Phosphorylating lignin enhances char formation and reduces heat release rates to replace halogenated compounds.
Chemical treatment of stored biomass extracts lignin while minimizing microbial degradation and dry matter loss.
Gradual pressure reduction keeps lignin below its glass transition temperature, preventing equipment fouling and maximizing energy recovery.
Direct lignin particle precipitation from organic solvent and water extraction mixtures using simple pH adjustment eliminates complex milling steps.
Aqueous ionic liquid extraction removes copper, arsenic, and chromium from treated wood, enabling safe biofuel conversion.
Alkaline peroxide extraction with C1-4 alcohols yields sulfur-free lignin, avoiding traditional kraft process sulfur contamination.
Thermal treatment reduces methoxyl content in alkaline lignin, resolving low reactivity constraints for phenolic resin applications.
Replacing Bisphenol-A with lignin eliminates toxicity in metal food containers while maintaining protective performance.
Dissolves functionalized lignin in depolymerized carrier liquid to resolve solubility bottlenecks and enable efficient hydrotreatment.
Biodegradable ketoacids stabilize lignin during extraction by forming protective ketals.
Adjusting filtrate pH to 3-4 precipitates low molecular weight lignin, resolving yield losses from conventional high-pH separation.
Using a lignin slurry eliminates splashing safety risks while fully utilizing reactivity for efficient resin preparation.
Carbonation precipitates lignin from black liquor, while acid washing displaces metal cations to produce low-salt fuel pellets.
Selective organic solvent extraction isolates sugar-free lignin from lignocellulosic biomass while retaining hemicellulose and lignin-carbohydrate complexes in the solid phase.
Turbulent agitation coalesces lignin particles into larger masses, preventing equipment fouling during biomass processing.
Selective electrochemical oxidation of lignin primary hydroxyls enhances acidolysis yield for aromatic monomers.
Acid treatment extracts hemicellulose from lignocellulosic biomass, resolving the trade-off between process complexity and material reliability.
Feruloyl-CoA:monolignol transferase incorporates monolignol ferulates into plant lignin structures.
Optimized lignin derivatives stabilize phenolic resin performance by controlling ethoxy and aliphatic hydroxyl contents to overcome feedstock inconsistency.
Sequential acidification stages separate lignin from black liquor, reducing fresh chemical consumption and odorous gas disposal.
Phenolated lignin resin allows molded article recovery at low costs while maintaining insulation properties and heat resistance.
Acid-catalyzed polycondensation of lignin with furan derivatives creates rigid polymer foam.
Cationic ring opening polymerization of oxiranes with lignin using acidic catalysts eliminates high-pressure requirements and prevents homopolymer formation.
Heating a lignin and base mixture creates stable dispersions, eliminating hazardous chemical use.
A lignin-based intumescent flame retardant system chemically couples biomass with phosphorus compounds to form a protective char layer.
A chelator-mediated Fenton reaction breaks C-C bonds in lignosulfonate to reduce molecular weight under mild conditions.
Mannich reaction modifies lignin to enable 60 wt% polyol substitution, resolving solubility and reactivity bottlenecks.
Segmented solvent process removes metal catalyst contamination during delignification, achieving high cellulose purity without increasing production costs.
Solvent precipitation yields stable colloidal lignin particles, eliminating pH instability and cross-linking requirements.
Direct chemical reagent injection into lignin process streams creates modified lignins before precipitation.
Acid precipitation separates lignin from alkaline alcoholic solutions, eliminating energy-intensive maturation steps.
A two-stage method precipitates lignin from alkaline spent liquor using controlled pH reduction before large-pore membrane filtration.
Esterified lignin mixes with carbon residues to form processable fiber precursors, overcoming poor viscoelasticity for successful spinning.
Optimized lignin derivatives enable carbon fiber spinnability through controlled alkoxy and carbon content.
Transition metal catalyst breaks down lignin polymers using an organic-water solvent mixture to enhance solubility and reduce molecular weight.
Adjusting solution pH precipitates alkali lignin, enabling low-viscosity concentration via membrane filtration to eliminate evaporation energy costs.
A batch process converts black liquor into bio-oil through controlled depolymerization and solvent extraction.
Neutral pH washing with sodium salts reduces acid consumption and maintains lignin purity for lime kiln fuel.
Mechanical milling reduces lignin particle size to nanometer scale, improving dispersion and tensile strength in tire composites.
Selective catalyst generates hydrogen from hemicellulose to depolymerize lignin without exogenous input, preserving cellulose structure.
Acid precipitation isolates lignin from alkaline solutions while crystallizing sodium or potassium salts for chemical recovery.
Chelator-mediated Fenton reaction converts insoluble lignin into water-soluble products while reducing energy consumption.
A method prepares low-molecular lignin derivatives by mixing hydrolyzed biomass with phenolic compounds and hydrophobic polar solvents.