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The principal pathway of oxidative degradation of phenolic units comprises the
abstraction of an electron from the phenolate anion by biradical oxygen, resulting
in the formation of the corresponding phenoxy and superoxide anion radicals.
The unstable cyclohexadienone hydroperoxide intermediates fragment to catechols
and various mono- and dicarboxylic acids, such as maleic and muconic
acids, by demethoxylation, ring-opening, and side-chain elimination reactions
[88]. The concentration of the catechols remain fairly constant throughout oxygen
delignification, implying that they are involved in the oxidation process as intermediates
[89]. Furthermore, the catechols also contribute to an improved solubility
of the oxidized lignin structures due to the increase in the hydrophilicity of the
lignin.
The overall outcome of these reactions is the degradation and elimination of
guaiacyl (softwood and hardwood) and syringyl phenolic (hardwood) units. The
degradation of the uncondensed phenolic units is more severe within the dissolved
lignins (51–67%) than in the residual lignins (3–46%) [90]. Condensed phenolic
units refer to those phenolic structures with C5 substituents other than
methoxyl. It is reported, that 56–58% of the total phenolic units present in the residual
softwood kraft lignin can be attributed to the condensed type [90,91]. The
proportion of condensed phenolic units in hardwood residual lignin is considerably
lower as compared to the softwood residual kraft lignin.
After applying oxygen delignification to a softwood kraft pulp, the content of
condensed phenolic units in the residual lignin is decreased only by 4–29%, while
the corresponding decrease within the dissolved lignin fraction is about 41–60%.
It is well established that 5,5′-biphenyl [92] and diphenylmethane structures [93]
are fairly resistant towards oxygen delignification. The latter structures were
found to accumulate during the whole oxygen delignification process. However,
some of the condensed phenolic structures seem to be susceptible to oxygen
delignification, as in general most reports demonstrate an overall decrease in the
total condensed phenolic units after oxygen delignification [90]. In a study by Lai
7.3 Oxygen Delignification 713
et al., it was indicated that b–5 linked phenylcoumaran-type structures are
degraded during the initial phase of oxygen delignification [94]. At very high temperatures
of about 140 °C the amount of condensed phenolic units decreases by
more than 50%, which confirms that the reactivity of softwood kraft lignin substantially
increases at temperatures above 110 °C.
The presence of carboxylic acid groups within the lignin structures is considered
to promote lignin solubilization during alkaline oxygen delignification. The
increase of the carboxylic content is particularly high in the residual softwood
kraft lignin, while the corresponding carboxylic content in the hardwood residual
lignin increases only moderately obviously due to the higher initial value [90].
Compared to the residual lignins, the dissolved lignins contain more carboxylic
acids. It is interesting to note that the rate of carboxylic group formation increases
drastically as the reaction temperature increases parallel to the degradation of the
uncondensed phenolic units. A significant increase in the carboxylic acid groups
is observed at temperatures greater than 120 °C [95]. After successive oxygen
delignification stages, the content of carboxylic acid groups in the residual lignin
decreases, which means that the lignin which is rich in carboxylic acid groups is
preferably removed in the subsequent oxygen delignification stages, leaving a residual
lignin containing fewer reactive groups [96]. The content of the residual lignin
(kappa number) also plays a decisive role in the overall reactivity of the lignin
structures. High-kappa number pulps are known to be easier to delignify than
low-kappa number pulps, clearly due to a lower proportion of condensed lignin
structures, particularly 5,5′-condensed lignin units and diphenylmethane structures
[93]. The extent of oxidation to carboxylic acid groups is found to be lower
than that in low-kappa lignins. It can be speculated that the lower amount of condensed
structures in these high-kappa number pulps requires less oxidation for
the removal. Nevertheless, it has been demonstrated in a study by Chirat and
Lachenal, and also later by Roost et al., that a significant fraction of the residual
lignin (>22–25% of the initial value) remains even after five oxygen treatments,
which suggests that the oxygen delignification levels off [97,98]. Elucidation of the
structures of residual lignin that is unsusceptible towards oxygen delignification
has certainly been the focus of recent research. Based on the experience that the
extent of lignin removal decreases with increasing hemicellulose content (particularly
xylan), it is assumed that the residual lignin is attached to carbohydrates by
lignin–carbohydrate complex (LCC) linkages [99–101]. In fact, xylan-linked lignin
is more resistant to oxidative reactions, while galactan-linked lignin is readily
degraded during oxygen delignification [96]. The removal of amorphous cellulose
during a first oxygen delignification stage causes an increase in cellulose crystallinity,
thus reducing the accessibility of residual lignin in the secondary wall.
Quite recently, the existence of p -hydroxyphenyl groups has been attributed to
the resistant lignin structures in residual kraft lignin [93,96,102]. Model experiments
indicated that these materials are less reactive than their guaiacol counterparts,
although they belong to the noncondensed phenolics. The content of p -hydroxyphenyl
groups in a residual softwood kraft lignin was shown to correlate
with delignification selectivity during oxygen delignification. The stability of p -
714 7Pulp Bleaching
hydroxybenzene during oxygen delignification is clearly confirmed by model compound
studies [93]. It can thus be concluded that the accumulation of 5,5′-biphenyl
structures occurring via phenoxy guaiacyl radical coupling reactions between
the liquor and the fiber and the p -hydroxyphenyl structures are amongst the major
factors impeding the efficiency of oxygen delignification.
The ratio between the light absorption coefficient and kappa number corrected
for the content of hexenuronic acids, k457 nm/kappa(**), is a measure of the specific
amount of chromophoric groups in the residual lignin (see Section 4.2.6, Influence
on bleachability). Quite surprisingly, the degree of oxygen delignification
was found to be somewhat higher for unbleached softwood kraft pulps with
increasing k457 nm/kappa(**) values, as shown in Fig. 7.46 [103].
0.6 0.9 1.2 1.5 1.8
k
457nm
/kappa, m2/kg
Degree of oxygen delignification, %
Fig. 7.46 Extent of oxygen delignification as a
function of the specific light absorption coefficient
[k457 nm/kappa(**)] (according to Gellerstedt
and Al-Dajani [103]). Unbleached Pinus sylvestris
kraft pulp, kappa numbers 15–19. Conditions
for oxygen delignification are given by Gustavvson
et al. [104]: 100 °C, 85 min, 12% consistency,
700 kPa pressure, 2.25% NaOH.
The slightly higher efficiency of oxygen delignification of the unbleached softwood
kraft pulps with the lower brightness was mainly attributed to the higher
content of reactive unsaturated aliphatic carbon atoms and phenolic hydroxyl
groups, as determined by a thorough analysis of the residual lignin structures
(two-dimensional NMR using the HSQC sequence) [103]. Prolonged cooking at a
low hydroxide ion concentration gives rise to the formation of these degraded lignin
structures due to preferred fragmentation reactions. However, the low hydroxide
ion concentration during residual delignification promotes the precipitation of
dissolved lignin, which then leads to a decrease in brightness and specific light
absorption coefficient. Despite their higher degree of delignification in the oxygen
stage, the pulps with a high unbleached k/kappa(**)-value require more bleaching
7.3 Oxygen Delignification 715
chemicals (expressed as OXE per kappa) for subsequent bleaching to full brightness
as compared to those pulps comprising a low unbleached k/kappa(**)-value
(see Fig. 7.47). The latter are produced with a high effective alkali charge and a
short cooking time.
0 300 600 900 1200 1500
0.6
0.8
1.0
1.2
1.4
1.6
1.8
k
457nm
/kappa, m2/kg
Consumed OXE / kappa
Fig. 7.47 k457 nm/kappa(**) versus quantity of oxidation equivalents
consumed (OXE) in an OQPQP-sequence to a brightness
of 87% ISO (according to Gellerstedt and Al-Dajani
[103]). The conditions for the QPQP-sequence are given by
Gustavvson et al. [104].
The better bleachability of pulps with low unbleached k/kappa(**)-values is associated
with a higher amount of b-O-4 structures [105]. It is generally agreed that
the bleachability of softwood kraft pulps in a TCF-sequence comprising oxygen
and peroxide as bleaching chemicals is positively correlated with the unbleached
pulp brightness, and thus with the amount of b-O-4-structures in the residual lignin
[106].
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