The following elementary irreversible reactions are processed in a flow reactor with negligible pressure drop(either PFR or CSTR, see below). The inlet consists of pure A at a temperature of 600°C and a pressure of 1 atm. A → B kı(600 °C) = 5min-1Ea1= 60KJ/molAHr(25°C) = +30 kJ/mol A → C ke (600 °C) = 1min-1Ea2= 30kJ/molAHr(25°C) = +30 kJ/mol www Cp.A= Cp.B=Cpc=50J/mol·K If the reactions are to be processed adiabatically with an exit conversion XA= 0.60, which reactor, PFR or CSTR, would give a higher total selectivity to B?

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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The following elementary irreversible reactions are processed in a flow
reactor with negligible pressure drop(either PFR or CSTR, see below).
The inlet consists of pure A at a temperature of 600°C and a pressure of
1 atm.
A
B kı(600 °C) = 5min-1Eat= 60KJ/molAHr(25°C) = +30 kJ/mol
www
A → C k2 (600 °C) = 1min-1E02= 30KJ/molAHr(25°C) = +30 kJ/mol
Cp.A= Cp.B=Cp.c=50J/mol·K
If the reactions are to be processed adiabatically with an exit conversion
XA= 0.60, which reactor, PFR or CSTR, would give a higher total
selectivity to B?
Transcribed Image Text:The following elementary irreversible reactions are processed in a flow reactor with negligible pressure drop(either PFR or CSTR, see below). The inlet consists of pure A at a temperature of 600°C and a pressure of 1 atm. A B kı(600 °C) = 5min-1Eat= 60KJ/molAHr(25°C) = +30 kJ/mol www A → C k2 (600 °C) = 1min-1E02= 30KJ/molAHr(25°C) = +30 kJ/mol Cp.A= Cp.B=Cp.c=50J/mol·K If the reactions are to be processed adiabatically with an exit conversion XA= 0.60, which reactor, PFR or CSTR, would give a higher total selectivity to B?
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