(755d) Small Pore Zeolite SSZ-13 Supported Pd As Highly Stable Low-Temperature Methane Combustion Catalysts | AIChE

(755d) Small Pore Zeolite SSZ-13 Supported Pd As Highly Stable Low-Temperature Methane Combustion Catalysts

Authors 

Gao, F. - Presenter, Pacific Northwest National Laboratory
Cui, Y., Pacific Northwest National Laboratory
Peng, B., Pacific Northwest National Laboratory
Kovarik, L., Pacific Northwest National Laboratory
Wang, Y., Washington State University

Small pore zeolite
SSZ-13 supported Pd as highly stable low-temperature methane combustion
catalysts

Yanran Cui, Bo Peng, Libor Kovarik, Yong Wang, Feng Gao*

Institute
for Integrated Catalysis, Pacific Northwest
National Laboratory

Richland, WA 99352, USA

*Corresponding author: feng.gao@pnnl.gov

Abstract

The
low-temperature catalytic combustion of methane has been extensively studied
for reducing methane emissions from lean-burn natural gas engine exhausts. Pd
supported on Al2O3 has been known to be the most active,
and therefore, the most commonly used catalyst for this application [1].
However below ~450 ºC, water vapor in engine exhausts severely deactivates this
catalyst [2]. The deactivation has been attributed to transformation of the
active PdO phase, e.g., sintering or the formation of an inactive Pd(OH)2
phase, or hydroxyl group accumulation on the alumina supports [3, 4].   

In this work, hydrothermally
stable small pore SSZ-13 zeolites are used as the PdO support. Si/Al ratios of
the supports are systematically varied from 6 to 36 to manipulate support
hydrophobicity, which is found to play a decisive role in Pd dispersion. For a
hydrophilic support at Si/Al = 6, Pd largely presents as atomically dispersed
cations in zeolite exchange positions. By increasing Si/Al ratio to increase
support hydrophobicity, Pd progressively occupies zeolite external surfaces as
PdO particles. Pd/SSZ-13 catalysts with Si/Al = 6 and 12 still suffer from
water-induced deactivation, the same as the Pd/Al2O3
reference catalyst studied here; at Si/Al ratios of 24 and 36, however, the
Pd/SSZ-13 catalysts become much more stable than Pd/Al2O3
in the presence of water vapor. To obtain insights into the stability
improvement of these latter Pd/SSZ-13 catalysts, detailed low-temperature methane
combustion kinetics are conducted. For Pd/Al2O3, the powder-law
dependence on H2O partial pressure is found at -1, fully consistent
with the inhibiting role of water vapor. For the Pd/SSZ-13 catalysts (Si/Al =
24 and 36), the ~0 powder-law dependence on H2O pressure explains
their improved stability. It is concluded that hydrophobicity of the support
plays a key role in promoting the stability and activity of methane combustion
catalysts.

References:

[1]
Gélin, P., Primet, M., Appl. Catal. B:
Environ.
39: 1-37, 2002

[2]
Mihai, O., Smedler, G., Nylén, U., Olofsson, M., Olsson, L., Catal. Sci. Technol. 7: 3084-3096, 2017

[3]
Roth, D., Gélin, P., Primet, M., Tena, E., Appl.
Catal. A: General 203: 37-45, 2000

[4] Schwartz, W. R., Ciuparu, D.,
Pfefferle, L. D., J. Phys. Chem. C 116: 8587-8593, 2012

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