Chemical Reaction Engineering
In an ideal tubular-flow reactor

There is no mixing in longitudinal direction
All of these
Mixing takes place in radial direction
There is a uniform velocity across the radius

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Chemical Reaction Engineering
In solid catalysed reactions the diffusional effects are more likely to affect the overall rate of reaction for

Fast reactions in catalyst of small pore diameter
Fast reaction in catalyst of large pore diameter
Slow reactions in catalyst of large pore diameter
Slow reactions in catalyst of small pore diameter

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