- InChI
- InChI=1S/C12H26O/c1-2-3-4-5-6-7-8-9-10-11-12-13/h13H,2-12H2,1H3
- InChI Key
- LQZZUXJYWNFBMV-UHFFFAOYSA-N
- Formula
- C12H26O
- SMILES
- CCCCCCCCCCCCO
- Molecular Weight1
- 186.33
- CAS
- 112-53-8
- Other Names
-
- 1-Dodecyl Alcohol
- 1-Hydroxydodecane
- Adol 10
- Adol 12
- Alcohol C-12
- Alfol 12
- CO-1214
- CO-1214N
- CO-1214S
- Cachalot l-50
- Cachalot l-90
- Conol 20P
- Conol 20PP
- DUODECYL ALCOHOL
- Dodecan-1-ol
- Dodecanol
- Dodecanol-1
- Dodecyl alcohol
- Dytol J-68
- Epal 12
- Hainol 12SS
- Hydroxydodecane
- Karukoru 20
- LAURIC ALCOHOL
- Laurinic alcohol
- Lauryl 24
- Lauryl alcohol
- Lorol 11
- Lorol 5
- Lorol 7
- Lorol C12
- MA-1214
- N-DODECYL ALCOHOL
- NAA 42
- Nacol 12-96
- Pisol
- S 1298
- Sipol L12
- Siponol 25
- Siponol L2
- Siponol L5
- Undecyl carbinol
- n-Dodecan-1-ol
- n-Dodecanol
- n-Lauryl alcohol
- n-Lauryl alcohol, primary
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation 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.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-7950.00; -7909.40] | kJ/mol |
|
| ΔcH°liquid | -7950.00 ± 10.00 | kJ/mol | NIST |
| ΔcH°liquid | -7909.40 ± 0.80 | kJ/mol | NIST |
| μ | 1.60 | debye | KDB |
| ΔfG° | -87.13 | kJ/mol | KDB |
| ΔfH°gas | [-443.10; -436.50] | kJ/mol |
|
| ΔfH°gas | -443.10 | kJ/mol | KDB |
| ΔfH°gas | -436.50 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | -436.50 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -528.50 ± 0.80 | kJ/mol | NIST |
| ΔfusH° | [37.74; 90.80] | kJ/mol |
|
| ΔfusH° | 40.20 | kJ/mol | Solid-L... |
| ΔfusH° | 40.31 | kJ/mol | Heat ca... |
| ΔfusH° | 90.80 | kJ/mol | Evaluat... |
| ΔfusH° | 37.74 | kJ/mol | Measure... |
| ΔsubH° | 129.30 | kJ/mol | NIST |
| ΔvapH° | 58.98 | kJ/mol | Joback Calculated Property |
| log10WS | [-4.80; -4.67] |
|
|
| log10WS | -4.67 | Aq. Sol... | |
| log10WS | -4.80 | Estimat... | |
| logPoct/wat | 3.900 | Crippen Calculated Property | |
| McVol | 185.810 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| Pc | [1990.00; 1994.00] | kPa |
|
| Pc | 1994.00 | kPa | KDB |
| Pc | 1990.00 ± 50.00 | kPa | NIST |
| Pc | 1994.00 ± 50.00 | kPa | NIST |
| Pc | 1994.00 ± 50.00 | kPa | NIST |
| Ptriple | 9.60e-05 ± 2.70e-05 | kPa | NIST |
| Inp | [250.63; 1490.00] |
|
|
| Inp | 1455.10 | NIST | |
| Inp | 1463.10 | NIST | |
| Inp | 1456.60 | NIST | |
| Inp | 1461.00 | NIST | |
| Inp | 1477.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1473.00 | NIST | |
| Inp | 1448.00 | NIST | |
| Inp | 1451.00 | NIST | |
| Inp | 1451.00 | NIST | |
| Inp | 1450.00 | NIST | |
| Inp | 1449.00 | NIST | |
| Inp | 1442.00 | NIST | |
| Inp | 1458.00 | NIST | |
| Inp | 1432.00 | NIST | |
| Inp | 1453.00 | NIST | |
| Inp | 1458.00 | NIST | |
| Inp | 1471.00 | NIST | |
| Inp | 1435.00 | NIST | |
| Inp | 1473.00 | NIST | |
| Inp | 1457.00 | NIST | |
| Inp | 1459.00 | NIST | |
| Inp | 1463.00 | NIST | |
| Inp | 1465.00 | NIST | |
| Inp | 1471.00 | NIST | |
| Inp | 1469.00 | NIST | |
| Inp | 1466.00 | NIST | |
| Inp | 1474.00 | NIST | |
| Inp | 1457.10 | NIST | |
| Inp | 1460.00 | NIST | |
| Inp | 1474.00 | NIST | |
| Inp | 1473.00 | NIST | |
| Inp | 1468.90 | NIST | |
| Inp | 1473.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1473.00 | NIST | |
| Inp | 1460.00 | NIST | |
| Inp | 1460.00 | NIST | |
| Inp | 1487.00 | NIST | |
| Inp | 1456.50 | NIST | |
| Inp | 1456.80 | NIST | |
| Inp | 1442.00 | NIST | |
| Inp | 1443.00 | NIST | |
| Inp | 1473.00 | NIST | |
| Inp | 1478.20 | NIST | |
| Inp | 1482.80 | NIST | |
| Inp | 1486.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1456.00 | NIST | |
| Inp | 1462.00 | NIST | |
| Inp | 1471.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1477.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1474.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1430.00 | NIST | |
| Inp | 1464.00 | NIST | |
| Inp | 1451.00 | NIST | |
| Inp | 1474.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1458.00 | NIST | |
| Inp | 1473.00 | NIST | |
| Inp | 1466.00 | NIST | |
| Inp | 1466.00 | NIST | |
| Inp | 1466.00 | NIST | |
| Inp | 1466.00 | NIST | |
| Inp | 1479.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1478.00 | NIST | |
| Inp | 1465.00 | NIST | |
| Inp | 1457.00 | NIST | |
| Inp | 1460.00 | NIST | |
| Inp | 1461.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1462.00 | NIST | |
| Inp | 1458.00 | NIST | |
| Inp | 1462.00 | NIST | |
| Inp | 1488.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1469.00 | NIST | |
| Inp | 1477.00 | NIST | |
| Inp | 1479.00 | NIST | |
| Inp | 1483.00 | NIST | |
| Inp | 1484.00 | NIST | |
| Inp | 1484.00 | NIST | |
| Inp | 1474.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1457.00 | NIST | |
| Inp | 1484.00 | NIST | |
| Inp | 1487.00 | NIST | |
| Inp | 1474.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1471.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1480.00 | NIST | |
| Inp | 1485.00 | NIST | |
| Inp | 1471.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1465.00 | NIST | |
| Inp | 1458.00 | NIST | |
| Inp | 1460.00 | NIST | |
| Inp | Outlier 250.63 | NIST | |
| Inp | Outlier 252.06 | NIST | |
| Inp | Outlier 251.68 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1483.00 | NIST | |
| Inp | 1457.00 | NIST | |
| Inp | 1471.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1469.00 | NIST | |
| Inp | 1474.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1456.50 | NIST | |
| Inp | 1455.10 | NIST | |
| Inp | 1450.00 | NIST | |
| Inp | 1453.00 | NIST | |
| I | [1919.00; 1984.00] |
|
|
| I | 1935.00 | NIST | |
| I | 1942.00 | NIST | |
| I | Outlier 1924.00 | NIST | |
| I | 1962.00 | NIST | |
| I | 1957.00 | NIST | |
| I | 1960.00 | NIST | |
| I | 1960.00 | NIST | |
| I | 1979.00 | NIST | |
| I | 1950.00 | NIST | |
| I | 1940.00 | NIST | |
| I | 1980.00 | NIST | |
| I | 1943.00 | NIST | |
| I | 1952.00 | NIST | |
| I | Outlier 1925.00 | NIST | |
| I | Outlier 1925.00 | NIST | |
| I | 1940.00 | NIST | |
| I | 1970.00 | NIST | |
| I | 1961.00 | NIST | |
| I | 1981.00 | NIST | |
| I | 1970.00 | NIST | |
| I | 1930.00 | NIST | |
| I | 1970.00 | NIST | |
| I | 1981.00 | NIST | |
| I | 1977.00 | NIST | |
| I | 1977.00 | NIST | |
| I | 1948.00 | NIST | |
| I | 1962.00 | NIST | |
| I | 1977.00 | NIST | |
| I | 1977.00 | NIST | |
| I | 1975.00 | NIST | |
| I | 1950.00 | NIST | |
| I | 1950.00 | NIST | |
| I | Outlier 1920.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1957.00 | NIST | |
| I | 1964.00 | NIST | |
| I | 1969.00 | NIST | |
| I | 1955.00 | NIST | |
| I | 1953.00 | NIST | |
| I | 1983.00 | NIST | |
| I | 1968.00 | NIST | |
| I | 1963.00 | NIST | |
| I | 1956.00 | NIST | |
| I | 1956.00 | NIST | |
| I | 1959.00 | NIST | |
| I | 1961.00 | NIST | |
| I | 1956.00 | NIST | |
| I | 1977.00 | NIST | |
| I | 1953.00 | NIST | |
| I | 1969.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1961.00 | NIST | |
| I | Outlier 1919.00 | NIST | |
| I | 1946.00 | NIST | |
| I | Outlier 1920.00 | NIST | |
| I | Outlier 1925.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1977.00 | NIST | |
| I | 1983.00 | NIST | |
| I | 1984.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1957.00 | NIST | |
| I | 1981.00 | NIST | |
| I | 1981.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | Outlier 1925.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1974.00 | NIST | |
| I | 1947.00 | NIST | |
| I | 1950.00 | NIST | |
| I | 1983.00 | NIST | |
| I | 1935.00 | NIST | |
| I | 1960.00 | NIST | |
| I | 1980.00 | NIST | |
| I | Outlier 1925.00 | NIST | |
| I | 1953.00 | NIST | |
| I | 1956.00 | NIST | |
| I | 1946.00 | NIST | |
| I | 1973.00 | NIST | |
| I | 1950.00 | NIST | |
| Tboil | [532.00; 534.20] | K |
|
| Tboil | 532.00 | K | KDB |
| Tboil | 532.50 | K | (Liquid... |
| Tboil | 534.20 | K | NIST |
| Tc | [719.40; 719.40] | K |
|
| Tc | 719.40 | K | KDB |
| Tc | 719.40 ± 1.50 | K | NIST |
| Tc | 719.40 ± 0.80 | K | NIST |
| Tc | 719.40 ± 0.80 | K | NIST |
| Tc | 719.40 | K | NIST |
| Tfus | [296.15; 297.78] | K |
|
| Tfus | 297.00 | K | KDB |
| Tfus | 297.65 | K | Aq. Sol... |
| Tfus | 297.78 | K | Solid-l... |
| Tfus | 297.22 | K | Thermod... |
| Tfus | 296.15 | K | The man... |
| Tfus | 296.90 | K | High Pr... |
| Tfus | 296.51 | K | Solid-L... |
| Ttriple | 296.95 ± 0.50 | K | NIST |
| Vc | 0.718 | m3/kmol | KDB |
| Zc | 0.2393550 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [478.39; 557.99] | J/mol×K | [566.14; 723.91] |
|
| Cp,gas | 478.39 | J/mol×K | 566.14 | Joback Calculated Property |
| Cp,gas | 493.02 | J/mol×K | 592.43 | Joback Calculated Property |
| Cp,gas | 507.08 | J/mol×K | 618.73 | Joback Calculated Property |
| Cp,gas | 520.59 | J/mol×K | 645.02 | Joback Calculated Property |
| Cp,gas | 533.57 | J/mol×K | 671.32 | Joback Calculated Property |
| Cp,gas | 546.03 | J/mol×K | 697.61 | Joback Calculated Property |
| Cp,gas | 557.99 | J/mol×K | 723.91 | Joback Calculated Property |
| Cp,liquid | [438.42; 462.00] | J/mol×K | [298.15; 316.00] |
|
| Cp,liquid | 438.42 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 439.40 | J/mol×K | 303.15 | NIST |
| Cp,liquid | 462.00 | J/mol×K | 316.00 | NIST |
| η | [0.0000863; 0.0205746] | Pa×s | [285.82; 566.14] |
|
| η | 0.0205746 | Pa×s | 285.82 | Joback Calculated Property |
| η | 0.0043527 | Pa×s | 332.54 | Joback Calculated Property |
| η | 0.0013501 | Pa×s | 379.26 | Joback Calculated Property |
| η | 0.0005414 | Pa×s | 425.98 | Joback Calculated Property |
| η | 0.0002601 | Pa×s | 472.70 | Joback Calculated Property |
| η | 0.0001425 | Pa×s | 519.42 | Joback Calculated Property |
| η | 0.0000863 | Pa×s | 566.14 | Joback Calculated Property |
| ΔfusH | [40.17; 40.31] | kJ/mol | [297.30; 300.20] |
|
| ΔfusH | 40.31 | kJ/mol | 297.30 | NIST |
| ΔfusH | 40.17 | kJ/mol | 300.20 | NIST |
| ΔfusH | 40.17 | kJ/mol | 300.20 | NIST |
| ΔsubH | 130.10 ± 1.20 | kJ/mol | 289.50 | NIST |
| ΔvapH | [57.10; 95.40] | kJ/mol | [297.00; 533.10] |
|
| ΔvapH | 95.00 ± 2.00 | kJ/mol | 297.00 | NIST |
| ΔvapH | 95.40 | kJ/mol | 305.00 | NIST |
| ΔvapH | 85.80 | kJ/mol | 325.50 | NIST |
| ΔvapH | 92.50 | kJ/mol | 330.00 | NIST |
| ΔvapH | 83.30 | kJ/mol | 333.00 | NIST |
| ΔvapH | 84.70 ± 0.50 | kJ/mol | 343.00 | NIST |
| ΔvapH | 84.76 | kJ/mol | 343.15 | NIST |
| ΔvapH | 80.50 | kJ/mol | 358.00 | NIST |
| ΔvapH | 73.80 | kJ/mol | 410.50 | NIST |
| ΔvapH | 67.60 | kJ/mol | 449.00 | NIST |
| ΔvapH | 67.60 | kJ/mol | 449.00 | NIST |
| ΔvapH | 71.50 | kJ/mol | 469.00 | NIST |
| ΔvapH | 66.70 | kJ/mol | 487.50 | NIST |
| ΔvapH | 57.10 | kJ/mol | 527.50 | NIST |
| ΔvapH | 67.70 | kJ/mol | 533.10 | KDB |
| n0 | [1.39640; 1.44120] | [298.15; 298.20] |
|
|
| n0 | 1.44058 | 298.15 | Liquid ... | |
| n0 | 1.39640 | 298.20 | (Liquid... | |
| n0 | 1.44120 | 298.20 | Solubil... | |
| ρl | [802.10; 835.00] | kg/m3 | [293.00; 338.15] |
|
| ρl | 835.00 | kg/m3 | 293.00 | KDB |
| ρl | 830.37 | kg/m3 | 298.15 | Liquid-... |
| ρl | 823.35 | kg/m3 | 298.15 | Phase b... |
| ρl | 829.60 | kg/m3 | 298.15 | Viscosi... |
| ρl | 830.90 | kg/m3 | 298.15 | Solid L... |
| ρl | 822.80 | kg/m3 | 308.15 | Viscosi... |
| ρl | 816.00 | kg/m3 | 318.15 | Viscosi... |
| ρl | 809.10 | kg/m3 | 328.15 | Viscosi... |
| ρl | 802.10 | kg/m3 | 338.15 | Viscosi... |
| ΔvapS | 246.74 | J/mol×K | 343.15 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [416.56; 561.39] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.66246e+01 | |||
| Coefficient B | -5.32811e+03 | |||
| Coefficient C | -9.04220e+01 | |||
| Temperature range, min. | 416.56 | |||
| Temperature range, max. | 561.39 | |||
| Pvap | 1.33 | kPa | 416.56 | Calculated Property |
| Pvap | 2.87 | kPa | 432.65 | Calculated Property |
| Pvap | 5.78 | kPa | 448.74 | Calculated Property |
| Pvap | 10.96 | kPa | 464.84 | Calculated Property |
| Pvap | 19.70 | kPa | 480.93 | Calculated Property |
| Pvap | 33.80 | kPa | 497.02 | Calculated Property |
| Pvap | 55.67 | kPa | 513.11 | Calculated Property |
| Pvap | 88.38 | kPa | 529.21 | Calculated Property |
| Pvap | 135.81 | kPa | 545.30 | Calculated Property |
| Pvap | 202.65 | kPa | 561.39 | Calculated Property |
| Pvap | [9.08e-05; 1905.88] | kPa | [296.95; 721.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.84704e+02 | |||
| Coefficient B | -2.24029e+04 | |||
| Coefficient C | -3.86309e+01 | |||
| Coefficient D | 1.56516e-05 | |||
| Temperature range, min. | 296.95 | |||
| Temperature range, max. | 721.00 | |||
| Pvap | 9.08e-05 | kPa | 296.95 | Calculated Property |
| Pvap | 0.02 | kPa | 344.07 | Calculated Property |
| Pvap | 0.47 | kPa | 391.18 | Calculated Property |
| Pvap | 5.00 | kPa | 438.30 | Calculated Property |
| Pvap | 27.33 | kPa | 485.42 | Calculated Property |
| Pvap | 95.91 | kPa | 532.53 | Calculated Property |
| Pvap | 251.64 | kPa | 579.65 | Calculated Property |
| Pvap | 546.80 | kPa | 626.77 | Calculated Property |
| Pvap | 1056.06 | kPa | 673.88 | Calculated Property |
| Pvap | 1905.88 | kPa | 721.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Dodecanol.
Mixtures
- 1-Dodecanol + Tributyl phosphate
- 1-Dodecanol + 1-Octanamine, N,N-dioctyl-
- 1-Dodecanol + Tripalmitin
- 1-Dodecanol + Butanoic acid + Water
- 1-Dodecanol + Propanoic acid + Water
- 1-Dodecanol + Quinoline
- 1-Dodecanol + Water
- 1-Dodecanol + 1-Octadecanol
- 1-Dodecanol + 1-Hexadecanol
- 1-Dodecanol + 1-Tetradecanol
- 1-Dodecanol + 1-Hexanol
- 1-Dodecanol + 1-Octanol
- 1-Dodecanol + 1-Decanol
- 1-Undecanol + 1-Dodecanol
- 1-Dodecanol + Dodecanoic acid
- 1-Dodecanol + n-Decanoic acid
- 1-Dodecanol + n-Hexadecanoic acid
- 1-Dodecanol + 1,4-Butanediol
- 1-Dodecanol + 2-Heptanone
- 2-Nonanone + 1-Dodecanol
Find more mixtures with 1-Dodecanol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- The influence of temperature on the liquid liquid solid equilibria of the ternary system water + ethanol + 1-dodecanol
- Phase equilibria of high molecular mass 1-alcohols in supercritical propane
- (Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
- The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
- Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
- Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
- Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
- Phase behavior of the carbon dioxide p 1-dodecanol system at high pressures
- Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
- (Liquid + liquid) equilibria of the (water + butyric acid + dodecanol) ternary system
- (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
- Thermodynamics of organic mixtures containing amines. VIII. Systems with quinoline
- Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
- Thermophysical properties and thermodynamic phase behavior of ionic liquids
- Solubility and Tie Line Data of the Water - Phosphoric Acid Solvents at T = (303.2 and 313.2) K: An Experimental and Correlational Study
- The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
- High Pressure Solid-Liquid Equilibrium of Fatty Alcohols Binary Systems from 1-Dodecanol, 1-Tetradecanol, 1-Hexadecanol, and 1-Octadecanol
- Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
- High Pressure Phase Behavior of the Homologous Series CO2 + 1-Alcohols
- Liquid-Liquid Equilibria of Lactic Acid/Water Solutions in Tri-iso-octylamine/Dodecane/1-Dodecanol at 306.1, 310.1, and 316.1 K. Experimental Data and Prediction
- Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
- Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
- Liquid Viscosity and Interfacial Tension of Binary and Ternary Mixtures Containing n-Octacosane by Surface Light Scattering
- Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
- Experimental Measurement and Thermodynamic Model of Liquid-Liquid Equilibrium for the Ternary System of 1-Dodecanol-Phenol-Water
- Heat capacities and derived thermodynamic functions of 1-dodecanol and 1-tridecanol between 10 K and 370 K and heat capacities of 1-pentadecanol and 1-heptadecanol between 300 K and 380 K and correlationos for the heat capacity and the entropy of liquid n-alcohols
- Density-Pressure Relationship in Hydrogen-Bonded Mixtures: 1,4-Butanediol + 1-Dodecanol
- Evaluation of the Vaporization, Fusion, and Sublimation Enthalpies of the 1-Alkanols: The Vaporization Enthalpy of 1-, 6-, 7-, and 9-Heptadecanol, 1-Octadecanol, 1-Eicosanol, 1-Docosanol, 1-Hexacosanol, and Cholesterol at T ) 298.15 K by Correlation Gas Chromatography
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Vapor-Liquid Equilibria of Binary Systems of Ethene Oxide + Dodecane, Ethene Oxide + 1-Decanol, and Ethene Oxide + 1-Dodecanol and Prediction with the Predictive Soave-Redlich-Kwong (PSRK) Equation of State
- Liquid-Liquid Phase Behavior of Solutions of 1-Dodecyl-3-methylimidazolium Bis(trifluoromethylsulphonyl)imide (C12mimNTf2) in n- Alkyl Alcohols
- Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
- Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
- Solid-Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate
- Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
- Solid Liquid Equilibria, Excess Molar Volumes, and Deviations in the Molar Refractivity for the Binary Systems of Alamine 304-1 + Decane, Dodecane, or Dodecanol
- Solubility Determination and Correlation of (2R,3S,4S,5S)-6-(Hydroxymethyl)-tetrahydro-2H-pyran-2,3,4, 5-tetraol in Fatty Alcohol
- Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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