- Name
- 1-Propanol
- InChI
- InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
- InChI Key
- BDERNNFJNOPAEC-UHFFFAOYSA-N
- Formula
- C3H8O
- SMILES
- CCCO
- Mol. Weight (g/mol)
- 60.09
- CAS
- 71-23-8
- Name
- Glycerin
- InChI
- InChI=1S/C3H8O3/c4-1-3(6)2-5/h3-6H,1-2H2
- InChI Key
- PEDCQBHIVMGVHV-UHFFFAOYSA-N
- Formula
- C3H8O3
- SMILES
- OCC(O)CO
- Mol. Weight (g/mol)
- 92.09
- CAS
- 56-81-5
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Datasets
- ρl - Mass density, kg/m3 (2)
- γ - Surface tension liquid-gas, N/m (2)
- Tboil - Boiling temperature at pressure P, K (2)
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Glycerin (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 799.6 |
| 298.15 | 0.0676 | 832.8 |
| 298.15 | 0.1402 | 867.3 |
| 298.15 | 0.2185 | 903.5 |
| 298.15 | 0.3031 | 942.9 |
| 298.15 | 0.3949 | 986.0 |
| 298.15 | 0.4946 | 1032.7 |
| 298.15 | 0.6036 | 1083.1 |
| 298.15 | 0.7230 | 1138.8 |
| 298.15 | 0.8545 | 1198.7 |
| 298.15 | 1.0000 | 1258.9 |
| 303.15 | 0.0000 | 795.5 |
| 303.15 | 0.0676 | 828.9 |
| 303.15 | 0.1402 | 863.2 |
| 303.15 | 0.2185 | 900.0 |
| 303.15 | 0.3031 | 939.3 |
| 303.15 | 0.3949 | 982.1 |
| 303.15 | 0.4946 | 1029.5 |
| 303.15 | 0.6036 | 1079.9 |
| 303.15 | 0.7230 | 1135.7 |
| 303.15 | 0.8545 | 1195.6 |
| 303.15 | 1.0000 | 1255.6 |
| 308.15 | 0.0000 | 791.5 |
| 308.15 | 0.0676 | 825.0 |
| 308.15 | 0.1402 | 859.4 |
| 308.15 | 0.2185 | 896.0 |
| 308.15 | 0.3031 | 935.6 |
| 308.15 | 0.3949 | 978.4 |
| 308.15 | 0.4946 | 1025.9 |
| 308.15 | 0.6036 | 1076.3 |
| 308.15 | 0.7230 | 1132.4 |
| 308.15 | 0.8545 | 1192.7 |
| 308.15 | 1.0000 | 1252.7 |
| 313.15 | 0.0000 | 787.3 |
| 313.15 | 0.0676 | 820.7 |
| 313.15 | 0.1402 | 855.4 |
| 313.15 | 0.2185 | 892.1 |
| 313.15 | 0.3031 | 931.5 |
| 313.15 | 0.3949 | 974.7 |
| 313.15 | 0.4946 | 1022.3 |
| 313.15 | 0.6036 | 1072.7 |
| 313.15 | 0.7230 | 1128.8 |
| 313.15 | 0.8545 | 1189.5 |
| 313.15 | 1.0000 | 1249.5 |
| 318.15 | 0.0000 | 783.3 |
| 318.15 | 0.0676 | 816.8 |
| 318.15 | 0.1402 | 851.3 |
| 318.15 | 0.2185 | 888.3 |
| 318.15 | 0.3031 | 927.7 |
| 318.15 | 0.3949 | 970.8 |
| 318.15 | 0.4946 | 1018.4 |
| 318.15 | 0.6036 | 1069.2 |
| 318.15 | 0.7230 | 1125.5 |
| 318.15 | 0.8545 | 1186.1 |
| 318.15 | 1.0000 | 1246.2 |
| 323.15 | 0.0000 | 779.0 |
| 323.15 | 0.0676 | 812.5 |
| 323.15 | 0.1402 | 847.2 |
| 323.15 | 0.2185 | 884.1 |
| 323.15 | 0.3031 | 923.6 |
| 323.15 | 0.3949 | 966.8 |
| 323.15 | 0.4946 | 1014.7 |
| 323.15 | 0.6036 | 1065.5 |
| 323.15 | 0.7230 | 1122.0 |
| 323.15 | 0.8545 | 1182.7 |
| 323.15 | 1.0000 | 1242.9 |
| 328.15 | 0.0000 | 774.9 |
| 328.15 | 0.0676 | 808.4 |
| 328.15 | 0.1402 | 843.1 |
| 328.15 | 0.2185 | 880.3 |
| 328.15 | 0.3031 | 919.7 |
| 328.15 | 0.3949 | 963.3 |
| 328.15 | 0.4946 | 1010.8 |
| 328.15 | 0.6036 | 1061.8 |
| 328.15 | 0.7230 | 1118.3 |
| 328.15 | 0.8545 | 1179.2 |
| 328.15 | 1.0000 | 1239.6 |
| 333.15 | 0.0000 | 770.8 |
| 333.15 | 0.0676 | 804.3 |
| 333.15 | 0.1402 | 839.2 |
| 333.15 | 0.2185 | 876.3 |
| 333.15 | 0.3031 | 915.7 |
| 333.15 | 0.3949 | 959.4 |
| 333.15 | 0.4946 | 1006.8 |
| 333.15 | 0.6036 | 1058.0 |
| 333.15 | 0.7230 | 1114.3 |
| 333.15 | 0.8545 | 1175.8 |
| 333.15 | 1.0000 | 1236.0 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Glycerin (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 799.6 |
| 298.15 | 0.0676 | 832.8 |
| 298.15 | 0.1402 | 867.3 |
| 298.15 | 0.2185 | 903.5 |
| 298.15 | 0.3031 | 942.9 |
| 298.15 | 0.3949 | 986.0 |
| 298.15 | 0.4946 | 1032.7 |
| 298.15 | 0.6036 | 1083.1 |
| 298.15 | 0.7230 | 1138.8 |
| 298.15 | 0.8545 | 1198.7 |
| 298.15 | 1.0000 | 1258.9 |
| 303.15 | 0.0000 | 795.5 |
| 303.15 | 0.0676 | 828.9 |
| 303.15 | 0.1402 | 863.2 |
| 303.15 | 0.2185 | 900.0 |
| 303.15 | 0.3031 | 939.3 |
| 303.15 | 0.3949 | 982.1 |
| 303.15 | 0.4946 | 1029.5 |
| 303.15 | 0.6036 | 1079.9 |
| 303.15 | 0.7230 | 1135.7 |
| 303.15 | 0.8545 | 1195.6 |
| 303.15 | 1.0000 | 1255.6 |
| 308.15 | 0.0000 | 791.5 |
| 308.15 | 0.0676 | 825.0 |
| 308.15 | 0.1402 | 859.4 |
| 308.15 | 0.2185 | 896.0 |
| 308.15 | 0.3031 | 935.6 |
| 308.15 | 0.3949 | 978.4 |
| 308.15 | 0.4946 | 1025.9 |
| 308.15 | 0.6036 | 1076.3 |
| 308.15 | 0.7230 | 1132.4 |
| 308.15 | 0.8545 | 1192.7 |
| 308.15 | 1.0000 | 1252.7 |
| 313.15 | 0.0000 | 787.3 |
| 313.15 | 0.0676 | 820.7 |
| 313.15 | 0.1402 | 855.4 |
| 313.15 | 0.2185 | 892.1 |
| 313.15 | 0.3031 | 931.5 |
| 313.15 | 0.3949 | 974.7 |
| 313.15 | 0.4946 | 1022.3 |
| 313.15 | 0.6036 | 1072.7 |
| 313.15 | 0.7230 | 1128.8 |
| 313.15 | 0.8545 | 1189.5 |
| 313.15 | 1.0000 | 1249.5 |
| 318.15 | 0.0000 | 783.3 |
| 318.15 | 0.0676 | 816.8 |
| 318.15 | 0.1402 | 851.3 |
| 318.15 | 0.2185 | 888.3 |
| 318.15 | 0.3031 | 927.7 |
| 318.15 | 0.3949 | 970.8 |
| 318.15 | 0.4946 | 1018.4 |
| 318.15 | 0.6036 | 1069.2 |
| 318.15 | 0.7230 | 1125.5 |
| 318.15 | 0.8545 | 1186.1 |
| 318.15 | 1.0000 | 1246.2 |
| 323.15 | 0.0000 | 779.0 |
| 323.15 | 0.0676 | 812.5 |
| 323.15 | 0.1402 | 847.2 |
| 323.15 | 0.2185 | 884.1 |
| 323.15 | 0.3031 | 923.6 |
| 323.15 | 0.3949 | 966.8 |
| 323.15 | 0.4946 | 1014.7 |
| 323.15 | 0.6036 | 1065.5 |
| 323.15 | 0.7230 | 1122.0 |
| 323.15 | 0.8545 | 1182.7 |
| 323.15 | 1.0000 | 1242.9 |
| 328.15 | 0.0000 | 774.9 |
| 328.15 | 0.0676 | 808.4 |
| 328.15 | 0.1402 | 843.1 |
| 328.15 | 0.2185 | 880.3 |
| 328.15 | 0.3031 | 919.7 |
| 328.15 | 0.3949 | 963.3 |
| 328.15 | 0.4946 | 1010.8 |
| 328.15 | 0.6036 | 1061.8 |
| 328.15 | 0.7230 | 1118.3 |
| 328.15 | 0.8545 | 1179.2 |
| 328.15 | 1.0000 | 1239.6 |
| 333.15 | 0.0000 | 770.8 |
| 333.15 | 0.0676 | 804.3 |
| 333.15 | 0.1402 | 839.2 |
| 333.15 | 0.2185 | 876.3 |
| 333.15 | 0.3031 | 915.7 |
| 333.15 | 0.3949 | 959.4 |
| 333.15 | 0.4946 | 1006.8 |
| 333.15 | 0.6036 | 1058.0 |
| 333.15 | 0.7230 | 1114.3 |
| 333.15 | 0.8545 | 1175.8 |
| 333.15 | 1.0000 | 1236.0 |
Surface tension liquid-gas, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
| 293.20 | 0.0000 | 0.0631 |
| 293.20 | 0.1000 | 0.0418 |
| 293.20 | 0.2000 | 0.0334 |
| 293.20 | 0.3000 | 0.0301 |
| 293.20 | 0.4000 | 0.0283 |
| 293.20 | 0.5000 | 0.0273 |
| 293.20 | 0.6000 | 0.0265 |
| 293.20 | 0.7000 | 0.0260 |
| 293.20 | 0.8000 | 0.0253 |
| 293.20 | 0.9000 | 0.0247 |
| 293.20 | 1.0000 | 0.0237 |
| 303.20 | 0.0000 | 0.0624 |
| 303.20 | 0.1000 | 0.0415 |
| 303.20 | 0.2000 | 0.0331 |
| 303.20 | 0.3000 | 0.0297 |
| 303.20 | 0.4000 | 0.0279 |
| 303.20 | 0.5000 | 0.0269 |
| 303.20 | 0.6000 | 0.0261 |
| 303.20 | 0.7000 | 0.0255 |
| 303.20 | 0.8000 | 0.0248 |
| 303.20 | 0.9000 | 0.0241 |
| 303.20 | 1.0000 | 0.0229 |
| 313.20 | 0.0000 | 0.0620 |
| 313.20 | 0.1000 | 0.0412 |
| 313.20 | 0.2000 | 0.0328 |
| 313.20 | 0.3000 | 0.0293 |
| 313.20 | 0.4000 | 0.0277 |
| 313.20 | 0.5000 | 0.0264 |
| 313.20 | 0.6000 | 0.0257 |
| 313.20 | 0.7000 | 0.0250 |
| 313.20 | 0.8000 | 0.0242 |
| 313.20 | 0.9000 | 0.0233 |
| 313.20 | 1.0000 | 0.0221 |
| 323.20 | 0.0000 | 0.0611 |
| 323.20 | 0.1000 | 0.0409 |
| 323.20 | 0.2000 | 0.0325 |
| 323.20 | 0.3000 | 0.0289 |
| 323.20 | 0.4000 | 0.0272 |
| 323.20 | 0.5000 | 0.0260 |
| 323.20 | 0.6000 | 0.0253 |
| 323.20 | 0.7000 | 0.0245 |
| 323.20 | 0.8000 | 0.0236 |
| 323.20 | 0.9000 | 0.0225 |
| 323.20 | 1.0000 | 0.0213 |
| 333.20 | 0.0000 | 0.0605 |
| 333.20 | 0.1000 | 0.0405 |
| 333.20 | 0.2000 | 0.0322 |
| 333.20 | 0.3000 | 0.0285 |
| 333.20 | 0.4000 | 0.0266 |
| 333.20 | 0.5000 | 0.0256 |
| 333.20 | 0.6000 | 0.0250 |
| 333.20 | 0.7000 | 0.0240 |
| 333.20 | 0.8000 | 0.0230 |
| 333.20 | 0.9000 | 0.0216 |
| 333.20 | 1.0000 | 0.0206 |
Surface tension liquid-gas, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
| 293.20 | 0.0000 | 0.0631 |
| 293.20 | 0.1000 | 0.0418 |
| 293.20 | 0.2000 | 0.0334 |
| 293.20 | 0.3000 | 0.0301 |
| 293.20 | 0.4000 | 0.0283 |
| 293.20 | 0.5000 | 0.0273 |
| 293.20 | 0.6000 | 0.0265 |
| 293.20 | 0.7000 | 0.0260 |
| 293.20 | 0.8000 | 0.0253 |
| 293.20 | 0.9000 | 0.0247 |
| 293.20 | 1.0000 | 0.0237 |
| 303.20 | 0.0000 | 0.0624 |
| 303.20 | 0.1000 | 0.0415 |
| 303.20 | 0.2000 | 0.0331 |
| 303.20 | 0.3000 | 0.0297 |
| 303.20 | 0.4000 | 0.0279 |
| 303.20 | 0.5000 | 0.0269 |
| 303.20 | 0.6000 | 0.0261 |
| 303.20 | 0.7000 | 0.0255 |
| 303.20 | 0.8000 | 0.0248 |
| 303.20 | 0.9000 | 0.0241 |
| 303.20 | 1.0000 | 0.0229 |
| 313.20 | 0.0000 | 0.0620 |
| 313.20 | 0.1000 | 0.0412 |
| 313.20 | 0.2000 | 0.0328 |
| 313.20 | 0.3000 | 0.0293 |
| 313.20 | 0.4000 | 0.0277 |
| 313.20 | 0.5000 | 0.0264 |
| 313.20 | 0.6000 | 0.0257 |
| 313.20 | 0.7000 | 0.0250 |
| 313.20 | 0.8000 | 0.0242 |
| 313.20 | 0.9000 | 0.0233 |
| 313.20 | 1.0000 | 0.0221 |
| 323.20 | 0.0000 | 0.0611 |
| 323.20 | 0.1000 | 0.0409 |
| 323.20 | 0.2000 | 0.0325 |
| 323.20 | 0.3000 | 0.0289 |
| 323.20 | 0.4000 | 0.0272 |
| 323.20 | 0.5000 | 0.0260 |
| 323.20 | 0.6000 | 0.0253 |
| 323.20 | 0.7000 | 0.0245 |
| 323.20 | 0.8000 | 0.0236 |
| 323.20 | 0.9000 | 0.0225 |
| 323.20 | 1.0000 | 0.0213 |
| 333.20 | 0.0000 | 0.0605 |
| 333.20 | 0.1000 | 0.0405 |
| 333.20 | 0.2000 | 0.0322 |
| 333.20 | 0.3000 | 0.0285 |
| 333.20 | 0.4000 | 0.0266 |
| 333.20 | 0.5000 | 0.0256 |
| 333.20 | 0.6000 | 0.0250 |
| 333.20 | 0.7000 | 0.0240 |
| 333.20 | 0.8000 | 0.0230 |
| 333.20 | 0.9000 | 0.0216 |
| 333.20 | 1.0000 | 0.0206 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Propanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0418 | 481.69 |
| 0.0474 | 467.41 |
| 0.0559 | 452.42 |
| 0.0629 | 435.93 |
| 0.0698 | 425.04 |
| 0.0920 | 415.69 |
| 0.1111 | 407.05 |
| 0.1380 | 402.35 |
| 0.1646 | 398.25 |
| 0.1881 | 395.05 |
| 0.2088 | 392.21 |
| 0.2418 | 390.31 |
| 0.2606 | 388.51 |
| 0.2730 | 387.26 |
| 0.3001 | 386.16 |
| 0.3207 | 385.36 |
| 0.3339 | 384.71 |
| 0.3518 | 383.96 |
| 0.3753 | 383.41 |
| 0.3928 | 383.01 |
| 0.4044 | 382.56 |
| 0.4273 | 382.26 |
| 0.4410 | 381.96 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Propanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0418 | 481.69 |
| 0.0474 | 467.41 |
| 0.0559 | 452.42 |
| 0.0629 | 435.93 |
| 0.0698 | 425.04 |
| 0.0920 | 415.69 |
| 0.1111 | 407.05 |
| 0.1380 | 402.35 |
| 0.1646 | 398.25 |
| 0.1881 | 395.05 |
| 0.2088 | 392.21 |
| 0.2418 | 390.31 |
| 0.2606 | 388.51 |
| 0.2730 | 387.26 |
| 0.3001 | 386.16 |
| 0.3207 | 385.36 |
| 0.3339 | 384.71 |
| 0.3518 | 383.96 |
| 0.3753 | 383.41 |
| 0.3928 | 383.01 |
| 0.4044 | 382.56 |
| 0.4273 | 382.26 |
| 0.4410 | 381.96 |
Sources
- Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
- Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
- Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures