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Tabla B.1 Datos selectos de propiedades fisicas“ Peso GE ART) AMT! (ARES (AfgiU Compuesto Fórmula molecular (20/49) TC) kJ/mol TAC)! KJ/mol TAKY Poatm)? kJ/mol kJ/mol Acetaldehido CH;CHO 44.05 0.78318º 123.7 - 20.2 25.1 461,0 = —166.2g) —1192.4(g) Acetato deetilo C4HsO, 88.10 0.901 —83.8 - 70 - 523.1 37.8 —463.2(1) -2246.4(1) -426.8(g) - Acetato de metilo C3H60> 74.08 0.933 -98.9 - 571 - 506.7 46.30 —409.4(1) —1595(1) Acetileno CH, 26.04 = - - -81.5 17.6 309.5 61.6 +226.75(g) —1299.6(g) Acetona CH 58.08 0.791 -95.0 5.69 56.0 30.2 508.0 47.0 -248.2(1) —1785.7(1) 216.78) -I8214(g) Ácido acético CH;COOH 60.05 1.049 16.6 12.09 118.2 24.39 594.8 571 —486.18(1) —871.69(1) -A38IS(g) 919.738) Ácido benzoico CjHçOs 122.12 1.266! 1222 = 249.8 + a es > -3226.7(g) Ácido fórmico CH,0, 46.03 1.220 830 12.68 100.5 22.25 = = -409.2(1) -262.8(1) -362.6(8) é Ácido fosfórico HsPO4 9800 183418 423 10.54 (-1H,04213º0) e = 28LI(O) e —1278.6(ac), - 1H,0 Ácido nítrico HNO; 63.02 1.502 41.6 10.47 86 30.30 - = —173.23(1) - -206.57(ac) Ácido oxálico CH04 90.04 1.90 Se descompone a 186ºC - -826.8(c) -251.9(s) Ácido sulfúrico HySOg 98.08 1.83418º 10.35 9.87 — Se descompone a 340ºC — - -811,32(1) - -907.51(ac) = Agua HO 18.016 1.00% 0.00 6.0095 100.00 40.656 6474 218.3 -285.84(1) = -241.83(g) E Alcohol bencílico C,HgO 108.13 1.045 -15.4 = 205.2 is - = - -3741.8(1) Alcohol etílico C,Hs50H 46.07 0.789 114.6 5.021 78.5 38.58 516,3 63.0 -277.631) —1366.91(1) (etanol) -23531(g) -1409.25(g) Alcohol C4H50H 60.09 0.785 —89.7 = 82.24 - 508.8 53.0 -310.9(1) —1986.6(1) isopropílico Alcohol metílico -CH;0H 32.04 0.792 —97.9 3.167 64.7 35.27 513.20 78.50 -238.6(1) 726.6(1) (metanol) -201.2g) —764.0(g) Alcohol C3Hs0H 60.09 0.804 -127 - 97.04 - 536.7 49.95 -300.70(1) -2010.4(1) n-propílico -255.2g) -2068.6(g) gopuody ze Amoniaco NH; EB = -n8 5653 3343 23351 4055 H13 67200) 46.192) — -382.58(g) Anilina CSH;N 93.12 1,022 -6.3 - 184.2 - 699 52.4 e Azufre Sg 256.53 1.96 n9 14.17 444.6 83.7 - = +0.30(c) - (monoclínico) Azufre Sg 256.53 2.07 "3 10.04 444.6 83.7 - - Mc) - (rómbico) Benceno CoH6 78.11 0.879 5.53 9.837 80.10 30.765 562.6 48.6 +48.66(1) -3267.6(1) +82.93g) -3301.5(g) Benzaldehido CoHsCHO 106.12 1.046 -26.0 - 179.0 38.40 - — -88.83(1) —3520.0(1) -40.04(g) = Bicarbonato de NaHCO; 84,01 2.20 Se descompone a 270ºC — E -945.6(0) = sodio Bisulfato de NaHSO, 120.07 2.742 - - - - - = —1126.3(c) a sodio Bromo Br; 159.83 3.119 —14 10.8 58.6 31.0 584 102 O(I) = Bromuro de etilo C,HsBr 108.98 1.460 =19.1 - 38.2 - 504 61.5 -54.4(g) - Bromuro de HBr 80.92 - -86 - -67 = ss es -36.23(g) - hidrógeno 1.2-butadieno CH6 54.09 - -136.5 - 10.1 = 446 = ER = 1.3-butadieno CH 54.09 - -109.1 - 4.6 - 425 427 - - n-butano CiHio 58.12 - -138.3 4.661 =0,6 22.305 425.17 3747 -147.0(]) —2855.6(1) -124.78) — -2878.5(g) 1-Buteno CaHg 56.10 - -185.3 3.8480 6.25 21.916 419.6 39.7 +LI7Mg) -2718.6(g) Carbonato de Caco; 100.09 2.93 Se descompone a 825ºC —1206.9(c) - calcio Carbonato de NayCO; 105.99 2.533 Se descompone a 854ºC = - —1130.9c) - sodio Carbono E 12.010 2.26 3600 46.0 4200 = - - O(c) -393.51(c) (grafito) Carburo de CaC, 64.10 2.2218º 2300 - = = - - —62.76(c) - calcio Cianuro de HCN 27.03 - -I4 - 26 - - - +130.54(g) - hidrógeno (continia) ££9 svoIsty sopepordosd op seigey Etano Éter dietílico 3-Etil hexano Etilbenceno Etilén glicol Etileno Fenol Fluoruro de hidrógeno Formaldehido Fosfato de calcio Fósforo (blanco) Fósforo (rojo) Glicerol Helio n-Heptano n-Hexano Hidrógeno Hierro Hidróxido de amonio Hidróxido de calcio Hidróxido de magnesio Hidróxido de sodio CH (C>Hs5)O CsHig CsHio CGHçO, CoHs CoHsOH HF HCO Cas(PO4) P4 Pq NH,0H Ca(0H) Mg(0H) NaoH 30.07 74.12 114.22 106.16 62.07 28.05 94.11 20.0 30.03 310.19 123.90 123.90 92.09 4.00 100.20 86.17 2.016 55.85 35.03 74.10 58.43 40.00 0.70825º 0.717 0.867 Boka LO712s 0.81520º 3.14 1.82 2.20 1.26050º 0.684 0.659 77 2.24 24 2.130 —183.3 -116.3 -94.67 =13 —169.2 42.5 =82: 1670 44.2 s908Batm 18.20 -269.7 -90.59 -95:32 —259.19 1535 319 2.859 7.30 9.163 11.23 3.350 11.43 2.51 8117 18.30 0.02 14.03 13.03 0.12 15.1 -88.6 14,72 305.4 34.6 26.05 467 118.5 34.27 567.0 136.2 35.98 619.7 197.2 56.9 EE —103.7 13.54 283.1 181.4 - 692.1 20 = 503.2 —19:3 24.48 - 280 49.71 - Se enciende con el aire, a 725ºC 290.0 - - -268.9 0.084 5.26 98.43 31.69 540.2 68.74 28.85 507.9 -252.76 0.904 333 2800 354.0 — (-H,0 A 580ºC) Se descompone a 350ºC€ 834 1390 - - 48.2 35.6 26.4 37.0 50.5 60.5 2.26 270 29.9 12.8 -84.67(g) =272.8(1) -250.5(1) -210.9(g) -12.46(1) +29.79(g) —451.5(1) -387.1(g) +52.28(g) -158.1(1) -90.8(g) -268.6(g) -316.9(ac, 200) —115.90(g) —4138(c) O(c) -665.9(1) Og) -224.4(1) -187.8(g) -198.8(1) -167.2g) Og) O(c) -366.48(ac) -986.59(€) -426.6() -469.4(ac) -1559.9(g) -2726.1(1) -5407.1(1) -5509.8(g) -45649(1) -4607.1(8) =1179.5(1) 1410.9948) -3063.5(8) -563.46(8) -17.6(c)- -1661.1(1) -4816.9(1) -4853.5(g) -4163.1(1) -4194.8(g) -285.84(g) (continia) seoIsIj sopepaidoid ap sejqer seo Tabla B.1 (Continuación.) Peso GE ABA Ta! ARUATO (AB (AfgiU Compuesto Fórmula molecular (20%4º) TiC) kJ/mol TAC)! KJ/mol TAK)! Poatm? kJ/mol kJ/mol Isobutano CH 58.12 - -159.6 4.540 11.73 21.292 408.1 36.0 -158.4(1) -2849.0(1) -134.5(g) -2868.8(g) Isopentano CsHia nas 062” 1601 ss 271 m 461.00 329º 73) 350750) E 15208) 352928) Magnesio Mg 24.32 1,74 650 EPA 1120 1318 - — O(c) so Mercurio Hg 200.61 13.546 -38.87 - -356.9 - - pi O(c) Ss Metano CH, 16.04 - -182.5 0.94 61.5 8.179 190.70 45.8 —74.85(g) -890.36(g) Metil amina CHSN 3106 69911" 927 - -69 429.9 7.60 -280g) I071.5(1) Metil etilcetona C,HçO 72.10 0.805 -87.1 - 78.2 32.0 = - = -2436(1) Monóxido de co 28.01 - -205.1 0.837 -191.5 6.042 133.0 34.5 —110.52(g) -282.99(g) carbono Naftaleno CiHg 128.16 1.145 80.0 sa 2178 = = ja E -5157(8) Níquel Ni 58.69 8.90 1452 = 2900 co = = O(c) - Nitrato de NH,NO; 80.05 178º 169.6 54 se descompone a 210ºC -365.14(c) - amonio -399.36(ac) - Nitrato de sodio NaNO; 85.00 2.257 310 15.9 Se descompone a 380ºC - -466.7(c) — Nitrito de sodio | NaNO; 69.00 2.1680º 271 - Se descompone a 320ºC - -359.4(c) - Nitrobenceno CoHs0,N 123.11 1.203 Ee) = 210.7 = - — - -3092.8(1) Nitrógeno N> 28.02 = -210.0 0.720 —195.8 5.577 126.20 33.5 Mg) - n-Nonano CoH0 128.25 0.718 —53.8 - 150.6 = 595 23.0 -229.0(1) -6124.5(1) -6171.0(g) n-Octano CsHig 114.22 0.703 -57.0 - 125.5 - 568.8 24.5 -249.9(1) -5470.7(1) -208.4(g) -5512.2g) Óxido de calcio CaO 56.08 332 2570 50 2850 - - - —635.6(c) - Óxido de Mgo 40.32 3.65 2900 ITA 3600 - - - —601.8(c) - magnesio Óxido de plomo PbO 22321 95 886 17º 14m 213 ss e -219.2(c) ce Óxido férrico Fe,O; 159.70 5.12 Se descompone a 1560ºC -822.2c) Óxido ferroso Feo 71.85 25 & = E 5 E as -2.66.5(c) E Óxido nítrico NO 30.01 - -163.6 2.301 1518 13.78 179.20 65.0 +90.37(g) É Óxidonitroso NO 4402 12268” 911 E -88.8 a 309.5 7170 +81.5(g) E Oxígeno [0 32.00 - -218.75 0.444 182.97 6.82 154.4 49.7 Ng) e a opudy 9g9 Tabla B. (Continuación,) Peso GE ST)! AMT (her (ahi Compuesto Fórmula molecular (20/4) TC) KJmol TAC) Kllmol TUKY/ Poatm) kJmol KJ/mol Tolueno CHg 92.13 0.866 94.99 6.619 110,62 347 5939 403 +2.00(1) —=3909.9(1) +50.00(g) -3947.9(g) Trióxido de SO; 80.07 - 16.84 25.48 33 4180 4914 83.8 — 395.18(g) - azufre m-Xileno CH 106.16 0.864 4787 11.569 139.10 36.40 619 346 -254U1) 455191) +17.24g) -4594.5(g) 0-Xileno CH 106.16 0.880 -25.18 13.598 14442 36.82 615 35.7 24441) 455291) +18.9Ng) -4596.Mg) p-Xileno CsaHio 106.16 0.861 13.26 7 138.35 3607 618 33.9 -2443M1) -4552.91(1) 11958) 459529) Yodo o) 2538 4.93 133 - 1842 - 826.0 - Oc) - “ Adaptado en parte de D. M. Himmelblau. Basic Principles and Caleulations in Chemical Engineering. 3º. edición. O 1974. tablas D.1 y F.1 Adaptado con autori- zación de Prentice-Hall, Inc., Englewood Cliffs, NJ. » Punto de fusión a | atm. “ Calor de fusión a Tm y | atm, “ Punto de ebullición a | atm. * Calor de vaporización a 7% y | atm. / Temperatura critica. 8 Presiôn crítica, 4 Calor de formación a 25ºC y | atm. E ! Calor de combustión a 25ºC y | atm. Los estados estândar de los productos son CO+(g), H>O(1), SO-(g), HCI(ac) y No(g). Para calcular AH, con H50(g) como producto, sume 44.0 In al valor tabulado, donde ny = moles de H50 formados/moles de combustible quemados. | Para transformar AH a kal/mol, divida el valor dado ente 4. 184; para convertir a Btu/lb/mol, multiplique por 430.28. 8€9 a ootpuody Tabla B.2 Capacidades calorificas” Forma 1: C,[kJ/mol-"C)] o [kJ/(mol-K)] = a + bT+cT2+d7 Forma 2: C,[kJ/mol-"C)] o [kJ(mol-K)] = a + b7+ cr? Ejemplo: (Cacetona(g) = 0:07196 + (20.10 X 105)T — (12.78 X 107872 + (34.76 X 1071273, donde T está en ºC. Nota: Las fórmulas para gases se aplican en forma estricta a presiones lo bastante bajas para que la ecuación de estado de los gases ideales sea válida. Rango Peso Unidad (unidades Compuesto Fórmula molecular Estado Forma detemp. axXI0 bxI0 cx 108 dx 10!2 de 7) Acetileno CH 26.04 g l SE: 42.43 6.053 —5.033 18.20 0-1200 Acetona CH;COCH; 58.08 l 1 “e 123.0 18.6 — 30-60 g 1 %€ 71.96 20.10 -12.78 34.76 0-1200 Ácido nítrico NHO; 63.02 | 1 *€ 10.0 25 Ácido sulfúrico H,SO4 98.08 1 | SE 139.1 15.59 10-45 Agua HO 18.016 1 1 his: 754 0-100 g 1 se 3346 0.6880 0.7604 -3.593 0-1500 Aire 29.0 g i “E: 28.94 0.4147 0.3191 -1.965 0-1500 g l K 28.09 0.1965 0.4799 -1.965 273-1800 Alcohol etílico (etanol) C,H50H 46.07 I | “o 103.1 0 1 1 SE 158.8 100 g l SE 61.34 15.72 —8.749 19.83 0-1200 Alcohol metílico CH;0H 32.04 I 1 E 75.86 16.83 0-65 (metanol) g l ºC 42.93 8.301 -1.87 -8.03 0-700 Amoniaco NH; 17.03 g 1 SE 35.15 2.954 0.4421 —6.686 0-1200 Azufre E) 32.07 c 1 K 152 2.68 273-368 (Rómbico) c 1 K 18.3 1.84 368-392 (Monoclínico) (contimia) SeoIsty sopepordosd op sejqer 6€9 g l “E 137.44 40.85 =23:02 57.66 0-1200 Hidrógeno H, 2.016 g l “E 28.84 0.00765 0.3288 —0.8698 0-1500 Hidróxido de calcio Ca(0H) TAI e 1 K 89.5 276-373 Isobutano CsHio 58.12 g 1 SC 89.46 30.13 -18.91 49.87 0-1200 Isobuteno CaHg 56.10 g 1 SE 82.88 25.64 —17.27 50.50 0-1200 Metano cHy 16.04 B ! ee) 3431 5.469 0.3661 11.00 0-1200 Es ! K 19.87 5.021 1.268 =11.00 273-1500 Metilciclohexano C;His 98.18 g 1 “E 121.3 56.53 =37.72 100.8 0-1200 Metilciclopentano CH 84.16 g l o: 98.83 45.857 -30.44 83.81 0-1200 Monóxido de carbono co 28.01 g 1 É 28.95 04110 0.3548 —2.220 0-1500 Nitrógeno N2 28.02 g ! Sc 29.00 0.2199 0.5723 -2.871 0-1500 Óxido de calcio Cao 56.08 [o 2 K 41.84 2.03 —4.52 x 1010 273-1173 Óxido de magnesio MgO 40.32 [o 2 K 45.44 0.5008 —8.732 x 1010 273-2073 Óxido férrico FO 159.70 c 2 K 103.4 671º A772x1010 — 273-1097 Óxido nítrico NO 30.01 g l ds 6 29.50 0.8188 =0.2925 0.3652 0-3500 Óxido nitroso NO 44.02 g I “e 37.66 4.151 2.694 10.57 0-1200 Oxigeno O, 32.00 g 1 Sc 29.10 1.158 —0.6076 1311 0-1500 n-Pentano CsHij 72.15 l | “E 155.4 43.68 0:36 g ! SC 114.8 34.09 -18.99 42.26 0-1200 Propano C3Hg 44.09 g 1 Ea) 68.032 22.59 = 13.11 31.71 0-1200 Propileno C3Hç 42.08 B ! SC 59.580 17.71 -10.17 24.60 0-1200 Tetracloruro de carbono CCls 153.84 | 1 K 93.39 12.98 273-343 Tetróxido de nitrógeno N,04 92.02 g ! E. 75.7 12.5 -11,3 0-300 Tolueno C;Hg 92.13 l ! “C 148.8 324 O-110 g ! C 94.18 38.00 -27.86 80.33 0-1200 Trióxido de azufre SO; 80.07 g 1 SE 48.50 9.188 -8.540 32.40 0-1000 Sulfato de amonio (NH4)SO4 132.15 e ! K 215.9 275-328 Sulfuro de hidrógeno HS 34.08 g ! SE 33.51 1.547 0.3012 3.292 0-1500 “Adaptado en parte de D. M. Himmelblau, Basic Principles and Calculations in Chemical Engineering, 3a. edición, O 1974, tabla E.1. Adaptado con autorización de Prentice-Hall, Inc., Englewood Cliffs, NJ. spoIsIy Sopepaidoid ap sejqrr 1r9 Tabla B.5 Propiedades del vapor saturado: tabla de temperaturas” Ver'/ke) OçckIkg) HE CKIMk E) TEC PCbar) Agua vapor Agua Vapor Agua Evaporación Vapor 0.01 0.00611 0.001000 206.2 cero 2375.6 + 0.0 2501.6 2501.6 > 0.00705 | 0.001000 179.9 ss 23783 84 2496.8 2505.2 a 0.00813 0.001000 157.3 16.8 23811 16.8 2492.1 2508.9 6 0.00935 0.001000 137.8 25.2 2383.8 25.2 2487.4 2512.6 s O.01072 0.001000 121.0 33.6 2386.6 33.6 2482.6 2516.2 10 0.01227 - 0.001000 106.4 42.0 23893 a2.0 2477.9 2519.9 12 9.01401 | 0.001000 93.8 sos 23921 so.4 2473.2 2523.6 14 001597. 0.001001 s2.9 58.8 23948 s8.s 2468.5 2527.2 16 O.01817 | 0.001001 73.4 67.1 2397.6 67.1 2463.8 2530.9 18 0.02062 0001001 Sosa 75.5 24003 75.5 2459.0 2534.5 20 0.0234 0.001002 57.8 9 24030 83.9 2454.3 2538.2 22 0.0264 09.001002 51.5 2 zaos8s 92.2 2449.6 2541.8 Za 0.0298 0.001003 as.o 6 24085 100.6 2444.9 2545.5 25 0.0317 9.001003 s 24099 104.8 2442.5 2547.3 26 0.0336 0.001003 2411.2 108.9 2440. 2 2549.1 28 0.0378 0.001004 2414.0 117.3 2435.4 2552.7 30 0.0424 0.001004 2416.7 125.7 2430. 7 2556.4 32 0.0475 0.001005 2419.4 134.0 2425.9 2560.0 34 0.0532 0.001006 26.6 24221 142.4 2421.2 2563.6 36 00594 0.001006 24.0 2424.8 150.7 2416.4 2567.2 38 0.0662 0.001007 21.6 2427.5 159.1 2411.7 2570.8 ao 0.0738 0.001008 19.55 2430.2 167.5 2406.9 25744 az 0.0820 0.001009 17.69 2432.9 175.8 2402.1 2577-9 as o.0910 0.001009 16.04 2435.6 184.2 2397.3 2581.5 as 0.1009 O.001010 14.56 2438.3 192.5 2392.5 2585.1 as 01116 0.001011 13.23 2440.9 200.9 2387.7 2588.6 so 0.1234 0.001012 12.05 2443.6 209.3 2382.9 2592.2 s2 0.1361 0.001013 10.98 2446 217: 2377 2595 sa 0.1500 o.o01014 10.02 2449 226.0 2373 2599 s6 0.1651 0.001015 9.158 2451 234.4 2368 2602 ss o.1815 0.001016 s380 zasa 242.8 2363 2606 so 0.1992 0.001017 7.678 2456 2511 2358 2609 62 02184 0.001018 7.043 2459 259.5 2353 2613 64 02391 o.001019 6.468 2461 267.9 2348 2616 66 0.2615 0.001020 5.947 2464 276.2 2343 2619 os 0.2856 0.00 1022 5475 2467 284.6 2338 2623 “Tomada de R. Haywood, Thermodyrnamic Tables in SI (Mericy Units, Cambridge University Press, Londres. P — volumen específico. É — energia interna específica. y Z7 — entalpia específica. Nota: KVkg =X 0.4303 — Brw/lbm. (cortinita) Tabla B.6 Propiedades del vapor saturado: tabla de presiones? Vemikg) Ú(kIikg) BXKkIIkg) P(bar) T(C) Agua Vapor Agua Vapor Agua Evaporación Vapor 0.00611 0.01 0.001000 206.2 cero 2375.6 +0.0 2501.6 2501.6 0.008 38 0.001000 159.7 15.8 2380.7 15.8 2492.6 2508.5 0.010 7.0 0.001000 129.2 293 2385.2 29.3 2485.0 2514.4 0.012 AU 0.001000 108.7 40.6 2388.9 40.6 24787 2519.3 0.014 12.0 0.001000 93.9 50.3 2392.0 50.3 24732 2523.5 0.016 14.0 0.001001 82.8 58.9 2394.8 58.9 2468.4 2527.3 0.018 15.9 0.001001 74.0 66.5 2397.4 66.5 2464.1 2530.6 0.020 17.5 0.001001 67.0 73.5 2399.6 73.5 2460.2 2533.6 0.022 19.0 0.001002 61.2 79.8 2401.7 79.8 2456.6 2536.4 0.024 20.4 0.001002 56.4 85.7 2403.6 85.7 2453.3 2539.0 0.026 21.7 0.001002 523 91.1 2405.4 91.1 2450.2 2541.3 0.028 23.0 0.001002 48.7 96.2 2407.1 96.2 2447.3 2543.6 0.030 241 0.001003 45.7 101.0 2408.6 101.0 2444.6 2545.6 0.035 26.7 0.001003 39.5 11.8 2412.2 111.8 2438.5 2550.4 0.040 29.0 0.001004 34.8 121.4 2415.3 121.4 2433.1 2554.5 0.045 31.0 0.001005 31.1 130.0 2418.1 130.0 2428.2 2558.2 0.050 32.9 0.001005 28.2 137.8 2420.6 137.8 2423.8 2561.6 0.060 36.2 0.001006 23.74 151.5 2425.1 151.5 2416.0 2567.5 0.070 39.0 0.001007 20.53 163.4 2428.9 163.4 2409.2 2572.6 0.080 41.5 0.001008 18.10 173.9 2432.3 173.9 2403.2 25771 0.090 43.8 0.001009 16.20 183.3 2435.3 183.3 2397.9 2581.1 0.10 45.8 0.001010 14.67 191.8 2438.0 191.8 2392.9 2584.8 0.11 477 0.001011 13.42 199.7 2440.5 199.7 2388.4 2588.1 0.12 49.4 0.001012 12.36 206.9 2442.8 206.9 2384.3 2591.2 0.13 La 0.001013 11.47 213.7 2445.0 213.7 2380.4 2594.0 0.14 52.6 0.001013 10.69 220.0 24470 220.0 2376.7 2596.7 a oopuody gho 0.15 0.16 0.17 0.18 0.19 0.20 0.22 0.24 0.26 0.28 0.30 0.35 0.40 0.45 0.50 0.55 0.60 0.65 0.70 0.75 0.80 0.85 0.90 0.95 1.00 1.01325 (1 atm) 59.0 100.0 0.001014 0.001015 0.001015 0.001016 0.001017 0.001017 0.001018 0.001019 0.001020 0.001021 0.001022 0.001025 0.001027 0.001028 0.001030 0.001032 0.001033 0.001035 0.001036 0.001037 0.001039 0.001040 0.001041 0.001042 0.001043 0.001044 10.02 9.43 8.91 8.45 8.03 765 6.45 5.98 5.58 5.23 4.53 3.58 3.24 2.96 2.73 2.53 2.36 2.22 2.087 1.972 1.869 1.777 1.694 1.673 226.0 231.6 236.9 242.0 246.8 251.5 260.1 268.2 275.6 282.7 289.3 304.3 317.6 329.6 340.5 350.6 359.9 368.5 376.7 384.4 391.6 398.5 405.1 411.4 4174 419.0 2448.9 2450.6 2452.3 2453.9 2455.4 2456.9 2459.6 2462.1 2464.4 2466.5 2468.6 2473.1 24771 2480.7 2484.0 2486.9 2489.7 2492.2 2494.5 2496.7 2498.8 2500.8 2502.6 2504.4 2506.1 2506.5 226.0 231.6 236.9 242.0 246.8 251.5 260.1 268.2 2757 282.7 289.3 304.3 317.7 329.6 340.6 350.6 359.9 368.6 376.8 384.5 391.7 398.6 405.2 411.5 417.5 419.1 2373.2 2370.0 2366.9 2363.9 2361.1 2358.4 2353.3 2348.6 2344.2 2340.0 2336.1 2327.2 2319.2 2312.0 2305.4 2299.3 2293.6 2288.3 22833 2278.6 22741 2269.8 2265.6 2261.7 2257.9 2256.9 2599.2 2601.6 2603.8 2605.9 2607.9 2609.9 2613.5 2616.8 2619.9 26227 2625.4 2631.5 2636.9 2641.7 2646.0 2649.9 2653.6 2656.9 2660.1 2663.0 2665.8 2668.4 2670.9 2673.2 2675.4 2676.0 “ Tomado de R. W. Haywood, Thermodynamic Tables in SI(Metric) Units, Cambridge University Press, Londres. À = volumen específico, Ú = energia interna específica, H = entalpia específica. Nota: kJ/kg X 0.4303 = Btu/lbg. (continha) seotstj sopepoidosd op seiqei 6+9 167.8 170.4 172.9 1754 177.7 179.9 182.0 184.1 186.0 188.0 189.8 191.6 195.0 198.3 201.4 204.3 209.8 212.4 214.9 217.2 219.6 221.8 223.9 226.0 230.0 232.0 233.8 237.4 240.9 247.3 0.001112 0.001115 0.001118 0.001121 0.001124 0.001127 0.001130 0.001133 0.001136 0.001139 0.001141 0.001144 0.001149 0.001154 0.001159 0.001163 0.001168 0.001172 0.001177 0.001181 0.001185 0.001189 0.001193 0.001197 0.001201 0.001205 0.001209 0.001213 0.001216 0.001224 0.001231 0.001238 0.001245 0.2554 0.2403 0.2268 02148 o. 1943 0.1855 0.1774 0.1700 0.1632 0.1569 0.1511 0.1407 0.1317 0.1237 0.1166 0.1103 0.1047 0.0995 0.0949 0.0868 0.0832 0.0799 0.0769 0.0740 0.0714 0.0689 0.0666 0.0624 0.0587 0.0554 0.0524 25733 2575.5 25771 2578.8 2580.4 2581.9 2583.3 2584.5 2585.8 2586.9 2588.0 2589.0 2590.8 2592.4 2593.8 2595.1 2597. 3 2598.2 2598.9 2599.6 2600.2 2601.2 2601.5 2601.8 2602. 3 2602.4 2602.5 2602.2 2601.9 2055.5 2046.5 2037.9 2029.5 2021.4 2013.6 2005.9 1998.5 1991.3 1984.3 1977.4 1970.7 1957.7 1945.2 1933.2 1921.5 1910.3 1899.3 1888.6 1878.2 1868.1 1858.2 1848.5 1839.0 1829.6 1820.5 1811.5 1802.6 1793.9 1776.9 1760.3 1744.2 1728.4 2801.7 2801.1 (continúa) seoIsty sopepordoid ap sejqey Is9 Tabla B.6 (Continuación) V(m?/kg) Ó(kIlkg) R(kJ/kg) P(bar) T(C) Agua Vapor Agua Vapor Agua Evaporación Vapor 40 250.3 0.001252 0.0497 1082.4 2601.3 1087.4 1712.9 2800.3 42 253.2 0.001259 0.0473 1096.3 2600.7 1101.6 1697.8 2799.4 44 256.0 0.001266 0.0451 1109.8 2599.9 1115.4 1682.9 2798.3 46 2588 0.001272 0.0430 11229 2599.1 1128.8 1668.3 27974 48 261.4 0.001279 0.0412 1135.6 2598.1 1141.8 1653.9 2795.7 50 263.9 0.001286 0.0394 11480 2597.0 1154.5 1639.7 2794.2 52 266.4 0.001292 0.0378 1160.1 2595.9 1166.8 1625.7 2792.6 54 268.8 0.001299 0.0363 1171.9 2594.6 1178.9 1611.9 2790.8 56 21.1 0.001306 0.0349 1183.5 2593.3 1190.8 1598.2 2789.0 58 273.3 0.001312 0.0337 1194.7 2591.9 12023 1584.7 2787.0 60 275.6 0.001319 0.0324 1205.8 2590.4 1213.7 1571.3 2785.0 62 27131 0.001325 0.0313 1216.6 2588.8 1224.8 1558.0 2782.9 64 279.8 0.001332 0.0302 1227.2 2587.2 1235.7 1544.9 2780.6 66 281.8 0.001338 0.0292 1237.6 2585.5 1246.5 1531.9 27783 68 2838 0.001345 0.0283 1247.9 2583.7 1257.0 1518.9 27759 70 2858 0.001351 0.0274 1258.0 2581.8 1267.4 1506.0 27735 72 287.7 0.001358 0.0265 1267.9 2579.9 1277.6 1493.3 277109 74 289.6 0.001364 0.0257 1277.6 2578.0 1287.7 1480.5 27683 76 2914 0.001371 0.0249 1287.2 2575.9 1297.6 1467.9 2765.5 78 293.2 0.001378 0.0242 1296.7 25738 1307.4 1455.3 27%62.8 so 295.0 0.001384 0.0235 1306.0 2571.7 1317.1 1442.8 2759.9 82 296.7 0.001391 0.0229 1315.2 2569.5 1326.6 14303 27570 84 298.4 0.001398 0.0222 13243 2567.2 1336.1 1417.9 27540 86 300.1 0.001404 0.0216 13333 2564.9 1345.4 1405.5 2705.9 88 301.7 0.001411 0.0210 1342.2 2562.6 1354.6 1393.2 2747.8 90 303.3 0.001418 0.02050 13510 2560.1 1363.7 1380.9 27446 92 304.9 0.001425 0.01996 1359.7 2557.7 1372.8 1368.6 27414 94 306.4 0.001432 0.01945 1368.2 2555.2 1381.7 13563 2738.0 gopuody 759 654 Apéndice B Tabla B.7 Propiedades del vapor sobrecalentados PCbar) Agua Vapor [Temperatura €Cy— Tam PE) sat. sat. so 7s 100 150 200 2s0 300 3so oo a — — 2595 2642 2689 2784 2880 2978 3077 3177 o — — 2446 zas1 2517 2589 2662 2736 2812 2890 a 2s84s.8 2593 2640 2688 2783 2880 2977 3077 3177 o 2438.0 zasa zaso 2516 2588 2661 2736 2812 2890 v 14.7 14.8 16.0 17.2 19.5 21.8 24.2 26.5 28.7 E 2646.0 209.3 313.9 2683 2780 2878 2979 3076 3177 o zass.0 209.2 313.9 2512 2586 2660 2735 28 2889 v 3.24 o.o0101 0.00103 3.41 3.89 4.35 4.83 s.29 5.75 a 2675.4 209.3 314.0 2676 2776 2875 2975 3074 3176 o 2506.1 209.2 313.9 2507 2583 2658 2734 2811 zsso v 1.69 o.o0101 o.o0103 1.69 1.94 217 2.40 2.64 2.87 a 2747.5 209.7 314.3 419.4 632.2 2855 2961 3065 3168 o 2560.2 209:2 313.8 418.8 631.6 2643 2724 2803 2883 v 0.375 0.00101 o.00103 o.oo104 o.oo109 0.425 0474 0.522 0.571 10 a 2776.2 210.1 314.7 419.7 632.5 2827 2943 3052 3159 (179.9) o 2582 209.1 313.7 418.7 631.4 2621 270 2794 2876 v 0.194 0.00101 0.00103 o.ootos 0.00109 0.206 0.233 0.258 0.282 zo a 2797.2 211.0 315.5 420.5 633.1 852.6 2902 3025 3139 (212.4) o 2598.2 209.0, 313.5 418.4 603.9 850.2 2679 2774 2862 v 0.09950 o.oo101 0.00102 o.oo104 o.oo10o9 0.00116 0.111 0.125 0.139 so 2 212.7 3171 422.0 634.3 853.4 1085.8 2962 3095 (250.3) o 2601.3 208.6 313.0 417.8 630.0 848.8 1080.8 2727 2829 ” 0.04975 0.00101 0.00102 o.oo104 o.o0109 0.00115 0.00125 o.osss 0.0665 so a 2785.0 214.4 318.7 423.5 635.6 854.2 1085.8 2sss 3046 (275.6) o 2590.4 208.3 312.6 417.3 629.1 847.3 1078.3 2668 2792 v 0.0325 o.oo101 o.oo1o3 oooios | oovIos ooolIs 0.00125 | 0.0361 0.0422 so a 2759.9 216. 320.3 425.0 636.8 8ss.1 1085.8 2787 2990 (95.0) o 2571.7 208.1 312.3 416.7 628.2 845.9 1075.8 2593 2750 v 0.0235 0.o0101 o.o0102 o.oo1os 0.00109 0.00115 0.00124 0.0243 0.0299 100 a 2727.7 217.8 322.9 426.5 638.1 Bss.9 1085.8 1343.4 2926 Gio o 2547.3 207.8 311.7 416.1 627.3 844.4 1073.4 1329.4 2702 > o.o181 o.o0101 o.00102 o.oo104 oooios oO01is 000124 000140 | 0.224 150 a 2615.0 2221 326.0 430.3 641.3 858.1 1086.2 1338.2 2695 (342.1) [24 2459.9 207.0 310.7 414.7 625.0 sas1.0 1067.7 1317.6 2523 v o.o1o3 o.oo1o1 o.o0102 o.o0104 oooTros | oooiI4 000123 000138 | oorIs 200 a 2418.4 226.4 330.0 434.0 644.5 860.4 1086.7 1334.3 1647.1 (365.7) o 2300.8 206.3 309.7 4132 622.9 837.7 10622 1307.1 16137 id 0.005875 0.00100 0.00102 o.o0o103 o.oo108 o.o0114 0.00122 0.00136 0.00167 Z21.2(P) a 2108 228.2 331.7 435.7 645.8 861.4 1087.0 1332.8 1635.5 GIST O 2037.8 206.0 309.2 412.8 622.0 836.3 1060.0 1302.9 1600.3 v 0.00317 0.00100 0.00102 0.00103 "000108 OOOIIs 000122 000135 0.00163 250 a — 230.7 334.0 437.8 6477 862.8 1087.5 1331.1 1625.0 Ss o — 205.7 308.7 4121 620.8 834.4 1057.0 1297'5 1585.0) v — 0.00100 0.00101 0.00103 o.oo108 0.00113 0.00122 0.00135 o.o0160 300 a — 235.0 338.1 441.6 650.9 865.2 1088.4 1328.7 1609.9 cs o mes 205.0 307.7 “10.8 618.7 831.3 1052.1 1563.3 v — 0.0009990 o.oo101 o.oo1o3 000107 OO0113 | 0.00121 0.00155 soo 2 — 251.9 354.2 456.8 664.1 875.4 1093.6 1323.7 1576.3 <—) o — 202.4 304.0 40s.s8 611.0 819.7 1034.3 1259.3 1504.1 v — 0.0009911 o.o0100 0.00102 o.o0106 0.00111 0.00119 0.00129 0.00144 1000 a ss 293.9 394.3 4951 s98.0 903.5 1113.0 1328.7 1550.5 pa o — 196.5 295.7 395.1 594.4 795.3 999.0 1207.1 1419.0 v — 0.0009737 0.0009852 0.001000 o.oo104 oootos 0.00114 0.00122 0.00131 “ Adaptado de R. W Haywood, Thermodynamic Tables in SI (Metric) Units. Cambridge University Press, Londres. El agua es energia interna específica (kJ/kg). volumen específico (m*kg). Nora: n liquido en la región comprendida entre SOC y 350ºC. /7 — entalpia específica (kJ/kg). O kI/kg X 0.4303 — Bw/lb, Ccontinia) Tablas de propiedades físicas 655 Tabla B.7 (Continuación) PQbar) Temperatura (*C)— 400 450 soo sso soo eso 700 750 2 3280 3384 3497 3597 3706 3816 3929 4043 9 2969 3050 3132 3217 3303 3390 3480 3591 a 3280 3384 3489 3596 3706 3816 3929 4043 o 2969 3050 3132 3217 3303 3390 3480 3571 v 21.1 33.3 3s.7 38.0 40.3 42.6 44.8 472 a 3279 3383 3489 3596 3705 3816 3929 4043 o 2969 3049 3132 3216 3302 3390 3480 3571 v 6.21 6.67 714 7.58 8.06 B.ss 9.01 9.43 1.0 A 3278 3382 a4ss 3596 3705 3816 3928 4042 (99.6) o 2968 3049 3132 3216 3302 3390 3479 3570 v 31 3.33 3.57 3.80 4.03 4.26 4.48 4.72 so a 3272 3379 aas4 3592 3702 3813 3926 4040 (151.8) o 2964 3045 3128 3213 3300 3388 3477 3569 v 0.617 0.664 0.711 0.758 0.804 o.8so 0.897 0.943 10 a 3264 3371 3478 3587 3697 3809 3923 4038 (179.9) o 2958 3041 3124 3210 3296 3385 3475 3567 v 0.307 0.330 0.353 0.377 0.402 0.424 0.448 0.472 20 a az49 3358 3467 3578 3689 3802 3916 4032 CQIz4) o 2946 3031 3115 3202 3290 3379 3470 3562 v 0.151 0.163 0.175 o1ss 0.200 -o2m 0.223 0.235 40 Eça 3216 3331 3445 3559 3673 3788 3904 4021 (250.3) o 2922 3011 3100 3188 3278 3368 3460 3554 P 00734 0.0799 0.0864 0.0926 0.0987 o.105 ot 0.117 so A 3180 3303 3422 3539 3657 3774 3892 4011 (275.6) o 2896 2991 3083 3174 3265 3357 3451 3sas 7 00474 0.0521 0.0566 0.0609 0.0652 0.0693 0.0735 0.0776 so a 3142 az74 3399 3520 3640 3759 3879 4900 (295.0) o 2867 2969 3065 3159 3252 3346 3441 3537 7 00344 0.0382 0.0417 0.0450 0.0483 o.os1s 0.0547 0.0578 100 a 3100 3244 3375 3500 3623 azas 3867 3989 [E TER) o 2836 2946 3047 3144 3240 3335 3431 3528 v o0264 0.0298 0.0328 0.0356 0.0383 o.0410 0.0435 0.0461 150 a 2975 3160 3311 3448 3sso 3708 3835 3962 (342.1) o 2744 2883 2999 3105 3207 3307 3407 3507 v oo1s7 o.o18s o.0208 0.0229 0.0249 0.0267 0.0286 0.0304 200 a 2820 3064 3241 3394 3536 3671 3804 3935 (365.7) [54 2622 2810 2946 3063 3172 3278 3382 3485 ? 0009950 0.0127 oo148 0.0166 0.0182 0.197 ozm 0.0225 221.2(P) 2733 3020 3210 3370 3516 3655 3790 3923 GIST) O 2553 2776 2922 3045 3157 3265 3371 3476 ? 008157 ooo o.0130 0.0147 0.0162 0.0176 o.0190 0.0202 250 a 2582 2954 3166 3337 3490 3633 3772 3908 — o 2432 2725 2888 3019 3137 3248 3356 3463 ? 0006013 | 0.009174 o.o111 0.0127 o.o141 o.o143 0.0166 0.0178 300 a 2162 2826 308s 3277 3443 3s9s 3740 38so ss o 2077 2623 2825 2972 3100 3218 3330 3441 ? 0002830 0.006734 0.008680 o.0102 ootIs 0.0126 0.0136 0.0147 soo A 1878 2293 2723 3021 3248 3439 3610 3771 — o 1791 2169 2529 2765 2946 3091 3224 3350 P 0001726 | 0.002491 0003882 O00SIIZ 0006112 0.007000 0007722 o.008418 1000 a 1798 2051 2316 2594 2857 3105 3324 3526 —s o 1653 1888 2127 2369 2591 2795 2971 3131 V 0001446 0.001628 0001893 0.002246 0.002668 | 0.003106 0.003536 | 0.003953 
