Butane (C4H10)(C4H10) and dry air are fed to a combustion reactor at a steady rate of 45.9 mol/s45.9 mol/s butane and 2500.0 mol/s2500.0 mol/s dry air. Assume the butane reacts completely to produce CO2CO2 and H2O.H2O. The reactants enter the reactor at 25 ∘C25 ∘C and the products leave the reactor at 1110.4 ∘C.1110.4 ∘C. Calculate the percent excess air. Now  Using the information below, find the heat interaction in kW Species Δ?fΔHf at 298 K(kJ/mol) ?P (kJ/kmol·K)CP (kJ/kmol·K) O2 0 3.5R N2 0 3.5R C4H10 -125.5 12R CO2 -393.5 3.5R H2O -241.8 3.5R

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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Butane (C4H10)(C4H10) and dry air are fed to a combustion reactor at a steady rate of 45.9 mol/s45.9 mol/s butane and 2500.0 mol/s2500.0 mol/s dry air. Assume the butane reacts completely to produce CO2CO2 and H2O.H2O. The reactants enter the reactor at 25 ∘C25 ∘C and the products leave the reactor at 1110.4 ∘C.1110.4 ∘C. Calculate the percent excess air.

Now 

Using the information below, find the heat interaction in kW

Species Δ?fΔHf at 298 K(kJ/mol) ?P (kJ/kmol·K)CP (kJ/kmol·K)
O2 0 3.5R
N2 0 3.5R
C4H10 -125.5 12R
CO2 -393.5 3.5R
H2O -241.8 3.5R
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