Vanillin production from chemical oxidation of Pinus
spp. Kraft lignin is investigated. At a
temperature of 130 °C, an oxygen partial pressure of 3 bar, a total
pressure of 9 bar, and a
lignin concentration of 60 g/L in an alkaline medium of 2 N NaOH, a
maximum vanillin yield
of 10% is obtained. On the basis of experimental results in a
batch reactor operated under
various conditions of temperature, oxygen partial pressure, total
pressure, initial lignin
concentration and pH, a kinetic model is proposed to simulate vanillin
production from oxidation
of Kraft lignin. The reaction rate of vanillin production is, for
pH > 11.5, r
C =
k
NC[O2]1.75[L]
−
k
CI[O2][C] and, for pH
< 11.5, r
C =
k
NC[O2]1.75[L]
− Af(pH)[C]2. An attempt to
predict pH variation
during the reaction is also made. The overall flowsheet of the
process is briefly addressed, and
the recovery of vanillin by adsorption is discussed.