Semi-Continuous Microwave System for Pretreatment of Microwave-Assisted Pyrolysis Using a Theoretical Method
by Paula Andrea Ramírez Cabrera, Alejandra Sophia Lozano Pérez and Carlos Alberto Guerrero Fajardo
Inventions 2025, 10(2), 24; https://doi.org/10.3390/inventions10020024 - 4 Mar 2025
Viewed by 206
Abstract
This article provides an overview of various microwave-assisted techniques, such as microwave-assisted extraction (MAE), microwave-assisted organic synthesis (MAOS), microwave-assisted pyrolysis (MAP), microwave-assisted hydrothermal treatment (MAHT), microwave-assisted acid hydrolysis (MAAH), microwave-assisted organosolv (MAO), microwave-assisted alkaline hydrolysis (MAA), microwave-assisted enzymatic hydrolysis (MAEH), and microwave-assisted fermentation [...] Read more.
This article provides an overview of various microwave-assisted techniques, such as microwave-assisted extraction (MAE), microwave-assisted organic synthesis (MAOS), microwave-assisted pyrolysis (MAP), microwave-assisted hydrothermal treatment (MAHT), microwave-assisted acid hydrolysis (MAAH), microwave-assisted organosolv (MAO), microwave-assisted alkaline hydrolysis (MAA), microwave-assisted enzymatic hydrolysis (MAEH), and microwave-assisted fermentation (MAF). Microwave-assisted biomass pretreatment has emerged as a promising method to improve the efficiency of biomass conversion processes, in particular microwave-assisted pyrolysis (MAP). The focus is on microwave-assisted pyrolysis, detailing its key components, including microwave sources, applicators, feedstock characteristics, absorbers, collection systems, and reactor designs. Based on different studies reported in the literature and a mathematical model, a mechanical design of a microwave oven adapted for pyrolysis is proposed together with a computer-aided design and a finite element analysis. The semi-continuous system is designed for a 40 L capacity and a power of 800 W. The material with which the vessel was designed is suitable for the proposed process. The challenges, opportunities, and future directions of microwave-assisted technologies for the sustainable use of biomass resources are presented. Full article
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<p>Frequency of microwaves adapted from [<a href="#B11-inventions-10-00024" class="html-bibr">11</a>].</p>
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<p>Heat transfer via conventional heating and microwave heating. Adapted from [<a href="#B31-inventions-10-00024" class="html-bibr">31</a>].</p>
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<p>Types of microwaves adapted from [<a href="#B46-inventions-10-00024" class="html-bibr">46</a>].</p>
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<p>Design for microwave-assisted pyrolysis. (<b>a</b>) Left side view of the design and (<b>b</b>) front side view of the design.</p>
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<p>Parts of the design for microwave-assisted pyrolysis. 1. Microwave oven. 2. Glass vessel lid. 3. Glass vessel. 4. Gas bullet. 5. Gas piping. 6. Thermometer. 7. Pump. 8. Pump piping. 9. Condensation piping. 10. Condensation tubes. 11. Condensation tank. 12. Tee support.</p>
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<p>Dimensions of the design for microwave-assisted pyrolysis.</p>
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<p>Total deformation for the glass vessel.</p>
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<p>Equivalent stress for the glass vessel.</p>
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16 pages, 642 KiB  
Article
Effects of Chlortetracycline on Lignin Biosynthesis in Arabidopsis thaliana
by Aaron Newborn, Ayesha Karamat and Benoit Van Aken
Int. J. Mol. Sci. 2025, 26(5), 2288; https://doi.org/10.3390/ijms26052288 - 4 Mar 2025
Viewed by 147
Abstract
Feedstock plants for biofuel production can be cultivated on polluted sites that are unsuitable for edible crop production. This approach combines environmental restoration and renewable energy production, therefore enhancing the economic viability of plant-derived biofuels. Previous studies have indicated that exposure to environmental [...] Read more.
Feedstock plants for biofuel production can be cultivated on polluted sites that are unsuitable for edible crop production. This approach combines environmental restoration and renewable energy production, therefore enhancing the economic viability of plant-derived biofuels. Previous studies have indicated that exposure to environmental pollutants may elevate lignin levels in exposed plants, potentially impacting the biomass digestibility and the efficiency of bioethanol conversion. In this study, we investigated the impact of the antimicrobial agent chlortetracycline on lignin biosynthesis in the reference organism Arabidopsis thaliana. Toxicity testing showed that exposure to chlortetracycline significantly reduced plant growth at concentrations above 2.5 mg L−1. Using Fourier-transform infrared spectroscopy (FTIR) analysis, we observed a significant increase in the lignin signature, ranging from 16 to 40%, in plants exposed to chlortetracycline as compared to non-exposed control plants. Transcriptomic analysis (RNA sequencing) was conducted to determine the molecular basis of plant response to chlortetracycline, revealing significant enrichment of several genes involved in lignin biosynthesis and the phenylpropanoid pathway, including cinnamyl alcohol dehydrogenase and peroxidases. Exposure to chlortetracycline also resulted in the overexpression of genes involved in the metabolism of xenobiotic compounds, including cytochrome P450 monooxygenases, glutathione S-transferases, and glycosyltransferases. Chlortetracycline also induced several genes involved in plant response to stress and defense mechanisms, including transcription factors (e.g., WRKY, MYB, AP2/ERF families), pathogenesis-related proteins, and genes involved in stress signaling. These results suggest that the antibiotic chlortetracycline triggers multiple stress responses in A. thaliana, which may cause changes in lignin biosynthesis, reductions in plant growth, increases in the lignin content, and induction of defense metabolic pathways. Full article
(This article belongs to the Special Issue Isolation, Characterization and Application of Lignin)
17 pages, 1585 KiB  
Article
Effect of Clay Amendment and Strategic Deep Tillage on Soil Water Dynamics and Plant Growth Under Controlled Environments
by Kanchana Wickramarachchi, Giacomo Betti and Gaus Azam
Plants 2025, 14(5), 799; https://doi.org/10.3390/plants14050799 - 4 Mar 2025
Viewed by 259
Abstract
Strategic deep tillage (SDT) practices, such as soil mixing following the application of soil amendments, are promising approaches to alleviate topsoil water repellence and other subsoil constraints and improve crop productivity. However, there is a lack of knowledge on the effect of SDT [...] Read more.
Strategic deep tillage (SDT) practices, such as soil mixing following the application of soil amendments, are promising approaches to alleviate topsoil water repellence and other subsoil constraints and improve crop productivity. However, there is a lack of knowledge on the effect of SDT on soil water dynamics, especially under water-limited environments. This study evaluates the effects of clay incorporation, soil inversion and deep soil mixing on soil water infiltration, surface evaporation rates, soil water storage and subsequent impacts on the below and aboveground growth of wheat (Triticum aestivum L. var Scepter) in controlled environments. Results show that soil mixing significantly improved water infiltration compared to an untreated control. Clay incorporation exhibited the highest bare soil surface evaporation rates immediately and two years post-tillage, leading to substantial water losses under warm and dry ambient conditions. Despite improving soil water storage in deeper layers, high evaporation rates in clay-incorporated soils negatively impacted wheat growth, with reduced shoot biomass and root length density. Conversely, soil inversion and mixing-only treatments demonstrated balanced improvements in water infiltration, soil water use, and wheat shoot biomass. These findings underscore the trade-offs associated with SDT practices, particularly in managing soil water loss and crop productivity in water-limited environments. This study also highlights the need for the careful selection of SDT for soil amelioration strategies tailored to soil types and climatic conditions to enhance agricultural productivity and sustainability. Full article
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<p>Infiltration of water (mm) from (<b>a</b>) the pond of the permeameter, (<b>b</b>) initial infiltration rate (<span class="html-italic">f</span>, mm/h), (<b>c</b>) infiltration rate (<span class="html-italic">f</span>, mm/h) over the duration of the experiment, and (<b>d</b>) steady state <span class="html-italic">f</span> (mm/h) for different soil amelioration treatments. Vertical error bars represent the standard error of the mean value. Bar graphs with different letters are significantly different at <span class="html-italic">p</span> ≤ 0.05. Note that the <span class="html-italic">Y</span>-axis scale differs between the figures.</p>
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<p>Daily loss of water through evaporation (E) from bare soil (<b>a</b>–<b>c</b>) immediately after tillage in 2019 at 30 °C and 80% relative humidity in a growth chamber and (<b>d</b>–<b>f</b>) two years after tillage in 2021 at 30 °C and 45% relative humidity in a glasshouse. DAW = days after watering. Vertical error bars represent the standard error of the mean value. Bar graphs with different letters for a given DAW are significantly different at <span class="html-italic">p</span> ≤ 0.05 (<b>a</b>,<b>b</b>,<b>d</b>,<b>e</b>). Note that the <span class="html-italic">Y</span>-axis scale differs between the figures.</p>
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<p>Effect of tillage treatments on (<b>a</b>) shoot dry biomass (SDB) and (<b>b</b>) root length density (RLD). Relationship between the wheat (<span class="html-italic">Triticum aestivum</span> L. var Scepter) shoot dry biomass and (<b>c</b>) total RLD, 0–30 cm, and (<b>d</b>) cumulative evaporative loss from the bare soils. Bar graphs with different letters are significantly different at <span class="html-italic">p</span> ≤ 0.05 and the absence of letters refers to non-significance (for 10–20 and 20–30 cm depths) at <span class="html-italic">p</span> ≤ 0.05. Note that the <span class="html-italic">Y</span>-axis scale differs between the figures.</p>
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<p>Soil volumetric water content (VWC, cm<sup>3</sup>/cm<sup>3</sup>) at (<b>a</b>) 0–10 cm, (<b>b</b>) 10–20 cm, and (<b>c</b>) 20–30 cm depths under four tillage treatments over 38 days after seeding (DAS). Vertical error bars represent the standard error of the mean value. Note that the <span class="html-italic">Y</span>-axis scale differs between the figures.</p>
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<p>(<b>a</b>) A typical sandy soil profile in southwestern Australia and (<b>b</b>) a schematic of the four tillage treatments.</p>
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<p>(<b>left</b>) CSIRO disc permeameter, and (<b>right</b>) a soil column with the evaporation dome.</p>
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22 pages, 1319 KiB  
Review
Effects of Lignocellulosic Biomass-Derived Hydrolysate Inhibitors on Cell Growth and Lipid Production During Microbial Fermentation of Oleaginous Microorganisms—A Review
by Qiwei Lyu, Rouf Ahmad Dar, Frank Baganz, Adam Smoliński, Abdel-Hamied Mohamed Rasmey, Ronghou Liu and Le Zhang
Fermentation 2025, 11(3), 121; https://doi.org/10.3390/fermentation11030121 - 4 Mar 2025
Viewed by 233
Abstract
For efficient production of microbial lipids also known as single cell oil (SCO), selection of favorable growth conditions including the substrate for maximum conversion into storage lipids is imperative. Utilization of lignocellulosic biomass for microbial oil production is a promising approach as it [...] Read more.
For efficient production of microbial lipids also known as single cell oil (SCO), selection of favorable growth conditions including the substrate for maximum conversion into storage lipids is imperative. Utilization of lignocellulosic biomass for microbial oil production is a promising approach as it is renewable, sustainable, and available in abundance, with a significant quantity of fermentable sugars. Because of their intricate structure and biomolecular composition, lignocellulosic substrates exhibit high recalcitrance and demand specific pretreatments to release the fermentable sugars. However, pretreating the lignocellulosic substrate not only produces assimilable sugars but also various fermentation inhibitors that can significantly impede microbial growth and/or lipogenesis. Therefore, in this review, we discuss different inhibitors present in the lignocellulosic hydrolysates, and the impact on oleaginous microbial growth and metabolic activity, particularly concerning lipid production. Furthermore, the mode of inhibition of the various inhibitors and potential strategies to detoxify these are discussed in this review. Full article
(This article belongs to the Special Issue Lignocellulosic Biomass Valorization)
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<p>Process stages and inhibitor formation in lignocellulosic biomass conversion to microbial lipids.</p>
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<p>Mechanisms of different inhibitors commonly found in a hydrolysate. The red arrows indicate typical cellular responses under different inhibitors, such as increased proton efflux, elevated ATP consumption, and decreased intracellular pH. The black arrows indicate the pathway or correlation between inhibitors and effects.</p>
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2 pages, 128 KiB  
Editorial
Statement of Peer Review
by Luis Olivera-Montenegro
Eng. Proc. 2025, 83(1), 28; https://doi.org/10.3390/engproc2025083028 - 3 Mar 2025
Viewed by 113
Abstract
In submitting conference proceedings to Engineering Proceedings, the volume editors of the proceedings certify to the publisher that all papers published in this volume have been subjected to peer review administered by the volume editors [...] Full article
19 pages, 4145 KiB  
Article
Enhanced Anaerobic Digestion Performance Through Acyl Homoserine Lactone-Mediated Quorum Sensing and Supplemental Voltage Regulation
by Jie Zhou, Mingxuan Xu, Diwen Cao, Shuhuan Li, Xiaorui Yang, Weiliang Dong, Honghua Jia and Xiayuan Wu
Fermentation 2025, 11(3), 117; https://doi.org/10.3390/fermentation11030117 - 2 Mar 2025
Viewed by 229
Abstract
Traditional anaerobic digestion (AD) technology continues to have severe limitations in terms of complicated substrate degradation efficiency and methane production. This study optimizes the AD system using corn straw and cattle manure as substrates by introducing an exogenous N-Hexanoyl-L-Homoserine lactone (C6-HSL) signaling molecule [...] Read more.
Traditional anaerobic digestion (AD) technology continues to have severe limitations in terms of complicated substrate degradation efficiency and methane production. This study optimizes the AD system using corn straw and cattle manure as substrates by introducing an exogenous N-Hexanoyl-L-Homoserine lactone (C6-HSL) signaling molecule in concert with an applied external voltage of 0.8 V, systematically investigating its impact on methanogenic performance and microbial community dynamics. The results show that the combined regulation significantly increased methane production (by 29.74%) and substrate utilization rate (by 74.73%) while preventing acid inhibition and ammonia nitrogen inhibition. Mechanistic analysis revealed that the external voltage enhanced the system’s electrocatalytic activity, while the C6-HSL signaling molecule further facilitated the electron transfer efficiency of the biofilm on the electrode. The combined regulation notably enriched hydrogenotrophic methanogens (with Methanobacterium predominating on the cathode and Methanobrevibacter in the digestate), establishing a stable metabolic cooperative network on both the electrode and in the digestate, optimizing the hydrogenotrophic methanogenesis pathway, and enhancing the synergistic effects among microbial communities and system robustness. This study uncovers the synergistic enhancement mechanism of C6-HSL and external voltage, providing new technological pathways and theoretical support for the efficient conversion of low-quality biomass resources and the production of clean energy. Full article
(This article belongs to the Section Industrial Fermentation)
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<p>Effects of different regulations on daily methane production (<b>a</b>), accumulative methane production (<b>b</b>), and the total production of biogas and methane (<b>c</b>) in AD systems (***, <span class="html-italic">p</span> &lt; 0.001; **, <span class="html-italic">p</span> &lt; 0.01; *, <span class="html-italic">p</span> &lt; 0.05), and comparison with related studies on AD performance (<b>d</b>).</p>
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<p>Effects of different regulations on pH (<b>a</b>), COD concentration (<b>b</b>), NH<sub>4</sub><sup>+</sup>-N concentration (<b>c</b>), VFAs concentration, (<b>d</b>) and coenzyme F420 concentration (<b>e</b>) in AD systems.</p>
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<p>Effects of different regulations on the total EPS concentration (<b>a</b>), protein concentration (<b>b</b>), and polysaccharide concentration (<b>c</b>) in AD systems.</p>
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<p>Effect of electrochemical regulation on current change (<b>a</b>), the anode CV (<b>b</b>), and EIS (<b>c</b>) curves on 5 d in AD systems.</p>
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<p>Microbial community structure analysis of biofilm at phylum (<b>a</b>) and genus level (<b>b</b>), and the methanogen community structure at the genus level (<b>c</b>) during AD.</p>
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<p>Microbial community structure analysis of fermentation broth at the phylum (<b>a</b>) and genus (<b>b</b>) level, and the methanogen community structure at the genus level in different AD systems (<b>c</b>).</p>
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<p>Spearman’s rank correlation analysis among environmental factors and microbial community of fermentation broth in the Control (<b>a</b>) and C6-HSL + 0.8 V (<b>b</b>) groups. The molecular ecological network analysis based on the genus level of microbial community in the Control (<b>c</b>) and C6-HSL + 0.8 V (<b>d</b>) groups (the nodes with different colors represent the different modules; the size of each node is proportional to the module degree; the red and green lines between two nodes indicate positive and negative correlations, respectively; <span class="html-italic">p</span> &lt; 0.05, r &gt; 0.5; ***, <span class="html-italic">p</span> &lt; 0.001).</p>
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<p>Proposed regulation mechanism of AHL coupled with microbial electrolysis for AD of agricultural wastes.</p>
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<p>Effects of different regulation on acetic acid (<b>a</b>), propionic acid (<b>b</b>), and butyric acid (<b>c</b>) concentration in AD systems.</p>
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<p>The changes in anode CV ((<b>a</b>): 0.8 V, (<b>b</b>): C6-HSL + 0.8 V) and EIS ((<b>c</b>): 0.8 V, (<b>d</b>): C6-HSL + 0.8 V) in different AD systems.</p>
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19 pages, 3414 KiB  
Article
24-Epibrassinolide Enhanced Plant Antioxidant System and Cadmium Bioavailability Under Soil Cadmium Stress
by Wenle Song, Hongen Li, Ziyi Zhao, Rongrong Si, Wen Deng, Mengqi Wang and Yepu Li
Plants 2025, 14(5), 765; https://doi.org/10.3390/plants14050765 - 2 Mar 2025
Viewed by 130
Abstract
Soil cadmium pollution poses significant environmental risks, prompting global concern. Previous studies have demonstrated that 24-epibrassinolide (Brs) can enhance plant photosynthesis, thereby potentially improving the efficiency of soil cadmium remediation by increasing biomass. Therefore, this study investigated the use of Brs to enhance [...] Read more.
Soil cadmium pollution poses significant environmental risks, prompting global concern. Previous studies have demonstrated that 24-epibrassinolide (Brs) can enhance plant photosynthesis, thereby potentially improving the efficiency of soil cadmium remediation by increasing biomass. Therefore, this study investigated the use of Brs to enhance Cd remediation by willow and alfalfa. After four months, we analyzed soil physicochemical properties, plant physiological and biochemical responses, biomass, Cd fractionation, plant Cd concentrations, and bioaccumulation factor (BCF). Willow and alfalfa cultivation without Brs increased soil pH and carbonates, reduced the exchangeable Cd fractionation, and increased Cd bound to Fe-Mn oxides and organic matter (p < 0.05). Conversely, Brs application increased soil total acids, increasing the bioavailable Cd (p < 0.05). Willow grown for four months accumulated Cd in leaves, stems, and roots at concentrations of 141.83−242.75, 45.91−89.66, and 26.73−45.68 mg kg−1, respectively, with leaf BCF ranging from 14.53 to 24.88. After five months, leaves of willow planted in Cd-contaminated soil (9.65 mg kg−1) contained 187.90−511.23 mg kg−1 Cd, with BCFs of 19.25−52.38. Brs also increases plant biomass by improving photosynthesis, detoxification, and antioxidant defenses. Treatments with Brs and willow extracted 1.57−1.81 times more Cd (0.56−1.37 mg pot−1) than without Brs (0.31−0.87 mg pot−1). This study offers guidelines for Cd phytoremediation and highlights an effective strategy to enhance Cd accumulation. Full article
(This article belongs to the Section Plant Physiology and Metabolism)
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<p><span class="html-italic">Chl a</span>, <span class="html-italic">Chl b</span>, and carotenoid in willow and alfalfa treated with and without Brs after four months. (<b>A</b>–<b>C</b>) indicate <span class="html-italic">Chl a</span>, <span class="html-italic">Chl b</span>, and Carotenoid for willow, respectively. (<b>D</b>–<b>F</b>) indicate <span class="html-italic">Chl a</span>, <span class="html-italic">Chl b</span>, and Carotenoid for alfalfa, respectively. W, A, and WA indicate that soils were planted with willow, alfalfa, and a combination of them, respectively. CK indicates that willow, alfalfa, and a combination of them were planted in the soil with 0.67 mg kg<sup>−1</sup> Cd pollution. Brs and NBrs indicate that willow, alfalfa, and a combination of them were treated with and without Brs in the Cd-polluted soils (9.65 mg kg<sup>−1</sup>), respectively. The different letters indicate the significant differences among different treatments.</p>
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<p><span class="html-italic">P<sub>n</sub></span> and T-SH in willow and alfalfa treated with and without Brs after four months. (<b>A</b>,<b>B</b>) indicate <span class="html-italic">P<sub>n</sub></span> for willow and alfalfa, respectively. (<b>C</b>,<b>D</b>) indicate T-SH for willow and alfalfa, respectively. W, A, and WA indicate that soils were planted with willow, alfalfa, and a combination of them, respectively. CK indicates that willow, alfalfa, and a combination of them were planted in the soil with 0.67 mg kg<sup>−1</sup> Cd pollution. Brs and NBrs indicate that willow, alfalfa, and a combination of them were treated with and without Brs in the Cd-polluted soils (9.65 mg kg<sup>−1</sup>), respectively. The different letters indicate the significant differences among different treatments.</p>
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<p>T-SOD, CAT, and MDA in willow and alfalfa were treated with and without Brs after four months. (<b>A</b>,<b>C</b>,<b>E</b>) indicate T-SOD, CAT, and MDA for willow, respectively. (<b>B</b>,<b>D</b>,<b>F</b>) indicate T-SOD, CAT, and MDA for alfalfa, respectively. W, A, and WA indicate that soils were planted with willow, alfalfa, and a combination of them, respectively. CK indicates that willow, alfalfa, and a combination of them were planted in the soil with 0.67 mg kg<sup>−1</sup> Cd pollution. Brs and NBrs indicate that willow, alfalfa, and a combination of them were treated with and without Brs in the Cd-polluted soils (9.65 mg kg<sup>−1</sup>), respectively. The different letters indicate the significant differences among different treatments.</p>
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<p>Plant total biomass of willow (<b>A</b>) and alfalfa (<b>B</b>) treated with and without Brs after four months. W, A, and WA indicate that soils were planted with willow, alfalfa, and a combination of them, respectively. CK indicates that willow, alfalfa, and a combination of them were planted in the soil with 0.67 mg kg<sup>−1</sup> Cd pollution. Brs and NBrs indicate that willow, alfalfa, and a combination of them were treated with and without Brs in the Cd-polluted soils (9.65 mg kg<sup>−1</sup>), respectively. The different letters indicate the significant differences among different treatments.</p>
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<p>Concentrations of EX-Cd (<b>A</b>), CAB-Cd (<b>B</b>), FMO-Cd (<b>C</b>), OM-Cd (<b>D</b>), RES-Cd (<b>E</b>), and ion Cd (<b>F</b>) in the rhizosphere soil after plant four months of growth. W, A, and WA indicate that soils were planted with willow, alfalfa, and a combination of them, respectively. Brs and NBrs indicate that willow, alfalfa, and a combination of them were treated with and without Brs in the Cd-polluted soils (9.65 mg kg<sup>−1</sup>), respectively. The different letters indicate the significant differences among different treatments.</p>
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<p>Concentrations of Cd in the plant tissues ((<b>A</b>) for willow and (<b>B</b>) for alfalfa) and the total extraction contents (<b>C</b>) by plants after four months of growth. W, A, and WA indicate that soils were planted with willow, alfalfa, and a combination of them, respectively. Brs and NBrs indicate that willow, alfalfa, and a combination of them were treated with and without Brs in the Cd-polluted soils (9.65 mg kg<sup>−1</sup>), respectively. The different letters indicate the significant differences among different treatments.</p>
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<p>Bioaccumulation factor of Cd in the different tissues of willow (<b>A</b>) and alfalfa (<b>B</b>). W, A, and WA indicate that soils were planted with willow, alfalfa, and a combination of them, respectively. Brs and NBrs indicate that willow, alfalfa, and a combination of them were treated with and without Brs in the Cd-polluted soils (9.65 mg kg<sup>−1</sup>), respectively. The different letters indicate the significant differences among different treatments.</p>
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