Biodegradation of mixture of phenol and formaldehyde in wastewater using a single-basin MSCR process.
A novel moving-bed sequential continuous-inflow reactor (MSCR) was developed and investigated for the degradation of high concentrations of phenol and formaldehyde. Results indicated the MSCR could simultaneously remove greater than 99% of the target compounds for concentrations up to 1300 mgL⁻¹ each (corresponding to the loading rate of 1.04 kgm⁻³d⁻¹), and around 96% of the chemical oxygen demand of ∼4800 mgL⁻¹ with a 6-h cycle time. An increase of the inlet concentrations to 1500 mgL⁻¹ (loading rates of 1.2 kgm⁻³d⁻¹), however, caused a slight reduction in the removal efficiency. The MSCR handled hydraulic shock loads of up to three times the normal flow rate without adversely affecting the elimination performance of the contaminants. These unique features, combined with the efficient and compact nature of the process, thus recommend MSCR as a promising technique for the removal of mixture of toxic compounds in a single-basin bioreactor.
Moussavi
Gholamreza
G
Department of Environmental Health, Faculty of Medical Sciences, Tarbiat Modares University, Tehran, Iran. Moussavi@modares.ac.ir
Heidarizad
Mahdi
M
D001673:Biodegradation, Environmental; D018533:Biomass; D019149:Bioreactors; D005557:Formaldehyde / Q000032:analysis / Q000378:metabolism*; D007220:Industrial Waste; D010100:Oxygen / Q000378:metabolism; D019800:Phenol / Q000032:analysis / Q000378:metabolism*; D013997:Time Factors; D014865:Waste Disposal, Fluid / Q000379:methods*; D014874:Water Pollutants, Chemical / Q000032:analysis / Q000378:metabolism
D007220:Industrial Waste; D014874:Water Pollutants, Chemical; D005557:Formaldehyde; D019800:Phenol; D010100:Oxygen