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Rice University

Alumina-supported palladium and palladium/copper catalysts: Characterization and use for selective hydrogenation of 1,3-butadiene

Abstract

dc:description.abstract

Butadiene is a normal deleterious contaminant that must be removed from C$\sb4$-olefin streams before being used in several industrial applications. While this impurity is substantially eliminated by selective catalytic hydrogenation, there is a considerable economic incentive to improve the currently employed palladium-based catalysts. The purpose of this research has been to investigate the effects of adding copper to alumina-supported palladium to enhance the selectivity of palladium for butadiene hydrogenation. 1,3-Butadiene semi-hydrogenation was studied in the presence of a 10:1 excess of 1-butene over supported bimetallic catalysts containing palladium in a vapor-phase atmospheric plug flow reactor in the temperature range 299-313 K. Copper addition to alumina-supported Pd increases its selectivity for converting butadiene to n-butenes without saturating or isomerizing the n-butenes. For example, with a Cu/Pd atomic ratio of two, the bimetallic catalyst selectively converts $>$99% of the diene to n-butenes while isomerizing or saturating less than 1% of the starting 1-butene. Under similar conditions, Pd alone maintains high n-butene selectivity to only about 50% conversion of the diene. Copper also promotes higher trans-2-butene selectivity at the expense of 1-butene production. The kinetics of 1,3-butadiene hydrogenation over the Pd and PdCu catalysts are first order in hydrogen and zero order in butadiene. Hydrogen sorption measurements show that copper addition decreases both surface adsorption and bulk absorption, suggesting surface decoration of Pd by Cu and possibly bulk Cu-Pd interactions in the supported bimetallic samples. Surface Cu-Pd mixing is confirmed by X-ray photoelectron spectroscopy (XPS) measurements. Extended X-ray absorption fine-structure (EXAFS) results reveal that oxidation of bulk palladium particles is slowed by the presence of copper. Probably copper surface mixing and/or decoration protects bulk palladium particles by suppressing oxygen diffusion. Combined, the results indicate that the bimetallic particles are present as bulk palladium particles with Cu-Pd mixing at the surface. These bimetallic catalysts containing Cu and Pd show promise for commercial use since they are considerably more selective than Pd-alone.

Degree

thesis:*
Name thesis:degree_name
Doctor of Philosophy
Level thesis:degree_level
Doctoral
Discipline thesis:degree_discipline
Engineering
Grantor
Rice University
Year dc:date.issued
1996

Author and committee

dc:creator, dc:contributor.*
Author dc:creator
  • Furlong, Brian Keith
Advisor dc:contributor.advisor
  • Hightower, Joe W.

Subjects

dc:subject × 4

Rights

dc:rights
Statement dc:rights
  • Copyright is held by the author, unless otherwise indicated. Permission to reuse, publish, or reproduce the work beyond the bounds of fair use or other exemptions to copyright law must be obtained from the copyright holder.
Language dc:language.iso
eng

Identifiers

dc:identifier.*
Handle dc:identifier.uri
https://hdl.handle.net/1911/16916
OAI identifier oai:identifier
oai:repository.rice.edu:1911/16916

Chain of custody

source
Harvested from
Rice University
Base URL
repository.rice.edu/server/oai/request
Last updated
2026-07-24
Source record
OAI-PMH GetRecord
citation

Furlong, Brian Keith. Alumina-supported palladium and palladium/copper catalysts: Characterization and use for selective hydrogenation of 1,3-butadiene. Doctoral thesis, Rice University, 1996. https://hdl.handle.net/1911/16916