The catalyst using ammonia as reducing agent, selective reduction decontamination nitric acid tail gas, nitrate tail gas, and due to the use of Nitric acid (nitrate) produces NOx. NOx is converted to N2 and H2O. Applicable to constant pressure, medium-pressure and double-pressurized nitric acid craft.
Technical Parameters
|
Product Specification |
Honeycomb, spheroids, Bar-Type |
|
Bulk Density |
0.7～0.8g/ml |
|
Pressure |
Open-Pressure |
|
Reaction Temperature |
160～420℃ |
|
NH3/NOx Molecular Proportion |
1.1～1.2 |
|
Airspeed |
3000~10000 h-1 |
|
NOx Conversion Rate |
>95％ |
|
Working Life |
≥2 Years |
Operating Principle
1) 6NO+4NH3→5N2+6H2O -1807.0KJ/mol
2) 6NO2+8NH3→7N2+12H2O -2659.9KJ/mol
Catalyst Loading and Activation
According to the size of NOx emission concentrations and gradually increase the ammonia, results in NH3/ NOx control in 1.1～1.2. The temperature of decontamination NOx is 160～420℃. |
