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H₂ + C₂H2CH₂ (a) Determine the rate law parameters from the data in the table below. There are four spinning baskets, each with 10 g of catalyst. Only hydro- gen and ethane are fed to the reactor at 300°C. TABLE P7-13 RATE DATA

H₂ + C₂H2CH₂ (a) Determine the rate law parameters from the data in the table below. There are four spinning baskets, each with 10 g of catalyst. Only hydro- gen and ethane are fed to the reactor at 300°C. TABLE P7-13 RATE DATA

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:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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The ethane hydrogenolysis over a commercial nickel catalyst was studied in a stirred tank solids reactor H₂ + C₂H2CH₂ (a) Determine the rate law parameters from the data in the table below. There are four spinning baskets, each with 10 g of catalyst. Only hydro- gen and ethane are fed to the reactor at 300°C. TABLE P7-13 RATE DATA Partial Pressure (atm) in Feed Hydrogen, PHO Total Molar Feed Rate to Reactor (mol/h) 1.7 1.2 0.6 0.3 0.75 2.75 Exthane, PAD 0.5 0.5 0.5 0.4 0.6 0.6 0.5 0.5 0.5 0.6 0.6 0.4 Mole Fraction CH4 in Exit Stream 0.05 0.07 0.16 0.16 0.1 0.06
Transcribed Image Text:The ethane hydrogenolysis over a commercial nickel catalyst was studied in a stirred tank solids reactor H₂ + C₂H2CH₂ (a) Determine the rate law parameters from the data in the table below. There are four spinning baskets, each with 10 g of catalyst. Only hydro- gen and ethane are fed to the reactor at 300°C. TABLE P7-13 RATE DATA Partial Pressure (atm) in Feed Hydrogen, PHO Total Molar Feed Rate to Reactor (mol/h) 1.7 1.2 0.6 0.3 0.75 2.75 Exthane, PAD 0.5 0.5 0.5 0.4 0.6 0.6 0.5 0.5 0.5 0.6 0.6 0.4 Mole Fraction CH4 in Exit Stream 0.05 0.07 0.16 0.16 0.1 0.06
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