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Fuel feed: 5.0799 mol CH4 ; 2.2822 mol C2H6 Air feed: 22.6844 mol O2 ; 85.3366 mol N2 Dry Burner Gas product: 8.6799 mol CO2 ; 0.9644 mol CO ; 5.0191 mol O2 ; 85.3366 mol N2 ; 17.0064 mol H2O   Calculate: Total heat of reaction per mole of fuel if the reaction products are in gas/vapor phase. (Use heats of formation method)

Fuel feed: 5.0799 mol CH4 ; 2.2822 mol C2H6 Air feed: 22.6844 mol O2 ; 85.3366 mol N2 Dry Burner Gas product: 8.6799 mol CO2 ; 0.9644 mol CO ; 5.0191 mol O2 ; 85.3366 mol N2 ; 17.0064 mol H2O   Calculate: Total heat of reaction per mole of fuel if the reaction products are in gas/vapor phase. (Use heats of formation method)

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
Section: Chapter Questions
Problem 1.1P
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Fuel feed: 5.0799 mol CH4 ; 2.2822 mol C2H6

Air feed: 22.6844 mol O2 ; 85.3366 mol N2

Dry Burner Gas product: 8.6799 mol CO2 ; 0.9644 mol CO ; 5.0191 mol O2 ; 85.3366 mol N2 ; 17.0064 mol H2O

 

Calculate: Total heat of reaction per mole of fuel if the reaction products are in gas/vapor phase. (Use heats of formation method)

 

Use only the following data: Species AH;°(kJ/mol) CH4 -74.520 C2H6 -83.820 CO -110.525 CO29) -393.509 -285.830 Oz(g) Heat of vaporization of water vapor at 25°C is 44,012J/mol
Transcribed Image Text:Use only the following data: Species AH;°(kJ/mol) CH4 -74.520 C2H6 -83.820 CO -110.525 CO29) -393.509 -285.830 Oz(g) Heat of vaporization of water vapor at 25°C is 44,012J/mol
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