In order to meet
the requirements of
sustainable development, the production of aromatic compounds from
renewable biomass is of great concern. Herein, a surfactant-free microemulsion
(SFME) system composed of n-octane, 2-propanol, and
water was explored for the depolymerization of lignin though a hydrogen
transfer reaction of 2-propanol with acidic ionic liquids (ILs) as
catalysts. Experimental results show that the phenol monomer yield
from bagasse lignin in the SFME system is at least 4 times higher
than that in its corresponding water-free binary system, together
with a high selectivity for 4-ethylphenol of 67.8%. In particular,
the results also reveal that the controllable polarity and large surface
area of the SFME and the aggregation of lignin at the SFME surface
are key factors in response to the enhanced yields of phenolic monomers
through intensive characterizations. Mechanism studies imply that
this system tailors mainly the esterified p-coumarate
unit in lignin, and 4-ethylphenol is produced by a cascade reaction,
involving hydrolysis, decarboxylation, and hydrogenation. Furthermore,
this SFME system also exhibits excellent performance for the depolymerization
of other herbaceous lignins, yielding 128.1 mg g–1 phenolic monomers with 59.1% 4-ethylphenol selectivity for corncob
lignin. It is thus believed that the process intensification by microemulsion
can significantly demonstrate unprecedented potential to accomplish
highly efficient lignin conversion.