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Kevin Bacon

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This is a homework problem that was posted in another forum, so there is no template

I have this problem for my reactor design course and I need some help wrapping my head around it.

We have to design a plug flow reactor (PFR), which can be modeled as five equal volume CSTR's in series. The PFR has an inlet volumetric flow rate of ##q_{in}## which contains species ##A_i, i = 1...n## having concentration ##C_{Ai,in}## (also the whole PFR is operated at a constant temperature ##T_{ref}##).

The PFR is initially filled with solution containing species at concentration ##C_{Ai,0}##. The density of the inlet stream is constant at ##\rho##. There are ##m## reactions taking place within the PFR, each defined by the stoichemetric coefficients ##v_{i,j}## where ##i = 1...n, j = 1...m##.

Our goal is to design the smallest possible PFR to achieve steady state conversion of ##X_{A1} = 0.75##.

We are given a matrix of the stoichometric coefficients:

[tex]

v =

\begin{bmatrix}

-a & -b & 0 & d\\

-a & 0 & 0 & d\\

a & 0 & -c & -d\\

0 & b & c & 0

\end{bmatrix}

[/tex]Basic rate laws:

[tex]

r_{A1,1} = -kC_{A1}C_{A2}^2\\

r_{A5,2} = kC_{A1}\\

r_{A4,3} = -kC_{A4}^2\\

r_{A3,4} = -kC_{A3}^2C_{A4}^2

[/tex]

All k = 1, the inlet volumetric flow rate is given and a vector of five values for ##C_{Ai,in}## and ##C_{Ai,0}## are given. My approach so far is to create the net generation term being:

r = [-k*(c(1)*c(2)^2+c(1)^2+c(3)^2*c(4)^2-0.5*c(4)^2);

k*(c(1)-c(1)*c(2)^2);

k*(c(1)-c(4)^2);

k*(c(1)*c(2)^2-c(1)^2+c(3)^2*c(4)^2-0.5*c(4)^2)]

But do I take the CSTR approach or the PFR approach? A general idea would be very helpful. Thank you!

We have to design a plug flow reactor (PFR), which can be modeled as five equal volume CSTR's in series. The PFR has an inlet volumetric flow rate of ##q_{in}## which contains species ##A_i, i = 1...n## having concentration ##C_{Ai,in}## (also the whole PFR is operated at a constant temperature ##T_{ref}##).

The PFR is initially filled with solution containing species at concentration ##C_{Ai,0}##. The density of the inlet stream is constant at ##\rho##. There are ##m## reactions taking place within the PFR, each defined by the stoichemetric coefficients ##v_{i,j}## where ##i = 1...n, j = 1...m##.

Our goal is to design the smallest possible PFR to achieve steady state conversion of ##X_{A1} = 0.75##.

We are given a matrix of the stoichometric coefficients:

[tex]

v =

\begin{bmatrix}

-a & -b & 0 & d\\

-a & 0 & 0 & d\\

a & 0 & -c & -d\\

0 & b & c & 0

\end{bmatrix}

[/tex]Basic rate laws:

[tex]

r_{A1,1} = -kC_{A1}C_{A2}^2\\

r_{A5,2} = kC_{A1}\\

r_{A4,3} = -kC_{A4}^2\\

r_{A3,4} = -kC_{A3}^2C_{A4}^2

[/tex]

All k = 1, the inlet volumetric flow rate is given and a vector of five values for ##C_{Ai,in}## and ##C_{Ai,0}## are given. My approach so far is to create the net generation term being:

r = [-k*(c(1)*c(2)^2+c(1)^2+c(3)^2*c(4)^2-0.5*c(4)^2);

k*(c(1)-c(1)*c(2)^2);

k*(c(1)-c(4)^2);

k*(c(1)*c(2)^2-c(1)^2+c(3)^2*c(4)^2-0.5*c(4)^2)]

But do I take the CSTR approach or the PFR approach? A general idea would be very helpful. Thank you!