hw4-17 - 17 150 300 450 1.29 0.72 0.54 1.4 1.2 1 0.8 Zi*Ki...

Info iconThis preview shows page 1. Sign up to view the full content.

View Full Document Right Arrow Icon
This is the end of the preview. Sign up to access the rest of the document.

Unformatted text preview: 17 150 300 450 1.29 0.72 0.54 1.4 1.2 1 0.8 Zi*Ki 0.6 0.4 0.2 0 100 150 200 f(x) = 0x + 1.6 Bubble Point 250 300 Pressure 350 400 450 500 Dew Point Pressure 50 100 150 0.69 1.35 1.87 Zi/Ki 2 1.8 1.6 1.4 1.2 1 0.8 0.6 0.4 0.2 0 40 f(x) = 0.01x + 0.12 60 80 100 Pressure 120 140 160 Gas Vaporization 21 0.6 0.7 0.8 0.9 1.15 1.06 1.01 0.99 1.2 1.15 1.1 Sum of Xf 1.05 1 0.95 0.9 0.5 0.6 0.7 nlf/nli 0.8 0.9 Sum 1 0.95 0.9 0.5 0.6 0.7 nlf/nli 0.8 0.9 22 60 80 120 1 1.01 1.03 Sum of Xf Pressure Reduction 1.04 1.03 1.03 1.02 1.02 1.01 1.01 1 1 0.99 0.99 40 f(x) = 0x + 0.97 50 60 70 80 90 100 110 120 Trial Pressure Special Problem 0 0.33 0.53 0.67 0.75 0.8 0.85 0.89 0.93 0.97 1 25 50 100 150 200 250 300 350 400 450 475 0 0 0.01 0.02 0.05 0.12 0.2 0.36 0.56 0.82 1 25 50 100 150 200 250 300 350 400 450 475 Phase Diagram (Ethane/Hept 500 450 400 350 Temperature(*F) 300 250 200 150 100 50 0 0 0.1 0.2 0.3 0.4 0.5 Heptane Mole Fractio 100 50 0 0 0.1 0.2 0.3 0.4 0.5 Heptane Mole Fractio 00 450 500 140 160 0.8 0.9 1 0.8 0.9 1 n 100 110 120 130 iagram (Ethane/Heptane Mix) 3 0.4 0.5 0.6 0.7 0.8 0.9 1 Heptane Mole Fraction 3 0.4 0.5 0.6 0.7 0.8 0.9 1 Heptane Mole Fraction Gas Vaporization 1.2 1.15 Sum of Xf 1.1 1.05 1 0.95 0.9 0.5 0.6 0.7 nlf/nli 0.8 0.9 1 Pressure Reduction 1.04 1.03 1.03 1.02 1.02 1.01 1.01 1 1 0.99 0.99 40 f(x) = 0x + 0.97 Sum of Xf 50 60 70 80 90 Trial Pressure 100 110 120 130 ...
View Full Document

This note was uploaded on 10/28/2010 for the course PHY 12343 taught by Professor Turner during the Spring '10 term at University of Texas at Austin.

Ask a homework question - tutors are online