Collect. Czech. Chem. Commun. 1977, 42, 1494-1501

The effect of the column diameter on the hydrodynamic parameters of bubble column with a plate as a gas distributor

F. Kaštánek

Individual author index pages

Other CCCC articles of these authors

  • F. Kaštánek, J. Kratochvíl and M. Rylek
    Mass transfer in bubble-type reactors without mechanical mixing
    1977, Vol. 42, Issue 12, pp. 3549–3554 [Abstract]
  • J. Pata, F. Kaštánek, J. Kratochvíl and M. Rylek
    Interfacial area, mass transfer coefficient and porosity in aqueous solutions of ammonia reacting with carbon dioxide
    1977, Vol. 42, Issue 9, pp. 2651–2665 [Abstract]
  • F. Kaštánek, J. Kratochvíl, J. Pata and M. Rylek
    Gas holdup in bubbled beds of aqueous solutions of electrolytes
    1977, Vol. 42, Issue 9, pp. 2642–2650 [Abstract]
  • F. Kaštánek
    The volume mass transfer coefficient in a bubble bed column
    1977, Vol. 42, Issue 8, pp. 2491–2497 [Abstract]
  • J. Čermák and F. Kaštánek
    Dynamic behaviour of bubbled beds on perforated plates of column reactors characteristic pressure fluctuations
    1977, Vol. 42, Issue 4, pp. 1325–1331 [Abstract]
  • F. Kaštánek
    The relation between interfacial area and the rate of energy dissipation in bubble column
    1976, Vol. 41, Issue 12, pp. 3709–3714 [Abstract]
  • F. Kaštánek, M. Rylek and J. Kratochvíl
    Pressure drop of perforated plates at parallel upward two-phase flow for the water-air system
    1976, Vol. 41, Issue 7, pp. 2010–2014 [Abstract]
  • V. Rod and F. Kaštánek
    Calculation of simultaneous absorption of two gases reacting with the absorbent
    1976, Vol. 41, Issue 5, pp. 1302–1309 [Abstract]
  • M. Rylek, F. Kaštánek, L. Nývlt and J. Kratochvíl
    Free area for gas flow through sieve plates with a bubbled bed
    1975, Vol. 40, Issue 11, pp. 3315–3318 [Abstract]
  • M. Řeháková and F. Kaštánek
    The pressure drop of perforated plates of extremely low free area and opening diameter
    1975, Vol. 40, Issue 8, pp. 2419–2423 [Abstract]
  • V. Nývlt and F. Kaštánek
    Measurement of interfacial area in bubble columns by the sulphite method
    1975, Vol. 40, Issue 6, pp. 1853–1861 [Abstract]
  • F. Kaštánek
    Gas-liquid mass transfer with chemical reaction in both phases
    1975, Vol. 40, Issue 4, pp. 971–976 [Abstract]
  • F. Kaštánek, M. Rylek and J. Nývlt
    Scaling-up of bubble-type reactors and the effect of reactor size on gas holdup in water-air systems
    1974, Vol. 39, Issue 11, pp. 3246–3255 [Abstract]
  • F. Kaštánek and V. Nývlt
    Interfacial area in bubble type plate reactor
    1974, Vol. 39, Issue 11, pp. 3068–3075 [Abstract]
  • F. Kaštánek, J. Zahradník and M. Rylek
    Back flow between stages in bubble-type reactors
    1974, Vol. 39, Issue 7, pp. 1672–1685 [Abstract]
  • J. Zahradník and F. Kaštánek
    The effect of plates on some parameters of a heterogeneous bed in bubble-type flow reactors
    1974, Vol. 39, Issue 6, pp. 1419–1425 [Abstract]
  • J. Zahradník, F. Kaštánek and M. Rylek
    Porosity of the heterogeneous bed and liquid circulation in multistage bubble-type column reactors
    1974, Vol. 39, Issue 6, pp. 1403–1418 [Abstract]
  • F. Kaštánek, V. Nývlt and M. Rylek
    Gas holdup and its relation to interfacial area in bubble-type reactors
    1974, Vol. 39, Issue 2, pp. 528–538 [Abstract]
  • F. Kaštánek and J. Zahradník
    Gas-liquid reactors. I. The residence time distribution in multistage bubble reactors
    1973, Vol. 38, Issue 12, pp. 3725–3741 [Abstract]
  • M. Rylek, F. Kaštánek, V. Braun and R. Audy
    Lower critical gas and liquid velocities of grid trays
    1973, Vol. 38, Issue 1, pp. 181–184 [Abstract]
  • M. Rylek and F. Kaštánek
    Pressure drop of foam bed on grid trays
    1972, Vol. 37, Issue 1, pp. 254–262 [Abstract]
  • F. Kaštánek and M. Rylek
    Turbogrid tray efficiencies
    1970, Vol. 35, Issue 11, pp. 3367–3378 [Abstract]
  • F. Kaštánek
    Efficiencies of different types of distillation plates
    1970, Vol. 35, Issue 4, pp. 1170–1187 [Abstract]
  • F. Kaštánek and Z. Novosad
    Multistage column reactors. VI. General model of liquid residence time distribution in a column with plates
    1968, Vol. 33, Issue 12, pp. 3946–3959 [Abstract]