There is a 2-m3 reactor in storage that is to be used to carry out the liquid-phase second-order reactionA + B ⎯⎯→CA and B are to be fed in equimolar amounts at a volumetric rate of 1 m3/min. The entering concentration of A is 2 molar, and the specific reaction rate is 1.5 m3/kmol • min. A tracer experiment was carried out and reported in terms of F as a function of time in minutes as shown in Figure P18-17B.Suggest a two-parameter model consistent with the data; evaluate the model parameters and the expected conversion. 1.0-F(t)0.5-2.0t (min)

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Answered: 1.0- F(t) 0.5- 2.0 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

Chapter1: Introduction

Section: Chapter Questions

Problem 1.1P

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There is a 2-m³ reactor in storage that is to be used to carry out the liquid-phase second-order reaction
A + B ⎯⎯→C
A and B are to be fed in equimolar amounts at a volumetric rate of 1 m³/min. The entering concentration of A is 2 molar, and the specific reaction rate is 1.5 m³/kmol • min. A tracer experiment was carried out and reported in terms of F as a function of time in minutes as shown in Figure P18-17_B.Suggest a two-parameter model consistent with the data; evaluate the model parameters and the expected conversion.

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