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NaOH 90.0 90.0
Na2S 40.0 39.0
Na2CO3 19.8 26.2
Na2SO4 4.5 8.0
Na2S2O3 2.0 4.0
Na2SO3 0.6 0.9
Other compounds 2.5
Total alkali (TA) 156.9 170.6
Total Sulfur (TS) 47.1 19.7
Effective alkali (EA) 110.0
Active alkali (AA) 130.0
4 Chemical Pulping Processes
In kraft cooking technology, the concentration of active chemicals are expressed
according to the following terminology:
_ Total alkali (TA) comprises the sum of all sodium salts, the
amount of total titratable alkali (TTA), the sum of sodium hydroxide,
sodium sulfide and sodium carbonate. Most important for
the characterization of the cooking liquor are the expressions
effective alkali (EA), active alkali (AA) and sulfidity (S), which are
defined according to Eqs. (3–5).
_ The EA-concentration (eq. 3) is equivalent with the concentration
of hydroxide ions because the sulfide ions are completely dissociated
to hydrogen sulfide ions and hydroxide ions under the conditions
occurring throughout kraft pulping (see Fig. 4.2).
EA = NaOH + 0.5 Na 2 S (3)
_ The AA-concentration (eq. 4) includes the whole sodium sulfide
concentration and can be used to express the sulfidity of the aqueous
solution according to Eq. (5):
AA =NaOH + Na 2 S (4)
S _
Na 2 S
AA _ 100_ _5_
For simplicity, all the chemicals are calculated as sodium equivalents and
expressed as weight of NaOH or Na2O (see Tab. 4.2).
_ The inter-relationship between EA- and AA-concentrations can be
displayed by Eq. (6):
EA = AA _1 _ 0_5 _ S _
AA=
EA
_1 _ 0_5 _ S _ _6_
where S is expressed as a fraction.
In pulping chemistry, molar units are preferred over weight units. As mentioned
previously, the OH– ion concentration is equivalent to the effective alkali
concentration. The HS– ion concentration, however, corresponds to only half of
the sodium sulfide concentration. The OH– ion and the sulfide ion concentrations
in molar units of the white liquor introduced in Tab. 4.2 are depicted in Tab. 4.3.
Based on molar units, the sulfidity of the white liquor can be calculated by
using Eq. (7):
S _
2 _ _ HS _
_ HS _ OH _ _ 100_ _7_
4.2 Kraft Pulping Processes
Tab. 4.3 Molar concentrations of hydroxide ions, hydrogen
sulfide ions and carbonate ions in the white liquor presented in
Tab. 4.2.
Species mol/l
OH– 2.75
HS– 0.50
CO3
2– 0.25
Reversed, the molar concentration of H2S may be derived from sulfidity (fraction)
and [OH– ]according to Eq. (8):
_ HS _ _
S _ _ OH _
_2 _ S _ _8_
Residual amounts of sodium carbonate in the white liquor are determined by the
extent of the causticizing reaction, which is an equilibrium reaction. The efficiency
of this reaction is characterized by the causticity (C) or causticizing efficiency,
and thus the concentration of sodium carbonate according to Eq. (9):
C _
NaOH
NaOH Na 2 CO 2 _ 100_ _9_
expressed as sodium hydroxide equivalents.
The causticity is a function of reaction time and the total salt concentration
(e.g., TTA). In dilute aqueous solutions and with longer retention times, the equilibrium
is shifted to the sodium hydroxide side, which in fact corresponds to a
higher causticizing efficiency. Table 4.2 shows also oxidized sulfur compounds,
such as sodium sulfate, sodium sulfite or sodium thiosulfate, which can be considered
inert with respect to the pulping reactions. From a process point of view,
the amount of oxidized sulfur compounds must be kept at the minimum achievable
level. The ratio between the reduced sulfur compounds (sodium sulfide) and
the total sulfur is designated as degree of reduction (DR). Actually, DR can be
related to both the total sulfur or the sulfate sulfur only, respectively [Eq. (10)]:
DRtot _
Na 2 S
Na 2 S Na 2 SO 4 Na 2 SO 3 Na 2 S 2 O 3 _ 100_ _10_
DRSO 2_ 4 _
Na 2 S
Na 2 S Na 2 SO 4 _ 100_ _10_
Table 4.4 lists the characteristics of the white liquor given in Tab. 4.2 by using the
expressions of Eqs. (5), (9) and (10).
4 Chemical Pulping Processes
Tab. 4.4 Sulfidity and efficiency of transformation to active
cooking chemicals based on the white liquor composition
given in Tab. 4.2.
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