Traitement des eaux résiduaires d’industrie de textile par électrocoagulation en réacteur continu
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Abstract
Electrocoagulation (EC) is an effective treatment for highly polluted industrial wastewater. It has
been used successfully for the treatment of various industrial effluents including effluents issues
from food industries, tanneries wastewater, water containing metals or heavy metals, wastewater
contained soluble oil issued from mechanical workshop, polymerization manufactures, and
textiles industries.
The main objective of this study was to investigate the effects of the operating parameters, such
as initial pH, initial concentration (C0), residence time (τ), current density (j), inlet flow rate (Q),
direct/ alternating current (DC/AC) and electrode connection systems on the removal of a red
nylosan dye (Acid Red 336) by EC process using aluminum electrode in a continuous
electrochemical reactor. The optimized parameters will be applied to the treatment of a real
textile effluent.
Our results suggest an opportunity for the application of continuous EC process to remove color
and turbidity from wastewater. For example, A rate of abatement between 87 % and 96 % for
color and turbidity was observed for the direct current, when the initial concentration of the dye
C0 was ranged from 100 mg/L to 1000 mg/L, current density j = 300 A/m², conductivity κ = 2.5
mS/cm, inlet flow rate Q = 15 L/h and 26 L/h, treatment time t = 30 min and initial pH ranged
from 3.46 to 9. The specific electrical energy consumption was 9.5 kWh per kilogramme of
removed dye for direct current and monopolar connection.
The recirculation of the wastewater increased considerably the elimination of the color and the turbidity
for the two modes of connection (MP and BP), but for (MP-P) connection, the effect was not significant.
For the influence of electrodes connection modes, the results showed that bipolar connection is
slightly more effective compared to monopolar connection (MP) in terms of abatement of the
color and turbidity. But in terms of consumption of energy, the bipolar mode (BP) consumes
more energy than the monopolar mode (20 kWh per kilogramme of removed dye)
