A nitrifying biofilm airlift suspension reactor (with nitrifiers growing in biofilms) was coupled with a denitrifying chemostat (with denitrifiers growing in suspension) for integrated nitrogen removal. Initially the process was run in post-denitrification setup, during which nitrification and denitrification went via nitrate. Later recirculation between both reactors was applied (pre-denitrification setup), resulting in circulation of the suspended denitrifiers between the two reactors. The setup was suitable for nitrification and denitrification: 75% total nitrogen removal efficiency was obtained at an aerobic ammonia load of 5 kg(N) m(-3) d(-1). In the pre-denitrification setup nitrification and denitrification mainly occurred with nitrite as an intermediate. Probably the nitrite oxidisers and reducers competed for nitrite, which competition was won by the nitrite reducers. A low average COD/N-ratio of 3.0 g(COD) g(N)(-1) was obtained, in accordance with the "nitrite route". (C) 1998 Elsevier Science Ltd. All rights reserved.
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UNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAINUNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAIN
vanBenthum, WAJ
GarridoFernandez, JM
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UNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAINUNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAIN
GarridoFernandez, JM
Tijhuis, L
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UNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAINUNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAIN
Tijhuis, L
vanLoosdrecht, MCM
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UNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAINUNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAIN
vanLoosdrecht, MCM
Heijnen, JJ
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UNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAINUNIV SANTIAGO DE COMPOSTELA, DEPT CHEM ENGN, SANTIAGO DE COMPOSTELA 15706, SPAIN