Research Article

A Comparison of Central Composite Design and Taguchi Method for Optimizing Fenton Process

Table 2

Experimental design matrix, experimental runs, and predicted values on COD removal and decolorization efficiency.

Independent variables ()Dependent variables (; (%))
Actual valuesPredicted values
RunDye (mg/L)H2O2 : Fe+2 (wt/wt)Dye : Fe+2 (wt/wt)pHCOD (%)Decolorization (%)COD (%)Decolorization (%)

120015305.575.395.473.295.1
220015305.576.495.473.295.1
33002550962.896.860.995.7
420025305.573.498.169.897.5
5300550934.880.035.179.8
620015305.573.495.573.295.1
7100510966.555.863.459.7
81002550287.799.285.3100.0
92001530965.878.967.380.3
1030015305.578.394.580.298.6
1110015305.577.190.173.986.7
12100510267.093.466.192.2
13100550930.256.132.954.4
1420015305.574.595.473.295.1
15300510977.989.179.485.9
162005305.560.884.363.385.6
171002510948.067.950.5165.1
1820015305.570.394.673.2095.1
193002510267.498.963.698.3
20300510261.495.262.595.6
211002510250.397.653.199.9
2220015105.567.798.267.797.7
233002510980.484.480.586.3
243002550275.599.481.897.7
252001530274.198.379.197.5
261002550944.773.644.975.4
2720015505.562.793.561.694.7
2820015305.573.496.673.295.1
29100550272.176.573.476.7
30300550261.278.955.979.4