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A part of the cooking chemical cycle, the preparation of white liquor consists of
Several process steps, and is accompanied by a separate chemical loop, the lime
Cycle (Fig. 9.10). The generated white liquor ought to contain a minimum of residual
Sodium carbonate in order to maintain the dead solids load in the cooking
Chemical cycle as low as possible.
Cooking /
Washing
COOKING
CHEMICAL
CYCLE
Evaporation
Recovery
Boiler
Smelt
Dissolving
Green liquor
filtration /
Slaking clarification
Causticising
Whilte liquor
Filtration
LIME
CYCLE
Lime reburning
Lime mud
Washing
Fig. 9.10 Major unit operations of causticizing and lime
Reburning in the context of the kraft chemical recovery cycle.
Process wise, the smelt coming from the smelt spouts of the recovery boiler
Drops into the smelt dissolving tank and becomes dissolved in weak wash, thereby
Forming green liquor. Since the smelt carries impurities which disturb the subsequent
Process steps, those must be removed by clarification or filtration of the
Green liquor. Then follow slaking, causticizing and white liquor filtration. After
Separation from the white liquor, the lime is washed and reburned for re-use in
Causticizing.
Chemistry
The basic chemical reactions in the causticizing plant and lime kiln start with the
Exothermic slaking reaction, where burned lime, CaO, is converted into calcium
hydroxide, Ca(OH)2 (slaked lime):
CaO _ H2O→Ca_OH_2 DH _ _65 kJ kmol_1 _12_
Recovery
Then the causticizing reaction transforms sodium carbonate from the smelt,
Na2CO3, to sodium hydroxide needed for cooking, thereby giving rise to calcium
carbonate, CaCO3:
Na2CO3 _ Ca_OH_2 _ 2NaOH _ CaCO3 DH≈ 0 kJ kmol_1 _13_
Calcium carbonate is separated from the white liquor and reburned at a temperature
above 820 °C following the endothermic calcination reaction:
CaCO3→CaO _ CO2 DH _ _178 kJ kmol_1 _14_
From a chemical perspective, white liquor is fundamentally characterized by
Active or effective alkali concentration, by sulfidity, as well as by causticizing and
Reduction efficiencies (see Section 4.2.2). In the causticizing plant, the total titratable
Alkali (TTA) is also of interest. Causticizing efficiency, CE, and TTA are
defined as follows:
CE _
NaOH
NaOH _ Na2CO3 _ 100_ _15_
TTA _ NaOH _ Na2S _ Na2CO3 _16_
The concentrations of the sodium salts in Eqs. (15) and (16) are, by convention,
expressed in g L–1 and in terms of NaOH or Na2O equivalents.
Lime (CaO), calcium hydroxide (Ca(OH)2) and calcium carbonate (CaCO3), also
referred to as “lime mud”, all have a very low solubility in water. Reactions related
To these components are basically happening in the solid phase.
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As minor streams are neglected, such as dust, sulfur dioxide, reduced sulfur compounds | | | The equilibrium of the slaking reaction is far on the product side of Eq. (12), |