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Determining silica solubility in bayer process liquor

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Abstract

The efficient precipitation of dissolved silica from Bayer process liquor is essential for the production of high-quality alumina and the reduction of excessive scaling in the heat exchangers in the evaporation building of Bayer processes. The accurate prediction of silica solubility in Bayer liquor is one of the key parameters in improving the design and operation of the desilication process. Previous findings, particularly with respect to the influence of temperature and concentrations of caustic soda and alumina on the solubility of silica, are inconclusive. In this article, experimental results are presented over a wide range of temperature and alumina and caustic soda concentrations. Attempts are made to utilize artificial neural networks for identifying the process variables and modeling. The radial basis function neural network architecture was used successfully to generate a nonlinear correlation for the prediction of the solubility of silica in Bayer process liquor. The resulting correlation can predict the present data and the control data of other investigators with good accuracy.

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Abbreviations

B:

CB0/CA0

C:

CC0/CA0

CA0 :

Concentration of Na2SiO3 in the liquor (kg/m3)

CB0 :

Concentration of NaAlO2 in the liquor (kg/m3)

CC0 :

Concentration of H2O in the liquor (kg/m3)

CD0 :

Concentration of caustic soda in the liquor (kg/m3)

CAL :

Alumina concentration [kg (Al2O3)/m3]

Cb :

Bulk silica concentration [kg (SiO2)/m3]

C*:

Saturation concentration of silica [kg/m3]

C*:

Output vector

D:

CD0/CA0

G:

Green function

I:

Identity matrix

kDSP :

Reaction constant (m4/kg · min.)

KD :

Equilibrium constant of dissolution reaction

KP :

Equilibrium constant of the precipitation reaction

m:

Constant in Equation 12

M:

Stoichiometric constant

N:

Number of exemplar

n:

DSP deposition rate (kg/m2 · min.)

t:

Center of Gaussian activation function

T:

Temperature (K)

x:

Input vector

X*:

Equilibrium fractional conversion of Na2SiO3

w:

Weight vector

Φ:

Interpolation matrix

φ(·):

Activation function

λ:

Regularization parameter

σ:

Radius of Gaussian activation function

References

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M. Jamialahmadi earned his Ph.D. in chemical engineering at Aston University in 1983. He is currently a professor and dean of the Petroleum Industry Research Center, Ahwar, Iran.

H. Müller-Steinhagen is currently a professor and head of the School of Engineering in the Environment, University of Surrey.

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Müller-Steinhagen, H. Determining silica solubility in bayer process liquor. JOM 50, 44–49 (1998). https://doi.org/10.1007/s11837-998-0286-6

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  • DOI: https://doi.org/10.1007/s11837-998-0286-6

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