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This model simulates the causticising reaction of green liquor with slaked lime. The reversible causticising reaction can be represented by,
Ca(OH)2 + Na2CO3 <-----> CaCO3 + 2NaOH
The model calculates the extent of reaction and the resulting changes in outlet stream composition.
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Data |
Unit |
Description |
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Set |
Item |
Type |
Native |
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Equipment Properties |
Height |
Length |
ft |
Height of cylindrical causticiser |
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Diameter |
Length |
ft |
Diameter of cylindrical causticiser |
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Rate |
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A parameter to control the rate of forward reaction in causticising default=1.0) |
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ExtOfCaustReact |
Fraction or Percent |
Fraction |
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The extent of reaction is computed from a model similar to the one presented in [1]. The causticiser is assumed to be an ideal CSTR in which case the following equation applies.
V/F0 = X/Rc
where, the rate of causticising, Rc is given by the kinetic model in [1],
Rc = k1( [NaCO3]0 (1-X) )a - k2(EA0+X [NaCO3]0 )b
k1 = Rf exp (-29.0/RT + 4.25)
k2 = exp (-25.6/RT - 8.3)
a = 1.0
b = 3.0
Nomenclature
V Volume of the CSTR
F0 Molar feed rate of sodium carbonate
X Fractional conversion of sodium carbonate
Rc Rate of causticising
[NaCO3]0 Initial sodium carbonate concentration g/l as Na2O
EA0 Initial Efffective alkali g/l as Na2O
R Gas constant
T Absolute temperature
Rf Rate of forward reaction (user specified, default = 1.0)
The exit conversion X is calculated iteratively from the above equations.
Missing Stream(s)!
Solution: check if all the streams are connected to the equipment.