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Reduction of nitric oxide by carbon monoxide and hdyrogen over a silica-supported rhodium catalyst

Thesis/Dissertation ·
OSTI ID:6917249

The mechanism and kinetics of NO reduction by CO, by H/sub 2/, and by mixtures of CO and H/sub 2/ over a Rh/silica catalyst were studied in detail. Experiments were carried out in a specially designed microreactor which doubled as an infrared cell. Gas phase compositions were measured by a unique GC system which permited accurate determination of NH/sub 3/, NO, N/sub 2/O, N/sub 2/, CO, and CO/sub 2/. Power law parameters and apparent activation energies characteristic of the rate of NO depletion and the rates of N/sub 2/O, N/sub 2/, and NH/sub 3/ formation were determined for each of the three reaction systems. Langmuir-Hinshelwood models were proposed to describe NO reduction by CO and NO reduction by H/sub 2/ and were shown to be consistent with both the infrared and the rate measurements. During NO reduction by CO, the rates of NO, N/sub 2/O, and N/sub 2/ exhibited slight positive-order dependencies on P/sub CO/, negative-order dependencies on P/sub NO/, and activation energies of 34 Kcal/mole. During NO reduction by H/sub 2/, the rates of NO, N/sub 2/O, N/sub 2/, and NH/sub 3/ exhibited strong positive-order dependencies on P/sub H/sub 2//, moderate negative-order dependencies on P/sub NO/, and activation energies of 22-27 Kcal/mole. The catalyst surface was again dominated by Rh-NO/sup delta/-under low and moderate NO conversion conditions. Strong effects of catalyst pretreatment on reaction rates, product selectivity, and infrared spectra were seen. Preoxidation (with 1-2% NO) gave greater activity, greater selectivity to N/sub 2/, and higher frequency IR bands for adsorbed NO than prereduction. A proposal that preoxidized Rh is more electropositive than the prereduced Rh is shown to be consistent with all of these observations.

OSTI ID:
6917249
Country of Publication:
United States
Language:
English