Definition
NOx reduction efficiency
NOx reduction efficiency is the percentage of inlet NOx removed by a DeNOx system. It depends on catalyst activity, mixing, temperature and cleanliness.
- Subject
- SCR and SNCR
- Also known as
- DeNOx efficiency, SCR efficiency, NOx conversion
NOx reduction efficiency is the percentage of inlet nitrogen oxides removed by a DeNOx system. It is commonly calculated as (NOx in - NOx out) / NOx in x 100, using consistent units, reference oxygen and dry or wet basis. The metric is central to SCR and SNCR performance.
Efficiency alone is not enough. A system can show high NOx removal while consuming too much ammonia, creating high ammonia slip, fouling downstream equipment or operating outside its permit basis.
Typical performance
| System | Typical reduction range | Typical ammonia slip |
|---|---|---|
| High-dust SCR | About 80 to 95% | About 2 to 5 ppm |
| Tail-end SCR | About 90 to 98% | About 1 to 3 ppm |
| SNCR | About 30 to 60% | About 5 to 10 ppm |
| SNCR plus SCR | Can approach 99% | Project-specific |
Actual performance depends on inlet NOx, temperature window, residence time, catalyst volume, ammonia distribution, fuel, load, dust loading and ageing.
What erodes efficiency over time
- Catalyst masking - ash covers active surface.
- Catalyst poisoning - chemical species deactivate active sites.
- Catalyst pluggage - blocked channels create bypass and maldistribution.
- AIG drift - poor ammonia-to-NOx distribution creates local slip and local under-treatment.
- Temperature excursions - gas too cold or too hot reduces reaction effectiveness.
- Erosion - fly ash or large particles remove active material.
Measurement context
NOx reduction should be evaluated with inlet and outlet CEMS or test data at comparable load and oxygen basis. Short-term values can be distorted by load ramps, ammonia control lag, analyser calibration, stratification and wet-to-dry corrections.
How cleaning preserves efficiency
Sonic horns and sootblowers help preserve catalyst cleanliness where ash masking and pluggage are the limiting mechanisms. Keeping the inlet face open improves gas distribution, slows pressure-drop rise and reduces the temptation to over-inject ammonia to compensate for lost activity.
Acoustic cleaning cannot reverse chemical poisoning or lost catalyst activity. Its value is strongest where the catalyst is still active but physically shielded by ash.
Measurement and operating detail
NOx reduction efficiency depends on where NOx is measured and how the flue gas is normalised. Inlet and outlet analysers should be corrected to the same dry or wet basis, oxygen reference and load condition. A short performance test at steady load may not represent low-load operation, fuel changes, ammonia-grid maldistribution or catalyst ageing. Plants therefore trend inlet NOx, outlet NOx, ammonia flow, ammonia slip, reactor temperature, pressure drop and catalyst-layer age together.
Common reasons for declining efficiency include low catalyst activity, ash masking, catalyst pluggage, poor ammonia mixing, failed injection nozzles, temperature outside the catalyst window, bypass leakage and changes in fuel nitrogen. In SNCR, residence time, temperature window and reagent distribution are the central limits. Adding more reagent can appear to restore efficiency while creating ammonia slip, ammonium-bisulphate fouling and downstream particulate issues.
Acoustic cleaning has a narrow but important role. It protects physical access between gas and active catalyst by reducing loose ash accumulation on the inlet face and around module edges. It does not change catalyst chemistry, reaction temperature or injection quality. A proper diagnosis separates cleaning recoverable masking from true catalyst deactivation before selecting the fix.
Performance-test detail
A DeNOx performance test should define the averaging period, minimum load, reagent quality, ammonia-to-NOx ratio, inlet NOx distribution and allowable ammonia slip. The same percentage reduction can represent very different performance depending on inlet NOx. Reducing 800 mg/Nm3 to 160 mg/Nm3 is not the same duty as reducing 250 mg/Nm3 to 50 mg/Nm3, even though both are 80 percent reduction.
Catalyst management also matters. Operators may add layers, replace modules, regenerate catalyst or adjust ammonia injection to preserve efficiency. If pressure drop is rising at the same time as efficiency is falling, ash masking or pluggage should be investigated before assuming the catalyst chemistry is spent. If pressure drop is stable but activity tests are poor, cleaning will not recover the lost reaction rate. Acoustic cleaning is therefore part of the physical-maintenance toolkit around the reactor, not the whole DeNOx strategy.
Related terms
Explore the subject
Related terms
4 terms
- Selective Catalytic ReductionSCR reduces NOx by injecting ammonia upstream of a catalyst. Temperature, mixing, catalyst condition and ash control determine performance.
- Selective Non-Catalytic ReductionSNCR injects ammonia or urea into a furnace temperature window to reduce NOx without catalyst. It is simpler than SCR but usually less efficient.
- Ammonia slipAmmonia slip is unreacted ammonia leaving the DeNOx system in the flue gas. It is regulated, expensive in lost reagent, and causes ammonium-bisulphate fouling downstream.
- Catalyst maskingCatalyst masking is the deposition of a thin ash layer on the SCR catalyst face that blocks ammonia and NOx from reaching the active sites. Distinct from pluggage and poisoning.
References