Using the data of Appendix A.3, estimate , , h, c , and c p for
Question:
Using the data of Appendix A.3, estimate β, κ, h, cν, and cp for H2O at 800 K and 1 bar.
Data From Appendix A.3
Transcribed Image Text:
T/ psat / MPa K v m³/kg 273.16 0.0006117 0.001000 206.0 0.0 0.0006985 0.001000 181.6 7.8 0.0009918 0.001000 130.2 28.8 335 340 345 350 355 360 UV /h²/h²V / hv / / SLV / sv/ m³/kg kJ/kg kJ/kg kJ/kg kJ/(kg K) kJ/(kg.K) kJ/(kg .K) 2500.9 2500.9 0.0 9.1555 9.1555 9.0783 8.8738 275 280 285 0.001389 0.001001 94.61 49.8 290 0.001920 0.001001 69.63 70.7 295 0.002621 0.001002 51.87 91.7 300 0.003537 0.001003 39.08 112.6 305 0.004719 0.001005 29.77 133.5 310 0.006231 0.001007 22.91 0.001009 17.80 175.3 315 0.008145 320 0.01055 0.001011 13.96 325 0.01 353 0.001013 11.04 330 0.01721 0.001015 8.806 0.02172 0.02719 0.03378 0.04168 0.05108 0.06219 0.07526 0.006231 365 310 325 330 0.001018 7.079 0.001021 5.734 0.001024 4.678 0.001027 3.842 0.001030 3.176 0.001034 2.642 0.001037 2.210 0.001007 22.91 315 0.008145 0.001009 17.80 320 0.01055 0.001011 13.96 0.01 353 0.001013 11.04 0.01721 0.001015 8.806 335 0.02172 0.001018 7.079 0.001021 5.734 340 0.02719 345 0.03378 350 0.04168 355 0.05108 360 0.06219 365 0.07526 0.001024 4.678 0.001027 3.842 0.001030 3.176 0.001034 2.642 370 0.09054 375 0.1083 380 0.1289 385 0.1525 390 0.1796 395 0.2106 400 0.2458 405 0.2856 2496.5 2504.3 0.0283 2484.7 2513.5 0.1041 2472.8 2522.6 0.1784 2461.0 2531.7 0.2513 2449.2 2540.8 0.3228 2437.3 2549.9 0.3931 2425.4 2558.9 0.4622 154.4 2413.5 2567.9 0.5302 2401.6 2576.8 0.5970 196.2 2389.6 2585.7 0.6629 217.1 2377.5 2594.6 0.7277 238.0 2365.4 2603.3 0.7915 258.9 2353.2 2612.1 0.8544 279.8 2340.9 2620.7 0.9164 2328.5 2629.3 0.9775 300.8 321.7 2316.0 2637.7 1.0378 2303.4 2646.1 1.0973 342.7 363.7 2290.7 2654.4 1.1560 2277.8 2662.5 1.2140 384.8 154.4 2413.5 2567.9 0.5302 175.3 2401.6 2576.8 0.5970 196.2 2389.6 2585.7 0.6629 217.1 2377.5 2594.6 0.7277 238.0 2365.4 2603.3 0.7915 258.9 2353.2 2612.1 0.8544 2340.9 2620.7 0.9164 279.8 300.8 2328.5 2629.3 0.9775 321.7 342.7 2303.4 2646.1 1.0973 363.7 2290.7 2654.4 1.1560 2316.0 2637.7 1.0378 384.8 2277.8 2662.5 1.2140 405.8 2264.8 2670.6 1.2713 0.001037 2.210 0.001041 1.859 0.001045 1.572 426.9 2251.6 2678.5 1.3279 0.001049 1.336 0.001053 1.141 469.2 0.001058 0.9794 490.4 2210.9 2701.3 1.4937 0.001062 0.8440 511.7 2197.0 2708.6 1.5477 0.001067 0.7303 532.9 2182.8 2715.7 1.6012 0.001072 0.6345 554.3 2168.3 2722.6 1.6542 448.0 2238.2 2686.3 1.3838 2224.7 2693.9 1.4390 8.6766 8.4862 8.3023 8.1244 7.9523 7.7856 7.6241 7.4674 7.3154 7.1678 7.0244 6.8849 6.7492 6.6171 6.4884 6.3629 6.2405 7.7856 7.6241 7.4674 7.3154 7.1678 7.0244 6.8849 6.7492 6.6171 6.4884 6.3629 6.2405 6.1209 6.0042 5.8900 5.7783 5.6690 5.5619 5.4569 5.3539 9.1066 8.9779 8.8550 8.7375 8.6251 8.5175 8.4145 8.3158 8.2211 8.1303 8.0431 7.9593 7.8787 7.8013 7.7267 7.6549 7.5857 7.5189 7.4545 8.3158 8.2211 8.1303 8.0431 7.9593 7.8787 7.8013 7.7267 7.6549 7.5857 7.5189 7.4545 7.3922 7.3320 7.2738 7.2174 7.1627 7.1096 7.0581 7.0080
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To estimate h c and cp for H2O at 800 K and 1 bar we first need to interpolate the data provided in ...View the full answer
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Thermodynamics Fundamentals And Engineering Applications
ISBN: 9780521862738
1st Edition
Authors: William C. Reynolds, Piero Colonna
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