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1. Please prepare a Pū Diagram for Propane based on peer-reviewed published data. You may use Moran et al. Table A-17 OR an equivalent source. Please be certain to cite the source of your data. Please use bar as the pressure units and L/mole for the molar volume units. Please allow the pressure-axis to range from about 10 bar to about 45 bar. Within the PD Diagram, please identify a. The Critical Point b. The Saturated Vapor Line c. Saturated Liquid Line.

1. Please prepare a Pū Diagram for Propane based on peer-reviewed published data. You may use Moran et al. Table A-17 OR an equivalent source. Please be certain to cite the source of your data. Please use bar as the pressure units and L/mole for the molar volume units. Please allow the pressure-axis to range from about 10 bar to about 45 bar. Within the PD Diagram, please identify a. The Critical Point b. The Saturated Vapor Line c. Saturated Liquid Line.

Elements Of Electromagnetics
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
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Kindly Solve all parts with detail Moran et al. Table A-17 is also attached with the Question
TABLE A-17 Properties of Saturated Propane (Liquid-Vapor): Pressure Table Pressure Conversions: 1 bar = 0.1 MPa - 10' kPa Specific Volume m'/kg Internal Energy kJ/kg Enthalpy kJ/kg Entropy kJ/kg · K Sat. Sat. Sat. Sat. Sat. Sat. Sat. Sat. Press. Temp. Liquid v, X 103 Liquid Vapor Liquid Vapor Liquid Evap. Vapor Vapor Press. bar °C he he bar 6.752 -93.28 -83.87 -69.55 -56.93 -48.68 0.05 1.570 -114.6 326.0 -114.6 474.4 359.8 -0.556 2.081 0.05 -95-1 -64.9 0.10 1.594 3.542 335.4 -95.1 465.9 370.8 -0.450 2.011 0.10 1.634 1.672 1.698 - 64.9 -37.6 0.25 1.513 350.0 452.7 387.8 -0.297 1.927 0.25 0.7962 0.5467 - 37-7 -19.6 0.50 363.1 -0.167 -0.085 1.871 1.841 440.5 402.9 0.50 0.75 371.8 -19.5 432.3 412.8 0.75 -42.38 0.4185 -5.6 378.5 396.6 408.7 418.0 1.00 1.719 -5.4 425.7 420.3 -0.023 1.822 1.00 2.00 -25.43 1.781 0.2192 33.1 406.9 1.782 1.762 33.5 440.4 0.139 2.00 -14.16 -5.46 3.00 1.826 0.1496 60.3 81.5 59.8 393.3 453.6 0.244 3.00 1.865 1.899 4.00 0.1137 80.8 382.0 463.5 0.324 1.751 4.00 5.00 1.74 0.09172 98.6 425.7 99.5 372.1 471.6 0.389 1.743 5.00 6.00 0.07680 1.931 1.960 1.989 7.93 363.0 354.6 114.2 432.2 115.3 478.3 0.446 1.737 6.00 7.00 0.06598 0.05776 13.41 128.2 438.0 129.6 142.6 484.2 0.495 1.733 7.00 8.00 18.33 141.0 443.1 447.6 451.8 346.7 489.3 493.8 0.540 8.00 1.729 1.726 9.00 22.82 2.016 0.05129 152.9 154.7 166.1 339.1 331.8 0.580 9.00 10.00 26.95 2.043 0.04606 164.0 497-9 0.618 1.723 10.00 11.00 30.80 2.070 0.04174 174.5 455.6 176.8 0.652 0.685 0.716 324.7 501.5 1.721 11.00 12.00 34.39 2.096 0.03810 184.4 459.1 462.2 465.2 467.9 187.0 196.7 317.8 504.8 1.718 12.00 13.00 37-77 2.122 0.03499 193-9 311.0 507.7 1.716 13.00 14.00 40.97 2.148 0.03231 0.02997 203.0 206.0 304.4 510.4 0.745 1.714 14.00 15.00 44.01 2.174 211.7 215.0 297-9 512.9 0.772 1.712 15.00 16.00 46.89 49.65 2.200 220.1 0.02790 0.02606 470.4 223.6 291.4 515.0 0.799 1.710 16.00 17.00 2.227 228.3 236.2 472.7 285.0 278.6 232.0 0.824 0.849 517.0 1.707 17.00 18.00 52.30 54.83 2.253 0.02441 474-9 240.2 518.8 1.705 18.00 19.00 2.280 476.9 478.7 0.02292 243.8 248.2 272.2 0.873 0.896 520.4 1.703 19.00 20.00 57.27 2.308 0.02157 251.3 255.9 265.9 521.8 1.700 20.00 22.00 61.90 2.364 0.01921 265.8 481.7 484.3 486.2 271.0 253.0 524.0 0.939 1.695 22.00 24.00 66.21 2.424 0.01721 279-7 285.5 525.6 526.5 526.6 240.1 0.981 1.688 24.00 26.00 70.27 2.487 0.01549 293.1 299.6 226.9 1.681 1.021 26.00 28.00 74.10 2.555 0.01398 0.01263 306.2 487.5 313.4 213.2 1.060 1.673 28.00 30.00 77-72 2.630 319.2 488.1 327.1 198.9 526.0 1.097 1.664 30.00 35.00 86.01 2.862 0.009771 351.4 486.3 361.4 159.1 520.5 1.633 1.190 35.00 93.38 96.70 40.00 3.279 0.007151 0.004535 387.9 474.7 401.0 102.3 503.3 1.295 1.574 40.00 42.48 4.535 434-9 434-9 454.2 0.0 454.2 1.437 1.437 42.48
Transcribed Image Text:TABLE A-17 Properties of Saturated Propane (Liquid-Vapor): Pressure Table Pressure Conversions: 1 bar = 0.1 MPa - 10' kPa Specific Volume m'/kg Internal Energy kJ/kg Enthalpy kJ/kg Entropy kJ/kg · K Sat. Sat. Sat. Sat. Sat. Sat. Sat. Sat. Press. Temp. Liquid v, X 103 Liquid Vapor Liquid Vapor Liquid Evap. Vapor Vapor Press. bar °C he he bar 6.752 -93.28 -83.87 -69.55 -56.93 -48.68 0.05 1.570 -114.6 326.0 -114.6 474.4 359.8 -0.556 2.081 0.05 -95-1 -64.9 0.10 1.594 3.542 335.4 -95.1 465.9 370.8 -0.450 2.011 0.10 1.634 1.672 1.698 - 64.9 -37.6 0.25 1.513 350.0 452.7 387.8 -0.297 1.927 0.25 0.7962 0.5467 - 37-7 -19.6 0.50 363.1 -0.167 -0.085 1.871 1.841 440.5 402.9 0.50 0.75 371.8 -19.5 432.3 412.8 0.75 -42.38 0.4185 -5.6 378.5 396.6 408.7 418.0 1.00 1.719 -5.4 425.7 420.3 -0.023 1.822 1.00 2.00 -25.43 1.781 0.2192 33.1 406.9 1.782 1.762 33.5 440.4 0.139 2.00 -14.16 -5.46 3.00 1.826 0.1496 60.3 81.5 59.8 393.3 453.6 0.244 3.00 1.865 1.899 4.00 0.1137 80.8 382.0 463.5 0.324 1.751 4.00 5.00 1.74 0.09172 98.6 425.7 99.5 372.1 471.6 0.389 1.743 5.00 6.00 0.07680 1.931 1.960 1.989 7.93 363.0 354.6 114.2 432.2 115.3 478.3 0.446 1.737 6.00 7.00 0.06598 0.05776 13.41 128.2 438.0 129.6 142.6 484.2 0.495 1.733 7.00 8.00 18.33 141.0 443.1 447.6 451.8 346.7 489.3 493.8 0.540 8.00 1.729 1.726 9.00 22.82 2.016 0.05129 152.9 154.7 166.1 339.1 331.8 0.580 9.00 10.00 26.95 2.043 0.04606 164.0 497-9 0.618 1.723 10.00 11.00 30.80 2.070 0.04174 174.5 455.6 176.8 0.652 0.685 0.716 324.7 501.5 1.721 11.00 12.00 34.39 2.096 0.03810 184.4 459.1 462.2 465.2 467.9 187.0 196.7 317.8 504.8 1.718 12.00 13.00 37-77 2.122 0.03499 193-9 311.0 507.7 1.716 13.00 14.00 40.97 2.148 0.03231 0.02997 203.0 206.0 304.4 510.4 0.745 1.714 14.00 15.00 44.01 2.174 211.7 215.0 297-9 512.9 0.772 1.712 15.00 16.00 46.89 49.65 2.200 220.1 0.02790 0.02606 470.4 223.6 291.4 515.0 0.799 1.710 16.00 17.00 2.227 228.3 236.2 472.7 285.0 278.6 232.0 0.824 0.849 517.0 1.707 17.00 18.00 52.30 54.83 2.253 0.02441 474-9 240.2 518.8 1.705 18.00 19.00 2.280 476.9 478.7 0.02292 243.8 248.2 272.2 0.873 0.896 520.4 1.703 19.00 20.00 57.27 2.308 0.02157 251.3 255.9 265.9 521.8 1.700 20.00 22.00 61.90 2.364 0.01921 265.8 481.7 484.3 486.2 271.0 253.0 524.0 0.939 1.695 22.00 24.00 66.21 2.424 0.01721 279-7 285.5 525.6 526.5 526.6 240.1 0.981 1.688 24.00 26.00 70.27 2.487 0.01549 293.1 299.6 226.9 1.681 1.021 26.00 28.00 74.10 2.555 0.01398 0.01263 306.2 487.5 313.4 213.2 1.060 1.673 28.00 30.00 77-72 2.630 319.2 488.1 327.1 198.9 526.0 1.097 1.664 30.00 35.00 86.01 2.862 0.009771 351.4 486.3 361.4 159.1 520.5 1.633 1.190 35.00 93.38 96.70 40.00 3.279 0.007151 0.004535 387.9 474.7 401.0 102.3 503.3 1.295 1.574 40.00 42.48 4.535 434-9 434-9 454.2 0.0 454.2 1.437 1.437 42.48
1. Please prepare a Pū Diagram for Propane based on peer-reviewed published data. You may use Moran et al. Table A-17 OR an equivalent source. Please be certain to cite the source of your data. Please use bar as the pressure units and L/mole for the molar volume units. Please allow the pressure-axis to range from about 10 bar to about 45 bar. Within the Pū Diagram, please identify a. The Critical Point b. The Saturated Vapor Line c. Saturated Liquid Line.
Transcribed Image Text:1. Please prepare a Pū Diagram for Propane based on peer-reviewed published data. You may use Moran et al. Table A-17 OR an equivalent source. Please be certain to cite the source of your data. Please use bar as the pressure units and L/mole for the molar volume units. Please allow the pressure-axis to range from about 10 bar to about 45 bar. Within the Pū Diagram, please identify a. The Critical Point b. The Saturated Vapor Line c. Saturated Liquid Line.
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