Peculiar Changes in Pt Accessibility and Morphology for Pt...

1
Peculiar Changes in Pt Accessibility and Morphology for Pt/BaO-Al 2 O 3 Lean NO x Trap Catalysts with Varying Sulfation Levels Xian-Qin Wang*, Do Heui Kim, Ja Hun Kwak, Chongmin Wang, Janos Szányi, Charles H.F. Peden Institute for Interfacial Catalysis, Pacific Northwest National Laboratory, P.O. Box 999, Richland, WA 99352 (USA) *[email protected] Introduction Lean NO x trap (LNT) catalysts composed of Pt/BaO-Al 2 O 3 represent a viable approach to meet the stringent NO x emission standards being imposed on diesel engines [1]. However, poisoning of LNTs by SO 2 represents a particularly challenging issue for this technology [1]; thus, it is important to develop more sulfur-durable LNT catalysts. As part of such an effort, we have been studying the effects of sulfation and desulfation on Pt accessibility and morphology changes in Pt/BaO-Al 2 O 3 model catalysts. In this work, a series of Pt/BaO-Al 2 O 3 catalysts with three different sulfation levels (non-sulfated, partially-sulfated, and fully- sulfated) were prepared. Pt accessibility after successive reductions in H 2 at elevated temperatures was measured by an irreversible volumetric H 2 chemisorption method. Moreover, the morphology of the sample after reduction at 800°C was characterized by HRTEM and XRD techniques. Materials and Methods Materials preparation. One typical LNT catalyst containing 1.5wt% Pt and 14 wt.% BaO was supplied by Johnson Matthey (Wayne, PA). This sample was calcined at 500°C, then sulfated with SO 2 and O 2 (1:1) at 300°C. We prepared the samples with the different sulfation levels by varying the sulfation process time. In this work, three different sulfation levels, zero sulfation (labeled as 0gS), partial sulfation (3gS) and complete sulfation (10gS), were investigated. Their platinum accessibility and morphology changes were studied as a function of reduction temperatures in order to decouple the thermal degradation from sulfur poisoning. Characterization methods. Platinum accessibility was evaluated with the number of hydrogen atoms per Pt (H/Pt) determined from irreversible H 2 chemisorption uptake measurements obtained after the sample was first reduced at varying temperatures. The morphologies of both the freshly sulfated samples and the samples after the chemisorption measurements at 800°C were characterized with high resolution TEM (HRTEM). The composition of the particles was analyzed by energy-dispersive X-ray spectroscopy (EDS). In order to understand the desulfation process, sulfur K absorption edge XAFS spectra were collected in-situ during the reduction of the catalysts in a flow of a 5% H 2 and 95% He gas mixture (~40 mL/min) at beamline X19A, and Pt L 3 -edge EXAFS spectra were collected in air at room temperature at beamline X18B of the NSLS at BNL. Results and Discussion H/Pt values determined from H 2 chemisorption experiments is a common way to measure the number of active sites and Pt accessibility for many supported Pt catalysts. Fig. 1 shows the H/Pt values obtained as a function of reduction temperature for the fresh (0gS), partially sulfated (3gS), and heavily sulfated (10gS) samples. We observed that Pt accessibility and morphology changes have a complex dependence on the levels of sulfation. The H/Pt ratio decreased uniformly as a function of reduction temperature for the non-sulfated sample. Compared to this one, the partially-sulfated sample instead displayed an optimum H/Pt value at 500°C, and then a slight increase in Pt particle sizes after thermal aging at 800°C. Still different behavior was observed for the fully sulfated sample which gave very low H/Pt ratios for all reduction temperatures, indicating essentially complete poisoning by SO 2 . 1 2 3 4 0 10 20 30 40 50 10g/L S FT magnitude of k 3 -weighted EXAFS R / Å Pt foil Fresh 3g/L S Pt-O in PtO 2 Pt-O in PtSO x Pt-Pt in PtSO x 1 2 3 4 0 10 20 30 40 50 10g/L S FT magnitude of k 3 -weighted EXAFS R / Å Pt foil Fresh 3g/L S Pt-O in PtO 2 Pt-O in PtSO x Pt-Pt in PtSO x 300 400 500 600 700 800 0.0 0.1 0.2 0.3 10 g sulfation 3 g sulfation H/Pt Temperature / o C 0 sulfation 300 400 500 600 700 800 0.0 0.1 0.2 0.3 10 g sulfation 3 g sulfation H/Pt Temperature / o C 0 sulfation Fig.1. Pt dispersion (H/Pt) as a function of Fig.2. Pt L 3 -edge EXAFS spectra for the reduction temperature in H 2 . variously sulfated catalysts and Pt foil. Fig.2 compares the Fourier transformed Pt L 3 -edge EXAFS spectra. The non-sulfated sample (0gS) primarily showed features similar to those of PtO 2 [2], while the fully sulfated sample (10gS) had features matching Pt sulfate clusters [3]. The partially sulfated sample (3gS) seems to have a pattern similar to that of 0gS sample, but the relative intensities of the two main peaks was different. With a simple linear fitting of the spectrum from the 3gS sample using those for the non-sulfated and fully sulfated samples, we estimate that there was around 20% Pt in the Pt sulfate cluster form in this 3gS sample. The EXAFS results were consistent with the initial Pt accessibility measurements in Fig. 1 and provided information regarding the reduction mechanism of the sulfated Pt/BaO/Al 2 O 3 LNT catalysts. Over partially sulfated sample, in particular, S spillover from Pt to Ba occurred gradually and H/Pt was a combined effect of PtS(PtSO 4 ) reduction and Pt sintering. For the fully saturated sample, Pt sintering was facilitated by mobile PtS thereby slowing S spill over to Ba from PtS. Significance This work shows that S levels in LNTs have a significant effect on Pt accessibility and morphology, and they can alter the reduction mechanism. The results aid in decoupling the effects of thermal degradation from sulfur poisoning for the deactivation of LNT samples. References 1. Epling, W. S.; Campbell, L. E.; Yezerets, A.; Currier, N. W.; Parks J. E. Catal. Rev. Sci. Eng. 46, 163 (2004). 2. Shishido, T., Tanaka, T., Hattori, H., J. Catal. 172, 24 (1997). 3. Pley, M., Wickleder, M. S., Z. Anorg. Allg. Chem. 630, 1036 (2004).

Transcript of Peculiar Changes in Pt Accessibility and Morphology for Pt...

Page 1: Peculiar Changes in Pt Accessibility and Morphology for Pt ...old.nacatsoc.org/20nam/abstracts/P-S4-24A.pdf · of reduction temperatures in order to decouple the thermal degradation

Peculiar Changes in Pt Accessibility and Morphology for Pt/BaO-Al2O3 Lean NOx Trap Catalysts with Varying Sulfation Levels

Xian-Qin Wang*, Do Heui Kim, Ja Hun Kwak, Chongmin Wang, Janos Szányi, Charles H.F.

Peden Institute for Interfacial Catalysis, Pacific Northwest National Laboratory, P.O. Box 999,

Richland, WA 99352 (USA) *[email protected]

Introduction

Lean NOx trap (LNT) catalysts composed of Pt/BaO-Al2O3 represent a viable approach to meet the stringent NOx emission standards being imposed on diesel engines [1]. However, poisoning of LNTs by SO2 represents a particularly challenging issue for this technology [1]; thus, it is important to develop more sulfur-durable LNT catalysts. As part of such an effort, we have been studying the effects of sulfation and desulfation on Pt accessibility and morphology changes in Pt/BaO-Al2O3 model catalysts. In this work, a series of Pt/BaO-Al2O3 catalysts with three different sulfation levels (non-sulfated, partially-sulfated, and fully-sulfated) were prepared. Pt accessibility after successive reductions in H2 at elevated temperatures was measured by an irreversible volumetric H2 chemisorption method. Moreover, the morphology of the sample after reduction at 800°C was characterized by HRTEM and XRD techniques.

Materials and Methods

Materials preparation. One typical LNT catalyst containing 1.5wt% Pt and 14 wt.% BaO was supplied by Johnson Matthey (Wayne, PA). This sample was calcined at 500°C, then sulfated with SO2 and O2 (1:1) at 300°C. We prepared the samples with the different sulfation levels by varying the sulfation process time. In this work, three different sulfation levels, zero sulfation (labeled as 0gS), partial sulfation (3gS) and complete sulfation (10gS), were investigated. Their platinum accessibility and morphology changes were studied as a function of reduction temperatures in order to decouple the thermal degradation from sulfur poisoning.

Characterization methods. Platinum accessibility was evaluated with the number of hydrogen atoms per Pt (H/Pt) determined from irreversible H2 chemisorption uptake measurements obtained after the sample was first reduced at varying temperatures. The morphologies of both the freshly sulfated samples and the samples after the chemisorption measurements at 800°C were characterized with high resolution TEM (HRTEM). The composition of the particles was analyzed by energy-dispersive X-ray spectroscopy (EDS). In order to understand the desulfation process, sulfur K absorption edge XAFS spectra were collected in-situ during the reduction of the catalysts in a flow of a 5% H2 and 95% He gas mixture (~40 mL/min) at beamline X19A, and Pt L3-edge EXAFS spectra were collected in air at room temperature at beamline X18B of the NSLS at BNL.

Results and Discussion

H/Pt values determined from H2 chemisorption experiments is a common way to measure the number of active sites and Pt accessibility for many supported Pt catalysts. Fig. 1 shows the H/Pt values obtained as a function of reduction temperature for the fresh (0gS), partially sulfated (3gS), and heavily sulfated (10gS) samples. We observed that Pt accessibility and

morphology changes have a complex dependence on the levels of sulfation. The H/Pt ratio decreased uniformly as a function of reduction temperature for the non-sulfated sample. Compared to this one, the partially-sulfated sample instead displayed an optimum H/Pt value at 500°C, and then a slight increase in Pt particle sizes after thermal aging at 800°C. Still different behavior was observed for the fully sulfated sample which gave very low H/Pt ratios for all reduction temperatures, indicating essentially complete poisoning by SO2.

1 2 3 40

10

20

30

40

50

10g/L S

FT m

agni

tude

of k

3 -wei

ghte

d EX

AFS

R / Å

Pt foil

Fresh

3g/L S

Pt-Oin PtO2

Pt-Oin PtSOx

Pt-Ptin PtSOx

1 2 3 40

10

20

30

40

50

10g/L S

FT m

agni

tude

of k

3 -wei

ghte

d EX

AFS

R / Å

Pt foil

Fresh

3g/L S

Pt-Oin PtO2

Pt-Oin PtSOx

Pt-Ptin PtSOx

300 400 500 600 700 8000.0

0.1

0.2

0.3

10 g sulfation

3 g sulfation

H/P

t

Temperature / oC

0 sulfation

300 400 500 600 700 8000.0

0.1

0.2

0.3

10 g sulfation

3 g sulfation

H/P

t

Temperature / oC

0 sulfation

Fig.1. Pt dispersion (H/Pt) as a function of Fig.2. Pt L3-edge EXAFS spectra for the reduction temperature in H2. variously sulfated catalysts and Pt foil. Fig.2 compares the Fourier transformed Pt L3-edge EXAFS spectra. The non-sulfated sample (0gS) primarily showed features similar to those of PtO2 [2], while the fully sulfated sample (10gS) had features matching Pt sulfate clusters [3]. The partially sulfated sample (3gS) seems to have a pattern similar to that of 0gS sample, but the relative intensities of the two main peaks was different. With a simple linear fitting of the spectrum from the 3gS sample using those for the non-sulfated and fully sulfated samples, we estimate that there was around 20% Pt in the Pt sulfate cluster form in this 3gS sample. The EXAFS results were consistent with the initial Pt accessibility measurements in Fig. 1 and provided information regarding the reduction mechanism of the sulfated Pt/BaO/Al2O3 LNT catalysts. Over partially sulfated sample, in particular, S spillover from Pt to Ba occurred gradually and H/Pt was a combined effect of PtS(PtSO4) reduction and Pt sintering. For the fully saturated sample, Pt sintering was facilitated by mobile PtS thereby slowing S spill over to Ba from PtS. Significance

This work shows that S levels in LNTs have a significant effect on Pt accessibility and morphology, and they can alter the reduction mechanism. The results aid in decoupling the effects of thermal degradation from sulfur poisoning for the deactivation of LNT samples. References 1. Epling, W. S.; Campbell, L. E.; Yezerets, A.; Currier, N. W.; Parks J. E.

Catal. Rev. Sci. Eng. 46, 163 (2004). 2. Shishido, T., Tanaka, T., Hattori, H., J. Catal. 172, 24 (1997). 3. Pley, M., Wickleder, M. S., Z. Anorg. Allg. Chem. 630, 1036 (2004).