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Tablas de datos tabulados Termodinámica.
Tipo: Apuntes
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Temp., T 8 C
Sat. press., Psat kPa
Sat. liquid, v f
Sat. vapor, v g
Sat. liquid, uf
Evap., ufg
Sat. vapor, ug
Sat. liquid, hf
Evap., hfg
Sat. vapor, hg
Sat. liquid, sf
Evap., sfg
Sat. vapor, sg
240 51.25 0.0007053 0.36064 2 0.036 207.42 207.38 0.00 225.86 225.86 0.00000 0.96869 0. 238 56.86 0.0007082 0.32718 2.472 206.06 208.53 2.512 224.62 227.13 0.01071 0.95516 0. 236 62.95 0.0007111 0.29740 4.987 204.69 209.68 5.032 223.37 228.40 0.02137 0.94182 0. 234 69.56 0.0007141 0.27082 7.509 203.32 210.83 7.559 222.10 229.66 0.03196 0.92867 0. 232 76.71 0.0007171 0.24706 10.04 201.94 211.97 10.09 220.83 230.93 0.04249 0.91569 0. 230 84.43 0.0007201 0.22577 12.58 200.55 213.12 12.64 219.55 232.19 0.05297 0.90289 0. 228 92.76 0.0007232 0.20666 15.12 199.15 214.27 15.19 218.25 233.44 0.06339 0.89024 0. 226 101.73 0.0007264 0.18947 17.67 197.75 215.42 17.75 216.95 234.70 0.07376 0.87776 0. 224 111.37 0.0007296 0.17398 20.23 196.34 216.57 20.31 215.63 235.94 0.08408 0.86542 0. 222 121.72 0.0007328 0.15999 22.80 194.92 217.71 22.89 214.30 237.19 0.09435 0.85323 0. 220 132.82 0.0007361 0.14735 25.37 193.49 218.86 25.47 212.96 238.43 0.10456 0.84119 0. 218 144.69 0.0007394 0.13589 27.96 192.05 220.00 28.07 211.60 239.67 0.11473 0.82927 0. 216 157.38 0.0007428 0.12550 30.55 190.60 221.15 30.67 210.23 240.90 0.12486 0.81749 0. 214 170.93 0.0007463 0.11605 33.15 189.14 222.29 33.28 208.84 242.12 0.13493 0.80583 0. 212 185.37 0.0007498 0.10744 35.76 187.66 223.42 35.90 207.44 243.34 0.14497 0.79429 0. 210 200.74 0.0007533 0.099600 38.38 186.18 224.56 38.53 206.02 244.55 0.15496 0.78286 0. 28 217.08 0.0007570 0.092438 41.01 184.69 225.69 41.17 204.59 245.76 0.16491 0.77154 0. 26 234.44 0.0007607 0.085888 43.64 183.18 226.82 43.82 203.14 246.95 0.17482 0.76033 0. 24 252.85 0.0007644 0.079889 46.29 181.66 227.94 46.48 201.66 248.14 0.18469 0.74921 0. 22 272.36 0.0007683 0.074388 48.94 180.12 229.07 49.15 200.17 249.33 0.19452 0.73819 0. 0 293.01 0.0007722 0.069335 51.61 178.58 230.18 51.83 198.67 250.50 0.20432 0.72726 0. 2 314.84 0.0007761 0.064690 54.28 177.01 231.30 54.53 197.14 251.66 0.21408 0.71641 0. 4 337.90 0.0007802 0.060412 56.97 175.44 232.40 57.23 195.58 252.82 0.22381 0.70565 0. 6 362.23 0.0007843 0.056469 59.66 173.84 233.51 59.95 194.01 253.96 0.23351 0.69496 0. 8 387.88 0.0007886 0.052829 62.37 172.23 234.60 62.68 192.42 255.09 0.24318 0.68435 0. 10 414.89 0.0007929 0.049466 65.09 170.61 235.69 65.42 190.80 256.22 0.25282 0.67380 0. 12 443.31 0.0007973 0.046354 67.82 168.96 236.78 68.17 189.16 257.33 0.26243 0.66331 0. 14 473.19 0.0008018 0.043471 70.56 167.30 237.86 70.94 187.49 258.43 0.27201 0.65289 0. 16 504.58 0.0008064 0.040798 73.31 165.62 238.93 73.72 185.80 259.51 0.28157 0.64252 0. 18 537.52 0.0008112 0.038317 76.07 163.92 239.99 76.51 184.08 260.59 0.29111 0.63219 0. 20 572.07 0.0008160 0.036012 78.85 162.19 241.04 79.32 182.33 261.64 0.30062 0.62192 0. 22 608.27 0.0008209 0.033867 81.64 160.45 242.09 82.14 180.55 262.69 0.31012 0.61168 0. 24 646.18 0.0008260 0.031869 84.44 158.68 243.13 84.98 178.74 263.72 0.31959 0.60148 0. 26 685.84 0.0008312 0.030008 87.26 156.89 244.15 87.83 176.90 264.73 0.32905 0.59131 0. 28 727.31 0.0008366 0.028271 90.09 155.08 245.17 90.70 175.03 265.73 0.33849 0.58117 0. 30 770.64 0.0008421 0.026648 92.93 153.24 246.17 93.58 173.13 266.71 0.34792 0.57105 0. 32 815.89 0.0008477 0.025131 95.79 151.37 247.17 96.49 171.19 267.67 0.35734 0.56095 0. 34 863.11 0.0008535 0.023712 98.67 149.48 248.15 99.41 169.21 268.61 0.36675 0.55086 0. 36 912.35 0.0008595 0.022383 101.56 147.55 249.11 102.34 167.19 269.53 0.37615 0.54077 0. 38 963.68 0.0008657 0.021137 104.47 145.60 250.07 105.30 165.13 270.44 0.38554 0.53068 0. 40 1017.1 0.0008720 0.019968 107.39 143.61 251.00 108.28 163.03 271.31 0.39493 0.52059 0. 42 1072.8 0.0008786 0.018870 110.34 141.59 251.92 111.28 160.89 272.17 0.40432 0.51048 0.
Temp., T 8 C
Sat. press., Psat kPa
Sat. liquid, v f
Sat. vapor, v g
Sat. liquid, uf
Evap., ufg
Sat. vapor, ug
Sat. liquid, hf
Evap., hfg
Sat. vapor, hg
Sat. liquid, sf
Evap., sfg
Sat. vapor, sg
46 1191.0 0.0008924 0.016866 116.28 137.43 253.71 117.34 156.46 273.80 0.42311 0.49020 0. 48 1253.6 0.0008997 0.015951 119.28 135.30 254.58 120.41 154.17 274.57 0.43251 0.48001 0. 52 1386.2 0.0009151 0.014276 125.35 130.89 256.24 126.62 149.41 276.03 0.45136 0.45948 0. 56 1529.1 0.0009317 0.012782 131.52 126.29 257.81 132.94 144.41 277.35 0.47028 0.43870 0. 60 1682.8 0.0009498 0.011434 137.79 121.45 259.23 139.38 139.09 278.47 0.48930 0.41746 0. 65 1891.0 0.0009751 0.009959 145.80 115.06 260.86 147.64 132.05 279.69 0.51330 0.39048 0. 70 2118.2 0.0010037 0.008650 154.03 108.17 262.20 156.15 124.37 280.52 0.53763 0.36239 0. 75 2365.8 0.0010373 0.007486 162.55 100.62 263.17 165.01 115.87 280.88 0.56252 0.33279 0. 80 2635.3 0.0010774 0.006439 171.43 92.22 263.66 174.27 106.35 280.63 0.58812 0.30113 0. 85 2928.2 0.0011273 0.005484 180.81 82.64 263.45 184.11 95.39 279.51 0.61487 0.26632 0. 90 3246.9 0.0011938 0.004591 190.94 71.19 262.13 194.82 82.22 277.04 0.64354 0.22638 0. 95 3594.1 0.0012945 0.003713 202.49 56.25 258.73 207.14 64.94 272.08 0.67605 0.17638 0. 100 3975.1 0.0015269 0.002657 218.73 29.72 248.46 224.80 34.22 259.02 0.72224 0.09169 0.
Source of Data: Tables A 2 11 through A 2 13 are generated using the Engineering Equation Solver (EES) software developed by S. A. Klein and F. L. Alvarado. The routine used in calculations is the R134a, which is based on the fundamental equation of state developed by R. Tillner 2 Roth and H.D. Baehr, “An International Standard Formulation for the Thermodynamic Properties of 1,1,1,2-Tetrafluoroethane (HFC-134a) for temperatures from 170 K to 455 K and pressures up to 70 MPa,” J. Phys. Chem, Ref. Data, Vol. 23, No. 5, 1994. The enthalpy and entropy values of saturated liquid are set to zero at 2408 C (and 2408 F).
v m^3 /kg
u kJ/kg
h kJ/kg
s kJ/kg·K
v m^3 /kg
u kJ/kg
h kJ/kg
s kJ/kg·K
v m^3 /kg
u kJ/kg
h kJ/kg
s kJ/kg·K
8 C
v m^3 /kg u kJ/kg h kJ/kg s kJ/kg·K v m^3 /kg u kJ/kg h kJ/kg s kJ/kg·K v m^3 /kg u kJ/kg h kJ/kg s kJ/kg·K
- APPENDIX