PROCESS FOR REDUCING THE CONTENT OF NOx AND N2O FROM A TAIL GAS OF A NITRIC ACID PROCESS
AssigneeCasale SA
InventorsFabio Laurenzi, Raffaele Ostuni, Jean Francois Granger
Life of this patent
Estimating the term…
Abstract
Process for reducing the content of NOx and N2O from an input tail gas (10) of a nitric acid process, said input tail gas having a temperature lower than 400° C., the process comprising an abatement stage at least including a deN2O stage and deNOx stage and providing a conditioned tail gas (12) having a temperature greater than the input tail gas (10), wherein, prior to submission to said abatement stage, said input tail gas (10) is pre-heated to a temperature of at least 400° C. by indirect heat exchange with at least a portion of said conditioned gas (12).
Claims20
1-15. (canceled)
A process for reducing the content of NOx and N2O from an input tail gas of a nitric acid process, said input tail gas having a temperature lower than 400° C., the process comprising:
- an abatement stage including at least a stage of catalytic N2O decomposition (deN2O) over an iron-loaded zeolite catalyst and a stage of catalytic NOx reduction (deNOx), said abatement stage providing a conditioned tail gas having a temperature greater than the input tail gas, wherein:
- prior to submission to said abatement stage, said input tail gas is pre-heated to a temperature of at least 400° C. by indirect heat exchange with at least a portion of said conditioned gas;
- said deN2O and deNOx stages being carried out in separated catalytic beds and said deNOx stage being carried out over at least one of:
- a vanadium catalyst, a copper-loaded zeolite catalyst, or an iron-loaded zeolite catalyst.
A system for reducing the content of NOx and N2O from a tail gas of a nitric acid process, the system comprising:
- a tail gas pre-heater, which provides a pre-heated tail gas;
- a catalytic reactor, receiving said pre-heated tail gas and carrying out catalytic N2O decomposition (deN2O) and catalytic NOx reduction (deNOx), thereby providing a conditioned gas;
- a flow line arranged to recycle at least a portion of said conditioned gas to said tail gas pre-heater, wherein said conditioned gas acts as hot heat exchange medium;
- wherein said catalytic reactor includes at least one catalytic bed wherein deN2O is carried out and at least one catalytic bed wherein deNOx is carried out.
A method for revamping a system for reducing the content of NOx and N2O from an input tail gas of a nitric acid process, said system comprising a catalytic reactor receiving said input tail gas and carrying out an abatement stage including a stage of deNOx and possibly a stage of deN2O, said catalytic reactor providing a conditioned tail gas, said method being comprising:
- installation of a tail gas pre-heater upstream of said catalytic reactor, said pre-heater being fed with said input tail gas and supplying a pre-heated tail gas to the catalytic reactor;
- and
- installation of a flow line arranged to recycle at least a portion of the conditioned gas to said newly installed tail gas pre-heater, wherein said conditioned gas acts as hot heat exchange medium.
Dependencies are inferred from the claim text.