Tablas de Propiedades - TEAT01.pdf

  • Upload
    ludlega

  • View
    23

  • Download
    0

Embed Size (px)

Citation preview

  • TABLAS TERMODINMICA 2 PGINA 1

    TABLAS DE PROPIEDADES

    ANLISIS TERMODINMICO DEL MOTOR

    Recopilado por:

    Rodrigo Parra Bruna.

  • TABLAS TERMODINMICA 2 PGINA 2

    T01M Masas atmicas o moleculares y propiedades crticas de elementos y compuestos comunes. M (kg/kmol) TC (K) PC (bar)

    SUSTANCIA Frmula qumica M TC PC

    Acetileno C2H2 26,04 309 62,8 Agua H2O 18,02 647,3 220,9 Aire 28,97 133 37,7 Amoniaco NH3 17,04 406 112,8 Argn Ar 39,94 151 48,6 Benceno C6H6 78,11 563 49,3 Butano C4H10 58,12 425 38,0 Carbono C 12,01 Cobre Cu 63,54 Dixido de azufre SO2 64,06 431 78,7 Dixido de carbono CO2 44,01 304 73,9 Etano C2H6 30,07 305 48,8 Etanol C2H5OH 46,07 516 63,8 Etileno C2H4 28,05 283 51,2 Helio He 4,003 5,2 2,3 Hidrgeno H2 2,018 33,2 13,0 Metano CH4 16,04 191 46,4 Metanol CH3OH 32,05 513 79,5 Monxido de carbono CO 28,01 133 35,0 Nitrgeno N2 28,01 126 33,9 Octano C8H18 114,22 569 24,9 Oxgeno O2 32 154 50,5 Propano C3H8 44,09 370 42,7 Propileno C3H6 42,08 365 46,2 R12 CCl2F2 120,92 385 41,2 R134a CF3CH2F 102,03 374 40,7

    Fuentes: Adaptado de International Critical Tables y L.C. Nelson y E.F. Obert, Generalized Compressibility Charts, Chem. Eng., 61:203 (1954)

  • TABLAS TERMODINMICA 2 PGINA 3

    T02M Entalpa especfica del nitrgeno (N2), como gas ideal.

    T (K) h (kJ/kmol) 0

    fh = 0 kJ/kmol

    T

    h

    T

    h

    T

    h

    T

    h

    0 0 600 17.563 1.000 30.129 1.800 57.651

    220 6.391 610 17.864 1.020 30.784 1.820 58.363 230 6.683 620 18.166 1.040 31.442 1.840 59.075 240 6.975 630 18.468 1.060 32.101 1.860 59.790 250 7.266 640 18.772 1.080 32.762 1.880 60.504 260 7.558 650 19.075 1.100 33.426 1.900 61.220 270 7.849 660 19.380 1.120 34.092 1.920 61.936 280 8.141 670 19.685 1.140 34.760 1.940 62.654 290 8.432 680 19.991 1.160 35.430 1.960 63.381 298 8.669 690 20.297 1.180 36.104 1.980 64.090

    300 8.723 700 20.604 1.200 36.777 2.000 64.810 310 9.014 710 20.912 1.220 37.452 2.050 66.612 320 9.306 720 21.220 1.240 38.129 2.100 68.417 330 9.597 730 21.529 1.260 38.807 2.150 70.226 340 9.888 740 21.839 1.280 39.488 2.200 72.040 350 10.180 750 22.149 1.300 40.170 2.250 73.856 360 10.471 760 22.460 1.320 40.853 2.300 75.676 370 10.763 770 22.772 1.340 41.539 2.350 77.496 380 11.055 780 23.085 1.360 42.227 2.400 79.320 390 11.347 790 23.398 1.380 42.915 2.450 81.149

    400 11.640 800 23.714 1.400 43.605 2.500 82.981 410 11.932 810 24.027 1.420 44.295 2.550 84.814 420 12.225 820 24.342 1.440 44.988 2.600 86.650 430 12.518 830 24.658 1.460 45.682 2.650 88.488 440 12.811 840 24.974 1.480 46.377 2.700 90.328 450 13.105 850 25.292 1.500 47.073 2.750 92.171 460 13.399 860 25.610 1.520 47.771 2.800 94.014 470 13.693 870 25.928 1.540 48.470 2.850 95.859 480 13.988 880 26.248 1.560 49.168 2.900 97.705 490 14.285 890 26.568 1.580 49.869 2.950 99.556

    500 14.581 900 26.890 1.600 50.571 3.000 101.407 510 14.876 910 27.210 1.620 51.275 3.050 103.260 520 15.172 920 27.532 1.640 51.980 3.100 105.115 530 15.469 930 27.854 1.660 52.686 3.150 106.972 540 15.766 940 28.178 1.680 53.393 3.200 108.830 550 16.064 950 28.501 1.700 54.099 3.250 110.690 560 16.363 960 28.826 1.720 54.807 570 16.662 970 29.151 1.740 55.516 580 16.962 980 29.476 1.760 56.227 590 17.262 990 29.803 1.780 56.938

  • TABLAS TERMODINMICA 2 PGINA 4

    T03M Entalpa especfica del oxgeno (O2), como gas ideal.

    T (K) h (kJ/kmol) 0

    fh = 0 kJ/kmol

    T

    h

    T

    h

    T

    h

    T

    h

    0 0 600 17.929 1.000 31.389 1.800 60.371

    220 6.404 610 18.250 1.020 32.088 1.820 61.118 230 6.694 620 18.572 1.040 32.789 1.840 61.866 240 6.984 630 18.895 1.060 33.490 1.860 62.616 250 7.275 640 19.219 1.080 34.194 1.880 63.365 260 7.566 650 19.544 1.100 34.899 1.900 64.116 270 7.858 660 19.870 1.120 35.606 1.920 64.868 280 8.150 670 20.197 1.140 36.314 1.940 65.620 290 8.443 680 20.524 1.160 37.023 1.960 66.374 298 8.682 690 20.854 1.180 37.734 1.980 67.127

    300 8.736 700 21.184 1.200 38.447 2.000 67.881 310 9.030 710 21.514 1.220 39.162 2.050 69.772 320 9.325 720 21.845 1.240 39.877 2.100 71.668 330 9.620 730 22.177 1.260 40.594 2.150 73.573 340 9.916 740 22.510 1.280 41.312 2.200 75.484 350 10.213 750 22.844 1.300 42.033 2.250 77.397 360 10.511 760 23.178 1.320 42.753 2.300 79.316 370 10.809 770 23.513 1.340 43.475 2.350 81.243 380 11.109 780 23.850 1.360 44.198 2.400 83.174 390 11.409 790 24.186 1.380 44.923 2.450 85.112

    400 11.711 800 24.523 1.400 45.648 2.500 87.057 410 12.012 810 24.861 1.420 46.374 2.550 89.004 420 12.314 820 25.199 1.440 47.102 2.600 90.956 430 12.618 830 25.537 1.460 47.831 2.650 92.916 440 12.923 840 25.877 1.480 48.561 2.700 94.881 450 13.228 850 26.218 1.500 49.292 2.750 96.852 460 13.535 860 26.559 1.520 50.024 2.800 98.826 470 13.842 870 26.899 1.540 50.756 2.850 100.808 480 14.151 880 27.242 1.560 51.490 2.900 102.793 490 14.460 890 27.584 1.580 52.224 2.950 104.785

    500 14.770 900 27.928 1.600 52.961 3.000 106.780 510 15.082 910 28.272 1.620 53.696 3.050 108.778 520 15.395 920 28.616 1.640 54.434 3.100 110.784 530 15.708 930 28.960 1.660 55.172 3.150 112.795 540 16.022 940 29.306 1.680 55.912 3.200 114.809 550 16.338 950 29.652 1.700 56.652 3.250 116.827 560 16.654 960 29.999 1.720 57.394 570 16.971 970 30.345 1.740 58.136 580 17.290 980 30.692 1.760 58.880 590 17.609 990 31.041 1.780 59.624

  • TABLAS TERMODINMICA 2 PGINA 5

    T04M Entalpa especfica del vapor de agua (H2O), como gas ideal.

    T (K) h (kJ/kmol) 0

    fh = 241.820 kJ/kmol

    T

    h

    T

    h

    T

    h

    T

    h

    0 0 600 20.402 1.000 35.882 1.800 72.513

    220 7.295 610 20.765 1.020 36.709 1.820 73.507 230 7.628 620 21.130 1.040 37.542 1.840 74.506 240 7.961 630 21.495 1.060 38.380 1.860 75.506 250 8.294 640 21.862 1.080 39.223 1.880 76.511 260 8.627 650 22.230 1.100 40.071 1.900 77.517 270 8.961 660 22.600 1.120 40.923 1.920 78.527 280 9.296 670 22.970 1.140 41.780 1.940 79.540 290 9.631 680 23.342 1.160 42.642 1.960 80.555 298 9.904 690 23.714 1.180 43.509 1.980 81.573

    300 9.966 700 24.088 1.200 44.380 2.000 82.593 310 10.302 710 24.464 1.220 45.256 2.050 85.156 320 10.639 720 24.840 1.240 46.137 2.100 87.735 330 10.976 730 25.218 1.260 47.022 2.150 90.330 340 11.314 740 25.597 1.280 47.912 2.200 92.940 350 11.652 750 25.977 1.300 48.807 2.250 95.562 360 11.992 760 26.358 1.320 49.707 2.300 98.199 370 12.331 770 26.741 1.340 50.612 2.350 100.846 380 12.672 780 27.125 1.360 51.521 2.400 103.508 390 13.014 790 27.510 1.380 52.434 2.450 106.183

    400 13.356 800 27.896 1.400 53.351 2.500 108.868 410 13.699 810 28.284 1.420 54.273 2.550 111.565 420 14.043 820 28.672 1.440 55.198 2.600 114.273 430 14.388 830 29.062 1.460 56.128 2.650 116.991 440 14.734 840 29.454 1.480 57.062 2.700 119.717 450 15.080 850 29.846 1.500 57.999 2.750 122.453 460 15.428 860 30.240 1.520 58.942 2.800 125.198 470 15.777 870 30.635 1.540 59.888 2.850 127.952 480 16.126 880 31.032 1.560 60.838 2.900 130.717 490 16.477 890 31.429 1.580 61.792 2.950 133.486

    500 16.828 900 31.828 1.600 62.748 3.000 136.264 510 17.181 910 32.228 1.620 63.709 3.050 139.051 520 17.534 920 32.629 1.640 64.675 3.100 141.846 530 17.889 930 33.032 1.660 65.643 3.150 144.648 540 18.245 940 33.436 1.680 66.614 3.200 147.457 550 18.601 950 33.841 1.700 67.589 3.250 150.272 560 18.959 960 34.247 1.720 68.567 570 19.318 970 34.653 1.740 69.550 580 19.678 980 35.061 1.760 70.535 590 20.039 990 35.472 1.780 71.523

  • TABLAS TERMODINMICA 2 PGINA 6

    T05M Entalpa especfica del monxido de carbono (CO), como gas ideal.

    T (K) h (kJ/kmol) 0

    fh = 110.530 kJ/kmol

    T

    h

    T

    h

    T

    h

    T

    h

    0 0 600 17.611 1.000 30.355 1.800 58.191

    220 6.391 610 17.915 1.020 31.020 1.820 58.910 230 6.683 620 18.221 1.040 31.688 1.840 59.629 240 6.975 630 18.527 1.060 32.357 1.860 60.351 250 7.266 640 18.833 1.080 33.029 1.880 61.072 260 7.558 650 10.141 1.100 33.702 1.900 61.794 270 7.849 660 19.449 1.120 34.377 1.920 62.516 280 8.140 670 19.758 1.140 35.054 1.940 63.238 290 8.432 680 20.068 1.160 35.733 1.960 63.961 298 8.669 690 20.378 1.180 36.406 1.980 64.684

    300 8.723 700 20.690 1.200 37.095 2.000 65.408 310 9.014 710 21.002 1.220 37.780 2.050 67.224 320 9.306 720 21.315 1.240 38.466 2.100 69.044 330 9.597 730 21.628 1.260 39.154 2.150 70.864 340 9.889 740 21.943 1.280 39.884 2.200 72.688 350 10.181 750 22.258 1.300 40.534 2.250 74.516 360 10.473 760 22.573 1.320 41.266 2.300 76.345 370 10.765 770 22.890 1.340 41.919 2.350 78.178 380 11.058 780 23.208 1.360 42.613 2.400 80.015 390 11.351 790 23.526 1.380 43.309 2.450 81.852

    400 11.644 800 23.844 1.400 44.007 2.500 83.692 410 11.938 810 24.164 1.420 44.707 2.550 85.537 420 12.232 820 24.483 1.440 45.408 2.600 87.383 430 12.526 830 24.803 1.460 46.110 2.650 89.230 440 12.821 840 25.124 1.480 46.813 2.700 91.077 450 13.116 850 25.446 1.500 47.517 2.750 92.930 460 13.412 860 25.768 1.520 48.222 2.800 94.784 470 13.708 870 26.091 1.540 48.928 2.850 96.639 480 14.005 880 26.415 1.560 49.635 2.900 98.495 490 14.302 890 26.740 1.580 50.344 2.950 100.352

    500 14.600 900 27.066 1.600 51.053 3.000 102.210 510 14.898 910 27.392 1.620 51.763 3.050 104.073 520 15.197 920 27.719 1.640 52.472 3.100 105.939 530 15.497 930 28.046 1.660 53.184 3.150 107.802 540 15.797 940 28.375 1.680 53.895 3.200 109.667 550 16.097 950 28.703 1.700 54.609 3.250 111.534 560 16.399 960 29.033 1.720 55.323 570 16.701 970 29.362 1.740 56.039 580 17.003 980 29.693 1.760 56.756 590 17.307 990 30.024 1.780 57.473

  • TABLAS TERMODINMICA 2 PGINA 7

    T06M Entalpa especfica del dixido de carbono (CO2), como gas ideal.

    T (K) h (kJ/kmol) 0

    fh = 393.520 kJ/kmol

    T

    h

    T

    h

    T

    h

    T

    h

    0 0 600 22.280 1.000 42.769 1.800 88.806

    220 6.601 610 22.754 1.020 43.859 1.820 90.000 230 6.938 620 23.231 1.040 44.953 1.840 91.196 240 7.280 630 23.709 1.060 46.051 1.860 92.394 250 7.627 640 24.190 1.080 47.153 1.880 93.593 260 7.979 650 24.674 1.100 48.258 1.900 94.793 270 8.335 660 25.160 1.120 49.369 1.920 95.995 280 8.697 670 25.648 1.140 50.484 1.940 97.197 290 9.063 680 26.138 1.160 51.602 1.960 98.401 298 9.364 690 26.631 1.180 52.724 1.980 99.606

    300 9.431 700 27.125 1.200 53.848 2.000 100.804 310 9.807 710 27.622 1.220 54.977 2.050 103.835 320 10.186 720 28.121 1.240 56.108 2.100 106.864 330 10.570 730 28.622 1.260 57.244 2.150 109.898 340 10.959 740 29.124 1.280 58.381 2.200 112.939 350 11.351 750 29.629 1.300 59.522 2.250 115.984 360 11.748 760 30.135 1.320 60.666 2.300 119.035 370 12.148 770 30.644 1.340 61.813 2.350 122.091 380 12.552 780 31.154 1.360 62.963 2.400 125.152 390 12.960 790 31.665 1.380 64.116 2.450 128.219

    400 13.372 800 32.179 1.400 65.271 2.500 131.290 410 13.787 810 32.694 1.420 66.427 2.550 134.368 420 14.206 820 33.212 1.440 67.586 2.600 137.449 430 14.628 830 33.730 1.460 68.748 2.650 140.533 440 15.054 840 34.251 1.480 69.911 2.700 143.620 450 15.483 850 34.773 1.500 71.078 2.750 146.713 460 15.916 860 35.296 1.520 72.246 2.800 149.808 470 16.351 870 35.821 1.540 73.417 2.850 152.908 480 16.791 880 36.347 1.560 74.590 2.900 156.009 490 17.232 890 36.876 1.580 76.767 2.950 159.117

    500 17.678 900 37.405 1.600 76.944 3.000 162.226 510 18.126 910 37.935 1.620 78.123 3.050 165.341 520 18.576 920 38.467 1.640 79.303 3.100 168.456 530 19.029 930 39.000 1.660 80.486 3.150 171.576 540 19.485 940 39.535 1.680 81.670 3.200 174.695 550 19.945 950 40.070 1.700 82.856 3.250 177.822 560 20.407 960 40.607 1.720 84.043 570 20.870 970 41.145 1.740 85.231 580 21.337 980 41.685 1.760 86.420 590 21.807 990 42.226 1.780 87.612

  • TABLAS TERMODINMICA 2 PGINA 8

    T07M Entalpa especfica del hidrgeno (H2), como gas ideal.

    T (K) h (kJ/kmol) 0

    fh = 0 kJ/kmol

    T

    h

    T

    h

    0 0 1.440 42.808

    260 7.370 1.480 44.091 270 7.657 1.520 45.384 280 7.945 1.560 46.683 290 8.233 1.600 47.990 298 8.468 1.640 49.303 300 8.522 1.680 50.662 320 9.100 1.720 51.947 340 9.680 1.760 53.279 360 10.262 1.800 54.618

    380 10.843 1.840 55.962 400 11.426 1.880 57.311 420 12.010 1.920 58.668 440 12.594 1.960 60.031 460 13.179 2.000 61.400 480 13.764 2.050 63.119 500 14.350 2.100 64.847 520 14.935 2.150 66.584 560 16.107 2.200 68.328 600 17.280 2.250 70.080

    640 18.453 2.300 71.839 680 19.630 2.350 73.608 720 20.807 2.400 75.383 760 21.988 2.450 77.168 800 23.171 2.500 78.960 840 24.359 2.550 80.755 880 25.551 2.600 82.558 920 26.747 2.650 84.386 960 27.948 2.700 86.186

    1.000 29.154 2.750 88.008

    1.040 30.364 2.800 89.838 1.080 31.580 2.850 91.671 1.120 32.802 2.900 93.512 1.160 34.028 2.950 95.358 1.200 35.262 3.000 97.211 1.240 36.502 3.050 99.065 1.280 37.749 3.100 100.926 1.320 39.002 3.150 102.793 1.360 40.263 3.200 104.667 1.400 41.530 3.250 106.545

  • TABLAS TERMODINMICA 2 PGINA 9

    T08M Entalpa de formacin para diversas sustancias a 298 K y 1 atm.

    0

    fh (kJ/kmol)

    SUSTANCIA Frmula qumica 0

    fh

    Carbono C (s) 0 Hidrgeno H2 (g) 0 Nitrgeno N2 (g) 0 Oxgeno O2 (g) 0 Monxido de carbono CO (g) 110.530 Dixido de carbono CO2 (g) 393.520 Agua H2O (g) 241.820 Agua H2O (l) 285.830 Perxido de hidrgeno H2O2 (g) 136.310 Amoniaco NH3 (g) 46.190 Oxgeno O (g) 249.170 Hidrgeno H (g) 218.000 Nitrgeno N (g) 472.680 Grupo oxidrilo OH (g) 39.460 Metano CH4 (g) 74.850 Acetileno C2H2 (g) 226.730 Etileno C2H4 (g) 52.280 Etano C2H6 (g) 84.680 Propileno C3H6 (g) 20.410 Propano C3H8 (g) 103.850 Butano C4H10 (g) 126.150 Pentano C5H12 (g) 146.440 Octano C8H18 (g) 208.450 Octano C8H18 (l) 249.910 Benceno C6H6 (g) 82.930 Metanol CH3OH (g) 200.890 Metanol CH3OH (l) 238.810 Etanol C2H5OH (g) 235.310 Etanol C2H5OH (l) 277.690 Dodecano C12H26 (l) 374.865

    Fuentes: Adaptado de K. Wark, Thermodyynamics, 4th ed., McGraw-Hill, 1983, basadas en JANAF Thermochemical Tables, NSRDS-NBS-37, 1971; Selected Values of Chemical Thermodynamic Properties, NBS Tech. Note 270-3, 1968; y API Research Project 44, Carnegie Press, 1953.

  • TABLAS TERMODINMICA 2 PGINA 10

    T09M Coeficientes conductivos y convectivos de elementos y compuestos comunes.

    MATERIAL Coeficiente conductivo (k)

    (W/mC)

    Aluminio 237 Cobre 401 Acero al carbn (ANSI 1.010) 60,5 Bronce comercial 52 Ladrillo comn 0,72 Fibra de vidrio 0,038 Espuma de lana mineral 0,046 Concreto 0,67 Asfalto 0,062 Vidrio 1,4 Hielo 1,88 Cuero 0,159 Papel 0,18 Mrmol 2,8 Caucho vulcanizado suave 0,13 Caucho vulcanizado duro 0,16 Tefln 0,35 Madera de roble 0,17 Madera de pino blanco 0,11 Madera de ciprs 0,097

    MEDIO Coeficiente convectivo (h)

    (W/m2C)

    Conveccin natural, aire 5 25 Conveccin natural, agua 20 100 Conveccin forzada, aire 10 200 Conveccin forzada, agua 50 10.000

  • TABLAS TERMODINMICA 2 PGINA 11

    T10M Propiedades del agua (H2O) saturada

    (kg/m3) CP (J/kgC) k (W/mC)

    Temp. C

    Presin kPa

    Densidad absoluta () Calor especfico

    (CP) Conductividad trmica

    (k)

    Lquido Sat.

    Vapor Sat.

    Lquido Sat.

    Vapor Sat.

    Lquido Sat.

    Vapor Sat.

    0,01 0,6113 999,8 0,0048 4.217 1.854 0,561 0,0171 5 0,8721 999,9 0,0068 4.205 1.857 0,571 0,0173 10 1,2276 999,7 0,0094 4.194 1.862 0,580 0,0176 15 1,7051 999,1 0,0128 4.186 1.863 0,589 0,0179 20 2,339 998,0 0,0173 4.182 1.867 0,598 0,0182 25 3,169 997,0 0,0231 4.180 1.870 0,607 0,0186 30 4,246 996,0 0,0304 4.178 1.875 0,615 0,0189 35 5,628 994,0 0,0397 4.178 1.880 0,623 0,0192 40 7,384 992,1 0,0512 4.179 1.885 0,631 0,0196 45 9,593 990,1 0,0655 4.180 1.892 0,637 0,0200

    50 12,35 988,1 0,0831 4.181 1.900 0,644 0,0204 55 15,76 985,2 0,1045 4.183 1.908 0,649 0,0208 60 19,94 983,3 0,1304 4.185 1.916 0,654 0,0212 65 25,03 980,4 0,1614 4.187 1.926 0,659 0,0216 70 31,19 977,5 0,1983 4.190 1.936 0,663 0,0221 75 38,58 974,7 0,2421 4.193 1.948 0,667 0,0225 80 47,39 971,8 0,2935 4.197 1.962 0,670 0,0230 85 57,83 968,1 0,3536 4.201 1.977 0,673 0,0235 90 70,14 965,3 0,4235 4.206 1.993 0,675 0,0240 95 84,55 961,5 0,5045 4.212 2.010 0,677 0,0246 100 101,33 957,9 0,5978 4.217 2.029 0,679 0,0251

    110 143,27 950,6 0,8263 4.229 2.071 0,682 0,0262 120 198,53 943,4 1,121 4.244 2.120 0,683 0,0275 130 270,1 934,6 1,496 4.263 2.177 0,684 0,0288 140 361,3 921,7 1,965 4.286 2.244 0,683 0,0301 150 475,8 916,6 2,546 4.311 2.314 0,682 0,0316 160 617,8 907,4 3,256 4.340 2.420 0,680 0,0331 170 791,7 897,7 4,119 4.370 2.490 0,677 0,0347 180 1.002,1 887,3 5,153 4.410 2.590 0,673 0,0364 190 1.254,4 876,4 6,388 4.460 2.710 0,669 0,0382 200 1.553,8 864,3 7,852 4.500 2.840 0,663 0,0401

    220 2.318 840,3 11,60 4.610 3.110 0,650 0,0442 240 3.344 813,7 16,73 4.760 3.520 0,632 0,0487 260 4.688 783,7 23,69 4.970 4.070 0,609 0,0540 280 6.412 750,8 33,15 5.280 4.835 0,581 0,0605 300 8.581 713,8 46,15 5.750 5.980 0,548 0,0695 320 11.274 667,1 54,57 6.540 7.900 0,509 0,0835 340 14.586 610,5 92,62 8.240 11.870 0,469 0,110 360 18.651 528,3 144,0 14.690 25.800 0,427 0,178

    374,14 22.090 317,0 317,0 ------ ----- ----- -----

  • TABLAS TERMODINMICA 2 PGINA 12

    T11M Propiedades del agua (H2O) saturada

    (kg/ms) Pr (1)

    Temp.

    C

    Presin kPa

    Viscosidad dinmica ()

    Nmero de Prandtl (Pr)

    Lquido Sat.

    Vapor Sat.

    Lquido Sat.

    Vapor Sat.

    0,01 0,6113 1,792103

    0,922105

    13,5 1,00

    5 0,8721 1,619103

    0,934105

    11,2 1,00

    10 1,2276 1,307103

    0,946105

    9,45 1,00

    15 1,7051 1,138103

    0,959105

    8,09 1,00

    20 2,339 1,002103

    0,973105

    7,01 1,00

    25 3,169 0,891103

    0,987105

    6,14 1,00

    30 4,246 0,798103

    1,001105

    5,42 1,00

    35 5,628 0,720103

    1,016105

    4,83 1,00

    40 7,384 0,653103

    1,031105

    4,32 1,00

    45 9,593 0,596103

    1,046105

    3,91 1,00

    50 12,35 0,547103

    1,062105

    3,55 1,00

    55 15,76 0,504103

    1,077105

    3,25 1,00

    60 19,94 0,467103

    1,093105

    2,99 1,00

    65 25,03 0,433103

    1,110105

    2,75 1,00

    70 31,19 0,404103

    1,126105

    2,55 1,00

    75 38,58 0,378103

    1,142105

    2,38 1,00

    80 47,39 0,355103

    1,159105

    2,22 1,00

    85 57,83 0,333103

    1,175105

    2,08 1,00

    90 70,14 0,315103

    1,193105

    1,96 1,00

    95 84,55 0,297103

    1,210105

    1,85 1,00

    100 101,33 0,282103

    1,227105

    1,75 1,00

    110 143,27 0,255103

    1,261105

    1,58 1,00

    120 198,53 0,232103

    1,296105

    1,44 1,00

    130 270,1 0,213103

    1,330105

    1,33 1,01

    140 361,3 0,197103

    1,365105

    1,24 1,02

    150 475,8 0,183103

    1,399105

    1,16 1,02

    160 617,8 0,170103

    1,434105

    1,09 1,05

    170 791,7 0,160103

    1,468105

    1,03 1,05

    180 1.002,1 0,150103

    1,502105

    0,983 1,07

    190 1.254,4 0,142103

    1,537105

    0,947 1,09

    200 1.553,8 0,134103

    1,571105

    0,910 1,11

    220 2.318 0,122103

    1,641105

    0,865 1,15

    240 3.344 0,111103

    1,712105

    0,836 1,24

    260 4.688 0,102103

    1,788105

    0,832 1,35

    280 6.412 0,094103

    1,870105

    0,854 1,49

    300 8.581 0,086103

    1,965105

    0,902 1,69

    320 11.274 0,078103

    2,084105

    1,00 1,97

    340 14.586 0,070103

    2,255105

    1,23 2,43

    360 18.651 0,060103

    2,571105

    2,06 3,73

    374,14 22.090 0,043103

    4,313105

    ----- -----

  • TABLAS TERMODINMICA 2 PGINA 13

    T12M Propiedades de lquidos (kg/m

    3) CP (J/kgC) k (W/mC) (kg/ms) (m

    2/s) Pr (1)

    Temp. C

    Densidad

    absoluta ()

    Calor especfico

    (CP)

    Conductividad trmica (k)

    Viscosidad dinmica ()

    Viscosidad cinemtica

    ()

    Nmero de

    Prandtl (Pr)

    METANO (CH4)

    150 405,0 3.580 0,1703 9,169105

    2,264107

    1,927

    140 388,8 3.700 0,1550 7,551105

    1,942107

    1,803

    130 371,1 3.875 0,1402 6,288105

    1,694107

    1,738

    120 351,4 4.146 0,1258 5,257105

    1,496107

    1,732

    110 328,8 4.611 0,1115 4,377105

    1,331107

    1,810

    100 301,0 5.578 0,0967 3,577105

    1,188107

    2,063

    90 261,7 8.902 0,00797 2,761105

    1,055107

    3,082

    METANOL (C3H3OH)

    20 788,4 2.515 0,1987 5,857104

    7,429107

    7,414

    30 779,1 2.577 0,1980 5,088104

    6,531107

    6,622

    40 769,6 2.644 0,1972 4,460104

    5,795107

    5,980

    50 760,1 2.718 0,1965 3,942104

    5,185107

    5,453

    60 750,4 2.798 0,1957 3,510104

    4,677107

    5,018

    70 740,4 2.885 0,1950 3,146104

    4,250107

    4,655

    ISOBUTANO (R600a)

    100 683,8 1.881 0,1383 9,305104

    1,360106

    12,65

    75 659,3 1.970 0,1357 5,624104

    8,531107

    8,167

    50 634,3 2.069 0,1283 3,769104

    5,942107

    6,079

    25 608,2 2.180 0,1181 2,688104

    4,420107

    4,963

    0 580,6 2.306 0,1068 1,993104

    3,432107

    4.304

    25 550,7 2.455 0,0956 1,510104

    2,743107

    3,880

    50 517,3 2.640 0,0851 1,155104

    2,233107

    3,582

    75 478,5 2.896 0,0757 8,785105

    1,836107

    3,363

    100 429,6 3.361 0,0669 6,483105

    1,509107

    3,256

  • TABLAS TERMODINMICA 2 PGINA 14

    T12M Propiedades de lquidos (continuacin) (kg/m

    3) CP (J/kgC) k (W/mC) (kg/ms) (m

    2/s) Pr (1)

    Temp. C

    Densidad

    absoluta ()

    Calor especfico

    (CP)

    Conductividad trmica (k)

    Viscosidad dinmica ()

    Viscosidad cinemtica

    ()

    Nmero de

    Prandtl (Pr)

    GLICERINA

    0 1.276 2.262 0,2820 10,49 8,219103

    84.101

    5 1.273 2.288 0,2835 6,730 5,287103

    54.327

    10 1.270 2.320 0,2846 4,241 3,339103

    34.561

    15 1.267 2.354 0,2856 2,496 1,970103

    20.570

    20 1.264 2.386 0,2860 1,519 1,201103

    12.671

    25 1.261 2.416 0,2860 0,9934 7,878104

    8.392

    30 1.258 2.447 0,2860 0,6582 5,232104

    5.631

    35 1.255 2.478 0,2860 0,4347 3,464104

    3.767

    40 1.252 2.513 0,2863 0,3073 2,455104

    2.697

    ACEITE PARA MOTOR (nuevo)

    0 899,0 1.797 0,1469 3,814 4,242103

    46.636

    20 888,1 1.881 0,1450 0,8374 9,429104

    10.863

    40 876,0 1.964 0,1444 0,2177 2,485104

    2.962

    60 863,9 2.048 0,1404 0,07399 8,565105

    1.080

    80 852,0 2.132 0,1380 0,03232 3,794105

    499,3

    100 840,0 2.220 0,1367 0,01718 2,045105

    279,1

    120 828,9 2.308 0,1347 0,01029 1,241105

    176,3

    140 816,8 2.395 0,1330 0,006558 8,029106

    118,1

    150 810,3 2.441 0,1327 0,005344 6,595106

    98,31