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Determine the specific gravity of the gas in TABLE 1. Note: Convert the weight fraction to mole fraction first and state your assumptions

Determine the specific gravity of the gas in TABLE 1. Note: Convert the weight fraction to mole fraction first and state your assumptions

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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Determine the specific gravity of the gas in TABLE 1. Note: Convert the weight fraction to mole fraction first and state your assumptions
TABLE 1: Gas Composition in Weight Fraction Composition Component (Weight fraction) Methane 0.790 Ethane 0.090 Propane 0.065 i-Butane 0.030 n-Butane 0.025 TOTAL 1.00
Transcribed Image Text:TABLE 1: Gas Composition in Weight Fraction Composition Component (Weight fraction) Methane 0.790 Ethane 0.090 Propane 0.065 i-Butane 0.030 n-Butane 0.025 TOTAL 1.00
APPENDIX A PHYSICAL PROPERTIES OF THE PARAFFIN HYDROCARBONS & MISCELLANEOUS COMPOUNDS GAS DENSITY CU FT GAS PER GALLON BOILING LIQUID DENSITY 80°F, 14.7 PSIA (PERFECT GAS) POUNDS MOLECULAR POINT AT CRITICAL CONSTANTS 14.7 PSIA PRESSURE TEMPERATURE PSIA COMPOUND 60°F, 14.7 PSIA WEIGHT Gm CU FT GAS POUNDS PER CU FT LIQUID PER GALLON "F "R PER PER (ACTUAL MCF LIQUID МЕТHANE 16.04 -258.7 673 344 42.27 ETHANE 30.07 -127.5 709 550 79.23 116.19 PROPANE -43.7 618 666 0.5072 35.78 31.66 35.12 36.43 44.09 36.35 ISO-BUTANE 58.12 10.9 530 733 0.5625 153.15 153.15 190.11 30.59 31.75 27.35 27.63 29.70 30.77 26.17 N-BUTANE 58.12 31.1 551 766 0.5836 ISO-PENTANE 72.15 82.1 482 830 0.6241 38.96 N-PENTANE 72.15 96.9 485 847 0.6305 39.36 190.11 227.07 26.36 N-HEXANE 86.17 155.7 434 915 0.6637 41.43 24.34 22.83 N-HEPTANE 209.2 258.2 303.4 345.2 397 973 0.6875 42.92 264.03 21.69 19.55 17.78 16.30 100.2 19.95 N-OCTANE 114.2 370 335 1025 0.7062 0.7211 44.09 300.99 337.95 374.91 17.77 N-NONANE N-DECANE 128.3 1073 45.02 15.88 142.3 312 1115 0.7333 44.78 14.30 AIR 28.97 -317.7 547 239 NITROGEN 28.02 -320.4 492 227 OXYGEN 32.00 -297.4 732 278 CARBON DIOXIDE 44.01 -109.3 1072 548 HYDROGEN 34.08 -76.5 1306 673 SULPHIDE WATER 18.02 212.0 3206 1165 0.9991 62.37
Transcribed Image Text:APPENDIX A PHYSICAL PROPERTIES OF THE PARAFFIN HYDROCARBONS & MISCELLANEOUS COMPOUNDS GAS DENSITY CU FT GAS PER GALLON BOILING LIQUID DENSITY 80°F, 14.7 PSIA (PERFECT GAS) POUNDS MOLECULAR POINT AT CRITICAL CONSTANTS 14.7 PSIA PRESSURE TEMPERATURE PSIA COMPOUND 60°F, 14.7 PSIA WEIGHT Gm CU FT GAS POUNDS PER CU FT LIQUID PER GALLON "F "R PER PER (ACTUAL MCF LIQUID МЕТHANE 16.04 -258.7 673 344 42.27 ETHANE 30.07 -127.5 709 550 79.23 116.19 PROPANE -43.7 618 666 0.5072 35.78 31.66 35.12 36.43 44.09 36.35 ISO-BUTANE 58.12 10.9 530 733 0.5625 153.15 153.15 190.11 30.59 31.75 27.35 27.63 29.70 30.77 26.17 N-BUTANE 58.12 31.1 551 766 0.5836 ISO-PENTANE 72.15 82.1 482 830 0.6241 38.96 N-PENTANE 72.15 96.9 485 847 0.6305 39.36 190.11 227.07 26.36 N-HEXANE 86.17 155.7 434 915 0.6637 41.43 24.34 22.83 N-HEPTANE 209.2 258.2 303.4 345.2 397 973 0.6875 42.92 264.03 21.69 19.55 17.78 16.30 100.2 19.95 N-OCTANE 114.2 370 335 1025 0.7062 0.7211 44.09 300.99 337.95 374.91 17.77 N-NONANE N-DECANE 128.3 1073 45.02 15.88 142.3 312 1115 0.7333 44.78 14.30 AIR 28.97 -317.7 547 239 NITROGEN 28.02 -320.4 492 227 OXYGEN 32.00 -297.4 732 278 CARBON DIOXIDE 44.01 -109.3 1072 548 HYDROGEN 34.08 -76.5 1306 673 SULPHIDE WATER 18.02 212.0 3206 1165 0.9991 62.37
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