A two-stage non-conventional bench scale biological treatment system was in
vestigated for the treatment of the wastewater laden with ammonium nitrate.
The first stage which consisted of a fixed film anoxic reactor effected de
nitrification of nitrate ion, while the second stage consisting of a pond e
ffected ammonia removal. Dissimilatory denitrification requires external ca
rbon source as an electron donor. Methanol was used as electron donor in th
is system. The system exhibited substantial nitrate and ammonia removal. Th
e influent nitrate-N concentration which was on average 193.87 +/- 12.68 mg
/l was reduced to 5.86 +/- 4.86 mg/l in the denitrification unit. There was
only a marginal reduction of ammonia in the denitrification unit and most
of the ammonia-N was removed in the pond. The ammonia-N was reduced from an
average value of 104.87 +/- 3.49 mg/l at denitrification unit inlet to 33.
37 +/- 8.12 mg/l at the pond outlet. There was no corresponding increase in
the nitrite or nitrate concentration in proportion to ammonia reduction in
the pond. The average nitrate concentration in the pond outlet was 2.4 +/-
0.93 mg/l. Microbiological investigation of the system revealed the presen
ce of significant populations of denitrifying organisms in the first stage,
and denitrifying, nitrifying and algal populations in the second stage. Th
e system also sustained wastewater of pH as low as 3.87 and appears to be v
ery promising for larger scale industrial wastewater treatment.