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Nitrogen Removal in Wastewater Treatment

Engineering approaches to meet stringent total nitrogen discharge limits.

Total nitrogen removal requires a combination of nitrification (converting ammonia to nitrate under aerobic conditions) and denitrification (converting nitrate to nitrogen gas under anoxic conditions). The revised EU Directive mandates TN < 10 mg/L for plants > 10,000 PE, with 80% minimum removal efficiency. Most existing plants achieve partial nitrogen removal but need process optimization or additional treatment stages to meet future limits.

Key Numbers

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mg/L
EU Total Nitrogen limit
0%
%
Minimum removal efficiency
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°C
Min. temp for nitrification
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mg O₂/L
DO required for nitrification

Technical Overview

Nitrogen exists in wastewater primarily as ammonium (NH4+) and organic nitrogen. Effective removal requires converting these forms through biological processes:

Nitrification: Autotrophic bacteria (Nitrosomonas, Nitrospira) oxidize ammonium to nitrate under aerobic conditions. This requires sufficient dissolved oxygen (>2 mg/L), adequate SRT (>8 days at 10°C), and alkalinity for pH buffering.

Denitrification: Heterotrophic bacteria reduce nitrate to nitrogen gas under anoxic conditions, using organic carbon as the electron donor. Internal recirculation returns nitrate-rich mixed liquor from the aerobic to the anoxic zone.

Advanced processes: For very low TN targets (<6 mg/L), post-denitrification with external carbon dosing or anammox-based processes may be required.

Engineering Insight: Carbon Management

The C:N ratio is critical for denitrification. A minimum BOD5:TN ratio of 4:1 is typically required. In plants with low influent carbon or high nitrification efficiency, external carbon sources (methanol, ethanol, glycerol) may be needed. This adds OPEX of €0.50–1.50 per kg N removed.

Technology Comparison

Pre-Denitrification (MLE)

high

Modified Ludzack-Ettinger process with anoxic zone upstream of aerobic zone and internal recirculation.

Footprint: Medium
Energy: Medium
Advantages
  • Uses influent carbon
  • Proven and reliable
  • Low chemical cost
  • Good for retrofit
Limitations
  • Limited by recirculation ratio
  • TN typically > 8 mg/L
  • Needs adequate C:N ratio

Post-Denitrification

high

Separate denitrification stage after nitrification with external carbon dosing.

Footprint: Medium-Large
Energy: Medium
Advantages
  • Very low TN achievable
  • Independent of influent C:N
  • Consistent performance
Limitations
  • External carbon cost
  • Additional reactor volume
  • Carbon dosing control complexity

SBR (Sequencing Batch Reactor)

medium

Time-based alternation between aerobic and anoxic phases in the same reactor.

Footprint: Small
Energy: Medium
Advantages
  • Flexible operation
  • Good for small plants
  • Single tank design
  • Simple to retrofit
Limitations
  • Batch operation
  • Decanting complexity
  • Limited throughput

MBBR Add-On

high

Moving bed biofilm reactor carriers added to existing tanks to increase nitrification capacity.

Footprint: Very small
Energy: Medium
Advantages
  • Minimal footprint
  • Uses existing tanks
  • Increases SRT
  • Quick installation
Limitations
  • Carrier cost
  • Screen maintenance
  • Aeration redesign needed

For Existing Plants

The most common nitrogen removal retrofit involves converting a portion of the existing aeration basin to anoxic operation and adding internal recirculation. This typically achieves TN < 12 mg/L. For stricter limits, supplemental carbon dosing or MBBR biofilm carriers can be added without expanding the tank footprint.

EU Nitrogen Limits

Directive (EU) 2024/3019, Article 7: Total Nitrogen ≤ 10 mg/L (annual average) or minimum 80% removal for plants > 10,000 PE. Stricter limits may apply in sensitive areas.

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Last reviewed: August 2026. Regulatory requirements may vary by national implementation. This content is for informational purposes and does not constitute legal or engineering advice.