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Acids. However, because hydrogen peroxide will not react easily with the

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  1. A Principal Reaction Schema for Oxygen Delignification
  2. Are degraded by alkali-catalyzed reactions. Thus, the organic material of the black
  3. Carbohydrate Reactions in Dioxygen-Alkali Delignification Processes
  4. Chemistry of hydrogen peroxide bleaching
  5. Comparison to Sulfonation Reactions under Conditions of Neutral Sulfite Pulping
  6. Dr Carter says he decided to improve his presentations because

Aromatic systems of lignin, its level of removal is moderate. In mechanical pulp

Bleaching, this is an advantage, and the yield and optical properties (opacity) are

Only moderately affected by the bleaching process. An example of the response of

Mechanical pulp to hydrogen peroxide is shown in Fig. 6.1.

Peroxide addition yields increasing brightness with charges up to about 5%. The

plateau is reached at about 82% ISO for softwood pulp, spruce (Picea spp.) and pine

(Pinus spp.), and 86% ISO for hardwood mechanical pulp, poplar and aspen (Populus

Bleaching of Mechanical Pulp

Bleaching with Hydrogen Peroxide

Spp.). The wood species, the age of the wood, storage of the logs and the bark content

Each have a huge impact on bleachability and the brightness ceiling.

During the bleaching process, a variety of compounds are dissolved, the main ones

Being acetic acid (from acetyl groups on carbohydrates) and low molecular-weight

Polyoses. Lignin dissolves only to a small extent. However, because the pulping process

Solubilizes only a small part of the wood, rather high effluent loads can result

From bleaching. Top brightness requires a high peroxide input and, for its activation,

A similarly large amount of caustic soda. The resultant brightness in bleaching softwood

TMP with increasing input of hydrogen peroxide is shown graphically in

Fig. 6.2, where different amounts of caustic soda were applied to achieve the best

Response in brightness. For a given residence time and temperature, there is an optimum

Level of activation. The shape of the curves shows, for the ratio of H2O2 to

NaOH, an increasingly wider range of tolerance. Clearly, the more peroxide

Applied, the less critical is the correct amount of caustic soda added.

0,5 1,0 1,5 2,0

H

O

H

O

H

O

H

O

Brightness [% ISO]

NaOH-charge [%]

Fig. 6.2 Increase in brightness with optimized charges of NaOH

for different peroxide amounts. Bleaching at 65 °C, 3 h, 20%

consistency, with a constant addition of 2% sodium silicate.

An inadequate activation results in an insufficient consumption of H2O2, but

Too-high charges are similarly detrimental, and the alkalinity consumes peroxide

And brightness decreases again. The process cannot be operated with the aim of

Consuming all of the hydrogen peroxide applied. An example of the brightness

Resulting from a constant input of hydrogen peroxide but a variation of the

Amount of caustic soda is shown in Fig. 6.3. The comparison of best brightness


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Читайте в этой же книге: Fig. 4.25 Exchange of hydroxyl groups by sulfonate groups | The X-groups as part of the A-groups in spruce lignin. | A conical refining gap inside one refiner housing (Fig. 4.30). | The control strategy of the paper machine. Varying refiner positions (1st stage, 2nd | Stretched length directionally) | Screens. The shives and stiff long fibers are removed as rejects from below, | Separation according to material density is carried out using hydrocyclones | In a TMP mill, heat recovery plays an essential role in economic operating. Normally, | Oxidative processes. | Initially, the zinc hydroxide is filtered off and reprocessed to zinc dust. Then, |
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Bleaching with Dithionite 1125| And remaining residual allows the conclusion to be made that the residual must

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