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The discovery of chlorine dioxide is generally credited to Sir Humphrey Davy, who
reported the results of the reaction of potassium chlorate with sulfuric acid which
destroyed the color of vegetable dyes [1]. In the 1920s, Schmidt et al. reported that
chlorine dioxide is a very selective bleaching agent which does not react with carbohydrates
[2,3]. However, the use of chlorine dioxide on an industrial scale began
only after World War II, when both suitable manufacturing processes from
sodium chlorate and corrosion-resistant materials became available. In 1946, three
Swedish kraft pulp mills began to apply chlorine dioxide for the production of
highly bleached kraft pulps. Shortly after that, Canadian and US American kraft
mills followed suit by installing chlorine dioxide bleaching stages. It can be stated
that, together with the invention of the Tomlinson furnace, chlorine dioxide
bleaching technology contributed to the breakthrough for the kraft process against
the sulfite process. Since such modification, it became possible to produce fully
bleached pulps (>88% ISO) with high strength properties (no significant decrease
in strength during bleaching operations). In its early application, chlorine dioxide
was solely used at, or near the end of bleaching sequences such as CEHD,
CEHDED, or CEDED refer to (Tab. 7.2). The use of chlorine dioxide in the delignification
stage began only when it became known that a partial replacement of
chlorine by chlorine dioxide improves final pulp quality [19]. In the bleaching of
hardwood sulfite pulps, it was found that the formation of sticky chlorinated res-
734 7Pulp Bleaching
ins could be avoided when chlorine dioxide was used instead of chlorine. In the
case of kraft pulps, 5–10% of chlorine was replaced with the equivalent amount of
chlorine dioxide to further improve the strength properties of the pulps. The
debate about the use of molecular chlorine for pulp bleaching evolved from
reports of the research conducted during the Swedish project “Environment/Cellulose”
[4]. As a result, the study showed that pulp mill effluents entering the Gulf
of Bothnia, Sweden, severely affected the diversity, biomass, and distribution of
invertebrates and plants. In the sediments outside the Swedish coast, chlorinated
compounds related to bleach plant effluents were detected which indicated a high
persistence of such substances. Moreover, the use of molecular chlorine for pulp
bleaching produces polychlorinated dibenzo- p -dioxins (PCDD) and dibenzofurans
(PCDF). The pattern of the tetrachlorinated congeners, as well as their concentration,
depends drastically on the amount of molecular chlorine applied in the first
delignification stage. It has been shown that the concentration of these compounds
decreases as the degree of substitution of chlorine with chlorine dioxide
increases, and cannot usually be detected at 60% chlorine dioxide substitution or
higher [5].
With this knowledge, authorities around the world began to implement new
regulations that limited the amount of chlorinated organic material discharged
from bleaching operations into the environment. Consequently, chlorine dioxide
has become a very popular bleaching agent in place of molecular chlorine. Today,
chlorine dioxide is certainly the most important bleaching chemical, since the use
of elemental chlorine is increasingly abandoned. Chlorine dioxide’s high selectivity
towards the oxidation of chromophoric structures makes it the first choice for
both delignification and pulp brightening, while retaining strength properties.
Furthermore, it meets the current environmental regulations in most countries by
generating approximately five times less chlorinated organic material as compared
to chlorine.
7.4.2
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