Tablas de termodinamica 1, Apuntes de Fisicoquímica

¡Descarga Tablas de termodinamica 1 y más Apuntes en PDF de Fisicoquímica solo en Docsity! Fact j 6 DIMENSIÓN MÉTRICO MÉTRICO/INGLÉS Aceleración 1 m/s? = 100 cm/s? 1 m/s? = 3.2808 ft/s? 1 ft/s? = 0.3048* m/s? Área 1 m? = 10% cm? = 108 mm? = 10-6 km? 1 m?= 1 550 in? = 10.764 11? 1 ft? = 144 in? = 0.09290304* m? Densidad 1 g/cm? = 1 kg/L = 1 000 kg/m* 1 g/cm? = 62.428 lbm/ft* = 0.036127 Ibm/in* 1728 lbm/ft? 0.062428 lbm/fté Energía, calor, trabajo, 1kJ=1000J=1000N.m= 1 kPa- m* 1 kJ = 0.94782 Btu energía intema, 1 kJ/kg = 1 000 m?/s? 1 Btu = 1.055056 kJ entalpía 1 kWh = 3 600 kJ = 5.40395 psia - ft? = 778.169 Ibf - ft 1 cal! = 4,184 J 1 Btu/lbm = 25 037 ft?/s? = 2.326* kJ/kg 1 IT cal! = 4.1868 J 1 kJ/kg = 0.430 Btu/lbm 1 Cal! = 4.1868 kJ 1 kWh = 3412.14 Btu 1 termia = 10% Btu = 1.055 x 10% kJ (gas natural) Fuerza 1N = 1 kg - m/s? = 105 dina 1N = 0,22481 Ibf 1 kgf = 9.80665 N 1 lbf = 32.174 Ibm - fs? = 4.44822 N Flujo de calor 1 Wicm? = 104 W/m? 1 W/m? = 0.3171 Btu/h - fé Coeficiente de trans- 1 W/m? -*C = 1 Wim? - K 1 W/m? - *C =0.17612 Btu/h - ft? - *F ferencia de calor Longitud 1 m= 100 cm = 1 000 mm = 10% zm 1 m= 39.370 in = 3.2808 ft = 1.0926 yd 1 km = 1000 m 1ft = 12 in = 0.3048* m 1 milla = 5 280 ft = 1.6093 km 1 in = 2.54% cm Masa 1 kg = 10008 1 kg = 2.2046226 lbm 1 tonelada métrica = 1 000 kg 1 Ibm = 0.45359237* kg 1 onza = 28,3495 g 1 slug = 32.174 Ibm = 14.5939 kg 1 ton corta = 2 000 Ibm = 907.1847 kg Potencia, velocidad 1W=1J/s 1kW=3412.14 Btuhn de transferencia 1000 W= 1.341 hp 737.56 Ibt - ft/s de calor 745.7 W 1 hp = 550 Ibf - ft/s = 0.7068 Btu/s = 42.41 Btu/min = 2544.5 Btu/h = 0,74570 kW 1 hp de caldera = 33 475 Btu/h 1 Btu/h = 1.055056 kJ/h 1 ton de refrigeración = 200 Btu/min Presión 1 Pa=1N/m? 1 Pa = 1.4504 x 10-* psia 1 kPa = 10% Pa = 10? MPa 0.020886 Ibt/1t? 1 atm = 101.325 kPa = 1.01325 bars 1 psi = 144 Ibf/ft? = 6.894757 kPa = 760 mm Hg a 0%C 1 atm = 14.696 psia = 29.92 in Hg a 30F = 103323 kgf/cm? 1 in Hg = 3.387 kPa 1 mm Hg = 0.1333 kPa Calor específico 1 kJ/kg + “C = 1 kJ/kg- K =1J/g -*C 1 Btulbm - *F = 4.1868 kJ/kg - “C 1 Btu/lbmol - R = 4.1868 kJ/kmol - K 1 kJ/kg -?C = 0.23885 Btu/lbm - *F 0.23885 Btu/lbm - R * Factores de conversión exactos entre las unidades métricas e inglesas. !La caloría se define originalmente como la cantidad de calor requerida para aumentar 1%C la temperatura de 1 g de agua, pero ésta varía con la temperatura. La caloría de la tabla de vapor internacional (11), generalmente preferida por los ingenieros, es exactamente 4.1868 J por definición y corresponde al calor específico del agua a 15'C. La caloría termoquímica, por lo general preferida por los físicos, es exactamente 4. 184 J por definición y corresponde al calor específico del agua a temperatura ambiente. La diferencia entre las dos es aproximadamente 0.06 por ciento, lo cual es despreciable. La Caloría con inicial mayúscula utilizada por los nutriólogos en realidad es una kilocaloría (1 000 calorías IT). DIMENSIÓN MÉTRICO Volumen específico Temperatura T(K) = TC) + 273.15 AT(K) = ATCC) Conductividad 1 W/m -*C = 1 Wm-K térmica Velocidad 1 m/s = 3.60 km/h Volumen 1 mé = 1.000 L = 10% cm? (cc) . 1 m?s = 60 000 L/min = 10% cms Tasa de flujo volumétrico 1 m?/kg = 1000 L/kg = 1 000 cm?/g MÉTRICO/INGLÉS 1 m3/kg = 16.02 ft/lbm 1 fté/lbm = 0.062428 m'/kg T(R) = TF) + 459.67 = 1.8T(K) TF) = 1.8 TC) + 32 AT(F) = ATR) = 1.8 ATIK) 1 W/m - *C = 0.57782 Btu/h - ft - 9F 1 m/s = 3.2808 ft/s = 2.237 mi/h 1 mi/h = 1.46667 ft/s 1 mi/h = 1.6093 km/h 1m? = 6.1024 x 10* in? = 35.315 ft” 264.17 gal (U.S.) 1 U.S. galón = 231 in? = 3.7854 L 1 fl onza = 29.5735 cm? = 0.0295735 L 1 U.S. galón = 128 fl onzas 1 m/s = 15 850 gal/min (gpm) = 35.315 1t/s = 2 118.9 ft'/min (cfm) “Caballo de fuerza mecánico. El caballo de vapor eléctrico se toma para que sea exactamente igual a 746 W. Algunas constantes físicas Constante universal de los gases Aceleración de la gravedad estándar Presión atmosférica estándar Constante de Stefan-Boltzmann Constante de Boltzmann Velocidad de la luz en el vacío Velocidad del sonido en aire seco a 0% y 1 atm Calor de fusión del agua a 1 atm Entalpía de vaporización del agua a 1 atm R, = 8.31447 kJ/kmol - K 8.31447 kPa - m*/kmol - K 0.0831447 bar - m*/kmol - K 82.05 L - atm/kmol - K 1.9858 Btu/lbmol - R 1 545.37 ft - Ibf/lbmol - R 10.73 psia - ft'/lbmol - R 9.80665 m/s? = 32.174 tus? 1 atm = 101.325 kPa 1.01325 bar 14.696 psia 760 mm Hg (0*C) 29.9213 in Hg (32"F) = 10.3323 m H30 (4*C) 5.6704 x 1078 Wim? . K* 0.1714 x 1072 Btu/h - ft? -R 1.380650 x 10-2 J/K 2.9979 x 10% m/s 9.836 x 108 ft/s 331.36 m/s 1089 ft/s 333.7 kJ/kg 143.5 Btu/lbm 2 256.5 kJ/kg 970.12 Btu/lbm 915 TABLA A-4 Agua saturada. Tabla de temperaturas (conclusión) Volumen específico, Energía interna, Entalpía, Entropía, m/kg KJ/kg K/kg K/kg - K Pres. Líq. Vapor Lía. Vapor Líq. Vapor — Lía. Vapor Temp., sat. sat, sat., sat., Evap., sat., sat., Evap., sat., sat., Evap., sat., TOC PakPa Y, ve “ Us hs 7 ho S; SES 205 17243 0.001164 0.11508 87286 1723.5 25964 874.87 19200 27948 2.3776 4.0154 6.3930 210 1907.7 0.001173 0.10429 895.38 1702.9 2598.3 897.61 1899.7 27973 2.4245 3.9318 6.3563 215 2105.9 0.001181 0.094680 918.02 1681.9 2599.9 920.50 18788 27993 2.4712 3.8489 6.3200 220 2319.6 0.001190 0.086094 940.79 1660.5 2601.3 943.55 18574 28010 2.5176 3.7664 6.2840 225 2549.7 0.001199 0.078405 963.70 1638.6 2602.3 966.76 1835.4 2802.2 2.5639 3.6844 6.2483 230 2797.1 0.001209 0.071505 986.76 1616.1 2602.9 990.14 18128 28029 2.6100 3.6028 6.2128 235 3062.6 0.001219 0.065300 10100 15932 26032 1013.7 17895 2803.2 2.6560 3.5216 6.1775 240 3347.0 0.001229 0.059707 10334 15698 2603.1 1037.5 1765.5 2803.0 2.7018 3.4405 6.1424 245 3651.2 0.001240 0.054656 1056.9 1545.7 2602.7 10615 17408 2802.2 2.7476 3.3596 6.1072 250 3976.2 0.001252 0.050085 1080.7 1521.1 26018 1085.7 17153 2801.00 2.7933 3.2788 6.0721 255 4322.9 0.001263 0.045941 1104.7 1495.8 2600.55 1110.1 1689.0 27991 2.8390 3.1979 6.0369 260 4692.3 0.001276 0.042175 11288 14699 25987 11348 16618 2796.6 2.8847 3.1169 6.0017 265 5085.3 0.001289 0.038748 1153.3 1443.2 25965 11598 1633.7 2793.5 2.9304 3.0358 5.9662 270 5503.0 0.001303 0.035622 11779 1415.7 25937 1185.1 1604.6 2789.7 2.9762 2.9542 5.9305 275 5946.4 0.001317 0.032767 12029 1387.4 25903 1210.7 15745 2785.22 3.0221 2.8723 5.8944 280 6416.6 0.001333 0.030153 1228.2 1358.2 25864 1236.7 1543.2 27799 3.0681 2.7898 5.8579 285 6914.6 0.001349 0.027756 1253.7 1328.1 25818 1263.1 1510.7 2773.7 3.1144 2.7066 5.8210 290 74418 0.001366 0.025554 1279.7 1296.9 25765 1289.8 1476.9 2766.7 3.1608 2.6225 5.7834 295 7999.0 0.001384 0.023528 13060 1264.5 25705 1317.1 14416 2758.7 3.2076 2.5374 5.7450 300 8587.9 0.001404 0.021659 1332.7 1230.9 25636 1344.8 14048 27496 3.2548 2.4511 5.7059 305 9209.4 0.001425 0.019932 13600 11959 25558 1373.1 1366.3. 27394 3.3024 2.3633 5.6657 310 9865.0 0.001447 0.018333 1387.7 11593 2547.1 14020 13259 2727.9 3.3506 2.2737 5.6243 315 10,556 0.001472 0.016849 1416.1 11211 25372 14316 12834 27150 3.3994 2.1821 5.5816 320 11,284 0.001499 0.015470 1445.1 1080.9 2526.0 14620 1238.5 2700.6 3.4491 2.0881 5.5372 325 12,051 0.001528 0.014183 14750 10385 25134 1493.4 11910 2684.3 3.4998 1.9911 5.4908 330 12,858 0.001560 0.012979 1505.7 993.5 24992 1525.8 1140.3 2666.0 3.5516 1.8906 5.4422 335 13,707 0.001597 0.011848 1537.5 945.5 24830 15594 1086.0 26454 3.6050 1.7857 5.3907 340 14,601 0.001638 0.010783 1570.7 893.8 24645 1594.6 10274 26220 3.6602 1.6756 5.3358 345 15,541 0.001685 0.009772 1605.5 837.7 24432 16317 963.4 2595.1 3.7179 1.5585 5.2765 350 16,529 0.001741 0.008806 1642.4 775.9 24183 16712 892.7 2563.9 3.7788 1.4326 5.2114 355 17,570 0.001808 0.007872 1682.2 706.4 23886 17140 8129 2526.9 3.8442 1.2942 5.1384 360 18,666 0.001895 0.006950 1726.2 625.7 23519 17615 720.1 2481.66 3.9165 1.1373 5.0537 365 19,822 0.002015 0.006009 1777.2 526.4 23036 1817.2 605.5 2422.7 4.0004 0.9489 4.9493 370 21,044 0.002217 0.004953 1844.5 385.6 2230.1 18912 443.1 23343 4.1119 0.6890 4.8009 373.95 22,064 0.003106 0.003106 2015.7 0 2015.7 2084.3 0 2084.3 4.4070 0 4.4070 Fuente: Las tablas A-4 a A-8 fueron generadas utilizando el programa para resolver ecuaciones de ingeniería (EES) desarrollado por S. A. Klein y F. L. Alvarado. La rutina utilizada en los cálculos es la altamente precisa Steam_IAPWS, que incorpora la Formulación 1995 para las Propiedades Termodinámicas de la Sustancia Agua Ordinaria para Uso Científico y General, editada por The International Association for the Properties of Water and Steam (lAPWS). Esta formulación reemplaza a la formulación de 1984 de Haar, Gallagher y Kell (NBS/NRC Steam Tables, Hemisphere Publishing Co., 1984), la cual está también disponible en EES como la rutina STEAM. La nueva formulación se basa en las correlaciones de Saul y Wagner (J. Phys. Chem. Ref. Data, 16, 893, 1987) con modificaciones para ajustarla a la Escala Internacional de Temperaturas de 1990. Las modificaciones están descritas por Wagner y Pruss (1. Phys. Chem. Ref. Data, 22, 783, 1993). Las propiedades del hielo están basadas en Hyland y Wexler, “Formulations for the Thermodynamic Properties of the Saturated Phases of H20 from 173.15 K a 473.15 K”, ASHRAE Trans., Part 2A, Paper 2793, 1983, 916 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-5 Agua saturada. Tabla de presiones Volumen específico, Energía interna, Entalpía, Entropía, mg K/kg kI/kg ki/kg - K Temp. —LíQ. Vapor Líd. Vapor Líg. Vapor — Líg. Vapor Pres., sat., sat., sat., sat., Evap., sat. sat, Evap., sat, sat, Evap., sat, Pkpa Ta Cv Y w Ug uy he Mg ha Ss, SES 1.0 6.97 0.001000 129.19 29.302 2355.2 2384.5 29.303 2484.4 2513.7 0.1059 8.8690 8.9749 1.5 13.02 0.001001 87.964 54.686 2338.1 23928 54.688 2470.1 2524.7 0.1956 8.6314 8.8270 2.0 17.50 0.001001 66.990 73.431 2325.5 2398.9 73.433 2459.5 2532.9 0.2606 8.4621 8.7227 2.5 21.08 0.001002 54.242 88.422 2315.4 24038 88.424 2451.0 2539.4 0.3118 8.3302 8.6421 3.0 24.08 0.001003 45.654 100.98 2306.9 2407.9 100.98 2443.9 2544.8 0.3543 8.2222 8.5765 4.0 28.96 0.001004 34.791 121.39 2293.1 24145 121.39 2432.3 2553.7 0.4224 8.0510 8.4734 5.0 32.87 0.001005 28.185 137.75 2282.1 24198 137.75 2423.0 2560.7 0.4762 7.9176 8.3938 7.5 40.29 0.001008 19.233 168.74 2261.1 24298 168.75 2405.3 2574.0 0.5763 7.6738 8.2501 10 45.81 0.001010 14.670 191.79 2245.4 2437.2 191.81 2392.1 2583.9 0.6492 7.4996 8.1488 15 53.97 0.001014 10.020 225.93 2222.1 2448.0 225.94 2372.3 2598.3 0.7549 7.2522 8.0071 20 60.06 0.001017 7.6481 251.40 2204.6 2456.0 251.42 2357.5 2608.9 0.8320 7.0752 7.9073 25 64.96 0.001020 6.2034 271.93 2190.4 2462.44 271.96 2345.5 2617.5 0.8932 6.9370 7.8302 30 69.09 0.001022 5.2287 289.24 2178.5 2467.7 289.27 2335.3 2624.6 0.9441 6.8234 7.7675 40 75.86 0.001026 3.9933 317.58 2158.8 2476.3 317.62 2318.4 2636.1 1.0261 6.6430 7.6691 50 81.32 0.001030 3.2403 340.49 2142.7 2483.2 340.54 2304.7 2645.2 1.0912 6.5019 7.5931 75 91.76 0.001037 2.2172 384.36 21118 2496.1 384.44 2278.0 2662.4 1.2132 6.2426 7.4558 100 99.61 0.001043 1.6941 417.40 2088.2 2505.6 417.51 2257.5 2675.0 1.3028 6.0562 7.3589 101.325 99.97 0.001043 1.6734 418.95 2087.0 2506.0 419.06 2256.5 2675.6 1.3069 6.0476 7.3545 125 105.97 0.001048 1.3750 444.23 2068.8 2513.0 444.36 2240.6 2684.9 1.3741 5.9100 7.2841 150 111.35 0.001053 1.1594 466.97 2052.3 2519.2 467.13 2226.0 2693.1 1.4337 5.7894 7.2231 175 116.04 0.001057 1.0037 486.82 2037.7 2524.5 487.01 2213.1 2700.2 1.4850 5.6865 7.1716 200 120.21 0.001061 0.88578 504.50 2024.6 2529.1 504.71 2201.6 2706.3 1.5302 5.5968 7.1270 225 123.97 0.001064 0.79329 520.47 2012.7 2533.2 520.71 21910 2711.7 1.5706 5.5171 7.0877 250 127.41 0.001067 0.71873 535.08 2001.8 2536.8 535.35 21812 2716.5 1.6072 5.4453 7.0525 275 130.58 0.001070 0.65732 548.57 1991.6 2540.1 548.86 2172.0 2720.9 1.6408 5.3800 7.0207 300 133.52 0.001073 0.60582 561.11 1982.1 2543.2 561.43 2163.5 2724.9 1.6717 5.3200 6.9917 325 136.27 0.001076 0.56199 572.84 1973.1 2545.9 573.19 21554 2728.6 1.7005 5.2645 6.9650 350 138.86 0.001079 0.52422 583.89 1964.6 2548.5 584.26 2147.7 2732.0 1.7274 5.2128 6.9402 375 141.30 0.001081 0.49133 594.32 1956.6 2550.9 594.73 2140.4 2735.1 1.7526 5.1645 6.9171 400 143.61 0.001084 0.46242 604.22 1948.9 2553.1 604.66 21334 2738.1 1.7765 5.1191 6.8955 450 147.90 0.001088 0.41392 622.65 1934.5 2557.1 623.14 2120.3 2743.4 1.8205 5.0356 6.8561 500 151.83 0.001093 0.37483 639.54 1921.2 2560.7 640.09 2108.0 2748.1 1.8604 4.9603 6.8207 550 155.46 0.001097 0.34261 655.16 1908.8 2563.9 655.77 2096.6 2752.4 1.8970 4.8916 6.7886 600 158.83 0.001101 0.31560 669.72 1897.1 2566.8 670.38 2085.8 2756.2 1.9308 4.8285 6.7593 650 161.98 0.001104 0.29260 683.37 1886.1 2569.4 684.08 2075.5 2759.6 1.9623 4.7699 6.7322 700 164.95 0.001108 0.27278 696.23 1875.6 25718 697.00 2065.8 2762.8 1.9918 4.7153 6.7071 750 167.75 0.001111 0.25552 708.40 1865.6 2574.0 709.24 2056.4 2765.7 2.0195 4.6642 6.6837 917 IA TABLA A-5 Agua saturada. Tabla de presiones (conclusión) Volumen específico, Energía interna, Entalpía, Entropía, m/kg 1J/kg K/kg K/kg - K Temp. Lía. Vapor Lía. Vapor Lía. Vapor Lía. Vapor Pres., sat., sat., sat., sat., Evap., sat. sat, Evap., sat, sat, Evap., sat, PkPa To Cv, ve “ Ug Ue hy he he S; SES 800 170.41 0.001115 0.24035 719.97 1856.1 2576.0 720.87 2047.5 2768.3 2.0457 4.6160 6.6616 850 172.94 0.001118 0.22690 731.00 1846.9 2577.9 731.95 2038.8 2770.8 2.0705 4.5705 6.6409 900 175.35 0.001121 0.21489 741.55 1838.1 2579.6 742.56 2030.5 2773.0 2.0941 4.5273 6.6213 950 177.66 0.001124 0.20411 751.67 1829.6 2581.3 752.74 2022.4 2775.2 2.1166 4.4862 6.6027 1000 179.88 0.001127 0.19436 761.39 1821.4 2582.8 762.51 2014.6 2777.1 2.1381 4.4470 6.5850 1100 184.06 0.001133 0.17745 779.78 1805.7 2585.5 781.03 1999.6 2780.7 2.1785 4.3735 6.5520 1200 187.96 0.001138 0.16326 796.96 1790.9 2587.8 798.33 1985.4 2783.8 2.2159 4.3058 6.5217 1300 191.60 0.001144 0.15119 813.10 1776.8 2589.9 814.59 1971.9 2786.5 2.2508 4.2428 6.4936 1400 195.04 0.001149 0.14078 828.35 1763.4 2591.8 829.96 1958.9 2788.9 2.2835 4.1840 6.4675 1500 198.29 0.001154 0.13171 842.82 1750.6 2593.4 844.55 1946.4 2791.0 2.3143 4.1287 6.4430 1750 205.72 0.001166 0.11344 876.12 1720.6 2596.7 878.16 1917.1 2795.2 2.3844 4.0033 6.3877 2000 212.38 0.001177 0.099587 906.12 1693.0 2599.1 908.47 1889.8 2798.3 2.4467 3.8923 6.3390 2250 218.41 0.001187 0.088717 933.54 1667.3 2600.9 936.21 1864.3 2800.5 2.5029 3.7926 6.2954 2500 223.95 0.001197 0.079952 958.87 1643.2 2602.1 961.87 1840.1 2801.9 2.5542 3.7016 6.2558 3000 233.85 0.001217 0.066667 1004.6 1598.5 2603.2 1008.3 1794.9 2803.2 2.6454 3.5402 6.1856 3500 242.56 0.001235 0.057061 1045.4 1557.6 2603.0 1049.7 1753.0 2802.7 2.7253 3.3991 6.1244 4000 250.35 0.001252 0.049779 1082.4 1519.3 2601.7 1087.4 1713.5 2800.8 2.7966 3.2731 6.0696 5000 263.94 0.001286 0.039448 1148.1 1448.9 2597.0 1154.5 1639.7 2794.2 2.9207 3.0530 5.9737 6000 275.59 0.001319 0.032449 1205.8 1384.1 2589.9 1213.8 1570.9 2784.6 3.0275 2.8627 5.8902 7000 285.83 0.001352 0.027378 1258.0 1323.0 2581.0 1267.5 1505.2 2772.6 3.1220 2.6927 5.8148 8000 295.01 0.001384 0.023525 1306.0 1264.5 2570.5 1317.1 1441.6 2758.7 3.2077 2.5373 5.7450 9000 303.35 0.001418 0.020489 1350.9 1207.6 2558.5 1363.7 1379.3 2742.9 3.2866 2.3925 5.6791 10,000 311.00 0.001452 0.018028 1393.3 1151.8 2545.2 1407.8 1317.6 2725.5 3.3603 2.2556 5.6159 11,000 318.08 0.001488 0.015988 1433.9 1096.6 2530.4 1450.2 1256.1 2706.3 3.4299 2.1245 5.5544 12,000 324.68 0.001526 0.014264 1473.0 1041.3 2514.3 1491.3 1194.1 2685.4 3.4964 1.9975 5.4939 13,000 330.85 0.001566 0.012781 1511.0 985.5 2496.6 1531.4 1131.3 2662.7 3.5606 1.8730 5.4336 14,000 336.67 0.001610 0.011487 1548.4 928.7 2477.1 1571.0 1067.0 2637.9 3.6232 1.7497 5.3728 15,000 342.16 0.001657 0.010341 1585.5 870.3 2455.7 1610.3 1000.5 2610.8 3.6848 1.6261 5.3108 16,000 347.36 0.001710 0.009312 1622.6 809.4 2432.0 1649.9 931.1 2581.0 3.7461 1.5005 5.2466 17,000 352.29 0.001770 0.008374 1660.2 745.1 2405.4 1690.3 857.4 2547.7 3.8082 1.3709 5.1791 18,000 356.99 0.001840 0.007504 1699.1 675.9 2375.0 1732.2 777.8 2510.0 3.8720 1.2343 5.1064 19,000 361.47 0.001926 0.006677 1740.3 598.9 2339.2 1776.8 689.2 2466.0 3.9396 1.0860 5.0256 20,000 365.75 0.002038 0.005862 1785.8 509.0 2294.8 1826.6 585.5 2412.1 4.0146 0.9164 4.9310 21,000 369.83 0.002207 0.004994 1841.6 391.9 2233.5 1888.0 450.4 2338.4 4.1071 0.7005 4.8076 22,000 373.71 0.002703 0.003644 1951.7 140.8 2092.4 2011.1 161.5 2172.66 4.2942 0.2496 4.5439 22,064 373.95 0.003106 0.003106 2015.7 0 2015.7 2084.3 0 2084.3 4.4070 O 4.4070 920 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-6 Vapor de agua sobrecalentado (continuación) 7 “e v u mike kJ/kg h IJ/kg s KJ/kg - Ki v u h m/kg kJikg kJ/kg s KJ/kg - K v u h s m?/kg — kJ/kg kJkg kJ/kg-K Sat. 275 300 350 400 450 500 600 700 800 900 1000 1100 1200 1300 Sat. 300 350 400 450 500 550 600 700 800 900 1000 1100 1200 1300 Sat. 325 350 400 450 500 550 600 650 700 800 900 1000 1100 1200 1300 P = 4.0 MPa (250.35 *C) P= 4.5 MPa (257.44 *C) P = 5.0 MPa (263.94 *C) 0.04978 2601.7 0.05461 2668.9 0.05887 2726.2 0.06647 2827.4 0.07343 2920.8 0.08004 3011.0 0.08644 3100.3 0.09886 3279.4 0.11098 3462.4 0.12292 3650.6 0.13476 3844.8 0.14653 4045.1 0.15824 4251.4 0.16992 4463.5 0.18157 4680.9 2800.8 2887.3 2961.7 3093.3 3214.5 3331.2 3446.0 3674.9 3906.3 4142.3 4383.9 4631.2 4884.4 5143.2 5407.2 6.0696 6.2312 6.3639 6.5843 6.7714 6.9386 7.0922 7.3706 7.6214 7.8523 8.0675 8.2698 8.4612 8.6430 8.8164 0.04406 2599.7 2798.0 0.04733 2651.4 2864.4 0.05138 2713.0 2944.2 0.05842 2818.6 3081.5 0.06477 2914.2 3205.7 0.07076 3005.8 3324.2 0.07652 3096.0 3440.4 0.08766 3276.4 3670.9 0.09850 3460.0 3903.3 0.10916 3648.8 4140.0 0.11972 3843.3 4382.1 0.13020 4043.9 4629.8 0.14064 4250.4 4883.2 0.15103 4462.6 5142.2 0.16140 4680.1 5406.5 6.0198 6.1429 6.2854 6.5153 6.7071 6.8770 7.0323 7.3127 7.5647 7.7962 8.0118 8.2144 8.4060 8.5880 8.7616 0.03945 2597.0 2794.2 5.9737 0.04144 2632.3 2839.5 6.0571 0.04535 2699.0 2925.7 6.2111 0.05197 2809.5 3069.3 6.4516 0.05784 2907.5 3196.7 6.6483 0.06332 3000.6 3317.2 6.8210 0.06858 3091.8 3434.7 6.9781 0.07870 3273.3 3666.9 7.2605 0.08852 3457.7 3900.3 7.5136 0.09816 3646.9 4137.7 7.7458 0.10769 3841.8 4380.2 7.9619 0.11715 4042.6 4628.3 8.1648 0.12655 4249.3 4882.1 8.3566 0.13592 4461.6 5141.3 8.5388 0.14527 4679.3 5405.7 8.7124 P = 6.0 MPa (275.59 *C) P = 7.0 MPa (285.83 *C) P = 8.0 MPa (295.01 *C) 0.03245 2589.9 0.03619 2668.4 0.04225 2790.4 0.04742 2893.7 0.05217 2989.9 0.05667 3083.1 0.06102 3175.2 0.06527 3267.2 0.07355 3453.0 0.08165 3643.2 0.08964 3838.8 0.09756 4040.1 0.10543 4247.1 0.11326 4459.8 0.12107 4677.7 2784.6 2885.6 3043.9 3178.3 3302.9 3423.1 3541.3 3658.8 3894.3 4133.1 4376.6 4625.4 4879.7 5139.4 5404.1 5.8902 6.0703 6.3357 6.5432 6.7219 6.8826 7.0308 7.1693 7.4247 7.6582 7.8751 8.0786 8.2709 8.4534 8.6273 0.027378 2581.0 2772.6 0.029492 2633.5 2839.9 0.035262 2770.1 3016.9 0.039958 2879.5 3159.2 0.044187 2979.0 3288.3 0.048157 3074.3 3411.4 0.051966 3167.9 3531.6 0.055665 3261.0 3650.6 0.062850 3448.3 3888.3 0.069856 3639.5 4128.5 0.076750 3835.7 4373.0 0.083571 4037.5 4622.5 0.090341 4245.0 4877.4 0.097075 4457.9 5137.4 0.103781 4676.1 5402.6 5.8148 5.9337 6.2305 6.4502 6.6353 6.8000 6.9507 7.0910 7.3487 7.5836 7.8014 8.0055 8.1982 8.3810 8.5551 0.023525 2570.5 2758.7 5.7450 0.024279 2592.3 2786.5 5.7937 0.029975 2748.3 2988.1 6.1321 0.034344 2864.6 3139.4 6.3658 0.038194 2967.8 3273.3 6.5579 0.041767 3065.4 3399.5 6.7266 0.045172 3160.5 3521.8 6.8800 0.048463 3254.7 3642.4 7.0221 0.054829 3443.6 3882.2 7.2822 0.061011 3635.7 4123.8 7.5185 0.067082 3832.7 4369.3 7.7372 0.073079 4035.0 4619.6 7.9419 0.079025 4242.8 4875.0 8.1350 0.084934 4456.1 5135.5 8.3181 0.090817 4674.5 5401.0 8.4925 P = 9.0 MPa (303.35 *C) P = 10.0 MPa (311.00 *C) P= 12.5 MPa (327.81 *C) 0.020489 2558.5 0.023284 2647.6 0.025816 2725.0 0.029960 2849.2 0.033524 2956.3 0.036793 3056.3 0.039885 3153.0 0.042861 3248.4 0.045755 3343.4 0.048589 3438.8 0.054132 3632.0 0.059562 3829.6 0.064919 4032.4 0.070224 4240.7 0.075492 4454.2 0.080733 4672.9 2742.9 2857.1 2957.3 3118.8 3258.0 3387.4 3512.0 3634.1 3755.2 3876.1 4119.2 4365.7 4616.7 4872.7 5133.6 5399.5 5.6791 5.8738 6.0380 6.2876 6.4872 6.6603 6.8164 6.9605 7.0954 7.2229 7.4606 7.6802 7.8855 8.0791 8.2625 8.4371 0.018028 2545.2 2725.5 0.019877 2611.6 2810.3 0.022440 2699.6 2924.0 0.026436 2833.1 3097.5 0.029782 2944.5 3242.4 0.032811 3047.0 3375.1 0.035655 3145.4 3502.0 0.038378 3242.0 3625.8 0.041018 3338.0 3748.1 0.043597 3434.0 3870.0 0.048629 3628.2 4114.5 0.053547 3826.5 4362.0 0.058391 4029.9 4613.8 0.063183 4238.5 4870.3 0.067938 4452.4 5131.7 0.072667 4671.3 5398.0 5.6159 5.7596 5.9460 6.2141 6.4219 6.5995 6.7585 6.9045 7.0408 7.1693 7.4085 7.6290 7.8349 8.0289 8.2126 8.3874 0.013496 2505.6 2674.3 5.4638 0.016138 2624.9 2826.6 5.7130 0.020030 2789.6 3040.0 6.0433 0.023019 2913.7 3201.5 6.2749 0.025630 3023.2 3343.6 6.4651 0.028033 3126.1 3476.5 6.6317 0.030306 3225.8 3604.6 6.7828 0.032491 3324.1 3730.2 6.9227 0.034612 3422.0 3854.6 7.0540 0.038724 3618.8 4102.8 7.2967 0.042720 3818.9 4352.9 7.5195 0.046641 4023.5 4606.5 7.7269 0.050510 4233.1 4864.5 7.9220 0.054342 4447.7 5127.0 8.1065 0.058147 4667.3 5394.1 8.2819 921 IA TABLA A-6 Vapor de agua sobrecalentado (conclusión) T v u h s v u h s v u h s “C míkg kikg kkg kikg-K|mí/kg kJkg kJkg kJ/kg-KlmVkg ki/kg kJ/kg kkg-K P = 15.0 MPa (342.16 *C) P= 17.5 MPa (354.67 *C) P = 20.0 MPa (365.75 *C) Sat. 0.010341 2455.7 2610.8 5.3108 0.007932 2390.7 2529.5 5.1435 |0.005862 2294.8 2412.1 4.9310 350 0.011481 2520.9 2693.1 5.4438 400 0.015671 2740.6 2975.7 5.8819 0.012463 2684.3 2902.4 5.7211 |0.009950 2617.9 2816.9 5.5526 450 0.018477 2880.8 3157.9 6.1434 0.015204 2845.4 3111.4 6.0212 |0.012721 2807.3 3061.7 5.9043 500 0.020828 2998.4 3310.8 6.3480 0.017385 2972.4 3276.7 6.2424 |0.014793 2945.3 3241.2 6.1446 550 0.022945 3106.2 3450.4 6.5230 0.019305 3085.8 3423.6 6.4266 |0.016571 3064.7 3396.2 6.3390 600 0.024921 3209.3 3583.1 6.6796 0.021073 3192.5 3561.3 6.5890 |0.018185 3175.3 3539.0 6.5075 650 0.026804 3310.1 3712.1 6.8233 0.022742 3295.8 3693.8 6.7366 |0.019695 3281.4 3675.3 6.6593 700 0.028621 3409.8 3839.1 6.9573 0.024342 3397.5 3823.5 6.8735 |0.021134 3385.1 3807.8 6.7991 800 0.032121 3609.3 4091.1 7.2037 0.027405 3599.7 4079.3 7.1237 |0.023870 3590.1 4067.5 7.0531 900 0.035503 3811.2 4343.7 7.4288 0.030348 3803.5 4334.6 7.3511 |0.026484 3795.7 4325.4 7.2829 1000 0.038808 4017.1 4599.2 7.6378 0.033215 4010.7 4592.0 7.5616 |0.029020 4004.3 4584.7 7.4950 1100 0.042062 4227.7 4858.6 7.8339 0.036029 4222.3 4852.8 7.7588 |0.031504 4216.9 4847.0 7.6933 1200 0.045279 4443.1 5122.3 8.0192 0.038806 4438.5 5117.6 7.9449 [|0.033952 4433.8 5112.9 7.8802 1300 0.048469 4663.3 5390.3 8.1952 0.041556 4659.2 5386.5 8.1215 |0.036371 4655.2 5382.7 8.0574 P= 25.0 MPa P= 30.0 MPa P= 35.0 MPa 375 0.001978 1799.9 1849.4 4.0345 0.001792 1738.1 1791.9 3.9313 |0.001701 1702.8 1762.4 3.8724 400 0.006005 2428.5 2578.7 5.1400 0.002798 2068.9 2152.8 4.4758 [|0.002105 1914.9 1988.6 4.2144 425 0.007886 2607.8 2805.0 5.4708 0.005299 2452.9 2611.8 5.1473 |0.003434 2253.3 2373.5 4.7751 450 0.009176 2721.2 2950.6 5.6759 0.006737 2618.9 2821.0 5.4422 |0.004957 2497.5 2671.0 5.1946 500 0.011143 2887.3 3165.9 5.9643 0.008691 2824.0 3084.8 5.7956 |0.006933 2755.3 2997.9 5.6331 550 0.012736 3020.8 3339.2 6.1816 0.010175 2974.5 3279.7 6.0403 |0.008348 2925.8 3218.0 5.9093 600 0.014140 3140.0 3493.5 6.3637 0.011445 3103.4 3446.8 6.2373 |0.009523 3065.6 3399.0 6.1229 650 0.015430 3251.9 3637.7 6.5243 0.012590 3221.7 3599.4 6.4074 |0.010565 3190.9 3560.7 6.3030 700 0.016643 3359.9 3776.0 6.6702 0.013654 3334.3 3743.9 6.5599 |0.011523 3308.3 3711.6 6.4623 800 0.018922 3570.7 4043.8 6.9322 0.015628 3551.2 4020.0 6.8301 |0.013278 3531.6 3996.3 6.7409 900 0.021075 3780.2 4307.1 7.1668 0.017473 3764.6 4288.8 7.0695 |0.014904 3749.0 4270.6 6.9853 1000 0.023150 3991.5 4570.2 7.3821 0.019240 3978.6 4555.8 7.2880 |0.016450 3965.8 4541.5 7.2069 1100 0.025172 4206.1 4835.4 7.5825 0.020954 4195.2 4823.9 7.4906 |0.017942 4184.4 48124 7.4118 1200 0.027157 4424.6 5103.5 7.7710 0.022630 4415.3 5094.2 7.6807 |0.019398 4406.1 5085.0 7.6034 1300 0.029115 4647.2 5375.1 7.9494 0.024279 4639.2 5367.6 7.8602 |0.020827 4631.2 5360.2 7.7841 P= 40.0 MPa P= 50.0 MPa P= 60.0 MPa 375 0.001641 1677.0 1742.6 3.8290 0.001560 1638.6 1716.6 3.7642 |0.001503 1609.7 1699.9 3.7149 400 0.001911 1855.0 1931.4 4.1145 0.001731 1787.8 1874.4 4.0029 |0.001633 1745.2 1843.2 3.9317 425 0.002538 2097.5 2199.0 4.5044 0.002009 1960.3 2060.7 4.2746 |0.001816 1892.9 2001.8 4.1630 450 0.003692 2364.2 2511.8 4.9449 0.002487 2160.3 2284.7 4.5896 |0.002086 2055.1 2180.2 4.4140 500 0.005623 2681.6 2906.5 5.4744 0.003890 2528.1 2722.6 5.1762 |0.002952 2393.2 2570.3 4.9356 550 0.006985 2875.1 3154.4 5.7857 0.005118 2769.5 3025.4 5.5563 [|0.003955 2664.6 2901.9 5.3517 600 0.008089 3026.8 3350.4 6.0170 0.006108 2947.1 3252.6 5.8245 |0.004833 2866.8 3156.8 5.6527 650 0.009053 3159.5 3521.6 6.2078 0.006957 3095.6 3443.5 6.0373 |0.005591 3031.3 3366.8 5.8867 700 0.009930 3282.0 3679.2 6.3740 0.007717 3228.7 3614.6 6.2179 |0.006265 3175.4 3551.3 6.0814 800 0.011521 3511.8 3972.6 6.6613 0.009073 3472.2 3925.8 6.5225 |0.007456 3432.6 3880.0 6.4033 900 0.012980 3733.3 4252.5 6.9107 0.010296 3702.0 4216.8 6.7819 |0.008519 3670.9 4182.1 6.6725 1000 0.014360 3952.9 4527.3 7.1355 0.011441 3927.4 4499.4 7.0131 |0.009504 3902.0 4472.2 6.9099 1100 0.015686 4173.7 4801.1 7.3425 0.012534 4152.2 4778.9 7.2244 |0.010439 4130.9 4757.3 7.1255 1200 0.016976 4396.9 5075.9 7.5357 0.013590 4378.6 5058.1 7.4207 |0.011339 4360.5 5040.8 7.3248 1300 0.018239 4623.3 5352.8 7.7175 0.014620 4607.5 5338.5 7.6048 |0.012213 4591.8 5324.5 7.5111 922 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-7 Agua líquida comprimida T v u h s v u h s v u h s “CC méí/kg Kkíkg kJkg kJ/kg-Km/kg kJ/kg kJ/kg kJ/kg-KlmYkg kkg kJ/kg kJkg-K P = 5 MPa (263.94 *C) P= 10 MPa (311.00 *C) P= 15 MPa (342.16 *C) Sat. 0.0012862 1148.1 1154.5 2.9207 | 0.0014522 1393.3 1407.9 3.3603 |0.0016572 1585.5 1610.3 3.6848 0 0.0009977 0.04 5.03 0.0001 | 0.0009952 0.12 10.07 0.0003 |0.0009928 0.18 15.07 0.0004 20 0.0009996 83.61 88.61 0.2954 | 0.0009973 83.31 93.28 0.2943 |0.0009951 ESO A 40 0.0010057 166.92 171.95 0.5705 | 0.0010035 166.33 176.37 0.5685 |0.0010013 165.75 180.77 0.5666 60 0.0010149 250.29 255.36 0.8287 | 0.0010127 249.43 259.55 0.8260 |0.0010105 248.58 263.74 0.8234 80 0.0010267 333.82 338.96 1.0723 | 0.0010244 332.69 342.94 1.0691 |0.0010221 331.59 346.92 1.0659 100 0.0010410 417.65 422.85 1.3034 | 0.0010385 416.23 426.62 1.2996 |0.0010361 414.85 430.39 1.2958 120 0.0010576 501.91 507.19 1.5236 | 0.0010549 500.18 510.73 1.5191 |0.0010522 498.50 514.28 1.5148 140 0.0010769 586.80 592.18 1.7344 | 0.0010738 584.72 595.45 1.7293 |0.0010708 582.69 598.75 1.7243 160 0.0010988 672.55 678.04 1.9374 | 0.0010954 670.06 681.01 1.9316 |0.0010920 667.63 684.01 1.9259 180 0.0011240 759.47 765.09 2.1338 | 0.0011200 756.48 767.68 2.1271 |0.0011160 753.58 770.32 2.1206 200 0.0011531 847.92 853.68 2.3251 | 0.0011482 844.32 855.80 2.3174 |0.0011435 840.84 858.00 2.3100 220 0.0011868 938.39 944.32 2.5127 | 0.0011809 934.01 945.82 2.5037 |0.0011752 929.81 947.43 2.4951 240 0.0012268 1031.6 1037.7 2.6983 | 0.0012192 1026.2 10383 2.6876 |0.0012121 1021.00 1039.2 2.6774 260 0.0012755 1128.5 1134.9 2.8841 | 0.0012653 1121.6 11343 2.8710 |0.0012560 1115.1 1134.0 2.8586 280 0.0013226 1221.8 12350 3.0565 |0.0013096 12134 12330 3.0410 300 0.0013980 1329.4 13433 3.2488 |0.0013783 1317.6 1338.3 3.2279 320 0.0014733 14319 14540 3.4263 340 0.0016311 15679 15924 3.6555 P = 20 MPa (365.75 *C) P= 30 MPa P = 50 MPa Sat. 0.0020378 1785.8 1826.6 4.0146 0 0.0009904 0.23 20.03 0.0005 | 0.0009857 0.29 29.86 0.0003 | 0.0009767 0.29 49.13 -0.0010 20 0.0009929 82.71 102.57 0.2921 | 0.0009886 82.11 111.77 0.2897 |0.0009805 80.93 129.95 0.2845 40 0.0009992 165.17 185.16 0.5646 | 0.0009951 164.05 193.9 0.5607 |0.0009872 161.90 211.25 0.5528 60 0.0010084 247.75 267.92 0.8208 | 0.0010042 246.14 276.26 0.8156 |0.0009962 243.08 292.88 0.8055 80 0.0010199 330.50 350.90 1.0627 | 0.0010155 328.40 358.86 1.0564 |0.0010072 324.42 374.78 1.0442 100 0.0010337 413.50 434.17 1.2920 | 0.001029 410.87 441.74 1.2847 |0.0010201 405.94 456.94 1.2705 120 0.0010496 496.85 517.84 1.5105 | 0.0010445 493.66 525.00 1.5020 |0.0010349 487.69 539.43 1.4859 140 0.0010679 580.71 602.07 1.7194 | 0.0010623 576.90 608.76 1.7098 |0.0010517 569.77 622.36 1.6916 160 0.0010886 665.28 687.05 1.9203 | 0.0010823 660.74 693.21 1.9094 |0.0010704 652.33 705.85 1.8889 180 0.0011122 750.78 773.02 2.1143 | 0.0011049 745.40 778.55 2.1020 |0.0010914 735.49 790.06 2.0790 200 0.0011390 837.49 860.27 2.3027 | 0.0011304 831.11 865.02 2.2888 |0.0011149 819.45 875.19 2.2628 220 0.0011697 925.77 949.16 2.4867 | 0.0011595 918.15 952.93 2.4707 |0.0011412 904.39 961.45 2.4414 240 0.0012053 1016.1 1040.2 2.6676 | 0.0011927 1006.9 1042.7 2.6491 |0.0011708 990.55 1049.1 2.6156 260 0.0012472 1109.0 1134.0 2.8469 | 0.0012314 1097.8 1134.7 2.8250 |0.0012044 1078.2 1138.4 2.7864 280 0.0012978 1205.6 1231.5 3.0265 | 0.0012770 1191.5 12298 3.0001 |0.0012430 1167.7 1229.9 2.9547 300 0.0013611 1307.2 1334.4 3.2091 | 0.0013322 1288.9 13289 3.1761 |0.0012879 1259.6 1324.0 3.1218 320 0.0014450 1416.6 1445.5 3.3996 | 0.0014014 1391.7 1433.7 3.3558 |0.0013409 1354.3 1421.4 3.2888 340 0.0015693 1540.2 1571.6 3.6086 | 0.0014932 1502.4 1547.1 3.5438 |0.0014049 1452.9 1523.1 3.4575 360 0.0018248 1703.6 1740.1 3.8787 | 0.0016276 1626.8 1675.6 3.7499 |0.0014848 1556.5 1630.7 3.6301 380 0.0018729 1782.0 1838.2 4.0026 |0.0015884 1667.1 17465 3.8102 929 IA TABLA A-13 Refrigerante 134a sobrecalentado T v u h s v u h s v u h s “C mí/kg kíkg kJkg kg-K| mig kJkg kJkg kJ/kg-K| m?/kg kJ/kg kJ/kg kJkg-K P = 0.06 MPa (T., = -36.95 C) P = 0.10 MPa (7, = 26.37 “C) P = 0.14 MPa (7, = 18.77 C) Sat. 0.31121 209.12 227.79 0.9644 0.19254 215.19 234.44 0.9518 0.14014 219.54 239.16 0.9446 -20 0.33608 220.60 240.76 1.0174 0.19841 219.66 239.50 0.9721 -10 0.35048 227.55 248.58 1.0477 0.20743 226.75 247.49 1.0030 0.14605 225.91 246.36 0.9724 O 0.36476 234.66 256.54 1.0774 0.21630 233.95 255.58 1.0332 0.15263 233.23 254.60 1.0031 10 0.37893 241.92 264.66 1.1066 0.22506 241.30 263.81 1.0628 0.15908 240.66 262.93 1.0331 20 0.39302 249.35 272.94 1.1353 0.23373 248.79 272.17 1.0918 0.16544 248.22 271.38 1.0624 30 0.40705 256.95 281.37 1.1636 0.24233 256.44 280.68 1.1203 0.17172 255.93 279.97 1.0912 40 0.42102 264.71 289.97 1.1915 0.25088 264.25 289.34 1.1484 0.17794 263.79 288.70 1.1195 50 0.43495 272.64 298.74 1.2191 0.25937 272.22 298.16 1.1762 0.18412 271.79 297.57 1.1474 60 0.44883 280.73 307.66 1.2463 0.26783 280.35 307.13 1.2035 0.19025 279.96 306.59 1.1749 70 0.46269 288.99 316.75 1.2732 0.27626 288.64 316.26 1.2305 0.19635 288.28 315.77 1.2020 80 0.47651 297.41 326.00 1.2997 0.28465 297.08 325.55 1.2572 0.20242 296.75 325.09 1.2288 90 0.49032 306.00 335.42 1.3260 0.29303 305.69 334.99 1.2836 0.20847 305.38 334.57 1.2553 100 0.50410 314.74 344.99 1.3520 0.30138 314.46 344.60 1.3096 0.21449 314.17 344.20 1.2814 P = 0.18 MPa (T,, = -12.73 C) P = 0.20 MPa (T,,, = —10.09 “C) P = 0.24 MPa (T,,, = -5.38 C) Sat. 0.11041 222.99 242.86 0.9397 0.09987 224.48 244.46 0.9377 0.08390 227.14 247.28 0.9346 -10 0.11189 225.02 245.16 0.9484 0.09991 224.55 244.54 0.9380 O 0.11722 232.48 253.58 0.9798 0.10481 232.09 253.05 0.9698 0.08617 231.29 251.97 0.9519 10 0.12240 240.00 262.04 1.0102 0.10955 239.67 261.58 1.0004 0.09026 238.98 260.65 0.9831 20 0.12748 247.64 270.59 1.0399 0.11418 247.35 270.18 1.0303 0.09423 246.74 269.36 1.0134 30 0.13248 255.41 279.25 1.0690 0.11874 255.14 278.89 1.0595 0.09812 254.61 278.16 1.0429 40 0.13741 263.31 288.05 1.0975 0.12322 263.08 287.72 1.0882 0.10193 262.59 287.06 1.0718 50 0.14230 271.36 296.98 1.1256 0.12766 271.15 296.68 1.1163 0.10570 270.71 296.08 1.1001 60 0.14715 279.56 306.05 1.1532 0.13206 279.37 305.78 1.1441 0.10942 278.97 305.23 1.1280 70 0.1519 287.91 315.27 1.1805 0.13641 287.73 315.01 1.1714 0.11310 287.36 314.51 1.1554 80 0.15673 296.42 324.63 1.2074 0.14074 296.25 324.40 1.1983 0.11675 295.91 323.93 1.1825 90 0.16149 305.07 334.14 1.2339 0.14504 304.92 333.93 1.2249 0.12038 304.60 333.49 1.2092 100 0.16622 31388 343.80 1.2602 0.14933 313.74 343.60 1.2512 0.12398_ 313.44 343.20 1.2356 P = 0.28 MPa (T,, = -1.25 C) P = 0.32 MPa (T,,, = 2.46 C) P = 0.40 MPa (T,,, = 8.91 0) Sat. 0.07235 229.46 249.72 0.9321 0.06360 231.52 251.88 0.9301 0.051201 235.07 255.55 0.9269 0 0.07282 230.44 250.83 0.9362 10 0.07646 238.27 259.68 0.9680 0.06609 237.54 258.69 0.9544 0.051506 235.97 256.58 0.9305 20 0.07997 246.13 268.52 0.9987 0.06925 245.50 267.66 0.9856 0.054213 244.18 265.86 0.9628 30 0.08338 254.06 277.41 1.0285 0.07231 253.50 276.65 1.0157 0.056796 252.36 275.07 0.9937 40 0.08672 262.10 286.38 1.0576 0.07530 261.60 285.70 1.0451 0.059292 260.58 284.30 1.0236 50 0.09000 270.27 295.47 1.0862 0.07823 269.82 294.85 1.0739 0.061724 268.90 293.59 1.0528 60 0.09324 278.56 304.67 1.1142 0.08111 278.15 304.11 1.1021 0.064104 277.32 302.96 1.0814 70 0.09644 286.99 314.00 1.1418 0.08395 286.62 313.48 1.1298 0.066443 285.86 312.44 1.1094 80 0.09961 295.57 323.46 1.1690 0.08675 295.22 322.98 1.1571 0.068747 294.53 322.02 1.1369 90 0.10275 304.29 333.06 1.1958 0.08953 303.97 332.62 1.1840 0.071023 303.32 331.73 1.1640 100 0.10587 313.15 342.80 1.2222 0.09229 312.86 342.39 1.2105 0.073274 312.26 341.57 1.1907 110 0.10897 322.16 352.68 1.2483 0.09503 321.89 352.30 1.2367 0.075504 321.33 351.53 1.2171 120 0.11205 331.32 362.70 1.2742 0.09775 331.07 362.35 1.2626 0.077717 330.55 361.63 1.2431 130 0.11512 340.63 372.87 1.2997 0.10045 340.39 372.54 1.2882 0.079913 339.90 371.87 1.2688 140 0.11818 350.09 383.18 1.3250 0.10314 349.86 382.87 1.3135 0.082096 349.41 382.24 1.2942 930 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-13 Refrigerante 134a sobrecalentado (conclusión) Toy u h s v u h s v u h s “CC mikg kJíkg kJkg kJ/kg-K|m/kg kJkg kJkg KkJ/kg-K| mg kJ/kg kJ/kg kJ/kg-K P = 0.50 MPa (Ty = 15.71 0) P = 0.60 MPa (T,, = 21.55 “C) P = 0.70 MPa (T.,, = 26.69 C) Sat. 0.041118 238.75 259.30 0.9240 0.034295 241.83 262.40 0.9218 0.029361 244.48 265.03 0.9199 20 0.042115 242.40 263.46 0.9383 30 0.044338 250.84 273.01 0.9703 0.035984 249.22 270.81 0.9499 0.029966 247.48 268.45 0.9313 40 0.046456 259.26 282.48 1.0011 0.037865 257.86 280.58 0.9816 0.031696 256.39 278.57 0.9641 50 0.048499 267.72 291.96 1.0309 0.039659 266.48 290.28 1.0121 0.033322 265.20 288.53 0.9954 60 0.050485 276.25 301.50 1.0599 0.041389 275.15 299.98 1.0417 0.034875 274.01 298.42 1.0256 70 0.052427 284.89 311.10 1.0883 0.043069 283.89 309.73 1.0705 0.036373 282.87 308.33 1.0549 80 0.054331 293.64 320.80 1.1162 0.044710 292.73 319.55 1.0987 0.037829 291.80 318.28 1.0835 90 0.056205 302.51 330.61 1.1436 0.046318 301.67 329.46 1.1264 0.039250 300.82 328.29 1.1114 100 0.058053 311.50 340.53 1.1705 0.047900 310.73 339.47 1.1536 0.040642 309.95 338.40 1.1389 110 0.059880 320.63 350.57 1.1971 0.049458 319.91 349.59 1.1803 0.042010 319.19 348.60 1.1658 120 0.061687 329.89 360.73 1.2233 0.050997 329.23 359.82 1.2067 0.043358 328.55 358.90 1.1924 130 0.063479 339.29 371.03 1.2491 0.052519 338.67 370.18 1.2327 0.044688 338.04 369.32 1.2186 140 0.065256 348.83 381.46 1.2747 0.054027 348.25 380.66 1.2584 0.046004 347.66 379.86 1.2444 150 0.067021 358.51 392.02 1.2999 0.055522 357.96 391.27 1.2838 0.047306 357.41 390.52 1.2699 160 0.068775 368.33 402.72 1.3249 0.057006 367.81 402.01 1.3088 0.048597 367.29 401.31 1.2951 P = 0.80 MPa (T,, = 31.31 0) P = 0.90 MPa (T,, = 35.51 “C) P= 1.00 MPa (T.,, = 39.37 0) Sat. 0.025621 246.79 267.29 0.9183 0.022683 248.85 269.26 0.9169 0.020313 250.68 270.99 0.9156 40 0.027035 254.82 276.45 0.9480 0.023375 253.13 274.17 0.9327 0.020406 251.30 271.71 0.9179 50 0.028547 263.86 286.69 0.9802 0.024809 262.44 284.77 0.9660 0.021796 260.94 282.74 0.9525 60 0.029973 272.83 296.81 1.0110 0.026146 271.60 295.13 0.9976 0.023068 270.32 293.38 0.9850 70 0.031340 281.81 306.88 1.0408 0.027413 280.72 305.39 1.0280 0.024261 279.59 303.85 1.0160 80 0.032659 290.84 316.97 1.0698 0.028630 289.86 315.63 1.0574 0.025398 288.86 314.25 1.0458 90 0.033941 299.95 327.10 1.0981 0.029806 299.06 325.89 1.0860 0.026492 298.15 324.64 1.0748 100 0.035193 309.15 337.30 1.1258 0.030951 308.34 336.19 1.1140 0.027552 307.51 335.06 1.1031 110 0.036420 318.45 347.59 1.1530 0.032068 317.70 346.56 1.1414 0.028584 316.94 345.53 1.1308 120 0.037625 327.87 357.97 1.1798 0.033164 327.18 357.02 1.1684 0.029592 326.47 356.06 1.1580 130 0.038813 337.40 368.45 1.2061 0.034241 336.76 367.58 1.1949 0.030581 336.11 366.69 1.1846 140 0.039985 347.06 379.05 1.2321 0.035302 346.46 378.23 1.2210 0.031554 345.85 377.40 1.2109 150 0.041143 356.85 389.76 1.2577 0.036349 356.28 389.00 1.2467 0.032512 355.71 388.22 1.2368 160 0.042290 366.76 400.59 1.2830 0.037384 366.23 399.88 1.2721 0.033457 365.70 399.15 1.2623 170 0.043427 376.81 411.55 1.3080 0.038408 376.31 410.88 1.2972 0.034392 375.81 410.20 1.2875 180 0.044554 386.99 422.64 1.3327 0.039423 386.52 422.00 1.3221 0.035317 386.04 421.36 1.3124 P = 1.20 MPa (T,, = 46.29 0) P= 1.40 MPa (T.,, = 52.40 0) P= 1.60 MPa (T.y, = 57.88 “C) Sat. 0.016715 253.81 273.87 0.9130 0.014107 256.37 276.12 0.9105 0.012123 258.47 277.86 0.9078 50 0.017201 257.63 278.27 0.9267 60 0.018404 267.56 289.64 0.9614 0.015005 264.46 285.47 0.9389 0.012372 260.89 280.69 0.9163 70 0.019502 277.21 300.61 0.9938 0.016060 274.62 297.10 0.9733 0.013430 271.76 293.25 0.9535 80 0.020529 286.75 311.39 1.0248 0.017023 284.51 308.34 1.0056 0.014362 282.09 305.07 0.9875 90 0.021506 296.26 322.07 1.0546 0.017923 294.28 319.37 1.0364 0.015215 292.17 316.52 1.0194 100 0.022442 305.80 332.73 1.0836 0.018778 304.01 330.30 1.0661 0.016014 302.14 327.76 1.0500 110 0.023348 315.38 343.40 1.1118 0.019597 313.76 341.19 1.0949 0.016773 312.07 338.91 1.0795 120 0.024228 325.03 354.11 1.1394 0.020388 323.55 352.09 1.1230 0.017500 322.02 350.02 1.1081 130 0.025086 334.77 364.88 1.1664 0.021155 333.41 363.02 1.1504 0.018201 332.00 361.12 1.1360 140 0.025927 344.61 375.72 1.1930 0.021904 343.34 374.01 1.1773 0.018882 342.05 372.26 1.1632 150 0.026753 354.56 386.66 1.2192 0.022636 353.37 385.07 1.2038 0.019545 352.17 383.44 1.1900 160 0.027566 364.61 397.69 1.2449 0.023355 363.51 396.20 1.2298 0.020194 362.38 394.69 1.2163 170 0.028367 374.78 408.82 1.2703 0.024061 373.75 407.43 1.2554 0.020830 372.69 406.02 1.2421 180 0.029158 385.08 420.07 1.2954 0.024757 384.10 418.76 1.2807 0.021456 383.11 417.44 1.2676 934 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-17 Propiedades de gas ideal del aire Toh u S TOooh u S Ko KkJlkg P, IJ/kg y, lJ/kg - K Ko Kike P, IJ/kg vw, lJ/kg - K 200 199.97 0.3363 142.56 1707.0 1.29559 580 586.04 14.38 419.55 115.7 2.37348 210 209.97 0.3987 149.69 1512.0 1.34444 590 596.52 15.31 427.15 110.6 2.39140 220 219.97 0.4690 156.82 1346.0 1.39105 600 607.02 16.28 434.78 1058 2.40902 230 230.02 0.5477 164.00 1205.0 1.43557 610 617.53 17.30 442.42 101.2 2.42644 240 240.02 0.6355 171.13 1084.0 1.47824 620 628.07 18.36 450.09 96.92 2.44356 250 250.05 0.7329 178.28 979.0 1.51917 630 638.63 19.84 457.78 9284 2.46048 260 260.09 0.8405 185.45 887.8 1.55848 640 649.22 20.64 465.50 88.99 2.47716 270 270.11 0.9590 192.60 808.0 1.59634 650 659.84 21.86 473.25 85.34 2.49364 280 280.13 1.0889 199.75 738.0 1.63279 660 670.47 23.13 481.01 8189 2.50985 285 285.14 1.1584 203.33 706.1 1.65055 670 681.14 24.46 488.81 78.61 2.52589 290 290.16 1.2311 206.91 676.1 1.66802 680 691.82 25.85 496.62 75.50 2.54175 295 295.17 1.3068 210.49 647.9 1.68515 690 702.52 27.29 504.45 72.56 2.55731 298 298.18 1.3543 212.64 631.9 1.69528 700 713.27 28.80 512.33 69.76 2.57277 300 300.19 1.3860 214.07 621.2 1.70203 710 724.04 30.38 520.23 67.07 2.5810 305 305.22 1.4686 217.67 596.0 1.71865 720 734.82 32.02 528.14 64.53 2.60319 310 310.24 1.5546 221.25 572.3 1.73498 730 745.62 33.72 536.07 62.13 2.61803 315 315.27 1.6442 22485 549.8 1.75106 740 756.44 35.50 544.02 59.82 2.63280 320 320.29 1.7375 228.42 528.6 1.76690 750 767.29 37.35 551.99 57.63 2.64737 325 325.31 1.8345 232.02 508.4 1.78249 760 778.18 39.27 560.01 55.54 2.66176 330 330.34 1.9352 235.61 489.4 1.79783 780 800.03 43.35 576.12 51.64 2.69013 340 340.42 2.149 24282 454.1 1.82790 800 821.95 47.75 592.30 48.08 2.71787 350 350.49 2.379 250.02 422.2 1.85708 820 843.98 52.59 608.59 44.84 2.74504 360 360.58 2.626 257.24 393.4 1.88543 840 866.08 57.60 624.95 4185 2.77170 370 370.67 2.892 264.46 367.2 1.91313 860 888.27 63.09 641.40 39.12 2.79783 380 380.77 3.176 271.69 343.4 1.94001 880 910.56 68.98 657.95 36.61 2.82344 390 390.88 3.481 278.93 321.5 1.96633 900 932.93 75.29 674.58 34.31 2.84856 400 400.98 3.806 286.16 301.6 1.99194 920 955.38 82.05 691.28 32.18 2.87324 410 411.12 4.153 293.43 283.3 2.01699 940 977.92 89.28 708.08 30.22 2.89748 420 421.26 4.522 300.69 266.6 2.04142 960 1000.55 97.00 725.02 28.40 2.92128 430 431.43 4.915 307.99 251.1 2.06533 980 1023.25 105.2 74198 26.73 2.94468 440 441.61 5.332 315.30 236.8 2.08870 |1000 1046.04 114.0 758.94 25.17 2.96770 450 451.80 5.775 322.62 223.6 2.11161 [1020 1068.89 123.4 776.10 23.72 2.99034 460 462.02 6.245 329.97 211.4 2.13407 [1040 1091.85 133.3 793.36 23.29 3.01260 470 472.24 6.742 337.32 200.1 2.15604 [1060 1114.86 143.9 810.62 21.14 3.03449 480 482.49 7.268 344.70 189.5 2.17760 [1080 1137.89 155.2 827.88 19.98 3.05608 490 492.74 7.824 352.08 179.7 2.19876 |1100 1161.07 167.1 845.33 18.896 3.07732 500 503.02 8.411 359.49 170.6 2.21952 [1120 1184.28 179.7 862.79 17.886 3.09825 510 513.32 9.031 366.92 162.1 2.23993 [1140 1207.57 193.1 880.35 16.946 3.11883 520 523.63 9.684 374.36 154.1 2.25997 [1160 1230.92 207.2 897.91 16.064 3.13916 530 533.98 10.37 381.84 146.7 2.27967 [1180 1254.34 222.2 915.57 15.241 3.15916 540 544.35 11.10 389.34 139.7 2.29906 |1200 1277.79 238.0 933.33 14.470 3.17888 550 555.74 11.88 396.86 133.1 2.31809 [1220 1301.31 254.7 951.09 13.747 3.19834 560 565.17 12.66 404.42 127.0 2.33685 |1240 1324.93 272.3 968.95 13.069 3.21751 570 575.59 13.50 411.97 121.2 2.35531 TABLA A-18 Propiedades de gas ¡deal del nitrógeno, Na (conclusión) T h u ES T h u ES K kJ/kmol kJ/kmol KkJ/kmol - K K kJ/kmol kJ/kmol kJ/kmol - K 1000 30,129 21,815 228.057 1760 56,227 41,594 247.396 1020 30,784 22,304 228.706 1780 56,938 42,139 247.798 1040 31,442 22,795 229.344 1800 57,651 42,685 248.195 1060 32,101 23,288 229.973 1820 58,363 43,231 248.589 1080 32,762 23,782 230.591 1840 59,075 43,777 248.979 1100 33,426 24,280 231.199 1860 59,790 44,324 249.365 1120 34,092 24,780 231.799 1880 60,504 44,873 249.748 1140 34,760 25,282 232.391 1900 61,220 45,423 250.128 1160 35,430 25,786 232.973 1920 61,936 45,973 250.502 1180 36,104 26,291 233.549 1940 62,654 46,524 250.874 1200 36,777 26,799 234.115 1960 63,381 47,075 251.242 1220 37,452 27,308 234.673 1980 64,090 47,627 251.607 1240 38,129 27,819 235.223 2000 64,810 48,181 251.969 1260 38,807 28,331 235.166 2050 66,612 49,567 252.858 1280 39,488 28,845 236.302 2100 68,417 50,957 253.726 1300 40,170 29,361 236.831 2150 70,226 52,351 254.578 1320 40,853 29,378 237.353 2200 72,040 53,749 255.412 1340 41,539 30,398 237.867 2250 73,856 55,149 256.227 1360 42,227 30,919 238.376 2300 75,676 56,553 257.027 1380 42,915 31,441 238.878 2350 77,496 57,958 257.810 1400 43,605 31,964 239.375 2400 79,320 59,366 258.580 1420 44,295 32,489 239.865 2450 81,149 60,779 259.332 1440 44,988 33,014 240.350 2500 82,981 62,195 260.073 1460 45,682 33,543 240.827 2550 84,814 63,613 260.799 1480 46,377 34,071 241.301 2600 86,650 65,033 261.512 1500 47,073 34,601 241.768 2650 88,488 66,455 262.213 1520 47,771 35,133 242.228 2700 90,328 67,880 262.902 1540 48,470 35,665 242.685 2750 92,171 69,306 263.577 1560 49,168 36,197 243.137 2800 94,014 70,734 264.241 1580 49,869 36,732 243.585 2850 95,859 72,163 264.895 1600 50,571 37,268 244.028 2900 97,705 73,593 265.538 1620 51,275 37,806 244.464 2950 99,556 75,028 266.170 1640 51,980 38,344 244.896 3000 101,407 76,464 266.793 1660 52,686 38,884 245.324 3050 103,260 77,902 267.404 1680 53,393 39,424 245.747 3100 105,115 79,341 268.007 1700 54,099 39,965 246.166 3150 106,972 80,782 268.601 1720 54,807 40,507 246.580 3200 108,830 82,224 269.186 1740 55,516 41,049 246.990 3250 110,690 83,668 269.763 Fuente: Las tablas A-18 a A-25 fueron adaptadas de Kenneth Wark, Thermodynamics, 4a. ed., Nueva York, McGraw-Hill, 1983, pp. 787-798. Publicadas originalmente en JANAF, Thermochemical Tables, NSRDS-NBS-37, 1971. 938 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-19 Propiedades de gas ideal del oxígeno, O, T h u Ss T h u ES K kJ/kmol kJ/kmol kJ/kmol - K K kJ/kmol kJ/kmol kJ/kmol-K 0 0 0 0 600 17,929 12,940 226.346 220 6,404 4,575 196.171 610 18,250 13,178 226.877 230 6,694 4,782 197.461 620 18,572 13,417 227.400 240 6,984 4,989 198.696 630 18,895 13,657 227.918 250 7,275 5,197 199.885 640 19,219 13,898 228.429 260 7,566 5,405 201.027 650 19,544 14,140 228.932 270 7,858 5,613 202.128 660 19,870 14,383 229.430 280 8,150 5,822 203.191 670 20,197 14,626 229.920 290 8,443 6,032 204.218 680 20,524 14,871 230.405 298 8,682 6,203 205.033 690 20,854 15,116 230.885 300 8,736 6,242 205.213 700 21,184 15,364 231.358 310 9,030 6,453 206.177 710 21,514 15,611 231.827 320 9,325 6,664 207.112 720 21,845 15,859 232.291 330 9,620 6,877 208.020 730 22,177 16,107 232.748 340 9,916 7,090 208.904 740 22,510 16,357 233.201 350 10,213 7,303 209.765 750 22,844 16,607 233.649 360 10,511 7,518 210.604 760 23,178 16,859 234.091 370 10,809 7,733 211.423 770 23,513 17,111 234.528 380 11,109 7,949 212.222 780 23,850 17,364 234.960 390 11,409 8,166 213.002 790 24,186 17,618 235.387 400 11,711 8,384 213.765 800 24,523 17,872 235.810 410 12,012 8,603 214.510 810 24,861 18,126 236.230 420 12,314 8,822 215.241 820 25,199 18,382 236.644 430 12,618 9,043 215.955 830 25,537 18,637 237.055 440 12,923 9,264 216.656 840 25,877 18,893 237.462 450 13,228 9,487 217.342 850 26,218 19,150 237.864 460 13,525 9,710 218.016 860 26,559 19,408 238.264 470 13,842 9,935 218.676 870 26,899 19,666 238.660 480 14,151 10,160 219.326 880 27,242 19,925 239.051 490 14,460 10,386 219.963 890 27,584 20,185 239.439 500 14,770 10,614 220.589 900 27,928 20,445 239.823 510 15,082 10,842 221.206 910 28,272 20,706 240.203 520 15,395 11,071 221.812 920 28,616 20,967 240.580 530 15,708 11,301 222.409 930 28,960 21,228 240.953 540 16,022 11,533 222.997 940 29,306 21,491 241.323 550 16,338 11,765 223.576 950 29,652 21,754 241.689 560 16,654 11,998 224.146 960 29,999 22,017 242.052 570 16,971 12,232 224.708 970 30,345 22,280 242.411 580 17,290 12,467 225.262 980 30,692 22,544 242.768 590 17,609 12,703 225.808 990 31,041 22,809 242.120 TABLA A-19 Propiedades de gas ideal del oxígeno, O, (conclusión) T h u ES T h u ES K kJ/kmol kJ/kmol kJ/kmol -K K kJ/kmol kJ/kmol kJ/kmol - K 1000 31,389 23,075 243.471 1760 58,880 44,247 263.861 1020 32,088 23,607 244.164 1780 59,624 44,825 264.283 1040 32,789 24,142 244.844 1800 60,371 45,405 264.701 1060 33,490 24,677 245.513 1820 61,118 45,986 265.113 1080 34,194 25,214 246.171 1840 61,866 46,568 265.521 1100 34,899 25,753 246.818 1860 62,616 47,151 265.925 1120 35,606 26,294 247.454 1880 63,365 47,734 266.326 1140 36,314 26,836 248.081 1900 64,116 48,319 266.722 1160 37,023 27,379 248.698 1920 64,868 48,904 267.115 1180 37,734 27,923 249.307 1940 65,620 49,490 267.505 1200 38,447 28,469 249.906 1960 66,374 50,078 267.891 1220 39,162 29,018 250.497 1980 67,127 50,665 268.275 1240 39,877 29,568 251.079 2000 67,881 51,253 268.655 1260 40,594 30,118 251.653 2050 69,772 52,727 269.588 1280 41,312 30,670 252.219 2100 71,668 54,208 270.504 1300 42,033 31,224 252.176 2150 73,573 55,697 271.399 1320 42,753 31,778 253.325 2200 75,484 57,192 272.278 1340 43,475 32,334 253.868 2250 77,397 58,690 273.136 1360 44,198 32,891 254.404 2300 79,316 60,193 273.891 1380 44,923 33,449 254.932 2350 81,243 61,704 274.809 1400 45,648 34,008 255.454 2400 83,174 63,219 275.625 1420 46,374 34,567 255.968 2450 85,112 64,742 276.424 1440 47,102 35,129 256.475 2500 87,057 66,271 277.207 1460 47,831 35,692 256.978 2550 89,004 67,802 277.979 1480 48,561 36,256 257.474 2600 90,956 69,339 278.738 1500 49,292 36,821 257.965 2650 92,916 70,883 279.485 1520 50,024 37,387 258.450 2700 94,881 72,433 280.219 1540 50,756 37,952 258.928 2750 96,852 73,987 280.942 1560 51,490 38,520 259.402 2800 98,826 75,546 281.654 1580 52,224 39,088 259.870 2850 100,808 77,112 282.357 1600 52,961 39,658 260.333 2900 102,793 78,682 283.048 1620 53,696 40,227 260.791 2950 104,785 80,258 283.728 1640 54,434 40,799 261.242 3000 106,780 81,837 284.399 1660 55,172 41,370 261.690 3050 108,778 83,419 285.060 1680 55,912 41,944 262.132 3100 110,784 85,009 285.713 1700 56,652 42,517 262.571 3150 112,795 86,601 286.355 1720 57,394 43,093 263.005 3200 114,809 88,203 286.989 1740 58,136 43,669 263.435 3250 116,827 89,804 287.614 942 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-21 Propiedades de gas ideal del monóxido de carbono, CO T h u so T h u ES K kJ/kmol kJ/kmol kJ/kmol - K K kJ/kmol kJ/kmol kJ/kmol - K 0 0 0 0 600 17,611 12,622 218.204 220 6,391 4,562 188.683 610 17,915 12,843 218.708 230 6,683 4,771 189.980 620 18,221 13,066 219.205 240 6,975 4,979 191.221 630 18,527 13,289 219.695 250 7,266 5,188 192.411 640 18,833 13,512 220.179 260 7,558 5,396 193.554 650 19,141 13,736 220.656 270 7,849 5,604 194.654 660 19,449 13,962 221.127 280 8,140 5,812 195.713 670 19,758 14,187 221.592 290 8,432 6,020 196.735 680 20,068 14,414 222.052 298 8,669 6,190 197.543 690 20,378 14,641 222.505 300 8,723 6,229 197.723 700 20,690 14,870 222.953 310 9,014 6,437 198.678 710 21,002 15,099 223.396 320 9,306 6,645 199.603 720 21,315 15,328 223.833 330 9,597 6,854 200.500 730 21,628 15,558 224.265 340 9,889 7,062 201.371 740 21,943 15,789 224.692 350 10,181 7,271 202.217 750 22,258 16,022 225.115 360 10,473 7,480 203.040 760 22,573 16,255 225.533 370 10,765 7,689 203.842 770 22,890 16,488 225.947 380 11,058 7,899 204.622 780 23,208 16,723 226.357 390 11,351 8,108 205.383 790 23,526 16,957 226.762 400 11,644 8,319 206.125 800 23,844 17,193 227.162 410 11,938 8,529 206.850 810 24,164 17,429 227.559 420 12,232 8,740 207.549 820 24,483 17,665 227.952 430 12,526 8,951 208.252 830 24,803 17,902 228.339 440 12,821 9,163 208.929 840 25,124 18,140 228.724 450 13,116 9,375 209.593 850 25,446 18,379 229.106 460 13,412 9,587 210.243 860 25,768 18,617 229.482 470 13,708 9,800 210.880 870 26,091 18,858 229.856 480 14,005 10,014 211.504 880 26,415 19,099 230.227 490 14,302 10,228 212.117 890 26,740 19,341 230.593 500 14,600 10,443 212.719 900 27,066 19,583 230.957 510 14,898 10,658 213.310 910 27,392 19,826 231.317 520 15,197 10,874 213.890 920 27,719 20,070 231.674 530 15,497 11,090 214.460 930 28,046 20,314 232.028 540 15,797 11,307 215.020 940 28,375 20,559 232.379 550 16,097 11,524 215.572 950 28,703 20,805 232.127 560 16,399 11,743 216.115 960 29,033 21,051 233.072 570 16,701 11,961 216.649 970 29,362 21,298 233.413 580 17,003 12,181 217.175 980 29,693 21,545 233.752 590 17,307 12,401 217.693 990 30,024 21,793 234.088 TABLA A-21 Propiedades de gas ideal del monóxido de carbono, CO (conclusión) T h u ES T h u ES K kJ/kmol kJ/kmol kJ/kmol - K K kJ/kmol kJ/kmol kJ/kmol - K 1000 30,355 22,041 234.421 1760 56,756 42,123 253.991 1020 31,020 22,540 235.079 1780 57,473 42,673 254.398 1040 31,688 23,041 235.728 1800 58,191 43,225 254.797 1060 32,357 23,544 236.364 1820 58,910 43,778 255.194 1080 33,029 24,049 236.992 1840 59,629 44,331 255.587 1100 33,702 24,557 237.609 1860 60,351 44,886 255.976 1120 34,377 25,065 238.217 1880 61,072 45,441 256.361 1140 35,054 25,575 238.817 1900 61,794 45,997 256.743 1160 35,733 26,088 239.407 1920 62,516 46,552 257.122 1180 36,406 26,602 239.989 1940 63,238 47,108 257.497 1200 37,095 27,118 240.663 1960 63,961 47,665 257.868 1220 37,780 27,637 241.128 1980 64,684 48,221 258.236 1240 38,466 28,426 241.686 2000 65,408 48,780 258.600 1260 39,154 28,678 242.236 2050 67,224 50,179 259.494 1280 39,844 29,201 242.780 2100 69,044 51,584 260.370 1300 40,534 29,725 243.316 2150 70,864 52,988 261.226 1320 41,226 30,251 243.844 2200 72,688 54,396 262.065 1340 41,919 30,778 244.366 2250 74,516 55,809 262.887 1360 42,613 31,306 244.880 2300 76,345 57,222 263.692 1380 43,309 31,836 245.388 2350 78,178 58,640 264.480 1400 44,007 32,367 245.889 2400 80,015 60,060 265.253 1420 44,707 32,900 246.385 2450 81,852 61,482 266.012 1440 45,408 33,434 246.876 2500 83,692 62,906 266.755 1460 46,110 33,971 247.360 2550 85,537 64,335 267.485 1480 46,813 34,508 247.839 2600 87,383 65,766 268.202 1500 47,517 35,046 248.312 2650 89,230 67,197 268.905 1520 48,222 35,584 248.778 2700 91,077 68,628 269.596 1540 48,928 36,124 249.240 2750 92,930 70,066 270.285 1560 49,635 36,665 249.695 2800 94,784 71,504 270.943 1580 50,344 37,207 250.147 2850 96,639 72,945 271.602 1600 51,053 37,750 250.592 2900 98,495 74,383 272.249 1620 51,763 38,293 251.033 2950 100,352 75,825 272.884 1640 52,472 38,837 251.470 3000 102,210 77,267 273.508 1660 53,184 39,382 251.901 3050 104,073 78,715 274.123 1680 53,895 39,927 252.329 3100 105,939 80,164 274.730 1700 54,609 40,474 252.751 3150 107,802 81,612 275.326 1720 55,323 41,023 253.169 3200 109,667 83,061 275.914 1740 56,039 41,572 253.582 3250 111,534 84,513 276.494 944 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-22 Propiedades de gas ideal del hidrógeno, Hz T h u so T h u ES K kJ/kmol kJ/kmol KJ/kmol - K K kJ/kmol kJ/kmol kJ/kmol-K 0 0 0 0 1440 42,808 30,835 177.410 260 7,370 5,209 126.636 1480 44,091 31,786 178.291 270 7,657 5,412 127.719 1520 45,384 32,746 179.153 280 7,945 5,617 128.765 1560 46,683 33,713 179.995 290 8,233 5,822 129.775 1600 47,990 34,687 180.820 298 8,468 5,989 130.574 1640 49,303 35,668 181.632 300 8,522 6,027 130.754 1680 50,622 36,654 182.428 320 9,100 6,440 132.621 1720 51,947 37,646 183.208 340 9,680 6,853 134.378 1760 53,279 38,645 183.973 360 10,262 7,268 136.039 1800 54,618 39,652 184.724 380 10,843 7,684 137.612 1840 55,962 40,663 185.463 400 11,426 8,100 139.106 1880 57,311 41,680 186.190 420 12,010 8,518 140.529 1920 58,668 42,705 186.904 440 12,594 8,936 141.888 1960 60,031 43,735 187.607 460 13,179 9,355 143.187 2000 61,400 44,771 188.297 480 13,764 9,773 144.432 2050 63,119 46,074 189.148 500 14,350 10,193 145.628 2100 64,847 47,386 189.979 520 14,935 10,611 146.775 2150 66,584 48,708 190.796 560 16,107 11,451 148.945 2200 68,328 50,037 191.598 600 17,280 12,291 150.968 2250 70,080 51,373 192.385 640 18,453 13,133 152.863 2300 71,839 52,716 193.159 680 19,630 13,976 154.645 2350 73,608 54,069 193.921 720 20,807 14,821 156.328 2400 75,383 55,429 194.669 760 21,988 15,669 157.923 2450 77,168 56,798 195.403 800 23,171 16,520 159.440 2500 78,960 58,175 196.125 840 24,359 17,375 160.891 2550 80,755 59,554 196.837 880 25,551 18,235 162.277 2600 82,558 60,941 197.539 920 26,747 19,098 163.607 2650 84,368 62,335 198.229 960 27,948 19,966 164.884 2700 86,186 63,737 198.907 1000 29,154 20,839 166.114 2750 88,008 65,144 199.575 1040 30,364 21,717 167.300 2800 89,838 66,558 200.234 1080 31,580 22,601 168.449 2850 91,671 67,976 200.885 1120 32,802 23,490 169.560 2900 93,512 69,401 201.527 1160 34,028 24,384 170.636 2950 95,358 70,831 202.157 1200 35,262 25,284 171.682 3000 97,211 72,268 202.778 1240 36,502 26,192 172.698 3050 99,065 73,707 203.391 1280 37,749 27,106 173.687 3100 100,926 75,152 203.995 1320 39,002 28,027 174.652 3150 102,793 76,604 204.592 1360 40,263 28,955 175.593 3200 104,667 78,061 205.181 1400 41,530 29,889 176.510 3250 106,545 79,523 205.765 948 AAA TABLA A-26 Entalpía de formación, función de Gibbs de formación y entropía absoluta a25%C, l atm y 5 se Sustancia Fórmula kJ/kmol kJ/kmol kJ/kmol - K Acetileno CaHa(8) +226,730 +209,170 200.85 Agua H20(£) 285,830 237,180 69.92 Alcohol etílico C¿H¿0H(g) 235,310 -168,570 282.59 Alcohol etílico C¿H¿0H(£) 277,690 -174,890 160.70 Alcohol metílico CH¿0H(g) 200,670 - 162,000 239.70 Alcohol metílico CH¿0H(£) -238,660 - 166,360 126.80 Amoniaco NHx(8g) 46,190 16,590 192.33 Benceno CóHalg) +82,930 +129,660 269.20 n-butano CaHiolg) 126,150 -15,710 310.12 Carbón C(s) 0 0 5.74 Dióxido de carbono COz(g) 393,520 394,360 213.80 n-dodecano Ci2Hos(8) -291,010 +50,150 622.83 Etano CoHa(8) -84,680 -32,890 229.49 Etileno CoHa(8) +52,280 +68,120 219.83 Hidrógeno Hg) 0 0 130.68 Hidrógeno Hg +218,000 +203,290 114.72 Hidroxilo 0H(g) +39,460 +34,280 183.70 Metano CHa(8) 74,850 50,790 186.16 Monóxido de carbono CO(g) -110,530 -137,150 197.65 Nitrógeno N8) 0 0 191.61 Nitrógeno N(g +472,650 +455,510 153.30 n-octano CaHys(8) 208,450 +16,530 466.73 n-octano CsHysl£) 249,950 +6,610 360.79 Oxígeno 028) 0 O 205.04 Oxígeno 0(g) +249,190 +231,770 161.06 Peróxido de hidrógeno H¿0,(g) -136,310 - 105,600 232.63 Propano CaHa(g) 103,850 23,490 269.91 Propileno CaHá(8) +20,410 +62,720 266.94 Vapor de agua H20(8) -241,820 228,590 188.83 Fuente: De JANAF, Thermochemical Tables, Midland, MI, Dow Chemical Co., 1971, Selected Values of Chemical Thermodynamic Properties, NBS Technical Note 270-3, 1968; y AP/ Research Project 44, Carnegie Press, 1953.. 964 AAA TABLA A-4E Agua saturada. Tabla de temperaturas Volumen específico, Energía interna, Entalpía, Entropía, fé/bm Btu/lbm Btu/lom Btu/lbm - R Pres. Líg. Vapor Líg. Vapor LíQ. Vapor — LíQ. Vapor Temp., — Sat., sal., sal., sal., Evap.. Sat, sal., Evap., — Sal, sat., Evap., — Sat, TF Ppsia y A Y Ug Y hy Mg Ma Ss, Sy S; 32.018 0.08871 0.01602 3299.9 0.000 10210 1021.00 0.000 1075.2 1075.2 0.00000 2.18672 2.1867 35 0.09998 0.01602 2945.7 3.004 10190 10220 3.004 1073.5 1076.5 0.00609 2.17011 2.1762 40 0.12173 0.01602 2443.6 8.032 1015.6 1023.7 8.032 1070.7 1078.7 0.01620 2.14271 2.1589 45 0.14756 0.01602 2035.8 13.05 10122 10253 13.05 1067.8 1080.9 0.02620 2.11587 2.1421 50 0.17812 0.01602 1703.1 18.07 1008.99 1026.9 18.07 1065.0 1083.1 0.03609 2.08956 2.1256 55 0.21413 0.01603 1430.4 23.07 10055 1028.6 23.07 1062.2 1085.3 0.04586 2.06377 2.1096 60 0.25638 0.01604 1206.1 28.08 10021 1030.2 28.08 1059.4 1087.4 0.05554 2.03847 2.0940 65 0.30578 0.01604 1020.8 33.08 998.76 1031.8 33.08 1056.5 1089.6 0.06511 2.01366 2.0788 70 0.36334 0.01605 867.18 38.08 995.39 1033.5 38.08 1053.7 1091.8 0.07459 1.98931 2.0639 75 0.43016 0.01606 739.27 43.07 992.02 1035.1 43.07 1050.9 1093.9 0.08398 1.96541 2.0494 80 0.50745 0.01607 632.41 48.06 988.65 1036.7 48.07 1048.0 1096.1 0.09328 1.94196 2.0352 85 0.59659 0.01609 542.80 53.06 985.28 1038.3 53.06 1045.2 1098.3 0.10248 1.91892 2.0214 90 0.69904 0.01610 467.40 58.05 981.90 1040.0 58.05 1042.4 1100.4 0.11161 1.89630 2.0079 95 0.81643 0.01612 403.74 63.04 978.52 1041.6 63.04 1039.5 1102.6 0.12065 1.87408 1.9947 100 0.95052 0.01613 349.83 68.03 975.14 1043.2 68.03 1036.7 1104.7 0.12961 1.85225 1.9819 110 1.2767 0.01617 264.96 78.01 968.36 1046.4 78.02 1031.0 1109.0 0.14728 1.80970 1.9570 120 1.6951 0.01620 202.94 88.00 961.56 1049.6 88.00 1025.2 1113.2 0.16466 1.76856 1.9332 130 2.2260 0.01625 157.09 97.99 954.73 1052.7 97.99 10194 1117.4 0.18174 1.72877 1.9105 140 28931 0.01629 12281 107.98 947.87 1055.99 107.99 1013.66 1121.6 0.19855 1.69024 1.8888 150 3.7234 0.01634 96.929 117.98 940.98 1059.0 117.99 1007.8 1125.7 0.21508 1.65291 1.8680 160 4.7474 0.01639 77.185 127.98 934.05 1062.00 128.00 10018 11298 0.23136 1.61670 1.8481 170 5.9999 —0.01645 61.982 138.00 927.08 1065.1 138.02 995.88 1133.9 0.24739 1.58155 1.8289 180 7.5197 0.01651 50.172 148.02 920.06 1068.1 148.04 989.85 1137.9 0.26318 1.54741 1.8106 190 9.3497 0.01657 40.920 158.05 912.99 10710 158.08 983.76 1141.8 0.27874 1.51421 1.7930 200 11.538 0.01663 33.613 168.10 905.87 10740 168.13 977.60 1145.7 0.29409 1.48191 1.7760 210 14.136 0.01670 27.798 178.15 898.68 10768 178.20 971.35 1149.5 0.30922 1.45046 1.7597 212 14.709 0.01671 26.782 180.16 897.24 10774 180.21 970.09 1150.3 0.31222 1.44427 1.7565 220 17.201 0.01677 23.136 188.22 891.43 10796 188.28 965.02 1153.3 0.32414 1.41980 1.7439 230 20.795 0.01684 19.374 198.31 884.10 1082.44 198.37 958.59 1157.0 0.33887 1.38989 1.7288 240 24.985 0.01692 16.316 208.41 876.70 1085.1 208.49 952.06 1160.5 0.35342 1.36069 1.7141 250 29.844 0.01700 13816 218.54 869.21 1087.7 218.63 945.41 1164.0 0.36779 1.33216 1.6999 260 35.447 0.01708 11.760 228.68 861.62 109.3 228.79 938.65 1167.4 0.38198 1.30425 1.6862 270 41.877 0.01717 10.059 238.85 853.94 10928 238.98 931.76 1170.7 0.39601 1.27694 1.6730 280 49.222 0.01726 8.6439 249.04 846.16 1095.2 249.20 924.74 1173.9 0.40989 1.25018 1.6601 290 57.573 0.01735 7.4607 259.26 838.27 10975 259.45 917.57 1177.0 0.42361 1.22393 1.6475 300 67.028 0.01745 6.4663 269.51 830.25 10998 269.73 910.24 1180.0 0.43720 1.19818 1.6354 310 77.691 0.01755 5.6266 279.79 822.11 11019 280.05 902.75 1182.8 0.45065 1.17289 1.6235 320 89.667 0.01765 4.9144 290.11 813.84 11040 290.40 895.09 1185.5 0.46396 1.14802 1.6120 330 103.07 0.01776 4.3076 300.46 805.43 1105.9 300.80 887.25 1188.1 0.47716 1.12355 1.6007 340 118.02 0.01787 3.7885 310.85 796.87 1107.7 311.24 879.22 1190.5 0.49024 1.09945 1.5897 350 134.63 0.01799 3.3425 321.29 788.16 11094 321.73 870.98 1192.7 0.50321 1.07570 1.5789 360 153.03 0.01811 2.9580 331.76 779.28 11110 332.28 862.53 119.8 0.51607 1.05227 1.5683 370 173.36 0.01823 2.6252 342.29 770.23 11125 342.88 853.86 1196.7 0.52884 1.02914 1.5580 380 195.74 0.01836 2.3361 352.87 761.00 11139 353.53 844.96 1198.5 0.54152 1.00628 1.5478 390 220.33 0.01850 2.0842 363.50 751.58 1115.1 364.25 835.81 1200.1 0.55411 0.98366 1.5378 965 TABLA A-4E Agua saturada. Tabla de temperaturas (conclusión) Volumen específico, Energía interna, Entalpía, Entropía, fé/lom Btu/lbm Btu/lbm. Btu/lbm - R Pres. Líg. Vapor — Líg. Vapor Líg. Vapor Líg. Vapor Temp., Sat., sal., sal., sal., Evap., — Sat, sal., Evap., — Sat., sal., Evap., sat, TF Popsia v, Uy Y Ug Y hy Mg Mg Ss, Sy Sy 400 247.26 0.01864 1.8639 374.19 741.97 1116.2 375.04 826.39 1201.4 0.56663 0.96127 1.5279 410 276.69 0.01878 1.6706 384.94 732.14 1117.1 385.90 816.71 1202.6 0.57907 0.93908 1.5182 420 308.76 0.01894 1.5006 395.76 722.08 1117.8 396.84 806.74 1203.6 0.59145 0.91707 1.5085 430 343.64 0.01910 1.3505 406.65 71180 11184 407.86 796.46 1204.3 0.60377 0.89522 1.4990 440 381.49 0.01926 1.2178 417.61 701.26 11189 418.97 785.87 1204.8 0.61603 0.87349 1.4895 450 422.47 0.01944 1.0999 428.66 690.47 11191 430.18 774.94 1205.1 0.62826 0.85187 1.4801 460 466.75 0.01962 0.99510 439.79 679.39 11192 441.48 763.65 1205.1 0.64044 0.83033 1.4708 470 514.52 0.01981 0.90158 451.01 668.02 11190 452.90 751.98 1204.9 0.65260 0.80885 1.4615 480 565.96 0.02001 0.81794 462.34 656.34 1118.7 464.43 739.91 1204.3 0.66474 0.78739 1.4521 490 621.24 0.02022 0.74296 473.77 644.32 11181 476.09 727.40 1203.5 0.67686 0.76594 1.4428 500 680.56 0.02044 0.67558 485.32 631.94 1117.3 487.89 714.44 1202.3 0.68899 0.74445 1.4334 510 744.11 0.02067 0.61489 496.99 619.17 1116.2 499.84 700.99 1200.8 0.70112 0.72290 1.4240 520 812.11 0.02092 0.56009 508.80 605.99 11148 511.94 687.01 1199.0 0.71327 0.70126 1.4145 530 884.74 0.02118 0.51051 520.76 592.35 1113.1 524.23 672.47 1196.7 0.72546 0.67947 1.4049 540 962.24 0.02146 0.46553 532.88 578.23 1111.1 536.70 657.31 1194.0 0.73770 0.65751 1.3952 550 1044.8 0.02176 0.42465 545.18 563.58 1108.8 549.39 641.47 1190.9 0.75000 0.63532 1.3853 560 1132.7 0.02207 0.38740 557.68 548.33 1106.0 562.31 624.91 1187.2 0.76238 0.61284 1.3752 570 1226.2 0.02242 0.35339 570.40 532.45 11028 575.49 607.55 1183.0 0.77486 0.59003 1.3649 580 1325.5 0.02279 0.32225 583.37 515.84 1099.2 588.95 589.29 1178.2 0.78748 0.56679 1.3543 590 1430.8 0.02319 0.29367 596.61 498.43 1095.0 602.75 570.04 11728 0.80026 0.54306 1.3433 600 1542.5 0.02362 0.26737 610.18 480.10 1090.3 616.92 549.67 1166.6 0.81323 0.51871 1.3319 610 1660.9 0.02411 0.24309 624.11 460.73 1084.8 631.52 528.03 1159.5 0.82645 0.49363 1.3201 620 1786.2 0.02464 0.22061 638.47 440.14 1078.6 646.62 504.92 1151.5 0.83998 0.46765 1.3076 630 1918.9 0.02524 0.19972 653.35 418.12 10715 662.32 480.07 1142.4 0.85389 0.44056 1.2944 640 2059.3 0.02593 0.18019 668.86 394.36 1063.2 678.74 453.14 1131.9 0.86828 0.41206 1.2803 650 2207.8 0.02673 0.16184 685.16 368.44 1053.6 696.08 423.65 1119.7 0.88332 0.38177 1.2651 660 2364.9 0.02767 0.14444 702.48 339.74 10422 714.59 390.84 1105.4 0.89922 0.34906 1.2483 670 2531.2 0.02884 0.12774 721.23 307.22 1028.5 734.74 353.54 1088.3 0.91636 0.31296 1.2293 680 2707.3 0.03035 0.11134 742.11 269.00 10111 757.32 309.57 1066.9 0.93541 0.27163 1.2070 690 2894.1 0.03255 0.09451 766.81 220.77 987.6 784.24 253.96 1038.2 0.95797 0.22089 1.1789 700 3093.0 0.03670 0.07482 801.75 146.50 948.3 822.76 168.32 991.1 0.99023 0.14514 1.1354 705.10 3200.1 0.04975 0.04975 866.61 0 866.6 896.07 0 896.1 1.05257 0 1.0526 Fuente: Las tablas A-4E a A-SE fueron generadas utilizando el programa para resolver ecuaciones de ingeniería (EES) desarrollado por S. A. Klein y F. L. Alvarado. La rutina utilizada en los cálculos es la altamente precisa Steam_IAPWS, que incorpora la Formulación 1995 para las Propiedades Termodi- námicas de la Sustancia Agua Ordinaria para Uso Científico y General, editada por The Intemational Association for the Properties of Water and Steam (LAPWS). Esta formulación reemplaza a la de 1984 de Haar, Gallagher y Kell (NBS/NRC Steam Tables, Hemisphere Publishing Co., 1984), la_cual está también disponible en EES como la rutina STEAM. La nueva formulación se basa en las correlaciones de Saul y Wagner (1. Phys. Chem. Ref. Data, 16, 893, 1987) con modificaciones para ajustarla a la Escala Internacional de Temperaturas de 1990. Las modificaciones están descritas por Wagner y Pruss (J. Phys. Chem. Ref. Data, 22, 783, 1993). Las propiedades del hielo están basadas en Hyland y Wexler, “Formulations for the Thermodynamic Properties of the Saturated Phases of H¿O from 173.15 K a 473.15 K”, ASHRAE Trans., Part 2A, Paper 2793, 1983. 968 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES INGLESAS) TABLA A-6E Vapor de agua sobrecalentado s s s T v u h Btu/ v u h Btu/ v u h Btu/ E ft/lbm Btu/lom Btu/lbm lbm-R | ft/lbm Btu/lbm Btu/lbm Ibm-R | ft/lbm Btu/lbm Btu/lbm lbm-R P = 1.0 psia (101.69F)* P = 5.0 psia (162.18) P = 10 psia (193.16*F) Sat? 333.49 1043.7 1105.4 1.9776 73.525 1062.7 1130.7 1.8438 38.425 1072.00 1143.1 1.7875 200 392.53 1077.5 1150.1 2.0509 78.153 1076.2 11485 1.8716 38.849 1074.5 1146.4 1.7926 240 416.44 1091.2 1168.3 2.0777 83.009 1090.3 1167.1 1.8989 41.326 1089.1 1165.5 1.8207 280 440.33 1105.0 1186.5 2.1030 87.838 1104.3 1185.6 1.9246 43.774 1103.4 1184.4 1.8469 320 464.20 11189 12048 2.1271 92.650 1118.4 1204.1 1.9490 46.205 1117.6 1203.1 1.8716 360 488.07 1132.9 12233 2.1502 97.452 1132.5 12226 1.9722 48.624 1131.9 12218 1.8950 400 511.92 1147.1 12418 2.1722 102.25 1146.7 1241.3 1.9944 51.035 1146.2 1240.6 1.9174 440 535.77 11613 1260.4 2.1934 107.03 1160.9 1260.0 2.0156 53.441 1160.5 12594 1.9388 500 571.54 11828 1288.6 2.2237 114.21 11826 1288.2 2.0461 57.041 1182.2 1287.8 1.9693 600 631.14 12194 1336.2 2.2709 126.15 12192 1335.9 2.0933 63.029 1219.0 1335.6 2.0167 700 690.73 12568 1384.6 2.3146 138.09 1256.7 1384.4 2.1371 69.007 1256.5 1384.2 2.0605 800 750.31 1295.1 1433.9 2.3553 150.02 1294.9 1433.7 2.1778 74.980 1294.8 1433.5 2.1013 1000 869.47 1374.2 1535.1 2.4299 173.86 13742 1535.0 2.2524 86.913 1374.1 1534.9 2.1760 1200 988.62 1457.1 1640.0 2.4972 197.70 1457.0 1640.0 2.3198 98.840 1457.0 1639.9 2.2433 1400 1107.8 1543.7 1748.7 2.5590 | 221.54 1543.7 1748.7 2.3816 |110.762 1543.66 1748.6 2.3052 P= 15 psia (212.99*F) P= 20 psia (227.92*F) P = 40 psia (267.22*F) Sat. 26.297 1077.7 1150.7 1.7549 20.093 1081.8 1156.2 1.7319 10.501 1092.1 1169.8 1.6766 240 27.429 1087.8 11639 1.7742 20.478 1086.5 1162.3 1.7406 280 29.085 1102.4 11832 1.8010 21.739 1101.4 1181.9 1.7679 10.713 1097.3 1176.6 1.6858 320 30.722 1116.9 1202.22 1.8260 22.980 1116.1 1201.2 1.7933 11.363 11129 1197.1 1.7128 360 32.348 1131.3 12211 1.8496 24.209 1130.7 1220.2 1.8171 11.999 1128.1 1216.9 1.7376 400 33.965 1145.7 12399 1.8721 25.429 1145.1 12393 1.8398 12.625 1143.1 1236.5 1.7610 440 35.576 1160.1 12588 1.8936 26.644 1159.7 1258.3 1.8614 13.244 1157.9 1256.0 1.7831 500 37.986 1181.9 1287.3 1.9243 28.458 1181.6 1286.9 1.8922 14.165 1180.2 1285.0 1.8143 600 41.988 1218.7 1335.3 1.9718 31.467 1218.5 1334.9 1.9398 15.686 1217.5 1333.6 1.8625 700 45.981 1256.3 1383.9 2.0156 34.467 1256.1 1383.7 1.9837 17.197 1255.3 1382.6 1.9067 800 49.967 1294.6 1433.3 2.0565 37.461 1294.5 1433.1 2.0247 18.702 1293.9 1432.3 1.9478 1000 57.930 1374.0 15348 2.1312 43.438 1373.8 1534.6 2.0994 21.700 13734 1534.1 2.0227 1200 65.885 1456.9 16398 2.1986 49.407 1456.8 1639.7 2.1668 24.691 1456.5 1639.3 2.0902 1400 73.836 1543.6 17485 2.2604 55.373 1543.5 1748.4 2.2287 27.678 1543.3 1748.1 2.1522 1600 81.784 1634.0 18610 2.3178 61.335 1633.9 1860.9 2.2861 30.662 1633.7 1860.7 2.2096 P = 60 psia (292.69*F) P = 80 psia (312.02F) P = 100 psia (327.81*F) Sat. 7.1766 1098.1 11778 1.6442 5.4733 1102.3 1183.4 1.6212 4.4327 1105.5 1187.5 1.6032 320 7.4863 1109.6 1192.7 1.6636 5.5440 1105.9 1187.9 1.6271 360 7.9259 1125.5 12135 1.6897 5.8876 1122.7 1209.9 1.6545 4.6628 11198 1206.1 1.6263 400 8.3548 1140.9 1233.7 1.7138 6.2187 1138.7 1230.8 1.6794 4.9359 1136.4 1227.8 1.6521 440 8.7766 1156.1 1253.6 1.7364 6.5420 1154.3 1251.2 1.7026 5.2006 1152.4 1248.7 1.6759 500 9.4005 1178.8 1283.1 1.7682 7.0177 1177.3 1281.2 1.7350 5.5876 1175.9 1279.3 1.7088 600 10.4256 1216.5 1332.2 1.8168 7.7951 1215.4 1330.8 1.7841 6.2167 12144 13294 1.7586 700 11.4401 1254.5 1381.6 1.8613 8.5616 1253.8 1380.5 1.8289 6.8344 1253.0 1379.5 1.8037 800 12.4484 1293.3 1431.5 1.9026 9.3218 1292.6 1430.6 1.8704 7.4457 1292.0 14298 1.8453 1000 14.4543 1373.0 1533.5 1.9777 10.8313 1372.6 1532.9 1.9457 8.6575 1372.2 15324 1.9208 1200 16.4525 1456.2 1638.9 2.0454 12.3331 1455.9 1638.5 2.0135 9.8615 1455.6 1638.1 1.9887 1400 18.4464 1543.0 17478 2.1073 13.8306 1542.8 1747.5 2.0755 11.0612 1542.6 1747.2 2.0508 1600 20.438 1633.5 1860.5 2.1648 15.3257 1633.3 1860.2 2.1330 12.2584 1633.2 1860.0 2.1083 1800 22.428 1727.66 1976.6 2.2187 16.8192 1727.5 1976.5 2.1869 13.4541 1727.3 1976.3 2.1622 2000 24.417 1825.2 2096.3 2.2694 18.3117 1825.0 2096.1 2.2376 14.6487 1824.9 2096.0 2.2130 * La temperatura entre paréntesis es la temperatura de saturación a la presión especificada. ! Propiedades del vapor saturado a la presión especificada. IN UP TABLA A-6E Vapor de agua sobrecalentado (continuación) s s s T v u h Btu/ v u h Btu/ v u h Btu/ F fé/ibm Btulbm Btulbm lbm-R | fé/bm Btu/lbm Btubm lom-R | fébm Btulbm Btu/lbm lbm-R P = 120 psia (341.25*F) P= 140 psia (353.03"F) P= 160 psia (363.54*F) Sat. 3.7289 1107.9 1190.8 1.5883 3.2202 11099 1193.4 1.5757 2.8347 11116 1195.5 1.5647 360 3.8446 1116.7 1202.1 1.6023 3.2584 11134 11978 1.5811 400 4.0799 1134.0 1224.6 1.6292 3.4676 1131.5 12214 1.6092 3.0076 11290 1218.0 1.5914 450 4.3613 1154.5 1251.4 1.6594 3.7147 11526 1248.9 1.6403 3.2293 1150.7 1246.3 1.6234 500 4.6340 11744 1277.3 1.6872 3.9525 11729 1275.3 1.6686 3.4412 11714 1273.2 1.6522 550 4.9010 1193.9 1302.8 1.7131 4.1845 1192.7 1301.1 1.6948 3.6469 11914 12994 1.6788 600 5.1642 12134 1328.0 1.7375 4.4124 12123 1326.6 1.7195 3.8484 12113 1325.2 1.7037 700 5.6829 1252.2 1378.4 1.7829 4.8604 12514 1377.3 1.7652 4.2434 1250.6 1376.3 1.7498 800 6.1950 1291.4 1429.0 1.8247 5.3017 1290.8 1428.1 1.8072 4.6316 1290.2 1427.3 1.7920 1000 7.2083 1371.7 1531.8 1.9005 6.1732 1371.3 1531.3 1.8832 5.3968 1370.9 1530.7 1.8682 1200 8.2137 1455.3 1637.7 1.9684 7.0367 1455.0 1637.3 1.9512 6.1540 1454.7 1636.9 1.9363 1400 9.2149 15423 1746.9 2.0305 7.8961 1542.1 1746.66 2.0134 6.9070 1541.8 1746.3 1.9986 1600 10.2135 1633.0 1859.8 2.0881 8.7529 1632.8 1859.5 2.0711 7.6574 1632.6 1859.3 2.0563 1800 11.2106 1727.2 1976.1 2.1420 9.6082 1727.0 1975.9 2.1250 8.4063 1726.9 1975.7 2.1102 2000 12.2067 18248 2095.8 2.1928 10.4624 1824.6 2095.7 2.1758 9.1542 1824.5 2095.5 2.1610 P = 180 psia (373.07F) P = 200 psia (381.80F) P= 225 psia (391.807) Sat. 2.5322 11130 1197.3 1.5548 2.2882 1114.1 11988 1.5460 2.0423 11153 1200.3 1.5360 400 2.6490 11263 1214.5 1.5752 2.3615 11235 1210.9 1.5602 2.0728 1119.7 1206.0 1.5427 450 2.8514 1148.7 1243.7 1.6082 2.5488 1146.7 1241.00 1.5943 2.2457 1144.1 1237.6 1.5783 500 3.0433 11698 1271.2 1.6376 2.7247 1168.2 12690 1.6243 2.4059 1166.2 1266.3 1.6091 550 3.2286 1190.2 1297.7 1.6646 2.8939 1188.9 1296.0 1.6516 2.5590 1187.2 12938 1.6370 600 3.4097 1210.2 1323.8 1.6897 3.0586 1209.1 13223 1.6771 2.7075 1207.7 1320.5 1.6628 700 3.7635 1249.8 1375.2 1.7361 3.3796 1249.0 1374.1 1.7238 2.9956 1248.0 1372.7 1.7099 800 4.1104 1289.5 1426.5 1.7785 3.6934 1288.9 1425.6 1.7664 3.2765 1288.1 1424.5 1.7528 900 4.4531 1329.7 1478.0 1.8179 4.0031 1329.2 1477.3 1.8059 3.5530 1328.5 1476.5 1.7925 1000 4.7929 1370.5 1530.1 1.8549 4.3099 1370.1 1529.6 1.8430 3.8268 1369.5 1528.9 1.8296 1200 5.4674 1454.3 1636.5 1.9231 4.9182 1454.0 1636.1 1.9113 4.3689 1453.6 1635.6 1.8981 1400 6.1377 1541.6 1746.0 1.9855 5.5222 15414 1745.7 1.9737 4.9068 1541.1 1745.4 1.9606 1600 6.8054 1632.4 1859.1 2.0432 6.1238 1632.2 1858.8 2.0315 5.4422 1632.0 1858.6 2.0184 1800 7.4716 1726.7 1975.6 2.0971 6.7238 1726.5 1975.4 2.0855 5.9760 1726.4 1975.2 2.0724 2000 8.1367 18244 2095.4 2.1479 7.3227 1824.3 20953 2.1363 6.5087 1824.1 2095.1 2.1232 P = 250 psia (400.97*F) P= 275 psia (409.45”F) P = 300 psia (417.35*F) Sat. 1.8440 11163 1201.6 1.5270 1.6806 1117.0 1202.6 1.5187 1.5435 1117.7 1203.33 1.5111 450 2.0027 11413 1234.0 1.5636 1.8034 1138.5 1230.3 1.5499 1.6369 1135.6 1226.4 1.5369 500 2.1506 1164.1 1263.6 1.5953 1.9415 11620 1260.8 1.5825 1.7670 11598 1257.9 1.5706 550 2.2910 1185.6 1291.5 1.6237 2.0715 1183.9 12893 1.6115 1.8885 1182.1 1287.0 1.6001 600 2.4264 1206.3 1318.6 1.6499 2.1964 1204.9 1316.7 1.6380 2.0046 1203.5 13148 1.6270 650 2.5586 1226.8 1345.1 1.6743 2.3179 1225.6 1343.5 1.6627 2.1172 12244 13419 1.6520 700 2.6883 1247.0 1371.4 1.6974 2.4369 1246.0 1370.0 1.6860 2.2273 1244.9 1368.6 1.6755 800 2.9429 1287.3 1423.5 1.7406 2.6699 1286.5 14224 1.7294 2.4424 1285.7 14213 1.7192 900 3.1930 1327.9 1475.6 1.7804 2.8984 1327.3 14748 1.7694 2.6529 1326.6 1473.9 1.7593 1000 3.4403 1369.0 1528.2 1.8177 3.1241 1368.5 1527.4 1.8068 2.8605 1367.9 1526.7 1.7968 1200 3.9295 1453.3 1635.0 1.8863 3.5700 14529 1634.5 1.8755 3.2704 1452.5 1634.0 1.8657 1400 4.4144 1540.8 1745.0 1.9488 4.0116 1540.5 1744.6 1.9381 3.6759 1540.2 1744.2 1.9284 1600 4.8969 1631.7 1858.3 2.0066 4.4507 1631.5 1858.0 1.9960 4.0789 1631.3 1857.7 1.9863 1800 5.3777 1726.2 1974.9 2.0607 4.8882 1726.0 1974.7 2.0501 4.4803 17258 1974.5 2.0404 2000 5.8575 1823.9 2094.9 2.1116 5.3247 1823.8 2094.7 2.1010 4.8807 1823.6 2094.6 2.0913 970 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES INGLESAS) TABLA A-6E Vapor de agua sobrecalentado (continuación) r E v ft/bm uv Btu/lbm s h Btu/ Btu/lbm_lbm-.R s v u h Btu/ fé/lbm Btu/lbm_ Btu/lbm lbm-R s v u h Btu/ f8/lbm Btu/lbm_ Btu/lbm_lbm-R Sat. 450 500 550 600 650 700 800 900 1000 1200 1400 1600 1800 2000 Sat. 500 550 600 650 700 800 900 1000 1100 1200 1400 1600 1800 2000 Sat. 550 600 650 700 750 800 900 1000 1100 1200 1400 1600 1800 2000 P = 350 psia (431.74) P = 400 psia (444.62*F) P= 450 psia (456.31*F) 1.3263 1118.5 1204.4 1.4973 1.1617 11190 1205.0 1.4852 1.0324 11192 1205.2 1.4742 1.3739 11293 12183 1.5128 1.1747 11225 1209.4 1.4901 1.4921 1155.2 1251.9 1.5487 1.2851 1150.4 1245.6 1.5288 1.1233 1145.4 1238.9 1.5103 1.6004 1178.6 1282.2 1.5795 1.3840 1174.9 1277.3 1.5610 1.2152 1171.1 12723 1.5441 1.7030 1200.6 1310.9 1.6073 1.4765 1197.6 1306.9 1.5897 1.3001 1194.6 1302.88 1.5737 1.8018 1221.9 1338.6 1.6328 1.5650 12194 1335.3 1.6158 1.3807 1216.9 1331.9 1.6005 1.8979 12428 1365.8 1.6567 1.6507 1240.7 1362.9 1.6401 1.4584 1238.5 1360.0 1.6253 2.0848 1284.1 1419.1 1.7009 1.8166 1282.5 1417.0 1.6849 1.6080 1280.8 1414.7 1.6706 2.2671 13253 1472.2 1.7414 1.9777 1324.0 1470.4 1.7257 1.7526 1322.7 1468.6 1.7117 2.4464 1366.9 1525.3 1.7791 2.1358 1365.8 1523.9 1.7636 1.8942 1364.7 1522.4 1.7499 2.7996 1451.7 1633.0 1.8483 2.4465 1450.9 1632.0 1.8331 2.1718 1450.1 16310 1.8196 3.1484 1539.6 1743.5 1.9111 2.7527 1539.0 1742.7 1.8960 2.4450 1538.4 1742.0 1.8827 3.4947 1630.8 1857.1 1.9691 3.0565 1630.3 1856.5 1.9541 2.7157 16298 1856.0 1.9409 3.8394 17254 1974.0 2.0233 3.3586 1725.0 1973.6 2.0084 2.9847 1724.6 1973.2 1.9952 4.1830 1823.3 2094.2 2.0742 3.6597 1823.0 2093.9 2.0594 3.2527 1822.6 2093.5 2.0462 P = 500 psia (467.04) P = 600 psia (486.24*F) P = 700 psia (503.13"F) 0.92815 1119.1 1205.0 1.4642 0.77020 1118.3 1203.9 1.4463 0.65589 1116.9 1201.99 1.4305 0.99304 1140.1 1231.9 1.4928 0.79526 1128.2 1216.5 1.4596 1.07974 1167.1 1267.0 1.5284 0.87542 1158.7 1255.9 1.4996 0.72799 1149.5 1243.8 1.4730 1.15876 1191.4 1298.6 1.5590 0.94605 1184.9 1289.9 1.5325 0.79332 1177.9 1280.7 1.5087 1.23312 1214.3 1328.4 1.5865 1.01133 1209.0 1321.3 1.5614 0.85242 1203.4 13138 1.5393 1.30440 1236.4 1357.0 1.6117 1.07316 1231.9 1351.0 1.5877 0.90769 1227.2 1344.8 1.5666 1.44097 1279.2 14125 1.6576 1.19038 1275.8 1408.0 1.6348 1.01125 1272.4 1403.4 1.6150 1.57252 1321.4 1466.9 1.6992 1.30230 1318.7 1463.3 1.6771 1.10921 1316.0 1459.7 1.6581 1.70094 1363.6 1521.0 1.7376 1.41097 1361.4 1518.1 1.7160 1.20381 1359.2 1515.2 1.6974 1.82726 1406.2 1575.3 1.7735 1.51749 1404.4 1572.9 1.7522 1.29621 1402.5 1570.4 1.7341 1.95211 1449.4 1630.0 1.8075 1.62252 1447.8 1627.9 1.7865 1.38709 1446.2 1625.9 1.7685 2.1988 1537.8 1741.2 1.8708 1.82957 1536.6 1739.7 1.8501 1.56580 1535.4 1738.2 1.8324 2.4430 16294 1855.4 1.9291 2.0340 16284 1854.2 1.9085 1.74192 1627.5 1853.1 1.8911 2.6856 1724.2 1972.7 1.9834 2.2369 17234 1971.8 1.9630 1.91643 1722.7 1970.9 1.9457 2.9271 18223 2093.1 2.0345 2.4387 1821.7 2092.4 2.0141 2.08987 1821.0 2091.7 1.9969 P = 800 psia (518.27) P= 1000 psia (544.65*F) P= 1250 psia (572.45*F) 0.56920 1115.0 1199.3 1.4162 0.44604 1110.1 1192.6 1.3906 0.34549 1102.0 11819 1.3623 0.61586 1139.4 1230.5 1.4476 0.45375 1115.2 1199.2 1.3972 0.67799 1170.5 1270.9 1.4866 0.51431 1154.1 1249.3 1.4457 0.37894 1129.5 1217.2 1.3961 0.73279 1197.6 1306.0 1.5191 0.56411 1185.1 1289.5 1.4827 0.42703 1167.5 1266.3 1.4414 0.78330 12224 1338.4 1.5476 0.60844 12124 1325.0 1.5140 0.46735 1198.7 1306.8 1.4771 0.83102 1246.0 1369.1 1.5735 0.64944 1237.6 1357.8 1.5418 0.50344 1226.4 1342.9 1.5076 0.87678 1268.9 1398.7 1.5975 0.68821 1261.7 1389.0 1.5670 0.53687 1252.2 1376.4 1.5347 0.96434 1313.3 1456.0 1.6413 0.76136 1307.7 1448.6 1.6126 0.59876 1300.5 1439.0 1.5826 1.04841 1357.0 15122 1.6812 0.83078 1352.5 1506.2 1.6535 0.65656 1346.7 1498.6 1.6249 1.13024 1400.7 1568.0 1.7181 0.89783 1396.9 1563.1 1.6911 0.71184 1392.2 1556.8 1.6635 1.21051 1444.6 16238 1.7528 0.96327 14414 1619.7 1.7263 0.76545 1437.4 1614.5 1.6993 1.36797 1534.2 1736.7 1.8170 1.09101 1531.8 1733.7 1.7911 0.86944 1528.7 1729.8 1.7649 1.52283 1626.5 1851.9 1.8759 1.21610 1624.6 1849.6 1.8504 0.97072 1622.2 1846.7 1.8246 1.67606 1721.9 1970.0 1.9306 1.33956 1720.3 1968.2 1.9053 1.07036 1718.4 1966.0 1.8799 1.82823 1820.4 2091.0 1.9819 1.46194 1819.1 2089.6 1.9568 1.16892 1817.5 2087.9 1.9315 977 IP TABLA A-12E Refrigerante 134a saturado. Tabla de presión Volumen específico, Energía interna, Entalpía, Entropía, fé/bm Btu/lbm Btu/lbm Btu/lbm - R Temp. — Líq. Vapor Lía. Vapor — Lía. Vapor Líq. Vapor Pres, sat, Sat, sal., sat., Evap., sat, sat, Evap., — sat, sal., Evap., sal., Ppsia TF 4 A y Ug Y hr Mg Mg Ss, Sí Sy 5 -53.09 0.01113 8.3785 -3.918 91.280 87.36 -3.907 99.022 95.11 -0.00945 0.24353 0.23408 10 -29.52 0.01144 4.3753 3.135 87.453 90.59 3.156 95.528 98.68 0.00742 0.22206 0.22948 15 -14.15 0.01165 2.9880 7.803 84.893 92.70 7.835 93.155 100.99 0.01808 0.20908 0.22715 20 -2.43 0.01182 2.2772 11.401 82.898 94.30 11.445 91.282 102.73 0.02605 0.19962 0.22567 25 7.17 0.01196 1.8429 14.377 81.231 95.61 14.432 89.701 104.13 0.03249 0.19213 0.22462 30 15.37 0.01209 1.5492 16.939 79.780 96.72 17.006 88.313 105.32 0.03793 0.18589 0.22383 35 22.57 0.01221 1.3369 19.205 78.485 97.69 19.284 87.064 106.35 0.04267 0.18053 0.22319 40 29.01 0.01232 1.1760 21.246 77.307 98.55 21.337 85.920 107.26 0.04688 0.17580 0.22268 45 34.86 0.01242 1.0497 23.110 76.221 99.33 23.214 84.858 108.07 0.05067 0.17158 0.22225 50 40.23 0.01252 0.94791 24.832 75.209 100.04 24.948 83.863 108.81 0.05413 0.16774 0.22188 55 45.20 0.01261 0.86400 26.435 74.258 100.69 26.564 82.924 109.49 0.05733 0.16423 0.22156 60 49.84 0.01270 0.79361 27.939 73.360 101.30 28.080 82.030 110.11 0.06029 0.16098 0.22127 65 54.20 0.01279 0.73370 29.357 72.505 101.86 29.510 81.176 110.69 0.06307 0.1579 0.22102 70 58.30 0.01287 0.68205 30.700 71.688 102.39 30.867 80.357 111.22 0.06567 0.15512 0.22080 75 62.19 0.01295 0.63706 31.979 70.905 102.88 32.159 79.567 111.73 0.06813 0.15245 0.22059 80 65.89 0.01303 0.59750 33.201 70.151 103.35 33.394 78.804 112.20 0.07047 0.14993 0.22040 85 69.41 0.01310 0.56244 34.371 69.424 103.79 34.577 78.064 112.64 0.07269 0.14753 0.22022 90 72.78 0.01318 0.53113 35.495 68.719 104.21 35.715 77.345 113.06 0.07481 0.14525 0.22006 95 76.02 0.01325 0.50301 36.578 68.035 104.61 36.811 76.645 113.46 0.07684 0.14307 0.21991 100 79.12 0.01332 0.47760 37.623 67.371 104.99 37.869 75.962 113.83 0.07879 0.14097 0.21976 110 85.00 0.01347 0.43347 39.612 66.091 105.70 39.886 74.641 114.53 0.08246 0.13703 0.21949 120 90.49 0.01360 0.39644 41.485 64.869 106.35 41.787 73.371 115.16 0.08589 0.13335 0.21924 130 95.64 0.01374 0.36491 43.258 63.696 106.95 43.589 72.144 115.73 0.08911 0.1299 0.21901 140 100.51 0.01387 0.33771 44.945 62.564 107.51 45.304 70.954 116.26 0.09214 0.12665 0.21879 150 105.12 0.01400 0.31401 46.556 61.467 108.02 46.945 69.795 116.74 0.09501 0.12357 0.21857 160 109.50 0.01413 0.29316 48.101 60.401 108.50 48.519 68.662 117.18 0.09774 0.12062 0.21836 170 113.69 0.01426 0.27466 49.586 59.362 108.95 50.035 67.553 117.59 0.10034 0.11781 0.21815 180 117.69 0.01439 0.25813 51.018 58.345 109.36 51.497 66.464 117.96 0.10284 0.11511 0.21795 190 121.53 0.01452 0.24327 52.402 57.349 109.75 52.912 65.392 118.30 0.10524 0.11250 0.21774 200 125.22 0.01464 0.22983 53.743 56.371 110.11 54.285 64.335 118.62 0.10754 0.10998 0.21753 220 132.21 0.01490 0.20645 56.310 54.458 110.77 56.917 62.256 119.17 0.11192 0.10517 0.21710 240 138.73 0.01516 0.18677 58.746 52.591 11134 59.419 60.213 119.63 0.11603 0.10061 0.21665 260 144.85 0.01543 0.16996 61.071 50.757 11183 61.813 58.192 120.00 0.11992 0.09625 0.21617 280 150.62 0.01570 0.15541 63.301 48.945 11225 64.115 56.184 120.30 0.12362 0.09205 0.21567 300 156.09 0.01598 0.14266 65.452 47.143 112.60 66.339 54.176 120.52 0.12715 0.08797 0.21512 350 168.64 0.01672 0.11664 70.554 42.627 113.18 71.638 49.099 120.74 0.13542 0.07814 0.21356 400 179.86 0.01757 0.09642 75.385 37.963 113.35 76.686 43.798 120.48 0.14314 0.06848 0.21161 450 190.02 0.01860 0.07987 80.092 32.939 113.03 81.641 38.041 119.68 0.15056 0.05854 0.20911 500 199.29 0.01995 0.06551 84.871 27.168 112.04 86.718 31.382 118.10 0.15805 0.04762 0.20566 978 TABLA A-13E Refrigerante 134a sobrecalentado r E uv v ftó/bm Btu/lbm Btu/lbm h s Btu/ Ibm. R v f/lbm uv s h Btu/ Btu/lbm Btu/lbm lbm-R v ft3/bm uv Btu/lbm Btu/lbm h s Btu/ lbm-R Sat. -20 20 40 60 80 100 120 140 160 180 200 220 160 180 200 220 240 260 280 Sat. 60 80 100 120 140 160 180 200 220 240 260 280 300 320 P= 10 psia (Ty = —29.52%F) P= 15 psia (Tea = 14.15%) P= 20 psia (T.,y = —2.43"F) 4.3753 90.59 98.68 0.22948 2.9880 92.70 100.99 0.22715 2.2772 94.30 102.73 0.22567 4.4856 92.13 100.43 0.23350 4.7135 95.41 104.14 0.24174 3.1001 95.08 103.68 0.23310 2.2922 94.72 103.20 0.22671 4.9380 98.77 107.91 0.24976 3.2551 98.48 107.52 0.24127 2.4130 98.19 107.12 0.23504 5.1600 102.20 111.75 0.25761 3.4074 101.95 111.41 0.24922 2.5306 101.70 111.07 0.24311 5.3802 105.72 115.67 0.26531 3.5577 105.50 115.38 0.25700 2.6461 105.28 115.07 0.25097 5.5989 109.32 119.68 0.27288 3.7064 109.13 119.42 0.26463 2.7600 108.93 119.15 0.25866 5.8165 113.01 123.78 0.28033 3.8540 112.84 123.54 0.27212 2.8726 112.66 123.29 0.26621 6.0331 116.79 127.96 0.28767 4.0006 116.63 127.74 0.27950 2.9842 116.47 127.52 0.27363 6.2490 120.66 132.22 0.29490 4.1464 120.51 132.02 0.28677 3.0950 120.37 131.82 0.28093 6.4642 124.61 136.57 0.30203 4.2915 124.48 136.39 0.29393 3.2051 124.35 136.21 0.28812 6.6789 128.65 141.01 0.30908 4.4361 128.53 140.84 0.30100 3.3146 128.41 140.67 0.29521 6.8930 132.77 145.53 0.31604 4.5802 132.66 145.37 0.30798 3.4237 132.55 145.22 0.30221 7.1068 136.98 150.13 0.32292 4.7239 136.88 149.99 0.31487 3.5324 136.78 149.85 0.30912 P= 30 psia (Ty = 15.37*F) P= 40 psia (za = 29.01”F) P= 50 psia (T.,y = 40.23*F) 1.5492 96.72 105.32 0.22383 1.1760 98.55 107.26 0.22268 0.9479 100.04 108.81 0.22188 1.5691 97.56 106.27 0.22581 1.6528 101.17 110.35 0.23414 1.2126 100.61 109.58 0.22738 1.7338 104.82 114.45 0.24219 1.2768 104.34 113.79 0.23565 1.0019 103.84 113.11 0.23031 1.8130 108.53 118.59 0.25002 1.3389 108.11 118.02 0.24363 1.0540 107.68 117.43 0.23847 1.8908 112.30 122.80 0.25767 1.3995 111.93 122.29 0.25140 1.1043 111.55 121.77 0.24637 1.9675 116.15 127.07 0.26517 1.4588 115.82 126.62 0.25900 1.1534 115.48 126.16 0.25406 2.0434 120.08 131.42 0.27254 1.5173 119.78 131.01 0.26644 1.2015 119.47 130.59 0.26159 2.1185 124.08 135.84 0.27979 1.5750 123.81 135.47 0.27375 1.2488 123.53 135.09 0.26896 2.1931 128.16 140.34 0.28693 1.6321 127.91 140.00 0.28095 1.2955 127.66 139.65 0.27621 2.2671 132.32 144.91 0.29398 1.6887 132.10 144.60 0.28803 1.3416 131.87 144.28 0.28333 2.3408 136.57 149.56 0.30092 1.7449 136.36 149.27 0.29501 1.3873 136.15 148.98 0.29036 2.4141 140.89 154.29 0.30778 1.8007 140.70 154.03 0.30190 1.4326 140.50 153.76 0.29728 2.4871 145.30 159.10 0.31456 1.8562 145.12 158.86 0.30871 1.4776 144.93 158.60 0.30411 2.5598 149.78 163.99 0.32126 1.9114 149.61 163.76 0.31543 1.5223 149.44 163.53 0.31086 P= 60 psia (Ta, = 49.84*F) P= 70 psia (T.a = 58.30%) P = 80 psia (T.,y = 65.89"F) 0.7936 101.30 110.11 0.22127 0.6821 102.39 111.22 0.22080 0.59750 103.35 112.20 0.22040 0.8179 103.31 112.39 0.22570 0.6857 102.73 111.62 0.22155 0.8636 107.23 116.82 0.23407 0.7271 106.76 116.18 0.23016 0.62430 106.26 115.51 0.22661 0.9072 111.16 121.24 0.24211 0.7662 110.76 120.68 0.23836 0.66009 110.34 120.11 0.23499 0.9495 115.14 125.68 0.24991 0.8037 114.78 125.19 0.24628 0.69415 114.42 124.69 0.24304 0.9908 119.16 130.16 0.25751 0.8401 118.85 129.73 0.25398 0.72698 118.52 129.29 0.25083 1.0312 123.25 134.70 0.26496 0.8756 122.97 134.31 0.26149 0.75888 122.68 133.91 0.25841 1.0709 127.41 139.30 0.27226 0.9105 127.15 138.94 0.26885 0.79003 126.89 138.58 0.26583 1.1101 131.63 143.96 0.27943 0.9447 131.40 143.63 0.27607 0.82059 131.16 143.31 0.27310 1.1489 135.93 148.69 0.28649 0.9785 135.71 148.39 0.28317 0.85065 135.49 148.09 0.28024 1.1872 140.30 153.48 0.29344 1.0118 140.10 153.21 0.29015 0.88030 139.90 152.93 0.28726 1.2252 144.75 158.35 0.30030 1.0449 144.56 158.10 0.29704 0.90961 144.37 157.84 0.29418 1.2629 149.27 163.29 0.30707 1.0776 149.10 163.06 0.30384 0.93861 148.92 162.82 0.30100 1.3004 153.87 168.31 0.31376 1.1101 153.71 168.09 0.31055 0.96737 153.54 167.86 0.30773 1.3377 158.54 173.39 0.32037 1.1424 158.39 173.19 0.31718 0.99590 158.24 172.98 0.31438 IN UP TABLA A-13E Refrigerante 134a sobrecalentado (conclusión) s s s T v u h Btu/ v u h Btu/ v u h Btu/ E fé/Ibm Btu/lbm_ Btu/lbm Ibm-R_|ft/lbm Btu/lbm_Btu/lbm_lbm-R |fé/bm Btu/lbm_Btu/lbm_ Ibm -R P= 90 psia (Ti = 72.78%) P= 100 psia (To = 79.12%F) P= 120 psia (T., = 90.49%) Sat. 0.53113 104.21 113.06 0.22006 |0.47760 104.99 113.83 0.21976|0.39644 106.35 115.16 0.21924 80 0.54388 105.74 114.80 0.22330 |0.47906 105.18 114.05 0.22016 100 0.57729 109.91 119.52 0.23189 |0.51076 109.45 118.90 0.22900|0.41013 108.48 117.59 0.22362 120 0.60874 114.04 124.18 0.24008 |0.54022 113.66 123.65 0.23733|0.43692 112.84 122.54 0.23232 140 0.63885 118.19 128.83 0.24797 |0.56821 117.86 128.37 0.24534[0.46190 117.15 127.41 0.24058 160 0.66796 122.38 133.51 0.25563 | 0.59513 122.08 133.09 0.25309|0.48563 121.46 132.25 0.24851 180 0.69629 126.62 138.22 0.26311|0.62122 126.35 137.85 0.26063|0.50844 125.79 137.09 0.25619 200 0.72399 130.92 142.97 0.27043 | 0.64667 130.67 142.64 0.26801|0.53054 130.17 141.95 0.26368 220 0.75119 135.27 147.78 0.27762 |0.67158 135.05 147.47 0.27523|0.55206 134.59 146.85 0.27100 240 0.77796 139.69 152.65 0.28468 | 0.69605 139.49 152.37 0.28233|0.57312 139.07 151.80 0.27817 260 0.80437 144.19 157.58 0.29162 |0.72016 143.99 157.32 0.28931|0.59379 143.61 156.79 0.28521 280 0.83048 148.75 162.58 0.29847 |0.74396 148.57 162.34 0.29618|0.61413 148.21 161.85 0.29214 300 0.85633 153.38 167.64 0.30522 | 0.76749 153.21 167.42 0.30296|0.63420 152.88 166.96 0.29896 320 0.88195 158.08 172.77 0.31189 |0.79079 157.93 172.56 0.30964|0.65402 157.62 172.14 0.30569 P= 140 psia (T¿, = 100.507) P= 160 psia (T¿, = 109.50%F) P= 180 psia (To, = 117.69%F) Sat. 0.33771 107.51 116.26 0.21879|0.29316 108.50 117.18 0.21836|0.25813 109.36 117.96 0.21795 120 0.36243 111.96 121.35 0.22773 |0.30578 111.01 120.06 0.22337|0.26083 109.94 118.63 0.21910 140 0.38551 116.41 126.40 0.23628 |0.32774 115.62 125.32 0.23230|0.28231 114.77 124.17 0.22850 160 0.40711 120.81 131.36 0.24443 |0.34790 120.13 130.43 0.24069|0.30154 119.42 129.46 0.23718 180 0.42766 125.22 136.30 0.25227 |0.36686 124.62 135.49 0.24871|0.31936 124.00 134.64 0.24540 200 0.44743 129.65 141.24 0.25988 | 0.38494 129.12 140.52 0.25645|0.33619 128.57 139.77 0.25330 220 0.46657 134.12 146.21 0.26730 |0.40234 133.64 145.55 0.26397|0.35228 133.15 144.88 0.26094 240 0.48522 138.64 151.21 0.27455 |0.41921 138.20 150.62 0.27131|0.36779 137.76 150.01 0.26837 260 0.50345 143.21 156.26 0.28166 |0.43564 142.81 155.71 0.27849|0.38284 142.40 155.16 0.27562 280 0.52134 147.85 161.35 0.28864 |0.45171 147.48 160.85 0.28554|0.39751 147.10 160.34 0.28273 300 0.53895 152.54 166.50 0.29551 |0.46748 152.20 166.04 0.29246|0.41186 151.85 165.57 0.28970 320 0.55630 157.30 171.71 0.30228 | 0.48299 156.98 171.28 0.29927|0.42594 156.66 170.85 0.29656 340 0.57345 162.13 176.98 0.30896 | 0.49828 161.83 176.58 0.30598|0.43980 161.53 176.18 0.30331 360 0.59041 167.02 182.32 0.31555 |0.51338 166.74 181.94 0.31260|0.45347 166.46 181.56 0.30996 P= 200 psia (Toy = 125.227) P= 300 psia (Tz = 156.09%F) P= 400 psia (Tz, = 179.86"F) Sat. 0.22983 110.11 118.62 0.21753 |0.14266 112.60 120.52 0.21512[|0.09642 113.35 120.48 0.21161 140 0.24541 113.85 122.93 0.22481 160 0.26412 118.66 128.44 0.23384 |0.14656 113.82 121.95 0.21745 180 0.28115 123.35 133.76 0.24229 |0.16355 119.52 128.60 0.22802|0.09658 113.41 120.56 0.21173 200 0.29704 128.00 138.99 0.25035 |0.17776 124.78 134.65 0.23733|0.11440 120.52 128.99 0.22471 220 0.31212 132.64 144.19 0.25812 |0.19044 129.85 140.42 0.24594|0.12746 126.44 135.88 0.23500 240 0.32658 137.30 149.38 0.26565 |0.20211 134.83 146.05 0.25410|0.13853 131.95 142.20 0.24418 260 0.34054 141.99 154.59 0.27298 |0.21306 139.77 151.59 0.26192|0.14844 137.26 148.25 0.25270 280 0.35410 146.72 159.82 0.28015 |0.22347 144.70 157.11 0.26947|0.15756 142.48 154.14 0.26077 300 0.36733 151.50 165.09 0.28718 |0.23346 149.65 162.61 0.27681|0.16611 147.65 159.94 0.26851 320 0.38029 156.33 170.40 0.29408 |0.24310 154.63 168.12 0.28398|0.17423 152.80 165.70 0.27599 340 0.39300 161.22 175.77 0.30087 |0.25246 159.64 173.66 0.29098|0.18201 157.97 171.44 0.28326 360 0.40552 166.17 181.18 0.30756 |0.26159 164.70 179.22 0.29786|0.18951 163.15 177.18 0.29035 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES INGLESAS) 984 TABLA A-18E Propiedades de gas ideal del nitrógeno, Na T h U E T h U E R Btu/lbmol Btu/lbmol Btu/lbmol -R R Btu/lbmol Btu/lbmol Btu/lbmol -R 300 2,082.0 1,486.2 41.695 1080 7,551.0 5,406.2 50.651 320 2,221.0 1,585.5 42.143 1100 7,695.0 5,510.5 50.783 340 2,360.0 1,684.4 42.564 1120 7,839.3 5,615.2 50.912 360 2,498.9 1,784.0 42.962 1140 7,984.0 5,720.1 51.040 380 2,638.0 1,883.4 43.337 1160 8,129.0 5,825.4 51.167 400 2,777.0 1,982.6 43.694 1180 8,274.4 5,931.0 51.291 420 2,916.1 2,082.0 44.034 1200 8,420.0 6,037.0 51.143 440 3,055.1 2,181.3 44.357 1220 8,566.1 6,143.4 51.534 460 3,194.1 2,280.6 44.665 1240 8,712.6 6,250.1 51.653 480 3,333.1 2,379.9 44.962 1260 8,859.3 6,357.2 51.771 500 3,472.2 2,479.3 45.246 1280 9,006.4 6,464.5 51.887 520 3,611.3 2,578.6 45.519 1300 9,153.9 6,572.3 51.001 537 3,729.5 2,663.1 45.743 1320 9,301.8 6,680.4 52.114 540 3,750.3 2,678.0 45.781 1340 9,450.0 6,788.9 52.225 560 3,889.5 2,777.4 46.034 1360 9,598.6 6,897.8 52.335 580 4,028.7 2,876.9 46.278 1380 9,747.5 7,007.0 52.444 600 4,167.9 2,976.4 46.514 1400 9,896.9 7,116.7 52.551 620 4,307.1 3,075.9 46.742 1420 10,046.6 7,226.17 52.658 640 4,446.4 3,175.5 46.964 1440 10,196.6 7,337.0 52.763 660 4,585.8 3,275.2 47.178 1460 10,347.0 7,447.6 52.867 680 4,725.3 3,374.9 47.386 1480 10,497.8 7,558.7 52.969 700 4,864.9 3,474.8 47.588 1500 10,648.0 7,670.1 53.071 720 5,004.5 3,574.7 47.785 1520 10,800.4 7,781.9 53.171 740 5,144.3 3,674.7 47.977 1540 10,952.2 7,893.9 53.271 760 5,284.1 3,774.9 48.164 1560 11,104.3 8,006.4 53.369 780 5,424.2 3,875.2 48.345 1580 11,256.9 8,119.2 53.465 800 5,564.4 3,975.17 48.522 1600 11,409.7 8,232.3 53.561 820 5,704.7 4,076.3 48.696 1620 11,562.8 8,345.7 53.656 840 5,845.3 4,177.1 48.865 1640 11,716.4 8,459.6 53.751 860 5,985.9 4,278.1 49.031 1660 11,870.2 8,573.6 53.844 880 6,126.9 4,379.4 49.193 1680 12,024.3 8,688.1 53.936 900 6,268.1 4,480.8 49.352 1700 12,178.9 8,802.9 54.028 920 6,409.6 4,582.6 49.507 1720 12,333.7 8,918.0 54.118 940 6,551.2 4,684.5 49.659 1740 12,488.8 9,033.4 54.208 960 6,693.1 4,786.7 49.808 1760 12,644.3 9,149.2 54.297 980 6,835.4 4,889.3 49.955 1780 12,800.2 9,265.3 54.385 1000 6,977.9 4,992.0 50.099 1800 12,956.3 9,381.7 54.472 1020 7,120.7 5,095.1 50.241 1820 13,112.7 9,498.4 54.559 1040 7,263.8 5,198.5 50.380 1840 13,269.5 9,615.5 54.645 1060 7,407.2 5,302.2 50.516 1860 13,426.5 9,732.8 54.729 985 E TABLA A-18E Propiedades de gas ideal del nitrógeno, N, (conclusión) T h U E T h U E R Btu/lbmol Btu/lbmol Btu/lbmol -R R Btu/lbmol Btu/lbmol Btu/lbmol -R 1900 13,742 9,968 54.896 3500 27,016 20,065 59.944 1940 14,058 10,205 55.061 3540 27,359 20,329 60.041 1980 14,375 10,443 55.223 3580 27,703 20,593 60.138 2020 14,694 10,682 55.383 3620 28,046 20,858 60.234 2060 15,013 10,923 55.540 3660 28,391 21,122 60.328 2100 15,334 11,164 55.694 3700 28,735 21,387 60.422 2140 15,656 11,406 55.846 3740 29,080 21,653 60.515 2180 15,978 11,649 55.995 3780 29,425 21,919 60.607 2220 16,302 11,893 56.141 3820 29,771 22,185 60.698 2260 16,626 12,138 56.286 3860 30,117 22,451 60.788 2300 16,951 12,384 56.429 3900 30,463 22,718 60.877 2340 17,277 12,630 56.570 3940 30,809 22,985 60.966 2380 17,604 12,878 56.708 3980 31,156 23,252 61.053 2420 17,392 13,126 56.845 4020 31,503 23,520 61.139 2460 18,260 13,375 56.980 4060 31,850 23,788 61.225 2500 18,590 13,625 57.112 4100 32,198 24,056 61.310 2540 18,919 13,875 57.243 4140 32,546 24,324 61.395 2580 19,250 14,127 57.372 4180 32,894 24,593 61.479 2620 19,582 14,379 57.499 4220 33,242 24,862 61.562 2660 19,914 14,631 57.625 4260 33,591 25,131 61.644 2700 20,246 14,885 57.750 4300 33,940 25,401 61.726 2740 20,580 15,139 57.872 4340 34,289 25,670 61.806 2780 20,914 15,393 57.993 4380 34,638 25,940 61.887 2820 21,248 15,648 58.113 4420 34,988 26,210 61.966 2860 21,584 15,905 58.231 4460 35,338 26,481 62.045 2900 21,920 16,161 58.348 4500 35,688 26,751 62.123 2940 22,256 16,417 58.463 4540 36,038 27,022 62.201 2980 22,593 16,675 58.576 4580 36,389 27,293 62.278 3020 22,930 16,933 58.688 4620 36,739 27,565 62.354 3060 23,268 17,192 58.800 4660 37,090 27,836 62.429 3100 23,607 17,451 58.910 4700 37,441 28,108 62.504 3140 23,946 17,710 59.019 4740 37,792 28,379 62.578 3180 24,285 17,970 59.126 4780 38,144 28,651 62.652 3220 24,625 18,231 59.232 4820 38,495 28,924 62.725 3260 24,965 18,491 59.338 4860 38,847 29,196 62.798 3300 25,306 18,753 59.442 4900 39,199 29,468 62.870 3340 25,647 19,014 59.544 5000 40,080 30,151 63.049 3380 25,989 19,277 59.646 5100 40,962 30,834 63.223 3420 26,331 19,539 59.747 5200 41,844 31,518 63.395 3460 26,673 19,802 59.846 5300 42,728 32,203 63.563 Fuente: Las tablas A-18E a A-23E se adaptaron de Kenneth Wark, Thermodynamics, 4a. ed., Nueva York, McGraw-Hill, 1983, pp. 834-844. Original- mente publicadas en J. H. Keenan y J. Kaye, Gas Tables, Nueva York, John Wiley £ Sons, 1945. TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES INGLESAS) 986 TABLA A-19E Propiedades de gas ideal del oxígeno, O. T h u T h u ES R Btu/lbmol Btu/lbmol Btu/lbmol -R R Btu/lbmol Btu/lbmol Btu/lbmol -R 300 2,073.5 1,477.8 44.927 1080 7,696.8 5,552.1 54.064 320 2,212.6 1,577.1 45.375 1100 7,850.4 5,665.9 54.204 340 2,351.7 1,676.5 45.797 1120 8,004.5 5,780.3 54.343 360 2,490.8 1,775.9 46.195 1140 8,159.1 5,895.2 54.480 380 2,630.0 1,875.3 46.571 1160 8,314.2 6,010.6 54.614 400 2,769.1 1,974.8 46.927 1180 8,469.8 6,126.5 54.748 420 2,908.3 2,074.3 47.267 1200 8,625.8 6,242.8 54.879 440 3,047.5 2,173.8 47.591 1220 8,782.4 6,359.6 55.008 460 3,186.9 2,273.4 47.900 1240 8,939.4 6,476.9 55.136 480 3,326.5 2,373.3 48.198 1260 9,096.7 6,594.5 55.262 500 3,466.2 2,473.2 48.483 1280 9,254.6 6,712.7 55.386 520 3,606.1 2,573.4 48.757 1300 9,412.9 6,831.3 55.508 537 3,725.1 2,658.7 48.982 1320 9,571.9 6,950.2 55.630 540 3,746.2 2,673.8 49.021 1340 9,730.7 7,069.6 55.750 560 3,886.6 2,774.5 49.276 1360 9,890.2 7,189.4 55.867 580 4,027.3 2,875.5 49.522 1380 10,050.1 7,309.6 55.984 600 4,168.3 2,976.8 49.762 1400 10,210.4 7,430.1 56.099 620 4,309.7 3,078.4 49.993 1420 10,371.0 7,551.1 56.213 640 4,451.4 3,180.4 50.218 1440 10,532.0 7,672.4 56.326 660 4,593.5 3,282.9 50.437 1460 10,693.3 7,793.9 56.437 680 4,736.2 3,385.8 50.650 1480 10,855.1 7,916.0 56.547 700 4,879.3 3,489.2 50.858 1500 11,017.1 8,038.3 56.656 720 5,022.9 3,593.1 51.059 1520 11,179.6 8,161.1 56.763 740 5,167.0 3,697.4 51.257 1540 11,342.4 8,284.2 56.869 760 5,311.4 3,802.4 51.450 1560 11,505.4 8,407.4 56.975 780 5,456.4 3,907.5 51.638 1580 11,668.8 8,531.1 57.079 800 5,602.0 4,013.3 51.821 1600 11,832.5 8,655.1 57.182 820 5,748.1 4,119.7 52.002 1620 11,996.6 8,779.5 57.284 840 5,894.8 4,226.6 52.179 1640 12,160.9 8,904.1 57.385 860 6,041.9 4,334.1 52.352 1660 12,325.5 9,029.0 57.484 880 6,189.6 4,442.0 52.522 1680 12,490.4 9,154.1 57.582 900 6,337.9 4,550.6 52.688 1700 12,655.6 9,279.6 57.680 920 6,486.7 4,659.7 52.852 1720 12,821.1 9,405.4 57.177 940 6,636.1 4,769.4 53.012 1740 12,986.9 9,531.5 57.873 960 6,786.0 4,879.5 53.170 1760 13,153.0 9,657.9 57.968 980 6,936.4 4,990.3 53.326 1780 13,319.2 9,784.4 58.062 1000 7,087.5 5,101.6 53.477 1800 13,485.8 9,911.2 58.155 1020 7,238.9 5,213.3 53.628 1820 13,652.5 10,038.2 58.247 1040 7,391.0 5,325.7 53.775 1840 13,819.6 10,165.6 58.339 1060 7,543.6 5,438.6 53.921 1860 13,986.8 10,293.1 58.428 IP TABLA A-20E Propiedades de gas ideal del dióxido de carbono, CO, (conclusión). T h u ES T h u ES R Btu/lbmol Btu/lbmol Btu/lbmol -R R Btu/lbmol Btu/lbmol Btu/lbmol -R 1900 19,698 15,925 64.999 3500 41,965 35,015 73.462 1940 20,224 16,372 65.272 3540 42,543 35,513 73.627 1980 20,753 16,821 65.543 3580 43,121 36,012 73.789 2020 21,284 17,273 65.809 3620 43,701 36,512 73.951 2060 21,818 17,727 66.069 3660 44,280 37,012 74.110 2100 22,353 18,182 66.327 3700 44,861 37,513 74.267 2140 22,890 18,640 66.581 3740 45,442 38,014 74.423 2180 23,429 19,101 66.830 3780 46,023 38,517 74.578 2220 23,970 19,561 67.076 3820 46,605 39,019 74.732 2260 24,512 20,024 67.319 3860 47,188 39,522 74.884 2300 25,056 20,489 67.557 3900 47,771 40,026 75.033 2340 25,602 20,955 67.792 3940 48,355 40,531 75.182 2380 26,150 21,423 68.025 3980 48,939 41,035 75.330 2420 26,699 21,893 68.253 4020 49,524 41,541 75.477 2460 27,249 22,364 68.479 4060 50,109 42,047 75.622 2500 27,801 22,837 68.702 4100 50,695 42,553 75.765 2540 28,355 23,310 68.921 4140 51,282 43,060 75.907 2580 28,910 23,786 69.138 4180 51,868 43,568 76.048 2620 29,465 24,262 69.352 4220 52,456 44,075 76.188 2660 30,023 24,740 69.563 4260 53,044 44,584 76.327 2700 30,581 25,220 69.771 4300 53,632 45,093 76.464 2740 31,141 25,701 69.977 4340 54,221 45,602 76.601 2780 31,702 26,181 70.181 4380 54,810 46,112 76.736 2820 32,264 26,664 70.382 4420 55,400 46,622 76.870 2860 32,827 27,148 70.580 4460 55,990 47,133 77.003 2900 33,392 27,633 70.776 4500 56,581 47,645 77.135 2940 33,957 28,118 70.970 4540 57,172 48,156 77.266 2980 34,523 28,605 71.160 4580 57,764 48,668 77.395 3020 35,090 29,093 71.350 4620 58,356 49,181 77.581 3060 35,659 29,582 71.537 4660 58,948 49,694 77.652 3100 36,228 30,072 71.722 4700 59,541 50,208 77.779 3140 36,798 30,562 71.904 4740 60,134 50,721 77.905 3180 37,369 31,054 72.085 4780 60,728 51,236 78.029 3220 37,941 31,546 72.264 4820 61,322 51,750 78.153 3260 38,513 32,039 72.441 4860 61,916 52,265 78.276 3300 39,087 32,533 72.616 4900 62,511 52,781 78.398 3340 39,661 33,028 72.788 5000 64,000 54,071 78.698 3380 40,236 33,524 72.960 5100 65,491 55,363 78.994 3420 40,812 34,020 73.129 5200 66,984 56,658 79.284 3460 41,388 34,517 73.297 5300 68,471 57,954 79.569 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES INGLESAS) 990 TABLA A-21E Propiedades de gas ideal del monóxido de carbono, CO T h U E T h U E R Btu/lbmol Btu/lbmol Btu/lbmol -R R Btu/lbmol Btu/lbmol Btu/lbmol - R 300 2,081.9 1,486.1 43.223 1080 7,571.1 5,426.4 52.203 320 2,220.9 1,585.4 43.672 1100 7,716.8 5,532.3 52.337 340 2,359.9 1,684.7 44.093 1120 7,862.9 5,638.7 52.468 360 2,498.8 1,783.9 44.490 1140 8,009.2 5,745.4 52.598 380 2,637.9 1,883.3 44.866 1160 8,156.1 5,851.5 52.726 400 2,776.9 1,982.6 45.223 1180 8,303.3 5,960.0 52.852 420 2,916.0 2,081.9 45.563 1200 8,450.8 6,067.8 52.976 440 3,055.0 2,181.2 45.886 1220 8,598.8 6,176.0 53.098 460 3,194.0 2,280.5 46.194 1240 8,747.2 6,284.7 53.218 480 3,333.0 2,379.8 46.491 1260 8,896.0 6,393.8 53.337 500 3,472.1 2,479.2 46.775 1280 9,045.0 6,503.1 53.455 520 3,611.2 2,578.6 47.048 1300 9,194.6 6,613.0 53.571 537 3,725.1 2,663.1 47.272 1320 9,344.6 6,723.2 53.685 540 3,750.3 2,677.9 47.310 1340 9,494.8 6,833.7 53.799 560 3,889.5 2,777.4 47.563 1360 9,645.5 6,944.7 53.910 580 4,028.7 2,876.9 47.807 1380 9,796.6 7,056.1 54.021 600 4,168.0 2,976.5 48.044 1400 9,948.1 7,167.9 54.129 620 4,307.4 3,076.2 48.272 1420 10,100.0 7,280.1 54.237 640 4,446.9 3,175.9 48.494 1440 10,252.2 7,392.6 54.344 660 4,586.6 3,275.8 48.709 1460 10,404.8 7,505.4 54.448 680 4,726.2 3,375.8 48.917 1480 10,557.8 7,618.7 54.522 700 4,886.0 3,475.9 49.120 1500 10,711.1 7,732.3 54.665 720 5,006.1 3,576.3 49.317 1520 10,864.9 7,846.4 54.757 740 5,146.4 3,676.9 49.509 1540 11,019.0 7,960.8 54.858 760 5,286.8 3,777.5 49.697 1560 11,173.4 8,075.4 54.958 780 5,427.4 3,878.4 49.880 1580 11,328.2 8,190.5 55.056 800 5,568.2 3,979.5 50.058 1600 11,483.4 8,306.0 55.154 820 5,709.4 4,081.0 50.232 1620 11,638.9 8,421.8 55.251 840 5,850.7 4,182.6 50.402 1640 11,794.7 8,537.9 55.347 860 5,992.3 4,284.5 50.569 1660 11,950.9 8,654.4 55.411 880 6,134.2 4,386.6 50.732 1680 12,107.5 8,771.2 55.535 900 6,276.4 4,489.1 50.892 1700 12,264.3 8,888.3 55.628 920 6,419.0 4,592.0 51.048 1720 12,421.4 9,005.7 55.720 940 6,561.7 4,695.0 51.202 1740 12,579.0 9,123.6 55.811 960 6,704.9 4,798.5 51.353 1760 12,736.7 9,241.6 55.900 980 6,848.4 4,902.3 51.501 1780 12,894.9 9,360.0 55.990 1000 6,992.2 5,006.3 51.646 1800 13,053.2 9,478.6 56.078 1020 7,136.4 5,110.8 51.788 1820 13,212.0 9,597.17 56.166 1040 7,281.0 5,215.7 51.929 1840 13,371.0 9,717.0 56.253 1060 7,425.9 5,320.9 52.067 1860 13,530.2 9,836.5 56.339 TABLA A-21E Propiedades de gas ideal del monóxido de carbono, CO (conclusión) 991 T h u T h u ES R Btu/lbmol Btu/lbmol Btu/lbmol -R R Btu/lbmol Btu/lbmol Btu/lbmol -R 1900 13,850 10,077 56.509 3500 27,262 20,311 61.612 1940 14,170 10,318 56.677 3540 27,608 20,576 61.710 1980 14,492 10,560 56.841 3580 27,954 20,844 61.807 2020 14,815 10,803 57.007 3620 28,300 21,111 61.903 2060 15,139 11,048 57.161 3660 28,647 21,378 61.998 2100 15,463 11,293 57.317 3700 28,994 21,646 62.093 2140 15,789 11,539 57.470 3740 29,341 21,914 62.186 2180 16,116 11,787 57.621 3780 29,688 22,182 62.279 2220 16,443 12,035 57.770 3820 30,036 22,450 62.370 2260 16,722 12,284 57.917 3860 30,384 22,719 62.461 2300 17,101 12,534 58.062 3900 30,733 22,988 62.511 2340 17,431 12,784 58.204 3940 31,082 23,257 62.640 2380 17,762 13,035 58.344 3980 31,431 23,527 62.728 2420 18,093 13,287 58.482 4020 31,780 23,797 62.816 2460 18,426 13,541 58.619 4060 32,129 24,067 62.902 2500 18,759 13,794 58.754 4100 32,479 24,337 62.988 2540 19,093 14,048 58.885 4140 32,829 24,608 63.072 2580 19,427 14,303 59.016 4180 33,179 24,878 63.156 2620 19,762 14,559 59.145 4220 33,530 25,149 63.240 2660 20,098 14,815 59.272 4260 33,880 25,421 63.323 2700 20,434 15,072 59.398 4300 34,231 25,692 63.405 2740 20,771 15,330 59.521 4340 34,582 25,934 63.486 2780 21,108 15,588 59.644 4380 34,934 26,235 63.567 2820 21,446 15,846 59.765 4420 35,285 26,508 63.647 2860 21,785 16,105 59.884 4460 35,637 26,780 63.726 2900 22,124 16,365 60.002 4500 35,989 27,052 63.805 2940 22,463 16,225 60.118 4540 36,341 27,325 63.883 2980 22,803 16,885 60.232 4580 36,693 27,598 63.960 3020 23,144 17,146 60.346 4620 37,046 27,871 64.036 3060 23,485 17,408 60.458 4660 37,398 28,144 64.113 3100 23,826 17,670 60.569 4700 37,751 28,417 64.188 3140 24,168 17,932 60.679 4740 38,104 28,691 64.263 3180 24,510 18,195 60.787 4780 38,457 28,965 64.337 3220 24,853 18,458 60.894 4820 38,811 29,239 64.411 3260 25,196 18,722 61.000 4860 39,164 29,513 64.484 3300 25,539 18,986 61.105 4900 39,518 29,787 64.556 3340 25,883 19,250 61.209 5000 40,403 30,473 64.735 3380 26,227 19,515 61.311 5100 41,289 31,161 64.910 3420 26,572 19,780 61.412 5200 42,176 31,849 65.082 3460 26,917 20,045 61.513 5300 43,063 32,538 65.252 994 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES INGLESAS) TABLA A-23E Propiedades de gas ideal del vapor de agua, H¿0 (conclusión) T h u ES T h u ES R Btu/lbmol Btu/lbmol Btu/lbmol - R R Btu/lbmol Btu/lbmol Btu/lbmol -R 1900 16,428 12,654 56.097 3500 34,324 27,373 62.876 1940 16,830 12,977 56.307 3540 34,809 27,779 63.015 1980 17,235 13,303 56.514 3580 35,296 28,187 63.153 2020 17,643 13,632 56.719 3620 35,785 28,596 63.288 2060 18,054 13,963 56.920 3660 36,274 29,006 63.423 2100 18,467 14,297 57.119 3700 36,765 29,418 63.557 2140 18,883 14,633 57.315 3740 37,258 29,831 63.690 2180 19,301 14,972 57.509 3780 37,752 30,245 63.821 2220 19,722 15,313 57.701 3820 38,247 30,661 63.952 2260 20,145 15,657 57.889 3860 38,743 31,077 64.082 2300 20,571 16,003 58.077 3900 39,240 31,495 64.210 2340 20,999 16,352 58.261 3940 39,739 31,915 64.338 2380 21,429 16,703 58.445 3980 40,239 32,335 64.465 2420 21,862 17,057 58.625 4020 40,740 32,757 64.591 2460 22,298 17,413 58.803 4060 41,242 33,179 64.715 2500 22,735 17,771 58.980 4100 41,745 33,603 64.839 2540 23,175 18,131 59.155 4140 42,250 34,028 64.962 2580 23,618 18,494 59.328 4180 42,755 34,454 65.084 2620 24,062 18,859 59.500 4220 43,267 34,881 65.204 2660 24,508 19,226 59.669 4260 43,769 35,310 65.325 2700 24,957 19,595 59.837 4300 44,278 35,739 65.444 2740 25,408 19,967 60.003 4340 44,788 36,169 65.563 2780 25,861 20,340 60.167 4380 45,298 36,600 65.680 2820 26,316 20,715 60.330 4420 45,810 37,032 65.797 2860 26,773 21,093 60.490 4460 46,322 37,465 65.913 2900 27,231 21,472 60.650 4500 46,836 37,900 66.028 2940 27,692 21,853 60.809 4540 47,350 38,334 66.142 2980 28,154 22,237 60.965 4580 47,866 38,770 66.255 3020 28,619 22,621 61.120 4620 48,382 39,207 66.368 3060 29,085 23,085 61.274 4660 48,899 39,645 66.480 3100 29,553 23,397 61.426 4700 49,417 40,083 66.591 3140 30,023 23,787 61.577 4740 49,936 40,523 66.701 3180 30,494 24,179 61.727 4780 50,455 40,963 66.811 3220 30,967 24,572 61.874 4820 50,976 41,404 66.920 3260 31,442 24,968 62.022 4860 51,497 41,856 67.028 3300 31,918 25,365 62.167 4900 52,019 42,288 67.135 3340 32,396 25,763 62.312 5000 53,327 43,398 67.401 3380 32,876 26,164 62.454 5100 54,640 44,512 67.662 3420 33,357 26,565 62.597 5200 55,957 45,631 67.918 3460 33,839 26,968 62.738 5300 57,279 46,754 68.172 TABLA A-26E Entalpía de formación, función de Gibbs de formación y entropía absoluta a 77%, 1 atm h; E so Sustancia Fórmula Btu/lbmol Btu/lbmol Btu/lbmol -R Acetileno CoHal8) +97,540 +87,990 48.00 Agua H20(€) -122,970 -102,040 16.71 Alcohol etílico C¿H5¿0H(g) 101,230 72,520 67.54 Alcohol etílico C¿H¿0H(£) 119,470 75,240 38.40 Alcohol metílico CH¿0H(g) 86,540 69,700 57.29 Alcohol metílico CH3¿0H(£) 102,670 71,570 30.30 Amoniaco NHa(8) -19,750 7,140 45.97 Benceno CóHal8) +35,680 +55,780 64.34 n-Butano CaHio(8) -54,270 -6,760 74.11 Carbón C(s) 0 0 1.36 Dióxido de carbono CO»(g) -169,300 -169,680 51.07 n-Dodecano Ci2Has(g) 125,190 +21,570 148.86 Etano CoHg(8) -36,420 -14,150 54.85 Etileno CoHa(8) +22,490 +29,306 52.54 Hidrógeno H(g) +93,780 +87,460 27.39 Hidrógeno H2(8) 0 0 31.21 Hidroxilo O0H(g) +16,790 +14,750 43.92 Metano CHa(8) -32,210 -21,860 44.49 Monóxido de carbono CO(g) 47,540 59,010 47.21 Nitrógeno N(8) 0 0 45.77 Nitrógeno N(g +203,340 +195,970 36.61 p-Octano CaHa(8) -89,680 +7,110 111.55 p-Octano CaHial() 107,530 +2,840 86.23 Oxígeno 048) 0 0 49.00 Oxígeno 0(g) +107,210 +99,710 38.47 Peróxido de hidrógeno H20,(g) -58,640 45,430 55.60 Propano CaHalg) -44,680 -10,105 64.51 Propileno CaHá(8) +8,790 +26,980 63.80 Vapor de agua H20(8) - 104,040 -98,350 45.11 Fuente: De JANAF, Thermochemical Tables, Midland, MI, Dow Chemical Co., 1971; Selected Values of Chemical Thermodynamic Properties, NBS Technical Note 270-3, 1968; y API Research Project 44, Carnegie Press, 1953. sde. FIGURA A-30a Gráfica generalizada de compresibilidad de Nelson-Obert-bajas presiones. (Utilizadas con permiso del Dr. Edward E. Obert, University of Wisconsin.) (a)0<R<10 1.00 o o 0.80| NOTA T,=25, 2=100 T =18=T,-300 [E ——DESVIACIÓN >1.0% En o >= o GRÁFICA GENERALIZADA DE COMPRESIBILIDAD DE NELSON-OBERT o o PRESIÓN REDUCIDA P, = E GRÁFICA 2 TEMPERATURA REDUCIDAT, = T N9 FACTOR DE COMPRESIBILIDAD 2= $ o a VOLUMEN Y” =— ] PSEUDORREDUCIDO RTa(P: 0.0 0.1 0.2 0.3 0.4 05 0.6 0.7 0.8 0.9 LO PRESIÓN REDUCIDA, P, A-52 GENERALI|ZED DEVIATION OF ENTROPY s*-s from values "at Zg=0.27: os 10h: 0 uba 02 03 04 m3 08 08 lo,t2 an dz 03040505 09 reduced pressure, py reduced pressure, Pr Dj for values of Z¿<0.27 Copyright 1960 O. A, NOUGEN, K, M. WATSON und Ra Á. MAGATZ y A AA . a E asS 03 040308 08 Lo 12 Dg for values of Zg>0. 32 y 3200 3 Saz 833 Ss RAT A ' ' ' ' a ' o 12 q ' 27 ' Fig. 143b | —A a ios AA A A V “ZIVOVH “Y “Y PUY NOSLVAM “MN, 'N 'NADNOH *V "O 0961 ->....,0/0/00 | | 4 ] ¿20=%Z $. san¡DÁ uJO4, (Ajuo espyd sob /0)) Z YOLOVW ALITIGISS3UANOI JO NOU LVIA3O (03ZIIVY3N39 “90b1 Dia, “IZ0» dz jo SOn|DA 10, %g ld'einssesd paonpal E ¿z30O<%z jo senioa 03 Pa Jd *elnssejd paonpal E zo — el o1 80 go so yO v0 zo ao fi PÍO 2: ZO 80 yo so v0 Eo 0% 0.1 0.2 030405 LO 2.0 3.0 4.050 10 20 30 Presión reducida, P, 5[, 0500 El < 0.400 ' z z Z YS z y 00 FIGURA A-29 27 Carta generalizada de desviación de 140 entalpía. 17 Fuente: John R. Howell y Richard O. Buckius, Y AE 200 | Fundamentals of Engineering Thermodynamics, ¡A as AS ss versión Sl, Nueva York, McGraw-Hill, 1987, p. 558, | Fig. C2 y p.561, Fig C.5.