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3.2 Denitrification of Wastewater
Technical Description
This technology is based upon biological denitrification and thermal
decomposition of the ammonium carbonate. The phases and operations of the
process are neutralization of nitrate and ammonia enriched waters (waters
containing NH4NO3 and NH3) with carbon dioxide (CO2), followed by
biological denitrification in an anaerobic activated sludge media. During
this process, pH corrections are made with the CO2, and the biomass is
stirred at the same time. The organic carbon source for bacterial growth
is contained within the wastewater. Subsequently, the effluent is
subjected to temperatures of 90oC to 95oC, at which temperatures thermal
decomposition of ammonium carbonate occurs. Gases containing ammonia
(NH3), CO2, nitrogen (N2), and water vapour, may be recycled into
fertilizer production where they can be converted from the calcium
nitrate, Ca(NO3)2, phase into ammonium nitrate, NH4NO3.
Extent of Use
This technology is used in Romania.
Operations and Maintence
Operation of this technology requires provision of biological
denitrification in a treatment system with two compartments, having an
internal connection which allows the biomass to be stirred by the
hydrostatic pressure differentials created by the CO2 used for pH
corrections during the denitrification process, which is injected under
pressure. The second element of the process is a column for ammonium
carbonate, (NH4)2CO3, decomposition, and NH3 and CO2 stripping. The
activated sludge portion of the treatment process, if lacking adequate
organic carbon for bacterial growth, may require addition of methanol as a
carbon source. The system requires specialist operating personnel.
Level of Involvement
This technology is implemented at the municipal and industrial levels.
Costs
The estimated cost of a purification plant treating wastewater at a rate
of 200 m3/h is approximately $6.1 million. Approximately $5 million of
this cost is incurred in plant construction.
Effectiveness of the Technology
This technology is best suited for treating wastewater flows of 200
m3/h, having a contaminant composition 5 000 mg/l NO3- and 2 500 mg/l
NH4+. For wastewaters meeting these characteristics, the technology is
highly efficient, and produces a treated effluent with a contaminant
concentration of less than 50 mg/l NO3-. In comparison with the classic
nitrification-denitrification and ammonia stripping-denitrification
processes, this technology allows the elimination of the nitrification
phase and the corresponding reductions in the consumption of energy,
oxygen, and sodium bicarbonate (Na2CO3); the elimination of the use of
sodium hydroxide (NaOH) as a free NH3 source in the stripping process; the
elimination of the use of sulphuric acid, H2SO4, as a neutralizer in the
denitrification process and avoids pollution of the water with sodium,
Na+, and sulphate, SO42-, ions as a consequence; and the reduction of
energy consumption for mechanical stirring of the biomass in the
bioreactor by using CO2 pressure.
Suitability
This technology is suitable for use in industries treating wastewater
contaminated with nitrogen fertilizers.
Advantages
This technology may be extended to provide for reuse of the product
water and byproducts. It may also be modified to achieve heavy metal
removal.
Disadvantages
No disadvantages have been identified.
Cultural Acceptability
The technology is culturally acceptable as an improved wastewater
treatment technique.
Further Development of the Technology
The technology is fully developed.
Information Sources
ICPEAR (Institutul de Cercetari pentru Epurarea Apelor
Reziduale - Research Institute for Waste Waters Treatment), Sos. Pandrui
nr 90-92, sector 5 Bucuresti, Bucharest COD 76231, Romania, Tel./fax: (
40-1) 410 67 16.
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