- InChI
- InChI=1S/C3H8O2/c1-3(5)2-4/h3-5H,2H2,1H3
- InChI Key
- DNIAPMSPPWPWGF-UHFFFAOYSA-N
- Formula
- C3H8O2
- SMILES
- CC(O)CO
- Molecular Weight1
- 76.09
- CAS
- 4254-16-4
- Other Names
-
- (.+-.)-1,2-propanediol
- (.+/-.)-1,2-Propanediol
- (R,S)-1,2-propanediol
- (RS)-1,2-Propanediol
- 1,2-Propandiol
- 1,2-Propylenglykol
- 1,2-dihydroxypropane
- 1,2-propanediol
- 1,2-propanediol (propylene glycol)
- 1,2-propylene glycol
- 2,3-Propanediol
- 2-hydroxypropanol
- DL-1,2-Propanediol
- DL-Propylene glycol
- Dowfrost
- Ilexan P
- Isopropylene glycol
- Methylethyl glycol
- Methylethylene glycol
- Monopropylene glycol
- NSC 69860
- PG 12
- Prolugen
- Propylene glycol USP
- Propylenglycol
- Sentry Propylene Glycol
- Sirlene
- Solar winter ban
- Solargard P
- Trimethyl glycol
- Ucar 35
- propane-1,2-diol
- propanediol
- propylene glycol (1,2-propanediol)
- «alpha»-Propylene glycol
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- εr : Dielectric Constant (Relative permittivity).
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- vspec : Specific Volume (m3/kg).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6581 | Relay (1.0) Calculated Property | |
| μ | 3.60 | debye | KDB |
| ΔfG° | -301.70 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -424.20 | kJ/mol | KDB |
| ΔfusH° | 8.18 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 72.66 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.24 | eV | Relay (1.0) Calculated Property |
| log10WS | 0.96 | Relay (1.0) Calculated Property | |
| logPoct/wat | -0.640 | Crippen Calculated Property | |
| McVol | 64.870 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 6070.00 | kPa | KDB |
| Tboil | 460.50 | K | KDB |
| Tc | 625.00 | K | KDB |
| Tfus | 213.00 | K | KDB |
| Vc | 0.237 | m3/kmol | KDB |
| Zc | 0.2768350 | KDB |
Temperature Dependent Properties
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 98.00 | 1032.56 |
| 303.15 | 98.00 | 1028.87 |
| 312.98 | 98.00 | 1022.16 |
| 335.78 | 98.00 | 1005.31 |
| 364.39 | 98.00 | 981.63 |
| 394.95 | 98.00 | 953.22 |
| 423.51 | 98.00 | 926.76 |
| 452.17 | 98.00 | 900.36 |
| 298.15 | 49030.00 | 1055.29 |
| 303.15 | 49030.00 | 1052.03 |
| 313.00 | 49030.00 | 1046.22 |
| 335.80 | 49030.00 | 1029.3 |
| 364.66 | 49030.00 | 1007.36 |
| 395.11 | 49030.00 | 982.98 |
| 423.62 | 49030.00 | 959.18 |
| 452.10 | 49030.00 | 934.51 |
| 298.15 | 98060.00 | 1072.94 |
| 303.15 | 98060.00 | 1070.79 |
| 313.05 | 98060.00 | 1065.24 |
| 335.76 | 98060.00 | 1050.34 |
| 364.83 | 98060.00 | 1031.15 |
| 395.17 | 98060.00 | 1010.62 |
| 423.90 | 98060.00 | 989.94 |
| 452.14 | 98060.00 | 965.53 |
| 298.15 | 147100.00 | 1088.48 |
| 303.15 | 147100.00 | 1086.25 |
| 313.03 | 147100.00 | 1081.67 |
| 335.78 | 147100.00 | 1068.19 |
| 364.87 | 147100.00 | 1051.61 |
| 395.38 | 147100.00 | 1033.92 |
| 423.97 | 147100.00 | 1016.34 |
| 452.19 | 147100.00 | 996.01 |
| 298.15 | 196130.00 | 1104.32 |
| 303.15 | 196130.00 | 1101.4 |
| 313.04 | 196130.00 | 1095.69 |
| 335.80 | 196130.00 | 1082.92 |
| 365.00 | 196130.00 | 1067.32 |
| 395.57 | 196130.00 | 1051.9 |
| 424.05 | 196130.00 | 1038.38 |
| 452.18 | 196130.00 | 1022.83 |
| 298.15 | 245160.00 | 1115.28 |
| 303.15 | 245160.00 | 1112.65 |
| 313.03 | 245160.00 | 1107.51 |
| 336.01 | 245160.00 | 1095.8 |
| 364.99 | 245160.00 | 1081.56 |
| 395.68 | 245160.00 | 1067.12 |
| 424.30 | 245160.00 | 1054.25 |
| 452.07 | 245160.00 | 1042.31 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 1047.1 |
| 278.15 | 1000.00 | 1047.3 |
| 278.15 | 5000.00 | 1049.2 |
| 278.15 | 10000.00 | 1051.2 |
| 278.15 | 15000.00 | 1053.4 |
| 278.15 | 20000.00 | 1055.5 |
| 278.15 | 25000.00 | 1057.6 |
| 278.15 | 30000.00 | 1059.6 |
| 278.15 | 35000.00 | 1061.6 |
| 278.15 | 40000.00 | 1063.6 |
| 278.15 | 45000.00 | 1065.6 |
| 278.15 | 50000.00 | 1067.5 |
| 278.15 | 55000.00 | 1069.3 |
| 278.15 | 60000.00 | 1071.4 |
| 288.15 | 100.00 | 1039.9 |
| 288.15 | 1000.00 | 1040.2 |
| 288.15 | 5000.00 | 1042.1 |
| 288.15 | 10000.00 | 1044.4 |
| 288.15 | 15000.00 | 1046.7 |
| 288.15 | 20000.00 | 1048.9 |
| 288.15 | 25000.00 | 1051.1 |
| 288.15 | 30000.00 | 1053.2 |
| 288.15 | 35000.00 | 1055.4 |
| 288.15 | 40000.00 | 1057.4 |
| 288.15 | 45000.00 | 1059.4 |
| 288.15 | 50000.00 | 1061.4 |
| 288.15 | 55000.00 | 1063.4 |
| 288.15 | 60000.00 | 1065.3 |
| 298.15 | 100.00 | 1032.5 |
| 298.15 | 1000.00 | 1032.9 |
| 298.15 | 5000.00 | 1034.8 |
| 298.15 | 10000.00 | 1037.2 |
| 298.15 | 15000.00 | 1039.6 |
| 298.15 | 20000.00 | 1041.9 |
| 298.15 | 25000.00 | 1044.1 |
| 298.15 | 30000.00 | 1046.3 |
| 298.15 | 35000.00 | 1048.4 |
| 298.15 | 40000.00 | 1050.6 |
| 298.15 | 45000.00 | 1052.5 |
| 298.15 | 50000.00 | 1054.6 |
| 298.15 | 55000.00 | 1056.6 |
| 298.15 | 60000.00 | 1058.5 |
| 308.15 | 100.00 | 1025.3 |
| 308.15 | 1000.00 | 1025.5 |
| 308.15 | 5000.00 | 1027.5 |
| 308.15 | 10000.00 | 1030.1 |
| 308.15 | 15000.00 | 1032.5 |
| 308.15 | 20000.00 | 1034.9 |
| 308.15 | 25000.00 | 1037.2 |
| 308.15 | 30000.00 | 1039.5 |
| 308.15 | 35000.00 | 1041.6 |
| 308.15 | 40000.00 | 1043.8 |
| 308.15 | 45000.00 | 1046.0 |
| 308.15 | 50000.00 | 1048.1 |
| 308.15 | 55000.00 | 1050.1 |
| 308.15 | 60000.00 | 1052.2 |
| 318.15 | 100.00 | 1017.7 |
| 318.15 | 1000.00 | 1018.0 |
| 318.15 | 5000.00 | 1020.2 |
| 318.15 | 10000.00 | 1022.8 |
| 318.15 | 15000.00 | 1025.4 |
| 318.15 | 20000.00 | 1027.9 |
| 318.15 | 25000.00 | 1030.3 |
| 318.15 | 30000.00 | 1032.7 |
| 318.15 | 35000.00 | 1035.0 |
| 318.15 | 40000.00 | 1037.2 |
| 318.15 | 45000.00 | 1039.4 |
| 318.15 | 50000.00 | 1041.5 |
| 318.15 | 55000.00 | 1043.6 |
| 318.15 | 60000.00 | 1045.7 |
| 328.15 | 100.00 | 1010.0 |
| 328.15 | 1000.00 | 1010.3 |
| 328.15 | 5000.00 | 1012.7 |
| 328.15 | 10000.00 | 1015.4 |
| 328.15 | 15000.00 | 1018.0 |
| 328.15 | 20000.00 | 1020.6 |
| 328.15 | 25000.00 | 1023.1 |
| 328.15 | 30000.00 | 1025.6 |
| 328.15 | 35000.00 | 1027.9 |
| 328.15 | 40000.00 | 1030.3 |
| 328.15 | 45000.00 | 1032.5 |
| 328.15 | 50000.00 | 1034.7 |
| 328.15 | 55000.00 | 1036.9 |
| 328.15 | 60000.00 | 1039.0 |
| 338.15 | 100.00 | 1002.2 |
| 338.15 | 1000.00 | 1002.4 |
| 338.15 | 5000.00 | 1004.8 |
| 338.15 | 10000.00 | 1007.6 |
| 338.15 | 15000.00 | 1010.4 |
| 338.15 | 20000.00 | 1013.0 |
| 338.15 | 25000.00 | 1015.6 |
| 338.15 | 30000.00 | 1018.2 |
| 338.15 | 35000.00 | 1020.7 |
| 338.15 | 40000.00 | 1023.2 |
| 338.15 | 45000.00 | 1025.5 |
| 338.15 | 50000.00 | 1027.9 |
| 338.15 | 55000.00 | 1030.2 |
| 338.15 | 60000.00 | 1032.4 |
| 348.15 | 100.00 | 994.1 |
| 348.15 | 1000.00 | 994.5 |
| 348.15 | 5000.00 | 996.9 |
| 348.15 | 10000.00 | 999.9 |
| 348.15 | 15000.00 | 1002.8 |
| 348.15 | 20000.00 | 1005.5 |
| 348.15 | 25000.00 | 1008.2 |
| 348.15 | 30000.00 | 1010.9 |
| 348.15 | 35000.00 | 1013.4 |
| 348.15 | 40000.00 | 1016.0 |
| 348.15 | 45000.00 | 1018.4 |
| 348.15 | 50000.00 | 1020.9 |
| 348.15 | 55000.00 | 1023.2 |
| 348.15 | 60000.00 | 1025.6 |
| 358.15 | 100.00 | 985.8 |
| 358.15 | 1000.00 | 986.2 |
| 358.15 | 5000.00 | 988.8 |
| 358.15 | 10000.00 | 991.9 |
| 358.15 | 15000.00 | 995.0 |
| 358.15 | 20000.00 | 997.8 |
| 358.15 | 25000.00 | 1000.6 |
| 358.15 | 30000.00 | 1003.4 |
| 358.15 | 35000.00 | 1006.0 |
| 358.15 | 40000.00 | 1008.5 |
| 358.15 | 45000.00 | 1011.2 |
| 358.15 | 50000.00 | 1013.6 |
| 358.15 | 55000.00 | 1016.1 |
| 358.15 | 60000.00 | 1018.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 272.69 | 5240.00 | 1054.19 |
| 272.68 | 10290.00 | 1056.38 |
| 272.68 | 15270.00 | 1058.53 |
| 272.72 | 20360.00 | 1060.64 |
| 272.73 | 30580.00 | 1064.73 |
| 272.73 | 50680.00 | 1072.45 |
| 272.77 | 71000.00 | 1079.68 |
| 272.74 | 91400.00 | 1086.61 |
| 272.76 | 50810.00 | 1072.51 |
| 272.78 | 15370.00 | 1058.52 |
| 293.18 | 5180.00 | 1039.1 |
| 293.18 | 10100.00 | 1041.39 |
| 293.18 | 15210.00 | 1043.73 |
| 293.18 | 20190.00 | 1045.96 |
| 293.18 | 30240.00 | 1050.35 |
| 293.18 | 50550.00 | 1058.66 |
| 293.18 | 70760.00 | 1066.35 |
| 293.18 | 90990.00 | 1073.55 |
| 293.18 | 50680.00 | 1058.72 |
| 293.18 | 15310.00 | 1043.77 |
| 313.12 | 5120.00 | 1024.21 |
| 313.13 | 10070.00 | 1026.73 |
| 313.13 | 15110.00 | 1029.21 |
| 313.12 | 20290.00 | 1031.71 |
| 313.13 | 30290.00 | 1036.38 |
| 313.12 | 50710.00 | 1045.31 |
| 313.12 | 71030.00 | 1053.5 |
| 313.12 | 91240.00 | 1061.08 |
| 313.12 | 50990.00 | 1045.42 |
| 313.12 | 15580.00 | 1029.43 |
| 352.99 | 5010.00 | 993.23 |
| 353.00 | 10100.00 | 996.26 |
| 353.00 | 15280.00 | 999.29 |
| 352.99 | 20210.00 | 1002.06 |
| 352.99 | 30360.00 | 1007.57 |
| 353.00 | 50610.00 | 1017.74 |
| 352.99 | 70750.00 | 1027.01 |
| 352.99 | 91060.00 | 1035.61 |
| 352.99 | 50620.00 | 1017.76 |
| 352.99 | 15390.00 | 999.36 |
| 392.94 | 5080.00 | 959.54 |
| 392.94 | 10090.00 | 963.15 |
| 392.95 | 15190.00 | 966.67 |
| 392.96 | 20230.00 | 970.02 |
| 392.97 | 30430.00 | 976.54 |
| 392.95 | 50730.00 | 988.44 |
| 392.94 | 70890.00 | 999.07 |
| 392.94 | 90950.00 | 1008.71 |
| 392.95 | 50820.00 | 988.49 |
| 392.96 | 15180.00 | 966.75 |
| 283.21 | 5190.00 | 1046.44 |
| 283.19 | 10060.00 | 1048.67 |
| 283.17 | 15100.00 | 1050.92 |
| 283.17 | 20200.00 | 1053.13 |
| 283.17 | 30530.00 | 1057.48 |
| 283.18 | 50550.00 | 1065.43 |
| 283.19 | 70990.00 | 1072.96 |
| 283.18 | 91270.00 | 1079.99 |
| 283.18 | 50490.00 | 1065.4 |
| 283.17 | 15140.00 | 1050.94 |
| 298.12 | 5090.00 | 1035.37 |
| 298.12 | 10070.00 | 1037.74 |
| 298.12 | 15240.00 | 1040.15 |
| 298.12 | 20170.00 | 1042.4 |
| 298.12 | 30300.00 | 1046.89 |
| 298.12 | 50590.00 | 1055.32 |
| 298.11 | 70930.00 | 1063.17 |
| 298.12 | 91050.00 | 1070.41 |
| 298.12 | 50650.00 | 1055.35 |
| 298.12 | 15160.00 | 1040.11 |
| 333.05 | 5260.00 | 1009.12 |
| 333.05 | 10050.00 | 1011.76 |
| 333.05 | 15120.00 | 1014.46 |
| 333.05 | 20250.00 | 1017.1 |
| 333.05 | 30400.00 | 1022.19 |
| 333.05 | 50610.00 | 1031.67 |
| 333.06 | 70910.00 | 1040.39 |
| 333.06 | 91130.00 | 1048.43 |
| 333.06 | 51080.00 | 1031.87 |
| 333.06 | 15210.00 | 1014.48 |
| 373.34 | 10320.00 | 980.11 |
| 373.34 | 15330.00 | 983.26 |
| 373.34 | 20360.00 | 986.4 |
| 373.34 | 30530.00 | 992.32 |
| 373.34 | 50610.00 | 1003.25 |
| 373.34 | 70990.00 | 1013.23 |
| 373.35 | 91190.00 | 1022.41 |
| 373.35 | 50860.00 | 1003.34 |
| 373.35 | 15540.00 | 983.34 |
| 373.35 | 5160.00 | 976.65 |
| 313.03 | 5190.00 | 1024.2 |
| 313.03 | 10100.00 | 1026.69 |
| 313.03 | 15280.00 | 1029.25 |
| 313.03 | 20240.00 | 1031.64 |
| 313.03 | 30440.00 | 1036.4 |
| 313.03 | 50660.00 | 1045.24 |
| 313.03 | 70960.00 | 1053.42 |
| 313.03 | 91090.00 | 1061.0 |
| 313.03 | 50710.00 | 1045.28 |
| 313.03 | 15210.00 | 1029.23 |
| Reference | ||
Speed of sound, m/s
Operational condition: Frequency, MHz = 8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 99.00 | 1494.429 |
| 303.15 | 5091.00 | 1513.504 |
| 303.15 | 10060.00 | 1532.024 |
| 303.15 | 15098.00 | 1550.199 |
| 303.15 | 20084.00 | 1567.713 |
| 303.15 | 25068.00 | 1584.711 |
| 303.15 | 30167.00 | 1601.587 |
| 313.15 | 99.00 | 1465.858 |
| 313.15 | 5014.00 | 1485.499 |
| 313.15 | 10053.00 | 1504.824 |
| 313.15 | 15011.00 | 1523.212 |
| 313.15 | 20095.00 | 1541.536 |
| 313.15 | 25202.00 | 1559.357 |
| 313.15 | 30222.00 | 1576.498 |
| 333.15 | 100.00 | 1408.863 |
| 333.15 | 5039.00 | 1429.721 |
| 333.15 | 10054.00 | 1450.066 |
| 333.15 | 15107.00 | 1469.848 |
| 333.15 | 20131.00 | 1488.963 |
| 333.15 | 25131.00 | 1507.384 |
| 333.15 | 30024.00 | 1524.874 |
| 353.15 | 99.00 | 1350.887 |
| 353.15 | 5042.00 | 1373.03 |
| 353.15 | 10055.00 | 1394.56 |
| 353.15 | 15135.00 | 1415.607 |
| 353.15 | 20093.00 | 1435.461 |
| 353.15 | 25086.00 | 1454.828 |
| 353.15 | 30207.00 | 1474.064 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [93.81; 211.98] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 9.06100e+00 | |||
| Coefficient B | 3.62720e-01 | |||
| Coefficient C | -2.03400e-04 | |||
| Coefficient D | 4.36000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 93.81 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 113.86 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 131.85 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 147.93 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 162.24 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 174.91 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 186.08 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 195.89 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 204.48 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 211.98 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.40; 208.10] | kPa | [335.73; 485.20] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.64972e+01 | |||
| Coefficient B | -4.64181e+03 | |||
| Coefficient C | -6.92380e+01 | |||
| Temperature range, min. | 335.73 | |||
| Temperature range, max. | 485.20 | |||
| Pvap | 0.40 | kPa | 335.73 | Calculated Property |
| Pvap | 1.11 | kPa | 352.34 | Calculated Property |
| Pvap | 2.74 | kPa | 368.95 | Calculated Property |
| Pvap | 6.19 | kPa | 385.55 | Calculated Property |
| Pvap | 12.87 | kPa | 402.16 | Calculated Property |
| Pvap | 24.96 | kPa | 418.77 | Calculated Property |
| Pvap | 45.58 | kPa | 435.38 | Calculated Property |
| Pvap | 79.01 | kPa | 451.98 | Calculated Property |
| Pvap | 130.83 | kPa | 468.59 | Calculated Property |
| Pvap | 208.10 | kPa | 485.20 | Calculated Property |
| Pvap | [8.87e-08; 6165.74] | kPa | [213.15; 626.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.23565e+02 | |||
| Coefficient B | -1.60975e+04 | |||
| Coefficient C | -3.08431e+01 | |||
| Coefficient D | 2.42067e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 213.15 | |||
| Temperature range, max. | 626.00 | |||
| Pvap | 8.87e-08 | kPa | 213.15 | Calculated Property |
| Pvap | 2.36e-04 | kPa | 259.02 | Calculated Property |
| Pvap | 0.03 | kPa | 304.89 | Calculated Property |
| Pvap | 0.91 | kPa | 350.77 | Calculated Property |
| Pvap | 9.52 | kPa | 396.64 | Calculated Property |
| Pvap | 55.54 | kPa | 442.51 | Calculated Property |
| Pvap | 227.08 | kPa | 488.38 | Calculated Property |
| Pvap | 751.49 | kPa | 534.26 | Calculated Property |
| Pvap | 2211.30 | kPa | 580.13 | Calculated Property |
| Pvap | 6165.74 | kPa | 626.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Propylene Glycol.
Mixtures
- Magnesium chloride + Propylene Glycol + Water
- Propylene Glycol + Water
- Propylene Glycol + Lithium chloride + Water
- lithium bromide + Propylene Glycol + Water
- Propylene Glycol + Carbon dioxide
- Propylene Glycol + sodium iodide + Methyl Alcohol
- Propylene Glycol + Methyl Alcohol
- Propylene Glycol + Methane
- Propylene Glycol + sodium chloride + Water
- Propylene Glycol + Propylamine
- Propylene Glycol + 2-Propanamine
- Propylene Glycol + Formamide
- Propylene Glycol + Butyl lactate
- Propylene Glycol + Threonine + Water
- Propylene Glycol + 1,2-Ethanediol
- 1,3-Propanediol + Propylene Glycol
- Propylene Glycol + Water + daidzein
- Propylene Glycol + daidzein
- 1-Propanol + Propylene Glycol
- Propylene Glycol + 1-Hexanol
Find more mixtures with Propylene Glycol.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Vapor liquid equilibrium in systems (water + organic solvent + salt) at low water concentrations but high ratios of salt to water: experimental results and modeling
- Thermodynamic study of the solubility of ibuprofen and naproxen in some ethanol + propylene glycol mixtures
- Methane and carbon dioxide solubility in 1,2-propylene glycol at temperatures ranging from 303 to 423 K and pressures up to 12 MPa
- Thermodynamic analysis of the solubility of ketoprofen in some propylene glycol + water cosolvent mixtures
- Thermodynamic studies of fluphenazine decanoate solubility in propylene glycol + water mixtures and correlation with the Jouyban Acree model
- Solution thermodynamics of indomethacin in propylene glycol + water mixtures
- Liquid phase behavior of hexafluorophosphate ionic liquids with polyhydric alcohols
- Solubility of sulfamethizole in some propylene glycol + water mixtures at several temperatures
- Solubility of sulfapyridine in propylene glycol + water mixtures and correlation with the Jouyban Acree model
- Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
- Measurement and correlation of the solubility of florfenicol in binary 1,2-propanediol + water mixtures from 293.15 K to 316.25 K
- Solubility of daidzein in propylene glycol plus water cosolvent mixtures
- Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
- Phase behavior of imidazolium and phosphonium tetrafluoroborates with dihydroxy alcohols
- tert-Butyl chloride as a probe of the solvophobic effects
- Vapor-liquid equilibrium for propylene glycols binary systems: Experimental data and regression
- Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
- Densities, surface tensions, and isobaric vapor-liquid equilibria for the mixtures of 2-propanol, water, and 1,2-propanediol
- Excess volumes and excess heat capacities of {1,2- alkanediol + methanol} mixtures and ionic volumes in these systems
- Volumetric, ultrasonic and spectroscopic (FT-IR) studies for the binary mixtures of imidazolium based ILs with 1,2-propanediol
- Density and viscosity of propylene glycol at high temperatures and high pressures
- Solubility evaluation and thermodynamic modeling of beta-lapachone in water and ten organic solvents at different temperatures
- Measurement and correlation of excess molar enthalpy for(1,2-propanediol, or 1,3-propanediol, or 1,4-butanediol + water) at the temperatures (298.15, 323.15, and 343.15) K
- Partial molar volumes of organic solutes in water. XIV. Polyhydric alcohols derived from ethane and propane at temperatures T = 298 K to T = 573 K and at pressures up to 30 MPa
- Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
- Densities and volumetric properties of (formamide + ethanol, or 1-propanol, or 1,2-ethanediol, or 1,2-propanediol) mixtures at temperatures between 293.15 K and 318.15 K
- Volumetric and compressibility properties of liquid water as a solute in glycolic, propylene carbonate, and tetramethylurea solutions at T = 298.15 K
- Excess molar volume and viscosity deviation for binary mixtures of polyethylene glycol dimethyl ether 250 with 1,2-alkanediols (C3 C6) at T = (293.15 to 323.15) K
- Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
- Experimental study of the excess molar volume of ternary mixtures containing {water + (1,2-propanediol, or 1,3-propanediol, or 1,2-butanediol, or 1,3-butanediol, or 1,4-butanediol, or 2,3-butanediol) + electrolytes} at a temperature of 298.15 K and atmospheric pressure
- Molar heat capacities of some aqueous 2-amino-2-hydroxymethyl-1,3-propanediol + glycol systems
- (Liquid + liquid) equilibrium data for the system (propylene glycol + water + tetraoctyl ammonium 2-methyl-1-naphthoate)
- Phase diagrams for (water + 1, 2-butanediol or 1, 2-propanediol + 2-ethyl-1-hexanol) systems: Experimental data and UNIQUAC
- Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
- Densities, viscosities, and refractive indices of the binary systems (PEG200 + 1,2-propanediol, +1,3-propanediol) and (PEG400 + 1,2-propanediol, +1,3-propanediol) at (288.15 to 333.15) K and atmospheric pressure: Measurements and modeling
- PqT measurements and derived properties of liquid 1,2-alkanediols
- Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
- Thermophysical characterization of aqueous ternary system containing n-tris-[hydroxymethyl]methyl-3-amino propanesulfonic acid and glycol (PG or DPG or TPG)
- Isobaric specific heat capacity of typical lithium chloride liquid desiccants using scanning calorimetry
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
- Thermal conductivity of dry anatase and rutile nano-powders and ethylene and propylene glycol-based TiO2 nanofluids
- Liquid extraction of polyhydric alcohols from water using [A336][SCN] as a solvent
- Solubility of rosuvastatin calcium in different neat solvents at different temperatures
- Excess properties and isobaric (vapor + liquid) equilibrium at sub-atmospheric pressures of binary (1,2-propanediol + 1,3-propanediol) system: Measurement and modelling
- Equilibrium solubility of sodium 2,4-diaminobenzene sulfonate in liquid mixtures (methanol + water, isopropanol + water, and 1,2-propanediol + water) from 273.15 K to 323.15 K
- Solubility and thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
- Speed of sound in saturated aliphatic alcohols (propan-2-ol, butan-2-ol, and 2-methylpropan-1-ol) and alkanediols (ethane-1,2-diol, propane-1,2- and -1,3-diol) at temperature between 253.15 K and 353.15 K and pressures up to 30 MPa
- Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
- Determination and correlation of solubility and thermodynamics of mixing of 4-aminobutyric acid in mono-solvents and binary solvent mixtures
- Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of 2-pyrrolidone with isomeric propanediols at temperatures from 303.15 K to 323.15 K
- Thermodynamic and transport properties of acetonitrile + alkanediols liquid mixtures at different temperatures, experimental measurements and modeling
- Equilibrium solubility, dissolution thermodynamics and preferential solvation of adenosine in aqueous solutions of N,N-dimethylformamide, N-methyl-2-pyrrolidone, dimethylsulfoxide and propylene glycol
- Potential heat transfer enhancement of functionalized graphene nanoplatelet dispersions in a propylene glycol-water mixture. Thermophysical profile
- Solubility modelling and preferential solvation of adenine in solvent mixtures of (N,N-dimethylformamide, N-methyl pyrrolidone, propylene glycol and dimethyl sulfoxide) plus water
- Measurement and correlation of the (p, rho, T) behavior of liquid propylene glycol at temperatures from (272.7 to 393.0) K and pressures up to 91.4 MPa
- Thermodynamic solubility modeling, solvent effect and preferential solvation of curcumin in aqueous co-solvent mixtures of ethanol, n-propanol, isopropanol and propylene glycol
- Solubility of CO2 in methanol, ethanol, 1,2-propanediol and glycerol from 283.15 K to 373.15 K and up to 6.0 MPa
- Enthalpies of solution of l-threonine in aqueous alcohol solutions
- Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
- Enthalpies of dilution of formamide in aqueous alcohol solutions at 298.15K
- Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
- DSC determination of partial ternary phase diagrams of methanol/sodium chloride/water and propylene glycol/sodium chloride/water and their applications for synthesized diagrams
- Heat Capacity of Several Mixed-Solvent Desiccants Containing Glycol + Water + MgCl2
- Molar heat capacity of several aqueous solutions of n-[tris(hydroxymethyl)methyl-3-amino]- propanesulfonic acid (TAPS) + glycol
- Thermodynamic study on some alkanediol solutions: measurement and molecular modeling
- Experimental measurements and modelling of volumetric properties, refractive index and viscosity of selected binary systems with butyl lactate at 288.15 to 323.15 K and atmospheric pressure. New UNIFAC-VISCO interaction parameters.
- Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
- Solubility and dissolution thermodynamics of N-(4-chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide in PG + water cosolvent mixtures at (298.15 to 338.15) K
- Isobaric Vapor Liquid Equilibria for Binary Systems of Diethyl Carbonate + Propylene Carbonate, Diethyl Carbonate + Propylene Glycol, and Ethanol + Propylene Carbonate at 101.3 kPa
- Solubility and Saturation Apparent Volume of Propranolol Hydrochloride in Some Binary Aqueous Cosolvent Mixtures at 298.15 K
- Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
- Solubility of Hydrogen Sulfide in Ethanediol, 1,2-Propanediol, 1-Propanol, and 2-Propanol: Experimental Measurement and Modeling
- Apparent Molar Volumes and Isentropic Compressibilities of Tetraalkylammonium Bromides in Aqueous Propane-1,2-diol. An Attempt to Design Hydraulic Liquids
- Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
- Solubility of Etoricoxib in Aqueous Solutions of Glycerin, Methanol, Polyethylene Glycols 200, 400, 600, and Propylene Glycol at 298.2 K
- Solubility and Modeling of Hesperidin in Cosolvent Mixtures of Ethanol, Isopropanol, Propylene Glycol, and n-Propanol + Water
- Density of Working Liquids for Diffusion Vacuum Pumps
- Viscosities, Densities, and Refractive Indices of Aqueous Propane-1,3-diol
- Thermophysical Properties of Ternary Systems Potassium Formate + Propylene Glycol/Glycerol + Water
- Solubility Determination and Modeling for Artesunate in Binary Solvent Mixtures of Methanol, Ethanol, Isopropanol, and Propylene Glycol + Water
- Experimental Solubility and Density Functional Theory Studies of Deferasirox in Binary Solvent Mixtures: Performance of Polarizable Continuum Model and Jouyban-Acree Model
- Measurement and Correlation of the Solubility of Palmatine Chloride in Four Different Binary Solvent Systems at (283.15-328.15) K
- Phase Equilibrium Involving Xylose, Water, and Ethylene Glycol or 1,2-Propylene Glycol at Different Temperatures
- Solubility of Bifonazole in Four Binary Solvent Mixtures: Experimental Measurement and Thermodynamic Modeling
- Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
- Densities, Dynamic Viscosities, Speeds of Sound, and Relative Permittivities for Water + Alkanediols (Propane-1,2- and -1,3-diol and Butane-1,2-, -1,3-, -1,4-, and -2,3-Diol) at Different Temperatures
- Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
- Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
- Solubility of Valdecoxib in the Presence of Glycerol, Propylene Glycol, and Poly(ethylene glycol) 400 at (298.15, 303.15, and 308.15) K
- Static Relative Permittivities of Water + Propane-1,2-diol and Water + Propane-1,3-diol under Pressures up to 300 MPa at 298.15 K
- Solubility of Rofecoxib in the Presence of Aqueous Solutions of Glycerol, Propylene Glycol, Ethanol, Span 20, Tween 80, and Sodium Lauryl Sulfate at (298.15, 303.15, and 308.15) K
- Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
- Solubility of 1H-1,2,4-Triazole in Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, Ethyl Formate, Methyl Acetate, Ethyl Acetate, and Butyl Acetate at (283 to 363) K
- Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
- Phase Equilibrium and Physical Properties for the Purification of Propylene Carbonate (PC) and y-Butyrolactone (GBL)
- Solubility of Dimethyl Fumarate in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Water from (289.95 to 347.15) K
- Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
- Solubility of Phenothiazine in Water, Ethanol, and Propylene Glycol at (298.2 to 338.2) K and Their Binary and Ternary Mixtures at 298.2 K
- Partial Molar Volumes and Partial Molar Isentropic Compressions of Three Polyhydric Alcohols Derived from Propane at Infinite Dilution in Water at Temperatures T = (278 to 318) K and Atmospheric Pressure
- Solubility of 3-Ethyl-5-methyl-(4RS)-2-((2-aminoethoxy)methyl)-4-(2-chlorophenyl)-1,4-dihydro-6-methyl-3,5-pyridinedicarboxylate Monobenzenesulfonate (Amlodipine Besylate) in Ethanol + Water and Propane-1,2-diol + Water Mixtures at Various Temperatures
- Solubility of Clonazepam and Diazepam in Polyethylene Glycol 200, Propylene Glycol, N-Methyl Pyrrolidone, Ethanol, and Water at (298.2 to 318.2) K and in Binary and Ternary Mixtures of Polyethylene Glycol 200, Propylene Glycol, and Water at 298.2 K
- Solubility, Density, Refractive Index, and Viscosity for the Polyhydric Alcohol + CsBr + H2O Ternary Systems at Different Temperatures
- Solid Liquid Equilibria of 1-Ethyl-3-methylimidazolium Hexafluorophosphate + Polyols
- Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
- Vapor Liquid Equilibrium for Ternary and Binary Mixtures of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa
- Heat Capacities of Four Promising Alternatives to Lithium Bromide Aqueous Solution in Absorption Refrigerators
- Solubilities of Carbon Dioxide in Eutectic Mixtures of Choline Chloride and Dihydric Alcohols
- Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
- Measurement and Correlation of Tadalafil Solubility in Five Pure Solvents at (298.15 to 333.15) K
- Solubility of Metoclopramide Hydrochloride in Six Green Solvents at (298.15 to 338.15) K
- Solubility of Bioactive Compound Hesperidin in Six Pure Solvents at (298.15 to 333.15) K
- Solubility of (2Z)-N-Cyclohexyl-2-(3-hydroxybenzylidine) Hydrazine Carbothioamide in Different Pure Solvents at (298.15 to 338.15) K
- Solubility of N-(4-Chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide (Isoniazid Analogue) in Five Pure Solvents at (298.15 to 338.15) K
- Correlation of Solubility of Bioactive Compound Reserpine in Eight Green Solvents at (298.15 to 338.15) K
- Measurement, Correlation, and Thermodynamics of Solubility of Isatin in Nine Different Green Solvents at (298.15 to 338.15) K
- Isobaric Vapor Liquid Equilibrium for Two Binary Systems{Propane-1,2-diol + Ethane-1,2-diol and Propane-1,2-diol + Butane-1,2-diol} at p = (10.0, 20.0, and 40.0) kPa
- Dielectric Constants of Aqueous Diisopropanolamine, Diethanolamine, N-Methyldiethanolamine, Triethanolamine, and 2-Amino-2-methyl-1-propanol Solutions
- Solubilities of 2-Methyl-1,4-naphthoquinone in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (293.15 to 337.92) K
- Study of the Acoustic and Thermodynamic Properties of 1,2- and 1,3-Propanediol by Means of High-Pressure Speed of Sound Measurements at Temperatures from (293 to 318) K and Pressures up to 101 MPa
- Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
- Solubility of Acetylsalicylic Acid in Ethanol, Acetone, Propylene Glycol, and 2-Propanol
- Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
- Solubilities of Menadione Sodium Bisulfite in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (297.67 to 337.76) K
- Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary and Ternary Liquid Mixtures of Methanol (1) + Ethanol (2) + 1,2-Propanediol (3) at P = 81.5 kPa
- Solubilities of Isonicotinic Acid in (Methanol, Ethanol, 1-Propanol, 2-Propanol, and 1,2-Propanediol, Respectively) from (289.65 to 358.75) K
- Solubility of Lamotrigine, Diazepam, Clonazepam, and Phenobarbital in Propylene Glycol + Water Mixtures at 298.15 K
- Solubility of 7-Chloro-2-methylamino-5-phenyl-3H-1,4-benzodiazepine-4-oxide, 7-Chloro-1,3-dihydro-1-methyl-5-phenyl-2H-1,4-benzodiazepin-2-one, and 7-Chloro-5-(2-chlorophenyl)-3-hydroxy-1,3-dihydro-1,4-benzodiazepin-2-one in (Propane-1,2-diol + Water) at a Temperature of 303.2 K
- Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
- Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
These property values are available through the Cheméo API. A free account gives you an access key.