The SO2 conversion rate of single absorbtion plants is lower than double absorbtion, and many single absorbtion plants installed tail gas scrubbers to reduce this SO2 content rather than convert the plant to double absorbtion. Scrubbing the tail gas to acceptable SO2 emission values can be done with seawater, caustic, lime slurry, hydrogen peroxide or ammonia. After exiting the absorber tower, the gas enters a scrubber tower where ammonia (NH3) is injected and contacts the SO2. Ammonium Sulphite and Bi-sulphite are formed and some of these salts are entrained in the exit air.
These salts are soluble, but can be emitted in quite large volumes, e.g. 2,000 – 15,000 mg/m3 and are generally < 3 microns in size, with a large amount < 1 mircron.
Prevent blockage of fibre bed by salts solidification.
Occasional risk of weak acid mist emission