Hostname: page-component-78c5997874-dh8gc Total loading time: 0 Render date: 2024-11-16T20:15:54.696Z Has data issue: false hasContentIssue false

Sintering of Pd Automotive Catalysts

Published online by Cambridge University Press:  02 July 2020

Q. Xu
Affiliation:
University of New Mexico, Department of Chemical and Nuclear Engineering, Albuquerque, NM, 87131, USA
K.C.C. Kharas
Affiliation:
Delphi-ASEC Environmental Catalysts, Tulsa, OK, 74015, USA
A.K. Datye
Affiliation:
University of New Mexico, Department of Chemical and Nuclear Engineering, Albuquerque, NM, 87131, USA
Get access

Abstract

The focus of this work is on processes that lead to loss of active metal surface area during high temperature operation of automotive catalysts. As under-floor catalytic converters are moved closer to the engine to achieve faster light off, the catalyst is subjected to higher operating temperatures during the normal driving cycle. Sintering of the active metal phase leading to loss of surface area represents one of the most important factors limiting the long-term durability of automotive catalysts. Despite its obvious technological importance, fundamental understanding of sintering is still lacking.

In this research, we have prepared a series of Pd metal catalysts on a θ alumina support. The metal loading was varied from 1.1 wt% to 7 wt%. The catalysts were subjected to sintering at 900 °C for up to 192 hours. To ensure relevance to automotive catalysts, the sintering was performed in a gas atmosphere that contained 10 mol % H2O in flowing N2 or in air.

Type
Characterization of Catalysts (Organized by S. Bradley)
Copyright
Copyright © Microscopy Society of America 2001

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

1. Granqvist, C.G. and Buhrman, R.A., Size Distributions of Supported Metal Catalysts: Coalescence Growth versus Ostwald Ripening. J. Catal., 1976. 42: p. 477479.Google Scholar

2. Financial Support from the National Science Foundation, GOALI program grant number CTS 99- 11174 and from Delphi-ASEC Environmental CatalystsGoogle Scholar