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30 pages, 7966 KiB  
Article
The Complex Valorization of Black Alder Bark Biomass in Compositions of Rigid Polyurethane Foam
by Alexandr Arshanitsa, Matiss Pals, Laima Vevere, Lilija Jashina and Oskars Bikovens
Materials 2025, 18(1), 50; https://doi.org/10.3390/ma18010050 (registering DOI) - 26 Dec 2024
Abstract
The use of black alder (BA) bark biomass in rigid polyurethane (PUR) foam compositions was the main task of investigation. Extractive compounds isolated from the bark through hot water extraction were used as precursors for bio-polyol synthesis via acid-free liquefaction with the polyether [...] Read more.
The use of black alder (BA) bark biomass in rigid polyurethane (PUR) foam compositions was the main task of investigation. Extractive compounds isolated from the bark through hot water extraction were used as precursors for bio-polyol synthesis via acid-free liquefaction with the polyether polyol Lupranol 3300 and through oxypropylation with propylene carbonate. The OH functionality and composition of the polyols were analyzed via wet chemistry and FTIR spectroscopy. The solid remaining after the isolation of extractive compounds was also utilized as a natural filler in PUR foams. The effects of replacing commercial polyols with bio-polyols on the foam rising rate and their mechanical properties, morphology, thermal conductivity, and thermal degradation characteristics were examined. The oxypropylated extractive-based PUR compositions demonstrated the most favorable balance between the biomass content and material properties. At an apparent density of 40 kg/m3, the compressive strength of the produced foams was enhanced by 1.4–1.5 times, while the maximum thermal degradation rate in air decreased by 3.8–6.5 times compared to reference materials without adversely affecting the foam morphology. The composition based on liquefied extractives showed lower performance but still improved properties relative to the reference foams. Introducing 3.7–14% of extracted bark into the foam compositions increased the biomass content to 22–24%, although this led to a decrease in the compressive strength and thermal stability. It was shown that partially substituting fossil-derived components with renewable bark biomass in the composition of PUR foams allows for materials with characteristics similar or better to petrochemical-based materials to be obtained. Therefore, the results presented can be considered a contribution to addressing environmental problems and promoting the development of a sustainable economy. Full article
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Graphical abstract

Graphical abstract
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<p>The content of OH groups of different originations in BA bark extractives according to <sup>31</sup>P NMR.</p>
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<p>The content of liquefied biomass in bio-polyols as a function of the duration and temperature of processing at different biomass contents in the starting suspension: 10% (<b>a</b>), 20% (<b>b</b>), 30% (<b>c</b>), 40% (<b>d</b>).</p>
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<p>Plots of liquefied biomass content in bio-polyol vs. biomass content in the initial suspension after 6 h of extractive liquefaction at different temperatures (<b>a</b>), and the effect of the duration on the yield of liquefied BA bark extractives, independent of the temperature and biomass content in the initial suspension (<b>b</b>).</p>
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<p>FTIR spectra of BA extract (<b>a</b>) pure Lupranol 3300 and bio-polyols with varying biomass contents liquefied at 150 °C for 6 h (<b>b</b>).</p>
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<p>FTIR spectra in the region of 1800–1500 cm<sup>−1</sup> of pure Lupranol 3300 and bio-polyols with varying biomass contents liquefied at 150 °C during 6 h (<b>a</b>) and FTIR spectra absorbance ratio (A<sub>1710 cm</sub><sup>−1</sup>/A<sub>1515 cm</sub><sup>−1</sup>) of bio-polyols synthesized at different temperatures vs. the biomass content in them (<b>b</b>).</p>
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<p>Experimental and calculated content of phenolic and OH<sub>COOH</sub> groups (in bio-polyols obtained at different temperatures) dependent on the liquified biomass content.</p>
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<p>OHV (<b>a</b>) and acid numbers (<b>b</b>) of bio-polyols obtained at different temperatures and dependence on the liquified biomass content in them.</p>
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<p>Flow curves (<b>a</b>) and dynamic viscosity at 25 °C (<b>b</b>) of bio-polyols with different contents of biomass synthesized at 150 °C.</p>
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<p>The DTG (<b>a</b>) and DSC (<b>b</b>) curves of untreated and extracted bark in air media.</p>
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<p>The particle size distribution of ground-extracted bark.</p>
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<p>SEM image of ground BA bark at different magnifications: ×500 (<b>left</b>) and ×5000 (<b>right</b>).</p>
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<p>The height (<b>a</b>) and rise rate (<b>b</b>) of PUR foams versus time.</p>
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<p>Effect of extracted bark content as a filler in PUR foam on the height (<b>a</b>,<b>c</b>,<b>e</b>) and foam rise rate (<b>b</b>,<b>d</b>,<b>f</b>) across different PUR foam compositions: Ref. 2 (<b>a</b>,<b>b</b>); BP-3/F (<b>c</b>,<b>d</b>); and BP-5/F (<b>e</b>,<b>f</b>).</p>
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<p>FTIR spectra of rigid PUR foams.</p>
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<p>Apparent density, normalized strength, and Young’s modulus under axial compression parallel to the foaming direction for reference and bio-polyol-based rigid PUR foams (sample abbreviations are consistent with <a href="#materials-18-00050-t003" class="html-table">Table 3</a>).</p>
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<p>Apparent density, normalized strength, and Young’s modulus under axial compression parallel to the foaming direction of reference and bio-polyol-based rigid PUR foams as a function of the filler content (sample abbreviations are consistent with <a href="#materials-18-00050-t003" class="html-table">Table 3</a>).</p>
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<p>The closed-cell content in reference and bio-polyol based PUR foams (<b>a</b>); the effect of filler content on the closed-cell content in bio-polyol based foams (<b>b</b>) (sample abbreviations are consistent with <a href="#materials-18-00050-t003" class="html-table">Table 3</a> and <a href="#materials-18-00050-t004" class="html-table">Table 4</a>).</p>
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<p>SEM images of reference and bio-polyols-based PUR foams in parallel with foaming directions. Ref. 2 (<b>a</b>); BP-3 (<b>b</b>); BP-4 (<b>c</b>).</p>
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<p>The TG and DTG curves of reference PUR foams and bio-polyol-based PUR foams in air.</p>
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<p>TG and DTG curves in air for unfilled (BP-3, BP-5) (<b>a</b>) and 13%-filler-containing (BP-3/F, BP-5/F) bio-polyol-based PUR foams (<b>b</b>).</p>
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20 pages, 2049 KiB  
Article
Biovalorization of Aquaculture Biofloc Waste Through Polyphenol Extraction by Alkaline Hydrolysis and Green Nanoparticle Synthesis Optimization
by Robson M. M. Gomes, Juan R. B. Ramírez, Alan C. S. Araujo, Andressa C. Pereira, Cynthia M. O. Couto, Corina Rojas, Luiz A. Pinto, Tito Junior, Daniela F. Ramos and José M. Monserrat
Processes 2025, 13(1), 29; https://doi.org/10.3390/pr13010029 (registering DOI) - 26 Dec 2024
Abstract
The present research aims to valorize biofloc waste by extracting polyphenols via alkaline hydrolysis, utilizing them as reducing and stabilizing agents in the optimization of green synthesis of silver nanoparticles (BIOAgNPs). For the alkaline extractions, potassium hydroxide (KOH) concentrations of 0 to 4 [...] Read more.
The present research aims to valorize biofloc waste by extracting polyphenols via alkaline hydrolysis, utilizing them as reducing and stabilizing agents in the optimization of green synthesis of silver nanoparticles (BIOAgNPs). For the alkaline extractions, potassium hydroxide (KOH) concentrations of 0 to 4 M were used in combination with ultrasound. Total polyphenol content and antioxidant activity were evaluated. BIOAgNPs synthesis was optimized using the response surface methodology and central composite design. The parameters time, temperature, AgNO3 concentration, and the percentage of the biofloc extract (2 M KOH), with measurements taken for the area under the curve (AUC) (400–500 nm) and the mean hydrodynamic diameter (DLS), were evaluated. Antibacterial activity was determined for Gram-negative and Gram-positive bacteria. Higher polyphenol content and antioxidant activity were observed using 2 M KOH. The optimized model for DLS and the AUC was obtained in 4 h, at 40 °C, using 2.4 mM AgNO3 and obtaining 2.5% of extract. Optimized BIOAgNPs had a diameter of 22.4 nm, hydrodynamic diameter of 106.5 nm, zeta potential of −28 mV, and polydispersity index of 0.26. BIOAgNPs demonstrated bactericidal activities. This study enhanced the valorization of aquaculture residues through improved polyphenol extraction techniques and developed an effective methodology for synthesizing silver nanoparticles with antimicrobial activity. Full article
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<p>Polyphenols and antioxidant activity from extraction by alkaline hydrolysis using potassium hydroxide. (<b>A</b>) Total polyphenol content. (<b>B</b>) DPPH radical. (<b>C</b>) ABTS radical. (<b>D</b>) Ferric reducing antioxidant power (FRAP). Different letters indicate statistical differences (<span class="html-italic">p</span> &lt; 0.05) after ANOVA and Tukey’s test.</p>
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<p>Response surfaces of the DLS response variable (nm). (<b>A</b>) Temperature and time. (<b>B</b>) Silver nitrate and time. (<b>C</b>) Temperature and extract percentage.</p>
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<p>Response surfaces of the AUC response variable (400–500 nm). (<b>A</b>) Temperature and extract percentage. (<b>B</b>) Silver nitrate and extract percentage. (<b>C</b>) Silver nitrate and time.</p>
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<p>Desirability multi-response for DLS and the AUC.</p>
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<p>Characterization of silver nanoparticles (BioAgNPs). (<b>A</b>) UV-Vis absorption scan of BioAgNPs and biofloc extract (2 M KOH). (<b>B</b>) Zeta potential. (<b>C</b>) Transmission electron microscopy (TEM). (<b>D</b>) Diameter frequency by TEM.</p>
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22 pages, 1658 KiB  
Article
Optimization of a Pressurized Extraction Process Based on a Ternary Solvent System for the Recovery of Neuroprotective Compounds from Eucalyptus marginata Leaves
by Soumaya Hasni, Hajer Riguene, Jose A. Mendiola, Elena Ibáñez, Lidia Montero, Gloria Domínguez-Rodríguez, Hanene Ghazghazi, Ghayth Rigane and Ridha Ben Salem
Int. J. Mol. Sci. 2025, 26(1), 94; https://doi.org/10.3390/ijms26010094 - 26 Dec 2024
Abstract
Green chemistry focuses on reducing the environmental impacts of chemicals through sustainable practices. Traditional methods for extracting bioactive compounds from Eucalyptus marginata leaves, such as hydro-distillation and organic solvent extraction, have limitations, including long extraction times, high energy consumption, and potential toxic solvent [...] Read more.
Green chemistry focuses on reducing the environmental impacts of chemicals through sustainable practices. Traditional methods for extracting bioactive compounds from Eucalyptus marginata leaves, such as hydro-distillation and organic solvent extraction, have limitations, including long extraction times, high energy consumption, and potential toxic solvent residues. This study explored the use of supercritical fluid extraction (SFE), pressurized liquid extraction (PLE), and gas-expanded liquid (GXL) processes to improve efficiency and selectivity. These techniques were combined in a single mixture design, where CO2 was used in the experiments carried out under SFE, while water and ethanol were used for the PLE and GXL experiments by varying the concentration of the solvents to cover all the extraction possibilities. The neuroprotective activity of the extracts was evaluated by measuring their antioxidant, anti-inflammatory, and acetylcholinesterase inhibition properties. The optimization resulted in a novel GXL extraction with an optimal ternary mixture of 27% CO2, 55% ethanol, and 18% water, with a high degree of desirability (R2 = 88.59%). Chromatographic analysis carried out by GC-MS and HPLC-ESI-MS/MS identified over 49 metabolites. The designed sustainable extraction process offers a promising approach for producing phenolic-rich plant extracts in industrial applications. Full article
(This article belongs to the Special Issue Neuroprotective Effects of Food Ingredients)
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<p>(<b>a</b>) Cumulative yield curves for various solvent compositions. (<b>b</b>) Total extraction yields represented in a ternary phase diagram.</p>
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<p>GC-MS chromatogram of the optimal GXL extract from <span class="html-italic">Eucalyptus marginata</span> leaves, obtained with CO<sub>2</sub>–ethanol–water (27:55:18, <span class="html-italic">v</span>/<span class="html-italic">v</span>/<span class="html-italic">v</span>) (100 bar, T = 50 °C).</p>
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<p>HPLC-ESI-MS chromatogram of the optimal GXL extract from <span class="html-italic">Eucalyptus marginata</span> leaves, obtained with CO<sub>2</sub>–ethanol–water (27:55:18, <span class="html-italic">v</span>/<span class="html-italic">v</span>/<span class="html-italic">v</span>) (100 bar, 50 °C).</p>
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<p>Suggested schematic and chemical structure for the fragmentation of quercetin-7-O-rutinoside (peak 12) in the HPLC-ESI-MS analysis.</p>
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<p>Suggested schematic and chemical structure for the fragmentation of kaempferol-rutinoside in the HPLC-ESI-MS analysis.</p>
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16 pages, 401 KiB  
Review
Potato Processing Waste as a Reservoir of Bioactive Hydroxycinnamates: A Critical Review
by Dimitris P. Makris
Biomass 2025, 5(1), 2; https://doi.org/10.3390/biomass5010002 - 25 Dec 2024
Abstract
Natural resources are currently overexploited to provide food supply for the ever-increasing world population, and because of the intensification of agricultural and food production, there is a growing rate of waste generation. This waste biomass is usually dumped into landfills, causing unprecedented damage [...] Read more.
Natural resources are currently overexploited to provide food supply for the ever-increasing world population, and because of the intensification of agricultural and food production, there is a growing rate of waste generation. This waste biomass is usually dumped into landfills, causing unprecedented damage to ecosystems. Nowadays, circular economy strategies are channeled towards waste harnessing, aiming at reducing the irrational use of resources and minimizing waste generation. Potatoes are the second largest food crop after cereals, and there is an overwhelming amount of waste derived from potato tuber processing, composed almost exclusively of peels. Potato peels (PPs) are considered a source of polyphenolic compounds, largely represented by chlorogenic acid and other structurally related hydroxycinnamates, which possess a spectrum of bioactivities; however, there is a lack of analytical data compilations that could be of assistance in pertinent studies. With this as the conceptual basis, the scope of this review focused on a particular class of polyphenols, the so-called hydroxycinnamates, to deliver compiled data associated with the occurrence, retrieval, and application of this group of compounds derived from potato waste with major emphasis being given to PPs. It is believed that the collection of data of this nature, due to their undisputed significance in studies pertaining to bioeconomy, biorefinery, and food waste valorization, would provide a highly useful contribution to the field. Full article
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<p>Some major hydroxycinnamates that are frequently encountered in plant foods and their processing residues.</p>
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46 pages, 2616 KiB  
Review
Applications of Natural Polymers in the Grapevine Industry: Plant Protection and Value-Added Utilization of Waste
by Daniela-Ionela Toma (Sărdărescu), Doina Manaila-Maximean, Irina Fierascu, Anda Maria Baroi, Roxana Ioana Matei (Brazdis), Toma Fistos, Irina Elena Chican and Radu Claudiu Fierascu
Polymers 2025, 17(1), 18; https://doi.org/10.3390/polym17010018 - 25 Dec 2024
Abstract
The grapevine industry is confronted with challenges such as plant stress from environmental factors and microbial infections, alongside the need for sustainable waste management practices. Natural polymers offer promising solutions to these issues due to their biocompatibility, biodegradability, and functional versatility. This review [...] Read more.
The grapevine industry is confronted with challenges such as plant stress from environmental factors and microbial infections, alongside the need for sustainable waste management practices. Natural polymers offer promising solutions to these issues due to their biocompatibility, biodegradability, and functional versatility. This review explores the dual role of natural polymers in enhancing the grapevine industry: as protective agents against various stressors and as carriers for the delivery of valuable compounds recovered from grapevine wastes. We examine the use of natural polymers such as chitosan, alginate, and cellulose in formulating bio-based protective coatings and treatments that bolster plant resistance to abiotic stress, pathogens, and pests. Additionally, the review delves into the innovative utilization of grapevine residues, including skins, seeds, and stems, as sources of polyphenols and other bioactive compounds. These compounds can be efficiently encapsulated in natural polymer matrices for applications in agriculture, food, and pharmaceuticals. Key topics include the mechanisms of action, benefits, and limitations of natural polymer-based interventions, as well as case studies demonstrating their practical implementation in vineyards. The review also addresses future research directions, emphasizing the need for integrated approaches that enhance sustainability and economic viability in the grapevine industry. Full article
(This article belongs to the Special Issue Biodegradable and Natural Polymers, 2nd Edition)
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<p>Aspects of grapevine industry.</p>
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<p>Grapevine industry challenges to be addressed by research.</p>
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<p>Representation of grapevine wastes valorization workflow.</p>
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16 pages, 6561 KiB  
Article
Strategic Resource Extraction and Recycling from Waste: A Pathway to Sustainable Resource Conservation
by Inna Pitak, Anastasiia Sholokhova, Arūnas Baltušnikas and Rita Kriūkienė
Resources 2025, 14(1), 1; https://doi.org/10.3390/resources14010001 - 25 Dec 2024
Abstract
This study examines calcium extraction from Bottom Ash (BA) and the use of Solid Residue (SR) as a substitute for White Lump Clay (WLC) in brick production. Experimental analyses identified calcium and silicon as the main elements in BA, with 50% of calcium [...] Read more.
This study examines calcium extraction from Bottom Ash (BA) and the use of Solid Residue (SR) as a substitute for White Lump Clay (WLC) in brick production. Experimental analyses identified calcium and silicon as the main elements in BA, with 50% of calcium carbonate recovered through leaching. SR was a viable alternative to WLC in ceramic bricks, as SEM-EDS and FTIR analyses revealed changes in composition and microstructure. This approach promotes circular economy principles by recovering resources and reducing waste. Calcium extraction from BA can produce 29,000 tons of CaCO3 annually for industrial use, while substituting SR for WLC in brick production could replace 30% of clay, saving 1500 tons of clay and producing millions of bricks annually. Less than 50% of incinerated Municipal Solid Waste (MSW) would require landfilling. The process supports sustainable construction by conserving natural resources, reducing landfill waste, and lowering CO2 emissions. It offers annual cost savings of 2,639,250 USD and preserves 74,812.5 tons of resources through waste and clay reduction. By demonstrating a scalable model for waste valorization, this research aligns with global goals for sustainable development, resource efficiency, and ecological balance. Full article
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<p>Initial and post-leachate products: (<b>a</b>) bottom ash, (<b>b</b>) solid residue, (<b>c</b>) calcium carbonate.</p>
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<p>SEM-EDS analysis results: (<b>a</b>) bottom ash, (<b>b</b>) solid residue, and (<b>c</b>) calcium carbonate.</p>
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<p>XRD analysis results of the leaching process in I BA (initial), II solid residue and III CaCO<sub>3</sub>.</p>
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<p>SEM-EDS analysis of clay with mapping interpretation.</p>
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<p>X-ray powder diffraction analysis of clay.</p>
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<p>DTA and TGA curves of BA, SR and WLC.</p>
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<p>SEM-EDS analysis of clay bricks: (<b>a</b>,<b>b</b>)—samples fired at 1000 and 1100 °C. WLC—clay brick without SR; SR<sub>10%</sub>, SR<sub>20%</sub>, SR<sub>30%</sub>—clay bricks with 10%, 20%, and 30% SR.</p>
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<p>FTIR of ceramic clay bodies with varying SR content fired at 1000 °C and 1100 °C.</p>
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<p>Physical and mechanical properties of clay brick samples after firing.</p>
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<p>Isotherm curves for the sample WLC fired at 1000 and 1100 °C (<b>a</b>) and BET summary for samples (<b>b</b>).</p>
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<p>Porosize distribution of fired samples (<b>a</b>) 1000 °C, (<b>b</b>) 1100 °C.</p>
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35 pages, 2056 KiB  
Review
Review of Reforming Processes for the Production of Green Hydrogen from Landfill Gas
by Dhruv Singh, Piero Sirini and Lidia Lombardi
Energies 2025, 18(1), 15; https://doi.org/10.3390/en18010015 - 24 Dec 2024
Abstract
The growing challenges of climate change, the depletion of fossil fuel reserves, and the urgent need for carbon-neutral energy solutions have intensified the focus on renewable energy. In this perspective, the generation of green hydrogen from renewable sources like biogas/landfill gas (LFG) offers [...] Read more.
The growing challenges of climate change, the depletion of fossil fuel reserves, and the urgent need for carbon-neutral energy solutions have intensified the focus on renewable energy. In this perspective, the generation of green hydrogen from renewable sources like biogas/landfill gas (LFG) offers an intriguing option, providing the dual benefits of a sustainable hydrogen supply and enhanced waste management through energy innovation and valorization. Thus, this review explores the production of green hydrogen from biogas/LFG through four conventional reforming processes, specifically dry methane reforming (DMR), steam methane reforming (SMR), partial oxidation reforming (POX), and autothermal reforming (ATR), focusing on their mechanisms, operating parameters, and the role of catalysts in hydrogen production. This review further delves into both the environmental aspects, specifically GWP (CO2 eq·kg−1 H2) emissions, and the economic aspects of these processes, examining their efficiency and impact. Additionally, this review also explores hydrogen purification in biogas/LFG reforming and its integration into the CO2 capture, utilization, and storage roadmap for net-negative emissions. Lastly, this review highlights future research directions, focusing on improving SMR and DMR biogas/LFG reforming technologies through simulation and modeling to enhance hydrogen production efficiency, thereby advancing understanding and informing future research and policy initiatives for sustainable energy solutions. Full article
(This article belongs to the Special Issue Biomass, Biofuels and Waste: 3rd Edition)
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<p>Number of papers published throughout the year (2015–2024).</p>
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<p>Process flow diagram steam methane reforming.</p>
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<p>Process flow diagram of dry methane reforming.</p>
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<p>Process flow diagram of partial oxidation process.</p>
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<p>Process flow diagram of methane autothermal reforming.</p>
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20 pages, 1277 KiB  
Article
Harnessing Livestock and Vineyard Residues for Sustainable Energy Production in Portugal
by Miguel Oliveira, Fernando Hermínio Ferreira Milheiro Nunes and Amadeu Duarte da Silva Borges
Clean Technol. 2025, 7(1), 1; https://doi.org/10.3390/cleantechnol7010001 - 24 Dec 2024
Abstract
This study investigates the potential of utilizing livestock waste and vineyard residues for sustainable energy production in Portugal. Through the physical and chemical characterization of swine waste, grape seeds and skins, cork powder, sawdust, and biochar, 53 distinct samples, including 11 individual biomasses [...] Read more.
This study investigates the potential of utilizing livestock waste and vineyard residues for sustainable energy production in Portugal. Through the physical and chemical characterization of swine waste, grape seeds and skins, cork powder, sawdust, and biochar, 53 distinct samples, including 11 individual biomasses and their derived mixtures, were analyzed to identify optimal combinations for biofuel pellet production. The best-performing mixture, composed of 50% swine waste, 25% grape seeds and skins, and 25% cork powder, achieved a Lower Heating Value (LHV) of 18.34 MJ/kg and low ash content, qualifying it as a class B pellet. This mixture offers significant energy potential while minimizing environmental impacts. The research also presents three energy valorization scenarios, with the most balanced scenario meeting up to 6% of Portugal’s electricity demand and providing energy savings equivalent to 485,463 tons of oil equivalent (toe) annually. A case study on a “Case Study Farm” in the Douro region, managing 2000 pigs and producing 500 tons of wine grapes annually, demonstrated that implementing the optimal biomass mixture could generate 3854 MWh of heat and 1156 MWh of electricity per year. This could result in annual revenues of EUR 189,258 from pellet sales, covering the initial investment of EUR 283,938 within 6.36 years, with a total surplus of EUR 689,666 over 20 years. These findings highlight the economic viability and environmental benefits of converting agricultural waste into renewable energy, contributing to Portugal’s carbon neutrality and reducing energy dependence. Full article
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<p>(<b>A</b>) Projection of the variables on the factor-plane (1 × 2); (<b>B</b>) projection of the cases on the factor-plane (1 × 2); (<b>C</b>) tree diagram for 53 cases.</p>
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<p>Pareto chart of t-values for coefficients.</p>
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<p>Representativity of renewable energy sources in total primary energy consumption in Portugal.</p>
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16 pages, 3833 KiB  
Article
Sequential Solid-State and Submerged Fermentation to Increase Yarrowia lipolytica Lipase Production from Palm Oil Production Chain By-Products
by Camila P. L. Souza, Adejanildo da S. Pereira, Érika C. G. Aguieiras and Priscilla F. F. Amaral
Fermentation 2025, 11(1), 3; https://doi.org/10.3390/fermentation11010003 - 24 Dec 2024
Abstract
This study investigates the potential of sequential solid-state and submerged fermentation (SeqF) to enhance lipase production by Yarrowia lipolytica using by-products from the palm oil production chain. Palm fiber and palm oil deodorizer distillate (PODD) were utilized as substrates in both fermentation stages. [...] Read more.
This study investigates the potential of sequential solid-state and submerged fermentation (SeqF) to enhance lipase production by Yarrowia lipolytica using by-products from the palm oil production chain. Palm fiber and palm oil deodorizer distillate (PODD) were utilized as substrates in both fermentation stages. Solid-state fermentation (SSF) yielded significant lipase activity when palm fiber was used alone (1.55 U/g in 48 h), while submerged fermentation (SmF) showed improved enzymatic production with the combination of fiber and PODD (1171 U/L in 72 h). The integration of SSF and SmF in SeqF achieved superior lipase activities, reaching 4464.5 U/L, an 8.3-fold increase compared to SmF alone, in Erlenmeyer flasks. SeqF-lyophilized biocatalysts from Erlenmeyer experiments showed better hydrolytic activity (131 U/g) when the best conditions were reproduced in a 4 L bioreactor (33 U/g). The SeqF-lyophilized biocatalyst was employed in esterification reactions to synthesize mono- and diacylglycerols, achieving a 24.3% conversion rate. The study highlights SeqF as a promising and sustainable approach for valorizing agro-industrial residues, contributing to biocatalyst production and advancing circular bioeconomy initiatives. Full article
(This article belongs to the Special Issue Fermentation of Organic Waste for High-Value-Added Product Production)
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<p>Palm oil deodorizer distillate (PODD) (<b>a</b>) and palm fiber (<b>b</b>).</p>
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<p>Schematic representation for determining the hydrolysis activity of <span class="html-italic">Yarrowia lipolytica</span> lipase.</p>
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<p>Erlenmeyer flask with palm fiber for solid-state fermentation (<b>a</b>) and palm fiber with palm oil deodorizer distillate (PODD) after sterilization (<b>b</b>).</p>
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<p>Lipase production by <span class="html-italic">Yarrowia lipolytica</span> during solid-state fermentation in 500 mL Erlenmeyer flasks containing 10 g of palm fiber with or without 1.5% (<span class="html-italic">w</span>/<span class="html-italic">w</span>) of palm oil deodorizer distillate (PODD) and moisture content adjusted with water or YP* medium. (<b>a</b>) Lipase production kinetic profile; (<b>b</b>) statistical difference observed in 48 h of fermentation—a–c, mean values with different letters differ from each other with a 95% confidence level by Turkey’s test.</p>
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<p>Lipase production by <span class="html-italic">Yarrowia lipolytica</span> during solid-state fermentation in 500 mL Erlenmeyer flasks containing 10 g of palm fiber and moisture content adjusted with YP* medium.</p>
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<p>Lipase activity during growth of <span class="html-italic">Yarrowia lipolytica</span> in submerged fermentation in 1 L stirred flasks containing 200 mL of YP* medium (control) and YP* medium with PODD, YP* medium with palm fiber, and YP* medium with PODD and fiber.</p>
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<p>Lipase production by <span class="html-italic">Yarrowia lipolytica</span> during sequential solid-state and submerged fermentation (SeqF) in 500 mL flasks containing 10 g of palm fiber with or without 1.5% of PODD, with the addition of 200 mL of YP medium after 72 h. SSF: solid-state fermentation stage of SeqF; SmF: submerged fermentation stage of SeqF.</p>
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<p>Lipase production by <span class="html-italic">Yarrowia lipolytica</span> during sequential solid-state and submerged fermentation (SeqF) in 500 mL flasks containing 10 g of palm fiber with or without 1.5% of PODD, with the addition of 200 mL of YP medium after 24 h. SSF: solid-state fermentation stage of SeqF; SmF: submerged fermentation stage of SeqF.</p>
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<p>Lipase activity of lyophilized biocatalysts (fermented fiber (Fiber), the centrifuged fermented medium (Supernatant), and the fermented fiber + the fermented medium (Fiber + supern.)) obtained during sequential solid-state and submerged fermentation (SeqF) in 500 mL flasks containing 10 g of palm fiber, with the addition of 200 mL of YP medium after 24 h. Fractions obtained after 24 h (only SSF), 48 h (SSF 24 h + SmF 24 h), and 72 h (SSF 24 h + SmF 48 h).</p>
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<p>Sequential solid-state and submerged fermentation (SeqF) in 4 L bioreactor with 150 g of palm fiber with the addition of 3 L of YP medium after 24 h. SSF: solid-state fermentation stage of SeqF (<b>a</b>); SmF: submerged fermentation stage of SeqF (<b>b</b>).</p>
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<p>Conversion of glycerol and oleic acid using lyophilized biocatalysts from SeqF performed in bioreactor using <span class="html-italic">Yarrowia lipolytica</span> (the centrifuged fermented medium (Supernatant) and the fermented fiber + the fermented medium (Fiber + supern.) obtained after 72 h in SeqF) and a commercial <span class="html-italic">Candida rugosa</span> lipase in 125 mL flasks for 72 h. Molar ratio of glycerol/oleic acid was 6:1, and 10% of water (<span class="html-italic">w</span>/<span class="html-italic">w</span>) was used.</p>
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16 pages, 3525 KiB  
Article
Digitization and Virtualization of Wood Products for Its Commercial Use
by Ladislav Odstrčil, Peter Valent, Vladislav Kaputa and Marek Fabrika
Forests 2024, 15(12), 2263; https://doi.org/10.3390/f15122263 - 23 Dec 2024
Abstract
Augmented reality (AR) offers several advantages in the commercialization of wood products, increasing both the efficiency and the attractiveness of the process of presenting and selling them. The digitization and virtualization of wood features/products for the purpose of their economic valorization represent a [...] Read more.
Augmented reality (AR) offers several advantages in the commercialization of wood products, increasing both the efficiency and the attractiveness of the process of presenting and selling them. The digitization and virtualization of wood features/products for the purpose of their economic valorization represent a significant advance in technology and its application in traditional industries such as wood processing and trade. We present a concrete process of digitization and virtualization of wood features through AR for the purpose of its commercial valorization. Three methods of object scanning are tested: convergent photogrammetry, LiDAR scanning using an iPhone, and handheld scanners. Wood samples with different textures, shapes, and surface properties were used for the research, while each method was tested on a trio of models. The methods showed specific limitations: convergent photogrammetry is time-consuming and prone to human error, LiDAR iPhone scanning provides lower output quality and struggles with reflective surfaces, while handheld scanners are expensive and require additional tools for capturing color. Convergent photogrammetry was evaluated as the optimal and available method for the widest range of users. The 3D models were integrated into the Virtual Wood Market application, created in the Unreal Engine environment. The use of augmented reality in wood product commercialization offers significant benefits, including enhanced material efficiency, improved design and fabrication processes, better supply chain management, and increased customer engagement. These advantages can lead to more sustainable practices and higher customer satisfaction, ultimately driving the success of wood product commercialization. Full article
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<p>The resulting 3D models created by the Lidar method showing medium model and texture quality compensated by ease of this method.</p>
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<p>The resulting 3D models created by the convergent photogrammetry method representing detailed models at cost of higher demands on processing skills.</p>
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<p>The resulting 3D models created by the structured illumination method producing highly detailed 3D models. Lack of color is caused by absence of color sensor.</p>
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<p>Flowchart of the process of environment scanning, image recognition, and 3D model display in AR.</p>
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<p>Virtual Wood Market home screen.</p>
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<p>Virtual Wood Market application structure.</p>
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<p>Manipulating the model in augmented reality on the basis of a printed leaflet.</p>
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<p>(<b>a</b>)—screen of the catalog of available products, (<b>b</b>)—screen of the selected item from the catalog, (<b>c</b>)—augmented reality view, (<b>d</b>)—model displayed on the Sketchfab platform.</p>
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19 pages, 3151 KiB  
Article
Catalyst-Free Depolymerization of Methanol-Fractionated Kraft Lignin to Aromatic Monomers in Supercritical Methanol
by Shubho Ghosh, Masud Rana and Jeong-Hun Park
Energies 2024, 17(24), 6482; https://doi.org/10.3390/en17246482 - 23 Dec 2024
Abstract
Lignin is considered a renewable source for the production of valuable aromatic chemicals and liquid fuel. Solvent depolymerization of lignin is a fruitful strategy for the valorization of lignin. However, Kraft lignin is highly prone to produce char (a by-product) during the hydrothermal [...] Read more.
Lignin is considered a renewable source for the production of valuable aromatic chemicals and liquid fuel. Solvent depolymerization of lignin is a fruitful strategy for the valorization of lignin. However, Kraft lignin is highly prone to produce char (a by-product) during the hydrothermal depolymerization process due to its poor solubility in organic solvents. Therefore, the minimization of char formation remains challenging. The purpose of the present study was to fractionate Kraft lignin in methanol to obtain low-molecular-weight fractions that could be further depolymerized in supercritical methanol to produce aromatic monomers and to suppress char formation. The results showed that the use of methanol-soluble lignin achieved a bio-oil yield of 45.04% and a char yield of 39.6% at 280 °C for 2 h compared to 28.57% and 57.73%, respectively, when using raw Kraft lignin. Elemental analysis revealed a high heating value of 30.13 MJ kg−1 and a sulfur content of only 0.09% for the bio-oil derived from methanol-soluble lignin. The methanol extraction process reduced the oxygen content and increased the hydrogen and carbon contents in the modified lignin and bio-oil, indicating that the extracted lignin fraction had an enhanced deoxygenation capability and a higher energy content. These findings highlight the potential of methanol-soluble Kraft lignin as a valuable resource for sustainable energy production and the production of aromatic compounds. Full article
(This article belongs to the Special Issue Cutting-Edge Developments in Waste-to-Energy Technologies)
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<p>Preparation of methanol-soluble lignin from raw Kraft lignin.</p>
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<p>Lignin depolymerization and bio-oil separation processes.</p>
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<p>FT-IR analysis of (A) raw Kraft lignin and (B) methanol-soluble Kraft lignin.</p>
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<p>Yields of depolymerized products obtained after hydrothermal liquefaction of methanol-soluble Kraft lignin in supercritical methanol under different (<b>A</b>) temperatures and (<b>B</b>) reaction times.</p>
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<p>Yields of depolymerized products obtained after hydrothermal liquefaction of raw Kraft lignin and methanol-soluble Kraft lignin in supercritical methanol at 280 °C after 2 h.</p>
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<p>Yields of major compounds obtained from raw Kraft lignin and methanol-soluble lignin depolymerization at 280 °C after 2 h.</p>
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<p>(<b>A</b>) FT-IR analysis of bio-oil obtained from methanol-soluble Kraft lignin with a reaction time of 2 h and temperatures of (a) 260 °C, (b) 280 °C, (c) 300 °C, and (d) 320 °C. (<b>B</b>) FT-IR analysis of bio-oil obtained from methanol-soluble Kraft lignin at a temperature of 280 °C and reaction times of (a) 1 h, (b) 2 h, (c) 3 h, and (d) 4 h.</p>
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<p>Van Krevelen diagrams of Kraft lignin, methanol-soluble Kraft lignin, and bio-oil. (<b>A</b>) O/C vs. H/C and (<b>B</b>) S/C vs. H/C ratios for Kraft lignin (a and a′), methanol-soluble Kraft lignin (b and b′), bio-oil obtained from Kraft lignin at 280 °C and 2 h (c and c′), and bio-oil obtained from methanol-soluble Kraft lignin at 260 °C and 2 h (d and d′), 280 °C and 1 h (e and e′), 280 °C and 2 h (f and f′), and 280 °C and 4 h (g and g′).</p>
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<p>Plausible decomposition pathway for methanol-soluble Kraft lignin in supercritical methanol.</p>
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16 pages, 4164 KiB  
Article
Hydrogenolysis of Benzyl Phenyl Ether Using Nickel–Molybdenum Clay Catalysts—A Model for Cleaving Ether Linkages in Lignin
by Indri B. Adilina, Muhammad A. Fitriady, Ferensa Oemry, Fauzan Aulia, Nino Rinaldi, Gagus K. Sunnardianto, Ian P. Silverwood and Stewart F. Parker
Catalysts 2024, 14(12), 953; https://doi.org/10.3390/catal14120953 - 23 Dec 2024
Abstract
The solvent-free hydrogenolysis (HDL) of benzyl phenyl ether (BPE), a model for the C–O (α-O-4) linkage in lignin, was investigated using NiMo-pillared clay catalysts in their reduced (NiMoPR) and sulfided (NiMoPS) forms. NiMoPS show higher activity and selectivity to give an equimolar mixture [...] Read more.
The solvent-free hydrogenolysis (HDL) of benzyl phenyl ether (BPE), a model for the C–O (α-O-4) linkage in lignin, was investigated using NiMo-pillared clay catalysts in their reduced (NiMoPR) and sulfided (NiMoPS) forms. NiMoPS show higher activity and selectivity to give an equimolar mixture of toluene and phenol, demonstrating selective cleavage of the Caliphatic–O of BPE, while non-equimolar amounts were found for NiMoPR. Strong acid sites are dominant in NiMoPS, giving a higher total acidity compared to NiMoPR, which explains the higher selectivity of the sulfided catalyst towards the HDL products and monomeric aromatics. To understand the interaction of BPE on the catalyst surface, we carried out a comprehensive investigation of the 2D potential energy surface (PES) of BPE and the vibrational spectra using neutron scattering and computational studies. The results suggest that BPE is weakly adsorbed on NiMoPS and the pillared clay support (PILC) via a van der Waals or H-bonding interaction, but they are strongly chemisorbed on the NiMoPR due to covalent bonding. Weakly adsorbed BPE allows higher mobility during diffusion to the catalytic site, which promotes the higher activity of NiMoPS for the HDL. This work demonstrates the potential use of clay-supported NiMo catalysts for lignin valorization and the future circular economy. Full article
(This article belongs to the Section Biomass Catalysis)
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<p>NH<sub>3</sub>-TPD profiles for (<b>a</b>) BT clay, (<b>b</b>) PILC, (<b>c</b>) NiMoPO, (<b>d</b>) NiMoPR, and (<b>e</b>) NiMoPS.</p>
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<p>HRTEM images (<b>a</b>,<b>c</b>) at two different locations and their respective slab length distributions (<b>b</b>,<b>d</b>) of the NiMoPS catalyst.</p>
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<p>Two-dimensional PES of BPE.</p>
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<p>Comparison of observed and calculated (<b>a</b>) infrared and (<b>b</b>) INS spectra of BPE. In each case, the experimental spectrum is in the middle, with the C<sub>s</sub> and C<sub>1</sub> conformers above and below it, respectively.</p>
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<p>INS spectra of BPE adsorbed on the catalysts: (<b>a</b>) PILC, (<b>b</b>) NiMoPR, and (<b>c</b>) NiMoPS.</p>
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<p>Schematic illustration of possible BPE configurations interacting with (<b>a</b>) PILC, (<b>b</b>) NiMoPR, and (<b>c</b>) NiMoPS.</p>
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<p>(<b>a</b>) Raw and (<b>b</b>) normalized elastic window scan of all the samples.</p>
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<p>Reaction pathway contributing to the HDL of BPE using NiMo-PILC catalysts.</p>
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23 pages, 3549 KiB  
Article
Experimental Assessment of Green Waste HTC Pellets: Kinetics, Efficiency and Emissions
by Yaniel Garcia Lovella, Abhishek Goel, Louis Garin, Julien Blondeau and Svend Bram
Energies 2024, 17(24), 6474; https://doi.org/10.3390/en17246474 - 23 Dec 2024
Abstract
The combustion of renewable solid fuels, such as biomass, is a reliable option for heat and power production. The availability of biomass resources within urban areas, such as tree leaves, small branches, grass, and other green city waste, creates an opportunity to valorize [...] Read more.
The combustion of renewable solid fuels, such as biomass, is a reliable option for heat and power production. The availability of biomass resources within urban areas, such as tree leaves, small branches, grass, and other green city waste, creates an opportunity to valorize such resources. The energy densification of such resources using hydrothermal carbonization (HTC) and pelletization of the carbonized material could create a new generation of domestic boiler biofuel. However, combustion efficiency and emission assessments should be carried out for HTC pellets. The primary objective of this study is to assess HTC pellets, provided by a waste upgrade company, in terms of kinetics, combustion efficiency, and emissions, taking as reference base ENplus A1 certified softwood pellets. Therefore, thermogravimetric analysis and combustion tests were conducted for both fuels to achieve this. It was observed that a third peak of the burning rate during the solid carbon oxidation of HTC pellets indicated a high activation energy. Combustion tests showed a 7% increase in boiler efficiency for HTC pellets compared to softwood pellets. However, higher particulate matter (PM), NOx, and CO emissions were recorded during the HTC pellets test. The results suggest that optimizing the air/fuel ratio could further improve the performance of HTC pellets in domestic boilers. Full article
(This article belongs to the Section B: Energy and Environment)
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<p>Scheme of equipment for measuring particulate and gaseous emissions. Source: taken from [<a href="#B27-energies-17-06474" class="html-bibr">27</a>] and modified by the authors.</p>
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<p>Thermal degradation of softwood pellets: (<b>a</b>) The derivative of thermogravimetry (DTG) analysis. (<b>b</b>) Thermogravimetry analysis (TGA).</p>
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<p>Thermal degradation of HTC pellets: (<b>a</b>) The derivative of thermogravimetry (DTG) analysis. (<b>b</b>) Thermogravimetry analysis (TGA).</p>
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<p>Fitting curve for reaction stages of softwood pellets: (<b>a</b>) temperature range from 197 °C to 357 °C and (<b>b</b>) temperature range from 357 °C to 500 °C.</p>
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<p>Fitting curve for reaction stages of HTC pellets (<b>a</b>) temperature range from 212 °C to 322 °C, (<b>b</b>) temperature range from 322 °C to 477 °C and (<b>c</b>) temperature range from 622 °C to 687 °C.</p>
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<p>Boiler efficiency (direct method) and combustion efficiency (calculated from the indirect method and using the empirical method).</p>
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<p>State of bottom ash at the end of the tests: (<b>a</b>) HTC pellets; (<b>b</b>) softwood pellets.</p>
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<p>Emission factor for softwood and HTC pellets.</p>
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<p>Emissions factor of softwood and HTC pellets for PM<sub>2.5</sub>.</p>
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<p>Particle number distribution and distribution of cumulative particle diameter. PNSD: particle number size distribution, and CD: cumulative distribution.</p>
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<p>Particle-number size distribution (PNSD) versus average particle’s diameter in logarithm coordinate.</p>
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26 pages, 1699 KiB  
Review
Marine Invasive Algae’s Bioactive Ingredients as a Sustainable Pathway in Cosmetics: The Azores Islands as a Case Study
by Marta Matos, Luísa Custódio and Catarina Pinto Reis
Mar. Drugs 2024, 22(12), 575; https://doi.org/10.3390/md22120575 - 23 Dec 2024
Abstract
Marine invasive species pose significant ecological, economic, and social challenges, disrupting native ecosystems, outcompeting local species and altering biodiversity. The spread of these species is largely driven by global trade, shipping, and climate change, which allow non-native species to establish themselves in new [...] Read more.
Marine invasive species pose significant ecological, economic, and social challenges, disrupting native ecosystems, outcompeting local species and altering biodiversity. The spread of these species is largely driven by global trade, shipping, and climate change, which allow non-native species to establish themselves in new environments. Current management strategies, including early detection, rapid response, and biosecurity measures, have had some success, but the complexity and scale of the problem require continuous monitoring. This review explores the possibility of using some marine invasive species as skincare ingredients and explores the Azorean islands as a case study for the valorization of biomass. Additionally, this review addresses legislative barriers that delay the development of sustainable cosmetic markets from invasive species, highlighting the regulatory landscape as a critical area. It concludes that marine invasive species present a regional and global problem that requires regional and global solutions. Such solutions strongly need to address environmental impacts and net socioeconomic benefits, but such solutions must also consider all regional differences, technical capacities and financial resources available. Thus, as a future perspective, strategies should emphasize the need for international collaboration and the development of more effective policies to prevent the spread of invasive species. There is still much work to be completed. By working together, the biodiversity for future generations will be better monitored and explored. Full article
(This article belongs to the Special Issue Marine Algal Biotechnology and Applications)
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<p>Number of publications in Google Scholar using “algae biomass cosmetics” as keywords, from 2019 to 2024 (incomplete year).</p>
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<p>Genera with most reported invasive taxa, as reviewed by Thomsen et al. [<a href="#B12-marinedrugs-22-00575" class="html-bibr">12</a>], and their described uses and impacts [<a href="#B27-marinedrugs-22-00575" class="html-bibr">27</a>,<a href="#B28-marinedrugs-22-00575" class="html-bibr">28</a>,<a href="#B29-marinedrugs-22-00575" class="html-bibr">29</a>,<a href="#B30-marinedrugs-22-00575" class="html-bibr">30</a>,<a href="#B31-marinedrugs-22-00575" class="html-bibr">31</a>,<a href="#B32-marinedrugs-22-00575" class="html-bibr">32</a>,<a href="#B33-marinedrugs-22-00575" class="html-bibr">33</a>,<a href="#B34-marinedrugs-22-00575" class="html-bibr">34</a>,<a href="#B35-marinedrugs-22-00575" class="html-bibr">35</a>,<a href="#B36-marinedrugs-22-00575" class="html-bibr">36</a>]. <span class="html-italic">Polysiphonia</span> image by Bárbara Ignacio, available under a Creative Commons Attribution-Noncommercial-Share Alike 4.0 License [<a href="#B37-marinedrugs-22-00575" class="html-bibr">37</a>] at [<a href="#B38-marinedrugs-22-00575" class="html-bibr">38</a>]. <span class="html-italic">Hypnea</span> image reproduced with permission from Olivier De Clerck, published by AlgaeBase [<a href="#B39-marinedrugs-22-00575" class="html-bibr">39</a>]. <span class="html-italic">Codium</span> image by Manuela Lopes, published by “Casa das Ciências”, available under a Creative Commons Attribution-Noncommercial-Share Alike 4.0 License [<a href="#B37-marinedrugs-22-00575" class="html-bibr">37</a>] at [<a href="#B40-marinedrugs-22-00575" class="html-bibr">40</a>]. <span class="html-italic">Gracilaria</span> image by António Palmeira, published by OMARE, available under a Creative Commons Attribution-Noncommercial 4.0 License at [<a href="#B41-marinedrugs-22-00575" class="html-bibr">41</a>]. <span class="html-italic">Caulerpa</span> image reproduced with permission from the Australian Institute of Marine Science, published by New Zealand Marine Biosecurity [<a href="#B42-marinedrugs-22-00575" class="html-bibr">42</a>].</p>
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<p>Typical species found in the Azorean intertidal area. Captured on 21 April 2024 at (<b>a</b>) Atalhada, (<b>b</b>) Cerco da Caloura and (<b>c</b>) Porto da Caloura, all in São Miguel, Azores.</p>
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<p>Accumulation of dried algae in the Caloura bathing site and in the Caloura port. Captured on 21 April 2024.</p>
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<p><span class="html-italic">Rugulopteryx okamurae</span> accumulation at Prainha de Água d’Alto. Captured on 21 April 2024.</p>
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14 pages, 280 KiB  
Review
Valorizing Grape Pomace: A Review of Applications, Nutritional Benefits, and Potential in Functional Food Development
by Vladimir S. Kurćubić, Nikola Stanišić, Slaviša B. Stajić, Marko Dmitrić, Saša Živković, Luka V. Kurćubić, Vladimir Živković, Vladimir Jakovljević, Pavle Z. Mašković and Jelena Mašković
Foods 2024, 13(24), 4169; https://doi.org/10.3390/foods13244169 - 23 Dec 2024
Abstract
Grape pomace (GP), a byproduct of winemaking, has gained significant attention as a sustainable and functional ingredient with applications in the food and nutraceutical industries. This review examines the potential of GP in meat products and analogs, functional foods, and nutraceuticals, highlighting its [...] Read more.
Grape pomace (GP), a byproduct of winemaking, has gained significant attention as a sustainable and functional ingredient with applications in the food and nutraceutical industries. This review examines the potential of GP in meat products and analogs, functional foods, and nutraceuticals, highlighting its composition, health benefits, and role in enhancing nutritional and functional properties. Rich in dietary fiber, polyphenols, essential fatty acids, and bioactive compounds, GP exhibits antioxidant, anti-inflammatory, and gut health-promoting effects, making it suitable for various food applications. Its incorporation into meat products, such as sausages and patties, improves texture, enhances shelf life, and increases nutritional value while reducing the environmental footprint. GP is also effective in functional foods such as baked goods, dairy and plant-based yoghurts, smoothies, and snack bars, where it can enrich fiber and polyphenol content, aid in satiety, and provide health benefits beyond basic nutrition. The challenge is how to maintain the sensory properties characteristic of conventional, unmodified products. In nutraceuticals, GP’s polyphenolic compounds and dietary fiber support antioxidant, anti-inflammatory, and metabolic health functions, with applications as antioxidant supplements, gut health boosters, weight management aids, and cardiovascular health supplements. Despite challenges such as taste modification and optimizing bioavailability, GP’s versatility and sustainability highlight its value in developing innovative, health-oriented products. This review emphasizes the promise of GP as a valuable ingredient in functional foods and nutraceutical formulations, contributing to health, sustainability, and resource efficiency. Full article
(This article belongs to the Special Issue Latest Research on Flavor Components and Sensory Properties of Food)
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