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2007 Speakers

A CASE STUDY: HUNTSVILLE, AL MANAGING SYSTEM EXPANSION, MAINTENANCE & REHABILITATION
Christian Dunaway, P.E. & Shane Davis, P.E.

MODELING IFAS AND MBBR PROCESSES USING LINPOR MEDIA Al Warakomski The WERF report on The Investigation of Hybrid Systems for Enhanced Nutrient Control (Project96-CTS-4) kicked off interest in IFAS (Integrated Fixed Film Activated Sludge) and MBBR (Moving BedBiological Reactors) systems in North America. The LinPor™ process was developed in Europe by Linde AG. It operates in either the IFAS or MBBR mode using a suspended media of highly porous polymer foam cubes that serve as a mobile carrier material for accumulation of microorganisms. This porous media allows the biological reactor to operate at 2 to 3 times greater total biomass concentration than a conventional air activated sludge process. In addition, because most of the biomass is retained in the media, the mass loading imposed on the secondary clarifier is minimized. The LinPor™ system can be configured according to the level of treatment required (carbonaceous, ammonia conversion, or total nitrogen reduction, with phosphorus reduction if necessary) and the process is ideally suited for the upgrade of existing plug flow diffused air systems to increase capacity, or to achieve higher levels of treatment, while minimizing modifications to existing facilities.

This presentation will address the development and evolution of the LinPor™ process from initial process design concepts, beginning pilot plant studies, and operation and performance results from installed full scale facilities. All the various process configurations for nitrogen control will be described and depicted, including those with biological phosphorus removal. A complete development of the methodology of the Linde's empirical process design will be illustrated. The BioWin® process simulation software can be adapted to model LinPor™ using this empirical process design basis. Data for the first North American LinPor™ plant at Westerly, RI, USA, where nitrafication and simultaneous denitrafication occur in the oxic reactor stage and denitrafication occurs in the anoxic stage will be presented along with data for several European plants. A complete list of world wide LinPor —CN and —N™ installations is included.