a/ (JK'mol") B/ (mJ K²mol") y/(µJK*mol*) CH,(g) 14.16 75.5 -17.99 CO,(g) 26.86 6.97 -0.82 (8)0 H,O(g) 25.72 12.98 -3.862 30.36 9.61 1.184
a/ (JK'mol") B/ (mJ K²mol") y/(µJK*mol*) CH,(g) 14.16 75.5 -17.99 CO,(g) 26.86 6.97 -0.82 (8)0 H,O(g) 25.72 12.98 -3.862 30.36 9.61 1.184
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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As remarked in Problem P2B.4, it is sometimes appropriate to express the temperature dependence of the heat capacity by the empirical expression Cp,m = α + βT + γT2. Use this expression to estimate the standard enthalpy of combustion of methane to carbon dioxide and water vapour at 500 K. Use the following data:
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