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The gas–liquid contacting effects on liquid dispersion in pilot scale upflow hydrotreaters

  • Published:2004-04 Issue:7 Volume:59 Page:1415-1422
  • ISSN:0009-2509
  • Container-title:Chemical Engineering Science
  • language:en
  • Short-container-title:Chemical Engineering Science

Author:

Bellos G.D.,Gotsis K.P.,Galtier P.A.,Papayannakos N.G.

Publisher

Elsevier BV

Subject

Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference19 articles.

1. Gas–liquid mass transfer coefficients for cocurrent upflow in packed beds-effect of packing shape at low flow rates;Alexander;Canadian Journal of Chemical Engineering,1976

2. Volumetric oxygen mass transfer coefficient in an upflow cocurrent packed-bed bioreactor;Deront;Chemical Engineering Science,1998

3. Kinetic modeling and reactor simulation in hydrodesulfurization of oil fractions;Froment;Industrial Engineering Chemical Research,1994

4. Trickle-bed reactor models for systems with a volatile liquid-phase;Khadilkar;Chemical Engineering Science,1999

5. Effects of liquid evaporation on the performance of trickle-bed reactors;Kocis;Chemical Engineering Research and Design,1986

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