02081nas a2200205 4500008004100000022001400041245009200055210006900147260000800216520137100224653000601595653001801601653004401619653002501663653001301688653001901701100002101720700002101741856011301762 2021 eng d a0161-494000aAdvances in solid catalysts for selective hydrogenolysis of glycerol to 1,3-propanediol0 aAdvances in solid catalysts for selective hydrogenolysis of glyc cJAN3 a

Glycerol is one of the top 12 platform chemicals obtained from biomass. Its surplus availability as a by-product of biodiesel, fat-splitting and soap manufacturing industries and affordable price lends significant opportunity for its valorization, using solid catalysts, into propanediols (PDOs), particularly to 1,3-propanediol (1,3-PDO), by selective hydrogenolysis. 1,3-PDO is an important chemical with wide applications including that as a precursor in polymers manufacturing. However, the synthesis of 1,3-PDO by selective cleavage of the secondary C-O bond of glycerol in the presence of hydrogen (instead of the primary C-O bond yielding 1,2-PDO) is highly challenging. Of late, supported Pt and Ir catalysts in combination with a reducible oxide (WO(x)or ReOx) were found selective for 1,3-PDO formation. Support, metals composition and additives (co-added metals) affect the performance of these catalysts. Detailed investigations revealed that metal dispersion, electronic connectivity between metal and metal oxide/support, hydrogen activation/spillover and Bronsted acidity are some parameters that influence the activity and selectivity of these bi-functional, metal-metal oxide catalysts. This review summarizes the latest advances in these solid catalysts for selective hydrogenolysis of glycerol to 1,3-PDO, a monomer for advanced polymers.

10a110a3-Propanediol10abifunctional metal-metal oxide catalyst10abiomass valorization10aGlycerol10aHydrogenolysis1 aBhowmik, Susmita1 aDarbha, Srinivas uhttps://library.ncl.res.in/content/advances-solid-catalysts-selective-hydrogenolysis-glycerol-13-propanediol02344nas a2200289 4500008004100000022001400041245008000055210006900135260000900204300001100213490000800224520144400232653002501676653003301701653001501734653001201749100002301761700002201784700002101806700001901827700002101846700002101867700001701888700002201905700002101927856010601948 2021 eng d a0959-652600aEnergy and life cycle impact assessment for xylitol production from corncob0 aEnergy and life cycle impact assessment for xylitol production f cJAN  a1232170 v2783 a

The conversion of biobased feedstocks into energy and value-added chemicals is one main approach to address the current global challenge for waste mitigation through the biorefinery mode. Corncob biomass which is one of the most abundant agricultural residue in India with a high hemicellulose content, can serve as a potential low-cost raw material for food-grade xylitol production. The present study demonstrates a process for xylitol production from corncob biomass with detailed energy and life cycle analysis for viability assessment. The major highlight of the process is the use of microbial fermentation, where biomass-derived D-xylose is converted to xylitol with high selectivity. Overall, 0.502 kg of xylitol crystals could be produced from 3.5 kg of corncob biomass. Simulation analysis revealed that the evaporators are the primary consumers of energy, and the process of heat integration can significantly reduce the energy requirements of the overall process. Environmental impacts of the system evaluated showed emission results of 8.68 kg CO2 equivalent and revealed that marine aquatic and freshwater eco-toxicity are the only possible contributors to the environment. The results suggest that the process would have favourable energy balances, which can be used in pilot plant and heat exchanger network design and operation for xylitol production scale up to 500 L. (C) 2020 Elsevier Ltd. All rights reserved.

10abiomass valorization10aLife cycle impact assessment10asimulation10axylitol1 aDasgupta, Diptarka1 aSidana, Arushdeep1 aGhosh, Prasenjit1 aSharma, Tripti1 aSingh, Jasvinder1 aPrabhune, Asmita1 aMore, Snehal1 aBhaskar, Thallada1 aGhosh, Debashish uhttps://library.ncl.res.in/content/energy-and-life-cycle-impact-assessment-xylitol-production-corncob02646nas a2200289 4500008004100000022001400041245012500055210006900180260000800249300001600257490000700273520167000280653001201950653002501962653001401987653002702001653002102028653001902049100002202068700002602090700002202116700001802138700002902156700002402185700001902209856012802228 2021 eng d a2155-543500aSupported MoOx and WOx solid acids for biomass valorization: interplay of coordination chemistry, acidity, and catalysis0 aSupported MoOx and WOx solid acids for biomass valorization inte cNOV a13603-136480 v113 aSupported molybdenum oxide (MoOx) and tungsten oxide (WOx) materials are a vital class of solid acid catalysts for the chemical industry because of their nontoxic nature, strong acidity, remarkable stability in water, hydrogen, and oxygen atmospheres, and excellent reusability performance. These fascinating solid acids play a pivotal role in developing sustainable catalytic routes for renewable biomass processing to produce value-added fuels, chemicals, and platform molecules. The coordination chemistry of MoOx and WOx on the support materials (oxides, carbons, or zeolites) controls their acidic strength, active site accessibility, and catalytic activity. Hence, significant efforts have been made toward optimizing the conditions used for catalyst synthesis and biomass processing to tune the coordination chemistry of MoOx and WOx with the substrate molecules and, thus, their acid-activity/selectivity performance. This Review provides a comprehensive overview of supported MoOx and WOx solid acids for biomass valorization. The importance of the biomass and the role of solid acids for biomass valorization were emphasized, followed by a brief discussion of supported MoOx and WO(x )solid acids. Afterward, the interplay of coordination chemistry, acidic strength, and catalytic activity of supported MoOx and WOx solid acids was discussed. Finally, their catalytic applications for the valorization of several biomass substrates and their derivatives were summarized. This Review will provide valuable insights for developing advanced supported WOx and MoOx solid acids for catalytic biomass valorization and other challenging acid-catalyzed processes.10aAcidity10abiomass valorization10acatalysis10aCoordination chemistry10amolybdenum oxide10atungsten oxide1 aSudarsanam, Putla1 aGupta, Navneet, Kumar1 aMallesham, Baithy1 aSingh, Nittan1 aKalbande, Pavan, Narayan1 aReddy, Benjaram, M.1 aSels, Bert, F. uhttps://library.ncl.res.in/content/supported-moox-and-wox-solid-acids-biomass-valorization-interplay-coordination-chemistry01967nas a2200229 4500008004100000022001400041245013600055210006900191260000800260490000700268520116500275653002501440653001101465653001301476653001701489653001101506100002201517700002801539700001801567700002201585856013001607 2025 eng d a1867-388000aContinuous flow hydrodeoxygenation of lignin-derived guaiacol to cyclohexanol over durable Al2O3 hollow fiber supported co catalyst0 aContinuous flow hydrodeoxygenation of ligninderived guaiacol to  cSEP0 v173 a

The drive to decarbonize the chemical, oil, and gas industries through use of bio-derived resources is intensifying. This study focuses on converting lignin-derived phenolic compounds into cyclohexanol, a precursor for adipic acid production. The alumina hollow fiber supported cobalt catalyst (5Co/AHF@capillary) prepared by capillary action method was found to consist cobalt in both metallic and +delta oxidation states. Initial tests in a batch-mode reactor showed promising results, with 5Co/AHF@capillary catalyst demonstrating catalytic activity comparable to Ru/Al2O3 systems (225 degrees C, 1 MPa H-2, 4 h), achieving similar to 86% cyclohexanol yield in guaiacol hydrodeoxygenation reactions. The catalytic system was then adapted for continuous flow reactors under milder conditions (300 degrees C, 2.5 MPa H-2, 18 mL min(-1)), resulting in 83% guaiacol conversion and 74% cyclohexanol yield. The durability of the catalyst was checked for >80 h and results claim that catalyst was active in yielding consistent results. The roles of catalyst preparation method, hydrogen pressure, solvent, WHSV were thoroughly checked and discussed.

10abiomass valorization10aCarbon10aCo/Al2O310aCyclohexanol10alignin1 aSingh, Dheerendra1 aJogdand, Shunottara, M.1 aDevi, Nandini1 aDhepe, Paresh, L. uhttps://library.ncl.res.in/content/continuous-flow-hydrodeoxygenation-lignin-derived-guaiacol-cyclohexanol-over-durable-al2o302340nas a2200265 4500008004100000022001400041245011700055210006900172260000800241300001100249490000800260520142700268653002501695653001801720653002201738100001701760700001701777700002001794700002001814700002301834700003701857700002101894700002701915856013201942 2025 eng d a0141-813000aExtraction of highly crystalline and thermally stable cellulose nanofiber from Heliconia psittacorum L.f. leaves0 aExtraction of highly crystalline and thermally stable cellulose  cMAY a1422640 v3083 a

Extracting cellulose nanofibers (CNF) from agro-waste is one of the promising and practical ways to develop sustainable nanocomposites. In this study, cellulose nanofibers were extracted from the leaves of Heliconia psittacorum for the first time. The combination of oxalic acid hydrolysis (5 wt%) and steam explosion was used for the isolation of CNF from the leaves of Heliconia psittacorum. The structural and chemical features of the prepared CNF were analyzed using various techniques, including Fourier Transform Infrared Spectroscopy (FTIR), Solid state 13C Nuclear Magnetic Resonance Spectroscopy (13C NMR), Scanning Electron Microscopy (SEM), Energy Dispersive X ray analysis (EDX), Transmission electron Microscopy (TEM), X-Ray Diffraction (XRD) and Thermogravimetric analysis (TGA). TEM micrographs reported 15 to 40 nm diameter for the nanofibers synthesized. XRD analysis reported 91 % crystallinity index for CNF, whereas that of the untreated sample was 76 %. The maximum degradation of the CNF is reported at 355 degrees C, exceeds the untreated sample (316 degrees C). The tensile strength of the CNF derived paper was found to be 23 MPa. The recovered nanocellulose can be further utilized for various applications such as the automobile industry for developing lightweight parts, biosensors, super capacitors, absorption of greenhouse gases, wastewater treatment, and packaging applications.

10abiomass valorization10aNanocellulose10aWaste to resource1 aPaul, Sharon1 aJoseph, Anto1 aHridhya, P., D.1 aBadawi, Michael1 aAjithkumar, T., G.1 aParameswaranpillai, Jyotishkumar1 aAsrofi, Mochamad1 aDominic, C., D. Midhun uhttps://library.ncl.res.in/content/extraction-highly-crystalline-and-thermally-stable-cellulose-nanofiber-heliconia-psittacorum02497nas a2200265 4500008004100000022001400041245016000055210006900215260000800284300001500292490000700307520156200314653002301876653001301899653002501912653001801937653002301955100002101978700002201999700002502021700002502046700002502071700001602096856011902112 2025 eng d a2192-650600aSynergistic effect of acidic-basic features of copper-doped layered double hydroxides nanocatalysts in valorization of biomass-derived furfural to biofuels0 aSynergistic effect of acidicbasic features of copperdoped layere cDEC ae2025004160 v903 a

Valorization of biomass-derived chemicals into high-quality compounds and biofuels is enormously fundamental to diminish dependence on fossil-based resources. Furfural is a bio-based valuable compound which can be proficiently upgraded to 4-(2-furyl)-3-buten-2-one (FAc) and 1,4-pentadiene-3-one, 1,5-di-2-furanyl (F 2 Ac) via aldol condensation of furfural with acetone. In the present work, efficient Cu-doped Mg-Al layered double hydroxides (LDH) nanocatalysts are fabricated by coprecipitation and are exploited for furfural conversion to obtained FAc and F 2 Ac. The structure-activity relationship is scrutinized by characterizing fresh and spent nanocatalysts via numerous techniques. The good correlation between the amount of weak acidic-weak basic catalytic sites and nanocatalysts performance is established. The superior performance of Cu-0.1 nanocatalyst (Cu-content = 1.85 wt%) in aldol condensation is attributed to the presence of optimum weak acidic sites (0.21 mmol g-1) and weak basic sites (0.36 mmol g-1), synergistic acidic-basic effect, nano-sized Cu(OH) 2 nanoparticles (1.6 nm), high BET surface area (181 m2 g-1), and mesoporous architecture of material. Cu-0.1 nanocatalyst delivered 98% FAc selectivity with 100% furfural conversion at 85 degrees C. Furthermore, at 100 degrees C, the nanocatalyst gives 55% F 2 Ac selectivity with 73% furfural conversion. The catalyst displays good recyclability (7 recycles) and stability. Plausible mechanistic pathway for transformation of furfural to FAc and F 2 Ac is proposed.

10aAldol condensation10abiofuels10abiomass valorization10ananocatalysis10asynergistic effect1 aGode, Nilesh, G.1 aNagpure, Atul, S.1 aRewatkar, Suresh, B.1 aBhagat, Shailesh, K.1 aDeshmukh, Ganpat, D.1 aSaini, Ajay uhttps://library.ncl.res.in/content/synergistic-effect-acidic-basic-features-copper-doped-layered-double-hydroxides02448nas a2200265 4500008004100000022001400041245011700055210006900172260000800241300001100249490000800260520154400268653002101812653002501833653002101858653002201879653001901901100002001920700002301940700001801963700001901981700002102000700003002021856013102051 2026 eng d a1385-894700aConcurrent glycerol oxidation and hydrogen production on Ce-Co oxide/carbon for sustainable biomass valorization0 aConcurrent glycerol oxidation and hydrogen production on CeCo ox cMAY a1757070 v5353 a

Integrating glycerol oxidation with water electrolysis offers a sustainable route for hydrogen production while enabling concurrent generation of industrially relevant C1-C3 value-added materials. This system replaces kinetically sluggish oxygen evolution reaction (OER) simultaneously delivering H-2 at the cathode with high turnover frequency, thereby lowering the overall cell voltage and enabling the valorization of glycerol, a major by-product of the biodiesel industry. However, the development of an efficient bifunctional electrocatalysts capable of driving cathodic as well as anodic half-cell reactions remains a key challenge. Herein, we present a cerium-cobalt oxide composite modified with an amorphous carbon layer (Ce,Co-O/C) as an effective bifunctional catalyst for glycerol-assisted water electrolysis. The interfacial electron distribution across the Co-Ce oxide heterojunction generated abundant redox-active sites and accelerates reaction kinetics, while the conductive carbon layer facilitates rapid charge transfer and imparts improved stability. Consequently, the Ce, Co-O/C catalyst exhibited high formate selectivity at 1.4 V (vs RHE) at room temperature and delivers a low cell voltage of 1.90 V at 100 mA cm(-2) in a symmetric Ce,Co-O/C vertical bar vertical bar Ce,Co-O/C system, maintaining operational stability over 100 h. This work provides a promising interface-engineering for designing self-supported bifunctional electrocatalysts toward integrated biomass assisted co-electrolysis systems.

10aAmorphous carbon10abiomass valorization10aelectrocatalysis10aenergy conversion10agreen hydrogen1 aJana, Jayasmita1 aChowdhury, Somnath1 aSaha, Avishek1 aKang, Sung, Gu1 aHur, Seung, Hyun1 aGopinath, Chinnakonda, S. uhttps://library.ncl.res.in/content/concurrent-glycerol-oxidation-and-hydrogen-production-ce-co-oxidecarbon-sustainable-biomass02989nas a2200277 4500008004100000022001400041245016400055210006900219260000800288300001100296490000800307520198800315653002502303653002102328653002202349653001902371100002302390700002802413700002902441700002102470700001802491700001802509700002602527700003002553856012802583 2026 eng d a1385-894700aPotential tuneable glucose oxidation to selective C6 molecules and CC cleavage, and parallel green H2 production: sustainable high current density electrolysis0 aPotential tuneable glucose oxidation to selective C6 molecules a cFEB a1726330 v5293 a

Current study elucidates the electrocatalytic efficacy of palladium-nanocubes (Pd-NCs) for the selective oxidation of glucose to value-added chemicals with concomitant hydrogen evolution. The Pd-NC catalyst demonstrated exceptional activity and product selectivity, achieving nearly quantitative glucose conversion (>99 %) with high gluconic and glucaric acid yield at low anodic overpotential (0.6 V vs. RHE) in alkaline electrolyte. At not-so-high elevated potentials (1.2 V vs. RHE), oxidative CC scission prevails, yielding shorter-chain carboxylates along with C6-acids. Reaction products are thoroughly characterized and quantitatively estimated by NMR spectral methods; NMR methods also provide CC cleavage and mechanistic pathways of glucose to various products. Complementary DFT calculations delineate the thermodynamic favorability of glucose adsorption on Pd-NC surfaces (-1.83 eV) and the exergonic oxidation pathway under applied bias, corroborating experimental product distributions. In a two-electrode electrolyzer, Pd-NC anode paired with Pt/C and Ni2P cathode demonstrates 100 mA/cm(2) at 0.99 V and 1.37 V, respectively, with 48 % reduction in energy input (26.6 kWh/kg H-2) compared to conventional alkaline electrolysis; critically, H-2 production energy is lower than the usable energy (33.3 kWh/kg H-2). Sustainable chronopotentiometric assays confirm sustainability (similar to 140 h) in alkaline as well as saline electrolytes, underscoring the system's resilience against chloride-mediated corrosion. Present work establishes a proof of concept for integrated biomass-component valorization and carbon-negative green hydrogen production, merging atomic-level mechanistic insights with scalable reactor design. Optimization of reaction parameters, including potential tuning, reaction temperature and electrolyte engineering, offers a compelling strategy to further enhance C6 and fragmented product selectivity and overall system efficiency.

10abiomass valorization10aelectrocatalysis10aenergy conversion10aSustainability1 aChauhan, Inderjeet1 aPatra, Kshirodra, Kumar1 aVijay, Pothoppurathu, M.1 aNalajala, Naresh1 aMehta, Shweta1 aJoshi, Kavita1 aRavindranathan, Sapna1 aGopinath, Chinnakonda, S. uhttps://library.ncl.res.in/content/potential-tuneable-glucose-oxidation-selective-c6-molecules-and-cc-cleavage-and-parallel