2016
DOI: 10.1039/c5gc01950h
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Lignin oxidation and depolymerisation in ionic liquids

Abstract: The depolymerisation of lignin directly in the black liquor was studied, comparing two ionic liquids as extracting solvents (butylimidazolium hydrogen sulphate and triethylammonium hydrogen sulphate), under oxidising conditions.

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Cited by 115 publications
(82 citation statements)
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“…Yield (%) with respect to the loaded lignin ranged from 0.26 to 0.99 for Nb2O5 catalyst and from 0.41 to 0.90 for CoCl2 catalyst, respectively, under the tested conditions. The product yields obtained from this study were comparable with results from previous studies using vanadium-based POM in presence of IL 1-butylimidazolium hydrogen sulfate and H2O2 with a product (vanillin, syringaldehyde, and guaiacol) yield of 0.055% (De Gregorio et al, 2016;Prado et al, 2016a). Low product yield in this study may be due to repolymerization of depolymerized lignin and/or over-oxidization products to other intermediates which were not detected in the GC/MS.…”
Section: Possible Reaction Sequencesupporting
confidence: 83%
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“…Yield (%) with respect to the loaded lignin ranged from 0.26 to 0.99 for Nb2O5 catalyst and from 0.41 to 0.90 for CoCl2 catalyst, respectively, under the tested conditions. The product yields obtained from this study were comparable with results from previous studies using vanadium-based POM in presence of IL 1-butylimidazolium hydrogen sulfate and H2O2 with a product (vanillin, syringaldehyde, and guaiacol) yield of 0.055% (De Gregorio et al, 2016;Prado et al, 2016a). Low product yield in this study may be due to repolymerization of depolymerized lignin and/or over-oxidization products to other intermediates which were not detected in the GC/MS.…”
Section: Possible Reaction Sequencesupporting
confidence: 83%
“…1 Identification and quantification of the monomeric products from the depolymerization reaction were performed by Agilent 7890B GC coupled 5977B MS with an HP-5ms (60 m × 0.32 mm) capillary column. The temperature program started at 50°C and increased to 120°C at 10°C min −1 with a holding time of 5 min; then it was raised to 280°C at 10°C min −1 with a holding time of 8 min and to 300°C at 10°C min −1 with holding time of 2 min (Prado et al, 2016a). Helium was used as a carrier gas at a flow rate of 1.2 mL min −1…”
Section: Methodsmentioning
confidence: 99%
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