The liquid phase reaction $A+BC$ is performed in a CSTR with $2$ stirrers. The stirring pattern of

the CSTR is such that the total reactor can be described as equal CSTRs in series with the amount of

tanks equal to the amount of stirrers. Reactants A and $B$ are fed through different tubes. The volume

of the total CSTR is equal to $620L$ and is initially fed with inert liquids. The inflow of both the

reactants to the CSTR are $3\mathrm{.}17\frac{L}{\text{m}\text{i}\text{n}}$ and $5\mathrm{.}74\frac{L}{\text{m}\text{i}\text{n}}$ for A and $B,$ respectively. The inlet concentrations

are equal to $C_A^0=C_B^0=2\mathrm{.}38\frac{\text{m}\text{o}\text{l}}{L}$ and the reaction rate constant is equal to $k=0\mathrm{.}082\frac{L}{\text{m}\text{o}\text{l}**(min)},$

i$.$e$.$ second order in A$.$

What is the stationairy conversion of $A$ in the CSTR in the situation described above?The liquid phase reaction A$+$B$->$C

is performed in a CSTR with $2$

stirrers. The stirring pattern of the CSTR is such that the total reactor can be described as equal CSTRs in series with the amount of tanks equal to the amount of stirrers. Reactants A and B are fed through different tubes. The volume of the total CSTR is equal to $620$

L

and is initially fed with inert liquids. The inflow of both the reactants to the CSTR are $3\mathrm{.}17$

Lmin

and $5\mathrm{.}74$

Lmin

for A and B$,$ respectively. The inlet concentrations are equal to C$0$A$=$C$0$B$=2\mathrm{.}38$

molL

and the reaction rate constant is equal to k$=0\mathrm{.}082$

Lmol$$min

$,$ i$.$e$.$ second order in A$.$

What is the stationairy conversion of A in the CSTR in the situation described above?