For a temperature uf 100°C and a production rate of R of 0.4 kg s* calculate: • The reactor volume required for a conversion of 0.7. • The heat exchange requirement to maintain a temperature of 100 °C. The heat transfer area required for this if the mean temperature of the cooling fluid is 40°C and the heat transfer coefficient U = 20 kJ m² K* min*.
For a temperature uf 100°C and a production rate of R of 0.4 kg s* calculate: • The reactor volume required for a conversion of 0.7. • The heat exchange requirement to maintain a temperature of 100 °C. The heat transfer area required for this if the mean temperature of the cooling fluid is 40°C and the heat transfer coefficient U = 20 kJ m² K* 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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Q1 in image ,,,

Transcribed Image Text:Question 1
A perfectly mixed flow reactor is to be used to carry out the exothermic isomerisation reaction A -> R.
The rate is given by:
(-ra) = kCa (1ª order)
where k = 4 x 10°e
s000/T
s*, where T is in K.
The enthalpy of reaction AH, = -167,480 kJ kmol*
The molecular mass M, (=Ma) = 100 kg kmol*
Cao initial concentration of A = 1 kmol m3
For a temperature uf 100°C and a production rate of R of 0.4 kg s* calculate:
• The reactor volume required for a conversion of 0.7.
• The heat exchange requirement to maintain a temperature of 100 °C.
The heat transfer area required for this if the mean temperature of the cooling fluid is 40°C
and the heat transfer coefficient U = 20 kJ m? K* min*.
What is the required length of the cooling coil of 0.051 m diameter?
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