- InChI
- InChI=1S/C3F6/c4-1(2(5)6)3(7,8)9
- InChI Key
- HCDGVLDPFQMKDK-UHFFFAOYSA-N
- Formula
- C3F6
- SMILES
- FC(F)=C(F)C(F)(F)F
- Molecular Weight1
- 150.02
- CAS
- 116-15-4
- Other Names
-
- 1,1,2,3,3,3-HEXAFLUORO-1-PROPENE
- 1-Propene, 1,1,2,3,3,3-hexafluoro-
- CF3CF=CF2
- HFC 1216
- Hexafluoro-1-propene
- Hexafluoropropene
- Hexafluoropropylene
- PERFLUOROPROPYLENE
- Perfluoro-1-propene
- Perfluoropropene
- Propylene, hexafluoro-
- UN 1858
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -1128.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1151.70 | kJ/mol | NIST |
| ΔfusH° | 12.17 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 16.19 | kJ/mol | Joback Calculated Property |
| IE | [10.30; 11.11] | eV |
|
| IE | 10.60 ± 0.03 | eV | NIST |
| IE | 10.60 ± 0.03 | eV | NIST |
| IE | 10.62 | eV | NIST |
| IE | 10.62 | eV | NIST |
| IE | 11.11 | eV | NIST |
| IE | 10.30 ± 0.20 | eV | NIST |
| log10WS | -2.64 | Crippen Calculated Property | |
| logPoct/wat | 2.626 | Crippen Calculated Property | |
| McVol | 59.450 | ml/mol | McGowan Calculated Property |
| Pc | 3480.65 | kPa | Joback Calculated Property |
| Inp | [268.00; 268.00] |
|
|
| Inp | 268.00 | NIST | |
| Inp | 268.00 | NIST | |
| Tboil | [244.00; 244.20] | K |
|
| Tboil | 244.00 | K | NIST |
| Tboil | 244.20 | K | NIST |
| Tboil | 244.00 ± 3.00 | K | NIST |
| Tc | 395.75 | K | Joback Calculated Property |
| Vc | 0.282 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [100.76; 131.83] | J/mol×K | [264.35; 395.75] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 100 105 110 115 120 125 130 300 350 | ||||
| Cp,gas | 100.76 | J/mol×K | 264.35 | Joback Calculated Property |
| Cp,gas | 106.72 | J/mol×K | 286.25 | Joback Calculated Property |
| Cp,gas | 112.36 | J/mol×K | 308.15 | Joback Calculated Property |
| Cp,gas | 117.67 | J/mol×K | 330.05 | Joback Calculated Property |
| Cp,gas | 122.68 | J/mol×K | 351.95 | Joback Calculated Property |
| Cp,gas | 127.39 | J/mol×K | 373.85 | Joback Calculated Property |
| Cp,gas | 131.83 | J/mol×K | 395.75 | Joback Calculated Property |
| ΔvapH | 21.90 | kJ/mol | 263.00 | NIST |
| Pvap | [64.00; 3128.10] | kPa | [233.17; 358.76] |
|
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 250 300 350 | ||||
| Pvap | 64.00 | kPa | 233.17 | Phase e... |
| Pvap | 102.00 | kPa | 243.23 | Phase e... |
| Pvap | 120.00 | kPa | 248.14 | Isother... |
| Pvap | 157.00 | kPa | 253.14 | Phase e... |
| Pvap | 149.70 | kPa | 253.26 | Experim... |
| Pvap | 150.00 | kPa | 253.27 | Isother... |
| Pvap | 184.10 | kPa | 258.26 | Experim... |
| Pvap | 225.00 | kPa | 263.01 | Isother... |
| Pvap | 224.50 | kPa | 263.16 | Experim... |
| Pvap | 224.50 | kPa | 263.17 | Isother... |
| Pvap | 233.00 | kPa | 263.20 | Phase e... |
| Pvap | 278.57 | kPa | 268.13 | Isother... |
| Pvap | 272.00 | kPa | 268.24 | Experim... |
| Pvap | 327.10 | kPa | 272.33 | Pure Co... |
| Pvap | 324.40 | kPa | 273.16 | Isother... |
| Pvap | 334.00 | kPa | 273.19 | Phase e... |
| Pvap | 326.80 | kPa | 273.24 | Experim... |
| Pvap | 394.08 | kPa | 278.14 | Isother... |
| Pvap | 392.00 | kPa | 278.20 | Vapor L... |
| Pvap | 389.00 | kPa | 278.21 | Experim... |
| Pvap | 388.60 | kPa | 278.22 | Experim... |
| Pvap | 420.70 | kPa | 279.64 | Pure Co... |
| Pvap | 452.00 | kPa | 282.92 | Isother... |
| Pvap | 459.00 | kPa | 283.23 | Experim... |
| Pvap | 542.58 | kPa | 288.14 | Isother... |
| Pvap | 537.10 | kPa | 288.21 | Experim... |
| Pvap | 538.00 | kPa | 288.22 | Vapor L... |
| Pvap | 617.00 | kPa | 292.76 | Isother... |
| Pvap | 641.00 | kPa | 293.12 | Isother... |
| Pvap | 625.90 | kPa | 293.19 | Experim... |
| Pvap | 641.00 | kPa | 293.96 | Vapor L... |
| Pvap | 670.00 | kPa | 295.42 | Vapor L... |
| Pvap | 721.00 | kPa | 297.93 | Vapor L... |
| Pvap | 729.82 | kPa | 298.14 | Isother... |
| Pvap | 728.30 | kPa | 298.22 | Experim... |
| Pvap | 763.30 | kPa | 299.34 | Pure Co... |
| Pvap | 774.00 | kPa | 300.38 | Vapor L... |
| Pvap | 825.70 | kPa | 302.24 | Pure Co... |
| Pvap | 838.00 | kPa | 302.94 | Isother... |
| Pvap | 832.00 | kPa | 303.07 | Isother... |
| Pvap | 834.00 | kPa | 303.08 | Vapor L... |
| Pvap | 839.70 | kPa | 303.22 | Experim... |
| Pvap | 890.00 | kPa | 305.40 | Vapor L... |
| Pvap | 953.00 | kPa | 307.90 | Vapor L... |
| Pvap | 963.24 | kPa | 308.19 | Isother... |
| Pvap | 963.40 | kPa | 308.21 | Experim... |
| Pvap | 1018.00 | kPa | 310.38 | Vapor L... |
| Pvap | 1077.30 | kPa | 312.33 | Pure Co... |
| Pvap | 1087.00 | kPa | 312.90 | Vapor L... |
| Pvap | 1094.00 | kPa | 312.91 | Isother... |
| Pvap | 1099.40 | kPa | 313.11 | Isother... |
| Pvap | 1099.90 | kPa | 313.21 | Experim... |
| Pvap | 1099.00 | kPa | 313.38 | Isother... |
| Pvap | 1159.00 | kPa | 315.32 | Vapor L... |
| Pvap | 1232.10 | kPa | 317.63 | Pure Co... |
| Pvap | 1235.00 | kPa | 317.82 | Vapor L... |
| Pvap | 1251.16 | kPa | 318.22 | Isother... |
| Pvap | 1250.60 | kPa | 318.22 | Experim... |
| Pvap | 1315.00 | kPa | 320.30 | Vapor L... |
| Pvap | 1398.00 | kPa | 322.79 | Vapor L... |
| Pvap | 1407.00 | kPa | 322.94 | Isother... |
| Pvap | 1408.00 | kPa | 323.06 | Isother... |
| Pvap | 1413.50 | kPa | 323.20 | Experim... |
| Pvap | 1488.00 | kPa | 325.34 | Vapor L... |
| Pvap | 1579.00 | kPa | 327.86 | Vapor L... |
| Pvap | 1595.10 | kPa | 328.21 | Experim... |
| Pvap | 1676.00 | kPa | 330.38 | Vapor L... |
| Pvap | 1776.00 | kPa | 332.85 | Vapor L... |
| Pvap | 1783.00 | kPa | 332.94 | Isother... |
| Pvap | 1788.20 | kPa | 333.11 | Isother... |
| Pvap | 1791.40 | kPa | 333.21 | Experim... |
| Pvap | 1863.00 | kPa | 334.96 | Isother... |
| Pvap | 1879.00 | kPa | 335.31 | Vapor L... |
| Pvap | 1993.00 | kPa | 337.90 | Vapor L... |
| Pvap | 2007.90 | kPa | 338.18 | Experim... |
| Pvap | 2110.00 | kPa | 340.34 | Vapor L... |
| Pvap | 2230.00 | kPa | 342.86 | Vapor L... |
| Pvap | 2225.00 | kPa | 342.92 | Isother... |
| Pvap | 2243.80 | kPa | 343.21 | Experim... |
| Pvap | 2345.00 | kPa | 345.26 | Isother... |
| Pvap | 2486.00 | kPa | 347.82 | Vapor L... |
| Pvap | 2500.50 | kPa | 348.22 | Experim... |
| Pvap | 2757.00 | kPa | 352.78 | Isother... |
| Pvap | 2778.20 | kPa | 353.14 | Isother... |
| Pvap | 2782.30 | kPa | 353.23 | Experim... |
| Pvap | 2903.00 | kPa | 355.24 | Experim... |
| Pvap | 2965.30 | kPa | 356.24 | Experim... |
| Pvap | 2998.50 | kPa | 356.76 | Experim... |
| Pvap | 3017.50 | kPa | 357.06 | Experim... |
| Pvap | 3031.00 | kPa | 357.27 | Experim... |
| Pvap | 3044.20 | kPa | 357.47 | Experim... |
| Pvap | 3050.40 | kPa | 357.56 | Experim... |
| Pvap | 3095.10 | kPa | 358.26 | Experim... |
| Pvap | 3128.10 | kPa | 358.76 | Experim... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 2000.00 | 1326.6 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 1130.00 | 273.17 | 488.3 |
| 1150.00 | 253.27 | 575.6 |
| 1160.00 | 288.15 | 424.2 |
| 1990.00 | 303.15 | 370.7 |
| 2300.00 | 323.18 | 288.3 |
| 4760.00 | 343.19 | 245.5 |
| 5200.00 | 288.15 | 468.9 |
| 8270.00 | 343.19 | 311.3 |
| 10090.00 | 303.15 | 463.9 |
| 10130.00 | 288.15 | 513.8 |
| 10400.00 | 273.17 | 567.9 |
| 10440.00 | 343.19 | 341.8 |
| 10450.00 | 363.15 | 287.0 |
| 10550.00 | 323.18 | 404.9 |
| 10940.00 | 253.27 | 645.3 |
| 15690.00 | 383.16 | 310.6 |
| 16670.00 | 403.14 | 288.3 |
| 19600.00 | 423.15 | 293.5 |
| 25040.00 | 273.17 | 660.8 |
| 25100.00 | 423.15 | 345.1 |
| 25130.00 | 448.15 | 318.1 |
| 25160.00 | 303.15 | 576.7 |
| 25160.00 | 473.14 | 298.7 |
| 25190.00 | 288.15 | 618.0 |
| 25500.00 | 363.15 | 442.0 |
| 25610.00 | 403.14 | 375.7 |
| 25690.00 | 383.16 | 407.4 |
| 25910.00 | 253.27 | 728.8 |
| 28790.00 | 323.18 | 547.0 |
| 50080.00 | 288.15 | 741.2 |
| 50150.00 | 273.17 | 779.5 |
| 50380.00 | 323.18 | 664.6 |
| 50460.00 | 473.14 | 462.3 |
| 50520.00 | 363.15 | 592.9 |
| 50530.00 | 383.16 | 562.3 |
| 50540.00 | 343.19 | 627.2 |
| 50710.00 | 448.15 | 485.0 |
| 50800.00 | 423.15 | 513.0 |
| 50890.00 | 403.14 | 537.5 |
| 50920.00 | 303.15 | 709.3 |
| 52820.00 | 253.27 | 844.3 |
| 75030.00 | 253.27 | 921.1 |
| 75240.00 | 448.15 | 596.6 |
| 75280.00 | 273.17 | 871.7 |
| 75340.00 | 323.18 | 767.2 |
| 75370.00 | 303.15 | 804.5 |
| 75400.00 | 423.15 | 623.9 |
| 75440.00 | 288.15 | 837.6 |
| 75490.00 | 363.15 | 700.6 |
| 75570.00 | 473.14 | 576.7 |
| 75610.00 | 343.19 | 730.9 |
| 75640.00 | 403.14 | 647.4 |
| 75940.00 | 383.16 | 673.9 |
| 100060.00 | 403.14 | 737.1 |
| 100170.00 | 288.15 | 916.1 |
| 100220.00 | 473.14 | 666.6 |
| 100230.00 | 273.17 | 949.0 |
| 100300.00 | 363.15 | 787.2 |
| 100500.00 | 383.16 | 761.1 |
| 100560.00 | 303.15 | 886.5 |
| 100630.00 | 253.27 | 997.3 |
| 100650.00 | 343.19 | 818.3 |
| 100710.00 | 423.15 | 715.4 |
| 100750.00 | 448.15 | 689.4 |
| 101090.00 | 323.18 | 852.8 |
| 125070.00 | 323.18 | 921.8 |
| 125170.00 | 343.19 | 890.4 |
| 125230.00 | 363.15 | 861.9 |
| 125320.00 | 423.15 | 791.3 |
| 125410.00 | 303.15 | 956.2 |
| 125430.00 | 273.17 | 1017.1 |
| 125510.00 | 288.15 | 986.4 |
| 125570.00 | 473.14 | 745.3 |
| 125630.00 | 383.16 | 837.2 |
| 125630.00 | 403.14 | 813.6 |
| 125710.00 | 448.15 | 766.5 |
| 125810.00 | 253.27 | 1063.0 |
| 150160.00 | 423.15 | 858.8 |
| 150270.00 | 273.17 | 1077.5 |
| 150340.00 | 343.19 | 956.2 |
| 150340.00 | 363.15 | 928.6 |
| 150360.00 | 403.14 | 880.3 |
| 150460.00 | 383.16 | 903.4 |
| 150630.00 | 288.15 | 1048.4 |
| 150670.00 | 323.18 | 987.4 |
| 150690.00 | 473.14 | 814.0 |
| 150770.00 | 448.15 | 834.5 |
| 150900.00 | 303.15 | 1020.1 |
| 151420.00 | 253.27 | 1123.6 |
| 174830.00 | 253.27 | 1174.3 |
| 175160.00 | 343.19 | 1014.7 |
| 175250.00 | 288.15 | 1103.9 |
| 175320.00 | 448.15 | 894.5 |
| 175340.00 | 303.15 | 1075.6 |
| 175410.00 | 423.15 | 920.3 |
| 175590.00 | 363.15 | 988.8 |
| 175620.00 | 403.14 | 941.6 |
| 175680.00 | 323.18 | 1045.2 |
| 175720.00 | 473.14 | 875.3 |
| 175770.00 | 383.16 | 964.4 |
| 175810.00 | 273.17 | 1133.8 |
| 200290.00 | 343.19 | 1069.0 |
| 200320.00 | 363.15 | 1042.8 |
| 200450.00 | 253.27 | 1224.7 |
| 200520.00 | 423.15 | 976.3 |
| 200670.00 | 403.14 | 997.2 |
| 200700.00 | 273.17 | 1184.6 |
| 200700.00 | 288.15 | 1156.6 |
| 200740.00 | 383.16 | 1019.4 |
| 200750.00 | 323.18 | 1098.6 |
| 200800.00 | 473.14 | 931.7 |
| 200820.00 | 448.15 | 951.6 |
| 200830.00 | 303.15 | 1129.0 |
| 250190.00 | 303.15 | 1221.9 |
| 250220.00 | 343.19 | 1165.9 |
| 250260.00 | 383.16 | 1116.8 |
| 250380.00 | 288.15 | 1249.0 |
| 250420.00 | 423.15 | 1075.9 |
| 250500.00 | 403.14 | 1096.0 |
| 250580.00 | 253.27 | 1315.5 |
| 250600.00 | 473.14 | 1031.5 |
| 250610.00 | 363.15 | 1141.2 |
| 250620.00 | 323.18 | 1193.8 |
| 250800.00 | 273.17 | 1276.7 |
| 250910.00 | 448.15 | 1051.8 |
| 299650.00 | 253.27 | 1393.8 |
| 300040.00 | 288.15 | 1331.1 |
| 300360.00 | 363.15 | 1226.7 |
| 300390.00 | 423.15 | 1163.6 |
| 300400.00 | 323.18 | 1278.0 |
| 300450.00 | 273.17 | 1358.2 |
| 300620.00 | 343.19 | 1252.0 |
| 300640.00 | 473.14 | 1119.7 |
| 300660.00 | 403.14 | 1183.8 |
| 300690.00 | 383.16 | 1204.6 |
| 300750.00 | 303.15 | 1306.5 |
| 300780.00 | 448.15 | 1139.3 |
| 350100.00 | 343.19 | 1327.9 |
| 350190.00 | 253.27 | 1468.5 |
| 350280.00 | 383.16 | 1282.6 |
| 350300.00 | 303.15 | 1381.1 |
| 350560.00 | 473.14 | 1199.0 |
| 350600.00 | 423.15 | 1243.0 |
| 350610.00 | 403.14 | 1262.3 |
| 350690.00 | 363.15 | 1305.3 |
| 350710.00 | 448.15 | 1218.3 |
| 350810.00 | 323.18 | 1355.4 |
| 350820.00 | 273.17 | 1432.3 |
| 350970.00 | 288.15 | 1407.7 |
| 400020.00 | 303.15 | 1450.2 |
| 400090.00 | 273.17 | 1499.6 |
| 400260.00 | 363.15 | 1376.0 |
| 400280.00 | 403.14 | 1333.6 |
| 400370.00 | 343.19 | 1399.8 |
| 400410.00 | 288.15 | 1475.2 |
| 400510.00 | 383.16 | 1354.3 |
| 400580.00 | 323.18 | 1424.9 |
| 400740.00 | 253.27 | 1535.4 |
| 400750.00 | 473.14 | 1272.0 |
| 400820.00 | 448.15 | 1291.1 |
| 400920.00 | 423.15 | 1315.6 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [173.19; 263.52] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.37505e+01 | |||
| Coefficient B | -2.04277e+03 | |||
| Coefficient C | -2.14600e+01 | |||
| Temperature range, min. | 173.19 | |||
| Temperature range, max. | 263.52 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 200 250 | ||||
| Pvap | 1.33 | kPa | 173.19 | Calculated Property |
| Pvap | 3.07 | kPa | 183.23 | Calculated Property |
| Pvap | 6.43 | kPa | 193.26 | Calculated Property |
| Pvap | 12.39 | kPa | 203.30 | Calculated Property |
| Pvap | 22.29 | kPa | 213.34 | Calculated Property |
| Pvap | 37.84 | kPa | 223.37 | Calculated Property |
| Pvap | 61.10 | kPa | 233.41 | Calculated Property |
| Pvap | 94.47 | kPa | 243.45 | Calculated Property |
| Pvap | 140.66 | kPa | 253.48 | Calculated Property |
| Pvap | 202.63 | kPa | 263.52 | Calculated Property |
| Pvap | [4.07e-04; 2809.65] | kPa | [116.65; 368.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 3.44036e+01 | |||
| Coefficient B | -3.28864e+03 | |||
| Coefficient C | -2.94220e+00 | |||
| Coefficient D | -1.05992e-06 | |||
| Temperature range, min. | 116.65 | |||
| Temperature range, max. | 368.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 | ||||
| Pvap | 4.07e-04 | kPa | 116.65 | Calculated Property |
| Pvap | 0.05 | kPa | 144.58 | Calculated Property |
| Pvap | 1.17 | kPa | 172.51 | Calculated Property |
| Pvap | 10.57 | kPa | 200.43 | Calculated Property |
| Pvap | 52.90 | kPa | 228.36 | Calculated Property |
| Pvap | 178.38 | kPa | 256.29 | Calculated Property |
| Pvap | 456.90 | kPa | 284.22 | Calculated Property |
| Pvap | 959.39 | kPa | 312.14 | Calculated Property |
| Pvap | 1737.31 | kPa | 340.07 | Calculated Property |
| Pvap | 2809.65 | kPa | 368.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Propene, hexafluoro-.
Mixtures
- Propene, hexafluoro- + Ethylene
- Propane + Propene, hexafluoro-
- Butane + Propene, hexafluoro-
- Carbon dioxide + Propene, hexafluoro-
- 1-Butene + Propene, hexafluoro-
- Propene + Propene, hexafluoro-
- Propene, hexafluoro- + Cyclohexane, methyl-
- Propene, hexafluoro- + Cyclohexane
- n-Hexane + Propene, hexafluoro-
- Propene, hexafluoro- + 2,2,3,3,4,4,4-Heptafluoro-butanol
- Propene, hexafluoro- + Furan, tetrahydro-2-methyl-
- Ethane + Propene, hexafluoro-
- Ethene, tetrafluoro- + Propene, hexafluoro-
- Propene, hexafluoro- + Hexafluoropropylene oxide
- Ethane, hexafluoro- + Propene, hexafluoro-
- Toluene + Propene, hexafluoro-
- Propene, hexafluoro- + Ethane, 2,2-dichloro-1,1,1-trifluoro-
- Propene, hexafluoro- + Cyclobutane, octafluoro-
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
- Phase equilibrium data for mixtures involving 1,1,2,3,3,3-hexafluoro-1-propene with either propane or n-butane between 312 and 343 K
- Phase equilibrium data for binary mixtures of carbon dioxide with {1,1,2,3,3,3-hexafluoro-1-propene or 2,2,3-trifluoro-3- (trifluoromethyl)oxirane} at temperatures between (233 and 273) K
- Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
- Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
- Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
- Vapor-Liquid Equilibrium Data for Binary Systems Consisting of Either Hexafluoropropene (HFP) or 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane (HFPO) with Carbon Dioxide (R-744) or 2,2-Dichloro-1,1,1-trifluoroethane (R-123)
- Vapor Liquid Equilibrium Measurements and Modeling for the Ethane (R-170) + 1,1,2,3,3,3-Hexafluoro-1-propene (R-1216) Binary System
- Speeds of Sound in Liquid and Supercritical Hexafluoropropylene (HFP) and Hexafluoropropylene Oxide (HFPO) at Pressures up to 400 MPa
- Liquid-Phase p-rho-T Data for 2,3,3,3-Tetrafluoroprop-1-ene (R-1234yf) and 1,1,2,3,3,3-Hexafluoroprop-1-ene (R-1216) at Temperatures from (208 to 353) K under Pressures up to 40 MPa
- Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K
- Isothermal Vapor Liquid Equilibrium Data for the Binary System 1,1,2,3,3,3-Hexafluoro-1-propene (R1216) + 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane from (268.13 to 308.19) K
- Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,3,3,3-Hexafluoroprop-1-ene +1,1,2,2,3,3,4,4-Octafluorocyclobutane Binary System: Measurement and Modeling from (292 to 352) K and Pressures up to 2.6 MPa
- Pure Component and Binary Vapor-Liquid Equilibrium + Modeling for Hexafluoropropylene and Hexafluoropropylene Oxide with Toluene and Hexafluoroethane
- Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene
- Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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