Chemical Reaction Engineering
The energy balance equation over a tubular reactor under transient conditions is

A non-linear partial differential equation
An algebric differential equation
An ordinary non-linear differential equation
A linear partial differential equation

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Chemical Reaction Engineering
Semibatch reactor is preferred, when a/an

A highly exothermic reaction is to be controlled
A gas is to be reacted with liquid (e.g. hydrogenation of fat)
Undersirable side reaction (at high concentration of one of the reactants) is to be avoided
All of these

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