In wastewater systems where specific forms of nitrogen are limited in permits or systems where monitoring is required, nitrite and nitrate concentrations through the system should be understood.
Systems that are required to monitor effluent total nitrogen (TN), total inorganic nitrogen (TIN) or NOx should sample for nitrite (NO 2 -) and nitrate (NO 3 -) at important locations thought the plant.
Nitrification and denitrification efficiency and stability depends on many factors: proper pH, alkalinity, dissolved oxygen (DO), temperature, available carbon, solids retention time (SRT), internal mixed liquor recycle rates (IMLR), and anoxic conditions among other factors for each respective biological system.
Nitrogen enters wastewater plants as ammonia (NH 3) or ammonium (NH 4 +) and is removed by biological treatment processes. Typical ammonia nitrogen levels in raw municipal influent ranges from 30 mg/L - 50 mg/L NH 3 -N. Nitrate levels indicate the stage of conversion of ammonia and organic nitrogen forms to nitrate by the aerobic biological treatment steps during nitrification.
Nitrification converts ammonia/ammonium to nitrate in an oxic condition with a stable population of nitrifying bacteria, proper oxygen (DO), alkalinity, pH, temperature and solids retention time (SRT).
Denitrification converts nitrate ultimately to nitrogen gas (N 2) where it’s removed from the system in an anoxic condition with adequate readily biodegradable carbon, proper detention time, temperature and void of free oxygen (DO). If the system has an internal recycle (IR or IMLR) to aid in denitrification, proper recycle rates should be monitored.
Anoxic zone nitrate monitoring is important to understand the effectiveness of denitrification. In systems with swing zone, capability can be an indicator to facilitate either anoxic or oxic swing zone requirements.
In systems that perform biological phosphorus removal (BPR), nitrates should be monitored in a return activated sludge (RAS) flow that enters the anaerobic zone. Nitrates entering this zone reduce or stop key functions of biological phosphorus removal in this stage.
In activated sludge mixed liquor (ML), nitrite and nitrate monitoring at the end of the biological system before it enters secondary clarification is important to understand. Improper solids retention time (SRT) can lead to excessive solids detention in secondary settling and if nitrite/nitrate concentrations are high, this can lead to floating sludge, clarifier blanket denitrification and high effluent solids.
Certain specialised anaerobic bacteria can perform shortcut nitrogen removal. These types of bacteria do not employ standard nitrification/denitrification paths for nitrogen removal. This type of nitrogen removal is typically performed in side stream systems where levels of nitrite and nitrate are key measurements at various stages in the process. Incomplete denitrification can lead to increased chlorine disinfection costs due to nitrite demand.
Effluent nitrite and nitrate monitoring may be required as a numerical limit or monitoring parameter either as individual pollutants or as part of a total nitrogen (TN) or total inorganic nitrogen (TIN). requirement.