Problem statement Chemical reactor engineering $-$ retake

Deadline $05/07/2024$

Problem $1$

Calculate the reactor volumes for each configuration shown below for the reaction data in the table when the molar flow rate is $52mo\frac{l}{m}in.-$ra is in terms of $mo\frac{l}{d}{m}^3*s$

$\backslash$table$[[x_A,0,0\mathrm{.}1,0\mathrm{.}2,0\mathrm{.}3,0\mathrm{.}4,0\mathrm{.}5,0\mathrm{.}6,0\mathrm{.}7,0\mathrm{.}8,0\mathrm{.}85],[-{?}_A,0\mathrm{.}0053,0\mathrm{.}0052,0\mathrm{.}0050,0\mathrm{.}0045,0\mathrm{.}0040,0\mathrm{.}0033,0\mathrm{.}0025,0\mathrm{.}0018,0\mathrm{.}00125,0\mathrm{.}001]]$

Please plot the results in Excel by using Levenspiel plot.

Problem $2$

A gas$-$phase reaction $A+B=C$ is to be conducted in a $10-L($initially$)$ isothermal batch reactor at $25C$ at constant pressure. The reaction is second$-$order with respect to $A,$ with $k_A=0\mathrm{.}023\frac{L}{?}$ mol s$.$ Determine the time required for $75\%$ conversion of $5$molA.

Problem $3$

Suppose the liquid$-$phase hydration of ethylene oxide $($A$)$ to ethylene glycol, $A+B=C,$ takes place in a CSTR of volume $(V)10,000L$; the rate constant is $k_A=2\mathrm{.}464**{10}^{-3}\frac{1}{m}in.$ Calculate the steady$-$state fractional conversion of $A$ if the feed rate $(4)$ is $0\mathrm{.}30Ls-$I and the feed concentration $(C_{AO})$ is $0\mathrm{.}120mo\frac{l}{L}.$