Ammonia recovery from acidogenic fermentation effluents using a gas-permeable membrane contactor.

A gas-permeable membrane (GPM) contactor was used to recover ammoniacal nitrogen from a synthetic and a biowaste fermentation broth under different pH (from 6 to 11) and temperatures (35 and 55 °C). Ammonia mass transfer constant (K) increased as pH and temperature increased. For synthetic broth, pH 10 provided the best results, when considering the K (9.2·10 m·s) and the reagents consumption (1.0 mol NaOH·mol TAN and 0.6 mol HSO·mol TAN). Biowaste fermentation generated a broth with a high concentration of ammoniacal nitrogen (4.9 g N·L) and volatile fatty acids (VFA) (41.1 g COD·L). Experiments using the biowaste broth showed a lower K (5.0·10 m·s at pH 10) than the synthetic broth, related to the solution matrix and other species interference. VFAs were not detected in the trapping solution. Overall, these results show that GPM is a suitable technology to efficiently separate ammoniacal nitrogen and VFA from fermentation broths.