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In TCF bleaching the brightness target of a final peroxide stage might require the
consumption of very large amounts of peroxide, and to achieve sufficient consumption
of H2O2 high temperature will be required. The application of pressure
is also recommended [50,51], with pressure applied ranging from 0.1 MPa to a
maximum of 0.5 MPa. These stages are frequently labeled as P(O) stage because
pressure is applied by oxygen gas addition. The positive effect was described as an
acceleration of an otherwise very slow brightening of the pulp. Later, pressurized
peroxide stages were also recommended for ECF sequences [56]. Several mills
have installed such equipment, although many typically operate without applying
pressure because bleaching is not improved by pressure or oxygen addition
[57,58]. This is in line with current knowledge of the reaction mechanism of alkaline
peroxide bleaching. The peroxide reactions are neither accelerated nor
improved by a moderate pressure increase, however, pressurized equipment is
more expensive than nonpressurized counterparts.
7.6.6
Technology of H2O2 Bleaching
Andreas W. Krotscheck
Atmospheric Peroxide Bleaching
The process flowsheet of a typical atmospheric peroxide bleaching system is
shown schematically in Fig. 7.122. Caustic soda is added to the MC pulp coming
from the previous bleaching stage, for example, to the repulper of a drum washer
or to the dilution conveyor after a wash press. The alkaline pulp falls into a standpipe
and is mixed with peroxide as it enters the MC pump.
The pump provides good mixing of the peroxide into the pulp suspension, and
a dedicated mixer is often not required. The pulp proceeds to an atmospheric
upflow reactor where the bleaching reaction takes place. Depending on the feed
requirements of the subsequent washing equipment, the pulp slurry is discharged
from the reactor either at low or medium consistency.
MC PUMP REACTOR WASHING
Pulp from
Preceding
Stage
Pulp to
Next stage
NaOH
H2O2
Fig. 7.122 Process flowsheet of a typical atmospheric peroxide bleaching system.
866 7Pulp Bleaching
Washing after a peroxide stage is usually carried out with single-stage washing
equipment, for example, with a wash press, a single-stage Drum Displacer™, an
atmospheric diffuser, or a vacuum drum washer.
The material of construction for wetted parts in a peroxide stage is typically a
higher grade of austenitic stainless steel.
Further information regarding atmospheric peroxide bleaching equipment,
including medium-consistency pumps and atmospheric upflow reactors, is provided
in Section 7.2. Pulp washing is detailed in Chapter 5.
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Thermal Stability of H2O2 and Bleaching Yield | | | Application in Chemical Pulp Bleaching |