scispace - formally typeset
Journal ArticleDOI

Degradation of solvolysis lignin using Lewis acid catalysts

TLDR
In this paper, Alcell-derived lignin was depolymerized in a batch reactor using the Lewis acid catalysts NiCl2 and FeCl3, achieving 30% and 26% from Ni and Fe, respectively, at reaction conditions of 305°C and 1 h reaction time.
Abstract
Alcell-derived lignin was depolymerized in a batch reactor using the Lewis acid catalysts NiCl2 and FeCl3. The objective was to investigate the use of Lewis acids in the production of useful liquid products directly from solvolysis lignin. The effects of reaction temperature, time and catalyst were studied on the conversion of this lignin to gas, solid and liquid products. Also, selected monomeric compounds in the ether solubles were monitored in terms of the variation in their yields with different reaction conditions. The highest conversions, 30% and 26% from Ni and Fe, respectively, were both attained at the reaction conditions of 305°C and 1 h reaction time. The Ni produced a somewhat higher yield of ether solubles, reflecting its slightly higher performance. Under the reaction conditions studied, both catalysts apparently favour condensation reactions leading to the formation of insoluble reactor residue from solvolysis lignin. Low quantities of monomeric compounds were produced, with phenols dominating over ketones and aldehydes for both catalysts. De la lignine obtenue par le procede Alcell a ete depolymerisee dans un reacteur discontinu a l'aide de catalyseurs acides de Lewis NiCl2 et FeCl2. L'objectif etait d'etudier l'utilisation des acides de Lewis dans la production de produits liquides utiles directement a partir de la lignine de solvolyse. On a etudie les effets de la temperature de reaction, du temps de reaction et du catalyseur sur la conversion de cette lignine en produits gazeux, solides et liquides. En outre, on a suivi la variation du rendement de composes monomeres selectionnes dans les solubles ethers dans differentes conditions de reaction. Les plus fortes conversions, soient 30% et 26% du Ni et du Fe respectivement, etaient dans les deux cas reliees aux conditions de reaction, soient une temperature de 305°C et un temps de reaction de 1 heure. Le Ni produit un rendement de solubles ethers un peu plus eleve, refletant sa performance sensiblement meilleure. Dans les conditions de reaction etudiees, les deux catalyseurs favorisent des reactions de condensation, ce qui mene a la formation de residus de reacteur insolubles a partir de la lignine de solvolyse. De faibles quantites de composes monomeres ont ete produites, les phenols dominant les cetones et aldehydes pour les deux catalyseurs.

read more

Citations
More filters
Journal ArticleDOI

Catalytic Transformation of Lignin for the Production of Chemicals and Fuels

TL;DR: This paper presents a new state-of-the-art implementation of the iChEM (Collaborative Innovation Center of Chemistry for Energy Materials) Key Laborotary of Catalysis, which automates the very labor-intensive and therefore expensive and therefore time-heavy and expensive process ofalysis.
Journal ArticleDOI

Chemicals from lignin: an interplay of lignocellulose fractionation, depolymerisation, and upgrading

TL;DR: This review provides a summary and perspective of the extensive research that has been devoted to each of these three interconnected biorefinery aspects, ranging from industrially well-established techniques to the latest cutting edge innovations.
Journal ArticleDOI

Hydrothermal conversion of lignin: A review

TL;DR: In this article, the authors compared three methods of lignin hydrothermal conversion, including their process parameters, possible conversion routes, catalysts, application of products, and effects of hot-compressed organic solvent-water mixture solution on conversion of Lignin.
Journal ArticleDOI

Lignin Depolymerization into Aromatic Monomers over Solid Acid Catalysts

TL;DR: In this article, the SiO2-Al2O3 catalyst gave exceptionally high yields of ca. 60% for organic solvent soluble extracted products with 95 ± 10% mass balance in the depolymerization of dealkaline lignin, bagasse and ORG lignins at 250 °C within 30 min.
References
More filters
Journal Article

The ALCELL process--a proven alternative to kraft pulping

E. K. Pye, +1 more
- 01 Jan 1991 - 
TL;DR: In this paper, the procede Alcell, which utilises l'ethanol aqueux comme liqueur de cuisson, was presented, and it was shown that telles installations peuvent etre economiquement interessantes for une production d'environ 300t/j.
Journal ArticleDOI

Improved alkaline oxidation process for the production of aldehydes (vanillin and syringaldehyde) from steam-explosion hardwood lignin

TL;DR: In this article, it was demonstrated that vanillin + syringaldehyde + hydroxybenzaldehyde can reach 14.6 wt% of the lignin isolated from the steam-explosion process.
Journal ArticleDOI

Hydrocracking of solvolysis lignin in a batch reactor

TL;DR: A prototype organosolv lignin was hydrocracked at temperatures of 370-410°C in the presence of tetralin, a hydrogen donor solvent as mentioned in this paper.
Journal ArticleDOI

Depolymerization of lignin at low pressure using Lewis acid catalysts and under high pressure using hydrogen donor solvents

TL;DR: In this article, the results showed that adding phenol or guaiacol to the reaction raixture increased liquefaction of lignin from steam-exploded wood in tetralin at about 140 kg/cm pressure and 300°C.
Journal ArticleDOI

Effects of Lewis acid catalysts on the hydrogenation and cracking of two-ring aromatic and hydroaromatic structures related to coal

TL;DR: Salim and Bell as discussed by the authors described the effects of lewis attacks on fuel and discussed the two-ring aromatic and hydrodynamic structure. But they did not discuss the effects on fuel.
Related Papers (5)