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Obtaining ethylene from ethane usually involves a thermal
cracking unit
which is a plug flow reactor.
The ethane enters the PFR where a furnace is used to hear the ethane to a
very high temperature which causes the ethane to react. The reactions are
as follows:
where
The material balance can be written as
Accumulation = Flow in - Flow out + Generation
A mole balance can be written for a cross-section of the tubular plug flow
reactor and the following differential equations are derived
Since the reaction is taking place while being heated by a furnace, the
isothermal assumption is no longer valid. Allowing the moles and
temperature to change and using the heat transfer relationship
the final equations for calculation are
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