Biological Nitrogen Removal Database

A manually curated data resource for microbial nitrogen removal


Water Treatment Plant


Experimental setup


Influent:Saline wastewater

Denitrification system:Sulfur-driven denitrification (SDN) system

Denitrifying reactor:Batch culture

Medium:Sulphur granules

Culture taken from:Sludge from the tidal flats

Organism (s) cultured:nan

Respiration:nan

Electron donor:Elemental sulphur

Electron acceptor:Nitrate


Experimental Information


Input NO3-N (mg/l):nan

Nitrate removal rate (mg NO3-N/l/h):8–50

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

Microorganisms identified:nan

Molecular tools:nan


Information about Article


Major findings:In this sulfur-driven denitrification application in high saline wastewater plan validated that, salinity affects the pH of the reactor and the efficiency of denitrification is affected by the pH. Also at high temperatures denitrification ceases.

Authors:Koenig and Liu., 2004

Title:Autotrophic Denitrification of High–Salinity Wastewater Using Elemental Sulfur: Batch Tests

Pubmed link:Link

Full research link:Link

Abstract:The feasibility of autotrophic denitrification of a highsalinity wastewater using sulfur–oxidizing autotrophic denitrificants was studied. These autotrophic bacteria oxidize elemental sulfur to sulfate while reducing nitrate to elemental nitrogen gas, thereby eliminating the need for the addition of organic carbon compounds. A series of bench–scale batch tests was performed with synthetic and actual flue gas desulfurization (FGD) wastewater to examine the effects of various environmental and operational factors such as temperature, pH, high salinity, and potentially toxic substances on the rate of autotrophic denitrification using elemental sulfur. Specific denitrification rates of 6 to 8 mg nitrate–nitrogen (NO3—?N)/g volatile suspended solids (VSS)·h were obtained. The highest denitrification rates were found between pH 7.0 and 8.0 and a temperature of 30 8 C. The denitrification rate started to decrease above an osmotic pressure of 19 atm (approximately 70% of seawater), independent of the type of salt ions, and amounted to approximately 70% activity at the concentration of seawater. Polyphosphate or pyrophosphate could be used as the source of phosphorus instead of orthophosphate because the latter caused immediate calcium phosphate precipitation in the FGD wastewater. Inhibiting factors attributed to inorganic or organic compounds originating from coal combustion were discussed.