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1. (Significant figures are having a volume of 4.7 gallons exhibits a pressure of 145 psig at 70.0 °F. Using the compressibility factor chart below determine whether the contents are important). A 20.0 lbs propane tank liquid, gas or a mixture of liquid in equilibrium with its vapor. If the contents are vapor liquid in equilibrium with its vapor, calculate the specific volume of the vapor phase in units of m'/Kg. The critical pressure of propane is 42 atm, its critical temperature is 369.9 K and its molecular weight is 44.09 g/mol а or a 1.5 1.4 1.3 з000 Generalized compressibility factors (z 0.27) 15.00 12 1.1 т, 15.00 10.00-5.00 3.00 1.0 2.00 50 2.00 1.30 20 .80 O.80 85 0.9 0 gn0,95. 1.70 1.Io 00 60 Saturated gas 1.50 0.8 1.40 1.35 0.7 1.30 .25 0.6 T0.75 1.20 0.80 0.5 1.15 0.85 1.10 1.08 0.90 0.4 1.06 0.95 1.04 0.3 1.02 90 1.00 0.2 0 50 0.1 Saturated liquid 0 0.1 3.0 4.0 5.0 30 0.2 0.3 04 05 1.0 2.0 10 20 Reduced pressure, P Compressibility factor, z S0.90

1. (Significant figures are having a volume of 4.7 gallons exhibits a pressure of 145 psig at 70.0 °F. Using the compressibility factor chart below determine whether the contents are important). A 20.0 lbs propane tank liquid, gas or a mixture of liquid in equilibrium with its vapor. If the contents are vapor liquid in equilibrium with its vapor, calculate the specific volume of the vapor phase in units of m'/Kg. The critical pressure of propane is 42 atm, its critical temperature is 369.9 K and its molecular weight is 44.09 g/mol а or a 1.5 1.4 1.3 з000 Generalized compressibility factors (z 0.27) 15.00 12 1.1 т, 15.00 10.00-5.00 3.00 1.0 2.00 50 2.00 1.30 20 .80 O.80 85 0.9 0 gn0,95. 1.70 1.Io 00 60 Saturated gas 1.50 0.8 1.40 1.35 0.7 1.30 .25 0.6 T0.75 1.20 0.80 0.5 1.15 0.85 1.10 1.08 0.90 0.4 1.06 0.95 1.04 0.3 1.02 90 1.00 0.2 0 50 0.1 Saturated liquid 0 0.1 3.0 4.0 5.0 30 0.2 0.3 04 05 1.0 2.0 10 20 Reduced pressure, P Compressibility factor, z S0.90

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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1. (Significant figures are having a volume of 4.7 gallons exhibits a pressure of 145 psig at 70.0 °F. Using the compressibility factor chart below determine whether the contents are important). A 20.0 lbs propane tank liquid, gas or a mixture of liquid in equilibrium with its vapor. If the contents are vapor liquid in equilibrium with its vapor, calculate the specific volume of the vapor phase in units of m'/Kg. The critical pressure of propane is 42 atm, its critical temperature is 369.9 K and its molecular weight is 44.09 g/mol а or a 1.5 1.4 1.3 з000 Generalized compressibility factors (z 0.27) 15.00 12 1.1 т, 15.00 10.00-5.00 3.00 1.0 2.00 50 2.00 1.30 20 .80 O.80 85 0.9 0 gn0,95. 1.70 1.Io 00 60 Saturated gas 1.50 0.8 1.40 1.35 0.7 1.30 .25 0.6 T0.75 1.20 0.80 0.5 1.15 0.85 1.10 1.08 0.90 0.4 1.06 0.95 1.04 0.3 1.02 90 1.00 0.2 0 50 0.1 Saturated liquid 0 0.1 3.0 4.0 5.0 30 0.2 0.3 04 05 1.0 2.0 10 20 Reduced pressure, P Compressibility factor, z S0.90
Transcribed Image Text:1. (Significant figures are having a volume of 4.7 gallons exhibits a pressure of 145 psig at 70.0 °F. Using the compressibility factor chart below determine whether the contents are important). A 20.0 lbs propane tank liquid, gas or a mixture of liquid in equilibrium with its vapor. If the contents are vapor liquid in equilibrium with its vapor, calculate the specific volume of the vapor phase in units of m'/Kg. The critical pressure of propane is 42 atm, its critical temperature is 369.9 K and its molecular weight is 44.09 g/mol а or a 1.5 1.4 1.3 з000 Generalized compressibility factors (z 0.27) 15.00 12 1.1 т, 15.00 10.00-5.00 3.00 1.0 2.00 50 2.00 1.30 20 .80 O.80 85 0.9 0 gn0,95. 1.70 1.Io 00 60 Saturated gas 1.50 0.8 1.40 1.35 0.7 1.30 .25 0.6 T0.75 1.20 0.80 0.5 1.15 0.85 1.10 1.08 0.90 0.4 1.06 0.95 1.04 0.3 1.02 90 1.00 0.2 0 50 0.1 Saturated liquid 0 0.1 3.0 4.0 5.0 30 0.2 0.3 04 05 1.0 2.0 10 20 Reduced pressure, P Compressibility factor, z S0.90
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