4.3 Article

Parametric optimization of hexavalent chromium removal by electrocoagulation technology with vertical rotating cylindrical aluminum electrodes using Taguchi and ANN model

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SPRINGER
DOI: 10.1007/s40201-023-00859-w

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Hexavalent chromium; Electrocoagulation; ANN; Taguchi method; Vertical rotating electrodes

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This study evaluates the performance of rotating aluminum electrodes in removing hexavalent chromium (Cr6+) from synthetic tannery wastewater using an electrocoagulation reactor. Taguchi and Artificial Neural Network (ANN) models were developed to optimize the conditions for maximum Cr6+ removal. The BR-ANN model provided better results compared to the Taguchi model, achieving higher Cr6+ removal efficiency, reduced energy demand, and improved accuracy. The SEM and XRF analysis confirmed the adsorption and precipitation of Cr6+ with metal hydroxide sludge.
This study aims to evaluate the performance of rotating aluminum electrodes in the electrocoagulation reactor for removing hexavalent chromium (Cr6+) from synthetic tannery wastewater. Taguchi and Artificial Neural Network (ANN) based models were developed to obtain the optimum condition for maximum Cr6+ removal. The optimum working condition obtained by Taguchi approach for the maximum Cr6+ removal (94%) was: Initial Cr6+ concentration (Cr-i(6+)) = 15 mg/L; Current Density (CD) = 14.25 mA/cm(2); Intial pH = 5; Rotational Speed of Electrode (RSE) = 70 rpm. In contrast, the optimal condition for maximum Cr6+ ions removal (98.83%) obtained from the BR-ANN model was: Cr-i(6+) = 15 mg/L; CD = 14.36 mA/cm(2); pHi = 5.2; RSE = 73 rpm. Compared to the Taguchi model, the BR-ANN model outperformed in terms of providing higher Cr6+ removal (+ 4.83%); reduced energy demand (-0.035 KWh/gm Cr6+ remove); lower error function value (chi(2) = -7.9674 and RMSE = -3.5414); and highest R-2 value (0.9991). The data for the conditions 91,007 < Re < 227,517 and Sc = 102.834 were found to fit the equation for the initial Cr6+ concentration of 15 mg/l; Sh = 3.143Re(0.125) Sc-0.33. The Cr6+ removal kinetics was best described by Pseudo 2(nd) Order model, as validated by high R-2 and lower error functions value. The SEM and XRF analysis confirmed that Cr6+ was adsorbed and precipitated along with metal hydroxide sludge. The rotating electrode led to lower SEEC (10.25 kWh/m(3)), as well as maximum Cr6+ removal (98.83%), compared to EC process with stationary electrodes.

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