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JOURNAL OFAPPLIFD AQUACULTURE <br />INTRODUCTION <br />The carrying capacity of aquaculture systems employing water <br />reuse is limited by the accumutation of ammonia, the principal ni- <br />trogenous excretory waste of cultured fish and invertebrates. Am- <br />monia exists in a pH- and temperature-governed equilibrium be- <br />tween atoxic un-ionized form (NNE) and a relatively innocuous <br />ionized form (NH4 } (Piper et al. 1983). <br />Ion exchange can be used to remove ammonia from freshwater <br />fish culture systems, but biofiltration is more commonly employed <br />for this purpose (Wheaton 1977; Spotte 1979). Biofittration is the <br />conversion of ammonia to relatively innocuous nitrate by a filter <br />that contains nitrifying bacteria that are attached to supporting me- <br />dia such as gravel, plastic rings, oyster shells, or other materials <br />with a large surface area. Nitrification is accomplished primarily by <br />two genera of aerobic, chemosynthetic bacteria: Nitrosomonas spp., <br />which oxidizes ammonia to nitrite, and Nitrobacter spp., which oxi- <br />dizes nitrite to nitrate. Other organisms also occur in the biofilter <br />bed, including heterotrophic bacteria that oxidize carbonaceous or- <br />ganic wastes (Spotte 1979). <br />There are numerous biofilter designs, including submerged (up- <br />flow, downflow, and horizontal), trickling, and rotating disk or <br />drum (Wheaton 1977; Kaiser and Wheaton 1983; Miller and Libey <br />1985; Palter and Lewis 1988). Submerged biofilters have the ad- <br />vantage of being mechanically simple and compatible with a wide <br />range of flow rates and media types. Recently, submerged biofilters <br />have been operated with fluidized filter beds, resulting in large in- <br />creases in carrying capacity and efficiency over conventional biofil- <br />ter designs (Palter and Lewis 1988; Jewell and Cummings 1989). <br />Previous research has demonstrated that the fixed biofilm (i.e., <br />biofilm attached to a substrate) nitrification process conforms to the <br />half-order/zero-order kinetic model introduced by Haremoes (1978). <br />Half-order kinetics (ammonia removal dependent upon, ammonia <br />concentration) occur at relatively low ammonia concentrations be- <br />cause of incomplete ammonia penetration through the biofilm. Zero- <br />order kinetics (ammonia removal independent of ammonia concen- <br />tration) occur at relatively high ammonia concentrations as a result <br />of insufficient oxygen diffusion through the biofilm or other limita- <br />