Consider the reaction A B +C carried out in a steam heated Non-isothermal Plug Flow Reactor. The internal diameter of the reactor tube may be taken as ID for length (L). Reactant A is fed at the rate of Fo at T₁. The following properties of reacting stream is: p= Density, C₂, Cp, M: Molecular weight, Ts: Temperature of steam for heating purposes, U: Heat transfer coefficient based on inside area of reactor tube, AH, is the heat of reaction, the first order reaction k = 0.1 exp[b (1-7)] = E RTS a: Arrhenius Constant, E.: Activation Energy, Derive ODE of conversion and temperatutr as a function of reactor length.
Consider the reaction A B +C carried out in a steam heated Non-isothermal Plug Flow Reactor. The internal diameter of the reactor tube may be taken as ID for length (L). Reactant A is fed at the rate of Fo at T₁. The following properties of reacting stream is: p= Density, C₂, Cp, M: Molecular weight, Ts: Temperature of steam for heating purposes, U: Heat transfer coefficient based on inside area of reactor tube, AH, is the heat of reaction, the first order reaction k = 0.1 exp[b (1-7)] = E RTS a: Arrhenius Constant, E.: Activation Energy, Derive ODE of conversion and temperatutr as a function of reactor length.
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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![Consider the reaction AB+C carried out in a steam heated Non-isothermal Plug Flow Reactor. The
internal diameter of the reactor tube may be taken as ID for length (L). Reactant A is fed at the rate of
Fo at Ti. The following properties of reacting stream is: p= Density, C₂, Cp, M: Molecular weight, Ts:
Temperature of steam for heating purposes, U: Heat transfer coefficient based on inside area of
reactor tube, AH, is the heat of reaction, the first order reaction
k = 0.1 exp[b (1-7)]
=
E
RTS
a: Arrhenius Constant, E.: Activation Energy,
Derive ODE of conversion and temperatutr as a function of reactor length.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F31d886e5-2759-4a55-97fd-39197728fad9%2F6ba29c39-e7f2-4aa4-952d-a1f320d29f9e%2F5fp56r_processed.jpeg&w=3840&q=75)
Transcribed Image Text:Consider the reaction AB+C carried out in a steam heated Non-isothermal Plug Flow Reactor. The
internal diameter of the reactor tube may be taken as ID for length (L). Reactant A is fed at the rate of
Fo at Ti. The following properties of reacting stream is: p= Density, C₂, Cp, M: Molecular weight, Ts:
Temperature of steam for heating purposes, U: Heat transfer coefficient based on inside area of
reactor tube, AH, is the heat of reaction, the first order reaction
k = 0.1 exp[b (1-7)]
=
E
RTS
a: Arrhenius Constant, E.: Activation Energy,
Derive ODE of conversion and temperatutr as a function of reactor length.
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