- 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
- Molecular Weight1
- 92.09
- CAS
- 56-81-5
- Other Names
-
- 1,2,3-Propanetriol
- 1,2,3-Trihydroxypropane
- 90 Technical glycerin
- 90 Technical glycerine
- Bulbold
- Clyzerin, wasserfrei
- Cristal
- Dagralax
- Emery 912
- Emery 916
- Glycerin, anhydrous
- Glycerin, synthetic
- Glycerine
- Glyceritol
- Glycerol
- Glycyl alcohol
- Glyrol
- Glysanin
- Grocolene
- IFP
- Incorporation factor
- MOON
- NSC 9230
- Ophthalgan
- Optim
- Osmoglyn
- Pricerine 9091
- Propane-1,2,3-triol
- Propanetriol
- Star
- Synthetic glycerin
- Synthetic glycerine
- Trihydroxypropane
- Vitrosupos
- 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).
- Cp,solid : Solid 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).
- 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).
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | [835.80; 874.80] | kJ/mol |
|
| PAff | 874.80 | kJ/mol | NIST |
| PAff | 840.70 | kJ/mol | NIST |
| PAff | 835.80 | kJ/mol | NIST |
| PAff | 848.60 ± 1.20 | kJ/mol | NIST |
| BasG | [805.50; 820.00] | kJ/mol |
|
| BasG | 820.00 | kJ/mol | NIST |
| BasG | 810.20 | kJ/mol | NIST |
| BasG | 805.50 | kJ/mol | NIST |
| BasG | 818.90 ± 0.50 | kJ/mol | NIST |
| ΔcH°liquid | [-1665.10; -1654.10] | kJ/mol |
|
| ΔcH°liquid | -1654.30 ± 0.40 | kJ/mol | NIST |
| ΔcH°liquid | -1654.10 | kJ/mol | NIST |
| ΔcH°liquid | -1655.30 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -1665.10 | kJ/mol | NIST |
| μ | 3.00 | debye | KDB |
| ΔfG° | -438.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-585.30; -576.90] | kJ/mol |
|
| ΔfH°gas | -585.30 | kJ/mol | KDB |
| ΔfH°gas | -577.90 ± 1.10 | kJ/mol | NIST |
| ΔfH°gas | -576.90 | kJ/mol | NIST |
| ΔfH°liquid | [-669.60; -668.60] | kJ/mol |
|
| ΔfH°liquid | -669.60 ± 0.60 | kJ/mol | NIST |
| ΔfH°liquid | -668.60 ± 0.42 | kJ/mol | NIST |
| ΔfusH° | 12.27 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [85.80; 91.70] | kJ/mol |
|
| ΔvapH° | 91.70 ± 0.90 | kJ/mol | NIST |
| ΔvapH° | 91.70 | kJ/mol | NIST |
| ΔvapH° | 91.70 ± 0.90 | kJ/mol | NIST |
| ΔvapH° | 85.80 | kJ/mol | NIST |
| log10WS | [1.12; 1.12] |
|
|
| log10WS | 1.12 | Aq. Sol... | |
| log10WS | 1.12 | Estimat... | |
| logPoct/wat | -1.668 | Crippen Calculated Property | |
| McVol | 70.740 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [6680.00; 7500.00] | kPa |
|
| Pc | 6680.00 | kPa | KDB |
| Pc | 7500.00 ± 200.00 | kPa | NIST |
| I | [2300.00; 2322.00] |
|
|
| I | 2322.00 | NIST | |
| I | 2314.00 | NIST | |
| I | 2300.00 | NIST | |
| S°solid,1 bar | [37.87; 42.34] | J/mol×K |
|
| S°solid,1 bar | 37.87 | J/mol×K | NIST |
| S°solid,1 bar | 42.34 | J/mol×K | NIST |
| Tboil | [512.25; 563.70] | K |
|
| Tboil | 563.00 | K | KDB |
| Tboil | 563.25 | K | NIST |
| Tboil | 563.15 ± 3.00 | K | NIST |
| Tboil | 563.70 ± 0.70 | K | NIST |
| Tboil | Outlier 512.25 ± 0.40 | K | NIST |
| Tboil | 562.00 ± 3.00 | K | NIST |
| Tboil | 563.15 ± 0.40 | K | NIST |
| Tboil | 563.00 ± 4.00 | K | NIST |
| Tc | [726.00; 850.00] | K |
|
| Tc | 726.00 | K | KDB |
| Tc | 850.00 ± 4.00 | K | NIST |
| Tfus | [286.00; 292.00] | K |
|
| Tfus | 291.00 | K | KDB |
| Tfus | 291.05 | K | NIST |
| Tfus | 291.05 ± 0.50 | K | NIST |
| Tfus | 291.05 ± 0.50 | K | NIST |
| Tfus | 292.00 ± 2.00 | K | NIST |
| Tfus | 291.33 ± 0.15 | K | NIST |
| Tfus | 291.80 ± 1.00 | K | NIST |
| Tfus | 291.20 ± 0.50 | K | NIST |
| Tfus | 292.00 ± 3.00 | K | NIST |
| Tfus | Outlier 286.00 ± 3.00 | K | NIST |
| Tfus | Outlier 286.00 ± 4.00 | K | NIST |
| Ttriple | [291.00; 291.80] | K |
|
| Ttriple | 291.80 ± 0.20 | K | NIST |
| Ttriple | 291.00 ± 0.20 | K | NIST |
| Vc | 0.255 | m3/kmol | KDB |
| Zc | 0.2821910 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [169.59; 196.19] | J/mol×K | [544.14; 702.69] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 170 175 180 185 190 195 550 600 650 700 | ||||
| Cp,gas | 169.59 | J/mol×K | 544.14 | Joback Calculated Property |
| Cp,gas | 174.50 | J/mol×K | 570.56 | Joback Calculated Property |
| Cp,gas | 179.21 | J/mol×K | 596.99 | Joback Calculated Property |
| Cp,gas | 183.73 | J/mol×K | 623.41 | Joback Calculated Property |
| Cp,gas | 188.07 | J/mol×K | 649.84 | Joback Calculated Property |
| Cp,gas | 192.22 | J/mol×K | 676.26 | Joback Calculated Property |
| Cp,gas | 196.19 | J/mol×K | 702.69 | Joback Calculated Property |
| Cp,liquid | [207.90; 229.30] | J/mol×K | [289.70; 313.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 210 215 220 225 230 290 300 310 | ||||
| Cp,liquid | 225.90 | J/mol×K | 289.70 | NIST |
| Cp,liquid | 219.20 | J/mol×K | 293.15 | NIST |
| Cp,liquid | 221.18 | J/mol×K | 293.15 | NIST |
| Cp,liquid | 218.50 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 213.80 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 207.90 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 221.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 218.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 223.40 | J/mol×K | 299.40 | NIST |
| Cp,liquid | 221.70 | J/mol×K | 301.20 | NIST |
| Cp,liquid | 229.30 | J/mol×K | 313.15 | NIST |
| Cp,solid | [49.79; 150.00] | J/mol×K | [85.12; 281.50] |
|
| Cp,solid | 50.21 | J/mol×K | 85.12 | NIST |
| Cp,solid | 49.79 | J/mol×K | 86.92 | NIST |
| Cp,solid | 150.00 | J/mol×K | 281.50 | NIST |
| η | [0.0083200; 2.1800000] | Pa×s | [288.10; 394.08] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.5 1 1.5 2 300 350 | ||||
| η | 2.1800000 | Pa×s | 288.10 | Studies... |
| η | 1.4700000 | Pa×s | 292.89 | The vis... |
| η | 1.2520000 | Pa×s | 296.50 | Viscosi... |
| η | 0.9338000 | Pa×s | 298.10 | Studies... |
| η | 0.9706000 | Pa×s | 298.10 | The vis... |
| η | 0.9438000 | Pa×s | 298.15 | Densiti... |
| η | 0.6458000 | Pa×s | 302.59 | The vis... |
| η | 0.6734000 | Pa×s | 302.80 | Viscosi... |
| η | 0.6289000 | Pa×s | 303.15 | Densiti... |
| η | 0.4203000 | Pa×s | 308.10 | Studies... |
| η | 0.4319000 | Pa×s | 308.15 | Densiti... |
| η | 0.3053000 | Pa×s | 312.81 | The vis... |
| η | 0.2959000 | Pa×s | 313.15 | Densiti... |
| η | 0.2606000 | Pa×s | 315.80 | Viscosi... |
| η | 0.1956000 | Pa×s | 318.10 | Studies... |
| η | 0.1858000 | Pa×s | 318.15 | Densiti... |
| η | 0.1512000 | Pa×s | 323.15 | Densiti... |
| η | 0.1489000 | Pa×s | 323.20 | Viscosi... |
| η | 0.1474000 | Pa×s | 323.88 | The vis... |
| η | 0.1043000 | Pa×s | 328.10 | Studies... |
| η | 0.1084000 | Pa×s | 328.15 | Densiti... |
| η | 0.0975000 | Pa×s | 332.70 | Viscosi... |
| η | 0.0848000 | Pa×s | 333.15 | Densiti... |
| η | 0.0847100 | Pa×s | 333.15 | The vis... |
| η | 0.0622000 | Pa×s | 338.15 | Densiti... |
| η | 0.0519000 | Pa×s | 343.20 | Viscosi... |
| η | 0.0498300 | Pa×s | 343.80 | The vis... |
| η | 0.0428000 | Pa×s | 348.20 | Viscosi... |
| η | 0.0318000 | Pa×s | 353.67 | The vis... |
| η | 0.0349000 | Pa×s | 354.20 | Viscosi... |
| η | 0.0210500 | Pa×s | 364.12 | The vis... |
| η | 0.0147400 | Pa×s | 374.38 | The vis... |
| η | 0.0110000 | Pa×s | 383.29 | The vis... |
| η | 0.0083200 | Pa×s | 394.08 | The vis... |
| ΔfusH | [18.28; 18.48] | kJ/mol | [291.00; 293.00] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 18.3 18.35 18.4 18.45 291 292 293 | ||||
| ΔfusH | 18.29 | kJ/mol | 291.00 | NIST |
| ΔfusH | 18.28 | kJ/mol | 291.00 | NIST |
| ΔfusH | 18.48 | kJ/mol | 291.75 | NIST |
| ΔfusH | 18.30 | kJ/mol | 292.00 | NIST |
| ΔfusH | 18.28 | kJ/mol | 293.00 | NIST |
| ΔfusH | 18.28 | kJ/mol | 293.00 | NIST |
| ΔvapH | [64.80; 86.80] | kJ/mol | [300.50; 516.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 65 70 75 80 85 300 400 500 | ||||
| ΔvapH | 71.50 | kJ/mol | 300.50 | NIST |
| ΔvapH | 86.80 | kJ/mol | 316.00 | NIST |
| ΔvapH | 85.80 | kJ/mol | 318.00 | NIST |
| ΔvapH | 67.50 | kJ/mol | 343.00 | NIST |
| ΔvapH | 66.80 | kJ/mol | 353.00 | NIST |
| ΔvapH | 66.20 | kJ/mol | 363.00 | NIST |
| ΔvapH | 65.50 | kJ/mol | 373.00 | NIST |
| ΔvapH | 64.80 | kJ/mol | 383.00 | NIST |
| ΔvapH | 86.00 | kJ/mol | 504.50 | NIST |
| ΔvapH | 78.50 | kJ/mol | 516.00 | NIST |
| Pvap | [4.15e-05; 95.99] | kPa | [303.59; 560.95] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 400 500 | ||||
| Pvap | 4.15e-05 | kPa | 303.59 | Thermod... |
| Pvap | 4.19e-05 | kPa | 303.61 | Thermod... |
| Pvap | 4.68e-05 | kPa | 304.56 | Thermod... |
| Pvap | 5.56e-05 | kPa | 306.03 | Thermod... |
| Pvap | 7.28e-05 | kPa | 308.43 | Thermod... |
| Pvap | 9.63e-05 | kPa | 310.89 | Thermod... |
| Pvap | 1.25e-04 | kPa | 313.29 | Thermod... |
| Pvap | 1.63e-04 | kPa | 315.71 | Thermod... |
| Pvap | 2.11e-04 | kPa | 318.12 | Thermod... |
| Pvap | 2.70e-04 | kPa | 320.57 | Thermod... |
| Pvap | 3.47e-04 | kPa | 322.95 | Thermod... |
| Pvap | 4.43e-04 | kPa | 325.42 | Thermod... |
| Pvap | 5.64e-04 | kPa | 327.82 | Thermod... |
| Pvap | 7.17e-04 | kPa | 330.30 | Thermod... |
| Pvap | 9.04e-04 | kPa | 332.72 | Thermod... |
| Pvap | 1.13e-03 | kPa | 335.14 | Thermod... |
| Pvap | 1.50e-03 | kPa | 338.25 | Thermod... |
| Pvap | 1.87e-03 | kPa | 340.68 | Thermod... |
| Pvap | 2.32e-03 | kPa | 343.08 | Thermod... |
| Pvap | 2.88e-03 | kPa | 345.51 | Thermod... |
| Pvap | 3.53e-03 | kPa | 347.91 | Thermod... |
| Pvap | 4.36e-03 | kPa | 350.34 | Thermod... |
| Pvap | 5.83e-03 | kPa | 351.80 | Vapor-L... |
| Pvap | 5.26e-03 | kPa | 352.57 | Thermod... |
| Pvap | 5.27e-03 | kPa | 352.58 | Thermod... |
| Pvap | 5.28e-03 | kPa | 352.60 | Thermod... |
| Pvap | 5.32e-03 | kPa | 352.73 | Thermod... |
| Pvap | 6.39e-03 | kPa | 354.98 | Thermod... |
| Pvap | 6.41e-03 | kPa | 354.99 | Thermod... |
| Pvap | 6.49e-03 | kPa | 355.18 | Thermod... |
| Pvap | 7.77e-03 | kPa | 357.39 | Thermod... |
| Pvap | 7.82e-03 | kPa | 357.42 | Thermod... |
| Pvap | 7.86e-03 | kPa | 357.57 | Thermod... |
| Pvap | 9.38e-03 | kPa | 359.80 | Thermod... |
| Pvap | 9.39e-03 | kPa | 359.82 | Thermod... |
| Pvap | 9.52e-03 | kPa | 360.01 | Thermod... |
| Pvap | 0.01 | kPa | 362.02 | Vapor-L... |
| Pvap | 0.01 | kPa | 362.42 | Thermod... |
| Pvap | 0.01 | kPa | 362.63 | Thermod... |
| Pvap | 0.01 | kPa | 362.66 | Thermod... |
| Pvap | 0.01 | kPa | 364.82 | Thermod... |
| Pvap | 0.01 | kPa | 365.07 | Thermod... |
| Pvap | 0.01 | kPa | 365.08 | Thermod... |
| Pvap | 0.02 | kPa | 367.45 | Thermod... |
| Pvap | 0.02 | kPa | 367.48 | Thermod... |
| Pvap | 0.02 | kPa | 369.89 | Thermod... |
| Pvap | 0.02 | kPa | 369.91 | Thermod... |
| Pvap | 0.03 | kPa | 372.06 | Vapor-L... |
| Pvap | 0.02 | kPa | 372.27 | Thermod... |
| Pvap | 0.02 | kPa | 372.29 | Thermod... |
| Pvap | 0.03 | kPa | 374.70 | Thermod... |
| Pvap | 0.03 | kPa | 374.73 | Thermod... |
| Pvap | 0.03 | kPa | 377.08 | Thermod... |
| Pvap | 0.03 | kPa | 377.11 | Thermod... |
| Pvap | 0.04 | kPa | 377.77 | Thermod... |
| Pvap | 0.04 | kPa | 380.17 | Thermod... |
| Pvap | 0.04 | kPa | 380.19 | Thermod... |
| Pvap | 0.05 | kPa | 382.08 | Vapor-L... |
| Pvap | 0.05 | kPa | 382.55 | Thermod... |
| Pvap | 0.05 | kPa | 382.59 | Thermod... |
| Pvap | 0.05 | kPa | 382.59 | Thermod... |
| Pvap | 0.06 | kPa | 384.99 | Thermod... |
| Pvap | 0.06 | kPa | 385.01 | Thermod... |
| Pvap | 0.07 | kPa | 387.37 | Thermod... |
| Pvap | 0.07 | kPa | 387.39 | Thermod... |
| Pvap | 0.08 | kPa | 389.80 | Thermod... |
| Pvap | 0.08 | kPa | 389.83 | Thermod... |
| Pvap | 0.09 | kPa | 392.18 | Thermod... |
| Pvap | 0.10 | kPa | 392.18 | Vapor-L... |
| Pvap | 0.09 | kPa | 392.20 | Thermod... |
| Pvap | 0.11 | kPa | 394.61 | Thermod... |
| Pvap | 0.11 | kPa | 394.64 | Thermod... |
| Pvap | 0.13 | kPa | 397.00 | Thermod... |
| Pvap | 0.13 | kPa | 397.02 | Thermod... |
| Pvap | 0.15 | kPa | 399.42 | Thermod... |
| Pvap | 0.15 | kPa | 399.45 | Thermod... |
| Pvap | 0.17 | kPa | 401.81 | Thermod... |
| Pvap | 0.17 | kPa | 401.81 | Thermod... |
| Pvap | 0.17 | kPa | 401.83 | Thermod... |
| Pvap | 0.18 | kPa | 402.16 | Vapor-L... |
| Pvap | 0.20 | kPa | 404.23 | Thermod... |
| Pvap | 0.20 | kPa | 404.26 | Thermod... |
| Pvap | 0.22 | kPa | 406.62 | Thermod... |
| Pvap | 0.22 | kPa | 406.62 | Thermod... |
| Pvap | 0.23 | kPa | 406.64 | Thermod... |
| Pvap | 0.27 | kPa | 409.68 | Thermod... |
| Pvap | 0.27 | kPa | 409.69 | Thermod... |
| Pvap | 0.31 | kPa | 412.08 | Thermod... |
| Pvap | 0.31 | kPa | 412.11 | Thermod... |
| Pvap | 0.32 | kPa | 412.24 | Vapor-L... |
| Pvap | 0.35 | kPa | 414.48 | Thermod... |
| Pvap | 0.35 | kPa | 414.49 | Thermod... |
| Pvap | 0.40 | kPa | 416.89 | Thermod... |
| Pvap | 0.40 | kPa | 416.92 | Thermod... |
| Pvap | 0.46 | kPa | 419.30 | Thermod... |
| Pvap | 0.46 | kPa | 419.30 | Thermod... |
| Pvap | 0.52 | kPa | 421.70 | Thermod... |
| Pvap | 0.52 | kPa | 421.73 | Thermod... |
| Pvap | 0.53 | kPa | 422.28 | Vapor-L... |
| Pvap | 0.59 | kPa | 424.10 | Thermod... |
| Pvap | 0.59 | kPa | 424.11 | Thermod... |
| Pvap | 0.67 | kPa | 426.50 | Thermod... |
| Pvap | 0.67 | kPa | 426.53 | Thermod... |
| Pvap | 0.76 | kPa | 428.91 | Thermod... |
| Pvap | 0.76 | kPa | 428.91 | Thermod... |
| Pvap | 0.86 | kPa | 431.31 | Thermod... |
| Pvap | 0.86 | kPa | 431.34 | Thermod... |
| Pvap | 0.98 | kPa | 432.45 | Vapor-L... |
| Pvap | 0.97 | kPa | 433.72 | Thermod... |
| Pvap | 0.97 | kPa | 433.73 | Thermod... |
| Pvap | 1.09 | kPa | 436.11 | Thermod... |
| Pvap | 1.09 | kPa | 436.13 | Thermod... |
| Pvap | 2.75 | kPa | 452.64 | Vapor-L... |
| Pvap | 4.10 | kPa | 462.86 | Vapor-L... |
| Pvap | 3.85 | kPa | 463.15 | Vapor P... |
| Pvap | 6.70 | kPa | 477.25 | Thermop... |
| Pvap | 8.64 | kPa | 483.15 | Vapor P... |
| Pvap | 13.30 | kPa | 493.35 | Thermop... |
| Pvap | 17.90 | kPa | 503.15 | Vapor P... |
| Pvap | 20.00 | kPa | 505.55 | Thermop... |
| Pvap | 26.70 | kPa | 513.95 | Thermop... |
| Pvap | 33.30 | kPa | 520.65 | Thermop... |
| Pvap | 34.50 | kPa | 523.15 | Vapor P... |
| Pvap | 62.60 | kPa | 543.15 | Vapor P... |
| Pvap | 66.66 | kPa | 547.25 | Isobari... |
| Pvap | 79.99 | kPa | 553.96 | Isobari... |
| Pvap | 95.99 | kPa | 560.95 | Isobari... |
| n0 | [1.46674; 1.47552] | [288.15; 323.15] |
|
|
|
T(K) Refractive Index 1.47 1.47 1.47 1.47 1.47 1.48 290 300 310 320 | ||||
| n0 | 1.47552 | 288.15 | Experim... | |
| n0 | 1.47400 | 293.15 | Experim... | |
| n0 | 1.47427 | 293.15 | Experim... | |
| n0 | 1.47260 | 298.15 | Liquid ... | |
| n0 | 1.47100 | 298.15 | (Vapor ... | |
| n0 | 1.47301 | 298.15 | Experim... | |
| n0 | 1.47175 | 303.15 | Experim... | |
| n0 | 1.47048 | 308.15 | Experim... | |
| n0 | 1.46920 | 313.15 | Experim... | |
| n0 | 1.46791 | 318.15 | Experim... | |
| n0 | 1.46674 | 323.15 | Experim... | |
| ρl | [1214.80; 1270.87] | kg/m3 | [278.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 1210 1220 1230 1240 1250 1260 1270 300 350 | ||||
| ρl | 1270.87 | kg/m3 | 278.15 | Volume ... |
| ρl | 1267.00 | kg/m3 | 283.15 | Effect ... |
| ρl | 1264.40 | kg/m3 | 288.15 | Volume ... |
| ρl | 1262.70 | kg/m3 | 288.15 | Density... |
| ρl | 1261.00 | kg/m3 | 293.00 | KDB |
| ρl | 1262.00 | kg/m3 | 293.15 | Density... |
| ρl | 1260.98 | kg/m3 | 293.15 | (Vapor-... |
| ρl | 1260.99 | kg/m3 | 293.15 | Volume ... |
| ρl | 1261.00 | kg/m3 | 293.15 | Effect ... |
| ρl | 1260.50 | kg/m3 | 293.15 | Density... |
| ρl | 1260.73 | kg/m3 | 293.15 | Thermod... |
| ρl | 1267.40 | kg/m3 | 295.00 | New dev... |
| ρl | 1259.00 | kg/m3 | 298.15 | Density... |
| ρl | 1258.52 | kg/m3 | 298.15 | Measure... |
| ρl | 1257.91 | kg/m3 | 298.15 | Volume ... |
| ρl | 1257.20 | kg/m3 | 298.15 | Density... |
| ρl | 1262.00 | kg/m3 | 298.15 | Solubil... |
| ρl | 1258.90 | kg/m3 | 298.15 | Densiti... |
| ρl | 1257.65 | kg/m3 | 298.15 | Thermod... |
| ρl | 1258.52 | kg/m3 | 298.15 | Phase e... |
| ρl | 1257.70 | kg/m3 | 298.20 | Deterpe... |
| ρl | 1254.80 | kg/m3 | 303.15 | Density... |
| ρl | 1255.00 | kg/m3 | 303.15 | Effect ... |
| ρl | 1255.80 | kg/m3 | 303.15 | Density... |
| ρl | 1254.48 | kg/m3 | 303.15 | Thermod... |
| ρl | 1257.13 | kg/m3 | 303.15 | Measure... |
| ρl | 1255.60 | kg/m3 | 303.15 | Densiti... |
| ρl | 1251.50 | kg/m3 | 308.15 | Density... |
| ρl | 1251.38 | kg/m3 | 308.15 | Thermod... |
| ρl | 1252.70 | kg/m3 | 308.15 | Density... |
| ρl | 1252.70 | kg/m3 | 308.15 | Densiti... |
| ρl | 1251.66 | kg/m3 | 308.15 | Volume ... |
| ρl | 1248.00 | kg/m3 | 313.15 | Effect ... |
| ρl | 1249.50 | kg/m3 | 313.15 | Densiti... |
| ρl | 1248.90 | kg/m3 | 313.15 | Density... |
| ρl | 1249.60 | kg/m3 | 313.15 | Density... |
| ρl | 1249.00 | kg/m3 | 313.15 | Experim... |
| ρl | 1246.00 | kg/m3 | 318.15 | Density... |
| ρl | 1246.20 | kg/m3 | 318.15 | Densiti... |
| ρl | 1246.40 | kg/m3 | 318.15 | Density... |
| ρl | 1242.90 | kg/m3 | 323.15 | Densiti... |
| ρl | 1242.40 | kg/m3 | 323.15 | Density... |
| ρl | 1242.11 | kg/m3 | 323.15 | Volume ... |
| ρl | 1242.40 | kg/m3 | 323.15 | Experim... |
| ρl | 1243.20 | kg/m3 | 323.15 | Density... |
| ρl | 1240.50 | kg/m3 | 328.15 | Density... |
| ρl | 1240.00 | kg/m3 | 328.15 | Density... |
| ρl | 1239.60 | kg/m3 | 328.15 | Densiti... |
| ρl | 1236.70 | kg/m3 | 333.15 | Density... |
| ρl | 1235.70 | kg/m3 | 333.15 | Experim... |
| ρl | 1236.00 | kg/m3 | 333.15 | Densiti... |
| ρl | 1235.71 | kg/m3 | 333.15 | Volume ... |
| ρl | 1233.40 | kg/m3 | 338.15 | Density... |
| ρl | 1230.10 | kg/m3 | 343.15 | Density... |
| ρl | 1228.90 | kg/m3 | 343.15 | Experim... |
| ρl | 1225.79 | kg/m3 | 348.15 | Volume ... |
| ρl | 1221.90 | kg/m3 | 353.15 | Experim... |
| ρl | 1214.80 | kg/m3 | 363.15 | Experim... |
| ΔfusS | [62.70; 62.80] | J/mol×K | [291.00; 292.00] |
|
| ΔfusS | 62.80 | J/mol×K | 291.00 | NIST |
| ΔfusS | 62.70 | J/mol×K | 292.00 | NIST |
| γ | [0.06; 0.07] | N/m | [288.10; 333.20] |
|
|
T(K) Surface Tension (N/m) 0.06 0.06 0.06 0.06 0.07 300 320 | ||||
| γ | 0.07 | N/m | 288.10 | Studies... |
| γ | 0.06 | N/m | 293.10 | Studies... |
| γ | 0.06 | N/m | 293.20 | Surface... |
| γ | 0.06 | N/m | 298.10 | Studies... |
| γ | 0.06 | N/m | 298.20 | Surface... |
| γ | 0.06 | N/m | 303.10 | Studies... |
| γ | 0.06 | N/m | 303.20 | Surface... |
| γ | 0.06 | N/m | 308.10 | Studies... |
| γ | 0.06 | N/m | 313.10 | Studies... |
| γ | 0.06 | N/m | 313.20 | Surface... |
| γ | 0.06 | N/m | 318.10 | Studies... |
| γ | 0.06 | N/m | 323.10 | Studies... |
| γ | 0.06 | N/m | 323.20 | Surface... |
| γ | 0.06 | N/m | 333.20 | Surface... |
| λ | [0.28; 0.28] | W/m×K | [283.15; 333.15] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.26 0.27 0.28 0.29 0.3 0.31 300 320 | ||||
| λ | 0.28 | W/m×K | 283.15 | Measure... |
| λ | 0.28 | W/m×K | 293.15 | Measure... |
| λ | 0.28 | W/m×K | 303.15 | Measure... |
| λ | 0.28 | W/m×K | 313.15 | Measure... |
| λ | 0.28 | W/m×K | 323.15 | Measure... |
| λ | 0.28 | W/m×K | 333.15 | Measure... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [459.28; 560.68] | K | [3.47; 94.93] |
|
| Tboil | 459.28 | K | 3.47 | Improvi... |
| Tboil | 560.68 | K | 94.93 | Experim... |
| Tboilr | 455.20 | K | 2.70 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 100.00 | 1.2 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 91.20 | 303.15 | 1255.0 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 1258.4 |
| 298.15 | 5000.00 | 1260.7 |
| 298.15 | 10000.00 | 1262.3 |
| 298.15 | 15000.00 | 1263.7 |
| 298.15 | 20000.00 | 1265.2 |
| 298.15 | 25000.00 | 1266.6 |
| 303.15 | 100.00 | 1255.7 |
| 303.15 | 5000.00 | 1257.8 |
| 303.15 | 10000.00 | 1259.3 |
| 303.15 | 15000.00 | 1260.8 |
| 303.15 | 20000.00 | 1262.3 |
| 303.15 | 25000.00 | 1263.7 |
| 308.15 | 100.00 | 1252.9 |
| 308.15 | 5000.00 | 1254.9 |
| 308.15 | 10000.00 | 1256.3 |
| 308.15 | 15000.00 | 1257.9 |
| 308.15 | 20000.00 | 1259.4 |
| 308.15 | 25000.00 | 1260.8 |
| 313.15 | 100.00 | 1250.1 |
| 313.15 | 5000.00 | 1251.8 |
| 313.15 | 10000.00 | 1253.4 |
| 313.15 | 15000.00 | 1254.9 |
| 313.15 | 20000.00 | 1256.4 |
| 313.15 | 25000.00 | 1257.9 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 101.13 | 1238.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [451.47; 591.41] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.39571e+01 | |||
| Coefficient B | -3.29185e+03 | |||
| Coefficient C | -2.10657e+02 | |||
| Temperature range, min. | 451.47 | |||
| Temperature range, max. | 591.41 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
| Pvap | 1.33 | kPa | 451.47 | Calculated Property |
| Pvap | 3.05 | kPa | 467.02 | Calculated Property |
| Pvap | 6.36 | kPa | 482.57 | Calculated Property |
| Pvap | 12.25 | kPa | 498.12 | Calculated Property |
| Pvap | 22.05 | kPa | 513.67 | Calculated Property |
| Pvap | 37.47 | kPa | 529.21 | Calculated Property |
| Pvap | 60.61 | kPa | 544.76 | Calculated Property |
| Pvap | 93.93 | kPa | 560.31 | Calculated Property |
| Pvap | 140.24 | kPa | 575.86 | Calculated Property |
| Pvap | 202.65 | kPa | 591.41 | Calculated Property |
| Pvap | [7.84e-06; 3545.31] | kPa | [290.15; 723.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.65510e+02 | |||
| Coefficient B | -1.67263e+04 | |||
| Coefficient C | -2.12587e+01 | |||
| Coefficient D | 1.10048e-05 | |||
| Temperature range, min. | 290.15 | |||
| Temperature range, max. | 723.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 600 | ||||
| Pvap | 7.84e-06 | kPa | 290.15 | Calculated Property |
| Pvap | 1.52e-03 | kPa | 338.24 | Calculated Property |
| Pvap | 0.06 | kPa | 386.34 | Calculated Property |
| Pvap | 0.96 | kPa | 434.43 | Calculated Property |
| Pvap | 7.77 | kPa | 482.53 | Calculated Property |
| Pvap | 40.79 | kPa | 530.62 | Calculated Property |
| Pvap | 159.30 | kPa | 578.72 | Calculated Property |
| Pvap | 507.43 | kPa | 626.81 | Calculated Property |
| Pvap | 1405.71 | kPa | 674.91 | Calculated Property |
| Pvap | 3545.31 | kPa | 723.00 | Calculated Property |
Similar Compounds
![1,2,3,4-Butanetetrol, [S-(R*,R*)]-.](data:image/png;base64,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)
Find more compounds similar to Glycerin.
Mixtures
- Isobutyl acetate + Glycerin + 1-Propanol, 2-methyl-
- Ethanol + Glycerin + Water
- Carbon dioxide + Glycerin
- Carbon dioxide + Pyrimido[1,2-a]azepine, 2,3,4,6,7,8,9,10-octahydro- + Glycerin
- Amylene hydrate + Glycerin + Water
- Toluene + Decane + Glycerin
- Isopropyl Alcohol + Glycerin
- Glycerin + Tetracycline hydrochloride
- Tetra-N-butylammonium bromide + Glycerin
- Glucose + Tetra-N-butylammonium bromide + Glycerin
- Choline chloride + Glycerin + Water
- Glycerin + Water
- Glycerin + Methyl Alcohol
- Ethanol + Glycerin
- Pyridine + Glycerin
- Glycerin + Methyl Alcohol + Water
- sodium chloride + Glycerin + Water
- sodium chloride + Glycerin
- Glycerin + Ethanol, 2-diethylamino-, hydrochloride
- Glycerin + Water + Ethanol, 2-diethylamino-, hydrochloride
Find more mixtures with Glycerin.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Conductometric Study of Some Metal Halides in Glycerol + Water Mixtures
- Liquid liquid equilibria of the systems isobutyl acetate + isobutyl alcohol +water and isobutyl acetate + isobutyl alcohol + glycerol at different temperatures
- New device for fast measuring surface tension, density and viscosity of liquids
- Osmotic coefficient data and an excess Gibbs energy function for single-phase complex system of glucose + alcohol +water
- Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
- Measurement and calculation of vapor liquid equilibria for methanol + glycerol and ethanol + glycerol systems at 493 573K
- Liquid-liquid equilibria for mixtures containing water, methanol, fatty acid methyl esters, and glycerol
- VLE of CO2 + glycerol + (ethanol or 1-propanol or 1-butanol)
- Densities of a deep eutectic solvent based on choline chloride and glycerol and its aqueous mixtures at elevated pressures
- Phase equilibria for the ternary systems ethanol, water + ethylene glycol or + glycerol at 101.3 kPa
- LLE for the systems ethyl palmitate (palmiticacid)(1) + ethanol(2) + glycerol (water)(3)
- Prediction of refractive index and density of deep eutectic solvents using atomic contributions
- Electrical conductivity of ammonium and phosphonium based deepeutectic solvents: Measurements and artificial intelligence-basedprediction
- Solubility of CO2 in glycerol at high pressures
- Densities and dynamic viscosities of (choline chloride + glycerol) deep eutectic solvent and its aqueous mixtures in the temperature range (283.15-363.15) K
- Measurements and modeling of CO2 solubility in 1,8-diazabicyclo-[5.4.0]-undec-7-ene - glycerol solutions
- Measurements and correlation at different temperatures of liquid-liquid equilibria of 2-butanol or 2-methyl-2-butanol + 1,2,3-propanetriol + water ternary systems
- Acoustic investigation of choline chloride based ionic liquids analogues
- Thermodynamic properties of glycerol: experimental and theoretical study
- Measurement of phase equilibria data for the extraction of toluene from alkane using different solvents
- Phase equilibria of triolein to biodiesel reactor systems
- Experimental vapour - liquid equilibrium data of the quaternary system Methanol (1) + Isopropyl Alcohol (2) + Water (3) + Glycerol (4) along with Isopropyl Alcohol (2) + Glycerol (4) and Isopropyl Alcohol (2) + Water (3) binary data at atmospheric and sub-atmospheric pressures.
- Liquid-liquid equilibrium for the ternary system of isopropyl acetate + 2-propanol + glycerol at different temperatures under atmospheric pressure
- A model to calculate concentration-dependent surface tension of binary systems
- Measurement and correlation of ternary vapor-liquid equilibria for methanol + glycerol + fatty acid methyl ester (methyl laurate, methyl myristate, methyl palmitate) systems at elevated temperatures and pressures
- Partitioning of diuron in a novel aqueous two-phase system based on polyols and tetrahydrofuran
- Formation of type III deep eutectic solvents and effect of water on their intermolecular interactions
- Acoustic, volumetric, transport, optical and rheological properties of benzyltripropylammonium based Deep Eutectic Solvents
- Thermodynamics of phase transfer for polar molecules from alkanes to deep eutectic solvents
- Liquid pharmaceuticals formulation by eutectic formation
- Solubility of glucose in tetrabutylammonium bromide based deep eutectic solvents: Experimental and molecular dynamic simulations
- Oil desulfurization using deep eutectic solvents as sustainable and economical extractants via liquid-liquid extraction: Experimental and PC-SAFT predictions
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- Viscometric study of myo-inositol in aqueous deep eutectic solvent solutions
- Extraction of benzothiazole and thiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive denitrogenation and desulfurization agents
- The experimental study on the influence of crown ethers and glycols on the mutual solubility of lithium bromide in water
- Sodium salts solubility in ternary glycerol+water+alcohol mixtures present in purification process of crude glycerol from the biodiesel industry
- Thermodynamic characterization of deep eutectic solvents at high pressures
- 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
- Apparent molar volumes and apparent molar heat capacities of aqueous adonitol, dulcitol, glycerol, meso-erythritol, myo-inositol, D-sorbitol, and xylitol at temperatures from (278.15 to 368.15) K and at the pressure 0.35 MPa
- Experimental (vapour + liquid) equilibrium data of (methanol + water), (water + glycerol) and (methanol + glycerol) systems at atmospheric and sub-atmospheric pressures
- (Vapor + liquid) equilibrium for the binary systems {water + glycerol} and {ethanol + glycerol, ethyl stearate, and ethyl palmitate} at low pressures
- (Liquid + liquid) equilibrium for the system {ethyl stearate(1) + ethanol(2) + glycerol(3)}
- 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
- Solubility of carbon dioxide in a eutectic mixture of choline chloride and glycerol at moderate pressures
- Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
- Densities, refractive indices, and viscosities of N,N-diethylethanol ammonium chloride - glycerol or - ethylene glycol deep eutectic solvents and their aqueous solutions
- Vapor-liquid equilibrium of the (water + ethanol + glycerol) system: Experimental and modelling data at normal pressure
- (Vapor-liquid) equilibria and excess Gibbs free energy functions of (ethanol + glycerol), or (water + glycerol) binary mixtures at several temperatures
- Liquid extraction of polyhydric alcohols from water using [A336][SCN] as a solvent
- NaCl and KCl effect on (vapour + liquid) equilibrium of binary, ternary and quaternary systems involving water, ethanol and glycerol at low pressures
- Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
- Liquid glycerol: Experimental densities at pressures of up to 25 MPa, and some derived thermodynamic properties
- Measurement and modelling of urea solubility in aqueous propane-1,2,3-triol and prop-2-enoic acid solutions
- Experimental determination of the LLE data of systems consisting of {hexane + benzene + deep eutectic solvent} and prediction using the Conductor-like Screening Model for Real Solvents
- Molar enthalpy of mixing and refractive indices of choline chloride-based deep eutectic solvents with water
- Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
- The viscosity of glycerol
- Density and refractive index measurements of transition-temperature mixture (deep eutectic analogues) based on potassium carbonate with dual hydrogen bond donors for CO2 capture
- Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
- Density studies of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures between 288.15 K and 328.15 K
- Experimental and modeling vapor-liquid equilibrium for the binary systems {ethanol(1) + glycerol(2)} and {tert-butanol(1) + glycerol(2)} at high pressures
- Studies on surface tension of 1,8-diazabicyclo [5.4.0] undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 323.1 K
- Volumetric and ultrasonic studies on interactions of ethylene glycol, diethylene glycol and triethylene glycol in aqueous solutions of glycerol at temperatures T = (293.15 K - 308.15) K
- Removal of 2- and 3-methylthiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive desulfurization agents
- Acoustical and volumetric investigation of polyethylene glycol 400 and polyethylene glycol 4000 in aqueous solutions of glycerol at different temperatures
- The NADES glyceline as a potential Green Solvent: A comprehensive study of its thermophysical properties and effect of water inclusion
- Solubility modelling and thermodynamic properties of allopurinol in aqueous solutions of four deep eutectic solvents
- Solubility and thermodynamic properties of NH3 in choline chloride-based deep eutectic solvents
- Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
- Studies on viscosity and conductivity of 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU)-glycerol and CO2-DBU-glycerol solutions at temperatures from 288.1 K to 328.1 K
- 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
- Enthalpies of dilution of formamide in aqueous alcohol solutions at 298.15K
- Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles
- Enthalpic Interaction Coefficients of N,N-Dimethylformamide in Aqueous Ethylene Glycol and Glycerol Solutions at 298.15K
- Densities of Ammonium and Phosphonium based Deep Eutectic Solvents: Prediction using Artificial Intelligent and Group Contribution Techniques
- Molar heat capacities of choline chloride-based deep eutectic solvents and their binary mixtures with water
- Vapor pressure of aqueous choline chloride-based deep eutectic solvents (ethaline, glyceline, maline and reline) at 30 to 70 deg C
- Molar heat capacities and electrical conductivities of two ammonium-based deepeutectic solvents and their aqueous solutions
- Volume properties of liquid mixture of water + glycerol over the temperature range from 278.15 to 348.15 K at atmospheric pressure
- Application of the Eotvos and Guggenheim empirical rules for predicting the density and surface tension of ionic liquids analogues
- Ionic Liquids Analogues Based on Potassium Carbonate
- Experimental densities and viscosities of binary mixture of 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or glycerol with sulfolane and their molecular interaction by COSMO-RS
- Measurements of the density, refractive index, electrical conductivity, thermal conductivity and dynamic viscosity for tributylmethylphosphonium and methylsulfate based ionic liquids
- Vapor Liquid Equilibrium of Water + Ethanol + Glycerol: Experimental Measurement and Modeling for Ethanol Dehydration by Extractive Distillation
- Glycerol-Based Deep Eutectic Solvents as Extractants for the Separation of MEK and Ethanol via Liquid Liquid Extraction
- Molar Heat Capacity of Selected Type III Deep Eutectic Solvents
- Experimental Measurement and Modeling of Vapor-Liquid Equilibrium for the Ternary System Water + 1-Propanol + Glycerol
- Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems
- Liquid Liquid Equilibrium for the Ternary System of Methyl Laurate/Methyl Myristate + Ethanol + Glycerol at 318.15 and 333.15 K
- Viscosities and Carbon Dioxide Solubilities of Guanidine Carbonate and Malic Acid-Based Eutectic Solvents
- Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
- Density Measurements of CO2-Expanded Liquids
- Solubility of Etoricoxib in Aqueous Solutions of Glycerin, Methanol, Polyethylene Glycols 200, 400, 600, and Propylene Glycol at 298.2 K
- Binary Diffusion Coefficients of Glycerol-Water Mixtures for Temperatures from 323 to 448 K by Dynamic Light Scattering
- Effect of the Type of Ammonium Salt on the Extractive Desulfurization of Fuels Using Deep Eutectic Solvents
- Deterpenation of Citrus Essential Oils Using Glycerol-Based Deep Eutectic Solvents
- Effect of Ethylene, Diethylene, and Triethylene Glycols and Glycerol on the Physicochemical Properties and Phase Behavior of Benzyltrimethyl and Benzyltributylammonium Chloride Based Deep Eutectic Solvents at 283.15-343.15 K
- Effect of Cosolvents DMSO and Glycerol on the Self-Assembly Behavior of SDBS and CPC: An Experimental and Theoretical Approach
- Thermophysical Properties of Ternary Systems Potassium Formate + Propylene Glycol/Glycerol + Water
- Solubilities and Thermodynamic Properties of NH3 in Glycerin and its Derivatives
- Thermophysical and Molar Volume Aberration of Amphiphilic Eutectic Mix of Bivalent Diols and Ammonium-Ionic Liquid
- Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
- Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
- Ternary Diffusion Coefficients of Glycerol + Acetone + Water by Taylor Dispersion Measurements at 298.15 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
- 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
- Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
- Phosphonium-Based Ionic Liquids Analogues and Their Physical Properties
- Experimental and Predicted (Vapor + Liquid) Equilibrium Data of Ternary Mixtures of Methanol, Water, and Propan-1,2,3-triol at 96 kPa
- Measurement and Correlation of Solubilities of Potassium Chloride and Potassium Sulfate in Aqueous Glycerol Solutions
- Solubilities, Densities, and Refractive Indices for the Ternary Systems Glycerin + MCl + H2O (M = Na, K, Rb, Cs) at (298.15 and 308.15) K
- Vapor-Liquid Equilibria of Glycerol, 1,3-Propanediol, Glycerol + Water, and Glycerol + 1,3-Propanediol
- Liquid-Liquid Equilibria for the System Dimethyl Carbonate + Methanol + Glycerol in the Temperature Range of (303.15 to 333.15) 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
- Article Ternary Liquid Liquid Equilibrium of Biodiesel Compounds for Systems Consisting of a Methyl Ester + Glycerin + Water
- Solubility of Sodium Salts in Ammonium-Based Deep Eutectic Solvents
- Experimental Vapor Liquid Equilibria for the Systems {2-Ethyl-1-hexanol + Glycerol + CO2} and {2-Methyl-2-propanol + Glycerol + CO2}
- Tetrabutylammonium Chloride Based Ionic Liquid Analogues and Their Physical Properties
- Liquid-liquid equilibria for the system acetone + solketal + glycerol at 303.2, 313.2 and 323.2 K
- Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
- Experimental Measurement and Modeling of Ternary Vapor Liquid Equilibrium for Water + 2-Propanol + Glycerol
- Liquid Liquid Equilibria of Three Ternary Systems: {Glycerol + Benzene + Methanol}, {Glycerol + Benzene + Ethanol}, and {Glycerol + Benzene + 1-Propanol}
- Isothermal Vapor Liquid Equilibrium of Ethanol + Glycerol and 2-Propanol + Glycerol at Different Temperatures
- 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
- 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
- Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols
- Physical Properties (Density, Excess Molar Volume, Viscosity, Surface Tension, and Refractive Index) of Ethanol + Glycerol
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
- Densities and Viscosities of Propane-1,2,3-triol + Ethane-1,2-diol at T = (298.15 to 338.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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