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  Paper Details                 Browse papers by sector
BNR Then vs. Now
Author            :Stantec
Designation    :Stantec
Company        :Stantec
 Biography  Synopsis   Download Paper

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Synopsis

An advanced wastewater treatment plant was commissioned in 1992 for the City of Kalispell, which is located in northwest Montana and discharging to a sensitive Rocky Mountain watershed. The plant featured a Biological Nutrient Removal (BNR) process and primary sludge fermentation to ensure complete Biological Phosphorus (Bio-P) removal. This plant was state-of-the-art BNR at the time and has performed exceptionally well since it’s commissioning having been awarded many federal, state, and local awards for its excellent effluent quality. Recent rapid growth within the community, however, has caused plant loading to near original design loading limits and consequently initiated a review of the facility. Stantec, the original designers of the BNR processes, was retained once again to review the process with two objectives in mind: 1) to determine the reserve capacity of the existing BNR process (i.e. bioreactors, secondary clarifiers, and primary sludge fermenter); and 2) toprovide a longer-term expansion / upgrade plan for the facility in order to provide treatment through to the year 2025.

BioWinTM modeling was conducted on the existing Modified University Cape Town (UCT) BNR process in order to determine any reserve capacity. Observations regarding favorable nitrifier growth rate, high bioreactor Hydraulic Residence Time, and good sludge settleability and control, were considered in the analysis and suggest the existing facility may treat an additional 35% BOD load in comparison to the original design loading. With just a fine-bubble retrofit, modeling suggests the existing process can extend treatment through to 2006-2007.

Beyond 2007, plant expansion is required. Stantec is recommending certain BNR upgrades be implemented in order to simplify the BNR process and reflect advances in the state of BNR technology from “then” to “now”. The primary changes recommended include converting the bioreactor configuration from a Modified UCT process to a Modified Johannesburg process, and converting from two-stage primary sludge fermentation to single-stage primary sludge fermentation.


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