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Debye Institute for Nanomaterials Science

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42<br />

Inorganic Chemistry and Catalysis<br />

Development of a hydrothermal stable non-noble metal catalyst <strong>for</strong><br />

Aqueous Phase Re<strong>for</strong>ming<br />

Tomas van Haasterecht, T.vanHaasterecht@uu.nl, phone: 06 - 22736372<br />

Sponsor: Catchbio, since January 2009<br />

Supervisors: Prof. dr. ir. Krijn P. de Jong and dr. Johannes H. Bitter<br />

H 2 -Chemisorption, HPLC/RID, GC/TCD, AAS<br />

Aqueous phase re<strong>for</strong>ming (APR) of renewable carbohydrates is an attractive process <strong>for</strong> the<br />

sustainable and economical production of H . The generated H can be used <strong>for</strong> efficient power<br />

2 2<br />

generation in a PEM fuel cell. Using APR with microreactor technology and an integrated fuel<br />

cell, we aim <strong>for</strong> the development of a compact power producing unit <strong>for</strong> portable applications, this<br />

part of the project is in collaboration with the TUE.<br />

In the APR process biomass derived oxygenated hydrocarbons are converted into, preferably H2 and CO , around 500 K using heterogeneous metal catalysts.<br />

2<br />

So far the process has been most successful using expensive platinum based catalyst and glycols as<br />

feedstock. [1] This research focuses on the development of a stable, non noble metal catalyst <strong>for</strong> the<br />

efficient and selective production of H from various biomass feeds. The most promising catalyst<br />

2<br />

can be integrated in the microreactor system at the TUE to demonstrate the applicability.<br />

We have investigate the possibility of using Carbon Nanofiber (CNF) supported Co, Ni and Cu<br />

catalysts with a focus on their hydrothermal stability. These catalysts, and a commercial 5%Pt/Al O 2 3<br />

catalyst, were tested in a batch reactor <strong>for</strong> the APR of a 1% Ethylene Glycol (EG) solution. The<br />

resulting conversion profiles are shown in Fig. 1. The highest conversion was achieved with the<br />

Ni/CNF catalyst while the Cu/CNF is almost inactive. The initial activity in terms of TOFi,EG<br />

is highest <strong>for</strong> the Co/CNF catalyst, however after an initial period of high activity the Co/CNF<br />

catalyst appears to deactivate.<br />

Indeed XRD analysis of the spent catalysts shows that Co/CNF is subject to sintering and oxidation.<br />

The Ni, Cu and Pt catalysts remain metallic, but sintering also occurs <strong>for</strong> the Ni/CNF catalyst.<br />

Furthermore, the amount of leached metal, detected in the liquid phase after the reaction, was<br />

significantly higher <strong>for</strong> the Co/CNF catalyst compared to other catalysts. Based on these result the<br />

Ni/CNF is the most promising alternative to platinum based catalyst in terms of activity and stability.<br />

Figure 1: EG conversion as function of time.<br />

[1] Appl. Catal. B. 56, 2005, 171.

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