For the thermal cracking of ethane in a tubular reactor the following data were obtained for the reaction rate constant at difference reference temperatures: T (K) k (s') | 0.15 | 0.273 | 0.333 | 0.595 | 0.923 | 1.492 2.138 2.718 4.137 4.665 975 998 1007 1027 1046 | 1062 | 1076 1083 | 1100 | 1110 Based on these data find the activation energy and preexponential coefficient using method of linear regression.

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
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For the thermal cracking of ethane in a tubular reactor the following data were obtained for the reaction rate constant at difference reference temperatures:

T (K) 975 998 1007 1027 1046 1062 1076 1083 1100 1110

k(s-1) 0.15 0.273 0.333 0.595 0.923 1.492 2.138 2.718 4.137 4.665
Based on these data find the activation energy and preexponential coefficient using method of linear regression.

For the thermal cracking of ethane in a tubular reactor the following data were
obtained for the reaction rate constant at difference reference temperatures:
1007 1027| 1046 1062 1076
k (s') | 0.15 | 0.273 | 0.333 | 0.595 | 0.923 | 1.492 2.138 || 2.718 | 4.137 4.665
T (K) | 975
998
1083 1100 | 1110
Based on these data find the activation energy and preexponential coefficient using
method of linear regression.
Transcribed Image Text:For the thermal cracking of ethane in a tubular reactor the following data were obtained for the reaction rate constant at difference reference temperatures: 1007 1027| 1046 1062 1076 k (s') | 0.15 | 0.273 | 0.333 | 0.595 | 0.923 | 1.492 2.138 || 2.718 | 4.137 4.665 T (K) | 975 998 1083 1100 | 1110 Based on these data find the activation energy and preexponential coefficient using method of linear regression.
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