Introduction to Chemical Engineering Thermodynamics
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: McGraw-Hill Education
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Problem 1. For an irreversible liquid phase reaction 2A -> B, the reaction rate is of the 2nd order with respect to the reactant concentration CA. The concentration-dependent reaction rate is plotted below. This reaction is performed in a cascade of two identical CSTRS (same reactor size and temperature). The inlet concentration of A of the 1st CSTR is 2 mol/L. The outlet concentration of A of the 2nd CSTR is 1 mol/L. The inlet flow rate of the 1st reactor is 100 L/h. Please use the graphical method to determine the outlet concentration of A of the first CSTR and the size of each CSTR. Please briefly show the procedure for reactor size calculation. (-4-7) 15225050 45 40 35 30 0 0.5 11.761.5 C₂ Q C (mol.L¹) Co 20 2.5
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Transcribed Image Text:Problem 1. For an irreversible liquid phase reaction 2A -> B, the reaction rate is of the 2nd order with respect to the reactant concentration CA. The concentration-dependent reaction rate is plotted below. This reaction is performed in a cascade of two identical CSTRS (same reactor size and temperature). The inlet concentration of A of the 1st CSTR is 2 mol/L. The outlet concentration of A of the 2nd CSTR is 1 mol/L. The inlet flow rate of the 1st reactor is 100 L/h. Please use the graphical method to determine the outlet concentration of A of the first CSTR and the size of each CSTR. Please briefly show the procedure for reactor size calculation. (-4-7) 15225050 45 40 35 30 0 0.5 11.761.5 C₂ Q C (mol.L¹) Co 20 2.5
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