Thermodynamics/Property tables and charts/CoolProp/Saturated refrigerant-134a - Temperature table
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| 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 Thermodynamics/Property tables and charts/CoolProp/Saturated refrigerant-134a - Temperature table/Code