Alkaline delignification of hemp woody core was studied to support the
development and optimization of an efficient and non-polluting alkali
ne pulping process. Shavings of hemp woody core were delignified isoth
ermally at different temperatures with 1 M sodium hydroxide in a flow-
through reactor. From literature data and from experimental data repor
ted in this article. it appears that the initial delignification stage
is completed before customary reaction temperatures are reached. Cons
equently, modelling of alkaline delignification kinetics can be restri
cted to the bulk and rest delignification stages, which can be describ
ed with two simultaneous first order reactions: L/L(0 = a2 exp (-k2t)
+ a3 exp (-k3t), with k(i) = A(i) exp -E(ai)/(RT). This equation has b
een solved integrally, calculating a2, a3, E(a2), E(a3), A2 and A3 for
the best fit for the experimental data, resulting in an accurate desc
ription of the delignification reactions. This kinetic model has also
been applied on literature data, supporting its validity towards alkal
ine delignification kinetics in general.