Question $1$

$0pts$

Consider an ideal CSTR with two inlets and one outlet.

Component $A$ is fed into inlet stream $1$ and component $B$ is fed into inlet stream $2$

The rate of reaction of species $A$ is as follows: $r_{rxn,A}=k_0{c}_A^{0\mathrm{.}5}{c}_B^{1\mathrm{.}5},$ where $k_0=0\mathrm{.}53\frac{L}{g}$mol$*s$

The reactor has the following characteristics:

The system is at a constant density of $1\mathrm{.}18\frac{g}{c}{m}^3$

The volumetric flowrate of stream $1$ is $8\mathrm{.}7\frac{L}{s}$

The mass flowrate of the outlet stream is $65\mathrm{.}8k\frac{g}{s}$

The entering concentration of $A$ is $1\mathrm{.}9$gmo$\frac{l}{L}$

The entering concentration of $B$ is $3\mathrm{.}6$gmo$\frac{l}{L}$

The conversion of species $A$ is $0\mathrm{.}6,$ while the conversion of species $B$ is $0\mathrm{.}53$

What is the required reactor volume in units of liters?