One reaction engineer indicated that he believes the Engineering Equation for the Batch reactor is given...
One reaction engineer indicated that he believes the Engineering
Equation for the Batch reactor is given (at the microscopic level)
by the classical dC/dt= R (C, T) since, he says, after all the
reactor does not show fluxes across the boundaries: Do you agree
with this engineer? Why?
B
Homework Answers
No.
The above equation for is valid for only constant volume systems. It cannot be applied for variable volume systems where is change in number of moles.
A more general equation as given below has to be adapted in such conditions:
Add Answer to:
One reaction engineer indicated that he believes the Engineering
Equation for the Batch reactor is given...
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