Abstract

The ability to use molecular hydrogen, H2, as a buffer gas in spin exchange optical pumping of noble gases enables the production of hydrogen gas containing a low percentile (5%) of hyperpolarized (HP) 129Xe as a tracer for in situ NMR spectroscopy of hydrogenation reactions. It is demonstrated that the xenon chemical shift, observed in the porous space of Pt-containing alumina pellets, can be used to monitor the temperature changes under rapidly progressing, nonsteady-state conditions during start-up of the catalytic reaction. Standard proton MR imaging was successfully applied to provide in situ evaluation of conversion for the catalyst used in this work.

Highlights

  • The vast majority of contemporary, industrially relevant, chemical processes are catalytic, and heterogeneous catalytic reactions are of particular interest.[1]

  • Even the methods that are based on direct magnetic resonance measurements of the reactants and products may impose certain restrictions on the experimental design; for instance, the use of nuclear magnetic resonance spectroscopy (NMR) line width for temperature evaluation precludes the use of a frequency encoding gradient for magnetic resonance imaging (MRI).[16]

  • The hyperpolarization methods are of particular interest including spin-exchange optical pumping (SEOP)[25] and parahydrogen-induced polarization (PHIP),[26,27] which provide a significant increase in NMR signals intensity, by up to several orders of magnitude

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Summary

ACS Catalysis

Letter exacerbated by magnetic field inhomogeneity at the surface of solid catalysts beads and within the entire catalytic reactor.[4]. The temperature dependence of the 129Xe chemical shift and the capability to generate HP 129Xe through SEOP of a 0.05:0.95 Xe:H2 gas mixture was utilized to observe a catalytic reaction during start-up with time-resolved 129Xe NMR spectroscopy (using 99% isotopically enriched 129Xe). Taking into account the temperature dependence of xenon chemical shift obtained in the calibration experiments, the average temperature inside the catalytic reactor was about 106 °C within 30 s after the start of the reaction and increased to about 200 °C within 70 s. MR images with selective suppression of 1H signals from either propane or propene during propene hydrogenation with normal hydrogen over the 1 wt % Pt/Al2O3 catalyst pellet placed at the bottom of a 5 mm NMR tube were acquired (Figure 2).

■ ACKNOWLEDGMENTS
■ REFERENCES
Behaviour and Oligomer Accumulation within Catalyst Pores during
Findings
Situ Analysis of Gas Phase Reaction Processes within Monolithic
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