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Optimization of electrochemical process for removing sulphate from drinking water by taguchi model

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Figure

Fig. 1. The batch electrochemical reactor
Fig. 2 showed the effects of anode and cathode electrode materials on the sulfate removal at the experimental conditions given in Table 2
Fig. 5. The anode weight lost in the electrochemical reactor as a function of current densities
Fig. 8 showedthe plots of the kinetics first, and second order reaction models fitted with the sulfateremoval experimental data in batch electrochemicalreactor at the experiments conditions given in Table 2

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