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The wood raw material has a decisive influence on the processability and final
pulp quality. The heterogeneous nature of the wood structure and the chemical
and physical differences between and within wood species are reflected in all
pulping processes. Acid sulfite pulping technology is known to be the most sensitive
process to the properties of the wood raw material, and many softwood species
– and also some hardwoods – are considered to be less suited to acid sulfite
pulping. The deficiencies involved with acid sulfite pulping of, for example pines
or larches, are high screenings, a high residual lignin content, and thus a low
screened yield. The poor pulping results are connected with either the presence of
certain extractives in the wood, especially in the heartwood, or limited impregnation
due to a dense wood structure. It has been found that phenolic resins – such
as pinosylvin in pine heartwood or taxifolin in Douglas fir – react with lignin in
acid sulfite liquors to form a condensation product that prevents delignification
[24–27]. Moreover, taxifolin tends to reduce hydrogen sulfite ions to thiosulfate
ions, thereby decreasing the stability of the sulfite cooking liquor [28].
Subsequently, much effort has been undertaken to modify the sulfite cooking
process to overcome the problems encountered with the use of resinous wood. It
was found that pretreatment of the wood with a sulfite cooking liquor of moderate
acidity, as with a pure hydrogen sulfite solution, and low temperature will favor
sulfonation of the reactive groups of the lignin over condensation reactions with
the phenolic resins. Another prerequisite of selective sulfonation comprises an
efficient pressure impregnation. This initial sulfonation stage is then followed by
a conventional acid sulfite cook at temperatures and H-factors selected according
to the grade desired. Hence, two-stage sulfite pulping with a preceding sulfonation
stage at low acidity or even neutral pH conditions makes possible the use of
pines and larches.
4.3 Sulfite Chemical Pulping 449
In the case of conventional and more simple one-stage acid sulfite pulping processes,
only a limited amount of wood species can be used. Most appropriate are
hardwoods with low resin contents and high density such as beech wood (Fagus
sylvatica) and certain eucalyptus species (E. globulus, E. saligna, E.urograndis, etc.).
Dense hardwoods with a low lignin content are favorable because of the high specific
pulp yield related to the volume of the digester. Replacing spruce with, for
example beech wood, results in an almost 50% higher yield at a given digester
volume (280 kg o.d. beech versus 190 kg o.d. spruce per m3 digester, respectively).
In the following section, four representative hardwoods – beech (Fagus sylvatica),
aspen (Populus tremulus), eucalypt (E. globulus) and birch (Betula pendula)
and one softwood species, spruce (Picea abies) – which together constitute the
most important wood raw material for acid sulfite pulping, are evaluated comparatively
with respect to their processability and unbleached pulp quality.
The chemical composition of the wood determines very important parameters
such as pulp yield and pulp properties. The purity of dissolving pulps is governed
by the content of noncellulosic carbohydrates and other impurities such as resins
or inorganic components of the wood raw material used.
Chemical analysis of the hardwood samples reveals high glucan and low xylan
contents for aspen and eucalypt. The low glucan and high xylan contents of birch
and beech, however, indicate low cellulose yield at high residual xylan contents in
the resulting dissolving pulps. Among the hardwood species, aspens shows a surprisingly
high mannose content. Spruce, as the only representative of softwoods
in this comparison, contains a relatively high glucan content and, together with
eucalypt, the lowest amount of hemicelluloses among the species investigated.
The hardwoods are characterized by a low and rather constant Klason lignin content
ranging from 18.9% to 21.0%, and by a high acid-soluble lignin content, with
the highest value by far determined for eucalypt. The low lignin content of the
hardwoods indicates a more efficient delignification as compared to spruce at given
cooking conditions.
The highest DCM-extractives contents were measured for birch and aspen, but
this may relate to a pitch problem during further processing of the corresponding
unbleached pulps.
Based on the chemical analysis of the main wood components, the highest cellulose
yields and cellulose purities can be expected for aspen and eucalypt. The
results of the chemical analysis of selected wood chips are detailed in Tab. 4.61
(see also Tab. 4.49).
The introduced five wood species were subjected to one-stage acid sulfite pulping
according to the procedure described in Section 4.3.5.1 (see also Fig. 4.157).
The cooking conditions applied namely the impregnation procedure, the cooking
acid composition, the liquor-to-wood ratios and the maximum cooking temperatures
were identical for beech, aspen, and eucalypt and comparable for spruce and
birch (Tab. 4.62). The slightly different cooking acid compositions in the case of
birch and spruce can be classified as rather insignificant with respect to their ion
product, [H+]·[HSO3
– ], which determines the rate of delignification.
450 4 Chemical Pulping Processes
Tab. 4.61 Chemical composition of beech, aspen, eucalyptus,
birch and spruce as used for the cooking experiments
(according to [14]).
Beech
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