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Kraft and sulfite pulps and two representatives of hardwood kraft pulps, on the
Basis of extended chemical characterization, is provided in Tab. 11.1.
Tab. 11.1 Comprehensive chemical characterization of a
representative selection of commercial paper-grade pulps [17].
Parameter Pine Spruce Eucalyptus Beech Spruce Spruce Beech
Kraft Kraft Sulfite Sulfite
ECF TCF ECF ECF TCF ECF TCF
Basic characteristics
Kappa number – 0.5 0.5 0.5 0.8 2.7 0.3 6.2
Brightness % ISO 89.0 90.7 89.7 87.6 85.9 92.7 90.3
Viscosity mL g–1 793 635 833 802 1020 868 1123
Extractives
DCM % od pulp 0.03 0.03 0.12 0.17 0.15 0.10 0.15
Acetone % od pulp 0.05 0.02 0.16 0.18 0.12 0.12 0.18
Alkali resistancies
R10 content % od pulp 87.0 87.2 91.9 90.0 87.7 87.4 84.6
R18 content % od pulp 87.1 88.0 94.6 93.6 89.8 90.5 87.6
Carbohydrates
Glucose % od pulp 84.7 86.1 80.4 73.3 89.7 91.6 84.9
Mannose % od pulp 6.6 5.8 0.3 0.2 5.2 5.0 1.2
Galactose % od pulp 0.2 0.2 0.1 0.1 0.0 0.0 0.0
Xylose % od pulp 7.3 6.9 18.4 25.5 4.1 2.7 12.2
Arabinose % od pulp 0.5 0.5 0.0 0.0 0.0 0.0 0.0
Pulp Properties and Applications
Tab. 11.1 Continued.
Parameter Pine Spruce Eucalyptus Beech Spruce Spruce Beech
Kraft Kraft Sulfite Sulfite
ECF TCF ECF ECF TCF ECF TCF
Hexenuronic acid (HexA) lmol g–1 1.1 1.5 1.4 1.1 0.7 0.7 0.6
Organochloric compounds ppm 130 33 203 n.d. <6 61 <6
Functional groups
Copper number % 0.3 0.2 0.8 0.5 1.0 1.3 1.4
Carbonyl groups (CCOA) lmol g–1 15 9 12 57 37
Carboxyl groups lmol g–1 37 46 84 131 54 40 70
Inorganic Compounds
Total ash % 0.33 0.19 0.19 0.34 0.30 0.20 0.23
Ca ppm 199 130 175 1208 655 453 916
Mg ppm 404 195 70 319 550 130 237
Si ppm 293 50 59 73 115 63 10
Fe ppm 49 11 6 16 25 4 2
Mn ppm 1.7 2.0 2.3 2.7 4.1 < 0.2 0.4
Water retention value (WRV) % 83.7 80.6 78.3 92.8 76.2 81.2 84.3
Zero-Span tensile index
dry Nm g–1 130.8 133.7 147.1 n.d. 113.1 103.6 98.8
rewetted Nm g–1 116.2 109.4 n.d. n.d. 96.5 82.9 84.4
The residual lignin content of all ECF- and the TCF-bleached softwood kraft
Pulps is far below 1, indicating a low tendency of light-induced yellowing. The
Two TCF-bleached sulfite pulps reveal slightly elevated kappa numbers, which
May be attributed to the applied bleaching concept, namely sequential alkaline
Oxidative bleachings step comprising oxygen delignification and hydrogen peroxide
Bleaching.
There are also some noticeable differences in pulp viscosity ranging from low
Level in the case of TCF-bleached softwood kraft pulp to generally high levels in
The case of the TCF-bleached sulfite pulps. The high bleaching selectivity of the
Latter is reflected in the high viscosity at a given brightness level.
Paper-Grade Pulp
The extractives content of a fully bleached commercial pulp depends on many
Different parameters, with the wood species, pulping, and bleaching processes
Being the most important influencing factors. The data in Tab. 11.1 confirm the
Predominant influence of the cooking process on the extractives content when
Comparing sulfite and kraft pulps based on spruce wood. The bleaching sequence,
However, seems not to exhibit a major influence on the extractives content. TCFand
ECF-bleached spruce sulfite pulps reveal similar resin contents. A further significant
Decrease in the extractives content due to bleaching operations may only
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High LODP, the high modulus in the stress-strain curve, the excellent swelling | | | Be expected when high dosages of, for example, ozone, or other bleaching chemicals |