The figure enclosed here shows the kinetic data for a particular liquid$-$phase reaction. The feed stream

has CAO $=7$ moVL, and $8500$ fractional conversion is desired. The feed stream needs to be processed at a

volumetric flowrate $($Vo$)$ of $1000$ L$/$min$.$ Obtain the required volume $($V$)$ and the order of arrangement $($if

more than one reactor$)$ for the following configurations:

a$)$ Single

b$)$ Single CSTR

c$)$ Best combination of PFR$/$CSTR in series

Hint: You don't need to transform the graph below to the Levenspiel plot. What are possible design

equations of PFR and CSTRs that you can use to determine volume? Are the any of those equations that

resemble the graph below?