Process description: The waste effluent contaminated with NH3 and NH4NO3 is treated, first, across a special strong cation resin which removes the NH4+ ions, afterwards, across a special weak anion resin which removes the NO3– ions.
The produced demineralised water with a conductivity value of 15 – 30 µS/cm is polished across a mixed bed exchanger (MB). The demineralised water leaving the MB with a conductivity value of less 0.1 µS/cm is recycled as boiler feed or process demineralised water to the process plants. The loaded cation resin is regenerated with 50-60 % cold HNO3 and the loaded anion resin is regenerated with 15 – 20 % NH3. The eluted cation and anion resin regeneration effluents are selective fractioned in several fractions. The most concentrated cation and anion fractions are mixed together and the resulted 18 -25 % NH4NO3 solution is recycled to the process plant.
The other fractions are recycled inside the Feretarex system and as result no supplementary waste effluents are produced.
More information about the process can be found here.