Cold soda pulping experiments were conducted using a PFI mill with a phosph
or bronze tackle. The PFI mill was modified and fitted with torque transduc
ers so that the reaction torque could be measured under load to allow the r
efining energy to be determined.
Preliminary trials showed that there were no latent properties in the pulps
and confirmed that the ideal beating load was 3.33 N/mm. Comparison of dat
a from the PFI mill and pilot-scale refiners including a Sunds Defibrator C
D300 and an Andritz Sprout-Bauer 12-1 CP showed that certain pulp propertie
s from young eucalypt plantation species did not correlate well, However, a
good correlation was found between cold soda pulp properties of 8-year-old
Eucalyptus nitens plantation species from the CD300 and a commercial cold
caustic soda pulping plant. Further PFI mill trials were conducted to deter
mine the effect of refining with a toothed brass sleeve insert to simulate
a disc type refiner. Long refining times resulted in unrealistic energy con
sumption.
It was concluded that the PFI mill is an unsuitable small-scale substitute
to replace pilot-scale disc refiners in the assessment of a pulpwood resour
ce and the establishment of a species ranking system.