- InChI
- InChI=1S/C3H8O2/c4-2-1-3-5/h4-5H,1-3H2
- InChI Key
- YPFDHNVEDLHUCE-UHFFFAOYSA-N
- Formula
- C3H8O2
- SMILES
- OCCCO
- Molecular Weight1
- 76.09
- CAS
- 504-63-2
- Other Names
-
- 1,3-Dihydroxypropane
- 1,3-Propylene glycol
- 1,3-Propylenediol
- 2-(Hydroxymethyl)ethanol
- 2-DEOXYGLYCEROL
- BETA-PROPYLENE GLYCOL
- NSC 65426
- PG
- Polypropylene glycol 425
- Propane-1,3-diol
- Propanediol-(1,3)
- Trimethylene glycol
- propan-1,3-diol
- «beta»-Propylene glycol
- «omega»-Propanediol
- «beta»-Propylene glycol
- «omega»-Propanediol
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | [837.90; 876.20] | kJ/mol |
|
| PAff | 876.20 | kJ/mol | NIST |
| PAff | 850.40 | kJ/mol | NIST |
| PAff | 837.90 | kJ/mol | NIST |
| PAff | 857.60 ± 0.50 | kJ/mol | NIST |
| BasG | [808.00; 827.30] | kJ/mol |
|
| BasG | 825.90 | kJ/mol | NIST |
| BasG | 820.00 | kJ/mol | NIST |
| BasG | 808.00 | kJ/mol | NIST |
| BasG | 827.30 ± 0.20 | kJ/mol | NIST |
| ΔcH°liquid | [-1859.00; -1843.00] | kJ/mol |
|
| ΔcH°liquid | -1843.00 ± 5.10 | kJ/mol | NIST |
| ΔcH°liquid | -1859.00 ± 2.30 | kJ/mol | NIST |
| μ | 3.70 | debye | KDB |
| ΔfG° | -299.26 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-409.10; -392.00] | kJ/mol |
|
| ΔfH°gas | -409.10 | kJ/mol | KDB |
| ΔfH°gas | -408.40 ± 5.10 | kJ/mol | NIST |
| ΔfH°gas | -392.00 ± 3.00 | kJ/mol | NIST |
| ΔfH°liquid | [-480.80; -465.00] | kJ/mol |
|
| ΔfH°liquid | -480.80 ± 5.10 | kJ/mol | NIST |
| ΔfH°liquid | -465.00 ± 3.00 | kJ/mol | NIST |
| ΔfusH° | 11.70 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 55.63 | kJ/mol | Joback Calculated Property |
| log10WS | 0.39 | Crippen Calculated Property | |
| logPoct/wat | -0.639 | Crippen Calculated Property | |
| McVol | 64.870 | ml/mol | McGowan Calculated Property |
| Pc | 8950.00 | kPa | KDB |
| Inp | [781.00; 820.00] |
|
|
| Inp | 820.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 820.00 | NIST | |
| I | [1747.00; 1820.00] |
|
|
| I | 1820.00 | NIST | |
| I | 1790.00 | NIST | |
| I | 1789.00 | NIST | |
| I | 1770.00 | NIST | |
| I | 1799.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1789.00 | NIST | |
| I | 1820.00 | NIST | |
| I | 1747.00 | NIST | |
| Tboil | [487.43; 487.60] | K |
|
| Tboil | 487.60 | K | KDB |
| Tboil | 487.43 | K | Vapor-l... |
| Tc | [721.00; 724.00] | K |
|
| Tc | 724.00 | K | KDB |
| Tc | 721.00 | K | Critica... |
| Tc | 721.00 | K | Vapor-l... |
| Tfus | [241.15; 332.00] | K |
|
| Tfus | 246.40 | K | KDB |
| Tfus | 332.00 ± 2.00 | K | NIST |
| Tfus | 246.50 ± 0.60 | K | NIST |
| Tfus | 241.15 ± 0.70 | K | NIST |
| Ttriple | 245.50 ± 0.10 | K | NIST |
| Vc | 0.241 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [135.27; 164.16] | J/mol×K | [452.40; 611.56] |
|
| Cp,gas | 135.27 | J/mol×K | 452.40 | Joback Calculated Property |
| Cp,gas | 140.55 | J/mol×K | 478.93 | Joback Calculated Property |
| Cp,gas | 145.64 | J/mol×K | 505.45 | Joback Calculated Property |
| Cp,gas | 150.54 | J/mol×K | 531.98 | Joback Calculated Property |
| Cp,gas | 155.25 | J/mol×K | 558.51 | Joback Calculated Property |
| Cp,gas | 159.79 | J/mol×K | 585.04 | Joback Calculated Property |
| Cp,gas | 164.16 | J/mol×K | 611.56 | Joback Calculated Property |
| Cp,liquid | [173.40; 202.89] | J/mol×K | [293.15; 353.15] |
|
| Cp,liquid | 173.40 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 174.11 | J/mol×K | 294.65 | Heat Ca... |
| Cp,liquid | 174.83 | J/mol×K | 296.15 | Heat Ca... |
| Cp,liquid | 175.54 | J/mol×K | 297.65 | Heat Ca... |
| Cp,liquid | 175.78 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 176.26 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 176.98 | J/mol×K | 300.65 | Heat Ca... |
| Cp,liquid | 177.70 | J/mol×K | 302.15 | Heat Ca... |
| Cp,liquid | 178.42 | J/mol×K | 303.65 | Heat Ca... |
| Cp,liquid | 179.15 | J/mol×K | 305.15 | Heat Ca... |
| Cp,liquid | 179.87 | J/mol×K | 306.65 | Heat Ca... |
| Cp,liquid | 180.59 | J/mol×K | 308.15 | Heat Ca... |
| Cp,liquid | 181.32 | J/mol×K | 309.65 | Heat Ca... |
| Cp,liquid | 182.05 | J/mol×K | 311.15 | Heat Ca... |
| Cp,liquid | 182.78 | J/mol×K | 312.65 | Heat Ca... |
| Cp,liquid | 183.51 | J/mol×K | 314.15 | Heat Ca... |
| Cp,liquid | 184.24 | J/mol×K | 315.65 | Heat Ca... |
| Cp,liquid | 184.97 | J/mol×K | 317.15 | Heat Ca... |
| Cp,liquid | 185.70 | J/mol×K | 318.65 | Heat Ca... |
| Cp,liquid | 186.44 | J/mol×K | 320.15 | Heat Ca... |
| Cp,liquid | 187.17 | J/mol×K | 321.65 | Heat Ca... |
| Cp,liquid | 187.91 | J/mol×K | 323.15 | Heat Ca... |
| Cp,liquid | 188.65 | J/mol×K | 324.65 | Heat Ca... |
| Cp,liquid | 189.38 | J/mol×K | 326.15 | Heat Ca... |
| Cp,liquid | 190.12 | J/mol×K | 327.65 | Heat Ca... |
| Cp,liquid | 190.87 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 191.61 | J/mol×K | 330.65 | Heat Ca... |
| Cp,liquid | 192.35 | J/mol×K | 332.15 | Heat Ca... |
| Cp,liquid | 193.10 | J/mol×K | 333.65 | Heat Ca... |
| Cp,liquid | 193.84 | J/mol×K | 335.15 | Heat Ca... |
| Cp,liquid | 194.59 | J/mol×K | 336.65 | Heat Ca... |
| Cp,liquid | 195.34 | J/mol×K | 338.15 | Heat Ca... |
| Cp,liquid | 196.09 | J/mol×K | 339.65 | Heat Ca... |
| Cp,liquid | 196.84 | J/mol×K | 341.15 | Heat Ca... |
| Cp,liquid | 197.59 | J/mol×K | 342.65 | Heat Ca... |
| Cp,liquid | 198.34 | J/mol×K | 344.15 | Heat Ca... |
| Cp,liquid | 199.10 | J/mol×K | 345.65 | Heat Ca... |
| Cp,liquid | 199.85 | J/mol×K | 347.15 | Heat Ca... |
| Cp,liquid | 200.61 | J/mol×K | 348.65 | Heat Ca... |
| Cp,liquid | 201.37 | J/mol×K | 350.15 | Heat Ca... |
| Cp,liquid | 202.13 | J/mol×K | 351.65 | Heat Ca... |
| Cp,liquid | 202.89 | J/mol×K | 353.15 | Heat Ca... |
| η | [0.0001719; 0.3206001] | Pa×s | [245.21; 452.40] |
|
| η | 0.3206001 | Pa×s | 245.21 | Joback Calculated Property |
| η | 0.0421146 | Pa×s | 279.74 | Joback Calculated Property |
| η | 0.0086422 | Pa×s | 314.27 | Joback Calculated Property |
| η | 0.0024266 | Pa×s | 348.80 | Joback Calculated Property |
| η | 0.0008566 | Pa×s | 383.34 | Joback Calculated Property |
| η | 0.0003591 | Pa×s | 417.87 | Joback Calculated Property |
| η | 0.0001719 | Pa×s | 452.40 | Joback Calculated Property |
| ΔfusH | 11.40 | kJ/mol | 249.00 | NIST |
| ΔvapH | [57.20; 73.00] | kJ/mol | [273.00; 460.50] |
|
| ΔvapH | 57.86 | kJ/mol | 273.00 | NIST |
| ΔvapH | 69.80 | kJ/mol | 298.15 | Vaporiz... |
| ΔvapH | 73.00 ± 2.00 | kJ/mol | 383.00 | NIST |
| ΔvapH | 57.20 | kJ/mol | 390.00 | NIST |
| ΔvapH | 63.30 | kJ/mol | 408.00 | NIST |
| ΔvapH | 60.40 | kJ/mol | 460.50 | NIST |
| Pvap | [1.67e-03; 101.30] | kPa | [292.50; 487.43] |
|
| Pvap | 1.67e-03 | kPa | 292.50 | Benchma... |
| Pvap | 1.86e-03 | kPa | 293.50 | Vapor P... |
| Pvap | 2.39e-03 | kPa | 296.40 | Benchma... |
| Pvap | 3.46e-03 | kPa | 300.40 | Benchma... |
| Pvap | 4.47e-03 | kPa | 303.20 | Vapor P... |
| Pvap | 5.84e-03 | kPa | 306.30 | Benchma... |
| Pvap | 7.88e-03 | kPa | 309.30 | Vapor P... |
| Pvap | 9.97e-03 | kPa | 312.20 | Vapor P... |
| Pvap | 0.01 | kPa | 313.20 | Vapor-L... |
| Pvap | 0.01 | kPa | 315.30 | Vapor P... |
| Pvap | 0.02 | kPa | 318.40 | Vapor P... |
| Pvap | 0.02 | kPa | 321.30 | Vapor P... |
| Pvap | 0.03 | kPa | 323.26 | Vapor-L... |
| Pvap | 0.03 | kPa | 324.30 | Vapor P... |
| Pvap | 0.04 | kPa | 327.30 | Vapor P... |
| Pvap | 0.04 | kPa | 330.30 | Vapor P... |
| Pvap | 0.06 | kPa | 333.23 | Vapor-L... |
| Pvap | 0.06 | kPa | 333.50 | Vapor P... |
| Pvap | 0.07 | kPa | 336.40 | Vapor P... |
| Pvap | 0.08 | kPa | 338.70 | Benchma... |
| Pvap | 0.08 | kPa | 339.40 | Vapor P... |
| Pvap | 0.11 | kPa | 342.30 | Vapor P... |
| Pvap | 0.12 | kPa | 343.16 | Vapor-L... |
| Pvap | 0.12 | kPa | 344.30 | Benchma... |
| Pvap | 0.14 | kPa | 346.40 | Benchma... |
| Pvap | 0.22 | kPa | 351.33 | Vapor-L... |
| Pvap | 0.43 | kPa | 361.61 | Vapor-L... |
| Pvap | 0.46 | kPa | 362.97 | Vapor-L... |
| Pvap | 0.79 | kPa | 371.65 | Vapor-L... |
| Pvap | 1.40 | kPa | 381.70 | Vapor-L... |
| Pvap | 2.38 | kPa | 391.70 | Vapor-L... |
| Pvap | 2.37 | kPa | 391.73 | Vapor-L... |
| Pvap | 3.88 | kPa | 401.64 | Vapor-L... |
| Pvap | 6.21 | kPa | 411.71 | Vapor-L... |
| Pvap | 6.67 | kPa | 414.20 | Excess ... |
| Pvap | 6.65 | kPa | 414.20 | Excess ... |
| Pvap | 9.93 | kPa | 420.80 | Excess ... |
| Pvap | 9.63 | kPa | 421.69 | Vapor-L... |
| Pvap | 13.33 | kPa | 427.55 | Excess ... |
| Pvap | 13.47 | kPa | 427.60 | Excess ... |
| Pvap | 14.62 | kPa | 431.74 | Vapor-L... |
| Pvap | 16.75 | kPa | 433.90 | Excess ... |
| Pvap | 19.99 | kPa | 438.05 | Excess ... |
| Pvap | 21.63 | kPa | 441.73 | Vapor-L... |
| Pvap | 23.46 | kPa | 441.95 | Excess ... |
| Pvap | 26.66 | kPa | 445.30 | Excess ... |
| Pvap | 30.22 | kPa | 448.65 | Excess ... |
| Pvap | 33.22 | kPa | 451.65 | Excess ... |
| Pvap | 31.44 | kPa | 451.78 | Vapor-L... |
| Pvap | 33.33 | kPa | 453.15 | Excess ... |
| Pvap | 36.69 | kPa | 454.65 | Excess ... |
| Pvap | 39.99 | kPa | 457.45 | Excess ... |
| Pvap | 40.04 | kPa | 457.49 | Excess ... |
| Pvap | 43.37 | kPa | 459.85 | Excess ... |
| Pvap | 44.81 | kPa | 461.85 | Vapor-L... |
| Pvap | 46.67 | kPa | 461.95 | Excess ... |
| Pvap | 46.66 | kPa | 461.95 | Excess ... |
| Pvap | 49.97 | kPa | 463.95 | Excess ... |
| Pvap | 53.24 | kPa | 465.45 | Excess ... |
| Pvap | 101.30 | kPa | 487.43 | Vapor-l... |
| n0 | [1.43099; 1.44089] | [288.15; 323.15] |
|
|
| n0 | 1.44089 | 288.15 | Experim... | |
| n0 | 1.43947 | 293.15 | Experim... | |
| n0 | 1.43930 | 293.15 | Vapor-l... | |
| n0 | 1.43860 | 298.15 | Densiti... | |
| n0 | 1.43800 | 298.15 | Study o... | |
| n0 | 1.43805 | 298.15 | Experim... | |
| n0 | 1.43665 | 303.15 | Experim... | |
| n0 | 1.43526 | 308.15 | Experim... | |
| n0 | 1.43387 | 313.15 | Experim... | |
| n0 | 1.43244 | 318.15 | Experim... | |
| n0 | 1.43099 | 323.15 | Experim... | |
| ρl | [1015.30; 1078.20] | kg/m3 | [253.15; 353.15] |
|
| ρl | 1078.20 | kg/m3 | 253.15 | Viscosi... |
| ρl | 1075.40 | kg/m3 | 258.15 | Viscosi... |
| ρl | 1072.30 | kg/m3 | 263.15 | Viscosi... |
| ρl | 1069.00 | kg/m3 | 268.15 | Viscosi... |
| ρl | 1065.90 | kg/m3 | 273.15 | Viscosi... |
| ρl | 1059.14 | kg/m3 | 283.15 | Excess ... |
| ρl | 1059.80 | kg/m3 | 283.15 | Viscosi... |
| ρl | 1055.89 | kg/m3 | 288.15 | Volumet... |
| ρl | 1055.96 | kg/m3 | 288.15 | Experim... |
| ρl | 1055.96 | kg/m3 | 288.15 | Densiti... |
| ρl | 1053.00 | kg/m3 | 293.00 | KDB |
| ρl | 1053.03 | kg/m3 | 293.15 | Thermod... |
| ρl | 1053.60 | kg/m3 | 293.15 | Viscosi... |
| ρl | 1053.00 | kg/m3 | 293.15 | Thermod... |
| ρl | 1052.85 | kg/m3 | 293.15 | Excess ... |
| ρl | 1052.87 | kg/m3 | 293.15 | Densiti... |
| ρl | 1052.80 | kg/m3 | 293.15 | Volumet... |
| ρl | 1052.86 | kg/m3 | 293.15 | Experim... |
| ρl | 1053.66 | kg/m3 | 293.15 | Densiti... |
| ρl | 1049.60 | kg/m3 | 298.15 | Investi... |
| ρl | 1049.90 | kg/m3 | 298.15 | Densiti... |
| ρl | 1049.90 | kg/m3 | 298.15 | Excess ... |
| ρl | 1049.00 | kg/m3 | 298.15 | Thermod... |
| ρl | 1049.68 | kg/m3 | 298.15 | Excess ... |
| ρl | 1049.61 | kg/m3 | 298.15 | Measure... |
| ρl | 1049.76 | kg/m3 | 298.15 | Densiti... |
| ρl | 1049.68 | kg/m3 | 298.15 | Isobari... |
| ρl | 1049.90 | kg/m3 | 298.15 | Thermod... |
| ρl | 1049.75 | kg/m3 | 298.15 | Experim... |
| ρl | 1050.29 | kg/m3 | 298.15 | Densiti... |
| ρl | 1049.60 | kg/m3 | 298.15 | Thermod... |
| ρl | 1049.68 | kg/m3 | 298.15 | Isobari... |
| ρl | 1049.69 | kg/m3 | 298.15 | Volumet... |
| ρl | 1046.63 | kg/m3 | 303.15 | Experim... |
| ρl | 1046.20 | kg/m3 | 303.15 | Investi... |
| ρl | 1047.00 | kg/m3 | 303.15 | Densiti... |
| ρl | 1046.57 | kg/m3 | 303.15 | Volumet... |
| ρl | 1047.09 | kg/m3 | 303.15 | Densiti... |
| ρl | 1046.20 | kg/m3 | 303.15 | Thermod... |
| ρl | 1046.77 | kg/m3 | 303.15 | Thermod... |
| ρl | 1046.00 | kg/m3 | 303.15 | Thermod... |
| ρl | 1046.64 | kg/m3 | 303.15 | Densiti... |
| ρl | 1046.48 | kg/m3 | 303.15 | Measure... |
| ρl | 1046.51 | kg/m3 | 303.15 | Excess ... |
| ρl | 1046.56 | kg/m3 | 303.15 | Densiti... |
| ρl | 1047.40 | kg/m3 | 303.15 | Viscosi... |
| ρl | 1043.43 | kg/m3 | 308.15 | Densiti... |
| ρl | 1043.50 | kg/m3 | 308.15 | Experim... |
| ρl | 1043.10 | kg/m3 | 308.15 | Investi... |
| ρl | 1043.92 | kg/m3 | 308.15 | Densiti... |
| ρl | 1042.70 | kg/m3 | 308.15 | Molecul... |
| ρl | 1043.63 | kg/m3 | 308.15 | Thermod... |
| ρl | 1043.34 | kg/m3 | 308.15 | Measure... |
| ρl | 1043.50 | kg/m3 | 308.15 | Densiti... |
| ρl | 1043.10 | kg/m3 | 308.15 | Thermod... |
| ρl | 1042.70 | kg/m3 | 308.15 | Structu... |
| ρl | 1044.10 | kg/m3 | 308.15 | Densiti... |
| ρl | 1043.43 | kg/m3 | 308.15 | Volumet... |
| ρl | 1040.49 | kg/m3 | 313.15 | Thermod... |
| ρl | 1040.19 | kg/m3 | 313.15 | Measure... |
| ρl | 1040.80 | kg/m3 | 313.15 | Densiti... |
| ρl | 1040.35 | kg/m3 | 313.15 | Experim... |
| ρl | 1041.10 | kg/m3 | 313.15 | Viscosi... |
| ρl | 1040.61 | kg/m3 | 313.15 | Densiti... |
| ρl | 1040.12 | kg/m3 | 313.15 | Excess ... |
| ρl | 1040.28 | kg/m3 | 313.15 | Volumet... |
| ρl | 1040.28 | kg/m3 | 313.15 | Densiti... |
| ρl | 1040.35 | kg/m3 | 313.15 | Densiti... |
| ρl | 1037.33 | kg/m3 | 318.15 | Thermod... |
| ρl | 1037.11 | kg/m3 | 318.15 | Volumet... |
| ρl | 1037.80 | kg/m3 | 318.15 | Densiti... |
| ρl | 1037.11 | kg/m3 | 318.15 | Densiti... |
| ρl | 1037.60 | kg/m3 | 318.15 | Densiti... |
| ρl | 1037.02 | kg/m3 | 318.15 | Measure... |
| ρl | 1037.17 | kg/m3 | 318.15 | Experim... |
| ρl | 1037.18 | kg/m3 | 318.15 | Densiti... |
| ρl | 1034.16 | kg/m3 | 323.15 | Thermod... |
| ρl | 1033.84 | kg/m3 | 323.15 | Measure... |
| ρl | 1033.98 | kg/m3 | 323.15 | Densiti... |
| ρl | 1034.51 | kg/m3 | 323.15 | Densiti... |
| ρl | 1033.92 | kg/m3 | 323.15 | Densiti... |
| ρl | 1033.98 | kg/m3 | 323.15 | Experim... |
| ρl | 1034.80 | kg/m3 | 323.15 | Densiti... |
| ρl | 1033.91 | kg/m3 | 323.15 | Volumet... |
| ρl | 1034.80 | kg/m3 | 323.15 | Viscosi... |
| ρl | 1031.40 | kg/m3 | 328.15 | Densiti... |
| ρl | 1030.77 | kg/m3 | 328.15 | Densiti... |
| ρl | 1031.00 | kg/m3 | 328.15 | Densiti... |
| ρl | 1027.53 | kg/m3 | 333.15 | Densiti... |
| ρl | 1028.40 | kg/m3 | 333.15 | Viscosi... |
| ρl | 1028.20 | kg/m3 | 333.15 | Densiti... |
| ρl | 1021.90 | kg/m3 | 343.15 | Viscosi... |
| ρl | 1015.30 | kg/m3 | 353.15 | Viscosi... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 383.20 | K | 1.60 | NIST |
Datasets
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 |
| 293.15 | 100.00 | 1635.213 |
| 293.15 | 5030.00 | 1649.982 |
| 293.15 | 10062.00 | 1664.642 |
| 293.15 | 15066.00 | 1678.921 |
| 293.15 | 20096.00 | 1692.938 |
| 293.15 | 24997.00 | 1706.35 |
| 293.15 | 30029.00 | 1719.901 |
| 313.15 | 99.00 | 1589.462 |
| 313.15 | 5048.00 | 1605.093 |
| 313.15 | 10031.00 | 1620.261 |
| 313.15 | 15138.00 | 1635.434 |
| 313.15 | 20064.00 | 1649.763 |
| 313.15 | 25191.00 | 1664.415 |
| 313.15 | 30167.00 | 1678.273 |
| 333.15 | 100.00 | 1544.067 |
| 333.15 | 5058.00 | 1560.325 |
| 333.15 | 10054.00 | 1576.249 |
| 333.15 | 15024.00 | 1591.679 |
| 333.15 | 20153.00 | 1607.231 |
| 333.15 | 25135.00 | 1622.05 |
| 333.15 | 30136.00 | 1636.643 |
| 353.15 | 101.00 | 1497.623 |
| 353.15 | 5038.00 | 1514.638 |
| 353.15 | 10023.00 | 1531.32 |
| 353.15 | 15089.00 | 1547.839 |
| 353.15 | 20158.00 | 1563.937 |
| 353.15 | 25109.00 | 1579.311 |
| 353.15 | 30076.00 | 1594.386 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 4625.02] | kPa | [377.04; 684.00] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.64154e+01 | |||
| Coefficient B | -4.84399e+03 | |||
| Coefficient C | -7.66890e+01 | |||
| Temperature range, min. | 377.04 | |||
| Temperature range, max. | 684.00 | |||
| Pvap | 1.33 | kPa | 377.04 | Calculated Property |
| Pvap | 6.90 | kPa | 411.15 | Calculated Property |
| Pvap | 26.38 | kPa | 445.25 | Calculated Property |
| Pvap | 80.30 | kPa | 479.36 | Calculated Property |
| Pvap | 205.42 | kPa | 513.47 | Calculated Property |
| Pvap | 458.68 | kPa | 547.57 | Calculated Property |
| Pvap | 918.86 | kPa | 581.68 | Calculated Property |
| Pvap | 1685.80 | kPa | 615.79 | Calculated Property |
| Pvap | 2877.40 | kPa | 649.89 | Calculated Property |
| Pvap | 4625.02 | kPa | 684.00 | Calculated Property |
Similar Compounds
![3-[3-(3-Methoxypropoxy)propoxy]-1-propanol.](data:image/png;base64,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)
Find more compounds similar to 1,3-Propanediol.
Mixtures
- 1,3-Propanediol + Water
- 1,3-Propanediol + Isopropyl Alcohol
- 1,3-Propanediol + Isopropyl Alcohol + Water
- 1,3-Propanediol + Propanoic acid, 2-hydroxy-, ethyl ester
- 1-Propanol + 1,3-Propanediol
- 1,3-Propanediol + Formamide, N,N-dimethyl-
- 2-Pyrrolidinone + 1,3-Propanediol
- 1,3-Propanediol + Pyridine
- 1,3-Propanediol + Ethanol
- 1,3-Propanediol + Ethanol + Water
- 1,3-Propanediol + Propylene Glycol
- 1,3-Propanediol + Pyridine, 3-(1-methyl-2-pyrrolidinyl)-, (S)-
- 1,3-Propanediol + Acetonitrile
- 1,3-Propanediol + 1-Hexanol
- 1,3-Propanediol + Propylamine
- 1,3-Propanediol + 2-Propanamine
- 1,3-Propanediol + 1,2-Ethanediol
- 1,3-Propanediol + Butyl lactate
- 1,3-Propanediol + Methyl Alcohol
- 1,3-Propanediol + Glycerin
Find more mixtures with 1,3-Propanediol.
Sources
- Crippen Method
- Crippen Method
- Solubility of Baicalein in Different Solvents from (287 to 323) K
- Liquid phase behavior of hexafluorophosphate ionic liquids with polyhydric alcohols
- Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
- Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
- Critical temperatures and pressures of straight-chain alkanediols (C3 to C12)
- Isobaric vapor-liquid equilibria for the binary and ternary mixtures of 2-propanol, water, and 1,3-propanediol at p = 101.3 kPa: Effect of the 1,3-propanediol addition
- 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
- Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
- Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
- Densities, viscosities and refractive indices of binary mixtures containing methyl ethyl ketone. Friction theory. New UNIFAC-VISCO and ASOG-VISCO parameter determination
- 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
- Structural and interactional studies of homologous series of a,x-alkanediols in N,N-dimethylformamide
- Molecular interactions of a,x-alkanediols in pyrrolidin-2-one: Thermophysical and spectroscopic measurements
- 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
- 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
- Investigation on some thermophysical properties of poly(ethylene glycol) binary mixtures at different temperatures
- Isobaric (vapor + liquid) equilibria for the ternary system of (ethanol + water + 1,3-propanediol) and three constituent binary systems at P = 101.3 kPa
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Benchmark thermodynamic properties of 1,3-propanediol: Comprehensive experimental and theoretical study
- Liquid extraction of polyhydric alcohols from water using [A336][SCN] as a solvent
- Excess properties and isobaric (vapor + liquid) equilibrium at sub-atmospheric pressures of binary (1,2-propanediol + 1,3-propanediol) system: Measurement and modelling
- 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
- Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of ethanol from diethoxymethane solution with different solvents
- 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
- Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
- Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
- 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.
- Vapor-liquid equilibria, density and sound velocity measurements of (water or methanol or ethanol + 1,3-propanediol) binary systems at different temperatures
- Viscosities, Densities, and Refractive Indices of Aqueous Propane-1,3-diol
- Liquid-Liquid Equilibrium Measurements and Correlation for Ternary Systems (Butyl Acetate + 1-Butanol + Ethylene Glycol/1,3-Propanediol/Ethanolamine) at 298.15 K
- Liquid-Liquid Equilibria in Binary Mixtures of Dihydroxy Alcohols and Imidazolium-Based Ionic Liquids
- 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
- Vaporization Enthalpies of the r,o-Alkanediols by Correlation Gas Chromatography
- Vapor Pressures and Enthalpies of Vaporization of a Series of the 1,3-Alkanediols
- Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
- Enthalpies of Dilution of 1,3-Propanediol and Isomers of 2,3-Butanediol in Dimethylsulfoxide + Water Mixtures at 298.15 K
- Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
- Liquid-Liquid Equilibria in Binary Mixtures of 1,3-Propanediol + Ionic Liquids [bmim][PF6], [bmim][BF4], and [emim][BF4]
- 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
- Heat Capacities of Some Liquid alpha,omega-Alkanediols within the Temperature Range between (293.15 and 353.15) K
- 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.