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Heat and Mass Transfer and Kinetic Processes Modeling in a Methane Steam Conversion Facility

[+] Author Affiliations
Gustavo A. Restrepo, Andrey N. Krylov, Eduard D. Sergievskiy

Moscow Power Engineering Institute (Technical University), Moscow, Russia

Paper No. HT2009-88425, pp. 125-129; 5 pages
doi:10.1115/HT2009-88425
From:
  • ASME 2009 Heat Transfer Summer Conference collocated with the InterPACK09 and 3rd Energy Sustainability Conferences
  • Volume 3: Combustion, Fire and Reacting Flow; Heat Transfer in Multiphase Systems; Heat Transfer in Transport Phenomena in Manufacturing and Materials Processing; Heat and Mass Transfer in Biotechnology; Low Temperature Heat Transfer; Environmental Heat Transfer; Heat Transfer Education; Visualization of Heat Transfer
  • San Francisco, California, USA, July 19–23, 2009
  • Conference Sponsors: Heat Transfer Division
  • ISBN: 978-0-7918-4358-1 | eISBN: 978-0-7918-3851-8
  • Copyright © 2009 by ASME

abstract

This paper deals with one of the most interesting methods of lowering heat losses: thermochemical recuperation (TCR) of waste heat present in high-temperature flue gases via methane steam reforming. An earlier proposed process flow diagram for TCR in a glass production facility was revised and a mathematical model was developed to predict the heat and mass transfer phenomena that take place in the catalytic chemical reactor included in that process. Comparison of data obtained by the new proposed model and published data confirmed the feasibility of using it in the investigation and synthesis of TCR processes. Obtained results also permit to find optimal temperature profile in order to increase the hydrogen rate formation.

Copyright © 2009 by ASME

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