Tabla de Propieades Termodinamicas SI

APÉNDICE1 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) Tabla A-1 Masa molar, constante de gas y propiedades del punto crítico Tabla A-21 Propiedades de gas ideal del monóxido de carbono, CO Tabla A-2 Calores específicos de gas ideal de varios gases comunes Tabla A-22 Propiedades de gas ideal del hidrógeno, H2 Tabla A-3 Propiedades de líquidos, sólidos y alimentos comunes Tabla A-23 Propiedades de gas ideal del vapor de agua, H2O Tabla A-4 Tabla A-5 Tabla A-6 Tabla A-7 Tabla A-8 Figura A-9 Figura A-10 Tabla A-11 Agua saturada. Tabla de temperaturas Tabla A-24 Propiedades de gas ideal del oxígeno monoatómico, O Tabla A-25 Propiedades de gas ideal del hidroxilo, OH Tabla A-26 Entalpía de formación, función de Gibbs de formación y entropía absoluta a 25°C, 1 atm Diagrama de Mollier para el agua Tabla A-27 Refrigerante 134a saturado. Tabla de temperatura Propiedades de algunos combustibles e hidrocarburos comunes Tabla A-28 Refrigerante 134a saturado. Tabla de presión Logaritmos naturales de la constante de equilibrio Kp Figura A-29 Carta generalizada de desviación de entalpía Diagrama P-h para refrigerante 134a Figura A-30 Carta generalizada de desviación de entropía Tabla A-12 Agua saturada. Tabla de presiones Vapor de agua sobrecalentado Agua líquida comprimida Hielo saturado. Vapor de agua Diagrama T-s para el agua Tabla A-13 Figura A-14 Figura A-15 Refrigerante 134a sobrecalentado Carta generalizada de compresibilidad de Nelson-Obert Figura A-31 Tabla A-16 Propiedades de la atmósfera a gran altitud Carta psicrométrica a 1 atm de presión total Tabla A-32 Tabla A-17 Tabla A-18 Propiedades de gas ideal del aire Funciones de flujo compresible unidimensional e isentrópico de un gas ideal con k  1.4 Tabla A-33 Funciones de choque normal unidimensional de un gas ideal con k  1.4 Tabla A-34 Funciones del flujo de Rayleigh para un gas ideal con k  1.4 Tabla A-19 Tabla A-20 Propiedades de gas ideal del nitrógeno, N2 Propiedades de gas del oxígeno, O2 Propiedades de gas ideal del dióxido de carbono, CO2 http://librosysolucionarios.net 18Appendix_01 ITALICAS.qxd 907 7/12/11 14:25:57 908 TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-1 Masa molar, constante de gas y propiedades del punto crítico Sustancia Fórmula Agua Aire Alcohol etílico Alcohol metílico Amoniaco Argón Benceno Bromo n-Butano Cloro Cloroformo Cloruro metílico Criptón Diclorodifluorometano (R-12) Diclorofluorometano (R-21) Dióxido de carbono Dióxido de sulfuro Etano Etileno Helio n-Hexano Hidrógeno (normal) Metano Monóxido de carbono Neón Nitrógeno Óxido nitroso Oxígeno Propano Propileno Tetracloruro de carbono Tetrafluoroetano (R-134a) Triclorofluorometano (R-11) Xenón H2O — C2H5OH CH3OH NH3 Ar C 6 H6 Br2 C4H10 Cl2 CHCl3 CH3Cl Kr CCl2F2 CHCl2F CO2 SO2 C 2 H6 C2H4 He C6H14 H2 CH4 CO Ne N2 N 2O O2 C 3 H8 C3H6 CCl4 CF3CH2F CCl3F Xe Propiedades del punto crítico Masa molar, M kg/kmol Constante de gas, R kJ/kg · K* Temperatura, K 18.015 28.97 46.07 32.042 17.03 39.948 78.115 159.808 58.124 70.906 119.38 50.488 83.80 120.91 102.92 44.01 64.063 30.070 28.054 4.003 86.179 2.016 16.043 28.011 20.183 28.013 44.013 31.999 44.097 42.081 153.82 102.03 137.37 131.30 0.4615 0.2870 0.1805 0.2595 0.4882 0.2081 0.1064 0.0520 0.1430 0.1173 0.06964 0.1647 0.09921 0.06876 0.08078 0.1889 0.1298 0.2765 0.2964 2.0769 0.09647 4.1240 0.5182 0.2968 0.4119 0.2968 0.1889 0.2598 0.1885 0.1976 0.05405 0.08149 0.06052 0.06332 647.1 132.5 516 513.2 405.5 151 562 584 425.2 417 536.6 416.3 209.4 384.7 451.7 304.2 430.7 305.5 282.4 5.3 507.9 33.3 191.1 133 44.5 126.2 309.7 154.8 370 365 556.4 374.2 471.2 289.8 Presión, MPa 22.06 3.77 6.38 7.95 11.28 4.86 4.92 10.34 3.80 7.71 5.47 6.68 5.50 4.01 5.17 7.39 7.88 4.48 5.12 0.23 3.03 1.30 4.64 3.50 2.73 3.39 7.27 5.08 4.26 4.62 4.56 4.059 4.38 5.88 Volumen, m3/kmol 0.0560 0.0883 0.1673 0.1180 0.0724 0.0749 0.2603 0.1355 0.2547 0.1242 0.2403 0.1430 0.0924 0.2179 0.1973 0.0943 0.1217 0.1480 0.1242 0.0578 0.3677 0.0649 0.0993 0.0930 0.0417 0.0899 0.0961 0.0780 0.1998 0.1810 0.2759 0.1993 0.2478 0.1186 *La unidad en kJ/kg · K es equivalente a kPa · m3/kg · K. La constante de gas se calcula de R  Ru /M, donde Ru  8.31447 kJ/kmol · K y M es la masa molar. Fuente: K. A. Kobe y R. E. Lynn, Jr., Chemical Review 52 (1953), pp. 117–236; y ASHRAE, Handbook of Fundamentals (Atlanta, GA: Sociedad Americana de Ingenieros de Calefacción, Refrigeración y Acondicionamiento de Aire, Inc., 1993), pp. 16.4 y 36.1. http://librosysolucionarios.net 18Appendix_01 ITALICAS.qxd 908 7/12/11 14:25:58 909 APÉNDICE 1 TABLA A-2 Calores específicos de gas ideal de varios gases comunes a) A 300 K Gas Fórmula Aire Argón Butano Dióxido de carbono Etano Etileno Helio Hidrógeno Metano Monóxido de carbono Neón Nitrógeno Octano Oxígeno Propano Vapor — Ar C4H10 CO2 C2H6 C2H4 He H2 CH4 CO Ne N2 C8H18 O2 C3H8 H2O Constante de gas, R kJ/kg · K 0.2870 0.2081 0.1433 0.1889 0.2765 0.2964 2.0769 4.1240 0.5182 0.2968 0.4119 0.2968 0.0729 0.2598 0.1885 0.4615 cp kJ/kg · K cv kJ/kg · K k 1.005 0.5203 1.7164 0.846 1.7662 1.5482 5.1926 14.307 2.2537 1.040 1.0299 1.039 1.7113 0.918 1.6794 1.8723 0.718 0.3122 1.5734 0.657 1.4897 1.2518 3.1156 10.183 1.7354 0.744 0.6179 0.743 1.6385 0.658 1.4909 1.4108 1.400 1.667 1.091 1.289 1.186 1.237 1.667 1.405 1.299 1.400 1.667 1.400 1.044 1.395 1.126 1.327 Nota: La unidad kJ/kg · K es equivalente a kJ/kg · °C. Fuente: Chemical and Process Thermodynamics 3a. ed., por Kyle, B.G., © 2000. Adaptado con permiso de Pearson Education, Inc., Upper Saddle River, Nueva Jersey. http://librosysolucionarios.net 18Appendix_01 ITALICAS.qxd 909 7/12/11 14:25:58 910 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 Temperatura, K cp kJ/kg · K cv kJ/kg · K cp kJ/kg · K k Aire 250 300 350 400 450 500 550 600 650 700 750 800 900 1000 1.003 1.005 1.008 1.013 1.020 1.029 1.040 1.051 1.063 1.075 1.087 1.099 1.121 1.142 0.716 0.718 0.721 0.726 0.733 0.742 0.753 0.764 0.776 0.788 0.800 0.812 0.834 0.855 14.051 14.307 14.427 14.476 14.501 14.513 14.530 14.546 14.571 14.604 14.645 14.695 14.822 14.983 9.927 10.183 10.302 10.352 10.377 10.389 10.405 10.422 10.447 10.480 10.521 10.570 10.698 10.859 k Dióxido de carbono, CO2 1.401 1.400 1.398 1.395 1.391 1.387 1.381 1.376 1.370 1.364 1.359 1.354 1.344 1.336 0.791 0.846 0.895 0.939 0.978 1.014 1.046 1.075 1.102 1.126 1.148 1.169 1.204 1.234 Hidrógeno, H2 250 300 350 400 450 500 550 600 650 700 750 800 900 1000 cv kJ/kg · K 0.602 0.657 0.706 0.750 0.790 0.825 0.857 0.886 0.913 0.937 0.959 0.980 1.015 1.045 1.314 1.288 1.268 1.252 1.239 1.229 1.220 1.213 1.207 1.202 1.197 1.193 1.186 1.181 cp kJ/kg · K 1.039 1.039 1.041 1.044 1.049 1.056 1.065 1.075 1.086 1.098 1.110 1.121 1.145 1.167 0.742 0.743 0.744 0.747 0.752 0.759 0.768 0.778 0.789 0.801 0.813 0.825 0.849 0.870 1.400 1.400 1.399 1.397 1.395 1.391 1.387 1.382 1.376 1.371 1.365 1.360 1.349 1.341 k Monóxido de carbono, CO 1.039 1.040 1.043 1.047 1.054 1.063 1.075 1.087 1.100 1.113 1.126 1.139 1.163 1.185 Nitrógeno, N2 1.416 1.405 1.400 1.398 1.398 1.397 1.396 1.396 1.395 1.394 1.392 1.390 1.385 1.380 cv kJ/kg · K 0.743 0.744 0.746 0.751 0.757 0.767 0.778 0.790 0.803 0.816 0.829 0.842 0.866 0.888 1.400 1.399 1.398 1.395 1.392 1.387 1.382 1.376 1.370 1.364 1.358 1.353 1.343 1.335 Oxígeno, O2 0.913 0.918 0.928 0.941 0.956 0.972 0.988 1.003 1.017 1.031 1.043 1.054 1.074 1.090 0.653 0.658 0.668 0.681 0.696 0.712 0.728 0.743 0.758 0.771 0.783 0.794 0.814 0.830 1.398 1.395 1.389 1.382 1.373 1.365 1.358 1.350 1.343 1.337 1.332 1.327 1.319 1.313 Fuente: Kenneth Wark, Thermodynamics, 4a. ed., Nueva York, McGraw-Hill, 1983, p. 783, Tabla A-4M. Publicada originalmente en Tables of Thermal Properties of Gases, NBS Circular 564, 1955. http://librosysolucionarios.net 18Appendix_01 ITALICAS.qxd 910 7/12/11 14:25:58 911 APÉNDICE 1 TABLA A-2 Calores específicos de gas ideal de varios gases comunes (conclusión) c) Como una función de la temperatura _ cp  a  bT  cT 2  dT 3 (T en K, cp en kJ/kmol · K) Sustancia Acetileno Aire Amoniaco Azufre Benceno i-Butano n-Butano Cloruro de hidrógeno Dióxido de azufre Dióxido de carbono Dióxido de nitrógeno Etano Etanol Etileno n-Hexano Hidrógeno Metano Metanol Monóxido de carbono Nitrógeno Óxido nítrico Óxido nitroso Oxígeno n-Pentano Propano Propileno Trióxido de azufre Agua (vapor) Fórmula C2H2 — NH3 S2 C6H6 C4H10 C4H10 a 21.8 28.11 27.568 27.21 36.22 7.913 3.96 b 9.2143 0.1967 2.5630 2.218 48.475 41.60 37.15 c        102 102 102 102 102 102 102 6.527 0.4802 0.99072 1.628 31.57 23.01 18.34 Rango de temp., K d        105 105 105 105 105 105 105 18.21 1.966 6.6909 3.986 77.62 49.91 35.00        109 % de error Máx. Prom. 109 109 109 109 109 109 273–1500 273–1800 273–1500 273–1800 273–1500 273–1500 273–1500 1.46 0.72 0.91 0.99 0.34 0.25 0.54 0.59 0.33 0.36 0.38 0.20 0.13 0.24 HCl 30.33 0.7620  102 1.327  105 4.338  109 273–1500 0.22 0.08 SO2 25.78 5.795  102 3.812  105 8.612  109 273–1800 0.45 0.24 CO2 22.26 5.981  102 3.501  105 7.469  109 273–1800 0.67 0.22 NO2 C2H6 C2H6O C2H4 C6H14 H2 CH4 CH4O 22.9 6.900 19.9 3.95 6.938 29.11 19.89 19.0 5.715  102 17.27  102 20.96  102 15.64  102 55.22  102 0.1916  102 5.024  102 9.152  102 3.52 6.406 10.38 8.344 28.65 0.4003 1.269 1.22         105 105 105 105 105 105 105 105 7.87 7.285 20.05 17.67 57.69 0.8704 11.01 8.039         109 109 109 109 109 109 109 109 273–1500 273–1500 273–1500 273–1500 273–1500 273–1800 273–1500 273–1000 0.46 0.83 0.40 0.54 0.72 1.01 1.33 0.18 0.18 0.28 0.22 0.13 0.20 0.26 0.57 0.08 CO N2 NO N2O O2 C5H12 C3H8 C3H6 28.16 0.1675  102 28.90 0.1571  102 29.34 0.09395  102 24.11 5.8632  102 25.48 1.520  102 6.774 45.43  102 4.04 30.48  102 3.15 23.83  102 0.5372 0.8081 0.9747 3.562 0.7155 22.46 15.72 12.18         105 105 105 105 105 105 105 105 2.222 2.873 4.187 10.58 1.312 42.29 31.74 24.62         109 109 109 109 109 109 109 109 273–1800 273–1800 273–1500 273–1500 273–1800 273–1500 273–1500 273–1500 0.89 0.59 0.97 0.59 1.19 0.56 0.40 0.73 0.37 0.34 0.36 0.26 0.28 0.21 0.12 0.17 SO3 H2O 16.40 32.24 32.42  109 3.595  109 273–1300 273–1800 0.29 0.53 0.13 0.24 14.58  102 0.1923  102 11.20  105 1.055  105 Fuente: B. G. Kyle, Chemical and Process Thermodynamics, Englewood Cliffs, Nueva Jersey, Prentice Hall, 1984. Usada con permiso. http://librosysolucionarios.net 18Appendix_01 ITALICAS.qxd 911 7/12/11 14:25:58 18 4.79 2.19 4.3 800.97 2.2 25.9 96.5 56.11 1.22 2.1 251 217.7 108 322.9 252.80 4.8 10.5 105. kJ/kg Datos de congelación Punto de congelación.5 218.59 2.7 510.00 1.28 0.6 — — 103.1 974 22. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-3 Propiedades de líquidos.14 1.0 Queroseno Refrigerante 134a Salmuera (20% de cloruro de sodio a base másica) 204–293 26.7 210 99.80 1. kJ/kg Aceite comestible (ligero) Agua 100 2257 0.06 2.5 195.9 — 17.560 423 301 787 809 596 703 1141 640 581 529 449 820 1443 1.1 306.46 2.5 0 25 20 20 268. kg/m3 Calor específico cp.4 28 126 80.qxd 912 7/12/11 14:25:59 .8 18.7 25 161.9 80.912 TABLAS DE PROPIEDADES. También.72 2.13 2. el dióxido de carbono existe como un sólido o un gas.7 161.6 114.18 4.1 179.7 Alcohol etílico Amoniaco 78.8 1100 198.8 183 — 42.4* 78.2 10. °C Calor latente de fusión hif .3 20 0 25 185.2 109 181.7 187.49 5.6 97.5 78.3 855 1357 156 77. °C hfg .8 180.5 138.25 2.8 160 20 183 20 42.) http://librosysolucionarios.8 11.2 70.1 0 25 Densidad r.2 160 38.9 — 259.5 161.5°C.139 3.8 11.43 * Temperatura de sublimación.22 4.60 4.32 22.0 2.3 Argón Benceno n-Butano Dióxido de carbono Etanol Etilén glicol Glicerina Helio Hidrógeno Isobutano Mercurio Metano 185.8 445.84 4.4 58.7 356. kJ/kg · K 910 1000 997 988 975 958 789 682 665 639 602 1394 879 601 298 783 1109 1261 146.9 182.5 (a 0°C) 838.2 230.6 33.0 24.84 2.7 11.10 1.2 198. sólidos y alimentos comunes a) Líquidos Datos de ebullición a 1 atm Sustancia Punto Calor latente de de ebullivaporización ción normal. (A presiones por debajo de la presión de punto triple de 518 kPa.71 2.4 — Propiedades de líquidos Temperatura.31 0.1 294. °C 25 0 25 50 75 100 20 33.8 13.27 1.7 367.2 0.7 80.43 4.6 20 0.5 100 25 195.3 5.3 212.1 200.9 268.8 57.6 — 59.23 1150 1374 1295 1207 3.7 13.4 189.53 3.4 Metanol Nitrógeno 64.6 394 385. la temperatura de punto de congelamiento del dióxido de carbono es la temperatura de punto triple de –56.55 2.3 Octano Oxígeno Petróleo Propano 124.9 252.52 4.1 0 50 20 50 20 26.7 230–384 427.7 593.0 2.34 1.net 18Appendix_01 ITALICAS.0 333. 02 Calor latente de fusión.79 4. versión SI.52 3. encino.32 1.78 1. 2% Zn.730 8.8 0.86 3. El punto de congelación es la temperatura a la que comienza la congelación para frutas y verduras.) Maderas suaves (abeto.89 1. °C 5.6 0.367 0.95 2.400 2.86 2. etc.949 0.32 3.840 8. http://librosysolucionarios.4 0.6 — 1.2 0. % (masa) Helado Mantequilla Manzanas Naranjas Papas Pavo Plátanos Queso suizo Salmón Sandía Tomates (maduros) 63 16 84 87 78 64 75 39 64 93 94 Punto de congelación.04 1.900 1520 1000 2110 1100 1150 2300 2420 2500 2700 0. Inc.830 0.21 1. pino.01 1.65 3. 35% Zn) Magnesio Níquel Plata Plomo Tungsteno 7.616 0.04 1.2 2.95 — 3.000 0.38 0.77 1. American Society of Heating.6 0.6 Calor específico.1 0.82 1. kJ/kg · K Por encima Por debajo del punto del punto de congede congelación lación 2.79 0.997 0.35 2. kJ/kg 301 277 247 224 267 311 301 247 294 317 247 Alimentos Contenido de agua.8 0.02 3.913 APÉNDICE 1 TABLA A-3 Propiedades de líquidos.90 1. kJ/kg 210 53 281 291 261 214 251 130 214 311 314 Fuente: Los valores han sido obtenidos de varios manuales y otras fuentes.342 0.128 0. 2% Al) Cobre 173°C 100°C 50°C 0°C 27°C 100°C 200°C Hierro Latón amarillo (65% Cu.880 0.0 2.0 c) Alimentos Alimentos Brócoli Camarón Carne de pollo Carne de res Cerezas Espinaca Fresas Huevo entero Leche entera Lechuga Maíz dulce Contenido de agua.56 1.45 2. Refrigerating and Air-Conditioning Engineers.8 0.235 0.8 10.254 0.97 1.77 Calor latente de fusión.909 0.6 2.381 0.400 1.920 1.08 3.99 1.75 3.98 3.403 0.45 0.26 1. % (masa) 90 83 74 67 80 93 90 74 88 95 74 Punto de congelación.400 1. etc. r kg/m3 cp kJ/kg · K Sustancia No metales Acero dulce Aluminio 200 K 250 K 300 K 350 K 400 K 450 K 500 K Bronce (76% Cu.33 1.) Mármol Piedra Piedra caliza Vidrio para ventanas Vidrio pirex Yeso o tabla de yeso 0.840 2..310 19.009 0. Tabla 1.86 3.68 1. Calor específico. r kg/m3 Sustancia Calor específico.929 0.11 0. Handbook of Fundamentals.470 11.96 3.71 1.77 1. Atlanta.98 3.973 0.130 8.01 2.890 10.500 Arena Arcilla Asfalto Caucho (blando) Caucho (duro) Concreto Diamante Grafito Granito Hielo 200 K 220 K 240 K 260 K 273 K Ladrillo común Ladrillo refractario (500°C) Madera contrachapada (abeto Douglas) Maderas duras (maple.97 1.310 0.711 1.qxd 913 7/12/11 14:25:59 .859 0. °C 0.800 0.62 3.5 Calor específico.386 0.902 0.700 8.63 1. kJ/kg · K Por encima Por debajo del punto del punto de congede congelación lación 3.3 0.440 0.01 2.920 0. así como la temperatura promedio de congelación para otros alimentos. o se han calculado. cp kJ/kg · K Metales Densidad. El contenido de agua y los datos de punto de congelación para alimentos provienen del ASHRAE.6 — 0. 1993.840 1.94 1.797 0.32 3.65 2. Capítulo 30.393 0.net 18Appendix_01 ITALICAS.96 3.800 0.85 2.800 0. Georgia. excepto que se indique otra cosa) Densidad.65 1.8 — 1.653 0. sólidos y alimentos comunes (conclusión) b) Sólidos (los valores son para temperatura ambiente.017 921 1922 2300 1.2 0.280 7.960 545 721 513 2600 1500 1650 2700 2230 800 1.15 2. 93 792.4 2453.5559 8.001001 0. sfg sg 2500.2 2534. sat.90 143.68 0.38 169.1935 5.4053 2.81 2256.5567 8.1392 2.4956 5.1647 7.1847 4.59 503. sf Vapor Evap.879 25.5 2626.022 62. ufg Vapor sat.09 2320.4678 6.8296 7.9 2406.2 2276.9 1959.7067 6.60 2087.44 2441.001141 0.4 1910.2556 8.043 31.0 2295.1 2563.7540 75 80 85 90 95 38.4737 1.5 2402..3672 0. Tabla de temperaturas Volumen específico.0906 2.00 828.001121 0.03 335.4 2333.99 334.42 503.6670 6.7 2409.0 2511.0396 209.001114 0.1 2726.8725 1.001000 0.0 1875.1 Entalpía.28 461.8 2346.1346 1.3 2146.47 697.2 1398.4368 0.06 440.0 1939.2 1996.0 1763.33 230.597 47.53 415.1291 3.9082 7.19384 0.9360 6.1556 9.7 2777.1 2173.5 2269.6650 175 180 185 190 195 200 892.001102 0.27 482.5447 6.4 2219.01 5 10 15 20 25 30 35 40 45 Energía interna.46 1839.6812 7.7 2523.5059 6.982 83.0 2546.7492 6.6 2667.7 2549.7 2190. hfg Vapor sat.1292 125 130 135 140 145 232.26 251. T °C Pres.2218 7.9 1.39248 0.6 2048.4 2659.001023 12.03 106.73 146.3 2282.9 2422.5 2739.6 2706.5 1993.02 763.5355 6.4 525.7680 0.92 783.0 2475.7803 8.2705 4.001096 0.2965 9. ug 0.5435 7. Psat kPa 0.001070 0.5639 7.53 188.001134 0.3 2175.5816 1.001060 1.77 610.4 2582.8 2586.8466 7.9 2517.0 2394.50850 0.001020 0.001 21.9808 313.6 2308.7 2594.001008 0.001000 0.7 2449.7908 5.7 2429.02 356.18 653.001006 0.3 2506.9 2117.64 167.38 567.5 2555.001040 4.43 2304.2281 1.9319 5.9 2751.67 0.8 2357.5 2567.2 741.7 2429.352 15.0152 7.18 0.2 2465.8261 2.0 1.9 1944.2 2781.5051 0.0763 0.2504 6.3 3.43 829.24 251.04 398.6386 8.5 2500.4 2374..79 675.5953 0.08 2113.4 2243.001075 0.79 696.9 2247.23 270.1 2720.15 461.6 2573.9 2510.6111 7.4089 6.83 125.7392 1.8 2571.02 761.14089 0.001004 0.8418 1.1633 0.05 785. hg Líq.1 2698.1829 7.7 2216.42 482.7 632.8 2417.07 546. vf Vapor sat.24260 631. kJ/kg Líq.3517 8.83 125.15636 0.8 2792. sat.1 1783.416 57.7 2345.8999 8.4 2436.3305 4.8827 150 155 160 165 170 476..6832 7.914 TABLAS DE PROPIEDADES.00 2161.7057 2.1 2144.9294 6.91 806..947 25.001127 0.7 2579.001149 0.7143 4.2 1977.8 2767.6 2554.3 1960.020 42.2853 6..66 653.9 2462.1698 4.1 2608.001080 0.4 0.3572 4.0919 7.1 314.7 2014.001085 0.1 2675.4782 7.78 852.83 546.3392 0.9 2381.5 2762.4 2040.001056 0.340 32.4 1977.2245 0.8 2494.18 198.18 272.001065 0.0158 1.2952 7.001012 0.000 21.6 2634.5 2544.6872 1.6013 7.24 719.75 589.96 376.001108 0.9487 8.4186 1.0 2369..8193 5.0 2065.8 2098.9923 2.0417 4.4 2691.6 1743..3 2455.3696 9.6661 104.3634 1. hf Entropía.4 0.6291 7.19 2009.1875 2.6 2131.3919 5.9 2360.020 62.16 610.6655 6.34 230.2901 5.32 77.26 2031.17390 0.202 0. sat.3 2539.0756 1.3 2129.4 2785.0 2071.913 2374.9426 1.97 398.8 2056.9773 6.8 2442.19 674.001015 0. kJ/kg Líq.12721 740.001029 0.6 2564.5279 6.0997 6.8 2388.7 2395.60 1002.001091 0. m3/kg Temp.8 2745.762 0.980 83.9551 7.89133 419.0 2102.8924 1.5 2582.07 2382.58179 0.3851 9.27244 0.9 2733.3 2481.02 377.41 588.7927 6.001010 43.609 0.3072 1.21659 0.9 209.23 700.4302 http://librosysolucionarios.2831 2.6242 6. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-4 Agua saturada. sat.4 1820.42 120.3 2290.9953 4.16 272.001052 0.8313 0.46 718.0000 0.1 2477.20 1927.34648 0..3710 7.6 2683.2382 7.74 146.1511 0.2469 5.63 167.8 2772.9 0.0 2651.3 1893.0 2082.64 2188.9 1802.77012 0.5 2559.9898 7.019 42..0748 7.3 2600.0360 0.7 2159.885 57.0249 8.4 1857.251 104.9 2025.66808 0.4448 4.001003 0.97 355.0769 6.12 293.5841 6.17 440.515 15.4151 100 105 110 115 120 101.16 543.00 147.53 188.49 618.8 1123.868 70.6233 6.7488 8.001017 0.5247 8.0265 6.0470 5.0 2591.5 2318..44600 524.0 2589.001036 0.2094 1..8 1.qxd 914 7/12/11 14:25:59 .1 2229.8066 4.0771 7.9 2575.001002 206.5 1255.1901 5.6720 1. uf Evap.3542 7.22 361.9 2489.6 2487.28 313.5335 4.6117 0. vg Líq.4 2468.10 567.0 2591.001157 0. sat.915 50 55 60 65 70 12.001032 0.net 18Appendix_01 ITALICAS.8 2757.3 2528.3593 1.0 2500.205 19.7092 5.8371 6.6 2643.19 807.09 293.2 2528.0 2202.026 9.9 419.1895 8.001043 0.183 84.1929 1.9002 4..001047 0.4520 8.30680 0..001000 0.5724 0. sat.0 2261.8 1554.1 0.763 19.04 2233.6346 1.1556 8.0 2.8937 0.1 2519.6 1.4188 1.1 2204.3 2537.18 850.6 2332.001026 0.7989 8.1 2415.7038 0.2355 2.8 2617.2 2713.3 2788. kJ/kg · K Evap. 001289 0.9 2499.001366 0.7 2105.1 2602.2765 5.02 940.9 1283.7 526.023528 0.001263 0.0 1899.004953 0.7 2749. ug Líq.002217 0.6 2793.9 2603.0369 6.044 22.001472 0.7 1878.3 2084.4712 2.3 2801.0681 3.5 443.0 3651.9 0.9489 0. uf Evap.50 943. kJ/kg · K Vapor sat.7 706.4 1366.7066 2. Part 2A.8 2547.4 2727.001252 0.2 2084.7476 2.8 2576..9 2715.8579 5. kJ/kg Entalpía.1 1080.7 2766.001499 0.5 1817. Phys. Las propiedades del hielo están basadas en Hyland y Wexler. 22.2076 3.0 1661.027756 0.7 1671.001209 0.5176 2.001741 355 360 365 370 373.1 2015. Phys.007872 0..8 1159..8 1185. “Formulations for the Thermodynamic Properties of the Saturated Phases of H2O from 173.8944 1358.3563 6.5372 5.6 0 2388.012979 0.3 5085.5 2563.4 0. T °C Pres. hg Líq. ASHRAE Trans.001303 0.5 1061.6844 6.0017 5.8 1559.021659 1228. sat.7 1605.7 1416.556 11.76 230 235 240 245 250 2797.001447 0.0 1493.4511 5.6 1404.5 2443.4 1373.2 1415..6 1574.4 625.8723 6.1 1134.3 1110. A..8 255 260 265 270 275 4322.3 3.9 1264.035622 0.4 1238.011848 0.0 5946.1169 3.87 897.7 2590.5 2593. hf 1724.5374 2.79 963.001276 0.1821 2.2 2418.net 18Appendix_01 ITALICAS. sat. 1983.003106 1682.11508 0.001229 0. m3/kg Temp.6100 2.001808 0.9 1159.030153 0.0 8587.1 1344.009772 0.5639 4.4491 3.7 1521.038748 0.2 2801.050085 986.0 1033.7 0.001895 0. Las modificaciones están descritas por Wagner y Pruss (J. kJ/kg Líq..0 2802.019932 0.5216 3.1373 0.1 605.1 0 2526.5 1191.7 2758.3 874.2 1726.0 10. 16.0 1195.001199 0.0004 4.70 1723. la cual está también disponible en EES como la rutina STEAM.016849 0.6 3347.3633 2.7 2334.9 2773.4 1835.8906 1.3930 6.001240 0.7898 2.8 1153.001560 0. Alvarado.0 1332.4070 Evap.1072 6.5 1638.2128 6..001317 0.6028 3.094680 0.3358 5.001597 0.5 1570.0358 2.064 0.8009 4.1 1210.4326 5.3 1525.7857 1.4 385.071505 0.7 1689..9 2303..0 2.9165 4.8 837.8390 2.065300 0.9911 5.6 6914.0221 3.0 1761.7 1387.8 1543. sfg sg 1920.2 2.5585 1.1 1445.4 280 285 290 295 300 6416. La rutina utilizada en los cálculos es la altamente precisa Steam_IAPWS.3200 6.6 2351.3 1325.1384 5.4908 0.3 5503.570 18.1608 3.7 1537.2 1844.008806 1505.1424 6.8 2797.5816 5.1979 3.2 1569.822 21.0 2739.7933 3. Chem.9 2586.7 1812.601 15.002015 0.3 2802.001384 0.2840 6.4 1594.. Esta formulación reemplaza a la formulación de 1984 de Haar.059707 0. Paper 2793.4 2794.7179 3.8 7999.2 2483.001173 0.001164 0.014183 330 335 340 345 350 12. editada por The International Association for the Properties of Water and Steam (IAPWS).8 1857.1 2563.6560 2.6 2596.7 305 310 315 320 325 9209.9 720.1144 3.3024 3.054656 0.2 2.3 1086. sat.9 2601.1 1475.2 1328.4 993.9762 3.9 1202.6756 1. 893.4 892.9318 3.6225 2.001190 0. 1984).qxd 915 7/12/11 14:26:00 .001181 0.7 1263.0 1431.7 1037.1119 4.8210 5.10429 0.4 9865.7 1128.38 918.8442 3. sf Vapor Evap.7 1604. ufg Vapor sat. vf Vapor sat. Data. Psat kPa 205 210 215 220 225 Energía interna.3 812.010783 0.707 14.2 3976.018333 0.5 2799..001425 0.6 3.9 4692.1 2537.0 1387.4 2598.5 2555.9 1495.045941 0.14 1013.001219 0.9 1038.7834 5.0154 3.2 0.7 2785.015470 0.5 2598. L.6657 5.0881 1.9 1441.95 17.7 1616.6 2549.5 2789.6 1462. sat. Chem.541 16.7 1279.2 2603. sat.2 2526.5 1702.7 2596.0 2464.2 1891.001685 0.6 2684. Gallagher y Kell (NBS/NRC Steam Tables.7 1306.9 1080.2114 0. Tabla de temperaturas (conclusión) Volumen específico.15 K”.9 2803.2548 2.2 1777.8 1469.5 1085.7664 3.8 1317.9 3.8 1715.001333 0.5 1740.0721 2600.7 2601.1 1593. Data.0537 4.1 3062.3 2599.4405 3.0 2700.915 APÉNDICE 1 TABLA A-4 Agua saturada.2 1510.3994 3.7059 1360.15 K a 473.2 2803.86 895.1 1289.7 1476.4422 5.8 1545.76 1010.3776 2.032767 1104.2 1253.7450 5.2942 1.5 893.1 1402.5 1642.9 1443.6890 0 5.5 1765.5 2015.7 2666.7018 2. 783. http://librosysolucionarios.5 1230.858 13. vg Líq.6 2422. Ref.2788 6..5 2570..61 920.6 1631.4 2622. 1987) con modificaciones para ajustarla a la Escala Internacional de Temperaturas de 1990. 1993).6 2230.9 1660.2 1140.8 1633.7 1714.0 2513.666 19. Klein y F.9305 5..4245 2.0 2802.3596 3. hfg Fuente: Las tablas A-4 a A-8 fueron generadas utilizando el programa para resolver ecuaciones de ingeniería (EES) desarrollado por S.8847 2.6 1236.025554 0.001528 0.1 1296.9493 4.3 1907.3 2602.6243 5.3506 3.6 7441.4070 1.9542 2.078405 872.2737 2.0 2645.5 945.9662 5.8 2779.3 3.9 2319.7 775. La nueva formulación se basa en las correlaciones de Saul y Wagner (J.3 2799.1 2602.2483 990.284 12.0 1027.8489 3.4 1056.4 2581.9 2481.6602 3.0 2595.8 1789.006009 0.086094 0. sat.1 2796.001349 0.9304 2.3 1121.4998 2.006950 0.9 1681.3907 5.001404 0. Ref. que incorpora la Formulación 1995 para las Propiedades Termodinámicas de la Sustancia Agua Ordinaria para Uso Científico y General. Hemisphere Publishing Co.5516 3.1775 6.003106 Entropía.042175 0.55 966.7788 1.529 0.001638 0.4 963.6050 3.051 0.3 1177. 8 2407.19 0.7886 6.001008 0.54 655.44 417.4558 7.0 2662.86 2213. ug Líq.7 2140.4 2222.36 417.8 2574.3543 8.04 120.6 2012.5 2550.97 105.6 1948.4850 1.1 2459.24 2065.75 0.6837 34.39 137.9918 4.001037 0.30 143.83 155.49133 0. Tsat °C Líq.6 2636.0 2583.47 535.1 2325.5 2.990 0.4 2470.95 444.2287 3.001064 0.4 2467.6717 1.1 561.1 1973.9073 7.0752 6.2132 1.6738 7.71873 0.97 111.3 2553.5968 5.75 168.6 2085.40 418.5 2392.0 697.2645 5.6314 8.40 1875.6421 8.001002 54.97 127.5 3.5 2158. m3/kg Pres.001067 0.001017 0.62 340.431 88.7227 8.2222 8.79 225.2 2448.1 1. sat.09 75. sfg Vapor sat.86 141.41 130.7675 7.4453 5.9 2539.7 2560.001026 0.2 2338.2 384.8 1991.0 7.6 2226.5 2720.90 151.1 1964.0261 1.4 2756.1 2282.96 32.06 64.3 2318.2172 1.41392 0.001111 0.1 2752.4 2675.001000 129.4762 0.8932 0.0 2096.2 2172.6430 6.50 21.0 121.27278 696.1 2372.23 0.001020 0.9 2543.001061 0.001104 0.3589 7.66 2163.96 289.06 444.9917 6.001057 0.233 14.001079 0.0071 20 25 30 40 50 60.001084 0.75 168.0476 5.2426 6.3200 5.001014 121.2 251.0 2443.5 10 15 28.5 2335.1059 0.2501 8.65732 486.4337 6.5 2529.5 1921.29260 622.0 2735.9308 1.8955 450 500 550 600 650 147.7 2716.2 0.5 2240.7274 1.0 2519.9 2553.5 2155.020 http://librosysolucionarios.0195 4.7322 700 750 164..2 2545.9 2548.39 137.8561 6.001070 1.5 2419.1645 5.0 5.3938 8.8205 1.001053 2.916 TABLAS DE PROPIEDADES. uf Evap.7 2608. hfg Vapor sat.0 2462.08 24.1 2738.7 2574.6 2506.6 1865.0 6.9402 6.98 0.65 639.8270 8..1 2201. kJ/kg Entalpía.2128 5.76 99.001048 0.5171 5.1 1.9 2403.9 2617.9171 6.0 2513.8970 1.35 0.001108 0.27 138.0 2181.3 2483.7593 6.001001 87.8 2569.4 623. sat.2034 5.96 69.001030 7.0 2068.7 2563.7153 6.7071 2056.001097 0.61 0.8 2762.1594 384.001003 45. sat.95 167.36 467.5 2743.2 1908.0912 7..7 2456.0 1.43 573.4734 8.6865 5.16 669.54 2357.001005 0.6 1.5765 4.1191 6.qxd 916 7/12/11 14:26:00 .8320 0.9603 4.3 2108.8207 6. Tabla de presiones Volumen específico.4 2304.9 2513.1 1886.001010 0.6642 6.433 88. ufg Vapor sat.6 2684.88578 0.11 572. hf Evap.5706 1. kJ/kg · K Líq.7 2.89 594.9749 8.0207 300 325 350 375 400 133.29 45.1 2261.0 2.8 2429.7765 5.5763 0.1716 7.4 2748.5 2345.6 2732.8 2142.0 2405.5931 75 100 101.32 604.3545 7.2 2087.303 54.3800 7.14 640.9 2693.185 19..3 2423.5 2451.31560 0.49 2204.74 191.58 340.8234 6. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-5 Agua saturada.97 2111.27 317.56199 0.6408 5.686 73.688 73.21 123.3028 1.670 10.97 13.37483 0.1 2557.94 2432.9441 1.0037 0.75 191.58 0.7 2001.4621 8.4 2147.8285 4.9933 3.35 548.1270 7.5019 7.46 158.001081 0. sf Evap.1 487.422 100.32 0.8 1.6 2191.3750 1.6 2190...8604 1.93 2293.73 604.24 317.242 0.9623 5.2841 7.6 1956. vg Energía interna.4 2306.19 584.8 2052.0 2257.1 2414. vf Vapor sat.0525 7.7526 1.0356 4.7 2532.71 520.08 2120.001043 0.38 684..8 2437.2522 8.9176 7.9 1.4996 7.7 2524.6 2571.001076 0.40 271.52422 0. sat.3069 1.81 53.6072 1.4224 0.9 2566.6691 7.6492 0.9370 6. sg 1.7549 8.001004 0. P kPa Temp.46242 561.0562 6.3 0.23 466.3 2392.8 2540.00 709.8 0.001088 0.2606 0.81 225.22 1982.0877 7.4 2724.9650 6.001001 66.4 2544.0510 7.791 28.2 2759.6481 6.08 548.7894 7.302 54.52 136.1 2560.424 100.2403 251..8302 7.6 2524..98 2484.5 2315.7005 1.4 2133. hg Líq.7699 6.9 2728.8 2398.3118 0.4 2178.87 40.84 583.42 271.2 2706.93 289.5302 1.6734 1.964 0.02 17.86 81.3302 8.7 2476.08 0.net 18Appendix_01 ITALICAS.1 2533..26 594.7 2024.5 2256.57 2037.71 535..83 161.325 125 150 91.97 0.3 2496.8 1897.34261 0.51 419.8690 8.25552 708.1488 8.2231 175 200 225 250 275 116.001043 0.1 2505..654 29.3741 1.37 1934. kJ/kg Entropía.9100 5.13 2278.9 2598.5 2624.8 2088.72 683.82 504.9 2384.8 2075.79329 0.0 2700.6941 1.61 99.8916 4.001093 0.01 504. sat.77 670.1 2245.001073 0.4 2765.0 2675.3 2711.1 2645.9 29.1956 0.2 2536.98 2355.60582 0.50 520.001101 0.09 655.001022 0. 78 796.5005 1.5520 6.74 762.1 2758.000 15.0256 4.0 391.001115 0.001770 0.2 585.1220 3.9 1776.4936 6.6 1151.0696 5.97 731.51 2047.0 1713.0 1667.000 14.6 2084.9 2579.0 1049.56 752.41 172.8 1450.7 2783.000 12. sf Evap.96 813.7 870.0941 2.35 177. sg 800 850 900 950 1000 170.7 2800.1 1846.59 285.057061 0.1 1205.4 161.6616 6.12 0.012781 0.5 2596.088717 933.4 2172.87 2603. sat.6 1379.005862 0.6 2.6927 6.13171 779.0 2339.8 1841.2 1598.2 2784.9 1384.5029 2.0705 2.21489 0.68 0.00 741.3 1643.8148 8000 9000 10.000 330.7 1407.001187 0.8 0 2375.83 0..003644 0.4964 2.5373 2.4 2576.6232 3.001121 0.59 829.96 191.6 2581.000 22.2558 6.6159 5.6 1693.2 1491.2508 2.7926 3.001526 0.4939 13.007504 0.3709 5.1287 6.7 3.5 2706.6 1720.001352 0.001286 0.9396 4.66 179.8627 2.0 1000.6 1660.4336 5.5 0 2510.0860 0.4 2015.3 3.014264 1306.6791 5.8082 1.5 2587.9 598.12 0.6409 6.3877 6. sat.7 1732.000 22.4299 3.16 347. hf Evap.009312 0.2942 4.5217 6.1791 18.3 2770.5 931.0 2603.001488 0.8 2593.4 781.1 857.9 1946.2496 0 5.000 16.5273 4.14078 0.1381 4.0457 2.1 1794.1071 4. ug Líq.3 2685.6454 4.75 369.001566 0.6 1888.1840 4.5544 5.0275 3.8 2030.5 1639.010341 0.9 2725.21 2602.2731 3.9 2795.3058 4.4 1585.9 2791.4 3.0 1610.001118 0.064 356.079952 958.8 2581.15119 0.95 233.10 828.85 0.006677 0.7497 1.0 2775.7966 2.3 1441.8 2589.008374 1511.000 17.8 1096.002038 0.47 365.6 2768.023525 0.002703 0..36 352.3 809.8902 5.6261 1.01 303.049779 0.3 1448.4470 6.0033 3.3143 4.7 1570.3 2570.4 2662.001840 0.3 2582.4070 1.1 2455.3108 5.7 1087.1 961.29 0.015988 0.000 21.1 1323.0 2601.1245 1.020489 0. kJ/kg Líq.9 2803.5 1622..000 20.000 11.9 2610.net 18Appendix_01 ITALICAS. sat.8 1763.5 1753. kJ/kg · K Vapor sat.29 0.4 2780.67 761.8 2233.0530 2.001133 0.0 1548..027378 1045.099587 906.001235 0.4 2014.3390 6.7005 0.85 336.8 2786.5439 4.001177 0.3 2800.8 2773.2159 2. hg Líq..1 2084.2466 5.2428 4.5 2092.6027 6.0 2466.71 373.4 1082.9207 3.000 295. Tsat °C Líq.00 318.2835 2.4467 2.4 2514.001384 0.001319 0.6 2772.39 1856.2866 3.04 198.88 0.6848 3. uf Evap.001217 0.6213 6.60 195.5 2038.0 2.2 2294.87 0.5850 1100 1200 1300 1400 1500 184..0 2577. Tabla de presiones (conclusión) Volumen específico.7 2432.4 1750.4 745.7016 3.004994 0.41 223..9737 5.8 720. m3/kg Pres.001610 0.2 2777.67 342.001252 0.1166 2.001149 0.9 1838.1244 6.003106 0.4430 1750 2000 2250 2500 3000 205.8076 4.9 509.1 1740.5 2788.qxd 917 7/12/11 14:26:00 .003106 1699.4 1531.5542 2. vf Vapor sat.08 324.0146 4.8923 3.001926 0.8730 1.5 1207.0 1264.8 689.96 844.3 1317.7 2015.3991 3.87 731.7253 2.001154 0.56 250.2 2798.000 19.001138 0.5 2801. sat.5 928.1 1363.002207 0.1 2496.9 1958.8720 3.0 2547.2077 3.9 936.1 908.8 1267.4 1971.35 842.7 675.9164 0.3728 5.8 1826.3925 2.94 175.3 1917.6 2477.55 1999.. vg Energía interna.2556 2.2954 6.19436 719.001452 0.03 798.3 1067.001418 0.7 2597.001710 0.5606 3.066667 1004.917 APÉNDICE 1 TABLA A-5 Agua saturada.0 2412..2 2802.16 2599.22690 0.9 1690.018028 0.4 1571.17745 0.5 1213.7 1790.5402 6.0 1350.1 1889.54 0.3 1433.9 140.16326 0.001166 0.6160 4.4675 6.2 2.0 2589.1 1194.9 2581.001144 0.2 1008.3 1649.20411 0.5 2558.3 1131.001197 0.6 1951.95 0.2 2530.6 1256.9 2591. P kPa Temp.1 1829.9310 4.5 2545.0 2011.3 777.0 1557.4070 http://librosysolucionarios.9 1393.4 1154.47 2600.82 1805.8 2794.3735 4.4 1148.7 878.72 212.11344 876.06 187.6 2585.001127 0.032449 0.011487 0.24035 0.83 373. sfg Vapor sat..2 1776.1064 5.8 1864.7450 5.94 275.1785 2.4862 4.5 450.3 1317. ufg Entalpía.35 311.6 1041.33 814.5705 4..35 263.9 1473.6 1519.1 2338.38 218.6 1821.3603 3.95 742.001657 0.7461 3.039448 0.001124 0.1856 3500 4000 5000 6000 7000 242.6 1985..3 1840.7 2742.9975 5.0 2405. hfg Vapor sat.2 985.3 1785.5 2022.8 1258.9 1505.99 361.2343 1. kJ/kg Entropía.55 751.1 2.3844 2. sat.7 2637. 3 2515.5153 3704.0 9.9 4687.918 TABLAS DE PROPIEDADES.net 18Appendix_01 ITALICAS.03155 1.95986 1.7100 3072.1 2564.8362 3705.3 4259.35442 0.2 8.2695 8.1338 8.47428 0.2345 7.98966 1.8280 11.3000 10.9 3132.35298 1.0 9.8692 8.3 3480.31623 1.2 2571.5 8.7 3856.1270 2769.89696 0.50 MPa (151.4 2808.57015 0.2364 9.61°C) 3.3271 3704.7 3129.70656 2.6 2748.51374 0.6893 8.3424 4160.42503 0.8755 6.05 MPa (81.41°C) 0.05603 1.7 3481.3 5412.69966 1.84980 0.1592 8.43442 0.6 6.063 35.0792 2865.97893 1.9003 8.79645 0.3589 P  0.2 7.81516 2553.373 67.8 3483.6 2675.7513 12.5132 8.143 58.9306 7.6 2962.2236 3487.8 2976.0 3479.5209 2511.4 4054.8429 P  0.0605 4397.5180 3069.3396 9.6071 9.2 7.1488 8.8431 5413.4 2780.6624 5150.49580 1.0 2687.989 72.7 3926.2 2443.88936 1.3420 9.8 5413.8659 9.6941 2505.826 24. 200 250 300 350 400 500 600 700 800 900 1000 1100 1200 1300 0.4062 2.90761 2576.8 5412.3 3700.7395 8.1 2752.5 4640.4598 4642.3 9.8345 4159.6 3168.2 2645.2 4642.18672 1.2 3855.8 5150.9 4055.136 26.0041 8.3 3132.3 3929.8897 4.66976 0.9274 9.3 3132.3 2883.61731 0.3 7.4900 4.4 2756.2 2801.527 54.1566 9.77265 0.90179 0.6626 9.9 6.4 2721.5735 7.1933 8.0 4259.7 7.4 4157.6 4398.5 4687.8998 10.5 u kJ/kg h kJ/kg s kJ/kg  K P  0. 150 200 250 300 400 500 600 700 800 900 1000 1100 1200 1300 0.6 7.8 4470.6312 10.9519 5.3 3706.93755 3.8 7.4187 3.13309 1.1 3925.9800 4893.9 3162.3 2723.6 4641.0 3130.45214 2529.4726 4893.7 8.0 1.39390 0.00558 1.56011 0.9 3303.6 10.5 3076.2 2582.58414 1.80417 1.0 2728.8185 9.5977 14.6616 6.6 3303.8 4055.8 3665.4 4470.50186 0.60582 0.2 3267.44332 0.2 3075.71095 0.4 3856.46859 1.9 2964.4056 10.qxd 918 7/12/11 14:26:00 .8 4686.38429 0.4897 10.4 8.196 19.39938 3.1 3663.67619 0.2810 2870.65489 0.4137 5.52261 0.30 MPa (133.29321 0.1741 8.8 3478.5 3128.4 2736.08227 1.3 2969.17480 1.0 3856.35972 1.5 2878.1 10.35212 0.4 2583.0 10.5229 9.37483 0.9367 2.7 4892.3 9. † Propiedades del vapor saturado a la presión especificada.4 3701.9518 9.0 2651.5 8.5452 3488.9 4641.7797 u kJ/kg v m3/kg h kJ/kg s kJ/kg  K P  0.31560 0.9047 10.5 2783.5655 4.3562 4.8356 2974.5677 7.9049 9.0157 P  0.6 2960.1724 2.5295 9.0577 8.61°C) 0.8 2860.73411 0.7 3477.2 4259.2 2726.1631 10.0 4158.6 2968.1 2855.2 3131.7 3280.79197 0.1723 7.1 2706.2 4641.0893 8.5 3927.83°C) 0.6094 9.1354 8.2605 2675.8 4893.9 2661.16848 3.8 8.6 2731.08049 1.2841 6.7 9.1 2715.3544 8.1 4053.9 4396.8 3480.6 5149.3 2839.0999 3929.7 2643.6061 8.9 3855.7 3706.5931 3.82457 0.0 3489.5978 8.1698 5150.7 4160.9 7.7 4054.8 3279.8 9.6599 4893.3 4157.4201 9.8 2639.1000 10.2029 P  0.513 21.83°C) 2560.21°C) Sat.2 9.5 3854.4132 11.6 3665.3 2682.9 2724.0610 7.2 2877.59520 0.6 8.8 2950.2172 3278.6 7.2403 0.0 4395.2 3126.4 4396.0 4470.5229 2506.680 40.2 2733.1521 9.1 3273.8 4258.2 4470.9683 7.6148 2875.2 6.7 4687.0 4686.0 4470.6 5412.9 4160.4 2805.0 3300.4 4398.5915 3928.5 4053.0279 4.4 4686.0347 3486.8883 10.8 2961.6955 1.47088 0.6 2957.4 5149. http://librosysolucionarios.4580 8.5625 *La temperatura entre paréntesis es la temperatura de saturación a la presión especificada.2 4686.0221 4159.7 2660.911 49.5 4891.3 3489.80 MPa (170.6 3663.9 7.7 4055.3740 7.46242 0.4263 9.2479 4397.3 4258.6 8.59200 0.9 2807.9 3664.53434 0.2 7.81°C)* Sat.3 4686.6 2977.7793 3928.8 9.2 3302.5481 7.4 9.3 4642.0 2966.34139 1.3804 7.2 9.8207 7.4107 7.0 2735.1 4892.3 4054.5 3664.8240 9.5 3703.1 3270.26728 1.5 2585.7037 3275.0 8.7988 7.3794 8.1833 7.0 4259.2827 9.446 31.1 2964.0 3064.5387 8.10 MPa (99.9 3485.3 9.88578 0.0 2879.1 2812.6 9.42019 v m3/kg 6.5 2587.47550 2.3 7.0346 3074.4 2881.758 63.8828 P  0.8 6.9 2658.1 7.0 3663.5 8.1 3272.6 3479.2326 11.87535 1.8497 5150.63026 Sat.4 3056.54934 1.26624 2.01302 2.0402 7.7 2968.6704 10.9 2797.604 2437.4 2647.60 MPa (158.6 3855.0 3929.7 5150.9813 9.0189 9.1015 9.8 2967.7956 8.296 44.6 4158.74725 0.23730 1.0 2963.5 3067.0 2631.5 7.8955 6.1027 3. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-6 Vapor de agua sobrecalentado T °C u kJ/kg v m3/kg h kJ/kg s kJ/kg  K P  0.3568 8.5 3702.24035 0.9 2810.2725 4642.9 5149.3 10.47443 0.40 MPa (143.6 9.7800 4642.1 2577.3 9.19890 1.1 2768.3 4260.5081 2971.2090 9.6346 7.6 3062.0429 11.4614 7.71643 0.6 3301.7 5413.1 9.0 3166.0 4054.4 3665.0 8.9 4470.12152 1.3 4469.61820 0.0362 9.65004 1.7102 9.7 4893.9 5150.2 3299.21012 2566.32416 0.1394 9.8 4259.6959 1.5 4259.8941 3277.6953 7.3372 6.9 4396.8 2803.† 50 100 150 200 250 300 400 500 600 700 800 900 1000 1100 1200 1300 14.2094 7.01 MPa (45.2 3856.9 3129.8177 7.8 4469.1 3480.1 2654.6 10.2725 7.7593 6.8 4687.5682 4398.3898 9.7012 8.7 2738.9413 8.6 4470.0304 5413.8 3301.7 8.63402 0.9 2592.6745 13.6 3298.8206 5.4489 8.8429 11.4 4892.26088 0.3132 2967.2 3662.3611 2776.1 2811.5857 P  0.6389 3.4 10.3 3927.32°C) 2483.80409 0.78142 2.4 3302.2 3479.9917 2761.24434 2.0 5412.20 MPa (120.7097 8.4 3484.11226 2.3 3856.4 3478.52°C) 2543.2 2850.95824 2.867 17.3504 5413.1 7.670 14.2 7. 1 3474.85 C) u kJ/kg v m3/kg h kJ/kg s kJ/kg  K P  1.9235 7.1872 P  3.9 4052.5 4885.5 3469.27941 0.2 2803.7 3029.29048 2594.4 2863.0 5148.5 2783.5 3476.11678 0.3 4683.33989 0.8878 9. 200 250 300 350 400 500 600 700 800 900 1000 1100 1200 1300 0.5 3292.3254 3686.9502 0.2 3682.7 4257.1384 P  3.9265 7.1856 0.1 2935.5475 2773.31951 0.0 3853.3 2637.3 3652.22658 0.4 2801.96 C) 0.0311 8.8428 7.7 2955.32606 0.12551 0.8618 5409.1 3338.00 MPa (212.8 2777.1308 9.3046 7.8 2816.9 3693.7488 6.7590 7.29342 0.07995 0.19549 0.09919 0.8 3912.17988 0.8 3288.4670 7.1 3121.7 7.9 2847.2 3112.0349 u kJ/kg h kJ/kg s kJ/kg  K P  1.0 6.40 MPa (195.35188 0.07680 0.5850 6.3 2943.12502 0.1183 8.4200 6.5 5411.3 4052.3 6.4 4152.0170 3351.3 3656.3 4682.1 8.8246 7.9 3457.1814 7.5217 6.net 18Appendix_01 ITALICAS.8331 9.0 2927.7043 3471.5 4634.7595 8.9 3040.7642 8.1791 3850.1057 9.1 8.00 MPa (179.8 2645.17459 0.11620 0.54083 0.9 2927.9 5147.7684 2860.1 6.6 3293.1 3698.27012 0.67983 0.7 4257.5955 8.7 2953.17568 0.0 3922.3 3847.5 4153.0 4468.4 3852.13293 0.16326 0. 225 250 300 350 400 500 600 700 800 900 1000 1100 1200 1300 0.6601 6.7 2869.0212 9.16849 0.95 C) 2602.9 4637.0 4254.7 3853.7 2872.3324 8.4045 8.7 4154.1 5411.7 4256.9 3120.2 4467.30865 0.4897 4887.4 4891.37 C) Sat.2 4394.6427 8.45059 0.2 6.1 2788.1904 8.7543 8.3 2903.0 4151.6 3924.4 2866.2139 7.5587 8.4 4632.2558 2805.5 4144.11 C) 0.3 8.8 3295.9 4391.7 4684.2028 8.4 7.0074 7.9 3141.3 4685.8101 8.919 APÉNDICE 1 TABLA A-6 Vapor de agua sobrecalentado (continuación) T °C u kJ/kg v m3/kg h kJ/kg s v kJ/kg  K m3/kg P  1.04 C) 0.2 4886.1 2857.1768 3462.7 5145.19551 0.20750 2624.30661 0.4 5148.6 3285.45247 0.5 2836.4 2836.6 2948.11325 0.9 3125.4965 8.4 2933.1 2798.9 4469.7 4051.7 3282.1 3474.1 4156.14190 0.3750 P  1.2 3016.63354 0.0120 7.4 4385.17835 0.0 2950.36687 0.8313 7.15410 0.6804 5146.11037 0.8 2978.8 2692.7 4252.05876 0.38614 0.1379 7.5 3123.0 3297.40111 0.7450 6.2 6.5909 6.35288 0.7771 8.9 6.5 6.4484 6.6 8.14025 0.4845 7.6 4890.1304 8.4176 8.0713 7.7 2777.4 3692.25330 0.8 2612.7842 4467.8 7.39589 0.80 MPa (207.3 6.9155 9.40341 2597.24674 0.72610 2582.5412 6.5 4050.6 3658.1 3231.3 3477.1244 0.7 4685.2394 7.06667 2603.16751 0.23455 0.08118 0.20 MPa (187.18087 0.21105 0.7 4889.20602 0.38 C) 0.5979 3915.8 2792.3 3118.1764 6.1 2828.21597 0.4593 P  1.51866 2591.5 3659.5537 6.36308 2599.0 6.2755 8.1 3258.33395 0.1 4394.8 2602.3 4638.5 2994.1292 3116.19007 0.50 MPa (223.3 3661.6 4464.4 4391.6 7.29464 0.6 4889.14303 0.19722 0.6 6.9553 7.18233 0.0 3654.7 4253.7 2738.2866 9.2359 7.2893 6.05706 2603.4 3296.5 4468.20029 0.9497 9.06845 0.12702 0.5 2939.9509 3658.8 4640.8 3695.08456 0.37297 0.23466 0.9 2803.0 2802.5 5148.0 3697.9 3473.13999 0.5 3451.5 3690.21386 0.9 2781.24207 2644.3458 8.9 8.23275 0.7 3472.3 2762.6855 7.9654 4684.15122 0.3 6.6 6.2418 P  2.1 3051.7 2957.6459 3127.19420 0.6 3846.4675 6.8 3851.0744 4389.0005 8.41933 0.50 MPa (242.2629 2880.6753 6.9 5411.7 4046.6 3158.6047 7.12012 0.6 3046.08026 0.2 3261.7 6.2 4256.1 5408.19962 0.5 9.19437 0.7 4466.3 3475.37766 0.24822 0.2 3108.5 3137.48928 0.7 3918.9 4387.6088 6.3 4393.6 3470.2 7.2 3223.2 4638.14078 0.09198 0.2022 9.3 5410.3 3116.0335 7.5 2795.16356 0.9 3248.6 5147.4 3660.1 7.8 2844.3 3154.6 3146.28597 0.7 2789.8 6.1 3104.8864 7.0 4467.4337 3291.8 2622.2 7.2 3264.6303 8.0 3104.9 6.6779 7.qxd 919 7/12/11 14:26:00 .31667 0.44783 0.0 8.2 5410.1 4392.2882 4635.5024 8.09959 0.3925 4050.0 4639.10979 0.4 2793.21782 0.6 4465.3029 7.5 3467.9 4047.60 MPa (201.13245 0.25216 0.0 4891.10381 0.6956 6.1246 7.8 3026.3793 7.8455 4149.0558 8.13015 0.3 3919.2 4146.24999 0.22029 0.8 7.2 5147.13860 0.9 2704.9456 8.3 9.09938 0.33780 0.5236 8.8786 http://librosysolucionarios.27426 0.9 3251.7150 8.7 2875.14061 0.5936 4255.9 3464.3390 2628.5410 7.88 C) Sat.7053 8.58721 0.9885 8.8310 9.4417 8.8 5410.6 4051.0689 9.9156 8.5 3479.2 8.0 2829.4160 2680.10789 0.30020 0.25799 0.5 8.5 3920.2 2852.5 3921.09894 0.5103 7.4357 7.15460 0.12374 0.4975 6.0 8.1 8.0143 9.5 3678.56652 0.2284 8.8 3254.4107 3009.27190 0.9 3468.9 2785.14841 0.8 5408.0 4685.0856 7.6 2856.2 4257.8 2663.9583 2945.1593 7.7 2698.3 7.19241 0.42488 0.6 6.07063 0.6 3021.56 C) 0.1 4681.2 4637.9 4155.8424 3240.6 4684.7 6.22200 0.7 3344.22326 0.9 6.6 3035.15931 0.8 4890.35411 0.15866 0.08705 0.2 3849.0 2686.6974 8.9 3150.4 4049.25482 0.2 3024.09056 0.16934 0.9 6.2 2911.1 3472.3 2710.4825 6.9 2919.2834 8.52792 0.3 3852.3775 6.45383 Sat.3 3661.48558 0.11150 0.60509 2587.7 3909.3036 P  2.28250 0.49438 0.7 2750.00 MPa (233. 225 250 300 350 400 450 500 600 700 800 900 1000 1100 1200 1300 0.16420 0.1 2604.8730 8.41184 0.4 5144. 4 3512.7 4037.16992 0.023525 0.6 4102.11715 0.8 4045.9 2668.44 C) 0.7962 8.0 4613.5 5401.048157 0. 325 350 400 450 500 550 600 650 700 800 900 1000 1100 1200 1300 0.0380 6.0 3338.2 2827.054342 0.038378 0.016138 0.5 2907.035655 0.079025 0.7 5398.3 2699.6 2885.6 2725.3 4461.3 4383.054829 0.7 5.8 3632.3 4619.032491 0.9386 7.6 4875.2 3267.0 3201.9220 8.1 4119.4 2920.0954 7.5 3205.9737 6.07076 0.023019 0.2 2956.5 4452.1 2957.8014 8.9 4023.8 3843.3 2748.6214 7.8 3324.6 3730.7124 P  8.4534 8.7 4872.5 3604.9 3900.8 3748.5843 6.3 5.59 C) Sat.2749 6.0 3248.3 3153.7616 P  7.0 5135.0 4457.6 2913.7071 6.7 4616.1 3225.8770 7.10769 0.08766 0.2 4123.1 4459.028033 0.3 5.0408 7.8000 6.038194 0.7 3023.036793 0.4247 7.062850 0.0 3625.6582 7.6 3635.0 3634.2 4628.090341 0.5 3835.022440 0.5185 7.01 C) 0.8 2887.0 3074.0221 7.04742 0.7714 6.8 4042.075492 0.7 4454.4 3882.5 2592.8 3894.5 4362.020030 0.0 3097.4 5137.1 2879.5 2770.0 3100.048463 0.1 3422.2 5406.029782 0.025816 0.3 4137.1 5141.8 4369.032811 0.029960 0.0 3643.1 3541.4 3531.3706 7.8210 6.3 4882.038724 0.0786 8.1429 6.7 3093.2 6.2305 6.6 4625.6 3040.8 3096.4 2713.0675 8.5 3343.039885 0.7 2786.9419 8.4371 u kJ/kg h kJ/kg s v kJ/kg  K m3/kg P  4.5153 6.5 4680.10543 0.5195 7.3 3399.04535 0.067082 0.058147 2826.3 3056.3 2924.2 3081.024279 0.04406 0.7 3832.2 3876.15824 0.9 2742.04733 0.0 3145.8 4677.0 3829.3 4133.920 TABLAS DE PROPIEDADES.2967 7.9 4676.0791 8.5 2810.1321 6.069856 0.11098 0.9 3159.1982 8.15103 0.0323 7.4638 0.3 3302.1 3870.13592 0.3 4043.4 5402.041767 0.080733 2558.2141 6.14527 2597.2 2839.05138 0.2 4365.0 3628.061011 0.046641 0.6 5.3 3279.2 3288.5 MPa (257.0 5394.4516 6.0 3448.03945 0.2312 6.2 3440.11326 0.7 3646.4085 7.4651 6.3 3457.0 4114.07870 0.8164 P  6.054132 0.7 4035.9045 7.045172 0.7458 7.03245 0.4 3160.5 4864.0308 7.83 C) 0.6 4680.7130 6.05842 0.9 3423.020489 0.025630 0.6 3091.7 2668.6 3888.6 4032.4 4240.4 3375.5 3047.3181 8.08004 0.9619 8.2822 7.1 4251.3874 u kJ/kg h kJ/kg s kJ/kg  K P  5.4502 6.4 3343.2854 6.7269 7.0 MPa (295.4 4463.0 5.05461 0.6273 P  9.5 2925.019877 0.3127 7.9 2800.084934 0.2 4672.5551 P  10.1693 7.7585 6.2876 6.9 2857.5 3521.7 3317.09850 0.4 2790.9 2789.9 4606.5 4233.083571 0.8164 6.13476 0.12292 0.5 6.9 3178.5 MPa (327.0 4622.6791 5.8 3642.6 2699.6 5399.097075 0.4060 8.qxd 920 7/12/11 14:26:01 .5388 8.06858 0.94 C) 0.6 4249.3658 6.058391 0.1 2624. 300 350 400 450 500 550 600 700 800 900 1000 1100 1200 1300 0.10916 0.0433 6.039958 0.2 4884.7450 5.013496 2505.1 4447.026436 0.6430 8.053547 0.4 3462.06647 0.064919 0.08644 0.05217 0.1 4376.4 2944.8 3065.0 3387.7219 6.5647 7.04978 0.08852 0.7266 6.4 3438.5 5127.05887 0.5579 6.0289 8.4 2893.06102 0.6317 6.0571 6.5432 6.9 3261.6 2833.7 3324.4219 6.9460 6.09756 0.018028 0.8855 8.0 4382.7 2651.0 MPa (303.8 4040.1350 8.3487 7.18157 h kJ/kg s v kJ/kg  K m3/kg P  4.0 3618.0 4242.8 4456.5 4245.4 3242.7937 6.9 2726.027378 0.1 3755. 275 300 350 400 450 500 600 700 800 900 1000 1100 1200 1300 0.2 3838.net 18Appendix_01 ITALICAS.2 3453.6 2914.3 3167.0 2864.051966 0.8148 5.4872 6.0118 8.2 5407.070224 0.4 3460.0910 7.7 2784.7 4667.048629 0.7 3443.034612 0.09816 0.06332 0.5 4373.7 3069.8800 7.2144 8.4 4671.1 3139.0 2809.9337 6.043597 0.0 2632.3 5131.8 4883.9 3841.2 3826.4 4879.8902 6.5 2979.050510 0.063183 0.0 2818.3 3118.6 3476.8349 8.2 2611.4612 8.09886 0.1 4674.5 5.7 3666.0 3648.08165 0.6603 6.4 3670.067938 0.023284 0.05197 0.7828 6.3357 6.2 3446.04225 0.9 3903.0540 7.7 2989.5 2647.6 2839.1 3502.08964 0.35 C) 2601.05784 0.034344 0.041018 0.090817 2570.1 4629.5 2758.06527 0.4606 7.044187 0.073079 0.8523 8.1 2944.1065 8.0198 6.16140 2599.059562 0.6290 7.6 4679.8 3818.0 3276.2 3854.5 3000.042861 0.5136 7.9 3016.14064 0.8 3011.4 3650.9 3083.3 3639.3 5405.6 3043.0 MPa (311.0922 7.0 MPa (275.04144 0.4 5143.8738 6.6 3844.05667 0.6 2967.6 3650.07343 0.3 4128.07652 0.0 5.2698 8.8826 7.5995 6.7 5133.7 4380.1 4247.4 4462.9507 7.1 5.0 3674.7372 7.6353 6.11972 0.042720 0.2126 8.3 2794.072667 2545.4925 P  12.5 4029.0696 6.8 3258.2 3126.1648 8.8 4870.4 3273.033524 0.7 5139.1693 7.8 3273.029492 0.06477 0.12107 2589.3 2961.3 3196.12655 0.2 3434.2 3005.2819 http://librosysolucionarios.5 4877.045755 0.13020 0.7596 5.8 4352.5 2988.3 4142.5 3254.03619 0.3 3658.9781 7.0 MPa (285.2625 8.07355 0.4 5404.030306 0.81 C) 0.2111 6.6 2674.029975 0. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-6 Vapor de agua sobrecalentado (continuación) T °C v m3/kg u kJ/kg Sat.0 MPa (250.9 4250.3810 8.103781 2581.0 3434.1 2772.0 2633.0 MPa (263.076750 0.6802 7.0055 8.3 3214.055665 0.5 3242.9227 7.9605 7.035262 0.0 2849.6159 5.9 4238.3 2725.5880 8.14653 0.1 3175.3639 6.0703 6.00 C) 0.8751 8.3 4140.3 3411.9 4631.048589 0.3566 8.2709 8.5836 7.2229 7.2 5142.1 2798.9 3906.35 C) Sat.2605 7.3 2864.5 3331.6483 6. 0 5360.005299 0.8 2821.2 5367.3 2610.7 3241.0403 6.5 2947.5243 6.8 2412.3 4801.0 3399.014904 0.021073 0.8819 6.4422 5.6 3679.024342 0.3 5040.1 3795.2 2902.2 2664.017473 0.7 3157.041556 0.5 3295.033215 0.9 3339.2 3972.7 P  35.002487 0.3821 7.8 3823.009073 0.2 3764.006737 0.0 3251.5616 7.6 1787.6034 7.0695 7.8233 6.003955 0.2 4378.018477 0.7841 P  60.0 4043.7149 3.0029 4.2 1762.001792 0.017385 0.1 3026.3 3693.8 1699.7819 7.0 3927.0 2974.9449 8.8 3279.2 3702.012721 0.9 4020.9449 5.019695 0.009176 0.9 2452.014360 0.3 3310.001911 0.4 2578.006933 0.7 4396.0 MPa 375 400 425 450 500 550 600 650 700 800 900 1000 1100 1200 1300 u kJ/kg 1702.6 1874.9099 7.9043 6.4623 6.3 2925.7 2284.7956 6.012213 1609.8 4307.5 2607.1 3409.0 4130.6 3228.8724 4.6 3996.6 4607.011441 0.0814 6.010341 0.1400 5.015204 0.9 2253.6 2880.7 3334.0 MPa (365.4033 6.8735 7.0 MPa 4.8 3397.002009 0.2 2570.3 3064.1952 0.4 4406.9107 7.5 3154.9 3902.013278 0.9 3310.001633 0.8 3609.8 3159.4758 5.3425 7.4906 7.1 2769.9 3308.5563 5.7 3776.3 3020.015686 0.2424 6.6 2866.3511 7.5357 7.0 MPa 3.7 1745.6933 7.001816 0.0192 8.3517 5.6 5122.8339 8.9 2740.1 2068.005623 0.921 APÉNDICE 1 TABLA A-6 Vapor de agua sobrecalentado (conclusión) T °C v m3/kg u kJ/kg Sat.022742 0.6 5386.016976 0.0 3675.0 4288.009930 0.002086 0.001701 0.7 3446.1435 P  25.023150 0.3390 6.3 3811.006957 0.5075 6.1145 4.013590 0.4118 7.003692 0.8 3140.2179 6.7 4004.1 4472.015430 0.005591 0.2078 6.0373 6.2829 7.7 4443.2 2001.2 2887.3030 6.9 4623.7 2529.7 3472.4 3743.4 3221.1946 5.6796 6.008348 0.5111 http://librosysolucionarios.1355 7.2 3493.9 4360.5 3.8 4555.8 1960.3 2497.015628 0.8 4184.7642 4.0 3560.6 1931.1 3095.016450 0.2 4858.8 2906.001731 0.010439 0. 350 400 450 500 550 600 650 700 800 900 1000 1100 1200 1300 0.4 3106.8 5324.4 2199.3 4270.8 5117.5 5.6 3190.9 3156.9 2055.011481 0.2 4757.4438 5.6331 5.5 3637.5 2364.7 4222.3 2845.7366 6.7857 6.6 4195.4 3521.9310 0.009053 0.6613 6.2 3.012590 0.9853 7.1 4227.0 3965.8 s v kJ/kg  K m3/kg P  17.4 3252.6048 0.8 4655.67 C) u kJ/kg 4.045279 0.1434 6.6 3978.4 2972.6 3749.9 2807.4074 6.6702 6.7211 6.020827 P  50.1 3712.004833 0.4 4152.026484 0.018185 0.7 3423.7751 5.9 2618.1 5338.9 3570.5 4659.8 3065.7 3780.8802 8.9 5382.001560 0.2 3991.1 4424.007886 0.8 2180.5 4325.8 2721.8 2693.6 4252.0 3511.6378 7.014793 0.1255 7.2 3396.7 4847.042062 0.002798 0.2 2681.019240 0.008519 0.2069 7.qxd 921 7/12/11 14:26:01 .1 4091.002952 0.1237 7.4 3276.006108 0.018922 0.015671 0.9093 6.026804 0.0 2511.010565 0.035503 0.1816 6.8 2611.048469 h kJ/kg s v kJ/kg  K m3/kg P  15.9 1843.75 C) P  30.038808 0.024279 1738.023870 0.8 4499.3 2945.8 4823.5 4527.036371 5.9 5094.024921 0.3 3807.1 P  40.7710 7.6 2875.0 4182.0 3084.0 MPa 3.9 4173.012534 0.006005 0.5 3103.5 MPa (354.6 3925.8301 7.5 1716.6759 5.5 2671.027157 0.1 3839.2 1791.3 4216.019398 0.1 4570.005862 2294.3248 7.8 4216.8245 6.5 2755.9643 6.7175 s kJ/kg  K P  20.6 3443.0574 2684.4288 7.4266 6.4 1988.003434 0.014140 0.5 3614.011521 0.4708 5.0 2950.008089 0.5 4591.007932 2390.4140 4.9573 7.5896 5.7 3711.4 3583.9 3359.001503 0.8 4067.4 3432.021134 0.6 3670.2037 7.031504 0.7 4599.2880 7.9 5058.022630 0.7991 7.016643 0.2 1892.2 3539.017942 0.4 4584.7 2520.8 1914.6 3165.8 3599.3 3175.028621 0.1473 5.5044 4.4 5103.008691 0.8 3733.5825 7.5 4010.3 2160.019305 0.5599 6.6 0.0212 6.9 2152.009504 0.001978 0.8 3551.0 2997.1 4663.4 4778.3 3952.6 3025.1215 0.009950 0.1 4631.9 3218.3 3281.8 3450.4 3111.9317 4.030348 0.1630 4.020828 0.033952 0.net 18Appendix_01 ITALICAS.013654 0.2 2816.6 4647.6 4592.9313 4.5 4812.016571 0.5 3282.011445 0.8 3192.9322 7.014620 1638.2 3209.010175 0.8 3031.005118 0.0 4852.0531 7.5 5375.002105 0.027405 0.9 5352.009523 0.1 2975.1762 5.4 3085.5890 6.3 5390.2373 6.7588 7.003890 0.0 MPa (342.8290 4.2244 7.007717 0.0345 5.6807 7.3 5.3 4334.6 2373.9 3061.8602 0.6725 6.0 MPa 375 400 425 450 500 550 600 650 700 800 900 1000 1100 1200 1300 h kJ/kg 0.025172 0.006985 0.5225 6.2 4415.002538 0.6 4541.029020 0.9 2428.1 3590.006265 0.007456 0.011523 0.5230 6.0131 7.4207 7.7 2805.8 2998.021075 0.2144 4.9 4433.1446 6.1668 7.3108 5.4 2060.16 C) 2455.010296 0.012736 0.1229 6.4744 5.8 3366.018239 1677.3 2528.1 2393.1 5075.6593 6.011339 0.0 1855.4 5085.4950 7.011143 0.029115 1799.3 1742.012980 0.3480 6.5526 5.5 4079.004957 0.5 2617.4 3385.1 0.5 4206.8867 6.001641 0.9494 h kJ/kg 0.3 4639.2 1849.2 4017.3 3880.036029 0.012463 0.0 MPa 3.3 4438.7 3175.7 2722.7409 6.9356 5.3 3531.020954 0.3740 6.022945 0.032121 0.0 2097.6527 5.3 3551.6 3561.7 3803.3 2901.5 3599.038806 0.1 4343.9 2824.4 3350.2746 4.0170 6.5 5.0 5112.3637 6.2 4835. 1 1675.0013322 0.6 1431.0010267 333.06 2.5646 0.29 82.5 1134.0011809 0.7344 1.1020 2.0009973 0.19 2.0010522 0.82 1038.93 1042.7098 1.0010886 0.94 1.7194 1.5148 1.0009962 0.3251 2.6156 1138.55 342.0009951 0.86 441.01 1026.4 1407.6 1307.0723 1.0010914 0.0009886 0.85 498.9 1433.43 1039.0010337 0.0016311 P  30 MPa 0.0010042 0.1 1154.4707 2.0011240 759.3 1454.2 1121.0009929 0.04 5.49 925.6983 2.74 346.0010445 0.net 18Appendix_01 ITALICAS.2 1167.0014932 0.0018248 1785.5236 1.3558 3.04 0.3 3.12 83.00 608.0012472 0.61 0.08 324.0012053 0.0020378 0.77 193.6676 2.71 665.90 276.05 773.01 165.3 1452.4 2.3996 3.45 904. 0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 0.8787 1393.17 517.75 C) Sat.6301 1746.0 3.0009992 0.6 1354.93 161.37 259.0011049 0.39 514.1 49.2705 539.4 3.16 1040.1 1213.9547 1324.2888 2.8 0.81 1021.00 947.78 837.0691 1.0010708 0.11 918.9 1391.1 3.9 u kJ/kg 0.86 111.0010 129.4867 2.1 1109.3 1134.0010769 586.0011697 0.6774 2.2091 3.07 93.57 185.7 1259.55 678.47 765.31 166.922 TABLAS DE PROPIEDADES.0790 875.28 176.50 582.2 1134.4 1317.11 164.0010201 0.40 410.2920 1.5 1288.0012755 1128.0012192 0.0014014 0.0005 0.3027 2.32 934.0015693 0.2628 961.0010576 501.74 745.8 1328.7 0.9 10.0410 3.5 0.9207 0.0009928 0.6555 P  50 MPa 0.4414 1049.5127 2.0009872 0.6 1740.95 0.6 20.00 C) 2.28 750.69 569.1218 1421.0011531 847.0010155 0.0010127 0.6 1540.02 952.0014848 0.8710 3.0011200 0.75 330.0010385 0.5705 0. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-7 Agua líquida comprimida T °C u kJ/kg v m3/kg h kJ/kg s v kJ/kg  K m3/kg P  5 MPa (263.09 0.0011927 0.5666 0.0012560 0.8841 0.0012430 0.68 855.2279 3.25 0.2897 0.4263 3.0010517 0.0009996 83.01 770.7864 1229.39 944. 0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 h kJ/kg 4.84 602.8250 3.0442 456.9316 2.0009805 0.92 171.03 102.0013783 0.43 332.8 1329.26 358.76 693.3603 0.7 3.90 243.6 1838.5438 3.2 s kJ/kg  K P  15 MPa (342.0004 0.0003 0.58 331.0010035 0.17 247.58 840.0010349 0.0009951 0.55 1078.0011160 0.7 1229.6848 0.0010679 0.21 778.49 819.8156 1.80 592.61 88.0016276 0.0012653 0.9 1567.2958 1.0627 1.6491 2.5528 292.88 0.36 1.7243 1.77 652.16 C) 0.69 667.63 753.2845 211.1338 2.95 0.0016572 0.16 267.0564 1.9203 2.0565 3.2921 0.8208 1.5105 1.0013096 0.85 1.27 949.71 165.48 844.62 510.87 493.03 0.1 2.0146 0.9094 2.29 255.32 858.0011595 0.55 865.73 595.9 1556.3174 2.40 831.15 1006.0010084 0.3 1235.0009857 0.0013980 P  20 MPa (365.0018729 h kJ/kg 1585.2888 1523.06 756.3 0.8889 790.0012862 1148.4 1445.qxd 922 7/12/11 14:26:01 .23 500.1271 2.19 0.2996 1.3034 1.94 426.33 735.7499 4.0011149 0.0012314 0.07 97.5 3.90 434.5 0.66 576.9374 2.0 1115.0010496 0.78 1.02 860.18 584.0010072 0.2847 1.91 507.5 1334.50 413.2 1703.0009977 0.0010361 0.4575 1630.2488 u kJ/kg 0.0012268 1031.14 328.65 422.9 1610.7 1502.07 687.0659 1.05 246.0011435 0.0010823 0.8102 http://librosysolucionarios.85 580.0010105 0.94 487.9 2.0014733 0.93 180.0003 0.4 3.96 0.8469 3.75 684.0010410 417.0010738 0.8287 1.0010704 0.0015884 0.8586 3.59 414.85 0.0011304 0.74 525.92 853.5191 1.5037 2.84 929.0001 0.5685 0.5607 0.18 83.0014522 0.50 496.45 681.18 0.0 1231.1206 2.82 338.0009904 0.6086 3.0010623 0.01 767.69 416.6 1221.77 1016.1143 2.2 1134.0014450 0.6916 705.0010988 672.0010290 0.39 990.90 660.0 1338.2 1416.0 1343.8 1782.72 670.9259 2.0010244 0.0012044 0.0011412 0.32 0.1761 3.45 2.0010013 0.92 430.0001 3.0010954 0.0010221 0.8234 1.75 248.8260 1.0009767 0.0 1592.2932 0.0013611 0.1 s v kJ/kg  K m3/kg P  10 MPa (311.4951 2.42 405.0009952 0.7293 1.6 1037.94 C) Sat.36 0.77 263.0014049 0.8055 374.0 29.92 350.0011868 938.8 1191.3 15.0013226 0.0026 0.2943 0.0010057 166.33 249.0011122 0.7 1134.0265 3.0013409 0.7 1547.13 0.3100 2.23 82.4859 622.0011752 0.29 80.80 945.0011708 0.0010149 250.43 1.6 1826.0011482 0.0010199 0.0 1205.5 1667.0012978 0.28 598.2954 0.0012121 0.0012879 0.5 1571.6876 2.0010549 0.68 0.9 1097.4 1626.0 1233.0012770 0.0011390 0.0010920 0.5020 1. 300 11.12492 0.8 2344.2 2363.72 404.8 2482.66 389.0 2951.0 2835.84 334.95 381.391 11.70 2833.141 10.08510 0.5141 1.47 393.0 2467.063 10.923 APÉNDICE 1 TABLA A-8 Hielo saturado..001086 0.001091 0.18 366.947 11.9 2833.7 2332.8 2445.7 3610.7 1992.13 374.4367 1.689 9.6 2346.761 9.17 241. hig Vapor sat.3 2463.13 374.2 2837.3 2838.413 9.2 2327.25990 0.5 2496.001087 0.6 2459..5 2374.001088 0. T °C Pres.001091 0.154 9.969 12.05725 0.5 2485.51 942.001089 0.2 2452.40 333.18 366.2 2726.7 2434.21732 0.12 358.2 2727.2976 1.6 1. Vapor de agua Volumen específico. kJ/kg · K Temp..001088 0. sat.95 381.9 2722.04 354.4 2835.001090 0.001085 0.484 11.001090 0.695 10.66 389.15068 0.4986 1.3130 1.4212 1.374 10. Psat kPa Hielo sat.303 10.6 2321.70 2707.7 2357..4 2838.218 9..18121 0.4 2710.001085 0.25 397.01 0 2 4 6 8 10 12 14 16 18 20 22 24 26 28 30 32 34 36 38 40 0.001084 205.36873 0.5 2837.qxd 923 7/12/11 14:26:01 . uig Vapor sat.02490 0.01285 0.27 394.02004 0.154 9.8 2369.9 2355.613 10.001089 0.93 350.209 11.1 2717.3 2426. m3/kg Energía interna..1 2724.3 2338. sg 0.673 11.40 408.61169 0.2 2838.07 411.17 362.1 2478.2 2713. vi Vapor sat.06991 0.43 337.3 2500.17 370.43748 0.4521 1.0 2729.0 2723.001087 0.4 2838.644 http://librosysolucionarios.2 2836.4 2838.5 2714.001086 0..8 2493. si Subl.8 2836.net 18Appendix_01 ITALICAS.9 2709.8 2716.1 6750.17 362.0 1644.66 467.0 2430.30998 0.72 404.174 9.0 333.453 10.2 2728.01608 0.121 11.3903 1. kJ/kg Entropía.557 10.5 2835.3 2718.2 2421.033 11.2667 1.06 377.5296 10.221 10.985 10.8 2712.549 9.1 2341.001091 0. ug Hielo sat.470 10.9 2707.3284 1.001088 0.2821 1.06 377.1 2729.001087 0.5 2371.82 385.001087 0.40 333.375 10.9 4432.00 400.4831 1.4 2437.770 11..3748 1.7 333.3593 1.533 10.47 393.5 2360.2513 1.9 2456.10326 0.2 2352.618 9.4057 1.12 358.6 2719.835 9.5 8376.9 2837.2204 1.4 2324.7 2471.3439 1.5 2500.001085 0.869 11.347 9.1 2838.17 554.43 337.5 2838..7 2837.9 2834.0 2366.5 2335.1 2441..04 354.03082 0. hi Subl.2 2725.40 408.2358 1.51 1131.63 341.480 9..862 10. vg Hielo sat.4 5460.5 2448.80 345.88 787.8 2319. sig Vapor sat.909 9.00 400.578 11.778 10.07 411.3 1362.071 12.99 206.001090 0.4 2838.386 10.17 370.4 2349.25 397.7 2720.9 2838.001086 0.51772 0.7 2374.61115 0.2202 1.4676 1.6 2836.9 2330.282 9.62 283.94 350.47 659.63 341.2 2489.4 2474. hg Hielo sat.. kJ/kg Entalpía.04673 0.80 345.9 2730.82 385.03802 0. ui Subl. 2 % 10 0 100 0 120 0 1 60 1800 2000 h 0 300 0 28 0 550 P = 300 20 00 ba r 1 00 0 5 100 000 80000 0 D e n 50 sida d= 4 00 6000 kg/m 3 30000 0 20 0 15 00 00 200 kJ/kg =h 2= 0 100 200 300 400 500 600 700 800 1000 60% FIGURA A-9 Diagrama T-s para el agua.3 kg/m 3 3 kg/m 3 8 9 2650 h = 2600 2650 kJ/kg 2550 2800 2900 3000 3100 0 10 100 200 300 400 500 600 700 800 900 1000 1100 10 1200 Copyright © 1984.4 0. Gallagher y George S. Temperatura.qxd 924 0 16 0. 1 6 0.8 1.01 kg/m 3 sida d= .6 0. kJ/kg · K 18 0 0 800 kg kJ/ 200 8 1 kg/m 3 9 3200 3300 3400 3500 3600 3700 3800 3900 4000 4100 4200 4300 4400 4500 4600 4700 4800 4900 5000 h = 5000 kJ/kg g/m 3 0.0 8 6 4 3 2 1. Kell.1 1000 2 30 3k 0. °C 5 100 k g/m 3 4 300 k g/m 3 50 0 10 0 900 3 30 kg /m 3 40 30 20 15 10 kg/m 3 0.0 5 0.0 0.1 0. Reproducido con permiso de Routledge/Taylor & Francis Books.net 7/12/11 14:26:02 .0 . 03 00 2 0 1200 TABLAS DE PROPIEDADES. 0 15 Den 0 1100 1 120 % 140 40% 0. 0 006 0 . Inc.08 0. FIGURAS Y DIAGRAMAS (UNIDADES SI) 924 http://librosysolucionarios. 2 0. 0 0.5 0. 0 04 0.00 8 18Appendix_01 ITALICAS. De NBS/NRC Steam Tables/1 por Lester Haar.04 3 0.3 0.0 0 2 .1 h = 400 0 0 = ad lid Ca 600 uid % 20 Líq 3 do ra atu os 0 140 2400 2600 4 00 50% 0 20 00 3200 3400 4000 3800 3600 4500 6 h h= =4200 k J /k 00 22 00 Va po rs g do h= 7 10 kg /m 3 6 7 26 h00= 24 kJ/ 00 kg GCa rlaidn atída== 9900% % 70 80% % atu ra 0 10 80 0 6 0 80 0 60 0 50 0 40 0 35 00 3 0 25 0 20 0 15 5 Entropía. John S. 6 0. kJ/kg · K FIGURA A-10 Diagrama de Mollier para el agua. 3 01 0.0 5 0.qxd 925 7/12/11 14:26:02 . Inc.1 kg/m 3 kg/m 3 /m 3 1 kg 150 00 200 00 250 00 300 00 bar C 800°°C P= 4000 C 700°°C 0°C 600° 3000 0°C 500° Entalpía.01 0.net 18Appendix_01 ITALICAS. John S.1 5 04 0.5 1. . P = r ba 08 0. 0.8 0.0 5 De nsi da d= 0. kJ/kg Densi 100 dad = 00 1000 800 kg/m 3 0 600 0 500 40000 3000 20 15 00 800 10 00 00 6 40000 5 00 30 2000 1 00 kg/m 3 80 1150 00 60 40 50 30 20 15 10 k 10 g/m 3 °C 900°C 4000 02 0.12 0 0. http://librosysolucionarios.0 2000 % 66 % 64 % 62 % 60 % 58 56% 54% 52% 50% 48% 46% 44% 42% 40% 1000 2 3 4 5 6 7 8 9 1000 10 Entropía. Copyright © 1984. Reproducido con permiso de Routledge/Taylor & Francis Books. Gallagher y George S.925 APÉNDICE 1 5000 2 3 4 5 6 7 8 9 10 5000 °C 1100°C C 0° 0 T= 11 °C 1000°C 0°C 400° 98% 96% Ca 9 4 % lid ad= 92% 90% 88 86% % 84% 82% 80% 78 76 % 74 % 72 % 70 % % 68 % 0°C T = 300° 2000 3000 0.08 0. .4 6 8 6 4 3 2 1. De NBS/NRC Steam Tables/1 por Lester Haar. Kell.0 0. 5 01 0 0. 3 0 0. 84 46.84 219.68410 0.92554 0.55 57.20 17.38 233.23 387.0007571 0.94564 0.14 184.63 54.07382 0. uf Evap.037 210.32 76.74 217.0007054 0.64 240.13 222.08 170.95144 0.96 10.97 175. sat.57 73.92859 0.92 212.0007172 0.09 187.99 59.83 238.39 229.39 173.92310 http://librosysolucionarios.69 198..30 0.51 2.17395 0.30 194.81 225.43 216.23356 0.0008113 0.14504 0.92 229.52 203.17 0.73 184..67356 0.0007845 0.64230 0.59 235.94176 0.0007684 0 2 4 6 8 293.52 199.22 233..37 0.09 30.88 10 12 14 16 18 414.18476 0.88 213.10463 0.76 20.85307 0.15995 12.97 62.66 46.29112 0.38 238.01 314.31 48.60 200.24323 0.76008 0.96 204.90 239.43 68.69 157.13583 0.069255 0..94222 0.27 258.95 73.26 165.0008066 0.82 144.0007265 0.10 249.25 22.992 7.0007535 0.08414 0.38 170.78 193.93 185.18 70.566 211.94941 0..93497 0.44 252.0007930 0. vg Líq.0007608 0. sat.11 244.052762 51.70540 0.0007083 0.000 208.0007763 0.94 192.96584 0.475 4.39 27.53 0.69 33.079804 0.40 41.73 111. T °C Psat kPa vf Vapor sat.24711 0.93372 0.91 255.93911 0.93031 0.50 49.91 211.074304 38.09 243.0007234 0.41 239.02138 0.56 76.049403 0.52 232. kJ/kg · K Evap.86 227.82908 0.17 35.0007362 0.89 443.51 245.77130 0.056398 0.54 225.01 256.56 168.72 246.53 176. sat.10 225.84 337. Temp.43 92.0007297 0. sfg Vapor sat.86527 0.17 205.08 224.88 235.0007723 0.42 185.07 201.66308 0.0007464 0.12 228..036 2.57 33.92828 0.40 25.20666 0.93139 0.75 237. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-11 Refrigerante 134a saturado.68 62.28159 0.40 216.80 227.37 121.90 362.77 253.17489 0.22580 0.91 0.92389 0.67 226.58 163. sg 207. sat.net 18Appendix_01 ITALICAS.03 43.69 20.84101 0.18946 0..05 207.95511 0.49 28.98 221.39 178.25286 0.87 242.86 62.73794 0.92927 0.91560 0.25 215.04 204.64 183.25 56.31 473.94748 25.040748 0.55 41.926 TABLAS DE PROPIEDADES.71 0.72701 0.18 208.14729 0.81729 0.043417 0.36 0.13501 0.91 30 28 26 24 22 84.07 195.37 0.82 20 18 16 14 12 132.30 35..11481 0.73 76.93253 0.48 234.04253 0.19459 0.95356 0.96866 0. m3/kg Energía interna..16 231.099516 0. hfg Vapor sat.29751 0.26246 0.0007112 0.83 70.092352 0.27 232.04 38.72 0.45 192.76 101.06344 0. Tabla de temperatura Volumen específico.93629 0.78263 0.79 207.12 197.19 504.61 252.0007203 0.0007396 0.61 223.68 215.90278 0.70 12.96 65. ug 40 38 36 34 32 51.17 218.74896 0. kJ/kg Líq.28 0.86 224.35 222.0007430 0.27 223.32732 0..19 43.58 51.67 236.59 15. sat.92641 0.515 209.03199 0. Líq.66 5.79406 0.58 537.71616 0.0007329 0.qxd 926 7/12/11 14:26:02 .40 206.36081 0.27090 0.65 15.27204 0. kJ/kg Pres.12493 0.98 30.33 22.25 59.80 172.517 10.0007804 0.96315 0.05301 0.52 Entalpía.21415 0.92 167.61 180.060338 0.16498 0.65 230..56 189. sf Evap. ufg Vapor sat..80561 0.92 234.72 196.95813 200.73 189.12542 0.01 190.91 219.67 203.55 217.13 17.52 190.11597 0.86 54.22387 0.87762 0.10 67.0008020 0.11 214.00000 0.95579 0.30 56.37 259.20439 0.62 218.60 197.63198 0..09441 0.96866 0.046295 0.51 193.064612 0.0007142 0.01072 0.16 257.69471 0.94063 0. hg Líq.08 234.09 187.19 230.0007499 0.35 250.15504 0.038271 65.94389 0.0007975 0.55 210.45 251.10736 10 8 6 4 2 200.95 69. hf Entropía.0007887 0.26 s237.85 272.92 214.65266 0.96 186.29 201.89012 0.91 248.92733 0.09 220.0007646 0.04 0.46 260.085802 0.81 7.13 181.93766 0.92470 0.96058 0. 0009317 0.34789 0.81215 Fuente: Las tablas A-11 a A-13 se generaron utilizando el programa para resolver ecuaciones de ingeniería (EES) desarrollado por S.17711 0.32 82.69 182.40 218.44 87.54066 0.32903 0. kJ/kg Líq.35 95.51039 0.67 71.59 262.53058 0.32 120.33 131.023691 0. sg 20 22 24 26 28 572. ufg Vapor sat.91879 0.90359 0.77 190.39039 0.35730 0.90880 0.9 3594.0008786 0.02 124.61473 0. Chem. 5.61149 0.1.47993 0.6 0..99 261. hfg Vapor sat.62 156. http://librosysolucionarios. Tabla de temperatura (conclusión) Volumen específico.29 173.035969 0.02 242.0 1253.10 266. “An Internacional Standard Formulation for the Thermodynamic Properties de 1.46 115.58800 0.91391 0.2 1529.14 84.38 110.08 171.07 194. núm.0008536 0.36670 0.45 153.14 79.0009750 0.0009150 0.0008854 0.72217 0.18 685.09 162.89 863.qxd 927 7/12/11 14:26:02 .11 272. 1994.19 263.68 265.49012 0.0008996 0.31011 0.84 727.58102 0.14 248.8 1891.64 84.43 154. sat. sat.0 2118. D. Tillner-Roth y H.92018 0.26 119.13 126.85289 0.67 264.57091 0.012771 0.82 0.85 174.47 29.60 256.49 137.004599 0.39 163.008642 0.08 250.54 145.48 99.16 160.55074 0.56241 0.0008366 0.52 137.06 243.26 111.0008720 0.0008595 0.927 APÉNDICE 1 TABLA A-11 Refrigerante 134a saturado.46 279.13 164.42302 0.033828 0.65 156.16 165.93 95.31 0.07 608.0010372 0.40 180. J. vol.79 106.64 815.007480 125..33272 0.015939 107. A.39 144.72 92.2 3246..32 115.29 56.30111 0.89 202.005486 0.30 278.24 184.26 143. la cual está basada en la ecuación fundamental de estado desarrollada por R.43863 0.92160 0.009950 0. Phys.77 259.47018 0.031834 0.014265 0.49 270.39486 0.0009498 0. kJ/kg Vapor sat.56082 0.68 0.0015269 0.66 267.2-Tetrafluoretano (HFC-134a) for temperatures from 170 K to 455 K and pressures up to 70 MPa”.27 272.12 245.028242 78.1 0.002630 171.59 279.46 280.69 176.85 275.019952 0. vg Líq.82 262.23 82. sat.44 262.86 81..026622 0.12 249. hf Entropía.53 0.10 244.60 141. m3/kg Pres.95 273. Klein y F.62172 0.42 135.52049 0.89512 80 85 90 95 100 2635.41363 0.21 257.68 254.018855 0.58 139...46 147.35 149.64336 0.44 82.7 1191.32 113.30063 0.36 147.35 65.87010 0.14 247.57 269.92088 0.88 126.8 0.05 241.38 139. sat.68 0.88912 0.04 93.38548 0.0008478 0.. hg Líq. Baehr.58 96.26 258.8 1130.22 151. kJ/kg · K Evap.14 169..45941 0.41749 0.51 277.98 87. sat.92234 0. Temp.76 207.26 114.0008313 0.28 117.59115 0.37 0.016853 0. Ref.31958 0..53755 0. 23.27 646.58 280..89982 0.27 180.98 149. T °C Psat kPa vf Energía interna.91067 0.43242 0.0010772 0.15 263.05 224.91811 0.0008421 0. Data.1 1072.64 263.22674 0.87 155.83 90.36227 0.2 2365.35 963.40425 0.0011932 0..net 18Appendix_01 ITALICAS.87 247.49 178.00 160.1.89 252.0008657 0.91675 0.80 253.29 250.18 258.60130 0.017824 0. ug Entalpía. L.37609 0.53 130.11 912.91 174.14 271.05 108.1 3975.011434 0.75 274.91236 52 56 60 65 70 75 1386.91 139.48920 0.66 101.0008261 0. La rutina utilizada en los cálculos es la R134a.42 158.0010037 0.67578 0.90669 0.91743 0.26644 0. Los valores de entalpía y entropía para el líquido saturado son cero a –40°C (y –40°F).0011270 0.79 98.39 0.0012933 0.22 260.55 104.33846 0.97 251.91536 0.86 158.0008161 0. Líq.40 102.1 1682. sf Evap.55 108.76 145.98 277.91606 40 42 44 46 48 1017.12 272..28 121.45126 0.003726 0.0008210 0.08999 0. Alvarado. sfg Vapor sat.63 263.006436 0.021119 92.029976 0.022364 0.10 132. uf Evap.91464 0.91315 0.17 167.50027 0.77 154.88117 0.3 2928.01 162.51320 0.14 100.26 90..91948 30 32 34 36 38 770.64 280.59 132.21 33.33 105.025108 0.67 156.28 116.62 268.0008924 0.58 246. 35 222.0008580 0. P kPa Temp.46 141.33 77.37 46.98 244.48 22.81 158.54 81.40 263.83 103.63 186.0007533 0.03 266.099867 22.21 14.66 50.81 255.73 96.69 106. sfg Vapor sat.54 196.027371 0.42441 0.0007437 0.54 165.10 148.92400 0.98 31.26 188.. kJ/kg · K Vapor Evap.0007487 0.029361 0.72 168.0008130 0.79826 0.28 249.0008266 0.95 33.37 101.034295 0.22 167.46 233.024069 88.96042 0.16 59.30 260.69 29.12 210.04711 0.67929 0.19254 3.0007259 0.98 183.14014 0.010559 0.841 7.45734 0.88 253.07188 0.71 194.45 77.27 188. sat.91624 0.0008520 0.14 229.680 11.90999 0.17794 0.92 59.94 171.38 1.86 244.798 7.25 218.51 257.0008458 0.94190 0.09 280.0009166 0..40 0.20 201.23270 0. sf Evap.53323 0.01634 0.43 214.17 280.0007985 0.0011406 0.83 111.0007324 0.66069 0.92836 0.28 223.94 148.91994 0.22 95.19 3.50294 0.12693 0.022683 0.46 213.83368 0..0007699 0.81 73.48 212..006936 0.82 8. Tabla de presión Volumen específico.31 17.47 260.11087 0.063604 0.72 251.23 137.009288 0.0007185 0.00 238.47911 0.18 55.91558 0.61378 0. sat.42873 0.76 169.75664 0. Tsat °C Líq.33230 0.88 212.83 38.95427 0.90 207.21 217. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-12 Refrigerante 134a saturado.47 80.62 247.97 54.37 17.64 163.47 98.24 154.94807 0.12348 0. sat.79 97.92282 0.90184 0.82 169.54 86.16 92.31121 0.93965 0.072352 0.041118 0.93458 0.31695 0.0008395 0.0007841 0.58763 0.39189 0.12 0..44 0.net 18Appendix_01 ITALICAS.60030 0.28 195.43 142.87 31.51 107.81 256.15 270.01 146.52509 0. kJ/kg Vapor sat.20 0.29 52.92535 0.46 15.57 197.91835 0.93 135.25776 0. uf Vapor Evap.07 44.97 38.08 31.00 220.26465 0.85503 0.93006 0.031646 68.51 37.78 166. sat.52368 0.29 268.44 63.95710 0.90 178.45315 0.65 26.82 92.083897 0.67 246.67 156.70 125.38 180.72 63.07 151.79 250.06008 0.79 247.08 191.92691 450 500 550 600 650 12. kJ/kg Líq..qxd 928 7/12/11 14:26:02 .045619 0.0008059 0.37377 0.21263 0.0008331 0.0009886 0.96441 0.037408 0.91762 900 950 1000 1200 1400 35.62118 0.69566 0..93 77.95183 120 140 160 180 200 22.46 5.57 190.11 130.90 206.0007907 0.0007772 0.87894 http://librosysolucionarios.97 239.99 224.35404 0.95 222.0010566 0.83 243.73 231.43 248.48863 0.71 265.40204 0. m3/kg Pres.11041 0.11 192.51 219.38301 0.53 259.91912 0.55 0.. vf Energía interna..56431 0.45 263.91692 0.014107 100..51 263.28023 0.24 91.91050 1600 1800 2000 2500 3000 57.0008934 0.62 199.85 88.63 277.26 270..45 227.020313 0.90 269.62821 0.55349 0.91 0.36413 0.15457 0.94779 0.71 185. ufg ug Entalpía.34345 0. sat.0007620 0. sg 60 70 80 90 100 36.75 240.15 14.22 258.38 235.99 183. hf Entropía.056738 0..65 217.35 241.0007144 0.73 10.48 39.94 202.30 199.71 18.79 279.46 0.31 0. vg Líq.50 176.99 273.21637 0.16 0.81496 0.66 165.82 163.16 186.64377 0.71369 0.77 0.54315 0.0008641 0.13 28.06 31.21 205.30799 0.29461 0.37 0.16 227.02 234.90784 0.45 116.26929 0.48 49.78316 0.46 231..92 262.67 179.20 267.0007383 0.32 117.59 94.68 253.61 173.51 85.04 124.87 67.10 144.09 0.93210 0.60 12.14139 0.55 24.11 128.48 237.88 215.90498 0.45 72.0008700 0.025621 0.09 34.19829 0.37675 0.77 15.61 104.25 160.88 62.85 249.60 176.20 68.73 21.94456 0.54 221.17 261.051201 44.89226 0.03267 0.09 0.08 152.98 209.16212 0.77 127.25 2.98 171.45 0.57531 0.92081 700 750 800 850 26.0008199 0.48 245.87995 0.09275 0.0009639 0.021438 0.32 18.02 84.928 TABLAS DE PROPIEDADES.93773 240 280 320 360 400 5.016715 0.93 144.16 241.87 156.730 11.92177 0.87 276.10 81. sat.03 236.012123 0.21 34.005275 134.49 27.52 233.40 26.62 182.32051 0.11 242.21 173.91303 0.08 209.73381 0.0007098 0. sat.23753 0.32 203.33 111.26 135.79 229.33 149.0009400 0.89419 0.86 279.57567 0.24761 0.04 117.0007223 0. hfg hg Líq.00 149.31 33.92775 0. 9446 0.79 279.58 262.2483 1.57 351.65 285.01 324.9269 0.11418 0.90 277.10 270.19 219.2356 P  0.93 263.066443 0.9721 1.48 322.19841 0. 0 10 20 30 40 50 60 70 80 90 100 110 120 130 140 0.07231 0.99 0.10 MPa (Tsat  26.56 286.0624 1.39302 0.2836 1.18 MPa (Tsat  12.056796 0.17 280.0595 1.9724 1.14 263.10045 0.76 248.0774 1.57 306.13641 0.58 268.9380 0.07530 0.59 279.71 278.1958 1.92 313.08675 0.0690 1.2732 1.41 306.07282 0.059292 0.59 270.64 255.15908 0.73 341.net 18Appendix_01 ITALICAS.1690 1.60 0.97 298.13 316.9798 1.9301 0.14933 224.87 382.05 296.34 298.64 280.07235 0.18412 0.49 255.02 232.23 314.26 325.93 343.05 261.33 330.66 276.09 334.11189 0.75 233.9321 0.20 0.98 332.061724 0. 10 0 10 20 30 40 50 60 70 80 90 100 0.99 344.37893 0.36 278.54 239.86 294.09812 0.72 296.39 349.95 °C) 209.54 382.33608 0.25 272.1195 1.38 295.32 312.98 306.079913 0.08390 227.79 240.1983 1.44 239.60 313.27626 0.35 255.26 321.69 314.9680 0.41 256.28 MPa (Tsat  1.2572 1.44 251.66 226.80 0.42102 0.0332 1.11722 0.3260 1.11675 0.2191 1.0528 1.20847 0.09961 0.40 MPa (Tsat  8.929 APÉNDICE 1 TABLA A-13 Refrigerante 134a sobrecalentado T °C v m3/kg Sat.24 0.2814 P  0.46 234.99 295.2942 http://librosysolucionarios.16 287.25 288.06 342.31121 0.70 294.69 267.2074 1.9831 1.1636 1.1021 1.42 344.75 305.94 281.2742 1.18 252.0157 1.09000 0.0031 1.14014 219.53 361.30 293.08 305.16 0.15 322.2602 P  0.35 256.09423 0.1298 1.59 302.54 253.15 286.16622 Sat.58 265.13 254.57 304.60 0.1369 1.66 248.0918 1.55 334.06 296.07997 0.29303 0.56 287.08 271.11041 0.46 °C) v m3/kg u kJ/kg h kJ/kg s kJ/kg  K P  0.68 289.66 272.3250 v m3/kg u kJ/kg h kJ/kg s kJ/kg  K P  0.10314 237.2249 1.32 340.14 247.20743 0.52 277.1163 1.29 238.12766 0.9644 1.35 372.89 287.11818 u kJ/kg h kJ/kg s kJ/kg  K P  0.2305 1.9305 0.06609 0.88 0.9377 0.18 0.0739 1.1256 1.80 352.1418 1.91 296.66 241.38 279.08395 0.0477 1.06360 231.40705 0.2171 1.2997 1.11205 0.68 305.09 °C) 0.2512 P  0.97 312.24 MPa (Tsat  5.10942 0.60 227.0303 1.64 297.14504 0.00 314.04 270.071023 0.0331 1.96 288.38 °C) 0.0285 1.00 323.91 304.14605 0.0718 1.25937 0.09324 0.9937 1.08338 0.85 304.58 270.31 271.36 260.1001 1.97 244.48 240.50410 Sat.073274 0.14715 0.1907 1.1805 1.07 284.54 264.50 253.95 241.11512 0.1714 1.068747 0.10587 0.37 °C) 0.12398 231.55 232.27 246.2882 1.70 297.71 272.49032 0.81 272.37 289.2553 1.1915 1.054213 0.86 275.3096 P  0.1762 1.051506 0.90 349.74 254.98 246.09503 0.44 238.89 331.50 261.91 233.22 303.15196 0.23373 0.14 343.00 247.9544 0.9484 0.1571 1.68 362.58 263.74 227.54 245.44883 0.99 225.09 239.17172 0.0004 1.12 220.0882 1.08 305.74 307.09991 0.78 315.25 °C) 229.97 260.75 326.36 254.15673 0.0102 1.93 333.14074 0.19254 0.36 279.35048 0.2463 1.9397 0.63 350.2092 1.36476 0.82 278.17794 0.051201 235.44 264.27 324.1474 1.16544 0.0814 1.1066 1.95 264.36 295.0030 1.18 278.22506 0.25 304.11874 0.9346 0.48 224.qxd 929 7/12/11 14:26:03 .63 334.25088 0.2626 1.9698 1.67 314.59 315.22 280.77 325.07823 0.63 371.1094 1.9856 1.55 0.2688 1.50 247.2339 1.1640 1.65 269.52 251.1203 1.22 255.42 305.30 248.46 230.0134 1.08617 0.2288 1.08111 0.06 262.26783 0.09 249.46 333.37 287.83 259.1280 1.082096 235.0862 1.08672 0.24233 0.35 288.2035 1.05 315.79 256.9628 0.3520 P  0.92 249.0628 1.67 247.11310 0.14 MPa (Tsat  18.46269 0.97 287.23 240.2105 1.064104 0.30138 215.87 383.16 253.3135 0.1484 1.10955 0.29 313.08953 0.49 343.2431 1.00 335.09775 0.1749 1.61 262.19025 0.16149 0.0174 1.47651 0.1441 1.17 246.60 262.9987 1.46 244.16 307.62 342.55 339.40 333.16 331.9518 0.86 258.15 279.1532 1.13248 0.13206 0.51 323.09026 0.077717 0.21630 0.73 296.1142 1.0576 1.12038 0.2367 1.55 234.0236 1.97 288.1353 1.60 269.43495 0.30 362.2020 1.53 303.0429 1.87 0.1840 1.86 245.91 °C) 0.32 MPa (Tsat  2.32 285.72 250.0451 1.20 0.02 331.075504 0.86 321.88 242.99 297.96 312.73 °C) 222.12748 0.9362 0.77 °C) 0.70 372.20 MPa (Tsat  10.1825 1.62 295.68 268.47 304.73 288.07646 0.09987 0.10570 0.10481 0.12322 0.39 352. 20 10 0 10 20 30 40 50 60 70 80 90 100 0.74 244.12240 0.0912 1.38 314.28 296.0399 1.28465 0.09644 0.0975 1.15263 0.10275 0.14230 0.41 263.1554 1.44 322.07 255.20242 0.13741 0.07 340.07 313.93 271.2997 1.09229 0.9519 0.06925 0.58 256.28 0.27 278.10897 0.06 MPa (Tsat  36.66 316.11 313.21449 225.79 271.57 344.19635 0.41 286.10193 0.2222 1. 2721 1.28 328.96 367.36 0.19 352.75 296.39 322.68 251.9240 0.1264 1.81 257.66 391.023355 0.25 357.1394 1.055522 0.40 250.1658 1.70 375.51 316.1971 1.9163 0.1536 1.64 335.044688 0.20 421.9383 0.18 380.2554 1.2623 1.0458 1.58 378.07 0.021155 0.76 346.0981 1.2577 1.86 390.033457 0.40 MPa (Tsat  52.2830 1.025086 0.2444 1.38 372.94 270.0121 1. 20 30 40 50 60 70 80 90 100 110 120 130 140 150 160 0.016060 0.019502 0.1900 1.0748 1.025398 0.52 327.07 332.050485 0.9525 0.0417 1.034295 241.2298 1.15 307.13 305.08 273.2467 1.1360 1.038813 0.03 334.048499 0.9313 0.33 318.83 281.81 306.0661 1.70 MPa (Tsat  26.9169 0.27 402.21 286.11 280.86 299.020194 0.1114 1.06 356.61 374.00 399.057006 249.29 276.55 °C) u kJ/kg h s kJ/kg kJ/kg  K P  0.26 383.02 361.03 0.3088 0.0280 1.60 MPa (Tsat  57.73 319.0194 1.3124 P  1.45 286.37 276.2067 1.0500 1.50 320.57 360.34 317.039423 248.64 300.15 318.2491 1.87 337.021506 0.059880 0.63 329.9267 0.037829 0.81 386.46 339.2186 1.9660 0.024757 264.020406 0.57 288.76 323.046318 0.9614 0.97 327.1632 1.58 290.02 374.033164 0.86 298.10 285.40 0.9389 0.017923 0.73 371.019597 0.028547 0.37 °C) 0.78 385.028367 0.46 392.020830 0.76 376.23 338.068775 238. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-13 Refrigerante 134a sobrecalentado (conclusión) T °C v m3/kg u kJ/kg h kJ/kg s kJ/kg  K P  0.025927 0.99 271.029158 253.039659 0.64 302.60 MPa (Tsat  21.73 301.2192 1.51 311.041118 0.2875 1.019545 0.70 327.2703 1.30 263.69 406.1580 1.1031 1.47 336.72 386.036373 0.37 363.11 364.07 396.61 354.024809 0.20 407.84 299.74 293.023375 0.73 319.69 293.31 0.53 350.034241 0.0835 1.06 366.76 0.035193 0.00 0.51 294.054331 0.047306 0.0011 1.031340 0.76 400.91 329.9733 1.89 271.40 348.2584 1.48 291.51 368.0309 1.20 274.45 327.17 302.0256 1.47 297.00 342.044710 0.1389 1.41 343.0883 1.027035 0.1118 1.036349 0.9954 1.99 267.31 386.38 325.26 267.0860 1.69 383.048597 247.2163 1.76 282.91 350.85 314.88 °C) 0.44 0.0987 1.81 280.9499 0.02 332.55 333.62 284.9938 1.041143 0.9327 0.63 325.81 270.01 313.01 282.59 288.018201 0.96 301.2807 0.037625 0.1684 1.66 357.10 337.1258 1.33 259.10 308.029592 0.15 410.3221 P  1.930 TABLAS DE PROPIEDADES.71 282.020529 0.022442 0.058053 0.69 °C) 0.25 305.26 305.2449 1.73 343.28 304.net 18Appendix_01 ITALICAS.033941 0.34 353.72 289.05 352.18 336.43 418.42 308.12 0.14 312.02 417.40 °C) 250.23 376.037384 0.51 373.72 0.054027 0.9156 0.027566 0.28 299.1705 1.06 308.9199 0.82 263.59 411.2321 1.48 265.018778 0.9130 0.039250 0.034875 0.1230 1.023348 0.69 408.9850 1.024261 0.30 260.53 298.86 266.15 283.030581 0.024061 0.19 346.025621 0.1949 1.94 326.88 316.34 319.0698 1.76 338.28 366.042115 0.067021 0.1530 1.89 293.017201 0.021904 0.46 356.61 311.81 290.89 339.11 345.48 275.2699 1.9535 0.050997 0.2061 1.9078 0.0408 1.2421 1.0110 1.043427 0.07 316.09 292.56 277.023068 0.0574 1.032068 0.45 278.23 389.026753 0.9218 0. 50 60 70 80 90 100 110 120 130 140 150 160 170 180 0.90 MPa (Tsat  35.41 367.028584 0.0949 1.026492 0.2676 http://librosysolucionarios.01 0.10 320.85 355.065256 0.0705 1.29 268.29 348.2999 1.2233 1.024228 0.37 330.030951 0.00 MPa (Tsat  39.31 °C) Sat.1924 1.22 399.049458 0.1773 1.77 295.71 365.2972 1.45 379.90 369.47 349.9976 1.015005 0.0836 1.32 379.1664 1.043358 0.035317 P  1.60 280.9183 0.01 282.018404 0.80 300.1798 1.98 309.0546 1.44 271.56 364.46 273.86 272.97 368.40 354.2747 1.046004 0.036420 0.9875 1.84 259.0160 1.02 367.38 303.69 377.89 292.027552 0.052519 0.04 347.63 267.2838 1.22 257.063479 0.3327 P  1.qxd 930 7/12/11 14:26:03 .80 315.044338 0.031696 0.040642 0.56 357.3249 P  0.40 388.043069 0.039985 0.035302 0.1308 1.59 359.0248 1.022636 0.55 338.29 °C) Sat.1504 1.042010 0.29 338.028630 0.05 389.029973 0.03 381.67 310.55 329.60 358.021796 0.01 385.047900 0.44 394.2951 P  0.19 328.2109 1.75 242.86 0.59 357.017500 0.1846 1.034392 0.71 °C) Sat.06 345.48 256.9641 0.61 340.51 °C) 0.1162 1.17 362.1414 1.046456 0.026146 0.02 402.53 356.80 330.016014 0.037865 0.0364 1.032659 0.029361 244.17 284.018882 0.81 386.40 347.77 344.52 269.50 MPa (Tsat  15.020388 0.012123 258.39 265.035984 0.1081 1.25 284.25 324.056205 0.88 375.016773 0.32 279.82 370.69 296.9105 0.016715 0.67 348.30 341.0599 1.1140 1.64 0.50 311.038408 0.52 401.09 363.1436 1.95 309.9802 1.13 262.39 315.30 347.032512 0.75 384.88 422.021456 260.72 276.79 254.044554 246.83 358.014107 256.9480 0.012372 0.55 422.061687 0.3080 1.2368 1.80 MPa (Tsat  31.47 277.1803 1.2210 1.029966 0.85 366.83 262.89 336.82 309.015215 0.87 291.27 289.66 397.2038 1. 40 50 60 70 80 90 100 110 120 130 140 150 160 170 180 0.20 MPa (Tsat  46.042290 0.12 372.95 319.9816 1.031554 0.2327 1.82 420.9179 0.2954 v m3/kg u kJ/kg h kJ/kg s kJ/kg  K v m3/kg P  0.1930 1.029806 0.017023 0.26 274.0795 1.013430 0.87 278.0549 1.07 322.027413 0.033322 0.85 253.9703 1.88 410.020313 0.04 270.041389 0.022683 0.052427 0.0056 1.46 274.014362 0. 4 0 2 2. Georgia.04 0.1 6k J/k gK 6 0. Inc.4 8 0.0 s= 2.72 o satu rado 0.1 1. pero no de ambas.9 0.60 1. Nota: El punto de referencia utilizado para la gráfica es diferente al empleado en las tablas de R-134a.52 1.6 4 2.4 1.7 0.qxd 931 7/12/11 14:26:03 .2 0.net 18Appendix_01 ITALICAS.4 2.8 0.12 1.2 4 8 2.01 100 4 3.5 250 0.7 2.8 0.2 –40 0.76 1. Reimpreso con autorización de la American Society of Heating.2 0..3 0.01 750 FIGURA A-14 Diagrama P-h para el refrigerante 134a. Por lo tanto.20 0.6 líquid 0.4 400 450 Entalpía.36 1.44 1.88 Presión.04 0. los problemas deberán resolverse utilizando todos los datos de propiedades obtenidos.3 2. MPa 2 32 20 T = 0°C 0°C 0° 1 4 90 70 60 50 40 80 4 750 20 700 0. Atlanta. kJ/kg 220 200 180 T = 160° 160°C 160 °C 140 120 100 80 60 40 20 0 –20 –40 satura do vapor 300 0.3 2.931 APÉNDICE 1 00 95 0 90 0 85 0 80 0 400 10 0 110 0 350 105 115 0 1250 kg/m 3 300 1200 1350 250 1300 1450 200 1400 10 150 1500 100 20 450 500 550 600 650 700 300 400 0 70 00 6 0 50 Densidad 10 /m3 = 200 kg 160 100 120 60 R-134a 2 40 24 1 16 12 0.68 1. http://librosysolucionarios.6 2.2 2.02 0.92 1.6 –60 200 X=0 0.00 1.4 0. Refrigerating and Air-Conditioning Engineers.04 –20 0.4 8 2.28 1.02 150 0.1 350 550 600 300 280 260 240 650 2 0.64 2.84 1.4 0. ya sea de las tablas o de la gráfica.80 0.2 1.96 0.1 .5 6 s= 8 500 0. Universidad de Wisconsin.40 1.6 1.50 0. TEMPERATURA REDUCIDA.0 Gráfica núm.95 0. 1 TR = —– v 0.9 Pv RT 0 1.20 0.00 3.60 .932 TABLAS DE PROPIEDADES.0 T TR = —– Tcr 1.3 1. 2 1953 TR = 1.0 2.00 3.5 3. Z = —– 2.10 1. P R FIGURA A-15 Carta generalizada de compresibilidad de Nelson-Obert.3 1.20 =0 vR 1. P PR = —– Pcr TEMPERATURA REDUCIDA.5 0.00 TR = 15 TR = 3.20 1. 35.7 0.8 0 1.60 0 0.10 0.30 0.60 1.00 = GRÁFICA GENERALIZADA DE COMPRESIBILIDAD DE NELSON-OBERT 0. v = —– R RTcr / Pcr 1.20 1.60 0.40 1. FIGURAS Y DIAGRAMAS (UNIDADES SI) a) Presiones bajas.0 0.90 0 Pv RT FACTOR DE COMPRESIBILIDAD.9 1.00 1. 1.1 0.25 0.00 0 1. Con autorización del doctor Edward E.20 1.00 2.5 5.80 .0 6. 1.5 Z 1.50 1.5 7.85 12 10 70 0. Obert.40 PRESIÓN REDUCIDA.9 0.7 0. 0 < PR < 1.90 0.50 GRÁFICA GENERALIZADA DE COMPRESIBILIDAD DE NELSON-OBERT 1.70 0.2 0.10 1.20 0.0 TR = 5.15 1. 0. VOLUMEN PSEUDORREDUCIDO.net 18Appendix_01 ITALICAS.30 0.90 0.10 TR = 5.0% R FACTOR DE COMPRESIBILIDAD.0 3.45 0 0.0 0.00 00 00 60 1.10 0.00 .4 5 0.15 1.6 0.qxd 932 7/12/11 14:26:03 . 75 0 3.9 0.0 80 7 0 0 .8 0.00 0.5 4.4 0.40 1.4 0.50 =0 v R 0. 20 1.30 0.7 T 2.00 00 3. 0 < PR < 7 3.6 0.05 PR 1953 0.95 0.5 6. Z = —– 0.50 1.0 PRESIÓN REDUCIDA.00 4.20 2 2.75 0.0 5.5 0.65 0.00 NOTA 0.05 0.30 0.3 0.80 0.00 TR = 2.0 5 5 ---DESVIACIÓN > 1.60 1.60 2.80 1.10 0.60 P P = —– R Pcr PRESIÓN REDUCIDA.00 1.00 30 0.40 .00 0 1.50 1 1.80 vRr 0. 0.90 20 15 0. v VOLUMEN PSEUDORREDUCIDO.50 2.8 1.9 v R= T Tcr Z Gráfica núm.0 PRESIÓN REDUCIDA. 1.5 2.7 0.00 6 5.00 1.60 8.05 1.80 2. http://librosysolucionarios.60 .8 5 0.00 2. 0. P R b) Presiones intermedias. 1. v = ––—––– R RTcr / Pcr 0.0 4.3 0.5 1.40 1.40 0 0. 0195 0.0219 0.6 314.615 1.0242 0.668      105 105 105 105 105 0.8 0.595 1.000 12.86 48.0 322.590 0.60 3.63 64.80 101.0217 0.027 1.7 318.805 9.0195 0.414 0.94 44.0212 0.802 9.5 331.1 295.790 9.1 333.5 338.752 1.0220 0.602      105 105 105 105 105 0.422 1.20 5.5 295.12 68.8 314.325 kPa.2 61. r = 1.62 51.783 1.2 321.798 332. Oficina de Impresiones del Gobierno de Estados Unidos.8 338.05 52.1 0.785 9.797 9.796 9.5 56.0 25.804 340.65 30.700      105 105 105 105 105 0.7 54.0 337.79 7.622 1.794 9.80 9. Standard Atmosphere Supplements.582 1. http://librosysolucionarios.08 9.732      105 105 105 105 105 0.7 334.9 318.5 18. Basadas en las condiciones medias anuales a una latitud de 45° y una variación de acuerdo con la época del año y con los patrones del clima.0222 0.47 42.792 324.771 1.0195 0.3 339.52 9.0238 0. kg/m3 Viscosidad m.648 1.89 3.5 36.92 9.3 308.568      105 105 105 105 105 0.0253 0.36 66.156 1.933 APÉNDICE 1 TABLA A-16 Propiedades de la atmósfera a gran altitud Altitud.61 94.788 9.819 0.726 1.751 299.0250 1000 1200 1400 1600 1800 8.791 9. 1966.764      105 105 105 105 105 0.19 79.805 9.800 9.70 0.628 1.007 0.764 9.967 0. m/s2 Velocidad del sonido.0230 0.66 60.60 83.32 92.422 1.646 0.76 71.30 89.795 328. m/s Densidad.2 47.561  105 1. Las condiciones al nivel del mar (z = 0) se consideran como P = 101.675 1.5 319.50 7.0224 0.179 1.909 0. W/m · K 0 200 400 600 800 15.0232 0.789 9.782 9.39 9.0248 0. T = 15°C.6 14.527  105 1.526 0.202 1.0236 0.1 21.55 75.80665 m2/s .1 295.6 327.758 1.134 1.0243 0.660 0.0223 6000 6200 6400 6600 6800 24.166 0.631 0.4 0.422 1.52 57.0227 0.3 1.70 12.98 12.000 49.0252 0.769 0.785 316.787 9.59 1. °C Presión.694 1.9 43.69 70.6 323.5 56.752 1.1 0.2 329.6 27.1 295.090 1.0251 0.789 1.804 9.07 58. g = 9.0229 5000 5200 5400 5600 5800 17.745 1.0201 0.5 26.779 312.947 0.000 14.50 77.4 1.770 9.0245 0.681 1.687 1.806 9.49 9.9 29.794 9.802 9.53 81.00 13.88 87.0239 3000 3200 3400 3600 3800 4.0252 0.791 9.90 4.713 1.987 0.1 317.854 0.5 56.17 10.786 9.1 303.801 336.617 0.8 327.312 0.458 1.872 0.788 9.575 1.799 9.0218 7000 8000 9000 30.49 5.000 18.57 9.3 0.797 9.7 331.0 330.63 73.28 9.9 56.4 22.11 35.588 1.0 326.228 0.112 1.9 16.493  105 0.0226 0.674 1.707 1.S.758 9.776 9.40 14.23 49.qxd 933 7/12/11 14:26:03 .608 1.785 320.800 9.803 9.9 334.94 63.3 26.09 8.69 43.655 1.604 1.10 9.5 315.2250 kg/m3.0244 2000 2200 2400 2600 2800 2.0241 0.736 0.0240 0.00 55.95 96.928 1.33 98.0 313.72 85.22 45.8 323.53 7.069 1.635      105 105 105 105 105 0.0234 4000 4200 4400 4600 4800 10. m Temperatura.0233 0.785 0.793 9.0195      Fuente: U.225 1.0237 0. kg/m · s Conductividad térmica.51 9.0221 0.721 0.467 1.40 11.642 1.0247 0.661 1.720 1.0206 10.777 1.048 1.4 0.00 0.807 9.739 1.4 335.50 19.2 325.837 1.27 9.802 0.0228 0.8 20.891 0.705 0.122 1.net 18Appendix_01 ITALICAS. kPa Gravedad g.0231 0.0235 0.799 9.4 41.422 105 105 105 105 105 0.0249 0.2 1.3 13.690 0.796 9.793 9.000 16. 97 230.00 105.16 293.069 3.35 536.72 35.08870 2.87324 2.04 1068.5477 0.37348 2.42 350.08 44.07732 3.742 7.49364 2.98 34.14 0.45 192.96770 2.0 123.82 702.67 676.27967 1100 1120 1140 1160 1180 1161.522 4.73498 1.05 89.31809 2.62 827.84 41.1 1.29 778.49 360.2 596.4 200.47716 2.11161 2.57 18.04142 2.31 32.12 36.24 264.96633 1.54175 2.0 121.0 1.69 454.74 565.99034 3.78 465.66 13.85 228.00 171.58 370.0 887.8 528.0 1084.85 27.84 179.0 254.8 223.28 1207.62 756.4 133.27 910.50985 2.63279 1.17760 1000 1020 1040 1060 1080 1046.32 523.33 979.02 496.7 170.1 189.77 2.55 1023.6 251.61 572.60319 310 315 320 325 330 310.98 866.67 380.1 154.01260 3.28 708.50 389.379 2.470 13.915 278.1 422.69 307.03 33.07 217.02 240.9 631.52 607.0 1.1 179.7375 1.85 1114.50 72.031 9.93 955.79783 2.95 14.70 236.28 97.17 575.93 286.34 396.3363 0.46048 2.38 15.98 592.89 78.31 1324.78 442.80 462.14 19.76 67.92128 2.04 734.8 808.98 2.13407 2.74 503.747 13.626 2.62 504.08 725.35 555.98 411.7 110.53 2.25 224.684 10.241 3.34 167.27 724.66802 1.806 4.27 43.17 298.27 320.40 26.28 185.17888 3.15 434.85 39.29 325.86 23.72 23.94468 440 450 460 470 480 441.3860 1.14 19.92 374.11 280.1 127.13 24.43557 1.8345 1.35 897.19 305.15916 540 550 560 570 544.31 16.2 2.064 15.64 21.13 285.2 393.332 5.43 3.3987 0.946 16.86 1137.245 6.18 300.84 20.94 776.13 59.93 238.55848 1.0 1512.3 549.1 647.05 260.56 149.84 88.62 329.35531 1200 1220 1240 1277.78249 1.30 608.2 222.29559 1.09825 3.6 508.25 75.52 713.18 800.79 1301.892 3.64737 2.6 105.44 767.09 115.47824 580 590 600 610 620 586.9352 221.82 57.75 203.21952 2.24 315.97 209.824 8.29 82.54 51.71787 2.26 431.92 1254.02 741.07 544.4686 206.66176 2.11883 3.34444 1.89748 2.02 513.06533 900 920 940 960 980 932.97 219.25997 2.99 560.40 657.42 411.4 367.58 691.08 888.2 845.39140 2.74504 2.481 3.33 862.59 624.31 330.7 272.2 343.33 951.85708 1.55 427.1 1.57277 2.28 17.6 162.29 21.15604 2.61 451.1584 178.2 674.68515 1.18 30.38 977.03449 3.10 11.3543 1.97 139.40902 2.33 520.63 533.7 2.02 235.80 30.04 596.02 617.86 404.70203 1.43 300.38 32.81 92.44356 250 260 270 280 285 250.30 322.8 101.22 28.0889 1.0 1346.17 23.12 62.30 18.09 68.71865 680 690 700 710 720 691.42 450.4690 0.97 337.net 18Appendix_01 ITALICAS.7 193.64 214.94001 800 820 840 860 880 821.89 1091.6442 1.4 1.69 156.47 681.2311 1.91 915.69013 340 350 360 370 380 340.4 1.50 37.qxd 934 7/12/11 14:26:04 .75 52.33685 2.79 880.58810 2.08 359.13 1707.10 793.3068 1.02 0.176 242.99 321.09 968.19834 3.16 295.77170 2.0 1205.89 114.9 155.6355 142.1 146.46 271.91 210.57 1230.95 641.53 628.63280 2.59 11.29 28.73 2.24 482.29906 2.3 143.9 621.6 211.5 301.8405 0.82 164.268 315.56 69.12 421.411 9.01 488.23 528.86 12.3 266.886 16.95 48.4 489.07 1184.0 738.64 2.9590 1.32 344.896 17.23993 2.36 810.22 1. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-17 Propiedades de gas ideal del aire T K h kJ/kg Pr u kJ/kg vr s° kJ/kg · K T K h kJ/kg Pr u kJ/kg vr s° kJ/kg · K 200 210 220 230 240 199.51917 1.2 96.91313 1.82344 390 400 410 420 430 390.88 400.99194 2.0 706.02 257.45 512.75106 1.99 85.92 1000.61803 2.34 1.79783 730 740 750 760 780 745.88543 1.36 381.36 419.7329 0.05608 490 500 510 520 530 492.88 25.02 472.02 551.82 25.49 5.59634 1.7 133.07 14.95 843.21751 http://librosysolucionarios.01 576.1 207.42644 2.22 659.13916 3.82790 1.39105 1.6 283.60 63.5546 1.55731 2.92 2.84856 2.25 481.934 TABLAS DE PROPIEDADES.3 933.60 199.775 6.153 4.61 2.35 39.63 649.84 670.34 81.07 64.5 2.52589 290 295 298 300 305 290.2 758.49 366.42 232.69528 1.56 47.149 2.49 212.63 55.50 473.65055 630 640 650 660 670 638.46 457.76690 1.61 2.09 270.37 352.19876 2.01699 2.59 57.14 75.82 250.98 7. 47712 3.8303 3.net 18Appendix_01 ITALICAS.295 3.7 2252.76 1443.5 672.49276 3.96 925.1 424.4 2189.49 1186. http://librosysolucionarios.0 1205.8901 3.7 2440. Fuente: Kenneth Wark.qxd 935 7/12/11 14:26:04 .7677 3.3 2127.00 1300 1320 1340 1360 1380 1395.046 3.9 1830.3 1823.46120 3.7354 3.835 3.022 2.0 506.52364 3.153 7.13 1168.51 1708.46 878.44 1563.10 1095.50 974.864 3.44516 3.30959 3.17 601. 1983.6 1630.435 3.9474 Pr u kJ/kg vr 791.29160 3.76 12.7994 1500 1520 1540 1560 1580 1635.48 1373.77 1150.526 8.25510 1600 1757.60 1467.36200 3.5979 3.6 2377.53879 Nota: Las propiedades Pr (presión relativa) y vr (volumen específico relativo) son cantidades adimensionales utilizadas en el análisis de procesos isentrópicos y no deben confundirse con las propiedades de presión y volumen específico.6684 3.301 6.5 750.8 310.23 1684.56867 3.4 986.63 1611.555 2. Thermodynamics.50829 2050 2100 2150 2200 2250 2314.27345 3.32724 3.52 1131.6 1161 1335.854 6. Nueva York.95 8.30 5. 785-786.8 5.97 1660.1 1310 1475 1655 1852 2068 1487.37901 3.012 1.919 8. McGraw-Hill.42 1539.43 1260.51 1587. 1948.6 1678.24 1392.175 2.9 1582. Gas Tables.8 710. Tabla A-5.8 1775.761 4.804 834.4 2303 2559 2837 3138 3464 1726.49 1491. Nueva York.2 1298. H.58335 3.82 1733.355 5.5 478.94 1077.747 10. Publicada originalmente en J. John Wiley & Sons.2 1880. pp.574 s° kJ/kg · K 3.8605 3.26 11.9191 3.7023 3.337 3.7 1439.24 290.152 6. Keenan y J.569 6. Kaye.801 7.5 375.82 1040.55381 3.55 1372.949 4.41247 3.2 1534.468 3.1 1025 1941.79 450.1 568.994 3.34474 1640 1660 1680 1700 1750 1806.147 4.88 1058.1 1316.39586 3.7 3.6336 1400 1420 1440 1460 1480 1515.601 3.3 2065.780 9.90 1004.87 1242.8 1872.328 3.57 1620 1782.776 3.41 1223.2 1022.9 537.99 1279.96 5.9 636.9 352.72 1354.247 9.65 7.23638 11.97 1419.3 2.6 1855.275 10.44 330.356 2.3 399.3 2503.2 2566. cuarta edición.4 1921.8 1113.42892 1800 1850 1900 1950 2000 2003.935 APÉNDICE 1 TABLA A-17 Propiedades de gas ideal del aire (conclusión) T K h kJ/kg Pr u kJ/kg vr s° kJ/kg · K T K h kJ/kg 1260 1280 1348. 990 220.914 900 910 920 930 940 26.574 12.450 212.469 15.883 20.558 7.932 12.786 9.757 17.574 9.784 15.792 208.168 222.478 7.190 187.640 11.489 214.301 219.188 0 182.398 15.844 21.830 218.471 10.895 8.306 9.662 16.658 24.975 7.424 206.328 21.772 12.413 215.991 20.141 8.723 9.599 16.647 225.770 4. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-18 Propiedades de gas ideal del nitrógeno.848 11.581 14.995 197.936 TABLAS DE PROPIEDADES.524 17.907 221.224 18.356 209.027 24.262 11.423 10.476 29.603 20.230 13.683 6.292 25.189 202.528 211. N2 _ _ T h u K kJ/kmol kJ/kmol _ s° kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 0 220 230 240 250 0 6.863 800 810 820 830 840 23.529 21.229 6.122 20.075 19.962 17.890 27.979 5.459 18.266 0 4.638 193.671 13.153 200.669 5.033 850 860 870 880 890 25.695 18.999 210.180 186.792 13.568 18.685 19.562 4.085 23.370 600 610 620 630 640 17.149 22.216 207.353 225.225 12.912 21.297 13.398 227.931 19.532 27.518 12.756 217.180 10.695 191.220 21.014 9.328 700 710 720 730 740 20.314 300 310 320 330 340 8.292 17.277 206.928 26.709 220.954 215.105 13.811 8.888 6.913 16.447 450 460 470 480 490 13.822 223.571 226.889 219.563 17.285 9.460 22.560 214.624 218.707 11.794 201.839 14.523 8.018 260 270 280 290 298 7.501 28.826 29.562 223.938 185.686 216.061 191.358 208.597 9.104 196.684 222.407 19.337 14.866 216.314 8.173 196.733 8.062 11.380 19.472 350 360 370 380 390 10.210 27.061 17.086 21.468 18.997 10.523 204.172 15.139 12.499 202.988 14.288 500 510 520 530 540 14.610 25.363 9.151 29.389 226.512 400 410 420 430 440 11.644 19.604 20.071 200.391 6.064 227.502 650 660 670 680 690 19.514 188.876 15.927 224.370 16.270 7.974 17.011 13.114 14.461 209.298 221.923 12.849 8.630 207.864 18.728 http://librosysolucionarios.437 6.687 7.492 11.460 15.331 750 760 770 780 790 22.194 223.562 950 960 970 980 990 28.541 214.qxd 936 7/12/11 14:26:04 .682 192.066 212.363 16.170 204.141 16.892 14.854 28.342 24.459 195.803 20.673 190.192 217.064 16.564 213.059 218.396 5.021 6.362 224.803 205.943 9.178 19.714 24.853 7.766 10.701 226.572 199.net 18Appendix_01 ITALICAS.693 13.645 6.067 222.210 203.055 11.813 6.614 189.166 18.002 225.055 213.347 7.234 15.635 10.008 15.049 211.047 550 560 570 580 590 16.562 194.763 11.728 227.399 13.113 220.639 183.248 26.432 8.772 23.604 5.794 198. 706 229.867 238.241 264.071 239.073 47.762 21. 1971. 787-798.168 49.171 94.361 29.777 247.580 259.790 60.793 267.760 35.973 233.768 242.376 238.227 42.747 2900 2950 3000 3050 3100 97.507 41.075 41. pp.668 268.488 90.407 103.685 43.075 47.170 266.163 262.799 232. Nueva York.301 2400 2450 2500 2550 2600 79.869 34.014 95.qxd 937 7/12/11 14:26:04 .304 22.571 51.988 45.424 244.328 92.365 249.280 24.324 245.784 31.806 38.938 57.213 262.607 251.613 65.958 254.990 3150 3200 3250 106.306 70.763 Fuente: Las tablas A-18 a A-25 fueron adaptadas de Kenneth Wark.589 248.902 263.363 59.129 30.166 246.591 1760 1780 1800 1820 1840 56.601 35.057 228.464 77.073 260.973 230.578 255.605 44.734 72.226 72.101 32.412 256.223 235.331 28.919 31.net 18Appendix_01 ITALICAS.705 99.181 49.686 53.423 45.845 234.798 248.104 24.099 54.779 62.780 25.786 26.242 251.195 248.685 243.488 26.580 246.676 77.650 59.470 49.594 42.771 48.393 37.981 84.810 66.502 250.651 58.133 35.504 61.593 75.014 33.366 60.199 231.543 34.585 2650 2700 2750 2800 2850 88. NSRDS-NBS-37.964 32.782 82.291 231.404 268.260 105.417 47.601 269.874 1200 1220 1240 1260 1280 36.539 42.682 46.129 38.302 1960 1980 2000 2050 2100 63.049 246.442 32.391 232.814 86.324 44.137 243. 1983.033 258.455 67. 4a.567 50.969 252.980 52.220 61.398 30.377 31.782 228.766 236. http://librosysolucionarios.853 41.973 46.819 28.896 245.231 43.090 64.351 53.878 2150 2200 2250 2300 2350 70.028 76.441 236.777 37.320 81.799 261.288 23.197 36.799 27.295 44.308 27.496 52.430 36.282 25.353 237.341 265.859 66.128 250.873 45.139 42.227 257.028 244.807 55.344 229.396 247.378 30.149 56.556 101.807 39.092 34.673 235..332 260.228 242.149 82.027 257.553 57.195 63.549 1860 1880 1900 1920 1940 59.375 239.726 1300 1320 1340 1360 1380 40.936 62.577 264.749 55.979 1100 1120 1140 1160 1180 33.426 34.516 39.170 40.538 266.865 240.815 22.902 79.654 44.858 253.831 237.810 1400 1420 1440 1460 1480 43.665 36.452 38.275 51. ed.224 83.957 251.489 33.830 110.937 APÉNDICE 1 TABLA A-18 Propiedades de gas ideal del nitrógeno. N2 (conclusión) _ _ _ T h u s° K kJ/kmol kJ/kmol kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 1000 1020 1040 1060 1080 30.381 64.524 249.748 250.115 73.186 269.965 40.227 56.827 241.344 38. Thermodynamics.972 108.732 241.856 75.115 234.350 240.612 68.007 1700 1720 1740 54.915 29.884 39.690 80.627 48.880 69.268 37.512 1500 1520 1540 1560 1580 47.464 244.040 73.895 1600 1620 1640 1660 1680 50. McGraw-Hill.795 23. Thermochemical Tables. Publicadas originalmente en JANAF. 997 900 910 920 930 940 27.822 9.358 231.656 800 810 820 830 840 24.272 28.140 14.664 6.955 216.112 208.net 18Appendix_01 ITALICAS.809 241.618 12.116 228.166 209.171 197.033 650 660 670 680 690 19.929 18.146 224.518 7.222 213.201 350 360 370 380 390 10.262 225.126 18.002 750 760 770 780 790 22.206 221.513 23.384 8.845 22.893 235.203 201.537 25.770 15.940 13.666 19.842 11.345 30.827 232.870 20.325 9.963 850 860 870 880 890 26.854 14.264 238.524 20.544 19.861 25.199 25.203 240.405 5.559 26.303 7.984 7.918 228.644 237.417 13.938 TABLAS DE PROPIEDADES.696 199.109 11.400 227.877 7.250 18.364 17.120 http://librosysolucionarios.291 232.899 27.409 7.306 20.443 8.589 221.185 237.111 17.491 239.453 6.382 18.877 17.850 24.012 12.150 19.411 242.462 450 460 470 480 490 13.445 20.091 234.580 240.971 17.660 239.232 12.748 233.055 237.242 27.935 10.998 12.241 215.043 9.071 11.533 220.809 11.405 230.823 240.041 21.694 6.280 22.151 14.765 210.219 12.544 22.810 236.128 203.842 14.575 4.864 238.346 226.859 16.242 6.386 217.706 20.514 21.928 28.711 12.895 19.383 14.027 202.051 239.020 208.409 222.649 234.314 12.925 20.603 8.218 26.613 5.904 700 710 720 730 740 21.197 0 196.858 8.657 13.566 7.920 230.923 8.616 28.932 229.708 16.703 223.654 16.754 22.052 242.357 231.160 10.584 19.960 29.528 234.184 21.614 10.844 23.652 29.885 300 310 320 330 340 8.768 242.430 229.016 218.782 4.213 206.604 211.618 233.439 500 510 520 530 540 14.395 15.387 400 410 420 430 440 11.989 5.275 0 4.423 212.186 16.150 8.733 7.177 207.682 5.218 205.692 31.525 13.213 10.736 9.898 226.708 225.872 18. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-19 Propiedades de gas ideal del oxígeno.607 16.178 13.967 21.916 6.960 235.877 227.032 6.808 950 960 970 980 990 29.230 236.765 214.301 11.885 600 610 620 630 640 17.626 14.264 213.408 19.572 18.364 15.191 204.510 215.qxd 938 7/12/11 14:26:05 .429 260 270 280 290 298 7.228 13.611 15.859 17.871 15.323 550 560 570 580 590 16.082 15.609 11.030 9.487 9.822 6.197 20.689 242.523 24.290 17. O2 _ _ T h u K kJ/kmol kJ/kmol _ s° kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 0 220 230 240 250 0 6.676 219.228 21.765 11.511 10.510 15.090 205.022 10.999 30.812 222.342 218.949 8.620 9.576 224.460 9.017 22.461 198.178 23.107 16.404 6.953 241.637 18.710 9.177 22.467 12.326 219.338 16. 804 286.113 265.881 69.132 2900 2950 3000 3050 3100 102.989 287.164 244.060 285.018 29.808 70.227 40.942 281.192 58.454 248.449 252.404 254.979 278.081 248.224 36.093 43.374 67.939 APÉNDICE 1 TABLA A-19 Propiedades de gas ideal del oxígeno.861 264.601 88.513 246.454 255.374 47.987 75.734 25.616 63.136 42.546 77.424 277.208 267.394 58.809 116.704 271.713 1700 1720 1740 56.821 37.952 38.701 265.772 71.389 32.243 55.588 270.307 1860 1880 1900 1920 1940 62.986 46.294 26.831 48.698 249.520 39.690 60.258 81.435 3150 3200 3250 112.214 243.944 260.827 86.868 65.906 250.734 48.193 61.912 39.594 41.024 50.697 57.625 276.057 89.net 18Appendix_01 ITALICAS.118 61.278 273.793 104.397 79.116 64.753 43.891 274.573 75.497 251.852 98.198 44.242 261.009 283.670 249.271 67.419 85.334 32.127 67.916 94.614 http://librosysolucionarios.379 27.005 263.112 87.194 23.033 42.844 245.923 246.756 51.333 260.102 47.475 256.079 251.780 108.870 2650 2700 2750 2800 2850 92.339 275.978 257.682 80.899 35.785 106. O2 (conclusión) _ _ _ T h u s° K kJ/kmol kJ/kmol kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 1000 1020 1040 1060 1080 31.568 30.475 44.151 47.256 255.658 40.490 52.402 259.275 268.171 1760 1780 1800 1820 1840 58.450 258.925 266.219 280.568 263.728 284.023 37.742 66.387 37.789 33.690 262.447 39.891 33.118 30.224 31.923 31.112 279.677 25.883 72.826 100.738 1500 1520 1540 1560 1580 49.471 244.607 24.818 247.162 39.433 73.292 50.405 45.004 90.283 264.088 32.802 69.877 40.115 267.219 64.825 45.325 253.129 35.371 61.008 34.837 83.517 43.696 54.075 23.809 1400 1420 1440 1460 1480 45.753 26.490 34.880 59.253 52.956 63.799 41.355 286.655 269.219 1960 1980 2000 2050 2100 66.434 55.567 35.357 1600 1620 1640 1660 1680 52.314 37.316 81.326 266.136 273.932 2150 2200 2250 2300 2350 73.784 78.836 27.469 29.319 48.521 1100 1120 1140 1160 1180 34.654 282.370 41.504 1300 1320 1340 1360 1380 42.776 253.778 110.648 46.399 272.174 85.620 47.203 89.727 54.624 60.891 268.669 262.965 258.505 1200 1220 1240 1260 1280 38.490 265.484 77.312 28.qxd 939 7/12/11 14:26:05 .968 256.207 277.365 64.606 36.485 280.928 259.571 263.172 55.652 57.791 261.653 252.904 49.868 254.088 257.881 96.078 50.866 44.795 114.247 44.561 34.668 50.722 267.048 283.399 285.778 32.142 24.665 51.961 53.474 2400 2450 2500 2550 2600 83.692 36. 948 222.728 265.199 243.548 0 202.068 9.968 500 510 520 530 540 17.700 236.983 244.670 http://librosysolucionarios.742 12.869 243.920 207.194 231.444 12.685 42.337 600 610 620 630 640 22.031 29.588 29.212 33.622 29.311 259.826 8.625 33.296 35.080 233.959 26.870 21.894 247.663 251.134 22.537 33.405 950 960 970 980 990 40.405 37.004 233.526 7.125 28.800 13.158 230.160 25.665 23.226 32.570 10.485 13.393 23.126 18.877 550 560 570 580 590 19.995 266.602 242.122 224.407 20.371 262.230 800 810 820 830 840 32.821 36.280 22.394 26.902 239.164 261.070 40.814 235.063 9.762 400 410 420 430 440 13.916 850 860 870 880 890 34.622 28.552 12.915 215.709 24.559 264.755 253.351 217.789 241.952 300 310 320 330 340 9.471 18.135 30.252 229.439 350 360 370 380 390 11.048 258.718 219.601 6.053 11.831 220.062 211.369 30.007 267.282 260 270 280 290 298 7.807 10.694 33.146 264.138 26.091 12.524 246.285 5.748 12.145 41.939 7.683 18.575 237.054 10.464 205.351 11.527 25.817 6.694 700 710 720 730 740 27.372 15.685 650 660 670 680 690 24.629 20.251 25.337 21.607 41.179 32.270 19. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-20 Propiedades de gas ideal del dióxido de carbono.818 31.392 9.171 32.267 257.758 245.507 249.772 5.253 14.674 25.979 8.622 14.net 18Appendix_01 ITALICAS.131 16.515 16.124 21.972 250.000 39.376 212.576 19.934 450 460 470 480 490 15.046 10.097 254.787 14.335 8.719 22.522 22.885 208.660 213.551 261.135 239.483 15.182 750 760 770 780 790 29.940 TABLAS DE PROPIEDADES.714 11.966 204.351 16.484 20.817 24.242 24.231 23.233 249.829 27.807 15.431 9.230 7.938 7.521 13.962 240.628 15.291 17.682 259.706 28.439 238.916 16.081 33.945 20.044 223.770 262.752 9.372 13.368 252.791 17.186 10.305 21.697 9.648 26.960 8.651 6.146 216.029 19.qxd 940 7/12/11 14:26:05 .347 36.078 20.232 11.754 23.065 252.631 19.935 38.439 8.032 247.119 268.751 16.672 20.922 30.885 14.678 18.408 258.717 210.476 260.773 248.364 5.304 265.378 10.148 12.250 227.719 263.131 213.773 35.452 256.268 31.144 232.121 28.566 268.091 6.535 29.280 7.996 234.669 25.644 31.444 267.369 6.959 6.206 14.292 900 910 920 930 940 37.258 228.125 27.190 17.730 34.225 226.393 225.534 218.026 5.876 27. CO2 _ _ _ T h u s° K kJ/kmol kJ/kmol kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 0 220 230 240 250 0 6.467 39.110 256.154 31.787 255.076 18.627 0 4.117 254. 791 89.743 290.456 131.586 286.845 305.859 44.445 275.238 38.620 62.621 55.185 86.217 302.648 97.qxd 941 7/12/11 14:26:05 .962 78.072 298.963 64.381 43.271 66.912 102.031 81.035 122.124 338.884 303.198 1100 1120 1140 1160 1180 48.592 67.283 139.011 1400 1420 1440 1460 1480 65.713 49.769 43.632 297.898 134.768 47.067 304.996 80.411 295.695 319.439 287.604 309.804 103.084 335.822 145.888 292.813 62.586 68.606 288.975 333.361 1860 1880 1900 1920 1940 92.174 269.219 131.533 143.116 48.293 271.212 326.023 94.109 339.106 288.606 100.374 1200 1220 1240 1260 1280 53.246 73.238 281.593 94.215 270.941 APÉNDICE 1 TABLA A-20 Propiedades de gas ideal del dióxido de carbono.721 69.114 336.630 292.356 298.609 60.089 150.962 1960 1980 2000 2050 2100 98.898 112.303 80.995 97.307 280.702 295.913 274.400 273.427 67.108 57.105 83.576 174.091 92.653 65.369 50.631 54.552 313.306 37.123 79.341 168.929 77.430 277.210 310.856 84.748 66.849 110.799 46.354 272.847 284.656 52.835 106.500 121.444 276.984 119.117 162.897 301.420 87.484 51.144 84.864 82.404 307.848 54.901 296. CO2 (conclusión) _ _ _ T h u s° T K kJ/kmol kJ/kmol kJ/kmol · K K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 1000 1020 1040 1060 1080 42.394 93.691 50.739 297.528 129.542 291.401 99.197 76.290 134.166 115.832 320.992 308.764 299.544 304.806 90.934 289.787 72.713 149.126 1700 1720 1740 82.112 40.939 115.009 159.620 146.643 283.751 307.258 49.158 282.988 316.006 41.160 1300 1320 1340 1360 1380 59.722 285.812 73.741 64.197 107.863 3150 3200 3250 171.590 76.944 78.037 334.277 99.612 88.613 61.566 322.957 42.834 45.606 59.455 35.871 44.911 53.672 51.549 328.670 63.684 329.153 34.057 41.078 72.808 324.801 337.793 95.066 282.482 300.504 113.226 165.486 81.953 46.231 68.781 2900 2950 3000 3050 3100 156.589 137.114 292.222 1500 1520 1540 1560 1580 71.668 66.695 177.808 152.051 47.283 2150 2200 2250 2300 2350 109.385 148.043 85.122 306.196 71.589 314.977 56.430 1760 1780 1800 1820 1840 86.487 306.449 105.356 317.000 91.403 278.net 18Appendix_01 ITALICAS.161 2650 2700 2750 2800 2850 140.609 57.868 75.417 74.896 1600 1620 1640 1660 1680 76.333 2400 2450 2500 2550 2600 125.724 39.800 330.666 61.177 300.396 327.840 74.069 http://librosysolucionarios.701 312.982 142.681 331.742 70.522 60.378 36.244 58.767 58.026 325.172 123.368 137.543 302.614 56.654 294.302 321.602 52.908 118.849 126.152 128. 052 222.070 20.217 203.193 17.317 231. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-21 Propiedades de gas ideal del monóxido de carbono.412 13.197 15.768 26.446 25.003 17.736 13.943 14.692 350 360 370 380 390 10.587 9.379 18.545 21.719 213.641 220.375 19.175 217.190 193.693 950 960 970 980 990 28.500 201.693 30.228 209.549 208.205 219.140 227.898 15.889 6.708 219.703 29.695 220.339 228.399 16.649 217.942 TABLAS DE PROPIEDADES.401 215.957 231.842 204.068 20.162 227.953 223.603 200.429 17.378 13.600 14.221 192.413 233.310 213.740 8.645 6.258 22.789 222.504 212.735 197.040 203.229 6.752 234.141 19.800 10.289 13.315 21.899 8.391 6.351 7.164 24.411 600 610 620 630 640 17.758 20.797 10.482 229.915 18.188 0 188.961 12.593 210.583 19.593 500 510 520 530 540 14.204 218.252 208.014 10.611 17.106 229.844 24.090 11.298 21.302 9.125 206.449 19.443 10.072 233.116 13.874 11.554 194.115 225.097 16.099 19.117 850 860 870 880 890 25.833 224.379 550 560 570 580 590 16.890 214.362 29.597 9.002 21.743 11.890 23.617 18.415 26.803 25.622 12.559 227.024 20.558 7.858 19.227 230.314 20.622 205.091 26.512 218.473 10.723 9.396 223.880 211.392 27.592 222.505 300 310 320 330 340 8.947 226.140 8.833 12.850 207.357 226.980 191.849 8.265 224.124 17.341 229.678 199.529 8.558 15.740 18.020 6.669 5.414 14.396 5.181 10.527 18.573 22.127 221.058 11.qxd 942 7/12/11 14:26:05 .762 400 410 420 430 440 11.723 16.187 14.856 230.929 800 810 820 830 840 23.181 12.793 232.533 225.437 6.307 11.765 11.524 11.028 232.713 196.232 12.526 12.483 24.805 21.255 16.952 228.689 7.854 7.724 450 460 470 480 490 13.812 6.005 14.221 18.562 4.022 16.208 23.870 15.319 8.708 14.460 215.654 195.656 221.951 9.644 11.843 13.051 21.375 9.115 216.179 260 270 280 290 298 7.723 198.826 20.480 7.163 206.033 29.271 7.306 9.665 17.543 650 660 670 680 690 19.979 5.674 232.821 8.371 700 710 720 730 740 20.014 9.902 18.727 233.962 14.266 0 4.628 21.938 12.432 8.062 197.771 4.020 900 910 920 930 940 27.497 15.683 6.383 750 760 770 780 790 22.957 225.690 21.066 27.088 http://librosysolucionarios.108 202.046 28.328 15.559 230.307 212.488 16.243 210.526 16.099 15.658 10.975 7.066 13.604 5.719 28.572 216.net 18Appendix_01 ITALICAS. CO _ _ _ T h u s° K kJ/kmol kJ/kmol kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 0 220 230 240 250 0 6.683 189.701 17. 794 62.434 33.344 35.385 246.382 39.864 72.293 38.755 267.750 38.844 244.715 80.688 74.370 1300 1320 1340 1360 1380 40.225 43.665 37.072 61.688 32.584 36.612 83.044 47.441 45.809 57.575 26.054 35.230 91.927 250.066 71.039 40.961 64.613 43.net 18Appendix_01 ITALICAS.910 59.355 31.988 54.088 26.331 253.426 28.684 65.383 60.046 35.609 238.667 111.497 1200 1220 1240 1260 1280 37.065 25.226 262.534 41.377 35.408 67.572 252.602 1600 1620 1640 1660 1680 51.049 234.366 244.124 36.361 256.837 39.628 70.914 276.253 266.945 268.516 63.901 252.508 245.147 2650 2700 2750 2800 2850 89.309 29.194 255.329 2900 2950 3000 3050 3100 98.053 51.122 257.367 32.600 259.725 30.678 29.222 58.730 1700 1720 1740 54.640 261.930 94.906 64.267 78.007 44.210 104.537 87.201 240.582 3150 3200 3250 107.249 272.345 78.733 36.033 251.763 52.919 42.743 257.482 62.485 268.323 56.766 265.728 236.876 247.169 253.868 258.202 1500 1520 1540 1560 1580 47.383 75.qxd 943 7/12/11 14:26:05 .095 37.110 46.207 248.108 255.222 48.226 41.236 242.997 46.552 47.756 57.637 28.470 251.839 2400 2450 2500 2550 2600 80.825 77.592 251.407 239.396 55.692 264.217 238.118 27.695 250.236 258.587 1100 1120 1140 1160 1180 33.989 1860 1880 1900 1920 1940 60.992 1760 1780 1800 1820 1840 56.817 239.494 http://librosysolucionarios.335 65.398 254.065 262.312 248.516 76.991 254.852 83.778 31.880 245.360 247.836 243.388 2150 2200 2250 2300 2350 70.123 42.495 100.364 236.635 50.557 25.251 30.905 269.751 253.041 23.778 44.123 274.240 249.976 256.238 44.707 45.326 275.306 31.073 105.544 24.534 81.780 38.663 241.060 61.480 1400 1420 1440 1460 1480 44.077 92.784 96.778 249.221 48.943 271.886 45.466 39.780 1960 1980 2000 2050 2100 63.596 270.540 23.224 69.504 72.015 81.939 74.900 33.584 257.473 58.023 41.316 243.602 237.629 42.692 85.191 58.408 46.884 273.508 274.128 241.928 49.020 31.513 275.844 27.164 272.352 102.029 22.943 APÉNDICE 1 TABLA A-21 Propiedades de gas ideal del monóxido de carbono.971 34.154 39.184 53.061 84.012 266.639 67.780 50.673 43.887 263.197 68.813 32.351 61.895 37.802 109.494 260.702 34.041 22.665 48.179 51.357 33.517 48.686 242.797 255.079 235. CO (conclusión) _ _ _ T h u s° T K kJ/kmol kJ/kmol kJ/kmol · K K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 1000 1020 1040 1060 1080 30.474 41.889 246.285 270.406 24.421 235.609 55.178 52.472 53. 891 162.279 54.989 6.863 154.607 188.429 56.154 17.144 196.786 32.358 97.554 60.400 40.657 7.839 160.152 76.724 380 400 420 440 460 10.410 178.277 163.976 14.580 32.682 2800 2850 2900 2950 3000 89.523 203.383 77.412 5.401 70.798 58.621 134.888 143.838 91.667 106.622 51.941 62.106 28.234 200.560 170.368 86.944 TABLAS DE PROPIEDADES.114 2550 2600 2650 2700 2750 80.632 182.558 84.510 3050 3100 3150 3200 3250 99.490 24.717 22.995 180.028 35.171 13.209 5.280 9.530 26.708 50.646 38.754 132.671 93.375 18.159 193.403 196.391 203.945 8.765 http://librosysolucionarios.618 35.061 79.652 181.990 30.440 6.520 152.539 198.593 176.719 128. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-22 Propiedades de gas ideal del hidrógeno.889 172.968 2050 2100 2150 2200 2250 63.268 130.235 19.451 12.775 1440 1480 1520 1560 1600 42.652 175.468 8.181 205.684 8.698 173.133 13.793 104.995 204.612 139.716 54.765 129.962 57.449 169.107 17.747 27.607 164. H2 _ _ _ T h u s° K kJ/kmol kJ/kmol kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 0 260 270 280 290 0 7.628 146.187 1840 1880 1920 1960 2000 55.680 10.311 58.594 13.979 190.100 9.669 16.604 78.687 174.148 189.179 7.645 156.359 25.039 1640 1680 1720 1760 1800 49.821 15.737 65.300 168.636 171.574 130.835 31.687 177.291 179.091 45.190 186.027 28.668 36.680 42.529 141.037 51.945 150.186 88.074 47.843 11.771 185.463 186.955 29.098 19.440 2300 2350 2400 2450 2500 71.512 95.847 66.773 10.976 69.502 37.668 60.284 167.904 187.608 75.796 191.233 0 5.935 16.611 11.645 39.008 59.384 25.654 37.069 55.157 202.755 82.705 43.335 63.002 40.839 73.545 73.775 148.683 47.960 52.592 205.617 5.885 201.807 21.268 200.384 46.192 27.518 8.907 199.119 64.065 100.175 193.746 33.749 39.355 137.106 140.551 26.921 194.923 159.522 9.153 179.947 53.630 20.432 145.936 9.584 68.net 18Appendix_01 ITALICAS.303 50.080 46.426 12.373 189.764 14.558 67.926 102.966 20.193 10.168 78.428 183.386 48.822 0 126.370 7.453 19.853 7.636 127.291 144.601 23.378 136.808 44.831 72.988 23.297 480 500 520 560 600 13.263 41.262 5.350 14.125 840 880 920 960 1000 24.884 166.211 66.328 157.707 75.735 44.820 298 300 320 340 360 8.027 6.973 184.364 31.669 195.802 34.010 12.527 202.948 29.qxd 944 7/12/11 14:26:06 .598 192.328 70.713 34.031 61.837 197.663 41.262 21.229 198.778 1240 1280 1320 1360 1400 36.575 1040 1080 1120 1160 1200 30.385 640 680 720 760 800 18.208 183.100 8. 300 25.943 26.795 210.896 28.561 18.628 7.075 211.651 225.123 225.247 34.741 27.419 216.959 19.303 14.601 18.466 6.232 8.136 193.755 206.639 10.720 222.856 15.339 20.098 192.032 31.399 186.998 9.135 12.662 24.720 650 660 670 680 690 22.527 218.122 214.970 23.980 25.245 12.470 223.807 750 760 770 780 790 25.215 221.030 10.144 700 710 720 730 740 24.920 213.347 231.715 24.139 185.257 16.699 14.345 24.678 20.265 26.705 850 860 870 880 890 29.693 224.255 9.510 19.436 24.982 205.207 400 410 420 430 440 13.840 25.174 224.012 196.961 8.112 207.765 21.081 196.725 7. H2O _ _ _ T h u s° K kJ/kmol kJ/kmol kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 0 220 230 240 250 0 7.631 9.402 20.841 34.428 15.487 188.517 226.521 200.978 215.057 226.130 21.228 32.071 300 310 320 330 340 9.202 229.716 6.088 24.621 228.268 18.497 204.499 230.112 17.992 12.230 22.482 13.707 350 360 370 380 390 11.715 5.356 13.472 7.779 23.828 32.831 600 610 620 630 640 20.477 11.673 199.791 188.039 14.734 203.472 25.968 7.331 12.627 8.707 215.054 181.475 209.541 212.763 229.955 800 810 820 830 840 27.399 17.125 195.029 226.592 450 460 470 480 490 15.975 16.714 16.549 21.966 10.653 35.402 23.320 950 960 970 980 990 33.139 900 910 920 930 940 31.652 11.134 209.826 17.742 8.672 29.976 217.189 220.529 214.062 29.828 17.294 0 5.965 6.610 219.413 15.070 550 560 570 580 590 18.924 231.142 219.181 17.771 194.388 14.339 11.215 0 178.028 14.904 6.869 12.576 180.977 26.126 16.940 13.444 218.032 33.240 30.247 204.160 201.471 182.639 20.302 10.284 28.014 8.767 232.314 7.693 15.854 19.513 9.637 230.973 227.358 26.799 208.813 11.688 17.043 14.350 201.495 21.318 19.218 25.978 8.039 20.616 187.920 197.qxd 945 7/12/11 14:26:06 .440 211.285 260 270 280 290 298 8.219 7.425 184.668 220.211 13.061 35.889 18.245 21.net 18Appendix_01 ITALICAS.080 15.928 190.551 10.603 11.855 22.125 27.976 11.429 22.702 212.777 16.090 23.413 207.941 221.464 24.671 12.148 19.945 APÉNDICE 1 TABLA A-23 Propiedades de gas ideal del vapor de agua.741 20.075 198.961 9.221 222.913 27.856 216.240 230.600 22.734 10.875 500 510 520 530 540 16.162 22.342 23.454 21.717 223.321 228.862 15.588 26.290 10.635 31.579 14.184 http://librosysolucionarios.295 7.296 9.466 5.403 202.534 17.846 30.030 191.597 18.426 227.629 33.672 13. 071 40.806 1760 1780 1800 1820 1840 70.330 92.915 246.304 47.470 40.390 285.462 281.151 258.780 42.969 262.223 27.888 60.273 287.243 232.084 47.137 47.466 43.110 238.546 37.513 73.978 1400 1420 1440 1460 1480 53.098 275.792 45.436 261.352 238.441 280.547 58.qxd 946 7/12/11 14:26:06 .846 72.859 239.656 274. H2O (conclusión) _ _ _ T h u s° T K kJ/kmol kJ/kmol kJ/kmol · K K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 1000 1020 1040 1060 1080 35.273 55.333 241.415 234.925 31.732 39.868 48.946 TABLAS DE PROPIEDADES.735 64.267 55.543 249.457 150.820 2400 2450 2500 2550 2600 103.455 54.305 252.923 41.039 51.960 243.952 94.500 270.868 111.593 85.841 52.600 1860 1880 1900 1920 1940 75.450 251.567 69.213 40.527 79.597 233.655 250.940 95.838 61.693 252.074 251.450 257. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-23 Propiedades de gas ideal del vapor de agua.256 279.999 58.692 116.535 71.128 57.912 2650 2700 2750 2800 2850 116.076 81.912 34.482 243.568 28.756 247.827 36.458 120.198 56.308 268.573 82.051 141.511 77.380 39.648 147.711 42.262 259.709 37.497 263.275 263.022 257.059 264.584 237.748 63.250 288.194 288.083 256.111 65.895 29.675 65.999 289.873 2900 2950 3000 3050 3100 130.540 60.588 101.542 38.241 247.290 255.517 78.223 235.020 235.259 65.884 290.057 241.642 43.567 30.877 244.226 43.301 32.380 45.270 240.565 114.553 85.717 133.112 35.364 92.453 125.445 50.679 271.199 100.264 139.062 41.589 3150 3200 3250 144.959 111.703 255.403 35.022 1200 1220 1240 1260 1280 44.838 267.240 51.183 1960 1980 2000 2050 2100 80.357 1100 1120 1140 1160 1180 40.997 33.156 87.111 254.773 242.111 70.611 32.429 1600 1620 1640 1660 1680 62.582 2150 2200 2250 2300 2350 90.991 119.528 46.081 1300 1320 1340 1360 1380 48.917 104.183 108.811 260.646 253.756 http://librosysolucionarios.649 76.506 55.717 122.286 277.185 249.269 99.351 54.612 51.464 282.338 286.407 1500 1520 1540 1560 1580 57.321 113.958 97.072 284.198 127.513 254.709 64.000 38.708 259.851 123.855 79.375 59.811 88.486 136.201 276.523 72.898 261.571 265.564 63.605 108.723 57.942 59.902 56.707 50.542 264.453 283.564 245.507 74.509 30.846 106.614 49.521 52.272 118.net 18Appendix_01 ITALICAS.989 44.562 98.082 90.880 61.042 60.454 74.207 258.506 76.102 1700 1720 1740 67.555 81.228 28.243 245.022 47.411 260.882 36.354 278.434 38.807 49.256 46.273 83.643 66.965 68.839 272.720 62.589 68.508 106.895 248.698 236.550 53.301 269. 945 211.425 65.592 210.177 69.429 0 6.578 117.539 82.592 82.646 45.740 245.088 250.373 4.358 66.820 33.801 80.400 40.987 54.150 34. OH _ _ T h u K kJ/kmol kJ/kmol _ s° kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 0 298 300 500 1000 1500 1600 1700 1800 1900 2000 2050 2100 2150 2200 2250 2300 2350 0 183.852 6.831 Propiedades de gas ideal del hidroxilo.093 260.193 32.279 210.301 51.234 36.687 66.024 21.506 234.962 65.811 49.556 44.148 208.447 34.824 73.196 59.932 71.143 196.606 240.089 59.187 252.749 11.757 68.685 25.339 55.338 247.851 38.067 201.979 54.162 69.095 96.679 20.746 41.806 89.505 62.879 2400 2450 2500 2550 2600 2650 2700 2750 2800 2850 2900 2950 3000 3100 3200 3300 3400 3500 77.436 29.061 58.241 60.013 42.673 79.947 APÉNDICE 1 TABLA A-24 Propiedades de gas ideal del oxígeno monoatómico.482 42.882 209.431 59.779 198.706 56.244 15.434 24.235 261.961 36.940 31.088 186.763 102.566 32.482 39.720 71.312 57.189 85.590 37.220 37.388 84.055 38.968 50.672 238.769 48.181 30.323 47.936 52.832 255.123 43.799 251.642 236.183 23.783 206.518 208.079 172.qxd 947 7/12/11 14:26:07 .697 http://librosysolucionarios.708 46.236 0 6.772 208.932 30.941 200.488 197.332 35.570 70.064 56.649 202.317 38.588 204.462 75.046 49.021 55.186 254.186 27.186 62.net 18Appendix_01 ITALICAS.619 69.332 62.314 TABLA A-25 0 9.999 207.592 212.641 203.152 58.547 246.694 73.530 254.712 257.266 95.398 19.894 51.135 201.418 85.932 205.806 61.955 219.892 11.935 26.240 209.728 47.572 63.145 109.428 68.212 248.983 72.927 98.151 202.286 61.624 232.944 161.378 63.628 249.713 32.751 198.575 36.917 244.811 28.499 252.283 43.931 22.709 6.622 91.045 204.119 203.015 78.442 93.116 247.601 206.040 13.594 183.062 29.832 204.188 9.453 242.809 33.919 259.220 212.094 256.075 34.688 30.362 205.196 206.852 0 4.221 243.364 250.389 207.468 256.864 253.347 262.309 88.108 57.123 46.703 35. O _ _ _ T h u s° K kJ/kmol kJ/kmol kJ/kmol · K T K _ h kJ/kmol _ u kJ/kmol _ s° kJ/kmol · K 0 298 300 500 1000 1500 1600 1700 1800 1900 2000 2050 2100 2150 2200 2250 2300 2350 0 160.641 52.855 113.493 2400 2450 2500 2550 2600 2650 2700 2750 2800 2850 2900 2950 3000 3100 3200 3300 3400 3500 50.398 7.687 46.571 41.520 67.952 64.358 52.678 195.820 76.447 106.564 43.605 44.560 27.642 48.077 243.995 87.197 21.400 73. Dow Chemical Co.310 103.600 23.180 168.20 310.63 269.680 +52.610 0 +231.94 188.530 0 +472.520 291.70 126.79 205.930 126.360 16.790 137.948 TABLAS DE PROPIEDADES.85 69. y API Research Project 44.120 0 +203.190 136.qxd 948 7/12/11 14:26:07 .720 228.290 +34. Midland.83 229. función de Gibbs de formación y entropía a 25°C.820 +209. NBS Technical Note 270-3. 1 atm _ _ gf° hf° Sustancia Fórmula kJ/kmol kJ/kmol Acetileno Agua Alcohol etílico Alcohol etílico Alcohol metílico Alcohol metílico Amoniaco Benceno n-butano Carbón Dióxido de carbono n-dodecano Etano Etileno Hidrógeno Hidrógeno Hidroxilo Metano Monóxido de carbono Nitrógeno Nitrógeno n-octano n-octano Oxígeno Oxígeno Peróxido de hidrógeno Propano Propileno Vapor de agua C2H2(g) H2O(ᐉ) C2H5OH(g) C2H5OH(ᐉ) CH3OH(g) CH3OH(ᐉ) NH3(g) C6H6(g) C4H10(g) C(s) CO2(g) C12H26(g) C2H6(g) C2H4(g) H2(g) H(g) OH(g) CH4(g) CO(g) N2(g) N(g) C8H18(g) C8H18(ᐉ) O2(g) O(g) H2O2(g) C3H8(g) C3H6(g) H2O(g) +226.770 105. 1953.730 285.49 219.450 249.890 162.190 +82.16 197.410 241.310 277.670 238.68 114. http://librosysolucionarios.150 32.72 183.92 282.150 0 +455.660 15.830 235. Carnegie Press. 1971.65 191.12 5.280 0 +218.06 232.150 0 393.650 208.80 622.80 192.83 Fuente: De JANAF.61 153.91 266.950 0 +249.570 174.33 269.170 237. Thermochemical Tables.460 74.280 50.710 0 394.660 46.74 213.70 186.010 84.590 absoluta _ s° kJ/kmol · K 200.510 +16.530 +6. 1968.83 130.360 +50.850 +20.000 +39.70 239.04 161. MI.73 360.890 +68.000 166. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-26 Entalpía de formación.690 200.850 110..net 18Appendix_01 ITALICAS.490 +62.30 466.590 +129.59 160. Selected Values of Chemical Thermodynamic Properties. 660 10.600 44.050 19.500 1A 1 atm y 20°C.qxd 949 7/12/11 14:26:07 .000 44.310 141.790 — 0.043 32.150 32.4 2.77 1.100 47.32 2.05 2.200 42.78 0.3 kJ/kg Poder calorífico inferior.84 2.8nN0.800 47.1n Gasolina (ᐉ) CnH1.177 2. http://librosysolucionarios.82–0.800 49.231 70.20 2.71 49.134 44.100 45.640 46.8n Diesel pesado (ᐉ) CnH1.69 1.000 44.670 50.100 47.150 16.285 170 200 30.626 — 0.800 44.240 43.141 Densidad.038 78.910 50.570 55.100 45.500 51. kg/kmol 26.4 2.123 12.760 50.800 47.000 44.500 48.75 2.400 48.520 26.84 0.660 — 0.097 92. y 1 atm y temperatura normal de ebullición para combustibles gaseosos.161 86.78–0.114 58.708 2.100 44.23 2.070 46.579 2 0.042 28.800 48.72–0.013 114.2 kJ/kg Calor específico.9 1. 3A 25°C.72 2.684 0.890 47.340 40.949 APÉNDICE 1 TABLA A-27 Propiedades de algunos combustibles e hidrocarburos comunes Combustible (fase) Fórmula Acetileno (g) C2H2 Benceno (ᐉ) C6H6 Butano (ᐉ) C4H10 Carbono (s) C Decano (ᐉ) C10H22 Diesel ligero (ᐉ) CnH1.53 1. de carbono (g) CO Octano (ᐉ) C8H18 1-Penteno (ᐉ) C5H10 Propano (ᐉ) C3H8 Tolueno (ᐉ) C7H8 Masa molar. Multiplique por la masa molar para obtener los valores caloríficos en kJ/kmol.42 0.069 18 100–110 100.net 18Appendix_01 ITALICAS.703 0.867 Entalpía de vaporización.730 0.370 32.87n Heptano (ᐉ) C7H16 Hexano (ᐉ) C6H12 Hexeno (ᐉ) C6H14 Hidrógeno (g) H2 Isopentano (ᐉ) C5H12 Metano (g) CH4 Metanol (ᐉ) CH4O Monóx.530 22.1 cp kJ/kg · K Poder calorífico superior.877 0.1 kg/L — 0.630 46. 2A 25°C para combustibles líquidos.900 29.500 0.300 48.740 120.673 0.641 0.970 41.24 1.3 kJ/kg — 433 362 — 361 270 230 172 919 — 350 365 392 366 — — 509 1168 — 363 363 335 412 1.21 2.2 1.204 84.7n Etano (g) C2H6 Etanol (ᐉ) C2H6O Gas natural (g) CnH3.810 45.790 — 0.27 14.280 40.44 2 2.20 2.016 72.920 10.400 44.000 47.011 142.88 — 0.330 42.430 44. 391 32.648 3.202 4000 0.685 3200 2.860 2.480 213.055 48. ed.011 28.576 1.894 1.429 0.182 14.294 4.945 0.005 500 92.843 103.032 106.120 3.671 2. Van Wylen y Richard E.832 4.304 25. The Dow Chemical Company.030 14.645 36. Midland.216 0.099 13.975 105.270 5.295 9.689 2.. 1986.771 4.433 3.534 3400 1.513 3.414 6.996 1.497 6.827 9. John Wiley & Sons.898 14.276 2600 6.630 45.921 0.888 1.392 0.072 1.796 2.616 23.719 3.486 5000 3. Con base en información termodinámica proporcionada en JANAF.865 H2O Δ H2 + 1/2O2 H2O Δ 1/2H2 + OH CO2 Δ CO + 1/2O2 92.701 1.312 0.842 10.011 66.169 0. Nueva York.742 22.937 2. Fundamentals of Classical Thermodyamics.497 7.560 2.807 4.517 2800 5.283 16.874 1400 24.609 11. Termal Research Laboratory.728 7.086 2.660 9.609 3800 0.197 3.111 0. 1971.497 0.005 27.451 1.114 1.827 1000 39.044 0.871 13. K H2 Δ 2H O2 Δ 2O N2 Δ 2N 298 164. versión inglés/SI.net 18Appendix_01 ITALICAS.725 5500 4.145 6.490 3.866 2000 12.285 18.926 0.619 4.895 5.937 17.208 60.002 3000 3.023 5.516 3600 0..150 35.245 1/ 2N2 + 1/2O2 Δ NO 35.341 Fuente: Gordon J.529 17.830 8.318 2.763 2.501 0.212 1.920 1.826 4.372 2.117 22.176 1. Sonntag.934 4500 2.599 2.034 20.963 367.329 56.666 2.590 186.931 3.826 8.935 0.743 6000 5.768 5.840 2200 10.359 19.950 TABLAS DE PROPIEDADES.691 23.622 11.127 80. Thermochemical Tables.051 41.635 5.356 1. Tabla A-14.281 26. MI.052 20.657 8.800 15.088 0.812 3.801 1.372 99.148 5.803 1200 30. 3a.357 3.762 57.569 6.521 5. 723.199 12.019 0.690 1.353 2400 8.208 52. http://librosysolucionarios.qxd 950 7/12/11 14:26:07 .388 7.066 10.513 1. p.019 2.536 3. FIGURAS Y DIAGRAMAS (UNIDADES SI) TABLA A-28 Logaritmos naturales de la constante de equilibrio Kp La constante de equilibrio Kp para la reacción nA A + nB B Δ nC C + nD D se define como Kp ≡ PCnC PDnD PAnA PBnB Temp.542 0.163 18.463 1600 19.686 0.637 1800 15.891 1.921 9. 0 1.5 0.400 = TR 0 0.10 0.4 0.98 2.25 3.75 0.10 1.60 1. 1.92 3.0 10 20 30 Presión reducida. 1.0 0.00 0 0.0 1.94 0.96 1.80 4.00 1.0 3.000 0 0. 561.65 0.5 0.10 0.08 0. Fig C.30 P R http://librosysolucionarios.00 2.90 2.5 1.20 Va p –– –– hideal – h hideal – h = ————– Desviación de entalpía Zh = ————– RuTcr RTcr R 1.net 18Appendix_01 ITALICAS.25 0.60 R 6.94 1. 1. 2.0 tu ra do 0.80 3.9 2.30 0.02 1. Nueva York. 1987.20 0 3 1.5.05 0.98 0. C.20 0.50 1.0 0. 80 TR 0 0. 558.100 Fuente: John R.70 6.20 0.85 4.85 2.70 1.0 0.80 os atu rad o 5. McGraw-Hill.5 0.60 0. P 0.0 Líq 0. Fig.2 y p.06 1.5 0.951 APÉNDICE 1 7.90 1. Fundamentals of Engineering Thermodynamics.50 7.0 2.500 0.96 1.80 1.60 0 5 1.55 T 0.3 0. versión SI.15 0.00 2.200 FIGURA A-29 Carta generalizada de desviación de entalpía.5 0.1 0.5 1.00 0.2 0.9 0 9 = 0.92 0. p.0 4.15 0.90 0 0.5 00 1.40 1.75 uid 0.5 o rad atu or s Vap .40 2.90 5.300 or sa 1.5 0. Howell y Richard O. Buckius.04 1. –– –– hideal – h hideal – h = ————– Desviación de entalpía Zh = ————– RuTcr RTcr 0.40 2.2 0 0 1.0 5.1 1.0 1.qxd 951 7/12/11 14:26:08 .00 4. 400 r po Va 0.80 2. Nueva York.90 =0 TR 0 1.00 0.15 2.0 sat 0. FIGURAS Y DIAGRAMAS (UNIDADES SI) 0.04 1.0 1.10 1 1.75 0.2 0.0 4.96 0.1 0.96 0. P R http://librosysolucionarios.10 1. Fundamentals of Engineering Thermodynamics.0 1.60 1.0 0.02 1.02 0.06 1.50 5.200 0.70 o sideal – s sideal – s = ————– Desviación de entropía Zs = ————– Ru R 0. Howell y Richard O.05 0. Buckius.80 0.65 d ura 0. p. versión SI.0 10 20 30 Presión reducida.25 0.0 0.qxd 952 7/12/11 14:26:08 .952 9.000 0 1.50 3.50 1.20 1.60 2.0 0. 559.98 1.85 4.0 5.3 0.10 0.3 y p.0 1.0 .5. McGraw-Hill. Fig C.85 3.20 0.0 sideal – s sideal – s = ————– Zs = ————– Ru R TABLAS DE PROPIEDADES.80 0.5 1.00 3.300 tur sa .06 1.0 2.94 0.08 0.90 0.20 1.00 1.98 0.10 1.40 1. 80 Desviación de entropía 10. do r satura Vapo 0 0.500 o ad 0.55 0.40.60 o uid Líq 6.20 1.15 0.0 0.92 0.40 4 1.0 TRr 8.94 1.92 0.95 00 FIGURA A-30 Carta generalizada de desviación de entropía. Fig.40 1.60 2.0 0.00 1.90 0.0 0.0. 1.75 0.net 18Appendix_01 ITALICAS.94 0.9 0 0.30 Fuente: John R.98 1. C. 1987. 561.30 PR 7.100 0. Inc.70 0.2 0 5. Refrigerating and Air-Conditioning Engineers.0 1.36 APÉNDICE 1 953 http://librosysolucionarios.0 –2.75 0. % 20 0% 25 m olu 2v Preparado por el Centro de Estudios Aplicados de Termodinámica.40 0. 0.7 8 Reproducida con permiso de la American Society of Heating.net 7/12/11 14:26:08 ΔHS Calor sensible —— —————– = Calor total ΔHT Relación de humedad (ω) (ω) gramos de humedad por kilogramo de aire seco (ω .0 2.8 6 % 40 30% 0. Refrigerating and Air-Conditioning Engineers.0 0. Georgia. Atlanta.50 0.6 0.0 –0.5 0.8 4 20 6 0. Temperatura de bulbo seco ºC % 50 edo úm oh eb ulb ra d atu per tem 0.0 Calor total ΔHT – 2.8 30 va d relati umeda 8 10% H 20% ºC 40 gr o sec ire de a o am en m 2 0. 10. 1 Temperatura normal Presión barométrica 101.5 % –0 90 etro ico cúb 80 © 1992 American Society of Heating.0 • 0.0 1.60 0.0 1.80 0.85 0.1 18Appendix_01 ITALICAS.8 0 0.4 –• 1.65 0.0 1. Inc.95 1.5 –5.0 0.45 0.0 3 0.325 kPa 2 4 6 8 50 10 12 14 16 18 20 22 24 26 28 30 60 70 80 90 100 110 120 0.0 4. usada con permiso.0 0.55 0.9 30 k 80 30 kilo 50 E lp a nt h) ( ía e ul jo ilo o am 70 gr li o k or sp a co se 30 por 40 Entalpía Δh ————————— = —— Relación de humedad Δ de ire 90 100 4 20 4.8 0.0 ΔHS – • Calor sensible —————– = —— – 4.0 10 15 m Te 60 25 0 0.9 FIGURA A-31 Carta psicrométrica a 1 atm de presión total. 0 5 2.5 5 10 10 r pe ra u at de 15 n ió ac ur 20 t sa ºC 0.8 0.9 70 ASHRAE Gráfica psicrométrica núm.90 0.0 0.qxd 953 % Nivel del mar .7 0..2 3.0 2. Universidad de Idaho. 8430 0.4374 0.8960 3.5283 0.0000 1.1094 0.0351 1.5913 0.0944 1.8 2.5(k 1 2 k 1 31 2 11 Ma224 Ma k 1 2 k (k 1) k 1 11 Ma22 2 1 (k 1) k 1 11 Ma22 2 1 k 1 11 Ma22 2 Ma TABLA A-32 k (k Funciones de flujo compresible unidimensional e isentrópico de un gas ideal con k  1.4 0.4647 0.8333 0.9725 0.0050 2.4254 1.9140 1.5 3.2 2.5 2.9921 0.5 r/r* P/P0 0 0 0.5001 4.9690 0.9930 0.2346 25.1472 0.8571 1.3257 0.5345 0.0501 0.0935 0.0382 1.0946 0.6348 0.6614 0.9328 0.3142 0.8 0.4 1.3557 0.5 1.0 0 0.0000 0.8405 0.7179 1.8865 0.6330 1.8 3.8956 0.0 A/A* Funciones de flujo compresible 2.6 1.1278 0.0 2.9640 2.1667 0 3.7184 0.4124 0.2361 2.5556 0.6 2.0 Ma* 1.7922 1.0368 0.7764 0.net 18Appendix_01 ITALICAS.6 0.9107 0.9823 0.2353 0.8606 0.5 Ma 2.6870 0.8852 0.1149 1.9524 0.5311 0.2 0.0019 0 1.000 1.4 2.7400 0.4313 0.1583 1.8218 2.9146 1.4252 0.0 1.5 0.9980 0.3571 0.qxd 954 7/12/11 14:26:08 .954 TABLAS DE PROPIEDADES.2868 0.9395 0.4 1) (k 1) Ma Ma* A/A* P/P0 r/r0 T/T0 0 0.6560 0.0000 0. FIGURAS Y DIAGRAMAS (UNIDADES SI) Ma* A A* P P0 + +0 T T0 1 2 1)Ma2 0.0089 1.5360 1.9 1.5 1.5081 0.0000 1.7 0.2502 1.7916 0.3 0.4390 1.0113 0 1.0304 1.2182 0.6339 0.9950 0.0 http://librosysolucionarios.5901 1.2495 5.4031 2.0 T/T0 0.0 5.1740 0.1882 1.7840 0.2999 1.0760 0.0684 0.9564 0.0 2.1179 0.7209 0.0000 0.7318 0.0272 0.9803 0.3894 0.6068 0.3398 1.2 1.1841 0.2300 0.6875 2.9243 0.9635 2.1 0.0 1.8251 0. 7 2.qxd 955 7/12/11 14:26:09 .9800 9.1200 2.8969 8.9794 0.4 2.3895 0.8952 0.6133 4.4 2 1 k 1 1 1)Ma21 (k 1)Ma21 V1 V2 1) 1) Ma22(k Ma21(k 1) 2 (k 4 1) 2 kMa21)[1 Ma22(k 1 kMa22 1)/[2(k 1) 2]k (k 1)] 1) Ma1 Ma2 P2/P1 r2/r1 T2/T1 P02/P01 P02/P1 1.5714 5.0 1.6897 1.5613 0.0000 1.9298 0.7705 1.7165 7.9783 5.4583 1.0000 0.1388 0.6405 0.5774 0.4752 0.1 2.4814 0.5632 2.1328 2.6684 0.2 1.8200 3.4512 2.5231 0.1909 1.000 1.5 2.6165 0.0 Ma1 2.7397 0.3022 12.3780 1.1418 5.9 3.4133 3.7136 3.7200 8.2547 1.6404 6.5133 1.0681 32.5401 0.3333 3.3592 2.6742 0.2450 1.5039 0.8929 2.3 2.8050 4.7674 0.8571 4.0845 3.1813 9.1654 6.5694 11.4490 3.5590 3.0000 1.4236 0.0000 1.8422 0.1280 1.3202 1.9582 0.6636 3.5471 0.0050 6.955 APÉNDICE 1 T01 Ma2 TABLA A-33 T02 (k 1)Ma21 2kMa21 k kMa21 kMa22 P2 P1 1 1 +2 +1 P2 P1 T2 T1 T2 T1 2 2 P 02 P 01 Ma1 1 3 Ma2 1 P 02 P1 (1 2kMa21 k (k 2 Ma21(k Ma22(k Funciones de choque normal unidimensional de un gas ideal con k  1.6281 0.0 T2/T1 2.0492 3.0 Ma2 P02/P01 0 1.7 1.9468 2.0403 2.4800 6.1 1.5833 0.1977 2.0617 0 1.9118 0.2238 4.3383 8.7629 3.9 2.5344 0.0000 6.3283 0.2119 3.0 r2/r1 3.net 18Appendix_01 ITALICAS.8050 2.6335 5.7011 0.4882 0.9928 0.5316 1.6790 4.3880 1.5000 4.8621 2.3333 18.5 1.4152 0.2 2.0 1.0649 1.4990 0.5533 7.5000 29.3577 0.4601 0.0610 21.6450 10.0 1.0 http://librosysolucionarios.9989 0.6695 5.5157 1.8119 2.4350 0.8557 0.0469 5.7860 0.7209 0.0 5.0450 4.5956 0.8127 0.6 1.0 4.6875 1.4583 2.3429 2.9512 3.4956 0.5261 9.8624 10.5157 2.6079 1.6 2.0317 2.3416 1.8569 1.4075 2.1375 2.2383 2.5 3.6667 2.4 1.2050 3.1250 7.3 1.5 2.8 1.0 P02/P1 P2/P1 Funciones de choque normal 4.5130 0.1691 1.0 2.0000 1.0000 0.8 2.8000 1.0 1.2937 7. 4444 0.5 1.0000 0.4611 0.2004 0.4038 0.6151 0.0753 1.7242 0.9 1.6970 0.4000 2.9921 1.4 Ma T0/T 0* P0/P 0* T/T* P/P* V/V* 0.3556 0.5 0.0 2.0777 1.8842 0.0 1.4046 1.2 2.1985 1.9085 0.5 2.5252 1.9343 0.7901 0.3403 1.0194 1.9167 0.5031 1.0000 0.1459 1.4 0.8363 0.6089 0.9929 1.0 V/V* 1.5 T/T* P/P* 0 0 0.2 0.956 TABLAS DE PROPIEDADES.2294 0.5745 0.0 0.0245 1.8 3.4245 0.5 1.3469 0.0049 1.5 3. FIGURAS Y DIAGRAMAS (UNIDADES SI) T0 T 0* 1)Ma2[2 (k 1)Ma2] (1 kMa2)2 (k P0 P*0 1 T T* Ma(1 k) 2 1 2 1 kMa2 k 1 2 1 1 kMa2 P P* 1 k kMa2 V V* +* + (1 1 (k k k)Ma2 kMa2 2 k (k 1) 1)Ma 2 1 TABLA A-34 Funciones del flujo de Rayleigh para un gas ideal con k  1.2591 1.6410 0.4177 2.3 0.0 2.0237 0.1 0.4 1.5236 0.0193 1.7 0.0000 1.0000 0.5 P0/P0* Funciones del flujo de Rayleigh 3.qxd 956 7/12/11 14:26:09 .4545 1.3636 0.6914 0.1314 1.2727 2.0 T0/T 0* 0.7778 1.5 Ma 2.7017 0.6738 0.0560 0.2679 1.7958 0.8054 0.2 1.9639 0.2066 0.8 2.2564 1.0255 1.1736 0.0468 0.7934 0.8189 0.7434 2.7561 0.1246 1.4938 1.0 0.0451 2.4335 0.1566 1.3086 0.0000 0.1765 0.3149 0.4235 1.0 2.4 2.0000 0.5957 1.8101 0.6540 1.5711 1.5289 0.6 0.3669 2.1141 1.1756 1.3137 0.2658 1.2803 2.8 0.0000 1.2346 1.5882 3.9118 0.3159 1.9608 1.5505 1.4089 0.0000 0.8731 3.6 1.net 18Appendix_01 ITALICAS.9110 1.6 2.0909 0.0 http://librosysolucionarios.5290 0.0 1.2648 0.6975 0.1918 0.0431 1.9787 0. Vapor de agua Diagrama T-s para el agua Diagrama de Mollier para el agua Refrigerante 134a saturado. O2 Tabla A-20E Propiedades de gas ideal del dióxido de carbono.net 19Appendix_02 ITALICAS. Tabla de temperaturas Agua saturada.APÉNDICE 2 TABLAS DE PROPIEDADES. Tabla de temperatura Refrigerante 134a saturado.qxd 957 7/12/11 14:26:49 . H2O Tabla A-26E Entalpía de formación. CO2 Tabla A-21E Propiedades de gas ideal del monóxido de carbono. constante de gas y propiedades del punto crítico Calores específicos de gas ideal de varios gases comunes Propiedades de líquidos. FIGURASY DIAGRAMAS (UNIDADES INGLESAS) Tabla A-1E Tabla A-2E Tabla A-3E Tabla A-4E Tabla A-5E Tabla A-6E Tabla A-7E Tabla A-8E Figura A-9E Figura A-10E Tabla A-11E Tabla A-12E Tabla A-13E Figura A-14E Tabla A-16E Masa molar. función de Gibbs de formación y entropía absoluta a 77°C. H2 Tabla A-23E Propiedades de gas ideal del vapor de agua. CO Tabla A-22E Propiedades de gas ideal del hidrógeno. Tabla de presiones Vapor de agua sobrecalentado Agua líquida comprimida Hielo saturado. 1 atm Tabla A-27E Propiedades de algunos combustibles e hidrocarburos comunes Figura A-31E Gráfica psicrométrica a 1 atm de presión total http://librosysolucionarios. N2 Tabla A-19E Propiedades de gas ideal del oxígeno. sólidos y alimentos comunes Agua saturada. Tabla de presión Refrigerante 134a sobrecalentado Diagrama P-h para refrigerante 134a Propiedades de la atmósfera a gran altitud Tabla A-17E Propiedades de gas ideal del aire Tabla A-18E Propiedades de gas ideal del nitrógeno.