Lignin
is the most abundant aromatic biopolymer on Earth, and its
aromatic structure makes it a promising platform for the production
of biobased chemicals and other valuable building blocks. The valorization
of lignin into chemicals currently presents a challenge, and its facilitation
is key in the development of viable lignocellulosic biorefinery processes.
This study presents a conceptual design for a recently demonstrated
process for lignin oxidative depolymerization. Modeling, simulation,
and analysis were performed based on experimental data to assess the
viability of the process. Mass and energy balances and main design
data were determined for a 700 t/y kraft lignin biorefinery. The production
capacity of aromatic chemicals, including vanillin, vanillic acid,
guaiacol, and acetovanillone, was 0.3 kg aromatics/kg net lignin use.
A heat-integrated process design is suggested, and the energy demands
and the CO2 emissions are evaluated and compared. Assuming
an interest rate of 10% and a plant lifetime of 10 years, the return
on investment was calculated to be 14%, indicating that such a biorefinery
is viable. A sensitivity analysis was carried out to assess the impact
of the vanillin selling price and the cost of lignin on the profitability
of the process. A quantitative investigation of process sustainability
resulted in an E-factor of ∼1.6 for the entire synthetic route,
that is, 38% material efficiency. The findings of this study underline
the need for further research to develop efficient lignin conversion
technologies with attractive yields in order to increase profitability
on an industrial scale.