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Feed:

Temperature: $70C,$ Pressure: $1$atm

Water: $8\mathrm{.}892$kmo$\frac{l}{h}$

Ethanol: $186\mathrm{.}59$kmo$\frac{l}{h}$

Acetic Acid: $192\mathrm{.}6$kmo$\frac{l}{h}$

For PFR and CSTR$,$ in "More

Specifications" section, select the

following:

Activation Energy: $J$

Molar flow: K$-$moles

Volume: Cubic meters

Time: Seconds

Stoichiometric Reactor

Ethanol: $70\%$ conversion

Gibbs Reactor

PFR; $L=2m,D=0\mathrm{.}3m$

CSTR; $V=0\mathrm{.}14m^3$

Equilibrium Reactor

Ethanol: $70\%$ conversion Please simulate the reactors given in the figure below. The reversible reaction, which takes

place at $70C$ and $1$atm, is given as:

Ethanol $+$ Acetic Acid ~~ Ethyl Acetate $+$ Water

The reaction is first order with respect to each of the reactants $($overall secand order$).$ The

preexponential factor is $1\mathrm{.}9{10}^2\frac{m^3}{k}$mol s and the activation energy is $5\mathrm{.}95{10}^7\frac{1}{k}$mol. For

the backward reaction, the preexponential factor is $5\mathrm{.}0{10}^7\frac{m^3}{k}$mol$-s$ and the activation

energy is $5\mathrm{.}95{10}^7\frac{J}{k}$mol. The reaction takes place in the liquid phase, and the components

are in mole basis. Please consider mixed phase as the valid phase for each reactor. Simulate

your process by using NRTL as the thermodynamic $K$ value model and Latent Heat as the

enthalpy model.

a$.$ What is the flow rate of ethyl acetate exiting each reactor in kmo$\frac{l}{h}?$

b$.$ What is the conversion of ethanol for each reactor?

c$.$ In the PFR reactor, for each component, draw the composition profile $($chose "moles"

as the composition option$)$ as a function of reactor volume.

Feed:

Temperature: $70C,$ Pressure: $1$atm

Water: $8\mathrm{.}892$kmo$\frac{l}{h}$

Ethanol $186\mathrm{.}59$kmo$\frac{l}{h}$

Acetic Acid: $192\mathrm{.}6$kmo$\frac{l}{h}$

For PFR and CSTR$,$ in "More

Specifications $"$ section, select the

following:

Activation Energy: $1$

Molar flow: $K-$moles

Volume: Cubic meters

Time: Seconds

Stolchiometric Reactor

Ethanal: $70\%$ comversion

Gibbs Reactor

$CST{R}_{-}V=0\mathrm{.}14m^2$

Equilibrium Reactor

Ethanol $70\%$ conversion

Please simulate the reactors given in the figure below. The reversible reaction, which takes

place at $70C$ and $1$atm, is given as:

Ethanol $+$ Acetic Acid ~~ Ethyl Acetate $+$ Water

The reaction is first order with respect to each of the reactants $($overall secand order$).$ The

preexponential factor is $1\mathrm{.}9{10}^2\frac{m^3}{k}$mol s and the activation energy is $5\mathrm{.}95{10}^7\frac{1}{k}$mol. For

the backward reaction, the preexponential factor is $5\mathrm{.}0{10}^7\frac{m^3}{k}$mol$-s$ and the activation

energy is $5\mathrm{.}95{10}^7\frac{J}{k}$mol. The reaction takes place in the liquid phase, and the components

are in mole basis. Please consider mixed phase as the valid phase for each reactor. Simulate

your process by using NRTL as the thermodynamic $K$ value model and Latent Heat as the

enthalpy model.

a$.$ What is the flow rate of ethyl acetate exiting each reactor in kmo$\frac{l}{h}?$

b$.$ What is the conversion of ethanol for each reactor?

c$.$ In the PFR reactor, for each component, draw the composition profile $($chose "moles"

as the composition option$)$ as a function of reactor volume.

Feed:

Temperature: $70C,$ Pressure: $1$atm

Water: $8\mathrm{.}892$kmo$\frac{l}{h}$

Ethanol $186\mathrm{.}59$kmo$\frac{l}{h}$

Acetic Acid: $192\mathrm{.}6$kmo$\frac{l}{h}$

For PFR and CSTR$,$ in "More

Specifications $"$ section, select the

following:

Activation Energy: $1$

Molar flow: $K-$moles

Volume: Cubic meters

Time: Seconds

Stolchiometric Reactor

Ethanal: $70\%$ comversion

Gibbs Reactor

$CST{R}_{-}V=0\mathrm{.}14m^2$

Equilibrium Reactor

Ethanol $70\%$ conversion