- 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)
- propan-1,3-diol
- trimethylene glycol
- «beta»-Propylene glycol
- «omega»-Propanediol
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- 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).
- εr : Dielectric Constant (Relative permittivity).
- 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).
- 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 Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- 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 |
|---|---|---|---|
| ω | 0.6309 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| 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 |
| Tig | 673.15 | K | NCMS SOLV-DB |
| 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 |
| εr | 35.00 | NCMS SOLV-DB | |
| 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° | [65.20; 73.00] | kJ/mol |
|
| ΔvapH° | 66.50 | kJ/mol | NIST |
| ΔvapH° | 70.50 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 69.10 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 70.60 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 72.40 | kJ/mol | NIST |
| ΔvapH° | 72.40 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 72.40 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 70.10 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 73.00 | kJ/mol | NIST |
| ΔvapH° | 71.40 | kJ/mol | NIST |
| ΔvapH° | Outlier 65.20 | kJ/mol | NIST |
| IE | 10.15 | eV | Relay (1.0) Calculated Property |
| log10WS | 0.52 | Relay (1.0) Calculated Property | |
| logPoct/wat | -1.693 | NCMS SOLV-DB | |
| McVol | 64.870 | ml/mol | McGowan Calculated Property |
| NFPA Health | 1 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | [6300.00; 8950.00] | kPa |
|
| Pc | 6300.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 6550.00 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| 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 | |
| Ip | [1747.00; 1820.00] |
|
|
| Ip | 1820.00 | NIST | |
| Ip | 1790.00 | NIST | |
| Ip | 1789.00 | NIST | |
| Ip | 1770.00 | NIST | |
| Ip | 1799.00 | NIST | |
| Ip | 1747.00 | NIST | |
| Ip | 1789.00 | NIST | |
| Ip | 1820.00 | NIST | |
| Ip | 1747.00 | NIST | |
| Tboil | [459.00; 489.65] | K |
|
| Tboil | 487.43 | K | 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) |
| Tboil | 487.60 | K | KDB |
| Tboil | 487.55 | K | NCMS SOLV-DB |
| Tboil | 487.00 | K | NIST |
| Tboil | 486.70 | K | NIST |
| Tboil | 488.05 ± 0.05 | K | NIST |
| Tboil | Outlier 459.00 ± 2.00 | K | NIST |
| Tboil | 486.65 ± 1.00 | K | NIST |
| Tboil | 488.15 ± 2.00 | K | NIST |
| Tboil | 486.65 ± 1.00 | K | NIST |
| Tboil | 487.85 ± 0.70 | K | NIST |
| Tboil | 483.65 ± 3.00 | K | NIST |
| Tboil | 487.00 ± 3.00 | K | NIST |
| Tboil | 489.65 ± 3.00 | K | NIST |
| Tboil | 489.15 ± 3.00 | K | NIST |
| Tc | [718.20; 724.00] | K |
|
| Tc | 721.00 | K | Critical temperatures and pressures of straight-chain alkanediols (C3 to C12) |
| Tc | 721.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tc | 722.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 718.20 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 724.00 | K | KDB |
| Tfus | [241.15; 332.00] | K |
|
| Tfus | 246.45 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 246.40 | K | KDB |
| Tfus | 246.45 | K | NCMS SOLV-DB |
| Tfus | Outlier 332.00 ± 2.00 | K | NIST |
| Tfus | 246.50 ± 0.60 | K | NIST |
| Tfus | 241.15 ± 0.70 | K | NIST |
| Ttriple | [245.50; 245.50] | K |
|
| Ttriple | 245.50 ± 0.10 | K | NIST |
| Ttriple | 245.50 ± 0.10 | K | NIST |
| Vc | 0.241 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
Temperature Dependent Properties
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 |
|---|---|---|---|---|
| Cp,gas | [94.13; 211.44] | 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 | 1.07430e+01 | |||
| Coefficient B | 3.56800e-01 | |||
| Coefficient C | -2.00200e-04 | |||
| Coefficient D | 4.41000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 94.13 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 113.87 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 131.61 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 147.48 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 161.64 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 174.21 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 185.33 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 195.15 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 203.81 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 211.44 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 4625.02] | kPa | [377.04; 684.00] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 |
| Pvap | [0.13; 100.79] | kPa | [332.60; 487.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.91005e+01 | |||
| Coefficient B | -7.14957e+03 | |||
| Coefficient C | 6.10100e+00 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 332.60 | |||
| Temperature range, max. | 487.40 | |||
| Pvap | 0.13 | kPa | 332.60 | Calculated Property |
| Pvap | 0.37 | kPa | 349.80 | Calculated Property |
| Pvap | 0.94 | kPa | 367.00 | Calculated Property |
| Pvap | 2.19 | kPa | 384.20 | Calculated Property |
| Pvap | 4.74 | kPa | 401.40 | Calculated Property |
| Pvap | 9.64 | kPa | 418.60 | Calculated Property |
| Pvap | 18.57 | kPa | 435.80 | Calculated Property |
| Pvap | 34.04 | kPa | 453.00 | Calculated Property |
| Pvap | 59.73 | kPa | 470.20 | Calculated Property |
| Pvap | 100.79 | kPa | 487.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.05; 0.03] | N/m | [246.15; 487.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 7.20954e-02 | |||
| Coefficient B | -9.03000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 246.15 | |||
| Temperature range, max. | 487.15 | |||
| γ | 0.05 | N/m | 246.15 | Calculated Property |
| γ | 0.05 | N/m | 272.93 | Calculated Property |
| γ | 0.05 | N/m | 299.71 | Calculated Property |
| γ | 0.04 | N/m | 326.48 | Calculated Property |
| γ | 0.04 | N/m | 353.26 | Calculated Property |
| γ | 0.04 | N/m | 380.04 | Calculated Property |
| γ | 0.04 | N/m | 406.82 | Calculated Property |
| γ | 0.03 | N/m | 433.59 | Calculated Property |
| γ | 0.03 | N/m | 460.37 | Calculated Property |
| γ | 0.03 | N/m | 487.15 | 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 + Methyl Alcohol
- 1,3-Propanediol + Ethanol
- n-Hexane + 1,3-Propanediol
- 1,3-Propanediol + Octane
- 1,3-Propanediol + Decane
- Ethane, 1,1'-[methylenebis(oxy)]bis- + 1,3-Propanediol + Ethanol
- Ethane, 1,1'-[methylenebis(oxy)]bis- + 1,3-Propanediol
- 1,3-Propanediol + Formamide, N,N-dimethyl-
- 1,3-Propanediol + Propylamine
- 1,3-Propanediol + 2-Propanamine
- 1,3-Propanediol + Ethanol + Water
- 1,3-Propanediol + Butyl lactate
- 1,3-Propanediol + 2-Propanol
- 1,3-Propanediol + 2-Propanol + Water
- 1,3-Propanediol + 1,2-Ethanediol
- 1,3-Propanediol + Propylene Glycol
- 1,3-Propanediol + 3-BUTOXYPROPYLAMINE + Water
- 1-Propanol + 1,3-Propanediol
- 1,3-Propanediol + LACTIC ACID, ETHYL ESTER
Find more mixtures with 1,3-Propanediol.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- 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
- A volumetric and acoustic study of pseudo-binary mixtures of (water + 1,3-propanediol + 3-butoxypropan-1-amine) from T = (283.15 to 303.15) K
- 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
- 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
- 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
- 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
- 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
- Liquid-Liquid Coexistence Curves of {x 1-Butyl-3-methylimidazolium Tetrafluoroborate + (1 - x) 1,3-Propanediol} and {x 1-Butyl-3-methylimidazolium Tetrafluoroborate + (1 - x) 1,4-Butanediol}
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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