Seasonal variation in light utilisation, biomass production and nutrient removal by wastewater microalgae in a full-scale high-rate algal pond

2013 ◽  
Vol 26 (3) ◽  
pp. 1317-1329 ◽  
Author(s):  
Donna L. Sutherland ◽  
Clive Howard-Williams ◽  
Matthew H. Turnbull ◽  
Paul A. Broady ◽  
Rupert J. Craggs
Water ◽  
2016 ◽  
Vol 8 (12) ◽  
pp. 551 ◽  
Author(s):  
Jun Zhai ◽  
Jun Xiao ◽  
Md. Rahaman ◽  
Yasinta John ◽  
Jingsong Xiao

2012 ◽  
Vol 112 ◽  
pp. 98-104 ◽  
Author(s):  
Rodrigo A. Mohedano ◽  
Rejane H.R. Costa ◽  
Flávia A. Tavares ◽  
Paulo Belli Filho

2017 ◽  
Vol 136 ◽  
pp. 225-232 ◽  
Author(s):  
M.C. Mesquita ◽  
A. Albuquerque ◽  
L. Amaral ◽  
R. Nogueira

1999 ◽  
Vol 39 (6) ◽  
pp. 113-118 ◽  
Author(s):  
Gerald M. Stevens ◽  
James L. Barnard ◽  
Barry Rabinowitz

During the initial years of the development of Biological Nutrient Removal (BNR) technology, it was assumed that the bacterial species responsible of the removal of phosphorus (BioP organisms) could not use nitrates as a final electron acceptor and could thus not denitrify. The carbon taken up in the form of Volatile Fatty Acids (VFA) in the anaerobic zone was thus deemed to be unavailable for denitrification in the anoxic zone. This was reinforced through experiments in which BioP organisms cultured in the high-rate Phoredox system in which no nitrification took place, did not denitrify when nitrates were added. Many researchers (e.g. Dold and Barker) have since shown that in BNR systems such as the 3-Stage Bardempho system, where nitrates are recycled to the anoxic zone which follows the anaerobic zone, a high degree of phosphorus uptake through denitrification does occur. In addition, the partial diversion of primary effluent directly to the anoxic zone has significantly improved phosphorus uptake under anoxic conditions. Full-scale operations at the Westbank, British Columbia, plant showed a substantial uptake of phosphorus in the anoxic zone in the absence of oxygen. The Westbank configuration includes side stream primary sludge fermentation, VFA rich fermenter supernatant addition directly to the anaerobic zone and diversion of a portion of primary effluent to the anoxic zone. This configuration stimulates P-uptake under anoxic conditions, demonstrates the efficient use of carbon and is instrumental in achieving an annual average effluent Total-P concentration of less than 0.17 mg/l. The phenomenon of denitrification by BioP organisms was included in the Biowin Model developed by Dold (Biowin Manual). This paper describes experiments and full-scale plant observations to establish the role of BioP organisms in the removal of nitrates in the anoxic zone of a plant which also receives a portion of the primary effluent and verification of the Biowin model.


2020 ◽  
Vol 82 (6) ◽  
pp. 1176-1183 ◽  
Author(s):  
Mayara L. Serejo ◽  
Sarah L. Farias ◽  
Graziele Ruas ◽  
Paula L. Paulo ◽  
Marc A. Boncz

Abstract The influence of the feeding regime on surfactant and nutrient removal and biomass production was evaluated in three high rate algal ponds for primary domestic wastewater treatment. Feeding times of 24, 12 and 0.1 h d−1 were studied in each reactor at a similar hydraulic retention time of 7.0 days and organic load of 2.3 mg m−2 d−1. Semi-continuous feeding at 12 and 0.1 h d−1 showed better microalgal biomass production (0.21–0.23 g L−1) and nutrient removal, including nitrogen (74–76%) and phosphorus (80–86%), when compared to biomass production (0.13 g L−1) and nitrogen (69%) and phosphorus (46%) removals obtained at continuous feeding (24 h d−1). Additionally, the removal efficiency of surfactant in the three reactors ranged between 90 and 97%, where the best result was obtained at 0.1 h d−1, resulting in surfactant concentrations in the treated effluent (0.3 mg L−1) below the maximum freshwater discharge limits.


1990 ◽  
Vol 22 (7-8) ◽  
pp. 35-43
Author(s):  
K. D. Tracy ◽  
S. N. Hong

The anaerobic selector of the A/0™ process offers many advantages over conventional activated sludge processes with respect to process performance and operational stability. This high-rate, single-sludge process has been successfully demonstrated in full-scale operations for biological phosphorus removal and total nitrogen control in addition to BOD and TSS removal. This process can be easily utilized in upgrading existing treatment plants to meet stringent discharge limitations and to provide capacity expansion. Upgrades of two full-scale installations are described and performance data from the two facilities are presented.


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