Collection of Czechoslovak Chemical Communications - digital archive 

Individual author index pages

• F. Kaštánek

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]
• F. Kaštánek
  The effect of the column diameter on the hydrodynamic parameters of bubble column with a plate as a gas distributor
  1977, Vol. 42, Issue 5, pp. 1494–1501 [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, 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]