Mass Transport Effects on the Kinetics of Nitrobenzene Reduction by Iron Metal

Michelle M. Scherer,* Kathleen M. Johnson, John C. Westall, and Paul G. Tratnyek§
Department of Civil and Environmental Engineering, University of Iowa, Iowa City, Iowa 52242-1527, Department of Chemistry, Oregon State University, 153 Gilbert Hall, Corvallis, Oregon 97331-4003, and Department of Environmental Science and Engineering, Oregon Graduate Institute of Science & Technology, 20000 NW Walker Road, Beaverton, Oregon 97006-8921
Environ. Sci. Technol., 2001, 35 (13), pp 2804–2811
DOI: 10.1021/es0016856
Publication Date (Web): May 25, 2001
Copyright © 2001 American Chemical Society

Abstract

To evaluate the importance of external mass transport on the overall rates of contaminant reduction by iron metal (Fe0), we have compared measured rates of surface reaction for nitrobenzene (ArNO2) to estimated rates of external mass transport in a permeable reactive barrier (PRB). The rate of surface reaction was measured at a polished Fe0 rotating disk electrode (RDE) in an electrochemical cell, and the rate of mass transport was estimated from a correlation for mass transport in packed-bed reactors. The kinetics of ArNO2 reduction were studied in pH 8.4 borate buffer at a potential below which an oxide film would form. The cathodic current measured in this system was dependent on the electrode rotation rate, and the measured first-order heterogeneous rate coefficient for surface reaction [krxn = (1.7 ± 0.2) × 10-3 cm s-1] was about 10 times faster than the first-order mass transport rate coefficient (kmt ≈ 2 × 10-4 cm s-1) estimated for PRBs. The similarity between rates of surface reaction and mass transport suggest that it may be important to consider mass transport processes in the design of PRBs for contaminants such as nitroaromatics that are highly reactive with Fe0.

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History

  • Published In Issue July 01, 2001
  • Received for review September 20, 2000
    Revised manuscript received April 6, 2001
    Accepted April 6, 2001

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