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Modeling and Optimization of Galena Dissolution in Hydrochloric Acid: Comparison of Central Composite Design and Artificial Neural Network

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^{2}of 0.991 and 1.00, respectively. A non-dominated optimal response of 85.25% yield of lead at 343.96 K leaching temperature, 3.11 M hydrochloric acid concentration, 0.021 g/ml solid/liquid ratio, 362.27 rpm stirring speed and 87.37 min leaching time was established as a viable route for reduced material and operating cost using RSM.

KEYWORDS

1. Introduction

Lead is a naturally occurring metallic element usually associated with other ore minerals such as pyrite, sphalerite, quartz and barite. Trace amounts of other elements including gold are sometimes found with lead ore. The most common ore mineral of lead is galena (PbS) also known as lead sulphide. Lead’s high density, atomic number, and formability form the basis for use of lead as a barrier that absorbs sound, vibration, and radiation. Lead has no natural resonance frequencies; as a result, sheet-lead is used as a sound deadening layer in the walls, floors, and ceilings of sound studies. Organ pipes are often made from a lead alloy, mixed with various amounts of tin to control the tone of each pipe. Lead is an established shielding material from radiation in nuclear science and in X-ray rooms due to its denseness and high attenuation coefficient. Molten lead has been used as a coolant for lead-cooled fast reactors [1] . The single most important commercial use of lead is in the manufacture of lead-acid storage batteries.

Response surface methodology (RSM) was developed by Box and Wilson [2] to enable the improvement of manufacturing processes in the chemical industry. It focused on optimizing chemical reactions in order to obtain, e.g., high yield and purity at low costs. This was accomplished through the use of sequential experimentation, involving factors such as temperature, pressure, duration of reaction, and proportion of reactants. The same methodology can be applied to model or optimize any response that is affected by the levels of one or more quantitative factors.

The most popular RSM is the central composite design (CCD). A CCD has three groups of design points: 1) two-level factorial or fractional factorial design points, 2) axial points (sometimes called star points), and 3) centre points. CCDs are designed to estimate the coefficient of a quadratic model. All point description is in terms of coded values of the factors.

Artificial Neural Network (ANN) is an empirical tool, which is analogous to the behavior of biological neural structures [3] . Neural networks are powerful tools that have the abilities to identify underlying highly complex relationships from input-output data only [4] . For the past two decades, artificial neural networks (ANNs), and, in particular, feed-forward artificial neural networks (FANNs), have been extensively studied to present process models, and their use in industry has been rapidly growing [5] .

Although response surface methodology (RSM) and artificial neural network (ANN) have been applied in several areas, there hasn’t been any reported work, to the best of our knowledge, of their application on lead dissolution from Nigerian galena ore. The present work therefore intends to identify the most significant factors and their possible interactions which influence the overall efficiency of the dissolution of lead from galena; analyze their effects and predict the possible route(s) to the desired optimal; evaluate and compare the dissolution efficiency of the galena ore using RSM and ANN, thus, establishing a faster and cost-effective means of extracting lead from galena ore for possible industrial applications.

2. Materials and Methods

2.1. Material

Sample Mining and Preparation

The galena ore used for this study was collected from Abakaliki, Enyigba mining site in Ebonyi State of Nigeria. The galena ore was finely pulverized and sieved with a 75 µm size sieve. All experiments were performed with the 75 µm fraction. HCl solutions were prepared from analytical grade reagents with deionized water.

2.2. Methods

2.2.1. Spectrophotometric Analysis

The X-ray fluorometer (XRF), X-supreme 600 oxford instruments was used for the elemental analysis of the ore. The mineralogical analysis of the ore was done using ARL X’TRA X-ray Diffractometer, Thermoscientific with the serial number 197492086 with CuKα (1.54 Å) radiation generated and 40 mA and 45 kV. This unit comprises of a single compact cabinet. The cabinet houses a high speed, high precision Goniometer; high efficiency generator (X-ray) and an automatic sample loading facility.

The petrographic slides of galena ore were prepared using Epoxy and Lakeside 70 media according to the method of Hutchison [6] .

2.2.2. FTIR and SEM Analysis

FTIR analysis was carried out using Buck Scientific M530 Infrared Spectrophotometer. SEM analysis was carried out using Q250 by FEI model from the Netherlands.

2.2.3. Experimental Procedure

Leaching experiments were performed in a 500 ml glass reactor fitted with a condenser to prevent losses through evaporation. The two major variables (heat and stirring rate) necessary for accelerating the rate of chemical reaction was provided by the aid of a magnetically-stirred hot plate (Model 78HW-1). For every leaching experiment, the solution mixture was freshly prepared by dissolving the required mass of the ore sample in the acid solution at the required temperature. At the end of each reaction time, the undissolved materials in the suspension was allowed to settle and separated by filtration. The resulting solutions were diluted and analyzed for lead using atomic absorption spectrophotometer (AAS).

The mole fraction of lead passing into the solution from galena was calculated by the formula given in Equation (1), where x designates quantity dissolution.

$x=\frac{\text{Amount of Pbpassing into the solution}}{\text{Amount of Pb in original sample}}$ (1)

2.2.4. Design of Experiment

The process variables affecting the dissolution of galena in hydrochloric acid were investigated using RSM combined with five-level, five factor fractional factorial design as established by Design Expert software (10.0 rented version). The process variables were leaching temperature, acid concentration, solid/liquid ratio, stirring rate and leaching time. The response variable was chosen as% yield of lead. The factor levels were coded as −α, −1, 0, +1 and +α. The range and levels are shown in Table 1.

A total of 32 runs were carried out to optimize the process variables and experiments were performed according to the actual experimental design matrix shown in Table 2. The experiments were performed randomly to avoid systemic error. The results were analyzed using the analysis of variance (ANOVA), contour, and response surface plots. In RSM, the most widely used second-order polynomial equation (Equation (2)) developed to fit the experimental data and identify the relevant model terms may be written as:

$Y={\beta}_{0}+{\displaystyle \underset{i=1}{\overset{k}{\sum}}{\beta}_{i}{x}_{i}}+{\displaystyle \underset{i<j}{\sum}{\displaystyle \sum {\beta}_{ij}{x}_{i}{x}_{j}}}+{\displaystyle \underset{i=1}{\overset{k}{\sum}}{\beta}_{ii}{x}_{i}^{2}}+\epsilon $ (2)

where Y is the predicted response variable which is the% yield of lead in this study,
${\beta}_{0}$ is the constant coefficient,
${\beta}_{i}$ is the i^{th} linear coefficient of the input variable
${x}_{i}$ ,
${\beta}_{ii}$ is the i^{th} quadratic coefficient of the input variable
${x}_{i}$ ,
${\beta}_{ij}$ is the different interaction coefficients between the input variables
${x}_{i}$ and
${x}_{j}$ and ε is the error of the model.

3. Results and Discussion

3.1. Results of Characterization Studies

3.1.1. Elemental Composition by XRF

The results of the elemental composition of galena by X-ray fluorescence technique showed that the galena mineral exist mainly as PbS with metals such as Na, Mg, Al, Ca, Fe and Zn occurring as minor elements, and K, Cr, and Sr as traces. The elemental analysis gave Pb (60.01%), S (14.66%), Fe (4.32%), Na (3.78%), Si (7.69%), Mg (1.21%), Al (1.94%), P (1.37%), Cl (1.19%), K (0.09%), Ca (1.99%), Cr (0.01%), Mn (0.49%), Zn (1.22%), and Sr (0.04%).

3.1.2. Phase Studies by XRD

The analysis of galena by X-ray diffraction gives a better description in terms of

Table 1. Levels of independent variables for CCD experimental design.

the mineral phases present in the ore. Table 2 present the results of the X-ray diffractogram of the ore and shows that the ore exist mainly as lead sulphide (PbS).

The galena ore gave three major peaks at 2.96, 3.42, and 2.09 Å, respectively as shown in Figure 1. All these supported the results of the elemental analysis by XRF.

Table 2. The X-ray diffraction data of the galena ore showing the angle 2θ and d-values of the compounds identified, with their relative intensity (%).

JCPDS File No.: Joint Committee on Power Diffraction Standards File Number.

Figure 1. X-ray diffraction pattern of galena ore.

3.1.3. FTIR Analysis of Galena

The FTIR spectra of galena ore is shown in Figure 2. The spectrum of the ore exhibit absorption bands at 3821 cm^{−1}, 3652 cm^{−1}, 3353 cm^{−1}, 2958 cm^{−1}, and 2564 cm^{−1}. These are attributed to O-H stretching. The band at 1410 cm^{−1} is

Figure 2. FTIR spectrum of galena ore.

attributed to O-H bending. The bands at 3519 cm^{−1}, 3353 cm^{−1} and 2564 cm^{−1} are attributed to N-H stretching. The band at 2564 cm^{−1} which is attributed to S-H stretching confirms the presence of sulphur in the ore. The band at 1634 cm^{−1} is attributed to Si-O and Al-O stretching while the band at 1634 cm^{−1} is also attributed to Al-O-H stretching.

The FTIR result is in agreement with XRF and XRD results which confirmed the presence of the minerals detected.

3.1.4. SEM Analysis of Galena

The scanning electron micrograph (SEM) of galena ore was obtained with magnifications of 240×, 520×, 1000×, and 1500× respectively as shown in Figure 3. The average cell diameter of the ore ranges from 8 to 62 µm while the average cell density ranges from 0.0042 to 1.13 cells/mm. The results indicate that the ore particles are very cohesive, forming an aggregate mass that appeared to have been formed by several flaky particles stacked together in form of agglomerates [7] . The particles have irregular shapes with rough edges, and are highly crystalline due to the high level of purity of the ore.

(a) (b)(c) (d)

Figure 3. SEM images of galena ore showing magnifications of 240× (a), 520× (b), 1000× (c), and 1500× (d) respectively.

The central composite design (CCD) for the leaching of lead from galena using hydrochloric acid is shown in Table 3 with the experimental values.

3.2. RSM Modelling

The responses obtained from different experimental runs carried out by combination of five variables are tabulated in the response column of Table 3. The five

Table 3. Fractional central composite design for galena dissolution in hydrochloric acid (HCl).

experimental variables gave a total of 32 experimental runs comprising of 26 individual runs and 6 similar runs. The responses obtained from various experimental runs were quite unique, indicating that each of the factors have considerable effect on the response.

3.3. Statistical Analysis

To determine the adequacy of the models depicting the removal of lead by the dissolution of galena in hydrochloric acid, two different tests, i.e. the lack of fit test and the model summary statistics, were conducted. From the lack of fit test, the highest order polynomial with non-significant p-value and is not aliased would normally be chosen. This test is used in the numerator in an F-test of the null hypothesis and indicates whether a proposed model fits well or not. It compares the variation around the model with pure variation within replicated observations and measures the adequacy of the model based on response surface analysis [8] . The results from the lack of fit test indicated that the 2FI, linear and the cubic model (aliased) did not provide a good description of the experimental data. The results are tabulated in Table 4. From the model summary statistics, it can be seen that the R-squared, adjusted R-squared and the predicted R-squared values for the quadratic model (0.9916, 0.9762, and 0.8565) showed a better correlation when compared with the cubic model (0.9948, 0.9732 and −1.4789) and the linear model (0.7281, 0.6758 and 0.6545) as shown in Table 5. The measure of how efficient the variability in the actual response values can be explained by the experimental variables and their interactions is given by the R-squared value. If the R-squared predicted and adjusted are too far from each other, there may be a problem with either the data or the model [8] . The results are tabulated in Table 5. The afore-mentioned results indicate that the quadratic model provided an excellent explanation for the relationship between the independent variables and the corresponding response. With respect to these results, the effect of each

Table 4. Lack of fit tests.

df = degree of freedom.

Table 5. Model summary statistics.

PRESS = Predicted residual sum of squares.

parameter was evaluated using the quadratic model as shown in Table 6.

The second-order model tested at the 95% confidence level obtained for extraction of lead from galena is shown in Equation (3):

$\begin{array}{c}\text{Yield}=83.52+3.44{X}_{1}+3.39{X}_{2}-3.57{X}_{3}+3.71{X}_{4}+3.41{X}_{5}-0.31{X}_{1}{X}_{2}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}+0.24{X}_{1}{X}_{3}-0.28{X}_{1}{X}_{4}-0.35{X}_{1}{X}_{5}+0.37{X}_{2}{X}_{3}-0.14{X}_{2}{X}_{4}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}-0.24{X}_{2}{X}_{5}+0.36{X}_{3}{X}_{4}-0.26{X}_{3}{X}_{5}-0.77{X}_{4}{X}_{5}-2.23{X}_{1}^{2}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}-2.25{X}_{2}^{2}-2.07{X}_{3}^{2}-2.26{X}_{4}^{2}-1.96{X}_{5}^{2}\end{array}$ (3)

The results were analyzed by using the analysis of variance (ANOVA) suitable for experimental design used and shown in Table 6. The ANOVA of the quadratic regression model indicates that the model is significant. The model F-value of 64.67 implied the model to be significant and there is only 0.01% chance that an F-value this large could occur due to noise. The F-value of the independent variables X_{1}, X_{2}, X_{3}, X_{4}, and X_{5} were estimated as 182.94, 177.66, 197.39, 212.39 and 179.41 respectively, showing that the effects of most independent variables on the dependent variable were significantly high. Model F-value was calculated as ratio of Adj. mean square of the regression and Adj. mean square of the residual. The model P-value (Prob. > F) is very low which shows that the model is significant. The P-values were used as a tool to check the significance of each of the model coefficients. The smaller the P-value the more significant is the corresponding coefficient. Values of P < 0.05 indicate the model terms to be significant. The values of P for the coefficients estimated indicate that among the

Table 6. ANOVA for Response surface reduced quadratic model.

tested variables used in the design, X_{1}, X_{2}, X_{3}, X_{4}, X_{5}, X_{4}X_{5},
${X}_{1}^{2}$ ,
${X}_{2}^{2}$ ,
${X}_{3}^{2}$ ,
${X}_{4}^{2}$ ,
${X}_{5}^{2}$ (where X_{1} = leaching temperature, X_{2} = acid concentration, X_{3} = solid/liquid ratio, X_{4} = stirring rate, and X_{5} = leaching time) are significant model terms. The “Lack of Fit F-value” of 1.59 implies that the Lack of Fit is not significant relative to the pure error. There is a 31.32% chance that a “Lack of Fit F-value” this large could occur due to noise. Non-significant lack of fit is good because it indicates that the model is well fitted. Since many insignificant model terms have been eliminated, the improved model can be used to predict effectively, the responses of the percentage recovery of lead from galena. The model equation with the significant coefficient is shown in Equation (4).

$\begin{array}{c}\text{Yield}=\text{83}.\text{52}+\text{3}.\text{44}{X}_{1}+\text{3}.\text{39}{X}_{2}-3.57{X}_{3}+3.71{X}_{4}+3.41{X}_{5}-0.77{X}_{4}{X}_{5}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}-2.23{X}_{1}^{2}-2.25{X}_{2}^{2}-2.07{X}_{3}^{2}-2.26{X}_{4}^{2}-1.96{X}_{5}^{2}\end{array}$ (4)

In terms of the actual factors the model equation (Equation (5)) is as follows:

$\begin{array}{c}\text{Yield}=-\text{1244}.0\text{9}+\text{7}.0\text{5}\ast \text{Leaching temperature}+\text{16}.\text{19}\ast \text{Acid concentration}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}+\text{98}.\text{32}\ast \text{Solid}/\text{Liquid ratio}+0.\text{15}\ast \text{Stirring rate}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}+0.\text{82}\ast \text{Leaching time}-\text{1}.\text{67E}-00\text{4}\ast \text{Stirring rate}\ast \text{Leaching time}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}-\text{9}.\text{92E}-00\text{3}\ast {\text{Leaching temperature}}^{\text{2}}-\text{1}.\text{44}\ast {\text{Acid concentration}}^{\text{2}}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}\u2013\text{2}0\text{7}0\text{4}.\text{55}\ast \text{Solid}/{\text{Liquid ratio}}^{\text{2}}-\text{9}.\text{4}0\text{E}-00\text{5}\ast {\text{Stirring rate}}^{\text{2}}\\ \text{\hspace{0.17em}}\text{\hspace{0.17em}}\u2013\text{2}.\text{18E}-00\text{3}\ast {\text{Leaching time}}^{\text{2}}\end{array}$ (5)

The CV called coefficient of variation which is defined as the ratio of the standard deviation of estimate to the mean value of the observed response is independent of the unit. It is also a measure of reproducibility and repeatability of the models [9] [10] . The results indicated the CV value of 1.65% which illustrated that the model can be considered reasonably reproducible [9] . The signal to noise ratio which is given as the value of the adequate precision is 31.307 as shown in Table 7. This indicates that an adequate relationship of signal to noise ratio exists. The result shows that the model can be used to navigate the design space.

The data were also analyzed to check the correlation between the experimental and predicted dissolution yield (Y%), as shown in Figure 4. The experimental values were the measured response data for the runs designed by the CCD model, while the predicted values were obtained by calculation from the quadratic equation. It can be seen from Figure 4 that the data points on the plot were reasonably distributed near to the straight line (R^{2} = 0.9916), indicating a good relationship between the experimental and predicted values of the response. This

Table 7. Summary of regression values.

Figure 4. Plot of predicted values versus experimental values.

shows that the model chosen is appropriate and that the central composite design (CCD) can be used to perform the optimization operation of the process.

3.4. Combined Effects of Operating Parameters on the Response

The dissolution process for the extraction of lead from galena was analyzed based on the various solutions obtained at possible reaction conditions from the model predictive Equation (2). RSM was considered appropriate owing to its flexibility in navigating the design space. The model equations were solved for the various interaction effects on lead yield considering at any instance the interaction between two factors only, assuming the other variables are set at their mean coded value of zero (0). The combined effects of adjusting the process variables within the design space were monitored using the 3D surface plots and contour plots.

As the leaching temperature is increased from 326 K to 342 K, the percentage recovery of lead increased from 75% to 85% as seen in Figure 5. This linear relationship is as a result of increase in kinetic energy with higher temperature which allows the solvent molecules to more effectively break apart the solute molecules that are held together by intermolecular attractions, hence increasing the diffusion rate from the solid bulk phase into the solvent region. The same trend was observed in Figures 6-8. The results obtained here are in agreement with the results of statistical analyses shown in Table 6 which reveals that the quadratic effect of temperature (X_{1} squared) on the response is significant within the factor range of the experiment with a p-value of <0.0001. This is in line with

Figure 5. 3D and contour plots on the effect of leaching temperature and acid concentration on % yield.

Figure 6. 3D and contour plot of the effect of leaching temperature and solid/liquid ratio on % yield.

Figure 7. 3D and contour plot of the effect of stirring rate and leaching temperature on % yield.

Figure 8. 3D and contour plot of the effect of leaching time and leaching temperature on % yield.

the report of several researchers [11] [12] [13] who agree that increase in temperature substantially increases the dissolution rate of solutes.

As the acid concentration is increased from 1.8 M to 3.18 M, the percentage recovery of lead increased from 75% to 85% as seen in Figure 5. This is attributed to the increase in the diffusion rates of Pb^{2+} from the solid to the solution as the concentration and diffusion of hydronium ion rises. The same trend was observed in Figures 9-11.

A plot for the combined interactive effects of reaction temperature and solid/liquid ratio on the recovery of lead is shown in Figure 6. As the solid/liquid ratio is decreased from 0.039 to 0.028 g/ml, the percentage recovery of lead increased from 75% to 85%. This could be attributed to the decrease in the fluid reactant per unit weight of the solid [11] . The same trend was observed in Figure 9, Figure 12 and Figure 13.

The plot for the combined effects of leaching temperature and stirring rate on the recovery of lead is shown in Figure 7. As the stirring rate is increased from 270.4 rpm to 429.5 rpm, the percentage recovery of lead increased from 75% to 85%. This could be attributed to the decrease in the thickness of the film layer as the stirring rate is increased [11] . The same trend was observed in Figure 10, Figure 12 and Figure 14.

As the leaching time is increased from 65 min to 93.2 min, the percentage recovery of lead increased from 74% to 84% as seen in Figure 8. The same trend was observed in Figure 11, Figure 13 and Figure 14. The results obtained above also indicate that the quadratic effects of acid concentration, solid/liquid ratio, stirring rate and leaching time on response are also very significant within the factor range of the experiment with p-values of <0.0001.

3.5. ANN Modeling

Artificial neural networks (ANNs) are machine-based computational techniques

Figure 9. 3D and contour plot of the effect of solid/liquid ratio and acid concentration on % yield.

Figure 10. 3D and contour plot of the effect of stirring rate and acid concentration on % yield.

Figure 11. 3D and contour plot of the effect of leaching time and acid concentration on % yield.

Figure 12. 3D and contour plot of the effect of stirring rate and solid/liquid ratio on % yield.

Figure 13. 3D and contour plot of the effect of leaching time and solid/liquid ratio on % yield.

Figure 14. 3D and contour plot of the effect of leaching time and stirring rate on % yield.

which attempt to simulate some of the neurological processing abilities of the human brain [14] . They can be considered as a nonlinear regression tool for making a relationship between input and output variables. Multilayer perceptron, radial basis function networks, linear networks, Bayesian networks (generalized regression), and Kohonen networks (probabilistic regression) are the most well-known ANN types.

Multilayer perceptrons (MLP) is perhaps the most popular network architecture in use today [15] . Neurons perform a weighed sum of their inputs and pass it through a transfer function f to produce their output. The MLP model used in this work was developed in MATLAB (The math works Inc. 2007b). For galena dissolution in HCl, the selected MLP model had three layers, where the first had five input units representing the process independent variables (temperature, acid concentration, solid/liquid ratio, stirring rate and leaching time), the second layer had nine hidden units, and the third layer had one output unit representing the percentage yield of lead. The MLP architecture is shown in Figure 15.

3.5.1. Network Training

In order to reduce the deviations of predictions from experimental values, a trial and error technique was employed to determine the adequate number of neurons required in the hidden layer. 70% of experimental results was used to train the network, 20% was used to validate the training while the remaining 10% was used for testing. After the selection of the hidden number of neurons, a number of runs were performed to get the best possible weights in error back propagation and the final selected network architecture was trained for 9 iterations. The mean square error of the trained network is 1.36847e−1 with a regression coefficient of 0.998520. The performance plots of the trained network as well as the regression plots for the training and validation are shown in the Figure 16 and Figure 17 respectively.

Figure 15. ANN architecture for galena dissolution showing 5 input units, 9 hidden units and 1 output unit.

Figure 16. Performance plot for galena dissolution in HCl ANN model.

Figure 17. Regression plots for the training (a) and validation (b) for galena dissolution in HCl ANN model using 5 input variables, 9 processing elements in the hidden layer and 1 output variable.

3.5.2. Comparison of RSM and ANN

A comparison between Artificial Neural Network (ANN) and Response Surface Methodology was carried out using the Absolute average deviation (AAD) and Coefficient of determination observed for both models. The AAD observed for both models gives an indication of how accurate the model predictions can be [16] .

$\text{AAD}\left(\%\right)=\left(\frac{1}{n}{\displaystyle \underset{i=1}{\overset{n}{\sum}}\left\{\frac{{R}_{\text{artpred}}-{R}_{\text{artexp}}}{{R}_{\text{artexp}}}\right\}}\right)\times 100$ (6)

where n is the number of sample points, ${R}_{\text{artpred}}$ is the predicted value of lead dissolution and ${R}_{\text{artexp}}$ is the experimentally determined value for lead dissolution [16] .

The linear fit model (Y =((1.0) * T + (0.22)) generated by the trained outputs vs target plots shown in Figure 17 was used to predict the ANN model values. Where Y = the ANN model value, T (Target) = the experimental value used to generate the corresponding ANN value. The graph of the correlation between the experimental values and the predictions by RSM and ANN is shown in Figure 18.

From the AAD estimation, RSM gave an AAD of 0.750% and ANN model gave an AAD of 0.295%. From the graph in Figure 18, the coefficient of determination for the RSM model is 0.991, while that of ANN is 1.0. These values are a measure of how close the predicted value of the response is to the actual experimental values. The closer each of these values is to 1, the better the prediction. Since the value of COD for both RSM and ANN are approximately equal to 1, it is evident that both models could efficiently predict the recovery of lead from galena [13] . RSM was then adopted for the optimization studies.

3.6. Process Optimization Using CCD

The optimization exercise for the dissolution process was conducted separately using the flexibility of the design expert tool function. Equation (4) was solved for the best solutions such that the responses (Y_{n}) are maximized within the design space. No unique solutions were possible. A usual approach, which involves selecting the best solution based on economic considerations, was adopted and

Figure 18. Plot for RSM and ANN model appraisal.

the chosen optimal solutions are presented in Table 8. The selection of desired optimum solution of Table 8 was mainly influenced by the cost of reagents and energy. By using the numerical optimization technique which is a feature of CCD in the design expert software, a combination of factors that concurrently satisfy the requirements placed on each of the responses and factors could be determined by the software [13] . In choosing the goal for each of the factors for the numerical optimisation, a number of considerations were made. The significance of each of the factors on the final response was the most important consideration. The response was set at maximum goal, all other factors were kept in range apart from the reaction time which was set to a minimum goal target. Based on these, the software predicted optimum reaction conditions with a desirability of 1.00 tabulated in Table 8.

In order to confirm the accuracy of this model, an experimental run was conducted under these optimal conditions. The experimentally obtained value for the% yield of lead was 84.54% and this was in reasonable agreement with that of CCD model of design expert (85.25%) as shown in Table 9. A non-dominated optimal response of 85.25% yield of lead at 343.96 K leaching temperature, 3.11 M hydrochloric acid concentration, 0.021 g/ml solid/liquid ratio, 362.27 rpm stirring speed and 87.37 min leaching time was established as a viable route for reduced material and operating cost using RSM.

4. Conclusion

The optimum conditions for the extraction of lead from galena were investigated in this work. Response surface methodology (RSM) and Artificial neural network (ANN) were used for the modeling and optimization of process parameters. The performances of the models were estimated on the basis of correlation coefficients, absolute average deviation (AAD) and mean square error (MSE). The experimental data for the central composite design (CCD) of RSM were fitted using the second-order polynomial equation. The best multilayer perceptron (MLP) model of ANN had nine neurons and a logistic sigmoid activation function in the hidden layer. CCD and ANN regression coefficients were obtained to be 0.991 and 1.00 respectively showing good agreement with the experimental

Table 8. CCD optimum predicted condition.

Table 9. Results of validation experiments.

data. The absolute average deviation (AAD) for RSM and ANN was obtained as 0.750% and 0.295% respectively. Both methodologies proved to be quick and useful tools for the optimization of lead recovery from galena. The higher value of the correlation coefficient and lower values of AAD and MSE for the MLP model indicate that the MLP of ANN provides better prediction of experimental data than the CCD model.

Cite this paper

*Journal of Minerals and Materials Characterization and Engineering*,

**6**, 294-315. doi: 10.4236/jmmce.2018.63021.

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