A particular bioreactor is described by a

Levenspiel plot shown in the figure. Estimate the

volume of a CSTR reactor fed with a rate of $1$kg$/$h

and substrate concentration Cs$0=0\mathrm{.}25$ g$/$dm$3$ that is

required to achieve conversion of $80\%.$ Assume

the density of the solution $1$kg$/$dm$3.$ Suggest a

combination of CSTR and PFR reactors to achieve

the same conversion with the minimal volume.

Estimate the volume required in this case.A particular bioreactor is described by a

Levenspiel plot shown in the figure. Estimate the

volume of a CSTR reactor fed with a rate of $1k\frac{g}{h}$

and substrate concentration $C_{s0}=0\mathrm{.}25\frac{g}{d}{m}^3$ that is

required to achieve conversion of $80\%.$ Assume

the density of the solution $1k\frac{g}{d}{m}^3.$ Suggest a

combination of CSTR and PFR reactors to achieve

the same conversion with the minimal volume.

Estimate the volume required in this case.