Development of a novel process for anoxic ammonia removal with sulphidogenesis

• Published in: Process biochemistry (1991) 2008-09, Vol.43 (9), p.984-991
• Main Author: Sabumon, P.C.
• Format: Article
• Language: English
• Subjects: Ammonia; Anoxic; Organic carbon; Sulphate; Sulphide; Sulphidogenesis
• ISSN: 1359-5113; 1873-3298
• DOI: 10.1016/j.procbio.2008.05.004

A novel process for anoxic ammonia removal with sulphidogenesis was developed in a 1.75 l capacity up-flow hybrid reactor in anoxic conditions (ORP = −225 ± 25 mV) for simultaneous removal of ammonia, organic carbon and sulphate. The process was operated for a total of 240 days. Synthetic feed was used during the first 220 days. After start-up and acclimatization of the process for 120 days, loading rate studies were carried out in continuous operation (at COD/SO 4 2− ratio = 1.3) at HRT of 1 day. The reactor performance decreased at a high organic loading rate of 3.75 kg COD/m 3/d due to sulphide inhibition. The continuous injection of air at a rate of 0.2 l/min at 40 cm height from the bottom of reactor helped in sulphide oxidation within the anoxic zone and this helped to increase the removals of NH 4 +, COD and SO 4 2− substantially. Application of the developed process for the treatment of primary treated combined tannery effluent was carried out during the final phase at an organic loading rate of 3.9 kg COD/m 3/d (COD/SO 4 2− ratio = 1.3) and at an ammonia loading rate of 0.3 kg NH 4 +/m 3/d. The percentage removals of NH 4 +, COD and SO 4 2− were in the ranges of 65.9–89.4, 51.9–70.7 and 70.8–83.1, respectively. The specific rates of sulphate reduction and anoxic ammonia removal of the reactor biomass were 0.36 kg SO 4 2−/kgMLVSS/d and 0.07 kg NH 4 +/kgMLVSS/d, respectively.