- InChI
- InChI=1S/C3H8O2/c1-3(5)2-4/h3-5H,2H2,1H3
- InChI Key
- DNIAPMSPPWPWGF-UHFFFAOYSA-N
- Formula
- C3H8O2
- SMILES
- CC(O)CO
- Molecular Weight1
- 76.09
- CAS
- 57-55-6
- Other Names
-
- (.+-.)-1,2-propanediol
- (.+/-.)-1,2-Propanediol
- (R,S)-1,2-propanediol
- (RS)-1,2-Propanediol
- 1,2-Dihydroxypropane
- 1,2-PROPANEDIOL
- 1,2-PROPYLENE GLYCOL
- 1,2-Propandiol
- 1,2-Propylenglykol
- 1,2-propanediol (propylene glycol)
- 2,3-Propanediol
- 2-Hydroxypropanol
- DL-1,2-Propanediol
- DL-Propylene glycol
- Dowfrost
- Ilexan P
- Isopropylene glycol
- METHYLETHYLENE GLYCOL
- Methylethyl glycol
- Monopropylene glycol
- NSC 69860
- PG 12
- Prolugen
- Propane-1,2-diol
- Propylene glycol USP
- Propylenglycol
- SIRLENE
- Sentry Propylene Glycol
- Solar winter ban
- Solargard P
- Trimethyl glycol
- Ucar 35
- propanediol
- propylene glycol (1,2-propanediol)
- «alpha»-Propylene glycol
- «alpha»-Propylene glycol
- 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).
- 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- vspec : Specific Volume (m3/kg).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-1838.10; -1822.90] | kJ/mol |
|
| ΔcH°liquid | -1822.90 ± 4.10 | kJ/mol | NIST |
| ΔcH°liquid | -1838.10 ± 2.30 | kJ/mol | NIST |
| ΔcH°liquid | -1823.50 ± 1.80 | kJ/mol | NIST |
| μ | 3.60 | debye | KDB |
| ΔfG° | -301.70 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-435.30; -421.00] | kJ/mol |
|
| ΔfH°gas | -424.20 | kJ/mol | KDB |
| ΔfH°gas | -429.80 ± 4.10 | kJ/mol | NIST |
| ΔfH°gas | -421.00 ± 3.00 | kJ/mol | NIST |
| ΔfH°gas | -435.30 | kJ/mol | NIST |
| ΔfH°liquid | [-501.00; -486.00] | kJ/mol |
|
| ΔfH°liquid | -501.00 ± 4.10 | kJ/mol | NIST |
| ΔfH°liquid | -486.00 ± 3.00 | kJ/mol | NIST |
| ΔfH°liquid | -500.30 ± 1.80 | kJ/mol | NIST |
| ΔfusH° | 8.18 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 55.24 | kJ/mol | Joback Calculated Property |
| log10WS | 0.28 | Crippen Calculated Property | |
| logPoct/wat | -0.640 | Crippen Calculated Property | |
| McVol | 64.870 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 6070.00 | kPa | KDB |
| Inp | [705.00; 764.00] |
|
|
| Inp | 745.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 710.00 | NIST | |
| Inp | 716.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 710.00 | NIST | |
| Inp | 710.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 745.00 | NIST | |
| I | [1583.00; 1612.00] |
|
|
| I | 1599.00 | NIST | |
| I | 1599.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1605.00 | NIST | |
| I | 1603.00 | NIST | |
| I | 1603.00 | NIST | |
| I | 1612.00 | NIST | |
| I | 1602.00 | NIST | |
| I | 1597.00 | NIST | |
| I | 1612.00 | NIST | |
| I | 1585.00 | NIST | |
| I | 1611.00 | NIST | |
| I | 1594.00 | NIST | |
| I | 1599.00 | NIST | |
| I | 1603.00 | NIST | |
| I | Outlier 1583.00 | NIST | |
| I | 1589.00 | NIST | |
| I | 1612.00 | NIST | |
| I | 1611.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1599.00 | NIST | |
| I | 1603.00 | NIST | |
| Tboil | [458.45; 462.00] | K |
|
| Tboil | 460.50 | K | KDB |
| Tboil | 460.20 | K | NIST |
| Tboil | 460.45 | K | NIST |
| Tboil | 460.15 ± 2.00 | K | NIST |
| Tboil | 459.15 ± 1.00 | K | NIST |
| Tboil | 461.15 ± 3.00 | K | NIST |
| Tboil | 460.60 ± 0.50 | K | NIST |
| Tboil | 461.00 ± 0.20 | K | NIST |
| Tboil | 459.80 ± 0.50 | K | NIST |
| Tboil | 459.15 ± 1.00 | K | NIST |
| Tboil | 460.55 ± 0.50 | K | NIST |
| Tboil | 462.00 ± 2.00 | K | NIST |
| Tboil | 460.15 ± 2.00 | K | NIST |
| Tboil | 459.15 ± 2.00 | K | NIST |
| Tboil | 458.45 ± 3.00 | K | NIST |
| Tboil | 461.65 ± 3.00 | K | NIST |
| Tc | 625.00 | K | KDB |
| Tfus | 213.00 | K | KDB |
| Vc | 0.237 | m3/kmol | KDB |
| Zc | 0.2768350 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [135.47; 165.24] | J/mol×K | [451.96; 614.38] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 135 140 145 150 155 160 165 450 500 550 600 | ||||
| Cp,gas | 135.47 | J/mol×K | 451.96 | Joback Calculated Property |
| Cp,gas | 140.93 | J/mol×K | 479.03 | Joback Calculated Property |
| Cp,gas | 146.19 | J/mol×K | 506.10 | Joback Calculated Property |
| Cp,gas | 151.24 | J/mol×K | 533.17 | Joback Calculated Property |
| Cp,gas | 156.10 | J/mol×K | 560.24 | Joback Calculated Property |
| Cp,gas | 160.76 | J/mol×K | 587.31 | Joback Calculated Property |
| Cp,gas | 165.24 | J/mol×K | 614.38 | Joback Calculated Property |
| Cp,liquid | [177.00; 215.30] | J/mol×K | [276.70; 353.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 180 190 200 210 280 300 320 340 | ||||
| Cp,liquid | 180.30 | J/mol×K | 276.70 | NIST |
| Cp,liquid | 189.90 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 177.00 | J/mol×K | 303.00 | NIST |
| Cp,liquid | 192.80 | J/mol×K | 303.15 | Heat ca... |
| Cp,liquid | 197.00 | J/mol×K | 313.15 | Heat ca... |
| Cp,liquid | 201.30 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 206.00 | J/mol×K | 333.15 | Heat ca... |
| Cp,liquid | 210.60 | J/mol×K | 343.15 | Heat ca... |
| Cp,liquid | 215.30 | J/mol×K | 353.15 | Heat ca... |
| η | [0.0057040; 0.0562100] | Pa×s | [293.15; 343.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 0.01 0.02 0.03 0.04 0.05 0.06 300 320 340 | ||||
| η | 0.0562100 | Pa×s | 293.15 | Excess ... |
| η | 0.0454403 | Pa×s | 298.15 | Densiti... |
| η | 0.0434340 | Pa×s | 298.15 | Densiti... |
| η | 0.0326300 | Pa×s | 303.15 | Excess ... |
| η | 0.0339949 | Pa×s | 303.15 | Densiti... |
| η | 0.0324000 | Pa×s | 303.15 | Vapour ... |
| η | 0.0242440 | Pa×s | 308.15 | Densiti... |
| η | 0.0263377 | Pa×s | 308.15 | Densiti... |
| η | 0.0191200 | Pa×s | 313.15 | Vapour ... |
| η | 0.0195800 | Pa×s | 313.15 | Excess ... |
| η | 0.0121000 | Pa×s | 323.15 | Vapour ... |
| η | 0.0127900 | Pa×s | 323.15 | Excess ... |
| η | 0.0081900 | Pa×s | 333.15 | Vapour ... |
| η | 0.0057040 | Pa×s | 343.15 | Vapour ... |
| ΔvapH | [47.50; 66.50] | kJ/mol | [353.00; 431.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 50 55 60 65 360 380 400 420 | ||||
| ΔvapH | 64.00 ± 2.00 | kJ/mol | 353.00 | NIST |
| ΔvapH | 58.20 | kJ/mol | 378.00 | NIST |
| ΔvapH | 58.60 | kJ/mol | 389.50 | NIST |
| ΔvapH | 66.50 | kJ/mol | 390.50 | NIST |
| ΔvapH | 56.20 ± 0.20 | kJ/mol | 430.50 | NIST |
| ΔvapH | 52.00 ± 0.30 | kJ/mol | 430.50 | NIST |
| ΔvapH | 47.50 ± 0.60 | kJ/mol | 430.50 | NIST |
| ΔvapH | 60.00 ± 0.30 | kJ/mol | 430.50 | NIST |
| ΔvapH | 56.00 | kJ/mol | 431.50 | NIST |
| Pvap | [0.62; 100.00] | kPa | [345.15; 460.79] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 350 400 450 | ||||
| Pvap | 0.62 | kPa | 345.15 | Vapor L... |
| Pvap | 0.70 | kPa | 347.15 | Vapor L... |
| Pvap | 0.84 | kPa | 350.15 | Vapor-l... |
| Pvap | 0.84 | kPa | 350.15 | Vapor L... |
| Pvap | 1.00 | kPa | 353.15 | Vapor L... |
| Pvap | 1.13 | kPa | 355.15 | Vapor-l... |
| Pvap | 1.13 | kPa | 355.15 | Vapor L... |
| Pvap | 1.27 | kPa | 357.15 | Vapor L... |
| Pvap | 1.51 | kPa | 360.15 | Vapor-l... |
| Pvap | 1.51 | kPa | 360.15 | Vapor L... |
| Pvap | 1.78 | kPa | 363.15 | Vapor L... |
| Pvap | 1.99 | kPa | 365.15 | Vapor L... |
| Pvap | 1.99 | kPa | 365.15 | Vapor-l... |
| Pvap | 2.21 | kPa | 367.15 | Vapor L... |
| Pvap | 2.60 | kPa | 370.15 | Vapor-l... |
| Pvap | 2.60 | kPa | 370.15 | Vapor L... |
| Pvap | 3.03 | kPa | 373.15 | Vapor L... |
| Pvap | 3.36 | kPa | 375.15 | Vapor-l... |
| Pvap | 3.36 | kPa | 375.15 | Vapor L... |
| Pvap | 3.72 | kPa | 377.15 | Vapor L... |
| Pvap | 4.00 | kPa | 378.00 | Phase E... |
| Pvap | 4.32 | kPa | 380.15 | Vapor-l... |
| Pvap | 5.50 | kPa | 385.15 | Vapor-l... |
| Pvap | 6.67 | kPa | 389.39 | Excess ... |
| Pvap | 6.95 | kPa | 390.15 | Vapor-l... |
| Pvap | 8.20 | kPa | 393.22 | Vapor-L... |
| Pvap | 8.21 | kPa | 393.25 | Vapor-L... |
| Pvap | 8.71 | kPa | 395.15 | Vapor-l... |
| Pvap | 10.00 | kPa | 396.95 | Excess ... |
| Pvap | 10.23 | kPa | 398.09 | Vapor-L... |
| Pvap | 10.00 | kPa | 398.23 | Isobari... |
| Pvap | 10.00 | kPa | 398.24 | Phase E... |
| Pvap | 10.86 | kPa | 400.15 | Vapor-l... |
| Pvap | 12.00 | kPa | 402.54 | Phase E... |
| Pvap | 13.33 | kPa | 402.95 | Excess ... |
| Pvap | 12.77 | kPa | 403.14 | Vapor-L... |
| Pvap | 12.77 | kPa | 403.15 | Vapor-L... |
| Pvap | 13.44 | kPa | 405.15 | Vapor-l... |
| Pvap | 15.89 | kPa | 408.30 | Vapor-L... |
| Pvap | 16.61 | kPa | 408.60 | Excess ... |
| Pvap | 16.53 | kPa | 410.15 | Vapor-l... |
| Pvap | 19.96 | kPa | 412.95 | Excess ... |
| Pvap | 19.36 | kPa | 413.10 | Vapor-L... |
| Pvap | 19.39 | kPa | 413.15 | Vapor-L... |
| Pvap | 19.99 | kPa | 413.23 | Excess ... |
| Pvap | 20.00 | kPa | 415.13 | Phase E... |
| Pvap | 20.22 | kPa | 415.15 | Vapor-l... |
| Pvap | 23.34 | kPa | 417.15 | Excess ... |
| Pvap | 23.68 | kPa | 418.16 | Vapor-L... |
| Pvap | 24.59 | kPa | 420.15 | Vapor-l... |
| Pvap | 26.62 | kPa | 421.20 | Excess ... |
| Pvap | 26.66 | kPa | 421.21 | Excess ... |
| Pvap | 28.69 | kPa | 423.15 | Vapor-L... |
| Pvap | 28.81 | kPa | 423.26 | Vapor-L... |
| Pvap | 30.00 | kPa | 424.50 | Excess ... |
| Pvap | 30.00 | kPa | 425.72 | Phase E... |
| Pvap | 33.33 | kPa | 427.16 | Excess ... |
| Pvap | 33.57 | kPa | 427.23 | Excess ... |
| Pvap | 36.61 | kPa | 429.55 | Excess ... |
| Pvap | 40.01 | kPa | 432.05 | Excess ... |
| Pvap | 39.99 | kPa | 432.05 | Excess ... |
| Pvap | 40.00 | kPa | 433.59 | Phase E... |
| Pvap | 43.33 | kPa | 433.70 | Excess ... |
| Pvap | 46.66 | kPa | 436.07 | Excess ... |
| Pvap | 50.00 | kPa | 437.77 | Excess ... |
| Pvap | 53.25 | kPa | 439.74 | Excess ... |
| Pvap | 50.00 | kPa | 439.90 | Phase E... |
| Pvap | 56.74 | kPa | 441.27 | Excess ... |
| Pvap | 59.99 | kPa | 443.15 | Excess ... |
| Pvap | 60.00 | kPa | 445.20 | Phase E... |
| Pvap | 70.00 | kPa | 449.79 | Phase E... |
| Pvap | 80.00 | kPa | 453.84 | Phase E... |
| Pvap | 90.00 | kPa | 457.48 | Phase E... |
| Pvap | 100.00 | kPa | 460.79 | Phase E... |
| n0 | [1.42230; 1.43411] | [288.15; 323.15] |
|
|
|
T(K) Refractive Index 1.42 1.42 1.43 1.43 1.43 1.43 1.43 290 300 310 320 | ||||
| n0 | 1.43411 | 288.15 | Experim... | |
| n0 | 1.43143 | 293.15 | Liquid-... | |
| n0 | 1.43247 | 293.15 | Experim... | |
| n0 | 1.43140 | 298.15 | Densiti... | |
| n0 | 1.43081 | 298.15 | Experim... | |
| n0 | 1.43100 | 298.15 | Study o... | |
| n0 | 1.43350 | 298.15 | Vapor L... | |
| n0 | 1.43230 | 298.15 | Excess ... | |
| n0 | 1.43262 | 298.15 | Phase E... | |
| n0 | 1.43230 | 298.15 | Densiti... | |
| n0 | 1.42915 | 303.15 | Experim... | |
| n0 | 1.42751 | 308.15 | Experim... | |
| n0 | 1.42581 | 313.15 | Experim... | |
| n0 | 1.42407 | 318.15 | Experim... | |
| n0 | 1.42230 | 323.15 | Experim... | |
| ρl | [982.60; 1065.80] | kg/m3 | [253.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 980 1000 1020 1040 1060 300 350 | ||||
| ρl | 1065.80 | kg/m3 | 253.15 | Viscosi... |
| ρl | 1062.20 | kg/m3 | 258.15 | Viscosi... |
| ρl | 1058.60 | kg/m3 | 263.15 | Viscosi... |
| ρl | 1054.90 | kg/m3 | 268.15 | Viscosi... |
| ρl | 1051.30 | kg/m3 | 273.15 | Viscosi... |
| ρl | 1052.17 | kg/m3 | 273.15 | Density... |
| ρl | 1043.89 | kg/m3 | 283.15 | Excess ... |
| ρl | 1044.74 | kg/m3 | 283.15 | Density... |
| ρl | 1042.90 | kg/m3 | 283.15 | Viscosi... |
| ρl | 1039.87 | kg/m3 | 288.15 | Experim... |
| ρl | 1039.87 | kg/m3 | 288.15 | Densiti... |
| ρl | 1039.78 | kg/m3 | 288.15 | Apparen... |
| ρl | 1039.77 | kg/m3 | 288.15 | Apparen... |
| ρl | 1039.87 | kg/m3 | 288.15 | Volumet... |
| ρl | 1036.00 | kg/m3 | 293.00 | KDB |
| ρl | 1036.25 | kg/m3 | 293.15 | Densiti... |
| ρl | 1036.58 | kg/m3 | 293.15 | Excess ... |
| ρl | 1036.22 | kg/m3 | 293.15 | Volume ... |
| ρl | 1036.21 | kg/m3 | 293.15 | Volume ... |
| ρl | 1035.73 | kg/m3 | 293.15 | Volumet... |
| ρl | 1035.50 | kg/m3 | 293.15 | Viscosi... |
| ρl | 1036.15 | kg/m3 | 293.15 | Apparen... |
| ρl | 1036.16 | kg/m3 | 293.15 | Apparen... |
| ρl | 1036.13 | kg/m3 | 293.15 | Volume ... |
| ρl | 1036.57 | kg/m3 | 293.15 | Densiti... |
| ρl | 1036.30 | kg/m3 | 293.15 | Densiti... |
| ρl | 1037.22 | kg/m3 | 293.15 | Density... |
| ρl | 1036.30 | kg/m3 | 293.15 | Thermod... |
| ρl | 1036.17 | kg/m3 | 293.15 | Volume ... |
| ρl | 1036.25 | kg/m3 | 293.15 | Experim... |
| ρl | 1036.00 | kg/m3 | 293.15 | Thermod... |
| ρl | 1036.25 | kg/m3 | 293.15 | Volumet... |
| ρl | 1032.59 | kg/m3 | 298.15 | Densiti... |
| ρl | 1032.03 | kg/m3 | 298.15 | Volumet... |
| ρl | 1032.70 | kg/m3 | 298.15 | Thermod... |
| ρl | 1032.55 | kg/m3 | 298.15 | Excess ... |
| ρl | 1033.60 | kg/m3 | 298.15 | Excess ... |
| ρl | 1033.00 | kg/m3 | 298.15 | Thermod... |
| ρl | 1032.50 | kg/m3 | 298.15 | Densiti... |
| ρl | 1032.59 | kg/m3 | 298.15 | Volumet... |
| ρl | 1032.58 | kg/m3 | 298.15 | Densiti... |
| ρl | 1031.90 | kg/m3 | 298.15 | Isobari... |
| ρl | 1032.52 | kg/m3 | 298.15 | Volume ... |
| ρl | 1032.62 | kg/m3 | 298.15 | Thermod... |
| ρl | 1032.56 | kg/m3 | 298.15 | Experim... |
| ρl | 1032.48 | kg/m3 | 298.15 | Apparen... |
| ρl | 1032.86 | kg/m3 | 298.15 | Excess ... |
| ρl | 1032.30 | kg/m3 | 298.15 | Isobari... |
| ρl | 1032.48 | kg/m3 | 298.15 | Volume ... |
| ρl | 1032.56 | kg/m3 | 298.15 | Volume ... |
| ρl | 1032.86 | kg/m3 | 298.15 | Densiti... |
| ρl | 1032.49 | kg/m3 | 298.15 | Apparen... |
| ρl | 1032.69 | kg/m3 | 298.15 | Densiti... |
| ρl | 1032.55 | kg/m3 | 298.15 | Volume ... |
| ρl | 1029.00 | kg/m3 | 303.15 | Thermod... |
| ρl | 1028.84 | kg/m3 | 303.15 | Volume ... |
| ρl | 1029.10 | kg/m3 | 303.15 | Excess ... |
| ρl | 1028.80 | kg/m3 | 303.15 | Thermod... |
| ρl | 1029.64 | kg/m3 | 303.15 | Density... |
| ρl | 1028.78 | kg/m3 | 303.15 | Volume ... |
| ρl | 1028.85 | kg/m3 | 303.15 | Volume ... |
| ρl | 1028.88 | kg/m3 | 303.15 | Densiti... |
| ρl | 1028.77 | kg/m3 | 303.15 | Apparen... |
| ρl | 1028.88 | kg/m3 | 303.15 | Volumet... |
| ρl | 1028.78 | kg/m3 | 303.15 | Apparen... |
| ρl | 1028.83 | kg/m3 | 303.15 | Volume ... |
| ρl | 1029.15 | kg/m3 | 303.15 | Densiti... |
| ρl | 1028.31 | kg/m3 | 303.15 | Volumet... |
| ρl | 1028.10 | kg/m3 | 303.15 | Viscosi... |
| ρl | 1028.91 | kg/m3 | 303.15 | Thermod... |
| ρl | 1028.88 | kg/m3 | 303.15 | Densiti... |
| ρl | 1028.88 | kg/m3 | 303.15 | Experim... |
| ρl | 1029.20 | kg/m3 | 303.15 | Densiti... |
| ρl | 1028.89 | kg/m3 | 303.15 | Densiti... |
| ρl | 1025.09 | kg/m3 | 308.15 | Volume ... |
| ρl | 1026.15 | kg/m3 | 308.15 | Excess ... |
| ρl | 1025.20 | kg/m3 | 308.15 | Thermod... |
| ρl | 1025.09 | kg/m3 | 308.15 | Volume ... |
| ρl | 1025.30 | kg/m3 | 308.15 | Densiti... |
| ρl | 1025.05 | kg/m3 | 308.15 | Volume ... |
| ρl | 1025.13 | kg/m3 | 308.15 | Densiti... |
| ρl | 1026.15 | kg/m3 | 308.15 | Excess ... |
| ρl | 1025.14 | kg/m3 | 308.15 | Experim... |
| ρl | 1025.10 | kg/m3 | 308.15 | Volume ... |
| ρl | 1025.14 | kg/m3 | 308.15 | Volumet... |
| ρl | 1025.57 | kg/m3 | 308.15 | Densiti... |
| ρl | 1025.21 | kg/m3 | 308.15 | Densiti... |
| ρl | 1024.55 | kg/m3 | 308.15 | Volumet... |
| ρl | 1025.16 | kg/m3 | 308.15 | Thermod... |
| ρl | 1025.03 | kg/m3 | 308.15 | Apparen... |
| ρl | 1025.14 | kg/m3 | 308.15 | Densiti... |
| ρl | 1021.28 | kg/m3 | 313.15 | Volume ... |
| ρl | 1021.25 | kg/m3 | 313.15 | Apparen... |
| ρl | 1020.75 | kg/m3 | 313.15 | Volumet... |
| ρl | 1021.44 | kg/m3 | 313.15 | Densiti... |
| ρl | 1021.35 | kg/m3 | 313.15 | Volumet... |
| ρl | 1021.24 | kg/m3 | 313.15 | Apparen... |
| ρl | 1021.39 | kg/m3 | 313.15 | Thermod... |
| ρl | 1021.31 | kg/m3 | 313.15 | Volume ... |
| ρl | 1021.31 | kg/m3 | 313.15 | Volume ... |
| ρl | 1021.48 | kg/m3 | 313.15 | Excess ... |
| ρl | 1021.35 | kg/m3 | 313.15 | Experim... |
| ρl | 1021.35 | kg/m3 | 313.15 | Densiti... |
| ρl | 1021.35 | kg/m3 | 313.15 | Densiti... |
| ρl | 1021.98 | kg/m3 | 313.15 | Density... |
| ρl | 1021.50 | kg/m3 | 313.15 | Densiti... |
| ρl | 1020.60 | kg/m3 | 313.15 | Viscosi... |
| ρl | 1021.35 | kg/m3 | 313.15 | Densiti... |
| ρl | 1021.31 | kg/m3 | 313.15 | Volume ... |
| ρl | 1017.47 | kg/m3 | 318.15 | Volume ... |
| ρl | 1017.49 | kg/m3 | 318.15 | Volume ... |
| ρl | 1017.52 | kg/m3 | 318.15 | Densiti... |
| ρl | 1017.52 | kg/m3 | 318.15 | Densiti... |
| ρl | 1017.59 | kg/m3 | 318.15 | Densiti... |
| ρl | 1017.43 | kg/m3 | 318.15 | Apparen... |
| ρl | 1017.52 | kg/m3 | 318.15 | Volumet... |
| ρl | 1017.49 | kg/m3 | 318.15 | Volume ... |
| ρl | 1017.51 | kg/m3 | 318.15 | Densiti... |
| ρl | 1017.42 | kg/m3 | 318.15 | Apparen... |
| ρl | 1016.92 | kg/m3 | 318.15 | Volumet... |
| ρl | 1018.00 | kg/m3 | 318.15 | Densiti... |
| ρl | 1017.52 | kg/m3 | 318.15 | Experim... |
| ρl | 1017.57 | kg/m3 | 318.15 | Thermod... |
| ρl | 1013.66 | kg/m3 | 323.15 | Experim... |
| ρl | 1013.00 | kg/m3 | 323.15 | Viscosi... |
| ρl | 1013.68 | kg/m3 | 323.15 | Densiti... |
| ρl | 1014.00 | kg/m3 | 323.15 | Densiti... |
| ρl | 1013.72 | kg/m3 | 323.15 | Thermod... |
| ρl | 1013.66 | kg/m3 | 323.15 | Volumet... |
| ρl | 1013.66 | kg/m3 | 323.15 | Densiti... |
| ρl | 1013.74 | kg/m3 | 323.15 | Densiti... |
| ρl | 1013.66 | kg/m3 | 323.15 | Densiti... |
| ρl | 1014.25 | kg/m3 | 323.15 | Density... |
| ρl | 1009.78 | kg/m3 | 328.15 | Densiti... |
| ρl | 1009.75 | kg/m3 | 328.15 | Densiti... |
| ρl | 1009.71 | kg/m3 | 328.15 | Densiti... |
| ρl | 1010.20 | kg/m3 | 328.15 | Densiti... |
| ρl | 1009.75 | kg/m3 | 328.15 | Densiti... |
| ρl | 1005.30 | kg/m3 | 333.15 | Viscosi... |
| ρl | 1005.86 | kg/m3 | 333.15 | Densiti... |
| ρl | 1005.79 | kg/m3 | 333.15 | Densiti... |
| ρl | 1006.20 | kg/m3 | 333.15 | Densiti... |
| ρl | 1005.80 | kg/m3 | 333.15 | Densiti... |
| ρl | 1006.45 | kg/m3 | 333.15 | Density... |
| ρl | 998.57 | kg/m3 | 343.15 | Density... |
| ρl | 997.86 | kg/m3 | 343.15 | Densiti... |
| ρl | 997.70 | kg/m3 | 343.15 | Viscosi... |
| ρl | 990.62 | kg/m3 | 353.15 | Density... |
| ρl | 989.50 | kg/m3 | 353.15 | Viscosi... |
| ρl | 982.60 | kg/m3 | 363.15 | Density... |
| csound,fluid | 1510.60 | m/s | 298.15 | Volumet... |
| λ | [0.18; 0.21] | W/m×K | [283.15; 450.80] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.19 0.19 0.2 0.2 0.21 300 350 400 450 | ||||
| λ | 0.21 | W/m×K | 283.15 | Thermal... |
| λ | 0.20 | W/m×K | 299.10 | Density... |
| λ | 0.21 | W/m×K | 303.15 | Thermal... |
| λ | 0.20 | W/m×K | 313.60 | Density... |
| λ | 0.21 | W/m×K | 323.15 | Thermal... |
| λ | 0.20 | W/m×K | 332.90 | Density... |
| λ | 0.21 | W/m×K | 343.15 | Thermal... |
| λ | 0.19 | W/m×K | 352.30 | Density... |
| λ | 0.19 | W/m×K | 371.60 | Density... |
| λ | 0.19 | W/m×K | 391.10 | Density... |
| λ | 0.19 | W/m×K | 411.40 | Density... |
| λ | 0.19 | W/m×K | 430.40 | Density... |
| λ | 0.18 | W/m×K | 450.80 | Density... |
| vspec | [9.52e-04; 9.79e-04] | m3/kg | [273.15; 313.15] |
|
|
T(K) Specific Volume (m3/kg) 9.50e-4 9.55e-4 9.60e-4 9.65e-4 9.70e-4 9.75e-4 9.80e-4 280 290 300 310 | ||||
| vspec | 9.52e-04 | m3/kg | 273.15 | Volumet... |
| vspec | 9.53e-04 | m3/kg | 274.15 | Volumet... |
| vspec | 9.53e-04 | m3/kg | 275.15 | Volumet... |
| vspec | 9.54e-04 | m3/kg | 276.15 | Volumet... |
| vspec | 9.54e-04 | m3/kg | 277.15 | Volumet... |
| vspec | 9.55e-04 | m3/kg | 278.15 | Volumet... |
| vspec | 9.56e-04 | m3/kg | 279.15 | Volumet... |
| vspec | 9.56e-04 | m3/kg | 280.15 | Volumet... |
| vspec | 9.57e-04 | m3/kg | 281.15 | Volumet... |
| vspec | 9.58e-04 | m3/kg | 282.16 | Volumet... |
| vspec | 9.58e-04 | m3/kg | 283.16 | Volumet... |
| vspec | 9.59e-04 | m3/kg | 284.16 | Volumet... |
| vspec | 9.60e-04 | m3/kg | 285.16 | Volumet... |
| vspec | 9.60e-04 | m3/kg | 286.16 | Volumet... |
| vspec | 9.61e-04 | m3/kg | 287.16 | Volumet... |
| vspec | 9.62e-04 | m3/kg | 288.05 | Volumet... |
| vspec | 9.62e-04 | m3/kg | 288.16 | Volumet... |
| vspec | 9.62e-04 | m3/kg | 288.31 | Volumet... |
| vspec | 9.62e-04 | m3/kg | 288.34 | Volumet... |
| vspec | 9.62e-04 | m3/kg | 289.16 | Volumet... |
| vspec | 9.63e-04 | m3/kg | 290.15 | Volumet... |
| vspec | 9.64e-04 | m3/kg | 291.15 | Volumet... |
| vspec | 9.64e-04 | m3/kg | 292.15 | Volumet... |
| vspec | 9.65e-04 | m3/kg | 293.15 | Volumet... |
| vspec | 9.66e-04 | m3/kg | 294.15 | Volumet... |
| vspec | 9.66e-04 | m3/kg | 295.15 | Volumet... |
| vspec | 9.67e-04 | m3/kg | 296.16 | Volumet... |
| vspec | 9.68e-04 | m3/kg | 297.16 | Volumet... |
| vspec | 9.68e-04 | m3/kg | 298.16 | Volumet... |
| vspec | 9.69e-04 | m3/kg | 299.16 | Volumet... |
| vspec | 9.70e-04 | m3/kg | 300.16 | Volumet... |
| vspec | 9.70e-04 | m3/kg | 301.16 | Volumet... |
| vspec | 9.71e-04 | m3/kg | 302.16 | Volumet... |
| vspec | 9.72e-04 | m3/kg | 303.16 | Volumet... |
| vspec | 9.73e-04 | m3/kg | 304.15 | Volumet... |
| vspec | 9.73e-04 | m3/kg | 305.15 | Volumet... |
| vspec | 9.74e-04 | m3/kg | 306.15 | Volumet... |
| vspec | 9.75e-04 | m3/kg | 307.15 | Volumet... |
| vspec | 9.75e-04 | m3/kg | 308.15 | Volumet... |
| vspec | 9.76e-04 | m3/kg | 309.15 | Volumet... |
| vspec | 9.77e-04 | m3/kg | 310.15 | Volumet... |
| vspec | 9.78e-04 | m3/kg | 311.15 | Volumet... |
| vspec | 9.78e-04 | m3/kg | 312.15 | Volumet... |
| vspec | 9.79e-04 | m3/kg | 313.15 | Volumet... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 98.00 | 1032.56 |
| 303.15 | 98.00 | 1028.87 |
| 312.98 | 98.00 | 1022.16 |
| 335.78 | 98.00 | 1005.31 |
| 364.39 | 98.00 | 981.63 |
| 394.95 | 98.00 | 953.22 |
| 423.51 | 98.00 | 926.76 |
| 452.17 | 98.00 | 900.36 |
| 298.15 | 49030.00 | 1055.29 |
| 303.15 | 49030.00 | 1052.03 |
| 313.00 | 49030.00 | 1046.22 |
| 335.80 | 49030.00 | 1029.3 |
| 364.66 | 49030.00 | 1007.36 |
| 395.11 | 49030.00 | 982.98 |
| 423.62 | 49030.00 | 959.18 |
| 452.10 | 49030.00 | 934.51 |
| 298.15 | 98060.00 | 1072.94 |
| 303.15 | 98060.00 | 1070.79 |
| 313.05 | 98060.00 | 1065.24 |
| 335.76 | 98060.00 | 1050.34 |
| 364.83 | 98060.00 | 1031.15 |
| 395.17 | 98060.00 | 1010.62 |
| 423.90 | 98060.00 | 989.94 |
| 452.14 | 98060.00 | 965.53 |
| 298.15 | 147100.00 | 1088.48 |
| 303.15 | 147100.00 | 1086.25 |
| 313.03 | 147100.00 | 1081.67 |
| 335.78 | 147100.00 | 1068.19 |
| 364.87 | 147100.00 | 1051.61 |
| 395.38 | 147100.00 | 1033.92 |
| 423.97 | 147100.00 | 1016.34 |
| 452.19 | 147100.00 | 996.01 |
| 298.15 | 196130.00 | 1104.32 |
| 303.15 | 196130.00 | 1101.4 |
| 313.04 | 196130.00 | 1095.69 |
| 335.80 | 196130.00 | 1082.92 |
| 365.00 | 196130.00 | 1067.32 |
| 395.57 | 196130.00 | 1051.9 |
| 424.05 | 196130.00 | 1038.38 |
| 452.18 | 196130.00 | 1022.83 |
| 298.15 | 245160.00 | 1115.28 |
| 303.15 | 245160.00 | 1112.65 |
| 313.03 | 245160.00 | 1107.51 |
| 336.01 | 245160.00 | 1095.8 |
| 364.99 | 245160.00 | 1081.56 |
| 395.68 | 245160.00 | 1067.12 |
| 424.30 | 245160.00 | 1054.25 |
| 452.07 | 245160.00 | 1042.31 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 1047.1 |
| 278.15 | 1000.00 | 1047.3 |
| 278.15 | 5000.00 | 1049.2 |
| 278.15 | 10000.00 | 1051.2 |
| 278.15 | 15000.00 | 1053.4 |
| 278.15 | 20000.00 | 1055.5 |
| 278.15 | 25000.00 | 1057.6 |
| 278.15 | 30000.00 | 1059.6 |
| 278.15 | 35000.00 | 1061.6 |
| 278.15 | 40000.00 | 1063.6 |
| 278.15 | 45000.00 | 1065.6 |
| 278.15 | 50000.00 | 1067.5 |
| 278.15 | 55000.00 | 1069.3 |
| 278.15 | 60000.00 | 1071.4 |
| 288.15 | 100.00 | 1039.9 |
| 288.15 | 1000.00 | 1040.2 |
| 288.15 | 5000.00 | 1042.1 |
| 288.15 | 10000.00 | 1044.4 |
| 288.15 | 15000.00 | 1046.7 |
| 288.15 | 20000.00 | 1048.9 |
| 288.15 | 25000.00 | 1051.1 |
| 288.15 | 30000.00 | 1053.2 |
| 288.15 | 35000.00 | 1055.4 |
| 288.15 | 40000.00 | 1057.4 |
| 288.15 | 45000.00 | 1059.4 |
| 288.15 | 50000.00 | 1061.4 |
| 288.15 | 55000.00 | 1063.4 |
| 288.15 | 60000.00 | 1065.3 |
| 298.15 | 100.00 | 1032.5 |
| 298.15 | 1000.00 | 1032.9 |
| 298.15 | 5000.00 | 1034.8 |
| 298.15 | 10000.00 | 1037.2 |
| 298.15 | 15000.00 | 1039.6 |
| 298.15 | 20000.00 | 1041.9 |
| 298.15 | 25000.00 | 1044.1 |
| 298.15 | 30000.00 | 1046.3 |
| 298.15 | 35000.00 | 1048.4 |
| 298.15 | 40000.00 | 1050.6 |
| 298.15 | 45000.00 | 1052.5 |
| 298.15 | 50000.00 | 1054.6 |
| 298.15 | 55000.00 | 1056.6 |
| 298.15 | 60000.00 | 1058.5 |
| 308.15 | 100.00 | 1025.3 |
| 308.15 | 1000.00 | 1025.5 |
| 308.15 | 5000.00 | 1027.5 |
| 308.15 | 10000.00 | 1030.1 |
| 308.15 | 15000.00 | 1032.5 |
| 308.15 | 20000.00 | 1034.9 |
| 308.15 | 25000.00 | 1037.2 |
| 308.15 | 30000.00 | 1039.5 |
| 308.15 | 35000.00 | 1041.6 |
| 308.15 | 40000.00 | 1043.8 |
| 308.15 | 45000.00 | 1046.0 |
| 308.15 | 50000.00 | 1048.1 |
| 308.15 | 55000.00 | 1050.1 |
| 308.15 | 60000.00 | 1052.2 |
| 318.15 | 100.00 | 1017.7 |
| 318.15 | 1000.00 | 1018.0 |
| 318.15 | 5000.00 | 1020.2 |
| 318.15 | 10000.00 | 1022.8 |
| 318.15 | 15000.00 | 1025.4 |
| 318.15 | 20000.00 | 1027.9 |
| 318.15 | 25000.00 | 1030.3 |
| 318.15 | 30000.00 | 1032.7 |
| 318.15 | 35000.00 | 1035.0 |
| 318.15 | 40000.00 | 1037.2 |
| 318.15 | 45000.00 | 1039.4 |
| 318.15 | 50000.00 | 1041.5 |
| 318.15 | 55000.00 | 1043.6 |
| 318.15 | 60000.00 | 1045.7 |
| 328.15 | 100.00 | 1010.0 |
| 328.15 | 1000.00 | 1010.3 |
| 328.15 | 5000.00 | 1012.7 |
| 328.15 | 10000.00 | 1015.4 |
| 328.15 | 15000.00 | 1018.0 |
| 328.15 | 20000.00 | 1020.6 |
| 328.15 | 25000.00 | 1023.1 |
| 328.15 | 30000.00 | 1025.6 |
| 328.15 | 35000.00 | 1027.9 |
| 328.15 | 40000.00 | 1030.3 |
| 328.15 | 45000.00 | 1032.5 |
| 328.15 | 50000.00 | 1034.7 |
| 328.15 | 55000.00 | 1036.9 |
| 328.15 | 60000.00 | 1039.0 |
| 338.15 | 100.00 | 1002.2 |
| 338.15 | 1000.00 | 1002.4 |
| 338.15 | 5000.00 | 1004.8 |
| 338.15 | 10000.00 | 1007.6 |
| 338.15 | 15000.00 | 1010.4 |
| 338.15 | 20000.00 | 1013.0 |
| 338.15 | 25000.00 | 1015.6 |
| 338.15 | 30000.00 | 1018.2 |
| 338.15 | 35000.00 | 1020.7 |
| 338.15 | 40000.00 | 1023.2 |
| 338.15 | 45000.00 | 1025.5 |
| 338.15 | 50000.00 | 1027.9 |
| 338.15 | 55000.00 | 1030.2 |
| 338.15 | 60000.00 | 1032.4 |
| 348.15 | 100.00 | 994.1 |
| 348.15 | 1000.00 | 994.5 |
| 348.15 | 5000.00 | 996.9 |
| 348.15 | 10000.00 | 999.9 |
| 348.15 | 15000.00 | 1002.8 |
| 348.15 | 20000.00 | 1005.5 |
| 348.15 | 25000.00 | 1008.2 |
| 348.15 | 30000.00 | 1010.9 |
| 348.15 | 35000.00 | 1013.4 |
| 348.15 | 40000.00 | 1016.0 |
| 348.15 | 45000.00 | 1018.4 |
| 348.15 | 50000.00 | 1020.9 |
| 348.15 | 55000.00 | 1023.2 |
| 348.15 | 60000.00 | 1025.6 |
| 358.15 | 100.00 | 985.8 |
| 358.15 | 1000.00 | 986.2 |
| 358.15 | 5000.00 | 988.8 |
| 358.15 | 10000.00 | 991.9 |
| 358.15 | 15000.00 | 995.0 |
| 358.15 | 20000.00 | 997.8 |
| 358.15 | 25000.00 | 1000.6 |
| 358.15 | 30000.00 | 1003.4 |
| 358.15 | 35000.00 | 1006.0 |
| 358.15 | 40000.00 | 1008.5 |
| 358.15 | 45000.00 | 1011.2 |
| 358.15 | 50000.00 | 1013.6 |
| 358.15 | 55000.00 | 1016.1 |
| 358.15 | 60000.00 | 1018.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 272.69 | 5240.00 | 1054.19 |
| 272.68 | 10290.00 | 1056.38 |
| 272.68 | 15270.00 | 1058.53 |
| 272.72 | 20360.00 | 1060.64 |
| 272.73 | 30580.00 | 1064.73 |
| 272.73 | 50680.00 | 1072.45 |
| 272.77 | 71000.00 | 1079.68 |
| 272.74 | 91400.00 | 1086.61 |
| 272.76 | 50810.00 | 1072.51 |
| 272.78 | 15370.00 | 1058.52 |
| 293.18 | 5180.00 | 1039.1 |
| 293.18 | 10100.00 | 1041.39 |
| 293.18 | 15210.00 | 1043.73 |
| 293.18 | 20190.00 | 1045.96 |
| 293.18 | 30240.00 | 1050.35 |
| 293.18 | 50550.00 | 1058.66 |
| 293.18 | 70760.00 | 1066.35 |
| 293.18 | 90990.00 | 1073.55 |
| 293.18 | 50680.00 | 1058.72 |
| 293.18 | 15310.00 | 1043.77 |
| 313.12 | 5120.00 | 1024.21 |
| 313.13 | 10070.00 | 1026.73 |
| 313.13 | 15110.00 | 1029.21 |
| 313.12 | 20290.00 | 1031.71 |
| 313.13 | 30290.00 | 1036.38 |
| 313.12 | 50710.00 | 1045.31 |
| 313.12 | 71030.00 | 1053.5 |
| 313.12 | 91240.00 | 1061.08 |
| 313.12 | 50990.00 | 1045.42 |
| 313.12 | 15580.00 | 1029.43 |
| 352.99 | 5010.00 | 993.23 |
| 353.00 | 10100.00 | 996.26 |
| 353.00 | 15280.00 | 999.29 |
| 352.99 | 20210.00 | 1002.06 |
| 352.99 | 30360.00 | 1007.57 |
| 353.00 | 50610.00 | 1017.74 |
| 352.99 | 70750.00 | 1027.01 |
| 352.99 | 91060.00 | 1035.61 |
| 352.99 | 50620.00 | 1017.76 |
| 352.99 | 15390.00 | 999.36 |
| 392.94 | 5080.00 | 959.54 |
| 392.94 | 10090.00 | 963.15 |
| 392.95 | 15190.00 | 966.67 |
| 392.96 | 20230.00 | 970.02 |
| 392.97 | 30430.00 | 976.54 |
| 392.95 | 50730.00 | 988.44 |
| 392.94 | 70890.00 | 999.07 |
| 392.94 | 90950.00 | 1008.71 |
| 392.95 | 50820.00 | 988.49 |
| 392.96 | 15180.00 | 966.75 |
| 283.21 | 5190.00 | 1046.44 |
| 283.19 | 10060.00 | 1048.67 |
| 283.17 | 15100.00 | 1050.92 |
| 283.17 | 20200.00 | 1053.13 |
| 283.17 | 30530.00 | 1057.48 |
| 283.18 | 50550.00 | 1065.43 |
| 283.19 | 70990.00 | 1072.96 |
| 283.18 | 91270.00 | 1079.99 |
| 283.18 | 50490.00 | 1065.4 |
| 283.17 | 15140.00 | 1050.94 |
| 298.12 | 5090.00 | 1035.37 |
| 298.12 | 10070.00 | 1037.74 |
| 298.12 | 15240.00 | 1040.15 |
| 298.12 | 20170.00 | 1042.4 |
| 298.12 | 30300.00 | 1046.89 |
| 298.12 | 50590.00 | 1055.32 |
| 298.11 | 70930.00 | 1063.17 |
| 298.12 | 91050.00 | 1070.41 |
| 298.12 | 50650.00 | 1055.35 |
| 298.12 | 15160.00 | 1040.11 |
| 333.05 | 5260.00 | 1009.12 |
| 333.05 | 10050.00 | 1011.76 |
| 333.05 | 15120.00 | 1014.46 |
| 333.05 | 20250.00 | 1017.1 |
| 333.05 | 30400.00 | 1022.19 |
| 333.05 | 50610.00 | 1031.67 |
| 333.06 | 70910.00 | 1040.39 |
| 333.06 | 91130.00 | 1048.43 |
| 333.06 | 51080.00 | 1031.87 |
| 333.06 | 15210.00 | 1014.48 |
| 373.34 | 10320.00 | 980.11 |
| 373.34 | 15330.00 | 983.26 |
| 373.34 | 20360.00 | 986.4 |
| 373.34 | 30530.00 | 992.32 |
| 373.34 | 50610.00 | 1003.25 |
| 373.34 | 70990.00 | 1013.23 |
| 373.35 | 91190.00 | 1022.41 |
| 373.35 | 50860.00 | 1003.34 |
| 373.35 | 15540.00 | 983.34 |
| 373.35 | 5160.00 | 976.65 |
| 313.03 | 5190.00 | 1024.2 |
| 313.03 | 10100.00 | 1026.69 |
| 313.03 | 15280.00 | 1029.25 |
| 313.03 | 20240.00 | 1031.64 |
| 313.03 | 30440.00 | 1036.4 |
| 313.03 | 50660.00 | 1045.24 |
| 313.03 | 70960.00 | 1053.42 |
| 313.03 | 91090.00 | 1061.0 |
| 313.03 | 50710.00 | 1045.28 |
| 313.03 | 15210.00 | 1029.23 |
| Reference | ||
Speed of sound, m/s
Operational condition: Frequency, MHz = 8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 99.00 | 1494.429 |
| 303.15 | 5091.00 | 1513.504 |
| 303.15 | 10060.00 | 1532.024 |
| 303.15 | 15098.00 | 1550.199 |
| 303.15 | 20084.00 | 1567.713 |
| 303.15 | 25068.00 | 1584.711 |
| 303.15 | 30167.00 | 1601.587 |
| 313.15 | 99.00 | 1465.858 |
| 313.15 | 5014.00 | 1485.499 |
| 313.15 | 10053.00 | 1504.824 |
| 313.15 | 15011.00 | 1523.212 |
| 313.15 | 20095.00 | 1541.536 |
| 313.15 | 25202.00 | 1559.357 |
| 313.15 | 30222.00 | 1576.498 |
| 333.15 | 100.00 | 1408.863 |
| 333.15 | 5039.00 | 1429.721 |
| 333.15 | 10054.00 | 1450.066 |
| 333.15 | 15107.00 | 1469.848 |
| 333.15 | 20131.00 | 1488.963 |
| 333.15 | 25131.00 | 1507.384 |
| 333.15 | 30024.00 | 1524.874 |
| 353.15 | 99.00 | 1350.887 |
| 353.15 | 5042.00 | 1373.03 |
| 353.15 | 10055.00 | 1394.56 |
| 353.15 | 15135.00 | 1415.607 |
| 353.15 | 20093.00 | 1435.461 |
| 353.15 | 25086.00 | 1454.828 |
| 353.15 | 30207.00 | 1474.064 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.40; 208.10] | kPa | [335.73; 485.20] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.64972e+01 | |||
| Coefficient B | -4.64181e+03 | |||
| Coefficient C | -6.92380e+01 | |||
| Temperature range, min. | 335.73 | |||
| Temperature range, max. | 485.20 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 0.40 | kPa | 335.73 | Calculated Property |
| Pvap | 1.11 | kPa | 352.34 | Calculated Property |
| Pvap | 2.74 | kPa | 368.95 | Calculated Property |
| Pvap | 6.19 | kPa | 385.55 | Calculated Property |
| Pvap | 12.87 | kPa | 402.16 | Calculated Property |
| Pvap | 24.96 | kPa | 418.77 | Calculated Property |
| Pvap | 45.58 | kPa | 435.38 | Calculated Property |
| Pvap | 79.01 | kPa | 451.98 | Calculated Property |
| Pvap | 130.83 | kPa | 468.59 | Calculated Property |
| Pvap | 208.10 | kPa | 485.20 | Calculated Property |
| Pvap | [8.87e-08; 6165.74] | kPa | [213.15; 626.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.23565e+02 | |||
| Coefficient B | -1.60975e+04 | |||
| Coefficient C | -3.08431e+01 | |||
| Coefficient D | 2.42067e-05 | |||
| Temperature range, min. | 213.15 | |||
| Temperature range, max. | 626.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 600 | ||||
| Pvap | 8.87e-08 | kPa | 213.15 | Calculated Property |
| Pvap | 2.36e-04 | kPa | 259.02 | Calculated Property |
| Pvap | 0.03 | kPa | 304.89 | Calculated Property |
| Pvap | 0.91 | kPa | 350.77 | Calculated Property |
| Pvap | 9.52 | kPa | 396.64 | Calculated Property |
| Pvap | 55.54 | kPa | 442.51 | Calculated Property |
| Pvap | 227.08 | kPa | 488.38 | Calculated Property |
| Pvap | 751.49 | kPa | 534.26 | Calculated Property |
| Pvap | 2211.30 | kPa | 580.13 | Calculated Property |
| Pvap | 6165.74 | kPa | 626.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Propylene Glycol.
Mixtures
- Propylene Glycol + Water
- Propylene Glycol + Propanoic acid, 2-hydroxy-, ethyl ester
- Propylene Glycol + Isopropyl Alcohol
- Propylene Glycol + Isopropyl Alcohol + Water
- Propylene Glycol + sodium iodide + Methyl Alcohol
- Propylene Glycol + Methyl Alcohol
- Propylene Glycol + Ethanol, 2-methoxy-
- Propylene Glycol + lithium chloride + Water
- lithium bromide + Propylene Glycol + Water
- Propylene Glycol + Tromethamine + Water
- Propylene Glycol + Pyridine
- 1-Propanol + Propylene Glycol
- Propylene Glycol + 1-Hexanol
- Propylene Glycol + 1-Octanol
- Magnesium chloride + Propylene Glycol + Water
- 1,3-Propanediol + Propylene Glycol
- Propylene Glycol + Pyridine, 3-(1-methyl-2-pyrrolidinyl)-, (S)-
- 2-Pyrrolidinone + Propylene Glycol
- Propylene Glycol + Acetonitrile
- Propylene Glycol + Propylamine
Find more mixtures with Propylene Glycol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Vapor liquid equilibrium in systems (water + organic solvent + salt) at low water concentrations but high ratios of salt to water: experimental results and modeling
- Thermodynamic study of the solubility of ibuprofen and naproxen in some ethanol + propylene glycol mixtures
- Methane and carbon dioxide solubility in 1,2-propylene glycol at temperatures ranging from 303 to 423 K and pressures up to 12 MPa
- Thermodynamic analysis of the solubility of ketoprofen in some propylene glycol + water cosolvent mixtures
- Thermodynamic studies of fluphenazine decanoate solubility in propylene glycol + water mixtures and correlation with the Jouyban Acree model
- Solution thermodynamics of indomethacin in propylene glycol + water mixtures
- Liquid phase behavior of hexafluorophosphate ionic liquids with polyhydric alcohols
- Solubility of sulfamethizole in some propylene glycol + water mixtures at several temperatures
- Solubility of sulfapyridine in propylene glycol + water mixtures and correlation with the Jouyban Acree model
- Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
- Measurement and correlation of the solubility of florfenicol in binary 1,2-propanediol + water mixtures from 293.15 K to 316.25 K
- Solubility of daidzein in propylene glycol plus water cosolvent mixtures
- Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
- Phase behavior of imidazolium and phosphonium tetrafluoroborates with dihydroxy alcohols
- Vapor-liquid equilibrium for propylene glycols binary systems: Experimental data and regression
- Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
- Densities, surface tensions, and isobaric vapor-liquid equilibria for the mixtures of 2-propanol, water, and 1,2-propanediol
- Excess volumes and excess heat capacities of {1,2- alkanediol + methanol} mixtures and ionic volumes in these systems
- Volumetric, ultrasonic and spectroscopic (FT-IR) studies for the binary mixtures of imidazolium based ILs with 1,2-propanediol
- Density and viscosity of propylene glycol at high temperatures and high pressures
- Solubility evaluation and thermodynamic modeling of beta-lapachone in water and ten organic solvents at different temperatures
- Measurement and correlation of excess molar enthalpy for(1,2-propanediol, or 1,3-propanediol, or 1,4-butanediol + water) at the temperatures (298.15, 323.15, and 343.15) K
- Partial molar volumes of organic solutes in water. XIV. Polyhydric alcohols derived from ethane and propane at temperatures T = 298 K to T = 573 K and at pressures up to 30 MPa
- Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
- Densities and volumetric properties of (formamide + ethanol, or 1-propanol, or 1,2-ethanediol, or 1,2-propanediol) mixtures at temperatures between 293.15 K and 318.15 K
- Volumetric and compressibility properties of liquid water as a solute in glycolic, propylene carbonate, and tetramethylurea solutions at T = 298.15 K
- Excess molar volume and viscosity deviation for binary mixtures of polyethylene glycol dimethyl ether 250 with 1,2-alkanediols (C3 C6) at T = (293.15 to 323.15) K
- Vapour pressures, densities, and viscosities of the aqueous solutions containing (triethylene glycol or propylene glycol) and (LiCl or LiBr)
- Experimental study of the excess molar volume of ternary mixtures containing {water + (1,2-propanediol, or 1,3-propanediol, or 1,2-butanediol, or 1,3-butanediol, or 1,4-butanediol, or 2,3-butanediol) + electrolytes} at a temperature of 298.15 K and atmospheric pressure
- Molar heat capacities of some aqueous 2-amino-2-hydroxymethyl-1,3-propanediol + glycol systems
- (Liquid + liquid) equilibrium data for the system (propylene glycol + water + tetraoctyl ammonium 2-methyl-1-naphthoate)
- Phase diagrams for (water + 1, 2-butanediol or 1, 2-propanediol + 2-ethyl-1-hexanol) systems: Experimental data and UNIQUAC
- Experimental determination and modeling of excess molar volumes, viscosities and refractive indices of the binary systems (pyridine + 1-propanol, + 1,2-propanediol, + 1,3-propanediol, and + glycerol). New UNIFAC-VISCO parameters determination
- Densities, viscosities, and refractive indices of the binary systems (PEG200 + 1,2-propanediol, +1,3-propanediol) and (PEG400 + 1,2-propanediol, +1,3-propanediol) at (288.15 to 333.15) K and atmospheric pressure: Measurements and modeling
- PqT measurements and derived properties of liquid 1,2-alkanediols
- Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
- Thermophysical characterization of aqueous ternary system containing n-tris-[hydroxymethyl]methyl-3-amino propanesulfonic acid and glycol (PG or DPG or TPG)
- Isobaric specific heat capacity of typical lithium chloride liquid desiccants using scanning calorimetry
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
- Thermal conductivity of dry anatase and rutile nano-powders and ethylene and propylene glycol-based TiO2 nanofluids
- Liquid extraction of polyhydric alcohols from water using [A336][SCN] as a solvent
- Solubility of rosuvastatin calcium in different neat solvents at different temperatures
- Excess properties and isobaric (vapor + liquid) equilibrium at sub-atmospheric pressures of binary (1,2-propanediol + 1,3-propanediol) system: Measurement and modelling
- Equilibrium solubility of sodium 2,4-diaminobenzene sulfonate in liquid mixtures (methanol + water, isopropanol + water, and 1,2-propanediol + water) from 273.15 K to 323.15 K
- Solubility and thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
- Speed of sound in saturated aliphatic alcohols (propan-2-ol, butan-2-ol, and 2-methylpropan-1-ol) and alkanediols (ethane-1,2-diol, propane-1,2- and -1,3-diol) at temperature between 253.15 K and 353.15 K and pressures up to 30 MPa
- Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
- Determination and correlation of solubility and thermodynamics of mixing of 4-aminobutyric acid in mono-solvents and binary solvent mixtures
- Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of 2-pyrrolidone with isomeric propanediols at temperatures from 303.15 K to 323.15 K
- Thermodynamic and transport properties of acetonitrile + alkanediols liquid mixtures at different temperatures, experimental measurements and modeling
- Equilibrium solubility, dissolution thermodynamics and preferential solvation of adenosine in aqueous solutions of N,N-dimethylformamide, N-methyl-2-pyrrolidone, dimethylsulfoxide and propylene glycol
- Potential heat transfer enhancement of functionalized graphene nanoplatelet dispersions in a propylene glycol-water mixture. Thermophysical profile
- Solubility modelling and preferential solvation of adenine in solvent mixtures of (N,N-dimethylformamide, N-methyl pyrrolidone, propylene glycol and dimethyl sulfoxide) plus water
- Measurement and correlation of the (p, rho, T) behavior of liquid propylene glycol at temperatures from (272.7 to 393.0) K and pressures up to 91.4 MPa
- Thermodynamic solubility modeling, solvent effect and preferential solvation of curcumin in aqueous co-solvent mixtures of ethanol, n-propanol, isopropanol and propylene glycol
- Solubility of CO2 in methanol, ethanol, 1,2-propanediol and glycerol from 283.15 K to 373.15 K and up to 6.0 MPa
- Enthalpies of solution of l-threonine in aqueous alcohol solutions
- Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
- Enthalpies of dilution of formamide in aqueous alcohol solutions at 298.15K
- Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
- DSC determination of partial ternary phase diagrams of methanol/sodium chloride/water and propylene glycol/sodium chloride/water and their applications for synthesized diagrams
- Heat Capacity of Several Mixed-Solvent Desiccants Containing Glycol + Water + MgCl2
- Molar heat capacity of several aqueous solutions of n-[tris(hydroxymethyl)methyl-3-amino]- propanesulfonic acid (TAPS) + glycol
- Thermodynamic study on some alkanediol solutions: measurement and molecular modeling
- Experimental measurements and modelling of volumetric properties, refractive index and viscosity of selected binary systems with butyl lactate at 288.15 to 323.15 K and atmospheric pressure. New UNIFAC-VISCO interaction parameters.
- Solubility and dissolution thermodynamics of N-(4-chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide in PG + water cosolvent mixtures at (298.15 to 338.15) K
- Isobaric Vapor Liquid Equilibria for Binary Systems of Diethyl Carbonate + Propylene Carbonate, Diethyl Carbonate + Propylene Glycol, and Ethanol + Propylene Carbonate at 101.3 kPa
- Solubility and Saturation Apparent Volume of Propranolol Hydrochloride in Some Binary Aqueous Cosolvent Mixtures at 298.15 K
- Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
- Solubility of Hydrogen Sulfide in Ethanediol, 1,2-Propanediol, 1-Propanol, and 2-Propanol: Experimental Measurement and Modeling
- Apparent Molar Volumes and Isentropic Compressibilities of Tetraalkylammonium Bromides in Aqueous Propane-1,2-diol. An Attempt to Design Hydraulic Liquids
- Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
- Solubility of Etoricoxib in Aqueous Solutions of Glycerin, Methanol, Polyethylene Glycols 200, 400, 600, and Propylene Glycol at 298.2 K
- Solubility and Modeling of Hesperidin in Cosolvent Mixtures of Ethanol, Isopropanol, Propylene Glycol, and n-Propanol + Water
- Density of Working Liquids for Diffusion Vacuum Pumps
- Viscosities, Densities, and Refractive Indices of Aqueous Propane-1,3-diol
- Thermophysical Properties of Ternary Systems Potassium Formate + Propylene Glycol/Glycerol + Water
- Solubility Determination and Modeling for Artesunate in Binary Solvent Mixtures of Methanol, Ethanol, Isopropanol, and Propylene Glycol + Water
- Experimental Solubility and Density Functional Theory Studies of Deferasirox in Binary Solvent Mixtures: Performance of Polarizable Continuum Model and Jouyban-Acree Model
- Measurement and Correlation of the Solubility of Palmatine Chloride in Four Different Binary Solvent Systems at (283.15-328.15) K
- Phase Equilibrium Involving Xylose, Water, and Ethylene Glycol or 1,2-Propylene Glycol at Different Temperatures
- Solubility of Bifonazole in Four Binary Solvent Mixtures: Experimental Measurement and Thermodynamic Modeling
- Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
- Densities, Dynamic Viscosities, Speeds of Sound, and Relative Permittivities for Water + Alkanediols (Propane-1,2- and -1,3-diol and Butane-1,2-, -1,3-, -1,4-, and -2,3-Diol) at Different Temperatures
- Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
- Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
- Solubility of Valdecoxib in the Presence of Glycerol, Propylene Glycol, and Poly(ethylene glycol) 400 at (298.15, 303.15, and 308.15) K
- Solubility of Rofecoxib in the Presence of Aqueous Solutions of Glycerol, Propylene Glycol, Ethanol, Span 20, Tween 80, and Sodium Lauryl Sulfate at (298.15, 303.15, and 308.15) K
- Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
- Solubility of 1H-1,2,4-Triazole in Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, Ethyl Formate, Methyl Acetate, Ethyl Acetate, and Butyl Acetate at (283 to 363) K
- Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
- Phase Equilibrium and Physical Properties for the Purification of Propylene Carbonate (PC) and y-Butyrolactone (GBL)
- Solubility of Dimethyl Fumarate in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Water from (289.95 to 347.15) K
- Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
- Solubility of Phenothiazine in Water, Ethanol, and Propylene Glycol at (298.2 to 338.2) K and Their Binary and Ternary Mixtures at 298.2 K
- Solubility of 3-Ethyl-5-methyl-(4RS)-2-((2-aminoethoxy)methyl)-4-(2-chlorophenyl)-1,4-dihydro-6-methyl-3,5-pyridinedicarboxylate Monobenzenesulfonate (Amlodipine Besylate) in Ethanol + Water and Propane-1,2-diol + Water Mixtures at Various Temperatures
- Solubility of Clonazepam and Diazepam in Polyethylene Glycol 200, Propylene Glycol, N-Methyl Pyrrolidone, Ethanol, and Water at (298.2 to 318.2) K and in Binary and Ternary Mixtures of Polyethylene Glycol 200, Propylene Glycol, and Water at 298.2 K
- Solubility, Density, Refractive Index, and Viscosity for the Polyhydric Alcohol + CsBr + H2O Ternary Systems at Different Temperatures
- Solid Liquid Equilibria of 1-Ethyl-3-methylimidazolium Hexafluorophosphate + Polyols
- Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa
- Vapor Liquid Equilibrium for Ternary and Binary Mixtures of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa
- Heat Capacities of Four Promising Alternatives to Lithium Bromide Aqueous Solution in Absorption Refrigerators
- Solubilities of Carbon Dioxide in Eutectic Mixtures of Choline Chloride and Dihydric Alcohols
- Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
- Measurement and Correlation of Tadalafil Solubility in Five Pure Solvents at (298.15 to 333.15) K
- Solubility of Metoclopramide Hydrochloride in Six Green Solvents at (298.15 to 338.15) K
- Solubility of Bioactive Compound Hesperidin in Six Pure Solvents at (298.15 to 333.15) K
- Solubility of (2Z)-N-Cyclohexyl-2-(3-hydroxybenzylidine) Hydrazine Carbothioamide in Different Pure Solvents at (298.15 to 338.15) K
- Solubility of N-(4-Chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide (Isoniazid Analogue) in Five Pure Solvents at (298.15 to 338.15) K
- Correlation of Solubility of Bioactive Compound Reserpine in Eight Green Solvents at (298.15 to 338.15) K
- Measurement, Correlation, and Thermodynamics of Solubility of Isatin in Nine Different Green Solvents at (298.15 to 338.15) K
- Isobaric Vapor Liquid Equilibrium for Two Binary Systems{Propane-1,2-diol + Ethane-1,2-diol and Propane-1,2-diol + Butane-1,2-diol} at p = (10.0, 20.0, and 40.0) kPa
- Solubilities of 2-Methyl-1,4-naphthoquinone in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (293.15 to 337.92) K
- Study of the Acoustic and Thermodynamic Properties of 1,2- and 1,3-Propanediol by Means of High-Pressure Speed of Sound Measurements at Temperatures from (293 to 318) K and Pressures up to 101 MPa
- Densities and Excess Molar Volumes for Binary Mixtures of 1,4-Butanediol + 1,2-Propanediol, + 1,3-Propanediol, and + Ethane-1,2-diol from (293.15 to 328.15) K
- Solubility of Acetylsalicylic Acid in Ethanol, Acetone, Propylene Glycol, and 2-Propanol
- Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
- Solubilities of Menadione Sodium Bisulfite in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (297.67 to 337.76) K
- Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary and Ternary Liquid Mixtures of Methanol (1) + Ethanol (2) + 1,2-Propanediol (3) at P = 81.5 kPa
- Solubilities of Isonicotinic Acid in (Methanol, Ethanol, 1-Propanol, 2-Propanol, and 1,2-Propanediol, Respectively) from (289.65 to 358.75) K
- Solubility of Lamotrigine, Diazepam, Clonazepam, and Phenobarbital in Propylene Glycol + Water Mixtures at 298.15 K
- Solubility of 7-Chloro-2-methylamino-5-phenyl-3H-1,4-benzodiazepine-4-oxide, 7-Chloro-1,3-dihydro-1-methyl-5-phenyl-2H-1,4-benzodiazepin-2-one, and 7-Chloro-5-(2-chlorophenyl)-3-hydroxy-1,3-dihydro-1,4-benzodiazepin-2-one in (Propane-1,2-diol + Water) at a Temperature of 303.2 K
- Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
- Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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