Depolymerization
of lignin to produce high yield lignin oil is
one of the prospective methods to achieve the sustainable and economic
development for human society. Molybdenum-based sepiolite (Mo/SEP)
catalyst presented a promising performance for lignin depolymerization
under supercritical ethanol (LDSE). Herein, the influence of reductive
treatments for calcined Mo/SEP (C-Mo/SEP) catalyst on lignin depolymerization
was systematically investigated under supercritical ethanol. Two reduced
catalysts N-Mo/SEP and H-Mo/SEP was obtained respectively through
the reduction process by NaBH4 and 10 vol % H2/N2 flow. The characterizations such as N2 adsorption–desorption,
SEM, XRD, FTIR, XPS, NH3-TPD, and Py-FTIR were employed
to investigate the variation of microcosmic structure and property
of Mo/SEP affected by reductive treatments. The results exhibited
that reduction treatment optimized the distributions of Mo5+ species and B/L acidic sites of Mo/SEP catalysts. During the LDSE
process at 290 °C under N2 atmosphere for 3 h, lignin
oil produced over N–Mo/SEP catalyst gave a higher heating value
of 34.92 MJ/kg, which slightly decreased from 36.07 MJ/kg that was
obtained over C-Mo/SEP. But N-Mo/SEP catalyst generated the highest
yields of lignin oil (112.0%) and petroleum ether soluble (PES) product
(74.6%). According to the GC-MS results, the possible mechanism of
N-Mo/SEP catalytic LDSE was proposed. The synergistic effect between
Mo5+ species and B/L acid sites promoted the cracking of
the Caryl–OCH3 bond, and the moderate
acid amounts enhanced the alkylation reaction.