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	<title>bio-based chemical synthesis &#8211; Science</title>
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		<title>Wheat Straw Hydrolysate Converted to Succinic Acid via Bacterial Fermentation</title>
		<link>https://scienmag.com/wheat-straw-hydrolysate-converted-to-succinic-acid-via-bacterial-fermentation/</link>
		
		<dc:creator><![CDATA[Alan Morgan]]></dc:creator>
		<pubDate>Sun, 06 Sep 2026 17:32:35 +0000</pubDate>
				<category><![CDATA[Technology and Engineering]]></category>
		<category><![CDATA[Actinobacillus succinogenes fermentation]]></category>
		<category><![CDATA[agricultural waste biorefinery]]></category>
		<category><![CDATA[bacterial fermentation of agricultural waste]]></category>
		<category><![CDATA[bacterial fermentation of lignocellulosic biomass]]></category>
		<category><![CDATA[bio-based chemical synthesis]]></category>
		<category><![CDATA[bio-based succinic acid production]]></category>
		<category><![CDATA[biobased chemicals from agricultural waste]]></category>
		<category><![CDATA[bioeconomy feedstock utilization]]></category>
		<category><![CDATA[bioeconomy waste valorization]]></category>
		<category><![CDATA[detoxification of wheat straw hydrolysate]]></category>
		<category><![CDATA[optimization of fermentation processes]]></category>
		<category><![CDATA[overcoming toxic compounds in biomass conversion]]></category>
		<category><![CDATA[overcoming toxic compounds in biomass fermentation]]></category>
		<category><![CDATA[renewable polymer precursors]]></category>
		<category><![CDATA[second-generation bioeconomy feedstock]]></category>
		<category><![CDATA[second-generation biorefineries]]></category>
		<category><![CDATA[succinic acid production from wheat straw]]></category>
		<category><![CDATA[sustainable bioplastics manufacturing]]></category>
		<category><![CDATA[sustainable biorefinery processes]]></category>
		<category><![CDATA[valorization of crop residues]]></category>
		<category><![CDATA[Wheat straw biomass conversion]]></category>
		<category><![CDATA[wheat straw hydrolysate detoxification]]></category>
		<guid isPermaLink="false">https://scienmag.com/wheat-straw-hydrolysate-converted-to-succinic-acid-via-bacterial-fermentation/</guid>

					<description><![CDATA[Every year, global agriculture generates hundreds of millions of tonnes of wheat straw, a fibrous residue that is often burned or left to decompose, releasing carbon back into the atmosphere without yielding anything of value. A team of researchers from the Technical University of Denmark, the Italian National Agency for New Technologies, Energy and Sustainable [&#8230;]]]></description>
										<content:encoded><![CDATA[<p>Every year, global agriculture generates hundreds of millions of tonnes of wheat straw, a fibrous residue that is often burned or left to decompose, releasing carbon back into the atmosphere without yielding anything of value. A team of researchers from the Technical University of Denmark, the Italian National Agency for New Technologies, Energy and Sustainable Economic Development (ENEA), and the University of Naples Federico II now reports a way to turn this abundant agricultural waste into succinic acid, one of the most sought-after building blocks of the emerging bioeconomy. Their study, published in the journal Waste and Biomass Valorization, demonstrates that careful adjustment of the fermentation medium can coax a bacterium called Actinobacillus succinogenes into converting non-detoxified wheat straw hydrolysate into biobased succinic acid at concentrations and yields that substantially outperform previous efforts with the same feedstock. The finding is significant because it sidesteps one of the most persistent obstacles in second-generation biorefineries: the toxic compounds that steam explosion pretreatment inevitably leaves behind in the sugar-rich broth.</p>
<p>Succinic acid is a four-carbon dicarboxylic acid that occupies a central position on most lists of top-value biobased chemicals. It serves as the precursor to polybutylene succinate, a biodegradable polyester used in packaging and agricultural films, and finds applications in pharmaceuticals, food additives, and resins. Traditionally it has been manufactured from petrochemical feedstocks, most commonly through the hydrogenation of maleic anhydride, but the drive to decarbonize the chemical industry has intensified interest in microbial fermentation as a greener route. Among the natural succinate producers, Actinobacillus succinogenes stands out. The bacterium fixes carbon dioxide into its product through the reductive branch of the tricarboxylic acid cycle, meaning the process can actually consume the greenhouse gas while it builds the acid. It is also remarkably promiscuous in its diet, capable of metabolizing pentoses such as xylose and arabinose alongside hexoses like glucose, galactose, mannose and fructose, as well as disaccharides and sugar alcohols. That metabolic breadth makes it a natural candidate for lignocellulosic hydrolysates, whose sugar profiles vary widely depending on the biomass and pretreatment used.</p>
<p>The problem lies in what else those hydrolysates contain. To liberate fermentable sugars from wheat straw, the researchers milled the material and subjected it to acid-catalyzed steam explosion at 203 degrees Celsius for five minutes at the ENEA Research Centre of Trisaia in southern Italy, followed by enzymatic hydrolysis with a Cellic Ctec2 preparation. This treatment efficiently breaks down the cellulose and hemicellulose fractions, which make up roughly 34 to 40 percent and 21 to 26 percent of the straw respectively, but it also generates a cocktail of microbial poisons: furfural, 5-hydroxymethylfurfural, phenolic derivatives, and acetic acid. These compounds disrupt redox balance, compromise membrane integrity and interfere with intracellular pH homeostasis. Earlier work by some of the same Italian researchers showed that even highly diluted wheat straw hydrolysate could suppress the growth of A. succinogenes by around 60 percent. Conventional responses, such as overliming, activated carbon adsorption or ion-exchange treatment, can remove the inhibitors, but they add cost, complexity and sugar losses to the process. The Danish-Italian team instead asked a different question: could the right combination of nutrients and buffering agents allow the bacterium to ferment the hydrolysate as it is, toxins included?</p>
<p>To answer it, the researchers designed a factorial experiment varying three parameters simultaneously: the fraction of hydrolysate in the fermentation medium, the concentration of yeast extract as a nitrogen source, and the amount of magnesium carbonate. Batch fermentations were run in sealed anaerobic bottles at 37 degrees Celsius with carbon dioxide sparging, using a 10 percent inoculum of A. succinogenes strain 130Z grown to exponential phase. The hydrolysate stock had been diluted 1:5 with sterile water before use, and the tested media contained 50, 70 or 90 percent of that stock, delivering initial total sugar concentrations ranging from 13.5 to 24.4 grams per litre, with glucose dominating over xylose. Yeast extract was tested at 10 and 25 grams per litre, and magnesium carbonate at 30 and 60 grams per litre. Magnesium carbonate plays a triple role in succinate fermentations: it buffers the broth against acidification, supplies dissolved inorganic carbon through the carbonate-bicarbonate equilibrium to feed the carboxylation reactions of the reductive TCA pathway, and provides magnesium ions required for the activity of phosphoenolpyruvate carboxykinase, a key enzyme of the succinate route.</p>
<p>The results revealed a nuanced interplay between the three variables. When the more diluted 50 percent hydrolysate was used, the different combinations of yeast extract and magnesium carbonate made little statistical difference, because the low sugar concentration itself was the limiting factor, capping succinic acid titers at roughly 5.9 grams per litre. The picture changed dramatically with the concentrated 90 percent hydrolysate. The best-performing condition combined 10 grams per litre of yeast extract with 60 grams per litre of magnesium carbonate, delivering 12.87 grams per litre of succinic acid with a yield of 0.621 grams of succinate per gram of sugar consumed, the highest figure reported for wheat straw fermentations of this kind. Productivity peaked at 0.44 to 0.46 grams per litre per hour, and succinic acid selectivity over the main by-products, formic and acetic acids, ranged from 37.0 to 43.1 percent across the tested conditions. Notably, the bacterium consumed essentially all of the available glucose and xylose within 28 hours in most conditions, with total sugar consumption reaching 100 percent, showing no apparent preference between the two sugars under these conditions.</p>
<p>Counterintuitively, more was not always better. Raising the yeast extract concentration to 25 grams per litre actually reduced cell growth, with optical density measurements at 660 nanometres falling by 55 to 60 percent compared with the best conditions, a finding the authors suggest may relate to the effect of specific amino acids such as methionine on A. succinogenes metabolism, although they caution that this remains a hypothesis. Similarly, the combination of maximum yeast extract and maximum magnesium carbonate produced the lowest succinate titer in the concentrated hydrolysate at 9.95 grams per litre. Since yeast extract is among the most expensive components of fermentation media, avoiding unnecessary supplementation matters both economically and environmentally. The study also benchmarked its results against fermentations of other agricultural residues, from rapeseed straw and rice husks to oil palm trunks and sweet sorghum bagasse, and found that despite starting with comparatively modest sugar concentrations, its wheat straw process achieved yields matching or exceeding those reported for feedstocks with far more available carbohydrate.</p>
<p>Beyond the bench experiments, the team brought computational optimization to bear on the medium design problem. The experimental data were used to train second-order polynomial response surface methodology models fitted by ordinary least squares regression, with coefficients of determination of 0.991 for succinate yield and 0.972 for selectivity, and these surrogate models were then coupled with the Non-dominated Sorting Genetic Algorithm II, a population-based evolutionary optimizer that sorts candidate solutions into Pareto fronts. Because yield and selectivity cannot necessarily be maximized at the same time, the algorithm mapped the trade-off surface between them and identified medium compositions offering the best compromises. A validation experiment at the algorithmically selected optimum of 90 percent hydrolysate, 10 grams per litre yeast extract and 45 grams per litre magnesium carbonate closely matched the model&#8217;s predictions, with selectivity agreeing to within 0.06 percent and yield showing only a modest overestimate of about 2 percent. The authors are transparent about the statistical limitations of their design, noting that with only nine unique conditions and ten model coefficients, the high R-squared values likely reflect near-interpolation rather than confirmed predictive accuracy, and they recommend face-centred or central composite designs with replicated centre points for future work.</p>
<p>The improvement over previous wheat straw fermentations is striking in context. Earlier work by Li and colleagues using Fibrobacter succinogenes S85 on wheat straw achieved only about 2 grams per litre of succinic acid, and the recent study by Casella and co-workers, which documented the severe inhibition caused by wheat straw-derived inhibitors, did not supplement the medium with nitrogen or magnesium at all. The new optimized process therefore achieved roughly six times the succinate concentration of the earlier benchmark, without any detoxification step, simply by rebalancing the fermentation medium. The authors interpret the benefit of magnesium carbonate as the combined result of buffering capacity, inorganic carbon availability, carbonate chemistry and possible magnesium ion contributions, while acknowledging that because pH and dissolved carbon dioxide were not independently monitored, the individual contributions of these mechanisms cannot be disentangled in the current setup. Controlled bioreactor experiments with independent pH and carbon dioxide regulation will be needed to resolve that question.</p>
<p>What elevates the study beyond a single-substrate optimization is the predictive framework it offers. The combination of factorial experimentation, response surface modeling and multi-objective genetic algorithms provides a transferable template for tackling the variable, inhibitor-laden hydrolysates that will inevitably arise as biorefineries process different biomass streams. Lignocellulosic hydrolysate composition is notoriously site-specific and season-specific, and a method that can rapidly identify the cheapest effective medium formulation for each new batch, without resource-intensive trial and error, addresses a genuine bottleneck in industrializing biobased chemical production. The authors also look ahead to the economics: yeast extract remains a costly input at industrial scale, and replacing it with cheaper nitrogen sources such as corn steep liquor or urea will be essential for commercial viability.</p>
<p>As the chemical industry searches for routes to decarbonize its platform molecules, processes that transform agricultural residues into valuable products while consuming carbon dioxide along the way hold obvious appeal. This work demonstrates that the toxins that once made wheat straw hydrolysate a hostile environment for fermentation can be tolerated, and even effectively neutralized, through intelligent medium engineering, bringing biobased succinic acid a step closer to competing with its fossil-derived counterpart on both performance and sustainability.</p>
<div class="scienmag-article-metadata"><strong>Subject of Research:</strong> Production of bio-based succinic acid by fermentation of non-detoxified steam-exploded wheat straw hydrolysate with Actinobacillus succinogenes 130Z, using factorial medium optimization, response surface methodology and NSGA-II multi-objective optimization.</p>
<p><strong>Article Title:</strong> Valorization of Wheat Straw Hydrolysate into Succinic Acid by Fermentation with Actinobacillus succinogenes</p>
<p><strong>Article References:</strong> Loffredo, R., Cariou, C., Casella, P., Rao, M. A., Liuzzi, F., De Bari, I., Molino, A., Zacharopoulos, I., &amp; Angelidaki, I. (2026). Valorization of Wheat Straw Hydrolysate into Succinic Acid by Fermentation with Actinobacillus succinogenes. <em>Waste and Biomass Valorization</em>. <a href="https://doi.org/10.1007/s12649-026-03787-6" target="_blank" rel="noopener noreferrer">https://doi.org/10.1007/s12649-026-03787-6</a></p>
<p><strong>Image Credits:</strong> AI Generated</p>
<p><strong>DOI:</strong> <a href="https://doi.org/10.1007/s12649-026-03787-6" target="_blank" rel="noopener noreferrer">10.1007/s12649-026-03787-6</a></p>
<p><strong>Keywords:</strong> succinic acid, Actinobacillus succinogenes, wheat straw hydrolysate, lignocellulosic biomass, medium optimization, response surface methodology, NSGA-II, biorefinery, fermentation, yeast extract, magnesium carbonate, non-detoxified hydrolysate</p>
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		<post-id xmlns="com-wordpress:feed-additions:1">188862</post-id>	</item>
		<item>
		<title>Microwave-Enhanced Hierarchical Liquefaction of Pentose Boosts Furfural Production and Separation</title>
		<link>https://scienmag.com/microwave-enhanced-hierarchical-liquefaction-of-pentose-boosts-furfural-production-and-separation/</link>
		
		<dc:creator><![CDATA[Alan Morgan]]></dc:creator>
		<pubDate>Thu, 26 Mar 2026 16:06:10 +0000</pubDate>
				<category><![CDATA[Agriculture]]></category>
		<category><![CDATA[advanced heating technologies for bio-refining]]></category>
		<category><![CDATA[bio-based chemical synthesis]]></category>
		<category><![CDATA[energy-efficient biomass processing]]></category>
		<category><![CDATA[furfural production optimization]]></category>
		<category><![CDATA[hemicellulose depolymerization techniques]]></category>
		<category><![CDATA[hierarchical liquefaction of pentose]]></category>
		<category><![CDATA[industrial furfural separation methods]]></category>
		<category><![CDATA[microwave heating for biomass]]></category>
		<category><![CDATA[microwave-assisted biomass liquefaction]]></category>
		<category><![CDATA[scalable furfural manufacturing]]></category>
		<category><![CDATA[solvent effects in furfural synthesis]]></category>
		<category><![CDATA[sustainable agricultural residue conversion]]></category>
		<guid isPermaLink="false">https://scienmag.com/microwave-enhanced-hierarchical-liquefaction-of-pentose-boosts-furfural-production-and-separation/</guid>

					<description><![CDATA[In recent years, the sustainable conversion of agricultural and forestry residues into high-value chemicals has garnered significant scientific attention. Among these biochemicals, furfural stands out as a pivotal platform molecule, essential for producing bio-based plastics, pharmaceuticals, and various industrial chemicals. The efficient and scalable production of furfural, however, remains a complex challenge that hinges critically [&#8230;]]]></description>
										<content:encoded><![CDATA[<p>In recent years, the sustainable conversion of agricultural and forestry residues into high-value chemicals has garnered significant scientific attention. Among these biochemicals, furfural stands out as a pivotal platform molecule, essential for producing bio-based plastics, pharmaceuticals, and various industrial chemicals. The efficient and scalable production of furfural, however, remains a complex challenge that hinges critically on the choice of solvents and heating methodologies employed during its synthesis.</p>
<p>Traditionally, furfural production has been dominated by conventional heating approaches that rely on thermal conduction within high-pressure reactors or hydrothermal autoclaves. These methods, while effective to some extent, inherently produce non-uniform heating environments. Such thermal gradients lead to several complications, including uneven reaction zones and suboptimal interaction between the solvent and biomass substrates. Consequently, these conditions hinder the full exploitation of solvent properties, resulting in low reaction efficiencies and limited overall yields.</p>
<p>One of the most notable drawbacks of conventional heating is its lack of synchronization between the substrate characteristics and the heating mechanism. Monosaccharide conversion to furfural is manageable under these traditional conditions; however, efficiently depolymerizing hemicellulose—a major biomass component—proves significantly less effective. This inefficiency mandates longer reaction times and elevated temperatures, ultimately inflating operational costs and energy consumption.</p>
<p>Microwave-assisted heating technologies have emerged as a promising alternative, offering distinctive advantages rooted in selective and volumetric heating. Unlike conventional methods, microwaves can couple directly with the solvent and substrate dielectric properties, enabling rapid and uniform energy transfer at the molecular level. Leveraging this capability could revolutionize furfural synthesis by enhancing reaction rates and yields under milder conditions.</p>
<p>At the forefront of this innovation, Academician Jiang Jianchun and his research team at the Chinese Academy of Forestry have pioneered a method that combines microwave energy with tailored solvent systems. Central to their strategy is the understanding and manipulation of solvent dielectric properties, which dictate their interaction with microwave radiation. The team proposed definitive screening principles focused on selecting solvents that exhibit optimal compatibility with microwave fields to maximize reaction efficiency.</p>
<p>Building upon these principles, the researchers designed a biphasic solvent system employing γ-valerolactone (GVL) combined with an aqueous saline solution containing sodium chloride. This configuration facilitates both the directed liquefaction of pentoses derived from biomass and the stepwise isolation of furfural. Importantly, the team systematically demonstrated that furfural&#8217;s partition coefficient (R)—a measure of its distribution between the two phases—is significantly enhanced under microwave irradiation. Comparative studies revealed an increase in R from 29.33 during conventional heating to 35.68 when microwaves were employed, indicative of improved extraction efficacy.</p>
<p>Delving deeper into the mechanistic underpinnings, kinetic studies detailed how microwave energy synergistically accelerates biomass depolymerization and furfural synthesis. The initial stage utilizes high-power microwave irradiation to rapidly cleave xylan glycosidic bonds within hemicellulose, liberating xylose with exceptional efficiency—up to 87.9 mol%. This swift depolymerization minimizes the formation of inhibitory byproducts common to slower processes. Subsequently, a reduced microwave power phase drives the dehydration of released xylose to furfural and facilitates its instant extraction into the organic phase. This layered energy input strategy mitigates side reactions and reduces product decomposition.</p>
<p>Optimization under these controlled conditions yielded remarkable results: at 140°C over 20 minutes, the furfural yield from xylan reached an impressive 85.38 mol%. This yield not only surpasses the 78.1 mol% attainable through conventional heating applied over 120 minutes but does so with substantially reduced reaction duration and energy input. The implications for industrial scalability, efficiency, and cost reductions are profound.</p>
<p>To validate this advanced approach under real-world conditions, the team extended their experiments to complex biomass substrates such as wheat straw. The process retained high effectiveness, delivering a furfural yield quantified at 62.72 wt%, underscoring the practical applicability of the microwave-coupled solvent system. Moreover, an energy consumption analysis revealed that microwave-assisted synthesis reduces energy demands by over 75% relative to conventional heating, positioning this technology as a compelling option for greener chemical manufacturing.</p>
<p>The success of this research hinges largely on the precise control of microwave power levels and exploitation of solvent dielectric traits. By integrating the reaction substrate’s unique chemical features with carefully selected solvent systems, the researchers engineered a process that maximizes microwave energy utilization while minimizing thermal losses. This selective heating paradigm represents a critical advancement in biomass valorization technologies, offering a much-needed blueprint for sustainable chemical production.</p>
<p>Looking ahead, the potential for industrial adoption of microwave-enhanced furfural synthesis appears promising. The methodology’s scalability and energy efficiency align with global trends toward greener manufacturing and resource utilization. Future developments could see the extension of these microwave-enabled protocols to other biochemicals, amplifying their contribution to the circular bioeconomy.</p>
<p>In summation, the breakthrough achieved by Jiang Jianchun’s team embodies a significant stride forward in biomass conversion science. By harmonizing solvent systems with microwave technology, they have demonstrated not only enhanced reaction kinetics and extraction but also meaningful energy savings and operational flexibility. This innovative approach offers an exciting pathway to transform low-value forest residues into high-value chemical precursors with unprecedented efficiency, thereby accelerating the transition to sustainable chemical industries worldwide.</p>
<p>Subject of Research: Not applicable</p>
<p>Article Title: Microwave-Derived Hierarchic Liquefaction of Pentose and Intensified Separation of Furfural</p>
<p>News Publication Date: 20-Nov-2025</p>
<p>Web References: http://dx.doi.org/10.34133/research.1008</p>
<p>Image Credits: Copyright © 2025 Ruixuan Yao et al.</p>
<p>Keywords: furfural, microwave heating, biomass conversion, solvent dielectric properties, γ-valerolactone, biphasic solvent system, hemicellulose depolymerization, xylan cleavage, xylose dehydration, selective microwave heating, energy efficiency, bio-based chemicals</p>
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