Spherical NiCo-MOFs catalytic hydrogenolysis of lignin dimers and enzymatic lignin to value-added liquid fuels under nitrogen atmosphere
•Lignin dimers was converted into cycloalkanes over MOF-derived spherical NiCo/C.•Enzymatic lignin can be converted to small molecules with low oxygen content.•Highest lignin oil yield (75.6 wt%) and lower O/C ratio (0.17) were obtained.•H2 can be generated from isopropanol over spherical NiCo/C cat...
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Published in | Fuel (Guildford) Vol. 315; p. 123156 |
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Main Authors | , , , , , , , |
Format | Journal Article |
Language | English |
Published |
Kidlington
Elsevier Ltd
01.05.2022
Elsevier BV |
Subjects | |
Online Access | Get full text |
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Summary: | •Lignin dimers was converted into cycloalkanes over MOF-derived spherical NiCo/C.•Enzymatic lignin can be converted to small molecules with low oxygen content.•Highest lignin oil yield (75.6 wt%) and lower O/C ratio (0.17) were obtained.•H2 can be generated from isopropanol over spherical NiCo/C catalysts.
Ni-based MOFs catalysts are promising candidates that can be used to achieve biomass valorization following the process of selective hydrogenolysis process. Here we report a spherical NiCo-based MOFs catalyst, which provides a larger BET surface to enhance 2-phenoxy-1-phenylethan-1-ol molecules enrichment and promote the hydrogenolysis on spherical NiCo-based MOFs catalyst surface. In addition, the synergistic interaction between Ni and Co species also shows great effect on catalytic hydrogenolysis of 2-phenoxy-1-phenylethan-1-ol molecules and enzymatic lignin. The yields of ethylcyclohexane and cyclohexanol are dramatically improved to more than 90 mol% over Ni3Co1-based MOFs catalyst under nitrogen atmosphere. Various lignin dimers derivatives are investigated over Ni3Co1-based MOFs catalyst, which indicates oxygen-containing functional groups played a critical role in the hydrogenolysis process. Isopropanol is used as solvent in the hydrogenolysis of 2-phenoxy-1-phenylethan-1-ol molecules and enzymatic lignin. 21% of H2 is observed in the GC/MS, suggesting that it is a catalytic transfer hydrogenolysis process. Catalytic hydrogenolysis of enzymatic lignin is also carried out under 280 ℃ over optimal Ni3Co1-based MOFs catalyst for 6 h, giving highest lignin oil yield (75.6 wt%) and lower O/C ratio (0.17). This work can be extended to different biomass valorizations to promote the catalytic behavior of spherical MOFs catalysts. |
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ISSN: | 0016-2361 1873-7153 |
DOI: | 10.1016/j.fuel.2022.123156 |