One mole of n-butane is held in a varying-volume reactor where its gas and liquid phases are in equilibrium at 100°C. The saturated pressure of n-butane at this temperature is 15.41 bar. Select all correct statements below. O a. Using RK cubic equation of state, the compressibility factor of the saturated Liquid is Z = 0.074. O b. Using RK cubic equation of state, the compressibility factor of the saturated vapor is Z = 0.65. If 20% of the total n-butane is in the vapor phase, then the volume occupied by the system is approximately 422.31 cm³. d. Calculating using RK CEOS, the molar volume of the gas is 1515.93 cm³/g. C. e. At this saturated state, both the liquid and vapor volumes calculated from the cubic equation of state are physically meaningful. O f. Calculating using RK CEOS, the molar volume of the gas is 1308.59 cm³/g. Og. At this saturated state, the third root of the CEOS is given by the critical molar volume, Vc and is only physically metastable.
One mole of n-butane is held in a varying-volume reactor where its gas and liquid phases are in equilibrium at 100°C. The saturated pressure of n-butane at this temperature is 15.41 bar. Select all correct statements below. O a. Using RK cubic equation of state, the compressibility factor of the saturated Liquid is Z = 0.074. O b. Using RK cubic equation of state, the compressibility factor of the saturated vapor is Z = 0.65. If 20% of the total n-butane is in the vapor phase, then the volume occupied by the system is approximately 422.31 cm³. d. Calculating using RK CEOS, the molar volume of the gas is 1515.93 cm³/g. C. e. At this saturated state, both the liquid and vapor volumes calculated from the cubic equation of state are physically meaningful. O f. Calculating using RK CEOS, the molar volume of the gas is 1308.59 cm³/g. Og. At this saturated state, the third root of the CEOS is given by the critical molar volume, Vc and is only physically metastable.
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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Transcribed Image Text:One mole of n-butane is held in a varying-volume reactor where its gas and liquid phases are in equilibrium at 100°C. The saturated pressure of n-butane at this
temperature is 15.41 bar. Select all correct statements below.
O a. Using RK cubic equation of state, the compressibility factor of the saturated Liquid is Z = 0.074.
O b. Using RK cubic equation of state, the compressibility factor of the saturated vapor is Z = 0.65.
O c. If 20% of the total n-butane is in the vapor phase, then the volume occupied by the system is approximately 422.31 cm3.
O d. Calculating using RK CEOS, the molar volume of the gas is 1515.93 cm³/g.
O e.
At this saturated state, both the liquid and vapor volumes calculated from the cubic equation of state are physically meaningful.
O f. Calculating using RK CEOS, the molar volume of the gas is 1308.59 cm³/g.
O g. At this saturated state, the third root of the CEOS is given by the critical molar volume, Vc and is only physically metastable.
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