With an aromatic structure, lignin
has great potential for the
production of high value-added chemicals. In this study, Co/m-ATP
catalyst was prepared by the co-impregnation method to depolymerize
lignin with inexpensive attapulgite as a carrier, 1,4-dioxane as a
solvent, and ethanol as an in situ hydrogen source. Meanwhile, formaldehyde
stabilization facilitates lignin monomer production during biomass
depolymerization. The effects of Co particle loading and reaction
conditions (e.g., temperature and reaction time) on lignin conversion
and product yield were investigated, resulting in a low char yield
(6.6 wt %) and high bio-oil yield (63.1 wt %) when alkali lignin was
depolymerized over the Co/m-ATP catalyst (cobalt loading of 15 wt
%) at 220 °C for 8 h. Therefore, this catalyst with the advantage
of low cost and high catalytic activity would be a potential catalyst
during the depolymerization of lignin.