Engineering Thermodynamics/Appendix/Saturated refrigerant-134a - Temperature table

+ Saturated properties of R134a Saturation temperature, Tsat(°C) Saturation pressure, psat(kPa) Specific volume,(m³/kg) Internal energy,(kJ/kg) Enthalpy,(kJ/kg) Entropy,(kJ/(kg·K)) Sat. liquid, vf Sat. vapor, vg Sat. liquid, uf Evap., ufg Sat. vapor, ug Sat. liquid, hf Evap., hfg Sat. vapor, hg Sat. liquid, sf Evap., sfg Sat. vapor, sg -40 51.21 0.0007054 0.36108 -0.036 207.40 207.37 -0.000 225.86 225.86 -0.00000 0.96873 0.96873 -35 66.14 0.0007127 0.28402 6.254 203.98 210.24 6.301 222.72 229.02 0.02669 0.93522 0.96192 -30 84.38 0.0007203 0.22594 12.59 200.52 213.11 12.65 219.53 232.17 0.05301 0.90284 0.95586 -25 106.40 0.0007281 0.18162 18.97 197.01 215.98 19.04 216.26 235.31 0.07899 0.87149 0.95048 -20 132.73 0.0007362 0.14739 25.39 193.45 218.85 25.49 212.92 238.41 0.10464 0.84108 0.94571 -15 163.94 0.0007447 0.12067 31.87 189.83 221.70 31.99 209.49 241.48 0.12998 0.81151 0.94148 -10 200.60 0.0007535 0.099590 38.40 186.14 224.54 38.55 205.97 244.52 0.15504 0.78270 0.93774 -5 243.34 0.0007627 0.082801 44.99 182.38 227.37 45.17 202.34 247.51 0.17983 0.75459 0.93442 0 292.80 0.0007723 0.069309 51.63 178.54 230.17 51.86 198.60 250.46 0.20439 0.72709 0.93148 5 349.66 0.0007824 0.058374 58.33 174.60 232.94 58.61 194.74 253.35 0.22872 0.70013 0.92885 10 414.61 0.0007930 0.049442 65.10 170.57 235.68 65.43 190.74 256.17 0.25286 0.67364 0.92650 15 488.37 0.0008042 0.042090 71.94 166.43 238.37 72.34 186.59 258.93 0.27682 0.64755 0.92438 20 571.71 0.0008161 0.035997 78.86 162.17 241.02 79.32 182.28 261.60 0.30063 0.62180 0.92243 25 665.38 0.0008287 0.030912 85.85 157.77 243.62 86.40 177.79 264.19 0.32431 0.59630 0.92062 30 770.20 0.0008421 0.026642 92.93 153.23 246.16 93.58 173.10 266.67 0.34789 0.57099 0.91888 35 886.98 0.0008565 0.023033 100.10 148.51 248.61 100.86 168.18 269.04 0.37140 0.54578 0.91718 40 1016.6 0.0008720 0.019966 107.38 143.61 250.99 108.27 163.02 271.28 0.39487 0.52058 0.91545 45 1159.9 0.0008888 0.017344 114.77 138.49 253.26 115.80 157.58 273.38 0.41833 0.49529 0.91362 50 1317.9 0.0009072 0.015089 122.28 133.12 255.41 123.48 151.81 275.29 0.44184 0.46979 0.91164 55 1491.5 0.0009274 0.013140 129.94 127.47 257.41 131.32 145.68 277.01 0.46545 0.44396 0.90940 60 1681.8 0.0009498 0.011444 137.76 121.48 259.24 139.36 139.12 278.49 0.48921 0.41760 0.90681 65 1889.8 0.0009750 0.009960 145.77 115.08 260.85 147.62 132.06 279.67 0.51321 0.39053 0.90374 70 2116.8 0.0010038 0.008653 154.01 108.18 262.19 156.14 124.37 280.51 0.53757 0.36243 0.89999 75 2364.1 0.0010372 0.007491 162.53 100.65 263.18 164.98 115.90 280.89 0.56243 0.33291 0.89533 80 2633.2 0.0010773 0.006448 171.41 92.28 263.69 174.25 106.42 280.67 0.58803 0.30135 0.88938 85 2925.8 0.0011272 0.005499 180.78 82.74 263.53 184.08 95.54 279.62 0.61477 0.26675 0.88152 90 3244.2 0.0011936 0.004613 190.91 71.39 262.30 194.78 82.49 277.27 0.64342 0.22714 0.87057 95 3591.2 0.0012942 0.003743 202.45 56.63 259.08 207.10 65.42 272.53 0.67593 0.17771 0.85364 100 3972.4 0.0015357 0.002681 219.05 29.84 248.89 225.15 34.39 259.54 0.72317 0.09215 0.81531 Calculation note: Values were generated with CoolProp 8.0.0 using the HEOS model for R134a. Pressure is absolute. Thermodynamic reference convention: CoolProp ASHRAE for R134a. Definition: Saturated liquid at −40 °C is assigned h = 0 kJ/kg and s = 0 kJ/(kg·K). Reference anchor for reproducibility: T = -103.3 °C, p = 0.38956379 kPa, Q = 0 (saturated liquid), u = -76.689297 kJ/kg, h = -76.689052 kJ/kg, and s = -0.38299348 kJ/(kg·K). See the code to reproduce the table here v:Thermodynamics/Property tables and charts/CoolProp/Saturated refrigerant-134a - Temperature table/Code