A mathematical model for kraft and soda pulping of Scandinavian spruce
has been developed. In deriving this model exprimental results raport
ed by Hagglund and Hedlund were used (see ref. 24). The model is prese
nted by a linear logarithmic dependence of the main characteristics of
pulping (yield and lignin content) on time and temperature parameters
, both expressed by the H-factor. It is more convenient to express the
logarithmic dependence yield vs. lignin content as the ratio yield/li
gnin vs. lignin content. This log-log plot is linear for a lignin cont
ent in pulp lower than 15%. The logarithmic dependence yield/H-factor
vs. H-factor is linear over the whole range of the H-factor. The logar
ithmic dependence lignin/H-factor vs. The H-factor is for kraft and so
da delignification linear, for an H-factor higher than 500 and 1000, r
esp. The derived model is caracterized by high values of the correlati
on coefficients (R2 = 0.999 - 1.000). The main characteristics of pulp
ing can be efficiently calculated by the power form of the logarithmic
straight line equation. As to the time temperature parameters, delign
ification is characterized by two phases: initial and bulk. Maximum te
mperatures of 150-degrees, 160-degrees and 170-degrees for kraft pulpi
ng and 160-degrees and 170-degrees for soda delignification, and a sma
ll difference in the input of EA (at equal input of AA) have no impact
on the pulping of Scandinavian spruce wood.