Kurt M, Dunn I J, Bourne J R
Chemical Engineering Department, ETH, CH-8092 Zurich, Switzerland.
Biotechnol Bioeng. 1987 Mar;29(4):493-501. doi: 10.1002/bit.260290414.
Biological denitrification of drinking water was studied in a fluidized sand bed reactor using a mixed culture. Hydrogen gas was used as the reaction partner. The reaction kinetics were calculated with a double Monod saturation function. The K(s) value for hydrogen was below 0.1% of saturation. No appreciable biofilm diffusion effects were detected. Reactor performance was a function of the culture's past history. Batch experiments always exhibited an accumulation of NO(2) (-), but continuous experiments with a sufficiently long residence time always resulted in complete nitrogen removal. Rates of up to 23 mg N/L h, 25 mg N/g DW h, and 7.9 mg H(2)/L h were achieved. Residence times of 4.5 h would be required for complete denitrification of water containing 25 mg NO(3) (-)-N/L or approximately 1 h for every 5 mg/L.