Abstract
The microalgal strain Chlorella sorokiniana isolated from a waste stabilization pond was used for tertiary treatment of municipal wastewater. Three light:dark (L:D) regimes of 12:12, 16:8, and 24:0 were used for treating wastewater in microalga (A), microalga + sludge (A + S), and sludge (S) reactors. The removal of nutrients (N and P) was found to be the highest in the microalga-based reactor, with more than 80% removal of biochemical oxygen demand (BOD) and 1.2–5.6 log unit removal of pathogens. The addition of sludge improved chemical oxygen demand (COD) removal. Nitrifiers were found to be predominant in the A + S reactor. Algal biomass productivity was more than 280 mg/L/d in all the L:D regimes. The increase in light regime improved nutrient removal and biomass productivity in the algal reactor. Results of the kinetic study showed that (i) nitrifiers had more affinity for ammonium than microalga, and hence, most of the ammonia was oxidized to nitrate, (ii) microalga assimilated nitrate as the primary nitrogen source in the A + S reactor, and (iii) solubilization of particulate organic nitrogen originated from dead cells reduced the nitrogen removal efficiency. However, in the microalga-based reactor, the ammonium uptake was higher than nitrate uptake. Among pathogens, the removal of Salmonella and Shigella was better in the A + S reactor than in the other two reactors (microalga and sludge reactor). Additionally, the heterotrophic plate count was drastically reduced in the presence of microalga. No such drastic reduction was observed in the stand-alone sludge reactor. Kinetic modeling revealed that microalga–pathogen competition and pH-induced die-off were the two predominant factors for pathogen inactivation.
Highlights
Introduction iationsIn conventional wastewater treatment, tertiary treatment is being used to remove nutrients such as nitrogen and phosphorous, which remain in wastewater after secondary treatment or the activated sludge process
The microalgal strain grew in a modified BG-11 medium that was maintained at 25 ± 2 ◦ C and at pH = 7 for six days to achieve the required algal inoculum dose (700 Mb represent the algal and bacterial biomass (mg/L) as total suspended solids (TSS))
This study was designed to understand the effects of light duration and sludge and microalga inoculum doses on the treatment efficiency, biomass production, and pathogen removal
Summary
Tertiary treatment is being used to remove nutrients such as nitrogen and phosphorous, which remain in wastewater after secondary treatment or the activated sludge process. Nitrification and denitrification cycles are used for nutrients removal; these processes are ineffective for achieving the nutrient level established by EU legislation. In addition to biological tertiary treatments, chemical-based methods such as precipitation (aluminum and iron salts) and coagulation are being employed; all these processes increase the treatment cost [1,2]. Conventional biological processes cannot reduce pathogen concentration to the desired values. Chlorination and UV treatment are used for reducing pathogen content in treated wastewater [3]. The presence of pathogenic strains is determined by the total coliform and fecal coliform counts.
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