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l Verizon LTE 10:23 AM 1 96% Done 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 a liquid in equilibrium with its vapor. If the contents are vapor or a 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 1.5 14 1.3 Generalized compressibility factors (z.=0.27) 1.2 d500 1.1 15.00 10.00-5.00 1.0 3.00 00 80 0.9 1.70 Saturated gas 1.60 0.8 150 0.7 1.35 1.30 0.6 0.75 25 1.20 0.80 0.5 | 0.85 110 0.90 0.4 1.08 106 0.95 1.04 0.3 1.02 1.00 0.2 0,50 0.1 Saturated liquid 0.1 0.2 0.3 04 05 1.0 2.0 3.0 4.0 5.0 30 Reduced pressure, P X + 20 10 00ot Compressibility factor, z

l Verizon LTE 10:23 AM 1 96% Done 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 a liquid in equilibrium with its vapor. If the contents are vapor or a 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 1.5 14 1.3 Generalized compressibility factors (z.=0.27) 1.2 d500 1.1 15.00 10.00-5.00 1.0 3.00 00 80 0.9 1.70 Saturated gas 1.60 0.8 150 0.7 1.35 1.30 0.6 0.75 25 1.20 0.80 0.5 | 0.85 110 0.90 0.4 1.08 106 0.95 1.04 0.3 1.02 1.00 0.2 0,50 0.1 Saturated liquid 0.1 0.2 0.3 04 05 1.0 2.0 3.0 4.0 5.0 30 Reduced pressure, P X + 20 10 00ot Compressibility factor, z

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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Hi this is what it can help please provide the explanation for solutions don’t worry about the  exactly values please read from the graph what you can thank

l Verizon LTE 10:23 AM 1 96% Done 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 a liquid in equilibrium with its vapor. If the contents are vapor or a 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 1.5 14 1.3 Generalized compressibility factors (z.=0.27) 1.2 d500 1.1 15.00 10.00-5.00 1.0 3.00 00 80 0.9 1.70 Saturated gas 1.60 0.8 150 0.7 1.35 1.30 0.6 0.75 25 1.20 0.80 0.5 | 0.85 110 0.90 0.4 1.08 106 0.95 1.04 0.3 1.02 1.00 0.2 0,50 0.1 Saturated liquid 0.1 0.2 0.3 04 05 1.0 2.0 3.0 4.0 5.0 30 Reduced pressure, P X + 20 10 00ot Compressibility factor, z
Transcribed Image Text:l Verizon LTE 10:23 AM 1 96% Done 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 a liquid in equilibrium with its vapor. If the contents are vapor or a 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 1.5 14 1.3 Generalized compressibility factors (z.=0.27) 1.2 d500 1.1 15.00 10.00-5.00 1.0 3.00 00 80 0.9 1.70 Saturated gas 1.60 0.8 150 0.7 1.35 1.30 0.6 0.75 25 1.20 0.80 0.5 | 0.85 110 0.90 0.4 1.08 106 0.95 1.04 0.3 1.02 1.00 0.2 0,50 0.1 Saturated liquid 0.1 0.2 0.3 04 05 1.0 2.0 3.0 4.0 5.0 30 Reduced pressure, P X + 20 10 00ot Compressibility factor, z
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