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Results: 757
Number of items: 757
  • Letzel, H. M., Schouten, J. C., van den Bleek, C. M., & Krishna, R. (1999). Gas holdup and mass transfer in bubble column reactors operated at elevated pressure. Chemical Engineering Science, 54, 2237-2246. https://doi.org/10.1016/S0009-2509(98)00418-7
  • Maretto, C., & Krishna, R. (1999). Modelling of a bubble column slurry reactor for Fischer Tropsch synthesis. Catalysis Today, 52, 279-289. https://doi.org/10.1016/S0920-5861(99)00082-6
  • Baur, R., Taylor, R., Krishna, R., & Copati, J. A. (1999). Influence of mass transfer in distillation of mixtures with a distillation boundary. Transactions of the Institution of Chemical Engineers. Part A: Chemical engineering research & design, 77, 561-565. https://doi.org/10.1205/026387699526467
  • van Wachem, B. G. M., Schouten, J. C., Krishna, R., & van den Bleek, C. M. (1999). Validation of the Eulerian simulated dynamic behaviour of gas-solid fluidised beds. Chemical Engineering Science, 54, 2141-2149. https://doi.org/10.1016/S0009-2509(98)00303-0
  • Ellenberger, J., & Krishna, R. (1999). Counter-current operation of structured catalytically packed distillation columns: pressure drop, holdup and mixing. Chemical Engineering Science, 54, 1339-1345. https://doi.org/10.1016/S0009-2509(99)00055-X
  • Higler, A., Taylor, R., & Krishna, R. (1999). The influence of mass transfer and liquid mixing on the performance of reactive distillation tray column. Chemical Engineering Science, 54, 2873-2881. https://doi.org/10.1016/S0009-2509(98)00317-0
  • Higler, A., Krishna, R., Ellenberger, J., & Taylor, R. (1999). Counter-current operation of a structured catalytically packed bed reactor: liquid phase mixing and mass transfer. Chemical Engineering Science, 54, 5145-5152. https://doi.org/10.1016/S0009-2509(99)00229-8
  • Higler, A., Krishna, R., & Taylor, R. (1999). A non-equilibrium cell model for packed distillation columns. The influence of maldistribution. Industrial & Engineering Chemistry Research, 38, 3988-3999. https://doi.org/10.1021/ie990261l
  • Higler, A., Krishna, R., & Taylor, R. (1999). Non-equilibrium cell model for multicomponent (reactive) separation processes. AIChE Journal, 45, 2357-2370. https://doi.org/10.1002/aic.690451111
  • Higler, A., Taylor, R., & Krishna, R. (1999). Nonequilibrium modelling of reactive distillation: multiple steady states in MTBE synthesis. Chemical Engineering Science, 54, 1389-1395. https://doi.org/10.1016/S0009-2509(99)00056-1
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