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The magnefite cooking process provides a number of advantages over the regular
acid sulfite process, including better pulp strength properties, provided that the
kappa number is kept above a certain level (e.g., 30). This, as has been outlined
above, requires a high subsequent bleaching effort for obtaining pulps of full
brightness (88% ISO and higher). A modification to the magnefite process – the
two-stage neutral magnefite – has been introduced in which the pH is increased
to about 6.0–6.5 during the latter part of the cook by the addition of magnesium
hydroxide [13]. There, the first stage is carried out according to the classical magnefite
process (pH 3.7) and after a period of 90 min at approximately 165 °C,
(hydrated) MgO is injected into the digester until a pH of 6.5 is reached. The
amount of magnesium hydroxide slurry required to reach the target pH level is
equivalent to about 4.0–5.0% on o.d. wood. It is worth mentioning that the best
pulp strength properties are obtained when the MgO addition is carried out when
the cook is in the 60–65% yield range. The introduction of magnesium hydroxide
slurry into the digester reduces the temperature of the acid by up to 15 °C. Subsequently,
the temperature must be raised to 170–175 °C, which is the cooking temperature
of the second stage. This temperature is maintained for about 120–
150 min. The solubility of MgO can be increased by adding sodium salts, or even
better by introducing it into a sulfite spent liquor from a previous cook [10]. The
overall cooking time is about 1 h longer than for a one-stage magnefite cook at the
same kappa number. In the case of softwoods, the yield is quite comparable to
that of a regular magnefite pulp. Pulps were stronger in all categories than from
single-stage magnefite, and were much stronger than from conventional acid sulfite
pulping. They were said to be comparable in tensile and burst, but inferior in
tear strength to kraft pulps from the same wood furnish.
4.3 Sulfite Chemical Pulping 467
Even though the unbleached brightness of the two-stage neutral pulps is lower
as compared to the magnefite pulps, the bleachability of both pulps remains
equally good. The combination of elevated pH levels close to neutral conditions
and the high temperature causes the extraction of hemicelluloses. In the case of
hardwood pulps, a very low pentosan content (6.4%) and a rather high alpha-cellulose
content (90.3%) were observed [13]. This concept of two-stage magnesiumbase
pulping has been installed at the Weyerhaeuser mill at Cosmopolis,
Washington, to produce high reactive dissolving pulps, termed “HO”. In addition,
the two-stage neutral sulfite pulps show slow hydrating properties and good opacity,
which permits the production of pulps of a wide range of properties [14].
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