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Chemical Reaction Engineering

Chemical Reaction Engineering
Fluid flow in a real packed bed can be approximated as __________ model.

Plug flow
Mixed flow
Tank in series
Dispersion

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Chemical Reaction Engineering
The molecularity and the order of reaction respectively, for the hydrolysis of methyl acetate in presence of acids are

11 & 2
2 && 2
2 & 1
1 & 1

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Chemical Reaction Engineering
A batch reactor suffers from following disadvantage.

Poor product quality control
High labour and handling cost
High shutdown time requirement for emptying, cleaning and refilling
All of these

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Chemical Reaction Engineering
Half life period of a first order irreversible reaction A → B is

K/2
Ln 0.5/k
Ln k/2
Ln 2/k

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Chemical Reaction Engineering
Which of the following chemical reactions will be favoured by low pressure ?

N₂ + O₂ ⇋ 2NO
2HI ⇋ H₂ + I₂
N₂O₂ ⇋ 2NO₂
None of these

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Chemical Reaction Engineering
The ratio of volume of mixed reactor to the volume of P.F.R. (for identical flow rate, feed composition and conversion) for zero order reaction is

1
∞
> 1

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