N
2 is the desired product over NO/N
2O for NH
3 oxidation on ammonia slip catalysts (ASC). [1] While the thermodynamic N
2 selectivity is larger than 99% at ASC conditions, the N
2 selectivity of highly active platinum group metals (PGMs) are often lower than 80%, [2] insufficient to meet the emission regulations. To date, there is no self-consistent comparison of intrinsic selectivity over PGMs. Here, we perform DFT computations of relevant reaction steps of ammonia oxidation on Pt, Pd and Rh (111). We show BrønstedâEvansâPolanyi relationships for NH
x* activations by both O* and OH* and the barriers for NH
x* activation follows Pt < Pd < Rh. We build microkinetic models to predict product selectivity at reaction conditions typical of ASC and observe that the N
2 selectivity follows Pt > Rh > Pd. We observe the dependence of selectivity on
T and pressure follows the same trend for the three metals: low
T and
P(O
2) :
P(NH
3) result in higher N* coverage and N
2 selectivity. The predicted selectivity of N
2, NO and N
2O agree well with experimental observations. We further perform sensitivity analysis and demonstrate the high selectivity observed for Pt originates from its smaller barriers to activate NH
x*. Higher N
2 selectivity on Rh than on Pd, however, results from the much larger barrier to form NO than N
2 on Rh, indicating
Ea,NHx+OHx and
Ea,N2(g) formation/ E
a,NxO(g) formation are two important factors determining the N
2 selectivity.
REFERENCES
- S. Shrestha, M. P. Harold, K. Kamasamudram, A. Kumar, L. Olsson, K. Leistner, Catal. Today 267(2016) 130.
- L. Chmielarz, M. JabÅonska, A. Struminski, Z. Piwowarska, A. Wegrzyn, S. Witkowski, M. Michalik, Appl. Catal. B 130-131(2013) 152.