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Costs of Advanced Treatment in Water Reclamation
Authors:Megan H Plumlee  Benjamin D Stanford  D Cory Hopkins  Shane A Snyder
Affiliation:1. Kennedy/Jenks Consultants, San Francisco, California 94107, USA;2. Hazen and Sawyer, Raleigh, North Carolina 27607, USA;3. Department of Chemical and Environmental Engineering, University of Arizona, Tucson, Arizona 85721, USA
Abstract:The additional removal of trace organic contaminants (TOrCs) provided by advanced water and wastewater treatment inevitably requires additional financial costs, which must be estimated to support utility planning and compare alternatives. This study presents conceptual-level (Class 4) capital and annual operations and maintenance (O&M) cost curve equations to aid evaluations of advanced treatment trains for water reuse. The cost curve equations are broadly applicable to the water reuse community, particularly those interested in ozone-based treatment trains. Unit processes include microfiltration or ultrafiltration membranes (MF/UF), nanofiltration or reverse osmosis membranes (NF/RO), ozone (with or without hydrogen peroxide, H2O2), ultraviolet (UV) treatment with H2O2 (UV/H2O2), and biological activated carbon (BAC); all cost curves are for a unit process and can be added together to obtain costs for a combined treatment train. The cost curves indicate that at all plant capacities (1 to 500 MGD), membrane treatment (e.g., MF or RO) represents the highest cost unit process, ozone the least, and BAC or UV/H2O2 fall in between. Additionally, the relationship between ozone dose and TOrC removal is discussed with a demonstration of how costs change with increasing ozone dose to achieve desired TOrC destruction.
Keywords:Ozone  Advanced Treatment Costs  Membranes  Trace Organic Contaminants  Water Reuse
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