concentrations at the output of the system. If the theoretical volume of the reactor is 1 Feeding volumetric flow rate is 0.1 m'/min, the rate constant is 0.28 m'/(kmol-min) feeding consists of an equimolar solution of A and B, with C = 2 kmol/m', calcu conversion that can be expected in the system. %3D F=C

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72.- The elementary reaction A + B C + D is carried out in a CSTR in which it is
suspected there is bypass and dead volume. The table attached shows the step tracer
concentrations at the output of the system. If the theoretical volume of the reactor is 1 m', the
feeding volumetric flow rate is 0.1 m'/min, the rate constant is 0.28 m'/(kmol-min) and the
feeding consists of an equimolar solution of A and B, with C = 2 kmol/m', calculate the
conversion that can be expected in the system.
%3D
F=C
t (min)
4
8.
10
14
16
18
00
C (mg/L)
1000
1333
1500
1666
1750
1800
2000
my
Activate Windows
Gto Settings to actival
Transcribed Image Text:72.- The elementary reaction A + B C + D is carried out in a CSTR in which it is suspected there is bypass and dead volume. The table attached shows the step tracer concentrations at the output of the system. If the theoretical volume of the reactor is 1 m', the feeding volumetric flow rate is 0.1 m'/min, the rate constant is 0.28 m'/(kmol-min) and the feeding consists of an equimolar solution of A and B, with C = 2 kmol/m', calculate the conversion that can be expected in the system. %3D F=C t (min) 4 8. 10 14 16 18 00 C (mg/L) 1000 1333 1500 1666 1750 1800 2000 my Activate Windows Gto Settings to actival
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