Tablas Termodinamicas, Apuntes de Calor y Transferencia de Masa

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Tabla A-1 Tabla A-2 Tabla A-3 Tabla A-4 Tabla A-5 Tabla A-6 Tabla A-7 Tabla A-8 Figura A-9 Figura A-10 Tabla A-11 Tabla A-12 Tabla A-13 Figura A-14 Figura A-15 Tabla A-16 Tabla A-17 Tabla A-18 Tabla A-19 Tabla A-20 Apénolce 1 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) Masa molar, constante de gas y propiedades del punto críti Calores específicos de gas ideal de varios gases comunes Propiedades de líquidos, sólidos y alimentos comunes Agua saturada. Tabla de temperaturas Agua saturada. Tabla de presiones Vapor de agua sobrecalentado Agua líquida comprimida Hielo saturado. Vapor de agua Diagrama 7-5 para el agua Diagrama de Mollier para el agua Refrigerante 134a saturado. Fabla de temperatura Relrigerante 134a saturado. Tabla de presión Refrigerante 134a sobrecalentado Diagrama P-h para refrigerante 134a Carta generalizada de compresibilidad de Nelson-Obert Propiedades de la atmóstera a gran altitud Propiedades de gas ideal del aire Propiedades de gas ideal del nitrógeno, N, Propiedades de gas del oxígeno, O, Propiedades de gas ideal del dióxido de carbono, CO, Tabla A-21 Tabla A-22 Tabla A-23 Tabla A-24 Tabla A-25 Tabla A-26 Tabla A-27 Tabla A-28 Figura A-29 Figura A-30 Figura A-31 Tabla A-32 Tabla A-33 Tabla A-34 Propiedades de gas ideal del monóxido de carbono, CO Propiedades de gas ideal del hidrógeno, Ha, Propiedades de gas ideal del vapor de agua, H,O Propiedades de gas ideal del oxígeno monoatómico, O Propiedades de gas ideal del hidroxilo, OH Entalpía de formación, función de Gibbs de formación y entropía absoluta a 25%, 1 atm Propiedades de algunos combustibles e hidrocarburos comunes Logaritmos naturales de la constante de equilibrio K,, Carta generalizada de desviación de entalpía Carta generalizada de desviación de entropía Carta psicrométrica a | atm de presión total Funciones de flujo compresible unidi- mensional e isentrópico de un gas ideal conk = 1.4 Funciones de choque normal unidimen- sional de un gas ideal conk= 1.4 Funciones del flujo de Rayleigh para un gas ideal conk = 14 904 i Tablas de propiedades, figuras y diagramas (unidades Si) TABLA A-1 Masa molar, constante de gas y propiedades del punto crítico Propiedades del punto crítica Constante AAA Masa molar, — de gas, Temperatura, Presión, Volumen, Sustancia Fórmula M kg/kmal RkJikg > K K MPa. _ mé/kmol Agua HO 18.015 0,4615 | 647.1 22.06 0.0560 Aire E 28.97 0.2870 132.5 Sql 0.0883 Alcohol etílico C7H50H 46.07 0.1805 516 6.38 0.1673 Alcohol metílico CH30H 32,042 0.2595 513.2 7:95) 0.1180 Amoniaco NH; 17.03 0.4882 405.5 11.28 0.0724 Argón Ar 39.948 0.2081 151 4.86 0.0749 Benceno CsHó 78.115 0,1064 562 4.92 0.2603 Bromo Br 159.808 0.0520 584 10.34 0.1355 n-Butano CaHio 58.124 0,1430 425.2 3.80 0,2547 Cloro Cl 70,906 0.1173 417 Lolo, 0.1242 Cloroformo CHCl 119.38 0.06964 536.6 5.47 0.2403 Cioruro metilico CcHzCt 50,488 0.1647 416.3 6.68 0,1430 Criptón Kr 83.80 0.09921 209.4 5.50 0.0924 Dictorodifluorometano (R-12) CelaF 120.91 0.06876 384.7 4.01 0.2179 Diclorofluorometana (R-21) CHCLF 102.92 0.08078 451.7 5 0.1973 Dióxida de carbono CO» 44.01 0.1889 304.2 189) 0.0943 Dióxido de sulfuro SO» 64.063 0,1298 430.7 7.88 0.1217 Etano CoHa 30.070 0,2765 305.5 4.48 0.1480 Etileno CoHa 28,054 0.2954 282,4 5.12 :0,1242 Helía He 4,003 2.0769 ES) 0.23 0.0578 rHexano CóHra 86.179 0.09647 507.9 3.03 0.36/7 Hidrógeno (normal) o 2.016 * 4.1240 33,3 1.30 0.0649 Metano CHa 16.043 0.5182 | 191.1 4.64 0.0993 Monóxido de carbono co 28.011 0.2968 133 3.50 0.0930 Neón Ne 20.183 0.4119 44.5 2.73 0.0417 Nitrógeno Na 28.013 0.2968 126.2 3.39 0,0899 Óxido nitroso N¿0 44.013 0.1889 309.7 727 0.0961 Oxigeno 0, 31.999 0.2598 | 154.8 5.08 0.0780 Propano CaHa 44,097 0.1885 | 370 4.26 0.1998 Propileno CaHó 42.081 0.1976 365 4.62 0.1810 Tetractoruro de carbono CCla 153.82 0,05405 556,4 4.56 0,2759 Tetrafluoroetano (R-134a) CF¿CH¿F 102.03 0.08149 374.2 4.059 0,1993 Triclorofluorometano (R-11) CchF 137.37 0.06052 471,2 4.38 0.2478 Xenón Xe 131.30 0.06332 | 289.8 5.88 0.1186 *La unidad en kVkg - K es equivalente a kPa - m”/kg - K. La constante de gas se calcula de R = R,/M, donde R, = 8.31447 kJ/kmol - K y Mes la masa molar. Fuente: K. A. Kobe y R. E. Lynn, Je, Chemical Review 52 (1953), pe. 117-236; y ASHRAE, Handbook of Fundamentals (Atlanta, GA: Sociedad Americana de Ingenieros de Calefacción, Refrigeración y Acondicionamiento de Are, Inc., 1993), pp. 16.4 y 36.1 906 Tablas de propiedades, figuras y diagramas (unidades SI) TABLA A-2 Calores específicos de gas ideal de varios gases comunes (continuación) b) A diversas temperaturas Ez C En 5 Cs; Es temperatura, CUE K kg Ke klikg= Ko kikg-K ko |kikgKk kiíkgK 4 K Aire Dióxido de carbono, CO, Monóxido de carbono, CO 250 1.003 0.716 1.401 0.791 0.602 1.314 1.039 0.743 1.400 300 1,005 0.718 1.400 0.846 0.657 1.288 1.040 0.744 1.399 350 1.008 0.721 1398 | 0.895 0.706 1.268 1.043 0.746 1.398 400 1,013 0.726 1.395 0.939 0.750 1.252 1.047 0.751 1.395 450 1.020 0.733 1:39 0.978 0.790 1.239 1,054 0.757 1.392 500 1.029 0.742 1.387 1.014 0.825 1.229 1.063 0.767 1.387 550 1.040 0.753 1.381 1.046 0.857 1.220 1.075 0.778 1.382 600 1.051 0.764 1.376 1.075 0.886 1.213 1.087 0,799 1.376 650 1.063 0.776 1.370 1.102 0.913 1.207 1.100 0.803 1.370 700 1.075 0.788 1.364 1.126 0.937 1.202 1.113 0.816 1.364 750 1.087 0.800 1.359 1,148 0.959 1.197 1.126 0.829 1.358 800 1.099 0.812 1.354 1.169 0.980 1198 1.139 0.842 1.353 900 1.121 0.834 1.344 1.204 1.015 1.186 1.163 0.866 1.343 1000 1.142 0.855 1.336 1.234 1.045 1.181 1.185 0.888 1.335 Hidrógeno, Hi Nitrógeno, Ny |__ Oxígeno, O, 250 14.051 9.927 1.416 1.039 0,742 1.400 0.913 0.653 1.398 300 14.307 10.183 1.405 1.039 0.743 1.400 0.918 0.658 1.395 350 14,427 10.302 1.400 1.041 0.744 1.399 0.923 0.668 1.389 400 14.476 10.352. 1.398 1,044 0.747 1.397 0.941 0.631 1.382 450 14.501 10.377 1.398 1.049 0.752 1,395 0.956 0.696 1.373 500 14,513 10.389 1.397 1,056 0.759 1.391 0.972 0.712 1.365 550 14.530 10.405 1.396 1,065 0.768 1.387 0.988 0.728 1.358 600 14.546 10.422 1.396 1.075 0.778 1.382 1.003 0.743 1.350 650 14.571 10.447 1.395 1.086 0.789 1.376 1.017 0.758 1.343 700 14.604 10,480 1.394 1.098 0.801 1.371 1.031 0.771 1.337 750 14.645 10.521 1.392 1.110 0.813 1.365 1.043 0.783 1.332 800 14.695 10.570 1.390 1.121 0.825 1.360 1.054 0.794 1.327 900 14.822 10.698 1.385 1,145 0.349 1.349 1.074 0.814 1.319 1000 14.983 10.859 1.380 1,167 0.870 1.341 1.090 0,830 1,313 Fuente: Kenneth Wark, Thermodynamics, da. ed., Nueva York. McGraw-Hill, 1983, p. 783, Tabia A-4MM, Publicada originalmente en Tables of Thermal Properties of Gases, NBS Circular 564, 1955. Apéndice 1 ¡ 907 TABLA A-2 Calores específicos de gas ideal de varios gases comunes (conclusión) €) Como una función de la temperatura C,= a+ bT + 0174 gr* (Ten K, 0,80 kia! % de error Rango de == Sustancia Fórmula a b [a d temp., K___ Máx. Prom. Acetileno CH) 21.8 9.2143 x 10? -6.527 x 1075 18.21 x 10* 273-1500 1.46 0.59 Aire o 28.11 0.1967 x 10? 0.4802 x 1075 1.966 x 10? 273-1800 0.72 0.33 Amoniaco NHz 27.568 2.5630 x 102 0.99072 x 107? -6.6909 x 10 * 273-1500 0.91 0.36 Azufre S» 27.21 2.218 x 10? -1.628 x 10? 3.986 x 109 273-1800 0.99 0.38 Benceno CóHó 36.22 48.475 x 10% 31,57 x 10? 77:62 x 10? 273-1500 0.34 0.20 FButano CoHio 7918 41.60 x 10? 23.01 x 10 49.91 x 10? 273-1500 0.25 0.13 a-Butano CHro 3.96 37.15 x 102 18.34 x 1075 35.00 x 10% 273-1500 0.54 0.24 Cloruro de hidrógeno a] 30.33 0.7620 x 107? 1.327 x 1075 4.338 x 10? 273-1500 0.22 0.08 Dióxido de azufre SO, 25.78 5.795 x 1072 -3.812 x 104 8.612 x 10? 273-1800 045 0.24 Dióxido de carbono CO, 22.26 5.981 x 107? -3.501 x 107% 7.469 x 107 273-1800 0.67 0.22 Diéxido de nitrógeno NO» 22,9 5,715 x -3.52 x 1075 7.87 x 107 273-1500 0.46 0.18 Etano CH 6.900 VIZ7AS -6,406 x 10 5 7.285 x 107? 273-1500 0.83 0.28 Etanol C2H¿0 19.9 20.96 x -10,38 x 10% 20,05 x 1079 273-1500 0.40 0,22 Etileno CH, 3.95 15.64 x 1 -8.344 x 10% 17.67 x 107? 273-1500 0.54 0.13 e-Hexano CóHia 6.938 55.22 x -28,65 x 1073 57,69 x 107? 273-1500 0.72 0.2 Hidrógeno Ha 29,11 -0.1916 x 102 0,4003 x 1075 -0.8704 x 107? 273-1800 1.01 0.26 Metano CH, 19.89 5.024 x 10? 1.269 x 11.01 x 10? 273-1500 133 0.57 Metanol CH¿0 19.0 9,152 x 1072 1 AOS -8,039 x 10* 273-1000 0.18 0.08 Monóxido de carbono [a 28,16 0.1675 x 107? 053725 1075 2.222 x 10? 273-1800 0.89 0.37 Nitrógeno N, 28.90 -0.1571x 0.8081 x 10% -2,873 x 10? 273-1800 0.59 0.34 Óxido nítrico NO 29,34 -0,09395 x 107? 0.9747 x 10 * -4,187 x 107? 273-1500 0.97 0.36 Óxido nitroso NO 24,11 5.8632 x 10? -3,562 x 107* 10.58 x 107? 273-1500 0.59 0.26 Oxígeno 0 25.48 1.520 x 10 ? 0,7155 x 107% 1.312 x 1072 273-1800 1.19 0.28 A-Pentano CsHia 6,774 45.43 x 10? " -22.46 x 1075 42,29 x 10? 273-1500 0.56 0.21 Propano CaHa 4.04 30.48 x 10 2 15,72 x 107% 3174 x 107* 273-1500 0.40 0,12 Propileno CyHg 3.15 23.83 x 1072 -12,18 x 1073 24.62 x 102 273-1500 0.73 0.17 Trióxido de azufre 50, 16,40 14,58 x 1072 -11.20 x 107% 32,42 x 10? 273-1300 0.29 0,13 Agua (vapor) H¿0 32.24 0.1923 x 10*2 1.055 x 10 > 3.595 x 10? 273-1800 0.53 0,24 Fuente: B. G. Kyle, Chemical and Process Thermadynamics, Englewoca Cliffs, Nueva Jersey, Prentice Hall, 1984. Usada con permiso. Apéndice 1 I 909 TABLA Propiedades de líquidos, sólidos y alimentos comunes (conclusión) D) Sólidos (los valores son para temperatura ambiente, excepto que se indique otra cosa) Densidad, Calor específico, Densidad, Calor específico, Sustancia e kglmi €, Kikg > K Sustancia p kgán? co kdikg > K Metales No metales Acero dulce 7,830 0.500 Arena 1520 0.800 Aluminio Arcilla 1000 0.920 200K 0.797 Asfalto 2110 0.920 250 K Caucho (blando) 1100 1.840 300 K 2,700 Caucho (duro) 1150 2.009 350 K Concreto 2300 0.653 400 K Diamante 2420 0.516 450 K Grafito 2500 0.711 500 K Granito 2700 1.017 Bronce (76% Cu, 2% Zn, 8,280 Hielo 2% Al) 200 K 1.56 Cobre 220K E, 1735 0.254 240 K 1.86 100% +0.342 260 K 2.01 500 0.367 273 K 921 2.11 oc 0.381 Ladriflo común 1922 0.79 27 8.900 0.386 Ladrillo refractario (500*C) 2300 0.960 100 0.393 Madera contrachapada 200% 0.403 tabeto Douglas) 545 Hierro 7,840 0.45 Maderas duras (maple, encino, etc.) 721 Latón amarillo (55% Cu, 8,310 0,400 Maderas suaves (abeto, pino, etc.) SUS: 35% Zn) Mármol 2600 Magnesio 1,730 1.000 Piedra 1500 Níquel 8,890 0.440 Piedra caliza 1650 Plata 10,470 0.235 Vidrio para ventanas 2700 Plomo 11,310 0.128 Vidrio pirex 2230 Tungsteno 19,400 0.130 Yeso o tabla de yeso 800 c) Alimentos 6 Calar espe JODA: UA Porenciria Por cebaja Calor Por encima Porcebajo Calor Contenido. — Panto del punto — del punto — Intente Contenido Punto del punto — del punto — latente de agua, deconge- decenge- deconge de fusión. deague deconge= de corge- decenge- de fusión, Alimentos % (masa) lación. *C tación ación A Alimentos % masa) tación “O lación lación kkg Brócoli 90 -0.6 3.86 1,97 301 Helado 63 -5.6 2.95 1.63 210 Camarón 83 paa 3.62 1.89 277 Mantequilla 16 == E 1.04 53 Carne de pollo 74 28 3.32 17% 247 Manzanas 84 11 3.65 190 281 Carne de res 67 - 3.08 1.68 224 Naranjas 87 -08 3.75 194 291 Cerezas 80 -1.8 3.52 1.85 267 Papas 78 0.6 3.45 1.82 261 Espinaca 93 -0.3 3.96 2.01 Si Pavo 64 ES 2.98 1.65 214 Fresas 90 -0.8 3.86 1.97 301 Plátanos 5 -0.8 3:35) 1.78 251 Huevo entero 74 08] 3.32 1.77 247 Queso suizo 39 10.0 2.15 1.33 130 Leche entera 88 -0.6 3.79 1.95 294 Salmón 64 =202 2.98 1.65 214 Lechuga 95 0.2 4.02 2.04 Sly Sandía 93 0.4 3.96 2.01 311 Maíz dulce 74 -06 3.32 139% 247 Tomates (maduros) 94 015, 3.99 2.02 314 Fuente: Los valores han sido obtenidos de varios manuales y otras fuentes, o se han calculado. El contenido de agua y los datos de punto de congelación para alimentos provienen del ASHRAE, Handbook of Fundamentals, versión SI, Atlanta, Georgla, American Society of Heating, Refrigerating and Air-Conditioning Engineers, Inc., 1993, Capítulo 30, Tabla 1. El punto de congelación es la temperatura a la que comienzala congelación para frutas y verduras, así como la temperatura promedio de congelación para otros alimentos. 910 TABLA 1 Tablas de propiedades, figuras y diagramas (unidades SI) Agua saturada. Tabla de temperaturas Temp.. T6U 0.01 5 10 15 20 25 30 35 40 45 50 s5 50 65 70 75 80 85 90 95 100 105 10 115 120 125 130 135 140 145 150 155 160 165 170 175 180 185 190 195 200 Volumen específico, Energía interna, Entalpía. Entropia, mkg KJ/kg kJikg lJ/kg K Pres. Líq. Vapor Lía. Vapor Líq. Vapor — Líg Vapor sat, sat, sat., sat., Evap., sat, sat., Evap,, sat., sat., Evap., sat., Pi kPa Y Va ue Ug Us he Po A ES Sa En 0.6117 0.001000 206.00 0.000 23749 23749 0.001 25009 2500,9 0.0000 9.1556 9.1586 0.8725 0.001000 147.03 21019 2360.8 23818 21.020 24891 2510.1 0.0763 89487 9.0249 1.2281 0.001000 106,32 42020 2346.6 2388.7 42022 24772 25192 0.1511 8.7488 8.8999 1.7057 0.001001 77.885 62.980 23325 23955 62.982 24654 2528.3 0.2245 8.5559 8.7803 2.3392 0001002 57.762 83.913 2318.4 24023 83.915 24535 25374 0.2965 8,3695 8.6661 3.1698 0.001003 43.340 10483 23043 2409.1 104.83 24417 25465 0.2672 8,1895 8.5567 4.2469 0001004 32.879 125.73 2290.2 24159 125.74 24298 2555.6 0.4368 8.0152 8.4520 5.6291 0001006 25.205 146.63 22760 24227 146.64 24179 2564.65 0.5051 7.8466 8.3517 7.3851 0.001008 19.515 167.53 22619 24294 167.52 24060 2573.5 0.5724 7.6832 8.2556 9.5953 0001010 15.251 188.43 2247.7 2436.1 188.44 23940 25824 0.6386 7,5247 8.1633 12.352 0001012 12.026 209.33 22334 24427 20934 23820 25913 0.7038 7.3710 8.0748 15.763 — 0001015 9.5639 23024 2219,1 24493 230.26 23698 2600,1 0.7680 7.2218 7.9898 19.947 — 0.001017 7.6670 251.16 2204,7 24559 251:18 2357,7 26088 08313 7.0769 7.9082 25.043 0.001020 6,1935 27209 219.3 24624 272.12 23454 26175 0.8937 6.9360 7.8296 31.202 0.001023 5.0396 293.04 21758 24689 293.07 23330 26261 0.9551 6.7989 7.7540 38.597 0001025 4.1291 313.99 2161.3 2475.3 314.03 2320.6 26346 1.0158 6.5655 7.6812 47416 0.001029 3.4053 334,97 2146.6 2481.6 33502 23080 2643,0 1.0756 6.5355 7.6111 57.868 0001032 28261 355.96 21319 2487.8 356.02 22953 26514 1.1346 6.4089 7.5435 70.183 —0.001036 2.3593 376.97 21170 249,0 377.04 22825 26596 1.1929 6.2853 7.4782 84.609 0001040 2.9808 398.00 21020 2500.1 398.09 22696 2667.6 1.2504 6.1647 7.4151 10142 0001043 1.6720 419.06 2087.0 25060 419.17 22564 26756 1.3072 6.0470 7.3542 120.90 0.001047 14186 440.15 20718 25119 440.28 2243.1 26834 1.3634 5.9319 7.2952 143.38 0.001052 1.2094 461.27 20564 2517.7 46142 22297 2691.1 14188 5.8193 7.2382 169.18 0.001056 1.0360 48242 2040.9 2523.3 482.59 22160 26986 1.4737 5.7092 7.1829 198.57 0001080 089133 503.60 20253 2528.9 50381 22021 27060 1.5279 5.6013 7.1292 232.23 0001065 0.77012 524.83 20095 25343 52507 21881 2713.1 1.5816 54956 7.0771 270.28 0001070 0.6808 546.10 19934 2539.5 545.38 21737 27201 1.6346 5.3919 7.0265 313.22 0001075 058179 567.41 19773 2544,7 567.75 21591 27269 1.6872 5.2901 6.9773 361.53 0.001080 0.50850 588.77 19609 25496 589.16 21443 27335 1,7392 5.1901 6.9294 41568 0.001085 044600 610.19 19442 25544 610.64 21292 27398 1.7908 5.0919 6.8827 476.16 0.001091 0.39248 631.66 19274 25591 632.18 21138 27459 1.8418 4.9953 6,8371 543.49 0.001096 0.34648 653.19 19103 25635 653.79 20980 27518 1,8924 4.9002 6,7927 618.23 0001102 0.30680 674.79 1893.0 25678 675.47 20820 27575 19426 4.8066 6.7492 700.93 0001108 0.27244 696.46 1875.4 25719 697.24 20656 27628 1.9923 4.7143 6.7067 792.18 OGO1IM4 024260 718.20 1857.5 25757 719.08 20488 27679 2.0417 4.6233 6.6650 89260 0001121 021659 740.02 18394 25794 741.02 20317 27727 2.0906 4.5335 6.6242 10028 0.001127 0.19384 761.92 1820.9 25828 763.05 2014.2 2777.2 2.1392 4.4448 6.5841 1123.5 0.001134 0.17390 783.91 1802.1 25860 785.19 1996.2 27814 2.1875 4.3572 6.5447 12552 0.001141 0.15636 80600 17830 25890 807.43 19779 27853 2.2355 4.2705 6.5059 1398.8 0.001149 0.14089 828.18 17636 25917 829.78 19590 27888 2.2831 4.1847 5.4578 1554.9 0001157 0.12721 85046 17437 2594.2 852/26 19398 27920 2.3305 4.0997 6.4302 912 | TABLA A-5 Agua saturada. Tabla de presiones Pres., PkPa 10 15 2.0 215 3.0 4.0 5.0 75 10 15 20 25 30 40 50 75 100 101.325 125 150 175 200 225 250 2218, 300 325 350 375 400 450 500 550 600 650 700 750 Temp, sab, Ta *0 6.97 13.02 17.50 21.08 24.08 28.96 32.87 40.29 45.81 53,97 60.06 64.96 69.09 75,86 81.32 91.76 99.61 99.97 105.97 111.35 116.04 120.21 123.97 127.41 130.58 183162 136.27 138.86 141.30 143.61 147.90 151.83 155.46 158.83 161,98 164.95 Volumen espec Energía interna. mákg - klikg Líq. Vapor Lío. Vapor sat., sal, sat., Evap., sat, ve Y ue Ue Us 0.001000 129.19 29.302 2355,2 2384.5 0.001001 87.964 54.686 2338.1 2392.8 0.001001 66.990 73.431 23255 2398.9 0.001002 54.242 88.422 23154 2403.8 0.001003 45.654 100.98 23069 2407.9 0.001004 34.791 121.39 22931 24145 0.001005 28.185 137.75 22821 2419.8 0.001008 19.233 158.74 2261.1 24298 0.001010 14.670 191,79 22454 2437.2 0.001014 10.020 225.93 2222.1 24480 0.001017 7.6481 251.40 22046 2456.0 0.001020 6.2034 27193 21904 24624 0.001022 5.2287 28924 21785 2467.7 0.001026 3.9933 317.58 21588 2476.3 0.001030 3.2403 340,49 21427 2483.2 0.001037 2.2172 384.36 21118 2496.1 0.001043 1.6941 41740 20882 2505.65 0.001043 1.6734 41895 2087.0 2506.0 0.001048 1.3750 444.23 20688 25130 0.001053 1.1594 466.97 20523 2519,2 0.001057 1.0037 486.82 2037.7 2524.55 0.001061 0.88578 504.50 20246 2529,1 0.001064 0.79329 520.47 20127 25332 0.001067 0.71873 535.08 20018 2536.8 0.001070 0.65732 548.57 1991.6 2540.1 0.001073 0.60582 561.11 19821 2543.2 0.001076 0.56199 572.84 1973.1 25459 0.001079 0.52422 583,89 19646 25485 0.001081 0.49133 594.32 19566 2550,9 0.001084 0.46242 604.22 19489 2553.1 0.001088 041392 622.65 19345 2557.1 0.001093 0.37483 639.54 1921.2 2560.7 0.001097 0.34261 655.16 19088 2563.9 0.001101 031560 669.72 1897.1 2566.8 0.001104 0.29260 683.37 1886.1 2569.4 0.001108 0.27278 696.23 18756 25718 0.001111 0.25552 708.40 1865.6 2574.0 167.75 Lía. sat, 29.303 54.688 73.433 88.424 100.98 121.39 137.75 168.75 191.81 225,94 251,42 271.96 289.27 317.62 340.54 384.44 417.51 419.06 444.36 467.13 487.01 504.71 520.71 535,35 548,86 561.43 573.19 584.26 594.73 604.66 623,14 640.09 655.77 670.38 684.08 697.00 709.24 Entalpía, Hg, Evap., Ma 2484,4 2470.1 2459,5 2451.0 2443.9 2432.3 2423,0 2405.3 2392.1 2372.3 2357.5 2345.5 2335.3 2318.4 2304.7 2278.0 2257.5 2256.5 2240.56 2226.0 2213.1 2201.6 2191.0 2181.2 2172.0 2163.5 2155,4 2147.7 2140.4 2133,4 2120.3 2108.0 2096.6 2085.8 2075.5 2065.8 2056,4 Vapor sat., Rh Ml 2513.7 2524.7 253928 2539.4 2544.8 2553.7 2560.7 2574.0 2583.9 2598.3 2608.9 2617.5 2624.6 2636.1 2645,2 2662.4 2675.0 2675.56 2684.9 2693,1 2700,2 2706,3 2711.7 2716.5 2720.9 2724,9 2728.6 2732.0 2735.1 2738.1 2743.4 2748.1 2752.4 2756.2 2759.6 2752.8 27657 Lía. sat., Se 0.1059 0.1956 0.2606 0.3118 0.3543 0.4224 0.4762 0.5763 0.6492 0.7549 0.8320 0.8932 0.9441 1.0261 1.0912 1.2132 1.3028 1.3069 1.3741 1,4337 1,4850 1.5302 1.5706 1.6072 1.6408 1.5717 1.7005 1.7274 1.7526 1.7765 1.8205 1.8604 1.8970 1,9308 1.9623 1.9918 2.0195 Entropia, kJikg - K Evap.. Sy 8.8690 8.6314 8.4621 8.3302 8,2222 8.0510 7.9176 7.6738 7,4996 7,2522 7.0752 6.9370 6.8234 6.6430 6.5019 6.2426 6.0562 6.0476 5.9100 5.7894 5.6865 5.5968 5.5171 5.4453 5.3800 5.3200 5.2645 5.2128 5.1645 5.1191 5.0356 4.9603 4,8916 4.8285 4.7699 4.7153 4.6642 Vapor sat., Sy 8.9749 8.8270 8.7227 8.6421 8.5765 8.4734 8.3938 8.2501 8.1488 8.0071 7.9073 7.8302 7.7675 7.6691 7.5931 7.4558 7.3589 7.3545 7.2841 7.2231 7.1716 7.1270 7.0877 7.0525 7.0207 6.9917 6.9650 5.9402 6.9171 6.8955 6.8561 6.8207 6.7886 6.75% 6.7322 6,7071 6.6837 Apéndice 1 | 913 TABLA Agua saturada. Tabla de presiones (conclusión) Entalpía, Entropía, Volumen específico, mig m ig KdIkgo Ko Temp. — Líq. Vapor Lía. Vapor Líq. Vapor Liíq. Vapor Pres., sat, sat., sat., sat. Evap., — Sat., sat, Evap., sat, sat., Evap., sat. PkPa Ta Cv Va Us Us Ue B Eg Re Sy Sí Sy 3800 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 17294 0.001118 0.22690 731.00 1846.9 25779 731.95 20388 2770.8 2.0705 4.5705 6.6409 900 175.35 0.001121 0.21489 741.55 1838.1 25796 742.56 2030.5 2773.0 2.0941 4.5273 6.6213 950 177.66 0.001124 0.20411 751.67 18296 2581,3 752.74 20224 2775.2 2.1166 4.4862 6.6027 1000 179.88 0,001127 0.19436 761,39 18214 25828 762.51 2014.6 2777.1 2.1381 4.4470 6.5850 1100 184.06 0.001133 0.17745 779.78 18057 2585.5 781.03 19996 2780.7 2.1785 4.3735 6.5520 1200 18796 0.001138 0.16326 796.95 17909 25878 798.33 1985.4 2783.8 2.2159 4.3058 6.5217 1300 191.60 0001144 0.15119 813.10 17768 25899 814,59 19719 2786.5 2.2508 4.2428 6.4936 1400 195.04 0.001149 0.14078 828.35 17634 25918 82996 1958.9 2788.9 2.2835 4.1840 6.4675 1500 198.29 0.001154 0.13171 842.82 17506 25934 844.55 1946.4 27910 2.3143 4.1287 6.4430 1750 20572 0.001166 0.11344 876.12 1720.6 2596.7 878,16 1917.1 2795.2 2.3844 4.0033 6.3877 2000 21238 0.001177 0.099587 906.12 16930 2599,1 908.47 1889.8 2798.3 2.4467 3,8923 6.3390 2250 21841 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 2602.21 961.87 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 17949 2803,2 2.5454 3.5402 6.1856 3500 242.56 0.001235 0.057061 1045.4 15576 2603.0 1049.7 1753.0 2802.7 2.7253 3.3991 6.1244 4000 250.35 0.001252 0.049779 1082.4 15193 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 11545 1639.7 2794,2 2.9207 3.0530 5.9737 6000 275.59 0.001319 0.032449 12058 1384,1 2589.9 12138 15709 2784.6 3.0275 2.8627 5.8902 7000 285.83 0.001352 0.027378 12580 13230 2581.0 1267.5 1505.2 2772.66 3.1220 2.6927 5.8148 8000 295.01 0.001384 0.023525 1306.0 12645 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 11518 2545.2 1407.8 1317.6 2726.5 3.3603 2.2556 5.6159 11,000 318.08 0.001488 0.015988 14339 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 15484 928.7 2477.1 1571.0 1067.0 2637.9 3.6232 1.7497 5.3728 15,000 342.16 0.001657 0.010341 15855 870.3 2455.7 1610.3 1000.5 2610.8 3.6848 1.6261 5.3108 16,000 347.386 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 1690.32 857.4 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 20,000 365.758 0.002038 0.005862 1785.8 509.0 2294.83 1826.6 585.5 24121 4.0146 0.9164 4.9310 21,000 369.83 0.002207 0.004994 18416 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 21726 4.2942 0.2496 4.5439 22,064 37395 0.003106 0.003106 2015.7 0 2015.7 20843 0 2084.3 4.4070 O 4.4070 TABLA A Apéndice 1 J 915 Vapor de agua sobrecalentado (continuación) T v u h s Y y h s v U h s GC mg Kike Kg kiíkg-K|mó/kg kíkg kikg Kkikg-K [míkg ki/kg kíkg kkg-Kk P= 1.00 MPa (179,880 MPa (187,96'0) P— 1.40 MPa (195.04 dl ll alt 81 2810) Sal. 0.19437 25828 2777.1 6.5850 |0.16326 2587.8 2783.8 6.5217 [|0.14078 25918 2788.9 6.4675 200 0.20602 26223 2828.3 6.6956 |0.16934 26129 2816.1 5.5909 [014303 26027 2803.0 6.4975 250 0.23275 27104 2943.1 6.9265 |0.19241 2704.7 2935.6 6.8313 [0.16356 2698.9 2927.9 6.7488 300 0.25799 2793.7 30516 7.1245 |0.21386 2789.7 3046.3 7.0335 [018233 2785.7 3040.9 6.9553 350 0.28250 2875.7 3158,2 7.3029 [023455 2872.7 3154.2 7.2139 [020029 28697 31501 7.1379 400 0.30661 2957.9 3264.5 7.4670 [0.25482 2955.5 3261.3 7.3793 |[0.21782 2953.1 32581 7.3046 500 035411 3125.0 34791 7.7642 [0.29464 3123.4 3477.0 7.6779 [0.25216 31218 3474.8 7.6047 600 040111 3297.5 3698.6 8.0311 [0.33395 3296.3 3697.0 7.9456 |0.28597 3295.1 36955 7.8730 700 0.44783 3476.3 3924.1 8.2755 [0.37297 3475.3 39229 81904 |0.31951 34744 39217 8.1183 300 0.49438 3661.7 4156.1 8.5024 [0.41184 3661.0 4155.2 8.4176 [0.35288 3660.3 41543 8.3458 300 0.54083 3353.9 4394.8 8.7150 [0.45059 3853.3 4394.0 8.6303 [0.38614 38527 4393.3 8.5587 1000 0.58721 4052.7 4640.0 8.9155 [0.48928 4052.2 46394 8.8310 [0.41933 40517 46388 8,7595 1100 0.63354 42579 4891.4 9.1057 [0.52792 4257,5 48910 9.0212 [045247 4257.0 4890,5 8.9497 1200 0.67983 4469.0 51489 9.2866 (0.56652 4468.7 5148.5 9.2022 [0.48558 468.3 51481 9,1308 1300 0.72610 46858 5411.9 9.4593 |0.60509 4685.5 5411.6 9.3750 ¡051866 4685.1 54113 9.3036 _ P - 1.60 MPa (201.37 P= 1.80 MPa (207.11%7 | P- 2.00 MPa (212.380) Sat. 0.12374 25948 27928 6.4200 |0.11037 25973 27959 6.3775| 0.09959 2599.1 2798.3 6.3390 225 0.13293 2645.1 28578 6.5537 |(0.11678 2637.0 2847,2 6.4825| 0.10381 2628.5 2836.1 6.4160 250 0.14190 26929 29199 6.6753 |0.12502 2686,7 2911.7 6.6088| 0.11150 2680.3 2903,3 6.5475 300 0.15366 2781.6 30354 6.8864 '0.14025 2777.4 3029,9 6.8246| 0.12551 27732 30242 6.7684 350 0.17459 28666 31460 7.0713 0.15460 2863.6 3141.9 7.0120| 0.13860 2860.5 3137.7 6.9583 400 0.19007 29508 3254.9 7.2394 |0.16849 29433 3251.6 7.1814| 0.15122 29459 3248.4 7.1292 500 0.2029 3120.1 34726 7.5410 [0.19551 31185 34704 7.4845 0,17568 31169 3468,3 7.4337 600 024999 3293.92 3693.9 7.8101 [0.22200 3292,7 3692.3 7.7543| 0.19962 3291.5 3690,7 7.7043 700 0.27941 3473.5 3920.5 8.0558 |(0.24822 3472.56 3919,4 8.0005| 0,22326 3471.7 3918,2 7.9509 800 030865 3659.5 4153.4 8.2834 [0.27426 36588 4152.4 8.2284| 0,24674 3658,0 4151.5 8.1791 900 0.33780 3852. 4392.6 8.4965 |0.30020 3851.5 43919 8,4417| 027012 3850.9 4391.1 8.3925 1000 0.36687 4051.2 4638.2 8.6974 |0.32606 4050.7 46376 8.6427| 0.29342 4050.2 4637.1 8,5936 1100 0.39589 4256.65 4390.0 8.8878 |0.35188 42562 4889.5 8.8331| 0.31667 4255.7 4889.1 8.7842 1200 0.42488 4467.9 5147.7 9.0689 |0.37756 4467.6 5147.3 9.0143] 0.33989 4467.2 5147.0 8.9654 1300 0.45383 46848 5410.9 9.2418 |0.40341 46845 5410.65 91872| 036308 4684,2 5410.3 9.1384 - P 2.50 MPa(223,950) | P= 3.00 MPa (233.85'0) P- 3.50 MPa (262.567 Sat 0.07995 2602.1 28019 6.2558 |0.06667 2603,2 2803,2 6.1856| 0.05706 2603.0 2802.7 6.1244 225 0.08026 2604.8 2805.5 6.2629 250 0.08705 26633 28809 6.4107 |0.07063 2644,7 2856.5 6.2893| 0.05876 26240 2829.7 6.1764 300 0.09894 27622 3009.6 6.6459 |0.08118 27508 2994,3 6,5412| 0.06845 2738.8 2978.4 6.4484 350 0.10979 2852,5 3127.0 6.8424 |0.09056 2844.4 3116.1 6.7450| 0.07680 2836.0 31049 6.6601 400 0.12012 2939,8 3240.1 7.0170 |0.09938 2933.6 3231.7 6.9235| 0.08456 2927.2 3223.2 6.8428 450 0.13015 3026.2 3351.6 7.1768 |0.10789 30212 33449 7.0856| 0.09198 3016.1 3338.1 7.0074 500 0.1399 31128 34628 7.3254 |0.11620 31086 3457,2 7.2359| 0.09919 3104.5 34517 7.15% 500 0.15931 3288.5 3686.8 7.5979 |0.13245 3285.5 3682.8 7.5103| 0.11325 3282.5 3678.9 7.4357 700 0.17835 3469.3 3915.2 7.8455 [0.1841 3467.0 39122 7.7590| 0.12702 3464.7 3909.3 7.6855 800 0.19722 3656.2 4149.2 8.0744 [016420 3654,33 41469 7.9885| 014061 36525 4144.6 7.9156 300 0.21597 3849.4 4389.3 8.2882 |0.17988 38479 4387.5 8.2028| 0.15410 3846.4 4385.7 8.1304 1000 0.23466 4049.0 46356 8.4897 [019549 4047,.7 4634.2 8.4045| 0.16751 4046.4 4632.7 8.3324 1100 0.25330 4254.7 4887.9 8.6804 [021105 42536 4886.7 8.5955| 0.18087 4252.5 4885.6 8.5236 1200 0.27190 4466.3 5146.0 8.8618 [0.22658 44653 51451 8,7771| 0.19420 4464.4 5144.1 8.7053 1300 0.29048 4683.4 5409.5 9.0349 |0.24207 46826 5403.38 8.9502| 0.20750 46818 5408.0 8.8786 916 | Tablas de propiedades, figuras y diagramas (unidades SI) Vapor de agua sobrecalentado (continuación) da v u ñ s v u h s v “ ñ s € mig klk kike ki/kg-K| migo klk kJíkg kikg > K mó/g k/kg kl/kg o kl/kgo K P = 4.0 MPa (250.350) P= 4.5 MPa (257,440, P= 5.0 MPa (263.940) Sat. 0.0497/8 2601.7 28008 6.0696 | 0.04406 2599.7 27980 6.0198 [0.03945 2597.0 2794.2 5.9737 275 0.05461 26689 2887.3 6.2312 | 0.04733 2651.4 2864.4 6.1429 |0.04144 2632.3 2839.5 6.0571 300 0.05887 27/26.2 2961.7 6.3639 |0.05138 2713.0 29442 6.2854 |0.04535 26990 2925.7 6.2111 350 0.06647 28274 3093,3 6.5843 |0.05842 2818.6 3081.5 6.5153 |0.05197 2809.5 3069.3 6.4516 400 0.07343 2920.8 3214.5 6.7714 |0.06477 29142 3205.7 6.7071 j0.05784 2907.5 3196.7 6.6483 450 0.08004 3011.00 3331.2 6.9386 | 0.07076 30058 33242 6.8770 [0.06332 3000.6 3317.2 6.8210 500 0.08644 3100.3 3446.0 7.0922 |0.07652 3096.00 3440.4 7.0323 |0.06858 3091.8 3434.7 6,9781 600 0.09886 3279.4 3674.9 7.3706 |0.08766 3276.4 3670.9 7.3127 |0.07870 3273.3 3666.9 7.2605 700 0.11098 34624 3906.3 7.6214 |0.09850 3460.0 3903.3 7.5647 [0.08852 3457.7 3900.3 7.5136 800 0.12292 3650.6 41423 7.8523 |0.10916 36488 4140.0 7.7962 [0.09816 3646.9 4137.7 7.7458 900 0.134/6 38448 43839 8.06/5 |0.11972 38433 4382.1 8.0118 |0.10769 3841.8 4380.2 7.9619 1000 0.14653 4045,1 46312 8.2698 | 0.13020 40439 46298 8.2144 |0.11715 4042.6 46283 8.1648 1100 0.15824 42514 4884.4 8.4612 | 0.14064 4250.4 48832 8.4060 [012655 4249,3 4882.1 8.3566 1200 0.16992 4463,5 5143,2 8.6430 |0.15103 44626 51422 8.5880 |0.13592 44616 51413 8.5388 1300 0.18157 4680.9 5407.2 8.8164 |0.16140 4689.1 54065 8.7618 |0.14527 4679.3 5405.7 8.7124 __P.= 6.0 MPa (275.59*C) P = 7.0 MPa (285.830) P = 8.0 MPa (295.010) Sat. 0.03245 25899 2784.86 5.8902 | 0.027378 2581.0 27726 5.8148 [0.023525 2570.5 2758.7 5.7450 300 0.03619 2668.4 2885.6 6.0703 | 0.029492 2633.5 28399 5.9337 |0.024279 2592.3 2786.5 5.7937 350 0.04225 2790.4 30439 6.3357 |0.035262 2770.1 3016.9 6.2305 |0.029975 2748.3 2988,1 6.1321 400 0.04/42 2893.7 31783 6.5432 |0.039958 2879,5 31592 5.4502 |0.034344 2864.65 3139.4 6.3658 450 0.05217 2989.9 3302.9 6.7219 | 0.044187 29790 32883 6.6353 |0.038194 2967.8 3273.3 6.5579 500 0.0566/ 3083.1 34231 6.8826 | 0.048157 30743 3411.4 5.8000 |0.041757 30585,4 3399.5 6.7266 550 0.06102 3175,2 3541.3 7.0308 | 0.051966 31979 35316 6.9507 [|0.045172 3150,.5 35218 $.8800 600 0.06527 3267.2 36588 7.1693 |0.055665 32610 3650,8 7.0910 |0.048463 32547 36424 7.0221 700 0.07355 34530 3894.3 7.4247 | 0.062850 3448.3 38883 7.3487 [0.054829 34436 3882.2 7.2822 800 0.08165 36432 41331 7.6582 | 0.069856 36395 41285 7.5836 |0.061011 3635.7 41238 7.5185 900 0.08964 3838.8 4376.6 7.8751 |0.076750 3835.7 43730 7.8014 [0.067082 3832.7 4369.3 7.7372 1000 0.09756 4040.1 4625.4 8.0786 | 0.033571 4037.5 4622.55 8.0055 |0.073079 4035.0 46196 7.9419 1100 010543 42471 4879.7 8,2709 |0.090341 42450 4877.4 8,1982 |0.079025 4242.8 4875.0 8.1350 1200 0.11326 44598 51394 8.4534 |0.097075 4457.9 51374 8.3810 |0.084934 4456.1 5135,5 3.3181 1300 9.12107 4677,7 5404.1 8.6273 |0.103781 4676.1 5402.6 855551 |0.090817 46745 5401.0 8,4925 _ P= 9.0 MPa(303,350) _P= 10.0 MPa (311.000) | P»12.5 MPa(327.81%0) Sat. — 0.020489 25585 2742.9 5.6791 |0.018028 2545.2 27255 5.5159 [0.013496 2505.6 26743 5.4638 328 0.023284 2647.6 28571 5.8738 |0.019877 2611.6 2810.3 5.7596 350 0.0258162725.0 2957.3 6.0380 |0.022440 2699.68 2924.0 5.9460 |0.016138 26249 2826.6 5.7130 400 0.029960 2849.2 31188 6.2876 |0.026436 2833.1 3097.5 6.2141 |0.020030 27895 3040.0 6.0433 450 0.033524 29563 32580 6.4872 | 0.029782 2944.5 32424 6.4219 [0.023019 2913.7 3201.5 6.2749 500 0.036/93 30563 3387.4 6.6603 |0.032811 3047.0 3375.1 6.5995 |0.025630 3023.2 3343.6 6.4651 550 0.039885 3153.0 35120 6.8164 | 0035655 3145.4 35020 6.7585 |0.028033 31261 3476.5 6.6317 600 0.042861 32484 3634.1 6.9605 |0.038378 32420 36258 6.9045 |0.030308 3225.8 3604.6 6.7828 650 0.045755 3343.4 3755.2 7.0954 |0.041018 3338.0 3748.1 7.0408 [0.032491 3324.1 3730.2 6.9227 700 0.048589 34388 3876.1 7.2229 |0.043597 34340 3870.0 7.1693 [0.034612 34220 3854.6 7.0540 800 0.0541323632.0 4119.2 7.4606 |0.048629 36282 41145 7.4085 |0.038724 36188 41028 7.2967 200 0.059562 3829.56 4365.7 7.6802 | 0.053547 3826.5 4362.0 7.6290 [0.042720 3818.9 4352.9 7.5195 1000 0.064919 40324 4616.7 7.8855 | 0.058391 40299 4613.8 7.8349 |0.046641 4023.5 4606.5 7.7269 1100 0.070224 4240.7 4872.7 8.0791 |0.063183 4238.53 4870.3 8.0289 |0.050510 4233.1 4854.5 7.9220 1200 0.075492 4454.2 51336 8.2625 | 0.067938 44524 51317 8.2126 |0.054342 4447.7 5127.0 8,1065 1300 0.080733 4672.9 5399.58 8.4371 |0.072667 46713 53980 8.3874 |0.058147 4667.3 5394.1 8.2819 318 Tablas de propiedades, figuras y diagramas (unidades SI) TABLA A Agua líquida comprimida T v u h s v u h s v L h s “Cc mékg kikg kiíkg k/kg-K mg kJíkg «kg «kg-K|mi/kg o kikg kikg kikg:K P= 5 MPa (263.940) P= 10 MPa (311.000) P= 15 MPa (342 160) _ Sat. 0.0012862 1148.1 11545 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 1507 0.0004 20 0.0009996 8361 88.61 0.2954 | 0.0009973 83.31 93.28 0.2943 [0.0009951 83.01 97.93 0.2932 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 332.69 352.94 1.0691 |0.0010221 33159 346.92 1.0659 100 0.0010410 417.65 422.85 1.3034 | 0.0010385 41623 426.62 1.2996 |0.0010361 414.85 430.39 1.2958 120 0.0010576 $01.91 507.19 1,5236 | 0,.0010549 500.18 510,73 1,5191 ¡00010522 498.50 514.28 1.5148 140 0.0010769 586.80 592.18 1.7344 |0.0010738 583.72 59545 1,7293 |0.0010708 582.69 598,75 1.7243 160 0.0010988 672.55 678.04 1.9374 | 0.0010954 670.08 681.01 1.9316 |0.0010920 667.63 684.01 1.9289 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 340.84 858.00 2.3100 220 0.0011868 938,39 94432 2.5127 | 0.0011809 934,01 945.82 2.5037 |0.0011752 929.81 947.43 2.4951 240 0.0012268 1031.6 10377 2.6983 | 0.0012192 1026.2 10383 2.6876 |0.0012121 1021.0 1039.2 2,6774 260 0.0012755 1128.5 11349 2.8841 | 0.0012653 11216 11343 2.8710 [|0.0012560 1115.1 1134.0 2.8586 280 0.0013225 1221.8 12350 3.0565 |0.0013096 12134 12330 3.0410 300 00013980 13294 13433 3.2488 |0.0013783 1317.6 13383 3.2279 320 0.0014733 1431.9 1454,0 3,4263 340 0.0016311 15679 15924 3.6555 P= 20 MPa (365.250) P= 30 MPa P= 50 MPa Sat. 0.0020378 1785.8 18266 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 8271 102.57 0.2921 [0.0009886 82.11 111.77 02897 [0.0009805 80.93 12995 0.2845 40 0.0009992 165.17 185.16 0.5646 | 0.0009951 16405 19390 05607 |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 30 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 ¡0.0010290 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 | 00010823 576.90 608.76 1.7098 |0.0010517 569.77 62236 1.6916 160 (0.0010886 665.28 687.05 1.9203 | 0.0010823 $60.74 693.21 1.9094 |0.0010704 652.33 705.85 1.8889 1380 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 83749 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 11340 2.8469 | 0.0012314 10978 11347 2.8250 | 00012044 10782 11384 2.7864 280 0.0012978 1205.6 12315 3.0265 | 0.0012770 1191.5 12298 3,0001 |0.0012430 1167,7 1229,9 2,9547 300 0.0013611 1307.2 13344 3.2091 |0.0013322 1288.9 13289 3.1761 [0.0012879 12596 13240 3.1218 320 0.0014450 1416.6 14455 3.3996 | 0.0014014 1391.27 14337 3133558 | 0.0013309 13543 14214 3.2888 340 0.0015693 1540.2 1571.6 3.6086 | 0.0014932 1502.4 15471 3.5438 |0.0014049 14529 1823.1 3.4575 360 0.0018248 1703.6 1740.1 38787 | 0.0016275 16268 16756 3.7499 [00014848 1556.5 1630.7 3.6301 380 0.0018729 1782.0 1838,2 3.0026 ¡0.0015884 1667.1 1746.5 3.8102 Apéndice 1 | 919 TA 2-8 Hielo saturado. Vapor de agua Volumen especifico. Energía interna, Entalpía, Entrepía, E kJ/kg «J/kg a o A Pres. Hielo Vapor Hielo Vapor Hielo Vapor Hielo Vapor Temp., sat, sat, sab, sat. Subl., sat, sat., Subl., Ssat., sat, Subl., sat, TO Raga Y Ue Y Y, le 1 ME 0.01 0.61169 0.001091 205.99 -333.40 2707.9 2374.5 -333.40 2833.9 2500.5 -1.2202 10.374 9.154 o 0.61115 0.001091 206,17 -333,43 2707.9 2374.5 -333.43 2833.9 2500.5 -1.2204 10.375 9.154 2 0.51772 0.001091 241.62 -337.63 2709.4 2371.8 -337.63 2834.5 24968 -1.2358 10.453 9,218 4 0.43748 0.001090 283,84 -341.80 2710.8 23690 -341.80 2835.0 24932 -1.2513 10.533 9.282 6 0.36873 0.00109D 334.27 -345.94 2712.2 2366.2 -345.93 2835.4 24895 -1.2667 10,613 9.347 E 0.30998 0.001090 394,66 -350.04 2713.5 2363.5 -350.04 2835.8 24858 -1.2821 10.695 9.413 10, 0.25990 0.001089 467,17 -354.12 27148 2360,7 -354.12 2836.2 2482.1 -1.2976 10.778 9.480 12 0,21732 0,001089 554.47 -358.17 2716.1 2357.9 -358.17 2836.6 2478.4 —1.3130 10.862 9.549 -14 0.18121 0.001088 659.88 -362.18 2717.3 2355.2 -362.18 2836.9 2474,7 -1.3284 10.947 9.618 -16 0,15068 0.001088 787.51 -366.17 2718.6 23524 -366.17 2837.2 2471.0 -1.3439 11.033 9.689 -18 0.12492 0.001088 942.51 -370.13 2719.7 23496 -370.13 2837.5 2467.3 -1.3593 11.121 9.761 20 0,10326 0.001087 1131.3 374,06 2720.9 23468 -374.06 2837.7 2463.6 1.3748 21.209 9.835 22 0.08510 0.001087 13620 -377.95 2722.0 2344.1 377.95 28379 24599 -1.3903 11.300 9.909 -24 0.06991 0001087 1644.7 381.82 2723.1 2341.3 -381.82 2838.1 2456.2 -1.4057 11.391 9.985 -26 0.05725 0.001087 19922 -385.66 2724.2 23385 -385.66 2838,2 2452.5 -—1.4212 11.484 10.063 -28 0.04673 0.001086 2421.0 -389.47 2725.2 2335,7 -389.47 2838,3 2448.8 -1.4367 11.578 10.141 30 0.03802 0.001086 2951.7 -393.25 27262 23329 -—393.25 2838.4 2445.1 —1.4521 11.673 10.221 =33 0.03082 0.001086 3610.9 397.00 2727.2 2330.2 -397.00 2838.4 24414 -1.4676 11.770 10.303 34 0.02490 0.001085 443214 -400.72 2728.1 2327.4 -400.72 2838.5 2437.7 -1.4831 11.869 10.386 36 0.02004 0.001085 5460.1 -404.40 27290 2324.6 -404.40 2838.4 2434.0 -1.4986 11.969 10.470 -38 0.01608 0.001085 6750.5 -408.07 27299 23218 -408.07 2838.4 2430.3 -1.5141 12.071 10.557 40 0.01285 0.001084 8376.7 -411.70 2730.7 23190 -411.70 2838,3 2426.66 -1.5296 12.174 10.644 hy he Ss 5 S Apéndice 1 | 921 E] 0. 5000 y 5000 4000 4000 2 E 2 E om |-> 3000 3 pa] 2000 000 E 1000 gl 10 Entropía, KJ/Kg + K FIGURA A-10 Diagrama de Mollicr para el agua. Copyrigia O 1984. De NESINRO Steam Tubles/) por Lester Huar, Joln $. Gallagher y George S. Kell, Reproducido con permiso de Rowaledee/Taylor « Francis Books, inc. 922 J Tablas de propiedades, figuras y diagramas (unidades Sl) TABLA 4-11 Refrigerante 134a saturado, Tabla de temperatura Volumen específico. Energía interna, Entaipia, Mg Ek . ES 3 Pres. Líg. Vapor Lía. Vapor — Líq. Vapor Líq. Temp., sat., sal., sal., sat., Evap., sat., sat., Evap., sat, sat., Evap., sat, TC PojpkPa v, Vo Ue Us U he Pa Ro ES Sig Sa -40 51.25 0.0007054 0.36081 —0.036 207.40 207.37 0.000 225.86 225.86 0.00000 0.96866 0.96866 -38 56.86 0.0007083 0.32732 2.475 206.04 208.51 2.515 224.61 227.12 0.01072 0.95511 0.96584 36 62.95 0.0007112 0.29751 4.992 204.67 209.66 5.037 22335 228.39 0.02138 0.94176 0.96315 -34 6956 0.0007142 0.27090 7.517 203.29 210.81 7.566 222.09 229.65 0.03199 0.92859 0.96058 -32 76.71 0.0007172 0.24711 10.05 201.91 211.96 10.10 220.81 230.91 0.04253 0.91560 0.95813 -30 84.43 0.0007203 0.22580 12.59 200.52 213.11 12.65 21952 232.17 0.05301 0.90278 0.95579 -28 92.76 0.0007234 0.20666 15.13 19912 214.25 1520 218.22 233.43 006344 089012 0.95356 -26 101.73 0.0007265 0.18948 17.69 197.72 215.40 17.76 216.92 234.68 0.07382 0.87762 0.95144 24 111.37 0.0007297 0.17395 20.25 19630 216.55 2033 215.59 23592 0.08414 0.86527 0.94941 -22 121.72 0.0007329 0.15995 22.82 19488 217.70 2291 214.26 s237.17 0.09441 085307 0.94748 -20 13282 0.0007362 0.14729 2539 193.45 218.84 25.49 21291 238.41 0,10463 084101 0.94564 -18 144.69 0.0007396 0.13583 27.98 192.01 21998 28.09 211.55 239.64 0.11481 082908 0.94389 -16 157.38 0.0007430 0.12542 3057 190.56 221.13 30.69 210.18 240.87 012493 081729 094222 -14 170.93 0.0007464 0.11597 33.17 189.09 222.27 33.30 208.79 242.09 0.13501 0.80561 0.94063 -12 185.37 0.0007499 0.10736 35.78 187.62 223,40 35.92 207.38 243,30 0,14504 0.79406 0.93911 -10 200.74 0.0007535 0.099516 38.40 186.14 224,54 38.55 205.96 244,51 C.15504 0.78263 0.93766 -8 217.08 0.0007571 0.092352 41,03 184,64 225.67 41.19 204.52 245.72 0.16498 0.77130 0.93629 =6 234.44 0.0007608 0.085802 43.66 183.13 226.80 4384 203.07 246.91 0.17489 076008 0.93497 =4 252.85 0.0007646 0.079804 46.31 181.61 227.92 46.50 201.60 248.10 0,18476 0.74896 0.93372 -2 27236 0.0007684 0.074304 48.96 180.08 229.04 49.17 200,11 249.28 0,19459 0.73794 0.93253 O 293.01 0.0007723 0.069255 51.63 178.53 230.16 51.86 198.60 250.45 020439 0.72701 0.93139 2 314.84 0.0007763 0.064612 54.30 176.97 231.27 54,55 197.07 251.61 0.21415 0.71616 0.93031 4 337.90 0.0007804 0.060338 56.99 175.39 232.38 57.25 195.51 252.77 0.22387 0.70540 0.92927 6 362.23 0.0007845 0.056398 59.68 173.80 233.48 59.97 193.94 253.91 0.23356 0.69471 092828 8 387,88 0.0007887 0.052762 62.39 172.19 234.58 62.69 192.35 255.04 0.24323 0.68410 0.92733 10 414.89 0.0007930 0.049403 65.10 170.56 235.67 65.43 190.73 256.16 0.25286 0.67356 0.92641 12 443.31 0.0007975 0.046295 67.83 16892 236.75 68.18 189.09 257,27 0.26246 0.66308 0.92554 14 473.19 0.0008020 0.043417 70.57 167.26 237.83 70.95 187.42 258.37 0.27204 065266 0.92470 16 504.58 0.0008066 0.040748 73.32 165.58 238.90 73.73 185,73 259.46 028159 064230 0.92389 18 537.52 0.0008113 0.038271 76.08 163.88 239.96 76.52 184.01 260.53 0.29112 0.63198 0.92310