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Bleaching of eucalyptus kraft pulps with chlorine dioxide : Factors affecting the efficiency of the final D stage

Sevastyanova, Olena (author)
KTH,Träkemi och massateknologi
Forsström, A. (author)
Wackerberg, E. (author)
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Lindström, Mikael (author)
KTH,Fiber- och polymerteknologi
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 (creator_code:org_t)
2012
2012
English.
In: TAPPI Journal. - 0734-1415. ; 11:3, s. 43-53
  • Journal article (peer-reviewed)
Abstract Subject headings
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  • We investigated the bleaching efficiency of the final chlorine dioxide (D 2) stage in the D 0(EP)D 1D 2 bleaching sequence, focusing on the effect of pH in relation to the bleaching history of pulp samples. The samples used were unbleached kraft Eucalyptus grandis pulps with kappa no. 14.8 and the same pulp oxygen-delignified to kappa nos. 12 and 9.8. The samples were bleached according to the D 0(EP)D 1 sequence to a brightness of about 86% ISO and then submitted to the final D 2 stage under identical conditions (e.g., chlorine dioxide charge, time, temperature, and final pH). The target final brightness was 90.5% ISO. Changes in the kappa number, brightness, viscosity, and contents of hexenuronic acid, 4-O-methylglucuronic acid, and the total amount of carboxylic acid (COOH) groups in pulps were monitored during the bleaching sequence. The final brightness of eucalyptus kraft pulps increased when the terminal pH of the D 2 stage was raised from 3.0 to 6.5. The 90.5% ISO target brightness in the D 2 stage was achieved for all pulps within a pH range of 4.5-6.5, but this required adjusting final pH for individual samples. The optimal pH value with respect to pulp viscosity was between 3 and 5. Despite dissimilar conditions applied in previous bleaching stages, the samples after the D 1 stage revealed similar residual lignin contents as shown by kappa number analysis. The content of hexenuronic acid in the samples, however, varied broadly, from 2 to 26 mmol/kg. Conductometric titration showed different amounts of carboxylic acid groups in pulps after the D 1 stage, of which hexenuronic acid accounted for only a minor part. The variations in the fiber charge resulted from the different bleaching conditions applied before the D 2 stage. The fiber charge affected the alkali demand in the final D 2 stage, whereas variations in the alkali demand affected the initial pH and associated process kinetics. Lower total fiber charge was found to be beneficial for improved final brightening and viscosity when bleached at higher final pH. Application: This study will help pulp mill engineers to better understand how a pulp's oxidative history may affect the process kinetics in the final D bleaching stage. Fiber charge is important when selecting optimal pH for the final brightening of eucalyptus kraft pulps.

Subject headings

NATURVETENSKAP  -- Kemi (hsv//swe)
NATURAL SCIENCES  -- Chemical Sciences (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Kemiteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Chemical Engineering (hsv//eng)

Keyword

Bleaching condition
Bleaching efficiency
Bleaching sequence
Carboxylic acid groups
Chlorine dioxides
Conductometric titrations
Effect of pH
Eucalyptus grandis
Eucalyptus kraft pulp
Fiber charges
Final pH
Hexenuronic acid
Identical conditions
Initial pH
Kappa numbers
pH range
pH value
Process kinetics
Pulp samples
Pulp viscosity
Residual lignins
Unbleached kraft
Carboxylic acids
Cleaning
Fibers
Kraft process
Kraft pulp
Luminance
Optimization
Paper and pulp mills
pH effects
Unbleached pulp
Bleaching
Chlorine Dioxide
Kraft Pulps
Paper Mills
Ph
Samples
Unbleached Pulps

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ref (subject category)
art (subject category)

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Sevastyanova, Ol ...
Forsström, A.
Wackerberg, E.
Lindström, Mikae ...
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NATURAL SCIENCES
NATURAL SCIENCES
and Chemical Science ...
ENGINEERING AND TECHNOLOGY
ENGINEERING AND ...
and Chemical Enginee ...
Articles in the publication
TAPPI Journal
By the university
Royal Institute of Technology

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