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Kinetics of glyphosate degradation in glyphosate wastewater over nitrogen-doped activated carbon catalyst in an upflow fixed bed reactor
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文摘
Catalytic wet oxidation (CWO) of glyphosate (PMG) wastewater over a nitrogen-doped activated carbon catalyst was performed in an upflow fixed bed reactor at mild temperature (35–125 °C) and oxygen partial pressure (0.05–0.25 MPa). The catalytic performance was characterized by PMG and organic phosphorus (OP) conversion. All CWO experiments were under kinetic control by choosing suitable average particle size (0.3 mm, 40–80 mesh) and gas flow rate (500 mL min−1). A power law kinetic model was developed to describe PMG and OP conversion, assuming first order kinetics with respect to PMG and OP. This model and its calculated parameters successfully predicted PMG and OP conversion. The obviously different rate constant and activation energy for PMG and OP conversion suggested that removal of the intermediate of aminomethylphosphonic acid is the control reaction for OP conversion. Finally, the competitive oxidation of formaldehyde was insignificant and this model also proved a satisfactory description for treatment of the real PMG wastewaters. OP conversion for the different PMG wastewaters can reach over 90% at mild conditions (125 °C, 0.2 MPa of oxygen partial pressure, 25 min of liquid space time).

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