Q1/ It is desired to produce 0.045 mol/liter of C from the following exothermic reaction liquid phase reaction 2AC+D in a mixed flow reactor with 45% conversion calculate: 1- the volume of reactor and temperature of coolant coil if it is operated isothermally. 2- the volume of reactor and outlet temperature if it is operated adiabatically. Data:- Feed temperature 77 °C UA-1200 J/min.K Specific reaction rate constant k at 0 °C-0.02m³/kmol.min. Activation energy (E)-4000 kJ/kmol Heat of reaction=- 8000 kJ/kmol Heat capacity of mixture 20 kJ/kmol.K Volumetric feed flow rate -30 liter/min. B is to be carried out in an adiabatic CSTR. If 0.

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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Q1/ It is desired to produce 0.045 mol/liter of C from the following exothermic reaction liquid
phase reaction 2AC+D in a mixed flow reactor with 45% conversion calculate:
1- the volume of reactor and temperature of coolant coil if it is operated isothermally.
2- the volume of reactor and outlet temperature if it is operated adiabatically.
Data:-
Feed temperature 77 °C
UA-1200 J/min.K
Specific reaction rate constant k at 0 °C-0.02m³/kmol.min.
Activation energy (E)-4000 kJ/kmol
Heat of reaction=- 8000 kJ/kmol
Heat capacity of mixture 20 kJ/kmol.K
Volumetric feed flow rate -30 liter/min.
B is to be carried out in an adiabatic CSTR. If 0.
Transcribed Image Text:Q1/ It is desired to produce 0.045 mol/liter of C from the following exothermic reaction liquid phase reaction 2AC+D in a mixed flow reactor with 45% conversion calculate: 1- the volume of reactor and temperature of coolant coil if it is operated isothermally. 2- the volume of reactor and outlet temperature if it is operated adiabatically. Data:- Feed temperature 77 °C UA-1200 J/min.K Specific reaction rate constant k at 0 °C-0.02m³/kmol.min. Activation energy (E)-4000 kJ/kmol Heat of reaction=- 8000 kJ/kmol Heat capacity of mixture 20 kJ/kmol.K Volumetric feed flow rate -30 liter/min. B is to be carried out in an adiabatic CSTR. If 0.
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