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APÉNDICE
1
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 de carbono, CO
Tabla A-2
Calores específicos de gas ideal de varios gases comunes
Tabla A-22
Propiedades de gas ideal H2
Tabla A-3
Propiedades de líquidos, sólidos y alimentos comunes
Tabla A-23
Propiedades de gas ideal 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 monoatómico, O
Tabla A-25
Propiedades de gas ideal OH
Tabla A-26
Entalpía de formación, func Gibbs de formación y entro a 25°C, 1 atm
Diagrama de Mollier para el agua
Tabla A-27
Refrigerante 134a saturado. Tabla de temperatura
Propiedades de algunos e hidrocarburos comunes
Tabla A-28
Refrigerante 134a saturado. Tabla de presión
Logaritmos naturales de de equilibrio K p
Figura A-29
Tabla A-12 Tabla A-13 Figura A-14 Figura A-15
Agua saturada. Tabla de presiones Vapor de agua sobrecalentado Agua líquida comprimida Hielo saturado. Vapor de agua Diagrama T-s para el agua
Refrigerante 134a sobrecalentado Diagrama P-h para refrigerante 134a Carta generalizada de compresibilidad de Nelson-Obert
Carta generalizada de desv de entalpía Sign up to vote on this title Figura A-30 Carta generalizada de desv Not useful Useful de entropía
Figura A-31
Carta psicrométrica a 1 atm total
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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 -Butano Cloro Cloroformo Cloruro metílico Criptón Diclorodifluorometano (R-12) Diclorofluorometano (R-21) Dióxido de carbono Dióxido de sulfuro Etano Etileno Helio n -Hexano -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 C6H6 Br2 C4H10 Cl2 CHCl3 CH3Cl Kr CCl 2F2 CHCl 2F CO2 SO2 C2H6 C2H4 He C6H14 H2 CH4 CO Ne N2 N2O O2 C3H8 C3H6 CCl4 CF 3CH2F CCl 3F Xe
Masa molar, M kg/kmol kg/kmol 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
Constante de gas, R kJ/kg · K*
Propiedades del punto crtico
Temperatura, K
Presión, MPa
0.4615 647.1 22.06 0.2870 132.5 3.77 0.1805 516 6.38 0.2595 513.2 7.95 0.4882 405.5 11.28 0.2081 151 4.86 0.1064 562 4.92 0.0520 584 10.34 0.1430 425.2 3.80 0.1173 417 7.71 0.06964 536.6 5.47 0.1647 416.3 6.68 0.09921 209.4 5.50 0.06876 384.7 4.01 0.08078 451.7 5.17 0.1889 304.2 7.39 0.1298 430.7 7.88 0.2765 305.5 4.48 0.2964 282.4 5.12 2.0769 5.3 0.23 0.09647 507.9 3.03 4.1240 33.3 1.30 0.5182 191.1 4.64 0.2968 133 3.50 0.4119 44.5 2.73 0.2968 126.2 3.39 0.1889 309.7 7.27 0.2598 154.8 5.08 0.1885 370 4.26 0.1976 365 4.62 0.05405 556.4 4.56 0.08149 374.2 4.059 Sign up to vote on this title 0.06052 471.2 4.38 0.06332 Useful 289.8 Not useful 5.88
Volum m3 /km
0.05 0.08 0.16 0.11 0.07 0.07 0.26 0.13 0.25 0.12 0.24 0.14 0.09 0.21 0.19 0.09 0.12 0.14 0.12 0.05 0.36 0.06 0.09 0.09 0.04 0.08 0.09 0.07 0.19 0.18 0.27 0.19 0.24 0.11
M , donde R u 8.31447 kJ/kmol · K y M es *La unidad en kJ/kg · K es equivalente a kPa · m 3 /kg · K. La constante de gas se calcula de R R u / M es la molar.
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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 -Butano Cloro Cloroformo Cloruro metílico Criptón Diclorodifluorometano (R-12) Diclorofluorometano (R-21) Dióxido de carbono Dióxido de sulfuro Etano Etileno Helio n -Hexano -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 C6H6 Br2 C4H10 Cl2 CHCl3 CH3Cl Kr CCl 2F2 CHCl 2F CO2 SO2 C2H6 C2H4 He C6H14 H2 CH4 CO Ne N2 N2O O2 C3H8 C3H6 CCl4 CF 3CH2F CCl 3F Xe
Masa molar, M kg/kmol kg/kmol 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
Constante de gas, R kJ/kg · K*
Propiedades del punto crtico
Temperatura, K
Presión, MPa
0.4615 647.1 22.06 0.2870 132.5 3.77 0.1805 516 6.38 0.2595 513.2 7.95 0.4882 405.5 11.28 0.2081 151 4.86 0.1064 562 4.92 0.0520 584 10.34 0.1430 425.2 3.80 0.1173 417 7.71 0.06964 536.6 5.47 0.1647 416.3 6.68 0.09921 209.4 5.50 0.06876 384.7 4.01 0.08078 451.7 5.17 0.1889 304.2 7.39 0.1298 430.7 7.88 0.2765 305.5 4.48 0.2964 282.4 5.12 2.0769 5.3 0.23 0.09647 507.9 3.03 4.1240 33.3 1.30 0.5182 191.1 4.64 0.2968 133 3.50 0.4119 44.5 2.73 0.2968 126.2 3.39 0.1889 309.7 7.27 0.2598 154.8 5.08 0.1885 370 4.26 0.1976 365 4.62 0.05405 556.4 4.56 0.08149 374.2 4.059 Sign up to vote on this title 0.06052 471.2 4.38 0.06332 Useful 289.8 Not useful 5.88
Volum m3 /km
0.05 0.08 0.16 0.11 0.07 0.07 0.26 0.13 0.25 0.12 0.24 0.14 0.09 0.21 0.19 0.09 0.12 0.14 0.12 0.05 0.36 0.06 0.09 0.09 0.04 0.08 0.09 0.07 0.19 0.18 0.27 0.19 0.24 0.11
M , donde R u 8.31447 kJ/kmol · K y M es *La unidad en kJ/kg · K es equivalente a kPa · m 3 /kg · K. La constante de gas se calcula de R R u / M es la molar.
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APÉND
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
c p
c
v
kJ/kg · K
kJ/kg · K
1.005 1.00 5 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
Nota: La unidad kJ/kg · K es equivalente a kJ/kg · C.
Fuente: Chemical and Process Thermodynam Thermodynamics ics 3a. 3a. ed., por Kyle, B.G., © 2000. Adaptado con permiso de Pearson Education, Inc., Upp Nueva Jersey.
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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 c p
Temperatura, K 250 300 350 400 450 500 550 600 650 700 750 800 900 1000
kJ/kg · K
c
c p
v
kJ/kg · K
k
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
kJ/kg · K
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 , H 2
250 300 350 400 450 500 550 600 650 700 750 800 900 1000
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
c p
v
kJ/kg · K
k
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
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
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
v
kJ/kg · K
k
Monóxido de carbono
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 , N 2
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
c
kJ/kg · K
Dióxido de carbono , CO 2
Aire
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
c
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
1.40 1.39 1.39 1.39 1.39 1.38 1.38 1.37 1.37 1.36 1.35 1.35 1.34 1.33
Oxígeno , O 2
1.400 0.913 0.653 1.400 0.918 0.658 1.399 0.928 0.668 1.397 0.941 0.681 1.395 0.956 0.696 1.391 0.972 0.712 1.387 0.988 0.728 1.382 1.003 0.743 1.376 1.017 0.758 1.371 1.031 0.771 1.365 1.043 0.783 1.360 1.054 0.794 1.349 1.074 0.814 1.341 1.090 0.830 Sign up to vote on this title
1.39 1.39 1.38 1.38 1.37 1.36 1.35 1.35 1.34 1.33 1.33 1.32 1.31 1.31
Fuente: Kenneth Wark, Thermodynamics , 4a. ed., Nueva York, McGraw-Hill, 1983, p. 783, Tabla A-4M. Publicada originalmente en Tables of Therm Useful Not useful Properties of Gases , NBS Circular 564, 1955.
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APÉND
TABLA A-2 Calores específicos de gas ideal de varios gases comunes (conclusión ) c ) Como una función de la temperatura
_
c p a bT cT 2 dT 3
(T en en K, c p en kJ/kmol · K) Sustancia
Fórmula
Acetileno Aire Amoniaco Azufre Benceno i -Butano -Butano n -Butano -Butano Cloruro de hidrógeno Dióxido de azufre Dióxido de carbono Dióxido de nitrógeno Etano Etanol Etileno n -Hexano -Hexano Hidrógeno Metano Metanol Monóxido de carbono Nitrógeno Óxido nítrico Óxido nitroso Oxígeno n -Pentano -Pentano Propano Propileno Trióxido de azufre Agua (vapor)
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
10 2 10 2 10 2 10 2 10 2 10 2 10 2
0.7620 10 2
c
d
6.527 10 5 0.4802 10 5
0.99072 1.628 31.57 23.01 18.34
10 5 10 5 10 5 10 5
10 9 10 9
10 9
273–1500 273–1800 273–1500 273–1800 273–1500 273–1500 273–1500
4.338 10 9
273–1500
10 9 10 9 10 9 10 9
HCl
30.33
SO2
25.78
5.795
10 2
3.812 10 5
8.612
10 9
273–1800
CO2
22.26
5.981
10 2
3.501 10 5
7.469
10 9
273–1800
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 10 2 17.27 10 2 20.96 10 2 15.64 10 2 55.22 10 2 0.1916 10 2 5.024 102 9.152 10 2
3.52 10 5 6.406 10 5
7.87 7.285 20.05 17.67 57.69 0.8704 11.01 8.039
10 9 10 9
273–1500 273–1500 273–1500 273–1500 273–1500 273–1800 273–1500 273–1000
CO N2 NO N2O O2 C5H12 C3H8 C3H6
28.16 28.90 29.34 24.11 25.48 6.774 4.04 3.15
0.1675 10 2 0.1571 10 2 0.09395 10 2 5.8632 10 2 1.520 10 2 45.43 10 2 30.48 10 2 23.83 10 2
0.5372 10 5 0.8081 10 5 0.9747 105 3.562 10 5 0.7155 10 5 22.46 10 5 15.72 10 5 12.18 10 5
SO3 H2O
16.40 32.24
10 2 10 2
11.20 10 5 1.055 10 5
14.58 0.1923
1.327
10 5 10 5
18.21 1.966 6.6909 3.986 77.62 49.91 35.00
Rango de temp., K
10.38 10 5 8.344 10 5 28.65 10 5 0.4003 10 5
1.269 1.22
10 5 10 5
10 9 10 9 10 9 10 9 10 9 10 9
2.222 10 9 2.873 10 9 4.187 10 9 10.58 10 9
1.312 42.29 31.74 24.62
10 9 10 9 10 9 10 9
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273–1800 273–1800 273–1500 273–1500 273–1800 273–1500 273–1500 273–1500 273–1300 273–1800
Fuente : B. G. Kyle, Chemical and Process Thermodynamics , Englewood Cliffs, Nueva Jersey, Prentice Hall, 1984. Usada con permiso.
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912
TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI)
TABLA A-3 Propiedades de líquidos, slidos y alimentos comunes a ) Líquidos Datos de ebullición a 1 atm
Datos de congelación
Punto Calor latente de Punto Calor latente de ebullivaporizacin de congede fusin Sustancia Aceite comestible (ligero) Agua
Alcohol etílico Amoniaco
ción normal, °C
100
78.6 33.3
Argón Benceno n -Butano Dióxido de carbono Etanol Etilén glicol Glicerina Helio Hidrógeno Isobutano Mercurio Metano
185.9
Metanol Nitrógeno
64.5 195.8
Octano Oxígeno Petróleo Propano
124.8 183 — 42.1
80.2 0.5 78.4*
78.2 198.1 179.9 268.9 252.8 11.7 356.7 161.5
h fg , kJ/kg
lación, °C
h if , kJ/kg
Propiedades de líquidos
Temperatura, °C
Densidad
Calor específi
kg/m3
c p , kJ/kg
r ,
25 910 1.80 0 1000 4.22 25 997 4.18 50 988 4.18 75 975 4.19 100 958 4.22 855 108 20 789 2.84 156 1357 322.4 682 4.43 77.7 33.3 665 4.52 20 0 639 4.60 25 602 4.80 161.6 28 1394 1.14 189.3 185.6 394 5.5 126 20 879 1.72 385.2 80.3 601 2.31 138.5 0.5 230.5 (a 0°C) 0 298 0.59 56.6 You're Reading a Preview 838.3 109 25 783 2.46 114.2 800.1 181.1 20 1109 2.84 10.8 Unlock 18.9 full access with a free trial. 974 200.6 20 1261 2.32 22.8 — — 146.2 22.8 268.9 445.7 70.7 10.0 259.2 Download With 59.5 Free Trial 252.8 160 11.7 367.1 105.7 593.8 2.28 294.7 11.4 25 13,560 0.139 38.9 510.4 58.4 423 3.49 182.2 161.5 301 5.79 100 1100 99.2 25 787 2.55 97.7 198.6 25.3 809 2.06 210 195.8 596 2.97 160 306.3 180.7 20 703 2.10 57.5 212.7 13.7 Sign upto 183 1141 1.71 218.8 vote on this title 230–384 20 640 2.0 Useful Not useful 427.8 80.0 581 2.25 187.7 42.1 0 529 2.53 50 449 3.13 2257
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APÉND
TABLA A-3 Propiedades de líquidos, slidos y alimentos comunes ( conclusión ) b ) Slidos (los valores son para temperatura ambiente, excepto que se indique otra cosa)
Densidad, r kg/m3
Sustancia
Calor específico, c p kJ/kg · K
Metales
Densidad, kg/m3
Sustancia
r
No metales
Acero dulce Aluminio 200 K 250 K 300 K 350 K 400 K 450 K 500 K Bronce (76% Cu, 2% Zn, 2% Al) Cobre
7,830
0.500 0.797 0.859 0.902 0.929 0.949 0.973 0.997 0.400
2,700
8,280
173°C
1520 1000 2110 1100 1150 2300 2420 2500 2700
0.254 0.342 0.367 0.381 0.386 0.393 0.403 You're0.45 Reading 0.400
240 K 260 K 273 K Ladrillo común Ladrillo refractario (500°C) Madera contrachapada (abeto Douglas) a Preview Maderas duras (maple, encino, etc.) Maderas suaves (abeto, pino, etc.) Unlock full access with aMármol free trial. 1.000 Piedra 0.440 Piedra caliza Download Trial 0.235 With Free Vidrio para ventanas 0.128 Vidrio pirex 0.130 Yeso o tabla de yeso
100°C 50°C
0°C 27°C 100°C 200°C Hierro Latón amarillo (65% Cu, 35% Zn) Magnesio Níquel Plata Plomo Tungsteno
Arena Arcilla Asfalto Caucho (blando) Caucho (duro) Concreto Diamante Grafito Granito Hielo 200 K 220 K
8,900
7,840 8,310 1,730 8,890 10,470 11,310 19,400
921 1922 2300 545 721 513 2600 1500 1650 2700 2230 800
c ) Alimentos
Calor específico kJ/kg · K
Calor específico, kJ/kg · K
Alimentos
Brócoli Camarón Carne de pollo Carne de res
Contenido de agua, % (masa)
90 83 74 67
Punto de congelación, °C 0.6 2.2 2.8
—
Por encima del punto de congelación
3.86 3.62 3.32 3.08
Por debajo del punto de congelación
1.97 1.89 1.77 1.68
Calor latente de fusión, kJ/kg
301 277 247 224
Contenido de agua, % (masa)
Punto de congelación, °C
Sign up to vote on this title
Alimentos
Helado Useful Mantequilla Manzanas Naranjas
63 Not useful 5.6 16 84 87
—
1.1 0.8
Por encima del punto de congelación
2.95 — 3.65 3.75
1 1 1 1
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TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI)
TABLA A-4 Agua saturada. Tabla de temperaturas Volumen específico, m 3 /kg
Temp., T °C
Pres. sat., P sat kPa
Líq. sat.,
Vapor sat.,
v f
v g
0.01 5 10 15 20
0.6117 0.8725 1.2281 1.7057 2.3392
0.001000 0.001000 0.001000 0.001001 0.001002
206.00 147.03 106.32 77.885 57.762
25 30 35 40 45
3.1698 4.2469 5.6291 7.3851 9.5953
0.001003 0.001004 0.001006 0.001008 0.001010
43.340 32.879 25.205 19.515 15.251
Energía interna, kJ/kg
Líq. sat., u f
Evap., u fg
Vapor sat., u g
0.000 21.019 42.020 62.980 83.913
2374.9 2360.8 2346.6 2332.5 2318.4
2374.9 2381.8 2388.7 2395.5 2402.3
104.83 125.73 146.63 167.53 188.43
2304.3 2290.2 2276.0 2261.9 2247.7
2409.1 2415.9 2422.7 2429.4 2436.1
2233.4 2219.1 2204.7 2190.3 2175.8
2442.7 2449.3 2455.9 2462.4 2468.9
50 55 60 65 70
12.352 15.763 19.947 25.043 31.202
0.001012 0.001015 0.001017 0.001020 0.001023
12.026 9.5639 7.6670 6.1935 5.0396
209.33 230.24 251.16 272.09 293.04
75 80 85 90 95
38.597 47.416 57.868 70.183 84.609
0.001026 0.001029 0.001032 0.001036 0.001040
4.1291 3.4053 2.8261 2.3593 1.9808
313.99 334.97 355.96 376.97 398.00
Entalpía, kJ/kg
Líq. sat., h f
Entropía, kJ/kg · K
Evap., h fg
Vapor sat., h g
Líq. sat., s f
Evap., sat. s fg
2500.9 2489.1 2477.2 2465.4 2453.5
2500.9 2510.1 2519.2 2528.3 2537.4
0.0000 0.0763 0.1511 0.2245 0.2965
9.1556 8.9487 8.7488 8.5559 8.3696
104.83 125.74 146.64 167.53 188.44
2441.7 2429.8 2417.9 2406.0 2394.0
2546.5 2555.6 2564.6 2573.5 2582.4
0.3672 0.4368 0.5051 0.5724 0.6386
8.1895 8.0152 7.8466 7.6832 7.5247
209.34 230.26 251.18 272.12 293.07
2382.0 2369.8 2357.7 2345.4 2333.0
2591.3 2600.1 2608.8 2617.5 2626.1
0.7038 0.7680 0.8313 0.8937 0.9551
7.3710 7.2218 7.0769 6.9360 6.7989
2161.3 2475.3 2146.6 2481.6 2131.9 2487.8 You're Reading 2117.0 2494.0 2102.0 2500.1
314.03 2320.6 335.02 2308.0 356.02 2295.3 a 377.04 Preview2282.5 398.09 2269.6
2634.6 2643.0 2651.4 2659.6 2667.6
1.0158 1.0756 1.1346 1.1929 1.2504
6.6655 6.5355 6.4089 6.2853 6.1647
2087.0 2506.0 2071.8 2511.9 2056.4 2517.7 Download With 2040.9 2523.3 2025.3 2528.9
419.17 2256.4 440.28 2243.1 461.42 Free Trial2229.7 482.59 2216.0 503.81 2202.1
2675.6 2683.4 2691.1 2698.6 2706.0
1.3072 1.3634 1.4188 1.4737 1.5279
6.0470 5.9319 5.8193 5.7092 5.6013
2713.1 2720.1 2726.9 2733.5 2739.8
0.001 21.020 42.022 62.982 83.915
Unlock full access with a free trial.
100 105 110 115 120
101.42 120.90 143.38 169.18 198.67
0.001043 0.001047 0.001052 0.001056 0.001060
1.6720 1.4186 1.2094 1.0360 0.89133
419.06 440.15 461.27 482.42 503.60
125 130 135 140 145
232.23 270.28 313.22 361.53 415.68
0.001065 0.001070 0.001075 0.001080 0.001085
0.77012 0.66808 0.58179 0.50850 0.44600
524.83 546.10 567.41 588.77 610.19
2009.5 1993.4 1977.3 1960.9 1944.2
2534.3 2539.5 2544.7 2549.6 2554.4
525.07 546.38 567.75 589.16 610.64
1.5816 1.6346 1.6872 1.7392 1.7908
5.4956 5.3919 5.2901 5.1901 5.0919
150 155 160 165 170
476.16 543.49 618.23 700.93 792.18
0.001091 0.001096 0.001102 0.001108 0.001114
0.39248 0.34648 0.30680 0.27244 0.24260
631.66 653.19 674.79 696.46 718.20
1927.4 1910.3 1893.0 1875.4 1857.5
2559.1 2563.5 2567.8 2571.9 2575.7
632.18 2113.8 2745.9 1.8418 653.79 2098.0 2751.8 1.8924 up to vote on this1.9426 title 675.47Sign2082.0 2757.5 697.24 2065.6 2762.8 1.9923 Useful Not useful 719.08 2048.8 2767.9 2.0417
4.9953 4.9002 4.8066 4.7143 4.6233
175 180
892.60 1002.8
0.001121 0.001127
0.21659 0.19384
740.02 761.92
1839.4 1820.9
2579.4 2582.8
741.02 763.05
4.5335 4.4448
2188.1 2173.7 2159.1 2144.3 2129.2
2031.7 2014.2
2772.7 2777.2
2.0906 2.1392
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TABLA A-4 Agua saturada. Tabla de temperaturas ( conclusión ) Volumen específico, m 3 /kg
Líq. sat,
Vapor sat.,
v f
v g
Energía interna, kJ/kg
Entalpía, kJ/kg
Temp., T °C
Pres. sat., P sat kPa
Líq. sat., u f
Evap., u fg
Vapor sat., u g
Líq. sat., h f
205 210 215 220 225
1724.3 1907.7 2105.9 2319.6 2549.7
0.001164 0.001173 0.001181 0.001190 0.001199
0.11508 0.10429 0.094680 0.086094 0.078405
872.86 895.38 918.02 940.79 963.70
1723.5 1702.9 1681.9 1660.5 1638.6
2596.4 2598.3 2599.9 2601.3 2602.3
874.87 897.61 920.50 943.55 966.76
1920.0 1899.7 1878.8 1857.4 1835.4
2794.8 2797.3 2799.3 2801.0 2802.2
2.3776 2.4245 2.4712 2.5176 2.5639
230 235 240 245 250
2797.1 3062.6 3347.0 3651.2 3976.2
0.001209 0.001219 0.001229 0.001240 0.001252
0.071505 0.065300 0.059707 0.054656 0.050085
986.76 1010.0 1033.4 1056.9 1080.7
1616.1 1593.2 1569.8 1545.7 1521.1
2602.9 2603.2 2603.1 2602.7 2601.8
990.14 1013.7 1037.5 1061.5 1085.7
1812.8 1789.5 1765.5 1740.8 1715.3
2802.9 2803.2 2803.0 2802.2 2801.0
2.6100 2.6560 2.7018 2.7476 2.7933
255 260 265 270 275
4322.9 4692.3 5085.3 5503.0 5946.4
0.001263 0.001276 0.001289 0.001303 0.001317
0.045941 0.042175 0.038748 0.035622 0.032767
1104.7 1128.8 1153.3 1177.9 1202.9
1495.8 1469.9 1443.2 1415.7 1387.4
2600.5 2598.7 2596.5 2593.7 2590.3
1110.1 1134.8 1159.8 1185.1 1210.7
1689.0 1661.8 1633.7 1604.6 1574.5
2799.1 2796.6 2793.5 2789.7 2785.2
2.8390 2.8847 2.9304 2.9762 3.0221
280 285 290 295 300
6416.6 6914.6 7441.8 7999.0 8587.9
0.001333 0.001349 0.001366 0.001384 0.001404
0.030153 0.027756 0.025554 0.023528 0.021659
1228.2 1253.7 1279.7 You're 1306.0 1332.7
1358.2 1328.1 1296.9 Reading 1264.5 1230.9
2586.4 1236.7 2581.8 1263.1 2576.5 1289.8 a2570.5 Preview1317.1 2563.6 1344.8
1543.2 1510.7 1476.9 1441.6 1404.8
2779.9 2773.7 2766.7 2758.7 2749.6
3.0681 3.1144 3.1608 3.2076 3.2548
305 310 315 320 325
9209.4 9865.0 10,556 11,284 12,051
0.001425 0.001447 0.001472 0.001499 0.001528
0.019932 0.018333 0.016849 0.015470 0.014183
1360.0 1195.9 1387.7 1159.3 1416.1 1121.1 Download With 1445.1 1080.9 1475.0 1038.5
2555.8 1373.1 2547.1 1402.0 2537.2 1431.6 Free Trial1462.0 2526.0 2513.4 1493.4
1366.3 1325.9 1283.4 1238.5 1191.0
2739.4 2727.9 2715.0 2700.6 2684.3
3.3024 3.3506 3.3994 3.4491 3.4998
330 335 340 345 350
12,858 13,707 14,601 15,541 16,529
0.001560 0.001597 0.001638 0.001685 0.001741
0.012979 0.011848 0.010783 0.009772 0.008806
1505.7 1537.5 1570.7 1605.5 1642.4
993.5 945.5 893.8 837.7 775.9
2499.2 2483.0 2464.5 2443.2 2418.3
1140.3 1086.0 1027.4 963.4 892.7
2666.0 2645.4 2622.0 2595.1 2563.9
3.5516 3.6050 3.6602 3.7179 3.7788
355 360 365 370 373.95
17,570 18,666 19,822 21,044 22,064
0.001808 0.001895 0.002015 0.002217 0.003106
0.007872 0.006950 0.006009 0.004953 0.003106
1682.2 1726.2 1777.2 1844.5 2015.7
706.4 625.7 526.4 385.6 0
2388.6 1714.0 812.9 2526.9 2351.9 1761.5 720.1 2481.6 up to vote on this2422.7 title 2303.6Sign1817.2 605.5 2230.1 1891.2 443.1 2334.3 Useful Not useful 2015.7 2084.3 0 2084.3
Unlock full access with a free trial.
1525.8 1559.4 1594.6 1631.7 1671.2
Evap., h fg
Vapor sat., h g
Líq. sat., s f
3.8442 3.9165 4.0004 4.1119 4.4070
Fuente : Las tablas A-4 a A-8 fueron generadas utilizando el programa para resolver ecuaciones de ingeniería (EES) desarrollado por S. A. Klei La rutina utilizada en los cálculos es la altamente precisa Steam_IAPWS, que incorpora la Formulación 1995 para las Propiedades Termodiná
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TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI)
TABLA A-5 Agua saturada. Tabla de presiones Volumen específico, m 3 /kg
Pres., P kPa
Temp. sat., T sat °C
Líq. sat.,
Vapor sat.,
v f
v g
Energía interna, kJ/kg
Líq. sat., u f
Evap., u fg
Vapor sat., u g
Entalpía, kJ/kg
Líq. sat, h f
Evap., h fg
Entropía, kJ/kg · K
Vapor sat., h g
Líq. sat., s f
Evap., s fg
1.0 1.5 2.0 2.5 3.0
6.97 13.02 17.50 21.08 24.08
0.001000 129.19 0.001001 87.964 0.001001 66.990 0.001002 54.242 0.001003 45.654
29.302 54.686 73.431 88.422 100.98
2355.2 2338.1 2325.5 2315.4 2306.9
2384.5 2392.8 2398.9 2403.8 2407.9
29.303 54.688 73.433 88.424 100.98
2484.4 2470.1 2459.5 2451.0 2443.9
2513.7 2524.7 2532.9 2539.4 2544.8
0.1059 0.1956 0.2606 0.3118 0.3543
8.8690 8.6314 8.4621 8.3302 8.2222
4.0 5.0 7.5 10 15
28.96 32.87 40.29 45.81 53.97
0.001004 0.001005 0.001008 0.001010 0.001014
121.39 137.75 168.74 191.79 225.93
2293.1 2282.1 2261.1 2245.4 2222.1
2414.5 2419.8 2429.8 2437.2 2448.0
121.39 137.75 168.75 191.81 225.94
2432.3 2423.0 2405.3 2392.1 2372.3
2553.7 2560.7 2574.0 2583.9 2598.3
0.4224 0.4762 0.5763 0.6492 0.7549
8.0510 7.9176 7.6738 7.4996 7.2522
20 25 30 40 50
60.06 64.96 69.09 75.86 81.32
0.001017 0.001020 0.001022 0.001026 0.001030
7.6481 6.2034 5.2287 3.9933 3.2403
251.40 271.93 289.24 317.58 340.49
2204.6 2190.4 2178.5 2158.8 2142.7
2456.0 2462.4 2467.7 2476.3 2483.2
251.42 271.96 289.27 317.62 340.54
2357.5 2345.5 2335.3 2318.4 2304.7
2608.9 2617.5 2624.6 2636.1 2645.2
0.8320 0.8932 0.9441 1.0261 1.0912
7.0752 6.9370 6.8234 6.6430 6.5019
75 91.76 100 99.61 101.325 99.97 125 105.97 150 111.35
0.001037 0.001043 0.001043 0.001048 0.001053
2.2172 1.6941 1.6734 1.3750 1.1594
384.36 417.40 418.95 444.23 466.97
2111.8 2496.1 384.44 2278.0 2088.2 2505.6 417.51 2257.5 You're Preview2256.5 2087.0 Reading 2506.0 a419.06 2068.8 2513.0 444.36 2240.6 Unlock full access a free trial.2226.0 2052.3 2519.2with467.13
2662.4 2675.0 2675.6 2684.9 2693.1
1.2132 1.3028 1.3069 1.3741 1.4337
6.2426 6.0562 6.0476 5.9100 5.7894
175 200 225 250 275
116.04 120.21 123.97 127.41 130.58
0.001057 0.001061 0.001064 0.001067 0.001070
1.0037 0.88578 0.79329 0.71873 0.65732
486.82 504.50 520.47 535.08 548.57
2037.7 2524.5 2024.6 2529.1 Download With 2012.7 2533.2 2001.8 2536.8 1991.6 2540.1
2700.2 2706.3 2711.7 2716.5 2720.9
1.4850 1.5302 1.5706 1.6072 1.6408
5.6865 5.5968 5.5171 5.4453 5.3800
300 325 350 375 400
133.52 136.27 138.86 141.30 143.61
0.001073 0.001076 0.001079 0.001081 0.001084
0.60582 0.56199 0.52422 0.49133 0.46242
561.11 572.84 583.89 594.32 604.22
1982.1 1973.1 1964.6 1956.6 1948.9
2543.2 2545.9 2548.5 2550.9 2553.1
561.43 573.19 584.26 594.73 604.66
2724.9 2728.6 2732.0 2735.1 2738.1
1.6717 1.7005 1.7274 1.7526 1.7765
5.3200 5.2645 5.2128 5.1645 5.1191
450 500 550 600 650
147.90 151.83 155.46 158.83 161.98
0.001088 0.001093 0.001097 0.001101 0.001104
0.41392 0.37483 0.34261 0.31560 0.29260
622.65 639.54 655.16 669.72 683.37
1934.5 1921.2 1908.8 1897.1 1886.1
2557.1 2560.7 2563.9 2566.8 2569.4
623.14 2743.4 Sign2120.3 up to vote on this1.8205 title 640.09 2108.0 2748.1 1.8604 Not useful Useful 655.77 2096.6 2752.4 1.8970 670.38 2085.8 2756.2 1.9308 684.08 2075.5 2759.6 1.9623
34.791 28.185 19.233 14.670 10.020
487.01 2213.1 504.71 Free Trial2201.6 520.71 2191.0 535.35 2181.2 548.86 2172.0 2163.5 2155.4 2147.7 2140.4 2133.4
5.0356 4.9603 4.8916 4.8285 4.7699
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TABLAS TERMO.pdf
1
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apendices cengel
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Search document
APÉND
TABLA A-5 Agua saturada. Tabla de presiones ( conclusión ) Volumen específico, m 3 /kg
Pres., P kPa
Temp. sat., T sat °C
Líq. sat.,
Vapor sat.,
v f
v g
Energía interna, kJ/kg
Líq. sat., u f
Evap., u fg
Vapor sat., u g
Entalpía, kJ/kg
Ent kJ/k
Líq. sat, h f
Evap., h fg
Vapor sat., h g
Líq. sat., s f
800 850 900 950 1000
170.41 172.94 175.35 177.66 179.88
0.001115 0.001118 0.001121 0.001124 0.001127
0.24035 0.22690 0.21489 0.20411 0.19436
719.97 731.00 741.55 751.67 761.39
1856.1 1846.9 1838.1 1829.6 1821.4
2576.0 2577.9 2579.6 2581.3 2582.8
720.87 731.95 742.56 752.74 762.51
2047.5 2038.8 2030.5 2022.4 2014.6
2768.3 2770.8 2773.0 2775.2 2777.1
2.0457 2.0705 2.0941 2.1166 2.1381
1100 1200 1300 1400 1500
184.06 187.96 191.60 195.04 198.29
0.001133 0.001138 0.001144 0.001149 0.001154
0.17745 0.16326 0.15119 0.14078 0.13171
779.78 796.96 813.10 828.35 842.82
1805.7 1790.9 1776.8 1763.4 1750.6
2585.5 2587.8 2589.9 2591.8 2593.4
781.03 798.33 814.59 829.96 844.55
1999.6 1985.4 1971.9 1958.9 1946.4
2780.7 2783.8 2786.5 2788.9 2791.0
2.1785 2.2159 2.2508 2.2835 2.3143
1750 2000 2250 2500 3000
205.72 212.38 218.41 223.95 233.85
0.001166 0.001177 0.001187 0.001197 0.001217
0.11344 876.12 0.099587 906.12 0.088717 933.54 0.079952 958.87 0.066667 1004.6
1720.6 1693.0 1667.3 1643.2 1598.5
2596.7 878.16 2599.1 908.47 2600.9 936.21 2602.1 961.87 2603.2 1008.3
1917.1 1889.8 1864.3 1840.1 1794.9
2795.2 2798.3 2800.5 2801.9 2803.2
2.3844 2.4467 2.5029 2.5542 2.6454
3500 4000 5000 6000 7000
242.56 250.35 263.94 275.59 285.83
0.001235 0.001252 0.001286 0.001319 0.001352
0.057061 0.049779 0.039448 0.032449 0.027378
1045.4 1557.6 2603.0 1049.7 1082.4 1519.3 2601.7 1087.4 You're Preview 1148.1 Reading 1448.9 a2597.0 1154.5 1205.8 1384.1 2589.9 1213.8 Unlock a free trial. 1258.0full access 1323.0with 2581.0 1267.5
1753.0 1713.5 1639.7 1570.9 1505.2
2802.7 2800.8 2794.2 2784.6 2772.6
2.7253 2.7966 2.9207 3.0275 3.1220
8000 9000 10,000 11,000 12,000
295.01 303.35 311.00 318.08 324.68
0.001384 0.001418 0.001452 0.001488 0.001526
0.023525 0.020489 0.018028 0.015988 0.014264
1306.0 1264.5 1350.9 1207.6 Download With 1393.3 1151.8 1433.9 1096.6 1473.0 1041.3
2570.5 1317.1 2558.5 1363.7 Free Trial 2545.2 1407.8 2530.4 1450.2 2514.3 1491.3
1441.6 1379.3 1317.6 1256.1 1194.1
2758.7 2742.9 2725.5 2706.3 2685.4
3.2077 3.2866 3.3603 3.4299 3.4964
13,000 14,000 15,000 16,000 17,000
330.85 336.67 342.16 347.36 352.29
0.001566 0.001610 0.001657 0.001710 0.001770
0.012781 0.011487 0.010341 0.009312 0.008374
1511.0 1548.4 1585.5 1622.6 1660.2
985.5 928.7 870.3 809.4 745.1
2496.6 2477.1 2455.7 2432.0 2405.4
1131.3 1067.0 1000.5 931.1 857.4
2662.7 2637.9 2610.8 2581.0 2547.7
3.5606 3.6232 3.6848 3.7461 3.8082
18,000 19,000 20,000 21,000 22,000 22,064
356.99 361.47 365.75 369.83 373.71 373.95
0.001840 0.001926 0.002038 0.002207 0.002703 0.003106
0.007504 0.006677 0.005862 0.004994 0.003644 0.003106
1699.1 1740.3 1785.8 1841.6 1951.7 2015.7
675.9 598.9 509.0 391.9 140.8 0
2375.0Sign 1732.2 up to vote777.8 on this2510.0 title 2339.2 1776.8 689.2 2466.0 Useful Not useful 1826.6 2294.8 585.5 2412.1 2233.5 1888.0 450.4 2338.4 2092.4 2011.1 161.5 2172.6 2015.7 2084.3 0 2084.3
1531.4 1571.0 1610.3 1649.9 1690.3
3.8720 3.9396 4.0146 4.1071 4.2942 4.4070
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TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI)
TABLA A-6 Vapor de agua sobrecalentado T °C
u kJ/kg
v
m3 /kg P †
Sat. 50 100 150 200 250 300 400 500 600 700 800 900 1000 1100 1200 1300
14.670 14.867 17.196 19.513 21.826 24.136 26.446 31.063 35.680 40.296 44.911 49.527 54.143 58.758 63.373 67.989 72.604 P
Sat. 150 200 250 300 400 500 600 700 800 900 1000 1100 1200 1300
0.37483 0.42503 0.47443 0.52261
s kJ/kg K
0.01 MPa (45.81°C)* 2437.2 2443.3 2515.5 2587.9 2661.4 2736.1 2812.3 2969.3 3132.9 3303.3 3480.8 3665.4 3856.9 4055.3 4260.0 4470.9 4687.4
0.88578 0.95986 1.08049 1.19890 1.31623 1.54934 1.78142 2.01302 2.24434 2.47550 2.70656 2.93755 3.16848 3.39938 3.63026 P
Sat. 200 250 300
h kJ/kg
2583.9 2592.0 2687.5 2783.0 2879.6 2977.5 3076.7 3280.0 3489.7 3706.3 3929.9 4160.6 4398.3 4642.8 4893.8 5150.8 5413.4
8.1488 8.1741 8.4489 8.6893 8.9049 9.1015 9.2827 9.6094 9.8998 10.1631 10.4056 10.6312 10.8429 11.0429 11.2326 11.4132 11.5857
0.20 MPa (120.21°C) 2529.1 2577.1 2654.6 2731.4 2808.8 2967.2 3131.4 3302.2 3479.9 3664.7 3856.3 4054.8 4259.6 4470.5 4687.1
2706.3 7.1270 2769.1 7.2810 2870.7 7.5081 2971.2 7.7100 3072.1 7.8941 3277.0 8.2236 3487.7 8.5153 3704.8 8.7793 3928.8 9.0221 4159.8 9.2479 4397.7 9.4598 4642.3 9.6599 4893.3 9.8497 5150.4 10.0304 5413.1 10.2029
0.50 MPa (151.83°C) 2560.7 2643.3 2723.8 2803.3
2748.1 2855.8 2961.0 3064.6
6.8207 7.0610 7.2725 7.4614
u kJ/kg
v
m3 /kg
P
h kJ/kg
s kJ/kg K
0.05 MPa (81.32°C)
P
3.2403
2483.2
2645.2
7.5931
3.4187 3.8897 4.3562 4.8206 5.2841 6.2094 7.1338 8.0577 8.9813 9.9047 10.8280 11.7513 12.6745 13.5977 14.5209
2511.5 2585.7 2660.0 2735.1 2811.6 2968.9 3132.6 3303.1 3480.6 3665.2 3856.8 4055.2 4259.9 4470.8 4687.3
2682.4 2780.2 2877.8 2976.2 3075.8 3279.3 3489.3 3706.0 3929.7 4160.4 4398.2 4642.7 4893.7 5150.7 5413.3
7.6953 7.9413 8.1592 8.3568 8.5387 8.8659 9.1566 9.4201 9.6626 9.8883 10.1000 10.3000 10.4897 10.6704 10.8429
P
0.30 MPa (133.52°C)
0.60582 2543.2 2724.9 6.9917 0.63402 2571.0 2761.2 7.0792 You're Reading a Preview 0.71643 2651.0 2865.9 7.3132 0.79645 2728.9 2967.9 7.5180 Unlock full access with a free trial. 0.87535 2807.0 3069.6 7.7037 1.03155 2966.0 3275.5 8.0347 1.18672 3130.6 8.3271 Download With3486.6 Free Trial 1.34139 3301.6 3704.0 8.5915 1.49580 3479.5 3928.2 8.8345 1.65004 3664.3 4159.3 9.0605 1.80417 3856.0 4397.3 9.2725 1.95824 4054.5 4642.0 9.4726 2.11226 4259.4 4893.1 9.6624 2.26624 4470.3 5150.2 9.8431 2.42019 4686.9 5413.0 10.0157 P
0.31560 0.35212 0.39390 0.43442
u kJ/kg
v
m3 /kg
h kJ/kg
s kJ/k
0.10 MPa (99.61°C)
1.6941 2505.6
2675.0
1.6959 1.9367 2.1724 2.4062 2.6389 3.1027 3.5655 4.0279 4.4900 4.9519 5.4137 5.8755 6.3372 6.7988 7.2605
2675.8 2776.6 2875.5 2974.5 3074.5 3278.6 3488.7 3705.6 3929.4 4160.2 4398.0 4642.6 4893.6 10.1 5150.6 10.3 5413.3 10.5
P
2506.2 2582.9 2658.2 2733.9 2810.7 2968.3 3132.2 3302.8 3480.4 3665.0 3856.7 4055.0 4259.8 4470.7 4687.2
0.40 MPa (143.61°C)
0.46242 2553.1 0.47088 2564.4 0.53434 2647.2 0.59520 2726.4 0.65489 2805.1 0.77265 2964.9 0.88936 3129.8 1.00558 3301.0 1.12152 3479.0 1.23730 3663.9 1.35298 3855.7 1.46859 4054.3 1.58414 4259.2 1.69966 4470.2 1.81516 4686.7
2738.1 2752.8 2860.9 2964.5 3067.1 3273.9 3485.5 3703.3 3927.6 4158.9 4396.9 4641.7 4892.9 5150.0 5412.8
6. 7. 7. 7. 7. 8. 8. 8. 8. 9.
9. 9.8
0.60 MPa (158.83°C) 0.80title MPa (170.41°C) Sign up to votePonthis 2566.8 2639.4 2721.2 2801.4
2756.2 6.7593 Useful 2850.6 6.9683 2957.6 7.1833 3062.0 7.3740
0.24035 2576.0 Not useful 0.26088 2631.1 0.29321 2715.9 0.32416 2797.5
2768.3 2839.8 2950.4 3056.9
6. 7. 7.
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TABLA A-6 Vapor de agua sobrecalentado (continuación ) T °C
u kJ/kg
v
m3 /kg P
Sat. 200 250 300 350 400 500 600 700 800 900 1000 1100 1200 1300
0.19437 0.20602 0.23275 0.25799 0.28250 0.30661 0.35411 0.40111 0.44783 0.49438 0.54083 0.58721 0.63354 0.67983 0.72610 P
Sat. 225 250 300 350 400 500 600 700 800 900 1000 1100 1200 1300
0.07995 0.08026 0.08705 0.09894 0.10979 0.12012
2777.1 2828.3 2943.1 3051.6 3158.2 3264.5 3479.1 3698.6 3924.1 4156.1 4394.8 4640.0 4891.4 5148.9 5411.9
6.5850 6.6956 6.9265 7.1246 7.3029 7.4670 7.7642 8.0311 8.2755 8.5024 8.7150 8.9155 9.1057 9.2866 9.4593
1.60 MPa (201.37 C) 2594.8 2645.1 2692.9 2781.6 2866.6 2950.8 3120.1 3293.9 3473.5 3659.5 3852.1 4051.2 4256.6 4467.9 4684.8
s v kJ/kg K m3 /kg
1.00 MPa (179.88 C) 2582.8 2622.3 2710.4 2793.7 2875.7 2957.9 3125.0 3297.5 3476.3 3661.7 3853.9 4052.7 4257.9 4469.0 4685.8
0.12374 0.13293 0.14190 0.15866 0.17459 0.19007 0.22029 0.24999 0.27941 0.30865 0.33780 0.36687 0.39589 0.42488 0.45383 P
Sat. 225 250 300 350 400
h kJ/kg
2792.8 2857.8 2919.9 3035.4 3146.0 3254.9 3472.6 3693.9 3920.5 4153.4 4392.6 4638.2 4890.0 5147.7 5410.9
2801.9 2805.5 2880.9 3009.6 3127.0 3240.1
P
0.16326 0.16934 0.19241 0.21386 0.23455 0.25482 0.29464 0.33395 0.37297 0.41184 0.45059 0.48928 0.52792 0.56652 0.60509 P
1.20
h kJ/kg
MPa (187.96 C)
2587.8 2612.9 2704.7 2789.7 2872.7 2955.5 3123.4 3296.3 3475.3 3661.0 3853.3 4052.2 4257.5 4468.7 4685.5
s kJ/kg K
2783.8 6.5217 2816.1 6.5909 2935.6 6.8313 3046.3 7.0335 3154.2 7.2139 3261.3 7.3793 3477.0 7.6779 3697.0 7.9456 3922.9 8.1904 4155.2 8.4176 4394.0 8.6303 4639.4 8.8310 4891.0 9.0212 5148.5 9.2022 5411.6 9.3750
1.80 MPa (207.11 C)
6.4200 0.11037 2597.3 2795.9 6.5537 0.11678 2637.0 2847.2 6.6753 0.12502 2686.7 2911.7 6.8864 0.14025 2777.4 3029.9 You're Reading a Preview 7.0713 0.15460 2863.6 3141.9 7.2394 0.16849 3251.6 Unlock full access2948.3 with a free trial. 7.5410 0.19551 3118.5 3470.4 7.8101 0.22200 3292.7 3692.3 8.0558 0.24822With 3472.6 3919.4 Download Free Trial 8.2834 0.27426 3658.8 4152.4 8.4965 0.30020 3851.5 4391.9 8.6974 0.32606 4050.7 4637.6 8.8878 0.35188 4256.2 4889.6 9.0689 0.37766 4467.6 5147.3 9.2418 0.40341 4684.5 5410.6
2.50 MPa (223.95 C) 2602.1 2604.8 2663.3 2762.2 2852.5 2939.8
u kJ/kg
6.2558 6.2629 6.4107 6.6459 6.8424 7.0170
P
6.3775 6.4825 6.6088 6.8246 7.0120 7.1814 7.4845 7.7543 8.0005 8.2284 8.4417 8.6427 8.8331 9.0143 9.1872
3.00 MPa (233.85 C)
u kJ/kg
v
m3 /kg P
0.14078 0.14303 0.16356 0.18233 0.20029 0.21782 0.25216 0.28597 0.31951 0.35288 0.38614 0.41933 0.45247 0.48558 0.51866 P
0.09959 0.10381 0.11150 0.12551 0.13860 0.15122 0.17568 0.19962 0.22326 0.24674 0.27012 0.29342 0.31667 0.33989 0.36308 P
1.40 MPa (19 2591.8 2602.7 2698.9 2785.7 2869.7 2953.1 3121.8 3295.1 3474.4 3660.3 3852.7 4051.7 4257.0 4468.3 4685.1
2599.1 2628.5 2680.3 2773.2 2860.5 2945.9 3116.9 3291.5 3471.7 3658.0 3850.9 4050.2 4255.7 4467.2 4684.2
2803.2
0.05706
2603.0
0.07063 0.08118 0.09056 0.09938
2644.7 2750.8 2844.4 2933.6
2856.5 0.05876 Useful6.2893 useful Not0.06845 2994.3 6.5412
2624.0 2738.8 2836.0 2927.2
3116.1 3231.7
6.7450 6.9235
0.07680 0.08456
28 29 30 31 32 34 36 39 41 43
3.50 MPa (24
2603.2
6.1856
278 280 292 304 315 325 347 369 392 415 439 463 489 514 541
2.00 MPa (21
0.06667
Sign up to vote on this title
h kJ/k
29 31 32
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TABLAS TERMO.pdf
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920
TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI)
TABLA A-6 Vapor de agua sobrecalentado (continuación ) T °C
u kJ/kg
v
m3 /kg P
Sat. 275 300 350 400 450 500 600 700 800 900 1000 1100 1200 1300
0.04978 0.05461 0.05887 0.06647 0.07343 0.08004 0.08644 0.09886 0.11098 0.12292 0.13476 0.14653 0.15824 0.16992 0.18157 P
Sat. 300 350 400 450 500 550 600 700 800 900 1000 1100 1200 1300
0.020489 0.023284 0.025816 0.029960 0.033524 0.036793
2800.8 2887.3 2961.7 3093.3 3214.5 3331.2 3446.0 3674.9 3906.3 4142.3 4383.9 4631.2 4884.4 5143.2 5407.2
6.0696 6.2312 6.3639 6.5843 6.7714 6.9386 7.0922 7.3706 7.6214 7.8523 8.0675 8.2698 8.4612 8.6430 8.8164
6.0 MPa (275.59 C)
2589.9 2668.4 2790.4 2893.7 2989.9 3083.1 3175.2 3267.2 3453.0 3643.2 3838.8 4040.1 4247.1 4459.8 4677.7
s v kJ/kg K m3 /kg
4.0 MPa (250.35 C)
2601.7 2668.9 2726.2 2827.4 2920.8 3011.0 3100.3 3279.4 3462.4 3650.6 3844.8 4045.1 4251.4 4463.5 4680.9
0.03245 0.03619 0.04225 0.04742 0.05217 0.05667 0.06102 0.06527 0.07355 0.08165 0.08964 0.09756 0.10543 0.11326 0.12107 P
Sat. 325 350 400 450 500
h kJ/kg
2784.6 2885.6 3043.9 3178.3 3302.9 3423.1 3541.3 3658.8 3894.3 4133.1 4376.6 4625.4 4879.7 5139.4 5404.1
5.8902 6.0703 6.3357 6.5432 6.7219 6.8826 7.0308 7.1693 7.4247 7.6582 7.8751 8.0786 8.2709 8.4534 8.6273
9.0 MPa (303.35 C)
2558.5 2647.6 2725.0 2849.2 2956.3 3056.3
2742.9 2857.1 2957.3 3118.8 3258.0 3387.4
5.6791 5.8738 6.0380 6.2876 6.4872 6.6603
u kJ/kg P
0.04406 0.04733 0.05138 0.05842 0.06477 0.07076 0.07652 0.08766 0.09850 0.10916 0.11972 0.13020 0.14064 0.15103 0.16140 P
s v kJ/kg K m3 /kg
4.5 MPa (257.44 C)
2599.7 2651.4 2713.0 2818.6 2914.2 3005.8 3096.0 3276.4 3460.0 3648.8 3843.3 4043.9 4250.4 4462.6 4680.1
h kJ/kg
2798.0 2864.4 2944.2 3081.5 3205.7 3324.2 3440.4 3670.9 3903.3 4140.0 4382.1 4629.8 4883.2 5142.2 5406.5
6.0198 6.1429 6.2854 6.5153 6.7071 6.8770 7.0323 7.3127 7.5647 7.7962 8.0118 8.2144 8.4060 8.5880 8.7616
7.0 MPa (285.83 C)
0.027378 2581.0 2772.6 5.8148 0.029492 2633.5 2839.9 5.9337 0.035262 2770.1 3016.9 6.2305 0.039958 3159.2 6.4502 You're2879.5 Reading a Preview 0.044187 2979.0 3288.3 6.6353 0.048157 3074.3 3411.4 Unlock full access with a free 6.8000 trial. 0.051966 3167.9 3531.6 6.9507 0.055665 3261.0 3650.6 7.0910 0.062850 3448.3With 3888.3 7.3487 Download Free Trial 0.069856 3639.5 4128.5 7.5836 0.076750 3835.7 4373.0 7.8014 0.083571 4037.5 4622.5 8.0055 0.090341 4245.0 4877.4 8.1982 0.097075 4457.9 5137.4 8.3810 0.103781 4676.1 5402.6 8.5551 P
0.018028 0.019877 0.022440 0.026436 0.029782 0.032811
10.0 MPa (311.00 C) 2545.2 2611.6 2699.6 2833.1 2944.5 3047.0
2725.5 2810.3 2924.0 3097.5 3242.4 3375.1
P
u kJ/kg
2597.0 2632.3 2699.0 2809.5 2907.5 3000.6 3091.8 3273.3 3457.7 3646.9 3841.8 4042.6 4249.3 4461.6 4679.3
2794.2 2839.5 2925.7 3069.3 3196.7 3317.2 3434.7 3666.9 3900.3 4137.7 4380.2 4628.3 4882.1 5141.3 5405.7
8.0 MPa (295.01 C)
0.023525 0.024279 0.029975 0.034344 0.038194 0.041767 0.045172 0.048463 0.054829 0.061011 0.067082 0.073079 0.079025 0.084934 0.090817 P
2570.5 2592.3 2748.3 2864.6 2967.8 3065.4 3160.5 3254.7 3443.6 3635.7 3832.7 4035.0 4242.8 4456.1 4674.5
2758.7 2786.5 2988.1 3139.4 3273.3 3399.5 3521.8 3642.4 3882.2 4123.8 4369.3 4619.6 4875.0 5135.5 5401.0
12.5 MPa (327.81
5.6159
0.013496 2505.6
2674.3
Useful 5.9460
0.016138 2624.9 Not useful 0.020030 2789.6 0.023019 2913.7 0.025630 3023.2
2826.6 3040.0 3201.5 3343.6
Sign up to vote on this title 5.7596 6.2141 6.4219 6.5995
s kJ/k
5.0 MPa (263.94 C)
0.03945 0.04144 0.04535 0.05197 0.05784 0.06332 0.06858 0.07870 0.08852 0.09816 0.10769 0.11715 0.12655 0.13592 0.14527 P
h kJ/kg
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TABLA A-6 Vapor de agua sobrecalentado (conclusión ) T °C
u kJ/kg
v
m3 /kg P
Sat. 350 400 450 500 550 600 650 700 800 900 1000 1100 1200 1300
0.010341 0.011481 0.015671 0.018477 0.020828 0.022945 0.024921 0.026804 0.028621 0.032121 0.035503 0.038808 0.042062 0.045279 0.048469
0.001978 0.006005 0.007886 0.009176 0.011143 0.012736 0.014140 0.015430 0.016643 0.018922 0.021075 0.023150 0.025172 0.027157 0.029115
2455.7 2520.9 2740.6 2880.8 2998.4 3106.2 3209.3 3310.1 3409.8 3609.3 3811.2 4017.1 4227.7 4443.1 4663.3
0.001641 0.001911 0.002538 0.003692 0.005623 0.006985
2610.8 2693.1 2975.7 3157.9 3310.8 3450.4 3583.1 3712.1 3839.1 4091.1 4343.7 4599.2 4858.6 5122.3 5390.3
5.3108 5.4438 5.8819 6.1434 6.3480 6.5230 6.6796 6.8233 6.9573 7.2037 7.4288 7.6378 7.8339 8.0192 8.1952
u kJ/kg
v
m3 /kg P
1849.4 2578.7 2805.0 2950.6 3165.9 3339.2 3493.5 3637.7 3776.0 4043.8 4307.1 4570.2 4835.4 5103.5 5375.1
1742.6 1931.4 2199.0 2511.8 2906.5 3154.4
u kJ/kg P
h kJ/kg
20.0 MPa (365.
2390.7 2529.5 5.1435
0.005862 2294.8 2412
0.012463 0.015204 0.017385 0.019305 0.021073 0.022742 0.024342 0.027405 0.030348 0.033215 0.036029 0.038806 0.041556
2684.3 2845.4 2972.4 3085.8 3192.5 3295.8 3397.5 3599.7 3803.5 4010.7 4222.3 4438.5 4659.2
0.009950 0.012721 0.014793 0.016571 0.018185 0.019695 0.021134 0.023870 0.026484 0.029020 0.031504 0.033952 0.036371
P
2902.4 3111.4 3276.7 3423.6 3561.3 3693.8 3823.5 4079.3 4334.6 4592.0 4852.8 5117.6 5386.5
P
0.001560 0.001731 0.002009 0.002487 0.003890 0.005118
5.7211 6.0212 6.2424 6.4266 6.5890 6.7366 6.8735 7.1237 7.3511 7.5616 7.7588 7.9449 8.1215
30.0 MPa
4.0345 0.001792 1738.1 1791.9 5.1400 0.002798 2068.9 2152.8 5.4708 0.005299 2452.9 2611.8 5.6759You're 0.006737 2618.9 2821.0 Reading a Preview 5.9643 0.008691 2824.0 3084.8 6.1816 0.010175 3279.7 Unlock full access 2974.5 with a free trial. 6.3637 0.011445 3103.4 3446.8 6.5243 0.012590 3221.7 3599.4 6.6702Download 0.013654 3334.3 With Free3743.9 Trial 6.9322 0.015628 3551.2 4020.0 7.1668 0.017473 3764.6 4288.8 7.3821 0.019240 3978.6 4555.8 7.5825 0.020954 4195.2 4823.9 7.7710 0.022630 4415.3 5094.2 7.9494 0.024279 4639.2 5367.6
3.8290 4.1145 4.5044 4.9449 5.4744 5.7857
s v kJ/kg K m 3 /kg
0.007932
40.0 MPa
1677.0 1855.0 2097.5 2364.2 2681.6 2875.1
h kJ/kg
17.5 MPa (354.67 C)
25.0 MPa
1799.9 2428.5 2607.8 2721.2 2887.3 3020.8 3140.0 3251.9 3359.9 3570.7 3780.2 3991.5 4206.1 4424.6 4647.2 P
375 400 425 450 500 550
s kJ/kg K
15.0 MPa (342.16 C)
P
375 400 425 450 500 550 600 650 700 800 900 1000 1100 1200 1300
h kJ/kg
50.0 MPa
1638.6 1787.8 1960.3 2160.3 2528.1 2769.5
2617.9 2807.3 2945.3 3064.7 3175.3 3281.4 3385.1 3590.1 3795.7 4004.3 4216.9 4433.8 4655.2 P
3.9313 4.4758 5.1473 5.4422 5.7956 6.0403 6.2373 6.4074 6.5599 6.8301 7.0695 7.2880 7.4906 7.6807 7.8602
0.001701 0.002105 0.003434 0.004957 0.006933 0.008348 0.009523 0.010565 0.011523 0.013278 0.014904 0.016450 0.017942 0.019398 0.020827
35.0 MPa
1702.8 1914.9 2253.3 2497.5 2755.3 2925.8 3065.6 3190.9 3308.3 3531.6 3749.0 3965.8 4184.4 4406.1 4631.2 P
2816 3061 3241 3396 3539 3675 3807 4067 4325 4584 4847 5112 5382
1762 1988 2373 2671 2997 3218 3399 3560 3711 3996 4270 4541 4812 5085 5360
60.0 MPa
1716.6 3.7642 0.001503 1609.7 Sign up4.0029 to vote on this title 1745.2 1874.4 0.001633 2060.7 4.2746 0.001816 useful 1892.9 Useful Not 2284.7 4.5896 0.002086 2055.1 2722.6 5.1762 0.002952 2393.2 3025.4 5.5563 0.003955 2664.6
1699 1843 2001 2180 2570 2901
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TABLAS DE PROPIEDADES, FIGURAS Y DIAGRAMAS (UNIDADES SI)
TABLA A-7 Agua líquida comprimida T °C
u kJ/kg
v
m3 /kg P
Sat. 0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340
0.0020378 0.0009904 0.0009929 0.0009992 0.0010084 0.0010199 0.0010337 0.0010496 0.0010679 0.0010886 0.0011122 0.0011390 0.0011697 0.0012053 0.0012472 0.0012978 0.0013611 0.0014450 0.0015693
s v kJ/kg K m3 /kg
5 MPa (263.94 C)
0.0012862 1148.1 1154.5 0.0009977 0.04 5.03 0.0009996 83.61 88.61 0.0010057 166.92 171.95 0.0010149 250.29 255.36 0.0010267 333.82 338.96 0.0010410 417.65 422.85 0.0010576 501.91 507.19 0.0010769 586.80 592.18 0.0010988 672.55 678.04 0.0011240 759.47 765.09 0.0011531 847.92 853.68 0.0011868 938.39 944.32 0.0012268 1031.6 1037.7 0.0012755 1128.5 1134.9
P Sat. 0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340
h kJ/kg
P 2.9207 0.0001 0.2954 0.5705 0.8287 1.0723 1.3034 1.5236 1.7344 1.9374 2.1338 2.3251 2.5127 2.6983 2.8841
20 MPa (365.75 C) 1785.8 0.23 82.71 165.17 247.75 330.50 413.50 496.85 580.71 665.28 750.78 837.49 925.77 1016.1 1109.0 1205.6 1307.2 1416.6 1540.2
1826.6 20.03 102.57 185.16 267.92 350.90 434.17 517.84 602.07 687.05 773.02 860.27 949.16 1040.2 1134.0 1231.5 1334.4 1445.5 1571.6
u kJ/kg
4.0146 0.0005 0.2921 0.5646 0.8208 1.0627 1.2920 1.5105 1.7194 1.9203 2.1143 2.3027 2.4867 2.6676 2.8469 3.0265 3.2091 3.3996 3.6086
0.0014522 0.0009952 0.0009973 0.0010035 0.0010127 0.0010244 0.0010385 0.0010549 0.0010738 0.0010954 0.0011200 0.0011482 0.0011809 0.0012192 0.0012653 0.0013226 0.0013980
h kJ/kg
s v kJ/kg K m3 /kg
10 MPa (311.00 C) 1393.3 0.12 83.31 166.33 249.43 332.69 416.23 500.18 584.72 670.06 756.48 844.32 934.01 1026.2 1121.6 1221.8 1329.4
1407.9 10.07 93.28 176.37 259.55 342.94 426.62 510.73 595.45 681.01 767.68 855.80 945.82 1038.3 1134.3 1235.0 1343.3
3.3603 0.0003 0.2943 0.5685 0.8260 1.0691 1.2996 1.5191 1.7293 1.9316 2.1271 2.3174 2.5037 2.6876 2.8710 3.0565 3.2488
u kJ/kg P
0.0016572 0.0009928 0.0009951 0.0010013 0.0010105 0.0010221 0.0010361 0.0010522 0.0010708 0.0010920 0.0011160 0.0011435 0.0011752 0.0012121 0.0012560 0.0013096 0.0013783 0.0014733 0.0016311
30 MPa You're PReading a Preview
h kJ/kg
15 MPa (342.16 C) 1585.5 0.18 83.01 165.75 248.58 331.59 414.85 498.50 582.69 667.63 753.58 840.84 929.81 1021.0 1115.1 1213.4 1317.6 1431.9 1567.9
P
1610.3 15.07 97.93 180.77 263.74 346.92 430.39 514.28 598.75 684.01 770.32 858.00 947.43 1039.2 1134.0 1233.0 1338.3 1454.0 1592.4
0.5 0.8 1.0 1.2 1.5 1.7 1.9 2.1 2.3 2.4
50 MPa
0.0009857 0.29 with 29.86 0.0009767 0.29 Unlock full access a free0.0003 trial. 0.0009886 82.11 111.77 0.2897 0.0009805 80.93 0.0009951 164.05 193.90 0.5607 0.0009872 161.90 0.0010042 246.14 276.26 0.8156 0.0009962 243.08 Download With Free Trial 0.0010155 328.40 358.86 1.0564 0.0010072 324.42 0.0010290 410.87 441.74 1.2847 0.0010201 405.94 0.0010445 493.66 525.00 1.5020 0.0010349 487.69 0.0010623 576.90 608.76 1.7098 0.0010517 569.77 0.0010823 660.74 693.21 1.9094 0.0010704 652.33 0.0011049 745.40 778.55 2.1020 0.0010914 735.49 0.0011304 831.11 865.02 2.2888 0.0011149 819.45 0.0011595 918.15 952.93 2.4707 0.0011412 904.39 0.0011927 1006.9 1042.7 2.6491 0.0011708 990.55 Sign up to vote on this title 0.0012314 1097.8 1134.7 2.8250 0.0012044 1078.2 0.0012770 1191.5 1229.8 3.0001 Useful0.0012430 Not 1167.7 useful 0.0013322 1288.9 1328.9 3.1761 0.0012879 1259.6 0.0014014 1391.7 1433.7 3.3558 0.0013409 1354.3 0.0014932 1502.4 1547.1 3.5438 0.0014049 1452.9
s kJ/k
49.13 129.95 211.25 292.88 374.78 456.94 539.43 622.36 705.85 790.06 875.19 961.45 1049.1 1138.4 1229.9 1324.0 1421.4 1523.1
0. 0.5 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.2 2.4
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TABLA A-8 Hielo saturado. Vapor de agua Volumen especfico, m 3 /kg
Energa interna, kJ/kg
Pres. Temp., sat.,
Hielo sat,
Vapor sat.,
Hielo sat.,
T °C
P sat kPa
v i
v g
u i
0.01 0 2 4 6 8 10 12 14 16 18 20 22 24 26 28 30 32 34 36 38 40
0.61169 0.61115 0.51772 0.43748 0.36873 0.30998 0.25990 0.21732 0.18121 0.15068 0.12492 0.10326 0.08510 0.06991 0.05725 0.04673 0.03802 0.03082 0.02490 0.02004 0.01608 0.01285
0.001091 0.001091 0.001091 0.001090 0.001090 0.001090 0.001089 0.001089 0.001088 0.001088 0.001088 0.001087 0.001087 0.001087 0.001087 0.001086 0.001086 0.001086 0.001085 0.001085 0.001085 0.001084
205.99 206.17 241.62 283.84 334.27 394.66 467.17 554.47 659.88 787.51 942.51 1131.3 1362.0 1644.7 1992.2 2421.0 2951.7 3610.9 4432.4 5460.1 6750.5 8376.7
333.40
Entalpa, kJ/kg
Subl.,
Vapor sat.,
Hielo sat.,
u ig
u g
h i
2707.9 2374.5 333.40 333.43 2707.9 2374.5 333.43 337.63 2709.4 2371.8 337.63 341.80 2710.8 2369.0 341.80 345.94 2712.2 2366.2 345.93 350.04 2713.5 2363.5 350.04 354.12 2714.8 2360.7 354.12 358.17 2716.1 2357.9 358.17 362.18 2717.3 2355.2 362.18 366.17 2718.6 2352.4 366.17 370.13 2719.7 2349.6 370.13 374.06 2720.9 2346.8 374.06 377.95 2722.0 2344.1 377.95 381.82 2723.1 2341.3 381.82 385.66 2724.2 2338.5 385.66 389.47 2725.2 2335.7 389.47 393.25 2726.2 2332.9 393.25 397.00 2727.2 2330.2 397.00 a Preview 400.72 Reading 2728.1 2327.4 You're 400.72 404.40 2729.0 2324.6 404.40 408.07full2729.9 2321.8 408.07 Unlock access with a free trial. 411.70 2730.7 2319.0 411.70
Entro kJ/kg
Subl.,
Vapor sat.,
Hielo sat.,
h ig
h g
s i
2833.9 2833.9 2834.5 2835.0 2835.4 2835.8 2836.2 2836.6 2836.9 2837.2 2837.5 2837.7 2837.9 2838.1 2838.2 2838.3 2838.4 2838.4 2838.5 2838.4 2838.4 2838.3
2500.5 2500.5 2496.8 2493.2 2489.5 2485.8 2482.1 2478.4 2474.7 2471.0 2467.3 2463.6 2459.9 2456.2 2452.5 2448.8 2445.1 2441.4 2437.7 2434.0 2430.3 2426.6
1.2202 1.2204 1.2358 1.2513 1.2667 1.2821 1.2976 1.3130 1.3284 1.3439 1.3593 1.3748 1.3903 1.4057 1.4212 1.4367 1.4521 1.4676 1.4831 1.4986 1.5141 1.5296
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