Eхаmple 6: The vessel (0.2m diameter, 2 m length) has been used as an reactor on the assumption of plug flow. The required conversion of second order reaction (k=2 liter/(mol*min), CA0=2mol/liter) was 90%. Calculate the throughtput necessary to achieve such conversion. Subsequent measurements of RTD are shown below. Calculate the conversion in a real reactor. E [min] 0,5 0.5 (area ) 1.0 3.4 t[min]

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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Eхаmple 6:
The vessel (0.2m diameter, 2 m length) has been used as an reactor on the
assumption of plug flow. The required conversion of second order
reaction (k=2 liter/(mol*min), CA0=2mol/liter) was 90%. Calculate the
throughtput necessary to achieve such conversion. Subsequent
measurements of RTD are shown below. Calculate the conversion in a
real reactor.
E [min]
0,5
0.5 (area )
1.0
3.4
t[min]
Transcribed Image Text:Eхаmple 6: The vessel (0.2m diameter, 2 m length) has been used as an reactor on the assumption of plug flow. The required conversion of second order reaction (k=2 liter/(mol*min), CA0=2mol/liter) was 90%. Calculate the throughtput necessary to achieve such conversion. Subsequent measurements of RTD are shown below. Calculate the conversion in a real reactor. E [min] 0,5 0.5 (area ) 1.0 3.4 t[min]
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