Biological Nitrogen Removal Database

A manually curated data resource for microbial nitrogen removal


Groundwater Water systems


Experimental setup


Influent:Tap water

Denitrification system:Sulfur-based autotrophic denitrification and heterotrophic denitrification

Denitrifying reactor:Column packed-bed reactor

Medium:nan

Culture taken from:Denitriying activated sludge

Organism (s) cultured:nan

Respiration:Anaerobic

Electron donor:Elemental sulfur

Electron acceptor:Nitrate


Experimental Information


Input NO3-N (mg/l):110-450

Nitrate removal rate (mg NO3-N/l/h):13.4-42.2

Denitrification rate (gNO3-N removed/m3/day):0.45

Microorganisms identified:nan

Molecular tools:nan


Information about Article


Major findings:Sodium bicarbonate was used as the alkalinity source it resulted in the enhanced the performance of the sulfur based autotrophic denitrification compared to when limestone was used. Stimulating mixtrophic denitrification process with methanol supplemented the process three folds.

Authors:Sahinkaya and Dursun., 2012

Title:Sulfur-oxidizing autotrophic and mixotrophic denitrification processes for drinking water treatment: Elimination of excess sulfate production and alkalinity requirement

Pubmed link:Link

Full research link:Link

Abstract:This study evaluated the elimination of alkalinity need and excess sulfate generation of sulfur-based autotrophic denitrification process by stimulating simultaneous autotrophic and heterotrophic (mixotrophic) denitrification process in a column bioreactor by methanol supplementation. Also, denitrification performances of sulfur-based autotrophic and mixotrophic processes were compared. In autotrophic process, acidity produced by denitrifying sulfur-oxidizing bacteria was neutralized by the external NaHCO(3) supplementation. After stimulating mixotrophic denitrification process, the alkalinity need of the autotrophic process was satisfied by the alkalinity produced by heterotrophic denitrifiers. Decreasing and lastly eliminating the external alkalinity supplementation did not adversely affect the process performance. Complete denitrification of 75 mg L(-1) NO(3)-N under mixotrophic conditions at 4 h hydraulic retention time was achieved without external alkalinity supplementation and with effluent sulfate concentration lower than the drinking water guideline value of 250 mg L(-1). The denitrification rate of mixotrophic process (0.45 g NO(3)-N L(-1) d(-1)) was higher than that of autotrophic one (0.3 g NO(3)-N L(-1) d(-1)). Batch studies showed that the sulfur-based autotrophic nitrate reduction rate increased with increasing initial nitrate concentration and transient accumulation of nitrite was observed.