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High temperature is known to promote ozone decomposition. Most studies have
concluded that an increase in temperature during ozonation of pulp impairs the
selectivity and efficiency of delignification. However, different opinions have been
expressed about the extent of the effect at a certain temperature level. Allison
found that with radiata pine kraft pulp the extent of delignification after 1% consumed
ozone decreased from only 37.1% lignin removal at 29 °C to 34.7% lignin
removal at 80 °C [59]. Chandra reported that ozone is most efficient in delignifying
kraft pulp at 23 °C, though selectivity gradually decreases with increasing temperature
[60]. Similar observations were made by Soteland [61] and by Liebergott
[24,62]. Patt et al. reported a 10% decrease in kappa number reduction when the
temperature was raised from 20 to 40 °C in HC ozone bleaching of beech sulfite
pulp [63]. Simoes and Castro showed that, for a given kappa number, an increase
in temperature from 4 to 43 °C led to a decrease of pulp viscosity by 80 SCAN
units in ultra-low consistency ozone bleaching of a pine kraft pulp [64]. The beneficial
effect of a low temperature in the ozone stage was also demonstrated by Dillner
and Peter [40]. In contrast to these findings, however, Lindquist reported an
unchanged selectivity when increasing the temperature from 30 to 60 °C in the
ozone stage [65,66].
The kappa number of an OZ(EOP)-treated softwood kraft pulp was substantially
lower when medium-consistency ozone bleaching was conducted at 30 °C as compared
to 50 °C and applying the same amount of ozone charge.
20 30 40 50 60 70 80
0.0
0.2
0.4
0.6
Viscosity [ml/g]
ÄKappa / O
-charge
Δ Kappa / kg O
-charge
Temperature [.C]
Viscosity
Fig. 7.93 Effect of temperature on delignification
efficiency, Dkappa/O3-charge, and on the
course of viscosity during ozonation (according
to [28]). Pulp: E/O-pretreated beech acid
sulfite dissolving wood pulp (B-AS), kappa
number 1.9, viscosity 627 mL g–1; mediumconsistency
ozone bleaching: 10% consistency,
pH 2.5, 10 s mixing time; ozone charge:
2.2–2.3kg odt–1, carry-over: 5 kg COD odt–1.
7.5 Ozone Delignification 813
The efficiency of delignification of an (E/O)-pretreated beech acid sulfite dissolving
and pulp was almost unaffected up to a temperature of 55 °C, while the viscosity
gradually decreased from 580 to 550 mL g–1 [28]. Temperatures above 55 °C,
however, accelerated both the loss in viscosity and the reduction in delignification
efficiency, as depicted in Fig. 7.93.
It can be summarized that delignification efficiency decreases at temperatures
above 50 °C, mostly as a result of increased ozone decomposition [60]. Ozone
bleaching in industrial practice is carried out in the temperature range between
40 and 55 °C. This temperature level is certainly significantly lower as compared
to that of other bleaching stages such as oxygen or peroxide, both of which are
more effective at higher temperatures. The conclusion is that the energy balance
is somewhat impaired by integrating an ozone bleaching stage into a bleaching
sequence.
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