The effect of pressure and temperature on the axial dispersion of gas was e
xamined in a fluidized bed of 10 cm I.D. x 100 cm, height. The employed par
ticle was zinc titanate catalyst and particle size was 150,um. The stimulus
-response method was employed in order to determine the axial dispersion co
efficient of gas in a bubbling fluidized bed. The hydrogen was used as the
trace gas. The experimental results showed that the increase of pressure an
d temperature did not significantly change the axial dispersion coefficient
in spite of significant increase of minimum fluidization velocity.