Conversion in equal volume CSTR and PFR

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Jaller1404
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Hello
I've been working on a problem that involves finding which reaction order gives a greater conversion for a CSTR over a PFR (Xcstr>Xpfr).
I was able to solve the mass balance for each reactor, finding:

Equation: X_CSTR divided by (1 minus X_CSTR) raised to the power n equals C_A0 raised to the power n minus 1, times tau, times k.


and

Equation: 1/(1-n) times [1 - (1 - X_PFR)^(1-n)] equals C_A0^(n-1) times tau times k, with X_PFR as the PFR conversion, n the reaction order, C_A0 the inlet concentration, tau the residence time and k the rate constant.


Allowing us to equate them. This is where I've been stuck for a while now, how can I find an inequation that would get me which reaction order gives XCSTR>XPFR? It is known that this happen when n<1
 
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  • Equation: X_CSTR divided by (1 minus X_CSTR) raised to the power n equals C_A0 raised to the power n minus 1, times tau, times k.
    upload_2017-12-5_1-25-15.png
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  • Equation: 1/(1-n) times [1 - (1 - X_PFR)^(1-n)] equals C_A0^(n-1) times tau times k, with X_PFR as the PFR conversion, n the reaction order, C_A0 the inlet concentration, tau the residence time and k the rate constant.
    upload_2017-12-5_1-28-13.png
    1.3 KB · Views: 1,104
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Set the two left hand sides equal, and then algebraically solve for Xpfr in terms of Xcstr. Then, for various values of n, plot a graph of Xpfr as a function of Xcstr. I suggest n = 0.5, 1, and 2.
 
Thanks for the tip, but wouldn't n=1 result in a 1/0 indetermination?
 
Jaller1404 said:
Thanks for the tip, but wouldn't n=1 result in a 1/0 indetermination?
For n = 1, you need to go back to the original differential equation. In the limit of n= 1, the solution approaches a natural log solution.
 
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