A second order, elementary reaction $2AB$ occurs in a liquid phase CSTR$,$ with the reaction rate constant $k=0\mathrm{.}13L*mo{l}^{-1}.s^{-1}.$ The feed concentration of $A,C_A^0,$ is $0\mathrm{.}52$mol.$L^{-1}{?}^{-1},$ the feed flowrate is $20L.S^{-1}$ and a conversion of $39\%$ is achieved. $($Give all answers to $4$ significant figures until the final answer$).$

What is the molar flowrate of $A$ in the reactor feed?

$mo\frac{l}{s}$

What is the molar flowrate of $A$ in the reactor outlet?

$mo\frac{l}{s}$

What is the concentration of $A$ in the reactor outlet?

$mo\frac{l}{L}$

Calculate the rate of reaction of $A$ in the CSTR$.$

mol. $L^{-1}*s^{-1}$

What is the required reactor volume?

L

Give the final reactor volume, taking into account the significant figures:

L

If a second CSTR is added in series so that the overall conversion is $59\%$ :

What is the concentration of $A$ at the exit of the second reactor? $($Give all answers to $4$ significant figures until the final answer$).$

$mo\frac{l}{L}$

Calculate the rate of reaction of $A$ in the second CSTR$.$

mol.$L^{-1}*s^{-1}$

Calculate the rate of reaction of $A$ in the CSTR$.$

mol.$L^{-1}*s^{-1}$

What is the required reactor volume?

L

Give the final reactor volume, taking into account the significant figures:

L

If a second CSTR is added in series so that the overall conversion is $59\%$ :

What is the concentration of $A$ at the exit of the second reactor?

$($Give all answers to $4$ significant figures until the final answer$).$

$mo\frac{l}{L}$

Calculate the rate of reaction of $A$ in the second CSTR$.$

mol$*L^{-1}*s^{-1}$

Calculate the concentration of $B$ at the exit of the second reactor.

$mo\frac{l}{L}$

Calculate the reactor volume of the second reactor.

L

Give the final volume for the second reactor, taking into account the significant figures:

L