2015
DOI: 10.1039/c5gc01442e
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Influence of bio-based solvents on the catalytic reductive fractionation of birch wood

Abstract: In the reductive catalytic fractionation of lignocellulose, the choice of solvent significantly impacts the delignification efficiency, carbohydrate retention in the pulp and the macrostructure of the pulp.

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Cited by 225 publications
(281 citation statements)
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“…35 Our previous studies also addressed the advantages of using ethylene glycol under acidolysis conditions.…”
Section: Resultsmentioning
confidence: 99%
“…35 Our previous studies also addressed the advantages of using ethylene glycol under acidolysis conditions.…”
Section: Resultsmentioning
confidence: 99%
“…Such methods typically afford ah ighly-aromatic lignin-derived stream (whereby the most reactive functional groups have been deactivated through catalytic reduction, e.g.,c onversion of aldehydic intermediates into alcohols,a nd hydrodeoxygenation of ketones to methylene groups) and aholocellulose stream, as two distinct, stable and easily-separable fractions. [198] Thet wo predominant approaches for such upstream catalytic processing of lignin under mild conditions are hydrogenation and deoxygenation reactions,u sing either an oble metal-supported catalyst [273][274][275][276][277][278][279][280] or inexpensive Ni catalysts (notably,R aneyNi). [198,281,282] ECCL performed on Birch wood sawdust (Ru/C catalyst, 3MPa H 2 ,250 8 8C) has been investigated as amethod to tune Angewandte Chemie Reviews 8188 www.angewandte.org the alcohol functional group content of lignin oils.T he carbohydrate fraction is retained as apulp that is conducive to further upgrading, and the lignin fraction is collected separately as ah ighly aromatic oil containing up to 50 %o ft he carbon intake as mono-aromatics.…”
Section: Early-stage Catalytic Conversion Of Lignin As As Trategy Formentioning
confidence: 99%
“…Deconstruction of lignin may afford as olid carbohydrate pulp fraction, suitable either for undergoing full enzymatic hydrolysis into sugar monomers or for paper production ( Figure 7). [198,[275][276][277][278]282] Separation of the catalyst is important, so as to avoid contamination of the downstream products derived from the two streams.F urthermore,d ue to the strong possibility of poisoning by trace components in the lignocellulose feedstock, the catalyst must be relatively inexpensive.R ecent investigations have centred on the use of Raney-Ni, am agnetic catalyst. [198,282] This property allows for facile separation of the catalyst from both lignin oil and holocellulose streams.H olocellulosic fractions are obtained as predominantly catalyst-free solids that are highly conducive to further downstream treatment ( Figure 7A).…”
Section: Early-stage Catalytic Conversion Of Lignin As As Trategy Formentioning
confidence: 99%
“…Technical lignin is burned because it contains highly recalcitrant CÀC linkagest hat render the material unsuitablef or selectived epolymerization to monomers. [11,20] Unfortunately,t hese lignin-derivedm onomers cannot be directly used as aromatic fuels (diesel additive) and fuel additives owing to their low volatility caused by the high oxygen content (20-25 wt %), which results in high boilingp oints (> 541 K). [11][12][13][14][15][16] RCF is typically performed in the presence of protic solvents at temperatures ranging from 453-523K using supportedt ransition metal catalysts (e.g.,r uthenium, palladium, or nickel) and hydrogen gas or other hydrogen transfer agents (e.g.,m ethanol,i sopropyl alcohol, or formic acid) as reductants.…”
Section: Introductionmentioning
confidence: 99%