A step tracer input was used on a real reactor with the following results:For t≤10 min, then CT= 0.For 10≤t≤30 min, then CT= 10 g/dm3.For t≥30 min, then CT= 40 g/dm3.The second-order reaction A→B with k= 0.1 dm3/mol • min is to be carried out in the real reactor with an entering concentration of A of 1.25 mol/dm3at a volumetric flow rate of 10 dm3/min. Here,k is given at 325 K.(a)What is the mean residence time tm?(b)What is the variance σ2?(c)What conversions do you expect from an ideal PFR and an ideal CSTR in a real reactor with tm?(d)What is the conversion predicted by(1)the segregation model?(2)the maximum mixedness model?(e)What conversion is predicted by an ideal laminar flow reactor?
A step tracer input was used on a real reactor with the following results:
For t≤10 min, then CT= 0.
For 10≤t≤30 min, then CT= 10 g/dm3.
For t≥30 min, then CT= 40 g/dm3.
The second-order reaction A→B with k= 0.1 dm3/mol • min is to be carried out in the real reactor with an entering concentration of A of 1.25 mol/dm3
at a volumetric flow rate of 10 dm3/min. Here,k is given at 325 K.
(a)What is the mean residence time tm?
(b)What is the variance σ2?
(c)What conversions do you expect from an ideal PFR and an ideal CSTR in a real reactor with tm?
(d)What is the conversion predicted by(1)the segregation model?(2)the maximum mixedness model?
(e)What conversion is predicted by an ideal laminar flow reactor?
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