4.7 Article

Oily wastewater treatment by a continuous flow electrocoagulation reactor with polarity switch: Assessment of the relation between process variables and the aluminum released to the environment

Journal

JOURNAL OF ENVIRONMENTAL MANAGEMENT
Volume 347, Issue -, Pages -

Publisher

ACADEMIC PRESS LTD- ELSEVIER SCIENCE LTD
DOI: 10.1016/j.jenvman.2023.119072

Keywords

Electroflotation; Oil in water; Dissolved aluminum; Power consumption; Electrode degradation

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Electrocoagulation with electrical polarity inversion was used to treat oil in water emulsions. The effects of time factors on the treatment process were investigated, and a correlation was found between electrode degradation, oil removal, and electric power consumption. Surface response analysis indicated that increasing the number of inversion cycles reduces electrode degradation. The treatment significantly reduced the chemical oxygen demand of the effluent. There is an inverse statistical correlation between aluminum in the treated effluent and oil removal, indicating the possibility of achieving higher oil removal with less environmental impact.
Electrocoagulation with electrical polarity inversion was used to treat oil in water emulsions (145 +/- 5 mg dm-3) using a cylindrical 4.8 dm3 reactor in continuous mode. The effects of spatial time and time between polarity inversion were explored using a three-level full factorial design (32), followed by Spearman correlation (ps), which has shown that the aluminum concentration in the treated effluent is not directly dependent on the mass of aluminum released by the electrodes. Nonetheless, the loss of mass of the electrodes is correlated (ps = 0.6970) to oil removal and to less electric power consumption (ps =-0.6909). Surface response analysis revealed that increasing the number of inversion cycles reduces electrode degradation. The treatment reduced the effluent's chemical oxygen demand by over 92.8%. Regarding environmental impact, there is an inverse statistical correlation between aluminum in the treated effluent and oil removal (ps =-0.7426), indicating that removing more oil with less environmental impact is possible. The better condition, considering oil removal and lower electrode consumption, was obtained with a spatial time of 36 min and a polarity inversion time of 10 s; for this condition, oil removal reached 87.0% with an energy expenditure of about 7.21 kW h.m- 3.

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