264874 Cu-SSZ-13 Catalysts for the Selective Catalytic Reduction of NOx with NH3: Catalyst Characterization and Reaction Mechanisms

Monday, October 29, 2012: 8:55 AM
319 (Convention Center )
Ja Hun Kwak1, Feng Gao1, Janos Szanyi1, Jong-Hwan Lee2 and Charles H. F. Peden1, (1)Institute for Integrated Catalysis, Pacific Northwest National Laboratory, Richland, WA, (2)Aftertreatment Engineering, Daimler Trucks North America, Detroit, MI


The abatement of environmentally harmful NOx compounds (NO, NO2, and N2O), especially when emitted from ‘lean-burn’ mobile or stationary power sources, remains a challenging task for the catalysis community. Selective catalytic reduction (SCR) with ammonia using metal-exchanged zeolites [1] is now being commercialized on diesel vehicles. In particular, recent patent literature indicates that the commercial formulations are based on zeolites with a chabazite (CHA) structure (see references 22 and 24 in [2]). We recently published the first open-literature paper describing the comparative performance of a Cu-CHA (SSZ-13) catalyst relative to Cu-beta and Cu-ZSM-5 for the SCR of NOx with NH3, particularly focusing on the activity and N2 selectivity [3]. In this presentation, we will describe results of more recent studies that address a number of additional aspects of these catalysts including the effects of NO/NO2 ratio and hydrothermal aging on performance, as well as structural studies that account for the relative performance of these materials. The implications of these results for understanding the NH3 SCR reaction mechanisms will also be discussed.


ZSM-5 (CBV-3024, Si/Al2 = 30), beta (CP-814C, Si/Al2 = 38) and Y (CBV-100, Si/Al2 = 5.2) zeolites were obtained from Zeolyst International Co.  The SSZ-13 zeolite was synthesized using the methods recently published by Fickel and Lobo [2], reported to give a material with a Si/Al2 ratio of ~12. Copper ions were then exchanged into the zeolite in an aqueous ion-exchange process, using Cu(NO3)2 as precursor. After drying and calcination, intact zeolite structures were confirmed with XRD measurements. The SCR activities of these powder catalysts have been examined in a flow reactor system at various temperatures in a gas mixture containing 350 ppm NOx, 350 ppm NH3, 14% O2 and 10% H2O with a balance of N2. Catalyst characterization included synchrotron 27Al NMR, XANES and EXAFS spectroscopies, XRD, TPR, and TPD, and with FTIR of probe molecules (e.g., CO and NO).

Results and Discussion

The effect of hydrothermal aging on selective catalytic reduction of NOx by NH3 was examined under both “standard” (NOx = NO only) and “fast” (NO=NO2) SCR conditions over several Cu-zeolites, with good performance observed for all fresh Cu/zeolite catalysts [4].  At higher temperatures, NO reduction activity was limited by the availability of ammonia as the ammonia oxidation reaction to NOx becomes significant.  A considerable amount of N2O was produced over Cu-Y [4] during “standard” SCR, and also over Cu-beta and Cu-ZSM-5 under “fast” SCR conditions.  In contrast, near 100% selectivity to N2 for NO reduction (less than 5 ppm N2O produced) was observed for Cu-SSZ-13 under all conditions studies.

Significant loss of “standard” NO reduction activity, in greatly varying extents, was observed for most of the Cu/zeolite catalysts after hydrothermal treatment in 10% H2O in air at 800°C for 16 h.  While Cu-SSZ-13 was found to show essentially no change in NO reduction activity, Cu-Y lost its activity completely.  Both Cu-ZSM-5 and Cu-beta were found to lose NO reduction activity primarily at low catalyst bed temperatures, but maintain reasonable activity at high (>350°C) temperatures.  Similar sensitivities to hydrothermal aging were observed for “fast” SCR conditions, and undesirable N2O selectivities were generally worse for all catalysts after aging except for Cu-SSZ-13 [4].

H2-TPR spectra collected over fresh Cu/zeolites could be divided into two groups based on the reducibility of Cu ions.  For fresh Cu-ZSM-5, three reduction peaks were observed at 155°C (perhaps due to overexchanged Cu), 207°C and 315°C.  Similar to Cu-ZSM-5, two reduction peaks were observed at 200°C and 390°C for Cu-beta; these higher temperature features can be attributed to the reduction of Cu2+ to Cu+, and that of Cu+ to Cu0, respectively.  On the other hand, the two reduction peaks observed at 195°C and 310°C for Cu-Y catalysts are assigned only to the reduction of Cu2+ to Cu+ based on the literature, which suggested that Cu2+ ions inside supercages of faujasite (FAU) zeolites are reduced to Cu+ at 195°C, while reduction of Cu2+ ions to Cu+ inside sodalite cages occurs at 310°C [5].  Interestingly, only one H2-TPR reduction peak at 230°C with a broad shoulder at ~300°C was obtained for Cu-SSZ-13.  During the TPR, Cu-SSZ-13 appeared white even at 700°C, which suggests the formation of Cu+, similar to Cu-Y.

Detailed characterization of these catalysts using 27Al NMR, EPR, synchrotron XANES and EXAFS spectroscopies, XRD, and TPD and FTIR of probe molecules (e.g., CO and NO) will be presented to rationalize these results in the context of proposed NH3 SCR reaction mechanisms (see, for example, [6,7]). References

1.    S. Brandenberger, O. Kröcher, A. Tissler, R. Althoff, Catal. Rev.-Sci. Eng.  50, 492 (2008).

2.    D.W. Fichel, R. Lobo, J. Phys. Chem. C  114, 1633 (2010).

3.    J.H. Kwak, R.G. Tonkyn, D.H. Kim, J. Szanyi, C.H.F. Peden, J. Catal.  275, 187 (2010).

4.    J.H. Kwak, D. Tran, S.D. Burton, J. Szanyi, J.H. Lee, C.H.F. Peden, J. Catal. 287, 203 (2012).

5.    S. Kieger, G. Delahay, B. Coq, B. Neveu, J. Catal. 183, 267 (1999).

6.    J.H. Kwak, D. Tran, S.D. Burton, J. Szanyi, J.H. Lee, C.H.F. Peden, Catal. Lett. 142, 295 (2012).

7.    J.H. Kwak, H. Zhu, J.H. Lee, C.H.F. Peden, J. Szanyi, Chem. Comm. 48, 4758 (2012).

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