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Thomas W. Chapman

Thomas W. Chapman

Thomas W. Chapman
Professor Emeritus

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    1008 Engineering Hall
    1415 Engineering Drive
    Madison, WI 53706
    Tel: 202/265-8165
    Fax: 608/262-5434

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    Summary

    Our research program focuses on a variety of chemical processes in which interactions between specific chemistry and transport effects introduce some challenging problems in equipment design and operation. The processes of interest generally involve electrochemical systems or multi-phase reactors. Our approach is to seek a quantitative description of a particular process chemistry and incorporate its specific features in a reactor model suitable for design or simulation.

    Much of our work is in the area of electrochemical reaction engineering. The analysis of electrochemical reactors involves consideration of all the phenomena important in conventional catalytic reactors. In addition, one must consider the effects of potential on electrode reaction kinetics and on ionic transport. As a result, reactor modelling requires characterization of potential and current distributions as well as the distributions of concentrations and temperature. Nonlinear interactions between transport processes and reaction kinetics give rise to some unique and challenging problems.

    Active projects in this area include developing an electrochemical process for producing acrylic acid or butanediol from ethylene, characterizing the manganese dioxide cathode in alkaline cells, fabricating micromechanical components by electrodeposition, and using packed-bed electrodes to destroy toxic chemicals in wastewater. Each of these projects involves measurements of reaction kinetics and their subsequent use for electrochemical reactor design and optimization.

    One growing area of research activity in biomass utilization is based on a collaboration with the U.S. Department of Agriculture Forest Products Laboratory, located in Madison. We are working on chemical pulping processes and the production of chemicals from wood.

    Earlier projects have involved kinetics, mass transfer and reactor modelling studies related to the production of xylose and acetic acid from hemicellulose by dilute-acid hydrolysis and to the fermentation of xylose to ethanol. Electrochemical conversion of biomass feedstocks




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