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consists of b-sitosterol [26]. During bleaching, the unsaponifiables are modified
To more polar compounds containing carboxyl groups; these compounds, together
With other polar extractives such as fatty acids, are favorable as surface
Active agents in the viscose process and account in part for good filtration of the
viscose prepared from this pulp [27,28].
Resins derived from pulps of high resin content – and particularly those containing
Higher amounts of nonpolar neutral substances such as hydrocarbons and
waxes – show a tendency to accumulate in the spinnerets. The deposits of resin
Inside the holes in the spinnerets increase the adhesion of precipitated zinc sulfide,
and this ultimately leads to clogging of the spinnerets [29]. In times of conventional
Bleaching, chlorination of extractives caused viscose turbidity, which
was closely associated with spinning jet clogging [30]. The introduction of hydrophilic
Groups by means of oxidation during bleaching operations (O, D, Z, P)
improves the dispersibility of pulp resin in sodium hydroxide [30].
Viscose quality was greatly affected by the ozone charge during the course of
TCF bleaching (O-A-Z-P) of an aspen PHK pulp [31]. A step-wise increase in
ozone charge from 1.0 to 3.3 kg odt–1 significantly decreased the content of acetone
Extractives while improving viscose quality, characterized as the relationship
Between the average particle volume and viscose filterability (Fig. 11.9).
Pulp Properties and Applications
0.20 0.15 0.10 0.05
Centricleaning
(3.3)
(1.9)
(1.0)
Particle Volume [ppm] PVC Filter value
PVC Filter Value Particle Content in Viscose
Acetone Extractives [% od]
Fig. 11.9 Relationship between the content of
Acetone extractives of a TCF-bleached aspen-
PHK pulp and viscose quality [31]. The reduction
Of acetone extractives was achieved by
Increasing charges of ozone and additional
Post cleaning with a centricleaner. Pulping
according to the VisCBC process: P-factor 750,
H-factor 600, EA concentration in cooking
liquor 0.875 g L–1; TCF-bleaching according to
O-A-Z-P to achieve brightness >91% ISO.
10 100
[5]
[4]
[3]
[2]
[1]
[5] 3.3 kg O
/odt and postcleaning
[4] 3.3 kg O
/odt
[3] 1.9 kg O
/odt and postcleaning
[2] 1.9 kg O
/odt
[1] 1.0 kg O
/odt
Frequency
Particle Diameter [μm]
Fig. 11.10 Particle size distribution of viscose samples made
From aspen PHK pulps of varying ozone charges and additional
post cleaning operations [31]. Pulping conditions
According to Fig. 11.9.
Dissolving Grade Pulp
Additional post cleaning by means of a centricleaner further reduced the
Amount of resins, thus improving viscose filterability. The particle spectrum in
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Extractives, resins | | | The viscose demonstrates both a clear reduction in the particle volume and a shift |