Converting nitrogen oxides into nitrogen and water

DeNOx SCR Systems

Selective Catalytic Reduction
The DeNOx SCR unit is used for the reduction of $\ce{NOx}$ content in the flue gas out of the boiler. The process of DeNOx SCR reduces nitrogen oxides $\ce{NOx}$ of combustion flue gases into molecular nitrogen $\ce{N2}$ and water vapor $\ce{H2O}$.

$\ce{4NO + 4NH3 + O2 -> 4N2 + 6H2O}$
$\ce{2NO2 + 4NH3 + O2 -> 3N2 + 6H2O}$
$\ce{NO + NO2 + 2NH3 -> 2N2 + 3H2O}$

$\ce{NOx}$ breaks down when it reacts with the reducing agent $\ce{NH3}$, in the presence of the catalyst. The ammonia $\ce{NH3}$ is distributed into the flue gas prior to the catalyst The catalyst, by providing active reaction sites, allows the reaction to occur at lower temperatures than usually used for this kind of reaction. The $\ce{NH3}$ diffuses into the catalyst pore structure and is adsorbed onto an active catalyst site. The $\ce{NOx}$ then reacts with the adsorbed $\ce{NH3}$, completing the reaction. The reaction depends primarily on available active sites (a function of geometric surface area, pore volume, and concentration of active catalyst component), flue gas temperature and reagent concentration. A well-balanced process will maintain appropriate output levels of residual $\ce{NOx}$ and $\ce{NH3}$.
DeNOx Systems
Converting nitrogen oxides
DeNOx System
The SCR system consists of the SCR reactor, where the catalyst is installed. For reaction of $\ce{NOx}$ and $\ce{NH3}$ to $\ce{N2}$ and $\ce{H2O}$ over the catalyst, an $\ce{NH3}$/air mixture is injected upstream the reactor by means of the ammonia injection grid (AIG).

For the $\ce{NH3}$ supply, aqueous ammonia $\ce{NH4OH}$ or urea is stored in tanks and evaporated by the vaporizer, mixed with hot dilution air and injected into the flue gas before the catalyst.

High-Dust


  • Coal Fired Boiler
  • Cement Rotary Kiln
  • Biomass Fired Boiler
  • Presence of different pollutants
  • In between the existing heat recovery system

Low-Dust


  • Gas Fired Boiler (HRSG)
  • Oil Fired Boiler
  • WtE (not recommended)
  • Presence of different pollutants
  • In between the existing heat recovery system

Tail End


  • WtE
  • Sinter Application
  • Cement Rotary Kiln (RDF)
  • Most pollutants are already reduced below emission limits except the $\ce{NOx}$
  • Most of the time need of a separate re-heating system

Delivery

Catalysts, injection systems, reagent storage and preparation, programming / visualization, piping materials and storage tanks.

DeNOx SNCR Systems

Selective Non-Catalytic Reduction
We provide the leading technologies regarding SNCR designs with ammonia and urea for optimal performance, reducing nitrogen oxides $\ce{NOx}$ in combustion flue gases into molecular nitrogen $\ce{N2}$ and water vapor $\ce{H2O}$.

The simplified reduction with ammonia ($\ce{NH3}$) of the nitrogen oxide is $\ce{4 NO + 4 NH3 + O2 -> 4 N2 + 6 H2O}$. In case of urea ($\ce{NH2CONH2}$) ammonia is first produced: $\ce{NH2CONH2 + H2O -> 2NH3 + CO2}$

$\ce{NOx}$ breaks down when it reacts with the reducing agent $\ce{NH3}$, without the presence of the catalyst at temperatures of $760^\circ\mathrm{C}$ to $1090^\circ\mathrm{C}$.

SNCR provides

  • lessening of nitrogen oxide emissions
  • simple and agile establishment
  • reduced investment expenses

Contact Us

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