(1) Component Methane Carbon Dioxide Ethane Propane n-Butane n-Pentane n-Hexane n-Heptane n-Octane n-Decane n-Tetradecane Total FIG. 23-16 Calculation of Liquid Density of a Mixture at 120°F and 1760 psia Mole Fraction 0.20896 0.39730 0.01886 0.02387 0.03586 0.02447 0.01844 0.02983 0.02995 0.18208 0.03038 1.00000 (3) Molecular Weight 16.043 44.010 30.070 44.097 58.123 72.150 86.177 100.204 114.231 142.285 198.394 (4) = (2)-(3) Weight, Ib 3.352 17.485 0.567 1.053 2.084 1.766 1.589 2.989 3.421 25.907 6.027 66.240 (5) Density (60°F), Ib/eu ft 51.016 31.619 36,423 39.360 41.400 42.920 44.090 45.790 47.815
(1) Component Methane Carbon Dioxide Ethane Propane n-Butane n-Pentane n-Hexane n-Heptane n-Octane n-Decane n-Tetradecane Total FIG. 23-16 Calculation of Liquid Density of a Mixture at 120°F and 1760 psia Mole Fraction 0.20896 0.39730 0.01886 0.02387 0.03586 0.02447 0.01844 0.02983 0.02995 0.18208 0.03038 1.00000 (3) Molecular Weight 16.043 44.010 30.070 44.097 58.123 72.150 86.177 100.204 114.231 142.285 198.394 (4) = (2)-(3) Weight, Ib 3.352 17.485 0.567 1.053 2.084 1.766 1.589 2.989 3.421 25.907 6.027 66.240 (5) Density (60°F), Ib/eu ft 51.016 31.619 36,423 39.360 41.400 42.920 44.090 45.790 47.815
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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