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reaction time required is short – 15–60 min is sufficient. The amounts of dithionite
vary, but are normally ca. 10 kg t–1 or 1% on fiber. As the number of available
Chromophores for the reduction process is limited, a brightness plateau is typically
reached at an input of between 1.2% and 1.5%. An addition above these levels
Triggers decomposition and the formation of thiosulfate. A technological alternative
To tower bleaching is the application of dithionite in the refiner. Although the
Brightness gains are slightly inferior, the application is simple and can eliminate
The need for a bleach plant.
As can be imagined, the reduction reactions may be reversible. For example, the
Reduction of an o-quinone to the catechol generates the leuco form, which can be
Re-oxidized by oxygen in the air. Despite this, the brightness of dithionite-bleached
Pulp is relatively stable in heat-induced aging. Stability is affected by light, UV radiation
Or transition metal-induced reactions of the phenolic groups within the
lignin, easily generating chromophores [35].
6.2
Bleaching with Hydrogen Peroxide
The application of hydrogen peroxide in bleaching mechanical pulp is by far older
Than its use in chemical pulp bleaching. A prerequisite of peroxide bleaching is
the “neutralization” of peroxide-decomposing transition metals (e.g., Mn). Chelation
Of the metal ions is achieved with compounds such as diethylene diamine
Penta-acetic acid (DTPA) or ethylene diamine tetra-acetic acid (EDTA) (see Section
II-5.4.2.4.5.1, Prerequisites of hydrogen peroxide application). The chelants are
Added most beneficially during screening after the refining process. This allows
Sufficient residence time and typically has the correct pH level (slightly acidic) for
effective chelation. The demand for chelant is between 0.1% and 0.3% on fiber (of
the commercial product with an active content of ~40%). The addition of chelant,
Together with the other chemicals (H2O2, NaOH, silicate) is another option,
Though it is slightly less effective because of the higher pH.
The limited aggressivity of hydrogen peroxide might be a disadvantage where
Delignification is required, but it may be advantageous if an improvement of
Brightness is the only target. In the past therefore, hydrogen peroxide bleaching
was often labeled as being “lignin-conserving”. As described in previous chapters,
This it not the case, and lignin is in fact removed during peroxide bleaching. Lignin
Side chains are cleaved and quinones oxidized to more water-soluble carboxylic
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Initially, the zinc hydroxide is filtered off and reprocessed to zinc dust. Then, | | | Acids. However, because hydrogen peroxide will not react easily with the |