Sidestream EBPR (S2EBPR) is an emerging alternative process to address common challenges in EBPR related to weak wastewater influent and may improve EBPR process stability. A systematic evaluation and comparison of the process performance and microbial community structure was conducted between conventional and S2EBPR facilities in North America. The statistical analysis suggested higher performance stability in S2EBPR than conventional EBPR, although possible bias associated with other plant‐specific factors might have affected the comparison. Variations in stoichiometric values related to EBPR activity and discrepancies between the observed values and current model predictions suggested a varying degree of metabolic versatility of PAOs in S2EBPR systems that warrant further investigation. Microbial community analysis using various techniques suggested comparable known candidate PAO relative abundances in S2EBPR and conventional EBPR systems, whereas the relative abundance of known candidate GAOs seemed to be consistently lower in S2EBPR facilities than conventional EBPR facilities. 16S rRNA gene sequencing analysis revealed differences in the community phylogenetic fingerprints between S2EBPR and conventional facilities and indicated statistically higher microbial diversity index values in S2EBPR facilities than those in conventional EBPRs. Practitioner Points Sidestream EBPR (S2EBPR) can be implemented with varying and flexible configurations, and they offer advantages over conventional configurations for addressing the common challenges in EBPR related to weak wastewater influent and may improve EBPR process stability. Survey of S2EBPR plants in North America suggested statistically more stable phosphorus removal performance in S2EBPR plants than conventional EBPRs, although possible bias might affect the comparison due to other plant‐specific factors. The EBPR kinetics and stoichiometry of the S2EBPR facilities seemed to vary and are associated with metabolic versatility of PAOs in S2EBPR systems that warrant further investigation. The abundance of known candidate PAOs in S2EBPR plants was similar to those in conventional EBPRs, and the abundance of known candidate GAOs was generally lower in S2EBPR than conventional EBPR facilities. Further finer‐resolution analysis of PAOs and GAOs, as well as identification of other unknown PAOs and GAOs, is needed. Microbial diversity is higher in S2EBPR facilities compared with conventional ones, implying that S2EBPR microbial communities could show better resilience to perturbations due to potential functional redundancy.

The first full-scale Bardenpho plant in the colder regions of North America was constructed in Kelowna and operated for about two years. The design was based on criteria developed by Barnard (1974) and based on experience of the design of similar plants in South Africa. Maximum flexibility leaving the operator many options for optimization was allowed. Effluent ortho-phosphate, nitrate and ammonia concentration averaged 0.43, 2.05 and 0.78 mg/ℓ respectively over the first year of operation. Operating results are compared with design predictions. Some results are presented and the design was tested using theories developed by Ekama et al (1984) whose models predicted that no phosphate removal would be possible. RESUME La premierè installation de Bardenpho, à grande échelle dans les régions les plus froides de l'Amérique du Nord a été construite à Kelowna et utilisée pendant plus de deux ans. Le dessin était fondé sur les information de Barnard (1974) et basé sur l'expérience du dessin d'installation sembables en Afrique du Sud. L'installation était flexible et laissait à l'opérateur le choix de plusieurs options pour l'optimisation. La concentration de ortho-phosphate, nitrate et ammoniaque avait les valeurs moyennes de 0,43; 2,05 et 0,78 mg/ℓ respectivement pendant la premiére année de travail. Les resultats sont presentés et la dessin a été mis à l'épreuve en utilisant les théories développées par Ekama et al (1984) dont les modèles ont predit. qu' aucun élimination de phosphate serait possible vu le petit réduction de nitrate qui le modèle ont prédit aux températures plus froides.

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A new wastewater treatment plant that utilizes the “Modified Bardenpho” process for nutrient removal has recently been commissioned in Kelowna, B.C. The 260 L/s facility (130 L/s in each of two parallel modules) has been operating at full design flow through one module for over 6 months.Two months of operating time was required to establish the nitrification–denitrification capabilities and to build up the phosphorus release–uptake mechanism in the biomass. Subsequent to that start-up period, the process has been capable of producing an effluent containing less than 5 mg/L total nitrogen and less than 0.3 mg/L orthophosphate when the influent sewage has contained some 30 mg/L of nitrogen and 6 mg/L of phosphorus. Key words: phosphorus removal, nitrogen removal, biological waste treatment, advanced waste treatment.