- InChI
- InChI=1S/C6H14O2/c1-2-3-5-8-6-4-7/h7H,2-6H2,1H3
- InChI Key
- POAOYUHQDCAZBD-UHFFFAOYSA-N
- Formula
- C6H14O2
- SMILES
- CCCCOCCO
- Molecular Weight1
- 118.17
- CAS
- 111-76-2
- Other Names
-
- .beta.-butoxyethanol
- 1,2-ethanediol, butyl ether
- 1,2-ethanediol, monobutyl ether
- 2-Butossi-etanolo
- 2-Butoxy-aethanol
- 2-Hydroxyethyl n-butyl ether
- 2-butoxy-1-ethanol
- 2-butoxyethan-1-ol
- 2-butoxyethanol
- 2-butoxyethanol (butyl cellosolve)
- 2-n-Butoxy-1-ethanol
- 2-n-butoxyethanol
- 3-oxa-1-heptanol
- BuCs
- Butoksyetylowy alkohol
- Butoxyethanol
- Butyglycol
- Butyl 2-hydroxyethyl ether
- Butyl Cellu-Sol
- Butyl icinol
- Butyl monoether glycol
- Butyl oxitol
- Butylcelosolv
- Chimec NR
- Dowanol EB
- EGBE
- Ektasolve EB
- Ektasolve EB solvent
- Ether alcohol
- Gafcol EB
- Glycol ether EB
- Glycol ether eb acetate
- Jeffersol EB
- Minex BDH
- Monobutyl ether of ethylene glycol
- NSC 60759
- O-Butyl ethylene glycol
- Poly-Solv EB
- UN 2369
- butyl cellosolve
- butyl glycol
- ethylene glycol butyl ether
- ethylene glycol mono-n-butyl ether
- ethylene glycol monobutyl ether
- ethylene glycol n-butyl ether
- glycol butyl ether
- glycol monobutyl ether
- monobutyl glycol ether
- n-Butoxyethanol
- n-butyl cellosolve
- «beta»-Butoxyethanol
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- εr : Dielectric Constant (Relative permittivity).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (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 |
|---|---|---|---|
| ω | 0.5114 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| εr | 9.30 | NCMS SOLV-DB | |
| Tflash,cc | 334.15 | K | NCMS SOLV-DB |
| ΔfG° | -242.18 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -466.82 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 16.57 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [56.59; 56.61] | kJ/mol |
|
| ΔvapH° | 56.61 | kJ/mol | NCMS SOLV-DB |
| ΔvapH° | 56.59 | kJ/mol | NIST |
| IE | 9.86 | eV | Relay (1.0) Calculated Property |
| log10WS | [-0.42; -0.42] |
|
|
| log10WS | -0.42 | Aq. Solubility Prediction | |
| log10WS | -0.42 | Estimated Solubility | |
| logPoct/wat | 0.830 | NCMS SOLV-DB | |
| McVol | 107.140 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | NCMS SOLV-DB | |
| NFPA Health | 2 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | [3269.76; 3270.00] | kPa |
|
| Pc | 3270.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 3269.76 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3270.00 ± 20.00 | kPa | NIST |
| ρc | 278.89 ± 5.91 | kg/m3 | NIST |
| Inp | [884.40; 936.00] |
|
|
| Inp | 888.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 898.60 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 884.40 | NIST | |
| Inp | 904.50 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 911.60 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 899.00 | NIST | |
| Inp | 909.30 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | Outlier 936.00 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 904.50 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 909.30 | NIST | |
| Inp | 911.60 | NIST | |
| Ip | [1361.00; 1455.00] |
|
|
| Ip | 1416.00 | NIST | |
| Ip | 1403.00 | NIST | |
| Ip | 1391.00 | NIST | |
| Ip | 1405.00 | NIST | |
| Ip | 1389.00 | NIST | |
| Ip | Outlier 1361.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1392.00 | NIST | |
| Ip | 1426.00 | NIST | |
| Ip | 1391.00 | NIST | |
| Ip | 1429.70 | NIST | |
| Ip | Outlier 1447.00 | NIST | |
| Ip | 1404.00 | NIST | |
| Ip | 1413.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1404.00 | NIST | |
| Ip | 1379.00 | NIST | |
| Ip | 1411.00 | NIST | |
| Ip | 1411.00 | NIST | |
| Ip | 1405.00 | NIST | |
| Ip | 1410.00 | NIST | |
| Ip | 1406.00 | NIST | |
| Ip | 1406.00 | NIST | |
| Ip | 1435.00 | NIST | |
| Ip | 1430.00 | NIST | |
| Ip | 1399.00 | NIST | |
| Ip | 1402.00 | NIST | |
| Ip | Outlier 1455.00 | NIST | |
| Ip | 1407.00 | NIST | |
| Ip | 1441.00 | NIST | |
| Ip | 1371.00 | NIST | |
| Ip | 1379.00 | NIST | |
| Ip | 1385.00 | NIST | |
| Ip | 1397.00 | NIST | |
| Ip | 1418.00 | NIST | |
| Ip | 1419.00 | NIST | |
| Ip | 1402.00 | NIST | |
| Ip | 1404.00 | NIST | |
| Ip | 1371.00 | NIST | |
| Ip | 1433.00 | NIST | |
| Ip | 1391.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1408.00 | NIST | |
| Ip | 1416.00 | NIST | |
| Ip | 1403.00 | NIST | |
| Ip | 1405.00 | NIST | |
| Ip | 1426.00 | NIST | |
| Ip | 1413.00 | NIST | |
| Ip | 1411.00 | NIST | |
| Ip | 1407.00 | NIST | |
| Ip | 1397.00 | NIST | |
| Ip | 1371.00 | NIST | |
| Ip | 1391.00 | NIST | |
| Ip | 1406.00 | NIST | |
| Ip | 1402.00 | NIST | |
| Tboil | [442.60; 444.35] | K |
|
| Tboil | 443.35 | K | NCMS SOLV-DB |
| Tboil | 444.20 | K | NIST |
| Tboil | 444.35 | K | NIST |
| Tboil | 444.30 ± 0.70 | K | NIST |
| Tboil | 442.60 ± 0.50 | K | NIST |
| Tc | [633.90; 634.00] | K |
|
| Tc | 634.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 633.90 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 633.90 ± 1.00 | K | NIST |
| Tc | 633.90 ± 1.20 | K | NIST |
| Tfus | [196.88; 202.75] | K |
|
| Tfus | 198.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 196.88 | K | Aq. Solubility Prediction |
| Tfus | 198.15 | K | NCMS SOLV-DB |
| Tfus | 202.75 | K | NIST |
| Vc | [0.424; 0.424] | m3/kmol |
|
| Vc | 0.424 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Vc | 0.424 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Zc | 0.2630000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 444.20 | K | 99.10 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 907.9 |
| 283.15 | 1000.00 | 908.3 |
| 283.15 | 3000.00 | 909.9 |
| 283.15 | 5000.00 | 911.0 |
| 283.15 | 10000.00 | 914.2 |
| 283.15 | 15000.00 | 917.1 |
| 283.15 | 20000.00 | 920.0 |
| 283.15 | 25000.00 | 922.8 |
| 283.15 | 30000.00 | 925.6 |
| 283.15 | 35000.00 | 928.4 |
| 283.15 | 40000.00 | 930.9 |
| 283.15 | 50000.00 | 935.7 |
| 283.15 | 60000.00 | 940.5 |
| 293.15 | 100.00 | 900.5 |
| 293.15 | 1000.00 | 900.6 |
| 293.15 | 3000.00 | 902.2 |
| 293.15 | 5000.00 | 903.2 |
| 293.15 | 10000.00 | 906.8 |
| 293.15 | 15000.00 | 910.0 |
| 293.15 | 20000.00 | 912.9 |
| 293.15 | 25000.00 | 915.9 |
| 293.15 | 30000.00 | 918.8 |
| 293.15 | 35000.00 | 921.4 |
| 293.15 | 40000.00 | 924.0 |
| 293.15 | 50000.00 | 929.5 |
| 293.15 | 60000.00 | 933.9 |
| 303.15 | 100.00 | 891.8 |
| 303.15 | 1000.00 | 892.1 |
| 303.15 | 3000.00 | 893.9 |
| 303.15 | 5000.00 | 895.4 |
| 303.15 | 10000.00 | 898.9 |
| 303.15 | 15000.00 | 902.0 |
| 303.15 | 20000.00 | 905.5 |
| 303.15 | 25000.00 | 908.7 |
| 303.15 | 30000.00 | 911.8 |
| 303.15 | 35000.00 | 914.5 |
| 303.15 | 40000.00 | 916.7 |
| 303.15 | 50000.00 | 921.8 |
| 303.15 | 60000.00 | 927.1 |
| 313.15 | 100.00 | 883.5 |
| 313.15 | 1000.00 | 884.0 |
| 313.15 | 3000.00 | 885.6 |
| 313.15 | 5000.00 | 887.1 |
| 313.15 | 10000.00 | 890.7 |
| 313.15 | 15000.00 | 894.1 |
| 313.15 | 20000.00 | 897.3 |
| 313.15 | 25000.00 | 900.7 |
| 313.15 | 30000.00 | 903.6 |
| 313.15 | 35000.00 | 906.7 |
| 313.15 | 40000.00 | 909.4 |
| 313.15 | 50000.00 | 915.1 |
| 313.15 | 60000.00 | 920.1 |
| 323.15 | 100.00 | 874.0 |
| 323.15 | 1000.00 | 875.0 |
| 323.15 | 3000.00 | 876.5 |
| 323.15 | 5000.00 | 878.1 |
| 323.15 | 10000.00 | 881.9 |
| 323.15 | 15000.00 | 885.5 |
| 323.15 | 20000.00 | 889.1 |
| 323.15 | 25000.00 | 892.1 |
| 323.15 | 30000.00 | 895.4 |
| 323.15 | 35000.00 | 898.5 |
| 323.15 | 40000.00 | 901.6 |
| 323.15 | 50000.00 | 907.3 |
| 323.15 | 60000.00 | 912.9 |
| 333.15 | 100.00 | 865.6 |
| 333.15 | 1000.00 | 866.1 |
| 333.15 | 3000.00 | 868.0 |
| 333.15 | 5000.00 | 869.5 |
| 333.15 | 10000.00 | 873.5 |
| 333.15 | 15000.00 | 877.3 |
| 333.15 | 20000.00 | 880.9 |
| 333.15 | 25000.00 | 884.4 |
| 333.15 | 30000.00 | 887.6 |
| 333.15 | 35000.00 | 890.8 |
| 333.15 | 40000.00 | 894.0 |
| 333.15 | 50000.00 | 900.1 |
| 333.15 | 60000.00 | 905.7 |
| 343.15 | 100.00 | 856.5 |
| 343.15 | 1000.00 | 857.4 |
| 343.15 | 3000.00 | 859.3 |
| 343.15 | 5000.00 | 861.1 |
| 343.15 | 10000.00 | 865.1 |
| 343.15 | 15000.00 | 869.1 |
| 343.15 | 20000.00 | 873.2 |
| 343.15 | 25000.00 | 876.5 |
| 343.15 | 30000.00 | 880.1 |
| 343.15 | 35000.00 | 883.5 |
| 343.15 | 40000.00 | 886.7 |
| 343.15 | 50000.00 | 893.0 |
| 343.15 | 60000.00 | 898.6 |
| 353.15 | 100.00 | 847.5 |
| 353.15 | 1000.00 | 848.4 |
| 353.15 | 3000.00 | 850.5 |
| 353.15 | 5000.00 | 852.2 |
| 353.15 | 10000.00 | 856.7 |
| 353.15 | 15000.00 | 860.9 |
| 353.15 | 20000.00 | 864.8 |
| 353.15 | 25000.00 | 868.7 |
| 353.15 | 30000.00 | 872.3 |
| 353.15 | 35000.00 | 875.9 |
| 353.15 | 40000.00 | 879.2 |
| 353.15 | 50000.00 | 885.6 |
| 353.15 | 60000.00 | 891.8 |
| 363.15 | 100.00 | 838.2 |
| 363.15 | 1000.00 | 839.4 |
| 363.15 | 3000.00 | 841.4 |
| 363.15 | 5000.00 | 843.4 |
| 363.15 | 10000.00 | 847.9 |
| 363.15 | 15000.00 | 852.6 |
| 363.15 | 20000.00 | 856.4 |
| 363.15 | 25000.00 | 860.4 |
| 363.15 | 30000.00 | 864.4 |
| 363.15 | 35000.00 | 868.1 |
| 363.15 | 40000.00 | 871.8 |
| 363.15 | 50000.00 | 878.4 |
| 363.15 | 60000.00 | 884.8 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Thermal conductivity, W/m/K - Liquid |
| 304.15 | 100.00 | 0.1529 |
| 304.15 | 16400.00 | 0.1579 |
| 304.15 | 27300.00 | 0.1612 |
| 304.15 | 41800.00 | 0.1646 |
| 304.15 | 56100.00 | 0.1689 |
| 304.15 | 70200.00 | 0.1722 |
| 304.15 | 79000.00 | 0.1740 |
| 304.15 | 83500.00 | 0.1749 |
| 304.15 | 98200.00 | 0.1785 |
| 304.15 | 112200.00 | 0.1820 |
| 304.15 | 124100.00 | 0.1836 |
| 304.15 | 140100.00 | 0.1870 |
| 304.15 | 149200.00 | 0.1885 |
| 304.15 | 100.00 | 0.1533 |
| 321.15 | 100.00 | 0.1497 |
| 321.15 | 16400.00 | 0.1548 |
| 321.15 | 27300.00 | 0.1585 |
| 321.15 | 41800.00 | 0.1628 |
| 321.15 | 56100.00 | 0.1665 |
| 321.15 | 70200.00 | 0.1701 |
| 321.15 | 84200.00 | 0.1739 |
| 321.15 | 98200.00 | 0.1770 |
| 321.15 | 112200.00 | 0.1800 |
| 321.15 | 126200.00 | 0.1830 |
| 321.15 | 134900.00 | 0.1851 |
| 321.15 | 150600.00 | 0.1879 |
| 321.15 | 100.00 | 0.1496 |
| 338.15 | 100.00 | 0.1461 |
| 338.15 | 16400.00 | 0.1518 |
| 338.15 | 27300.00 | 0.1555 |
| 338.15 | 41800.00 | 0.1601 |
| 338.15 | 56100.00 | 0.1640 |
| 338.15 | 70200.00 | 0.1677 |
| 338.15 | 84200.00 | 0.1717 |
| 338.15 | 98200.00 | 0.1751 |
| 338.15 | 108700.00 | 0.1775 |
| 338.15 | 123400.00 | 0.1807 |
| 338.15 | 140100.00 | 0.1844 |
| 338.15 | 100.00 | 0.1463 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [160.67; 366.05] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.82250e+01 | |||
| Coefficient B | 5.44620e-01 | |||
| Coefficient C | -2.22000e-04 | |||
| Coefficient D | 1.52000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 160.67 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 193.79 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 224.22 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 252.01 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 277.21 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 299.87 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 320.04 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 337.75 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 353.07 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 366.05 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [341.68; 468.10] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.63176e+01 | |||
| Coefficient B | -4.43972e+03 | |||
| Coefficient C | -6.47130e+01 | |||
| Temperature range, min. | 341.68 | |||
| Temperature range, max. | 468.10 | |||
| Pvap | 1.33 | kPa | 341.68 | Calculated Property |
| Pvap | 2.89 | kPa | 355.73 | Calculated Property |
| Pvap | 5.84 | kPa | 369.77 | Calculated Property |
| Pvap | 11.07 | kPa | 383.82 | Calculated Property |
| Pvap | 19.91 | kPa | 397.87 | Calculated Property |
| Pvap | 34.14 | kPa | 411.91 | Calculated Property |
| Pvap | 56.13 | kPa | 425.96 | Calculated Property |
| Pvap | 88.91 | kPa | 440.01 | Calculated Property |
| Pvap | 136.24 | kPa | 454.05 | Calculated Property |
| Pvap | 202.65 | kPa | 468.10 | Calculated Property |
| Pvap | [6.30; 98.58] | kPa | [365.80; 443.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44056e+01 | |||
| Coefficient B | -3.48016e+03 | |||
| Coefficient C | -8.88150e+01 | |||
| Reference | Dykyj, Seprakova, et al., 1957 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 365.80 | |||
| Temperature range, max. | 443.40 | |||
| Pvap | 6.30 | kPa | 365.80 | Calculated Property |
| Pvap | 9.21 | kPa | 374.42 | Calculated Property |
| Pvap | 13.16 | kPa | 383.04 | Calculated Property |
| Pvap | 18.44 | kPa | 391.67 | Calculated Property |
| Pvap | 25.34 | kPa | 400.29 | Calculated Property |
| Pvap | 34.24 | kPa | 408.91 | Calculated Property |
| Pvap | 45.54 | kPa | 417.53 | Calculated Property |
| Pvap | 59.69 | kPa | 426.16 | Calculated Property |
| Pvap | 77.19 | kPa | 434.78 | Calculated Property |
| Pvap | 98.58 | kPa | 443.40 | Calculated Property |
| Pvap | [6.30; 98.58] | kPa | [365.80; 443.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44056e+01 | |||
| Coefficient B | -3.48016e+03 | |||
| Coefficient C | -8.88150e+01 | |||
| Reference | Dykyj, Seprakova, et al., 1957, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 365.80 | |||
| Temperature range, max. | 443.40 | |||
| Pvap | 6.30 | kPa | 365.80 | Calculated Property |
| Pvap | 9.21 | kPa | 374.42 | Calculated Property |
| Pvap | 13.16 | kPa | 383.04 | Calculated Property |
| Pvap | 18.44 | kPa | 391.67 | Calculated Property |
| Pvap | 25.34 | kPa | 400.29 | Calculated Property |
| Pvap | 34.24 | kPa | 408.91 | Calculated Property |
| Pvap | 45.54 | kPa | 417.53 | Calculated Property |
| Pvap | 59.69 | kPa | 426.16 | Calculated Property |
| Pvap | 77.19 | kPa | 434.78 | Calculated Property |
| Pvap | 98.58 | kPa | 443.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.01] | N/m | [198.15; 441.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 5.04690e-02 | |||
| Coefficient B | -8.16000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 198.15 | |||
| Temperature range, max. | 441.15 | |||
| γ | 0.03 | N/m | 198.15 | Calculated Property |
| γ | 0.03 | N/m | 225.15 | Calculated Property |
| γ | 0.03 | N/m | 252.15 | Calculated Property |
| γ | 0.03 | N/m | 279.15 | Calculated Property |
| γ | 0.03 | N/m | 306.15 | Calculated Property |
| γ | 0.02 | N/m | 333.15 | Calculated Property |
| γ | 0.02 | N/m | 360.15 | Calculated Property |
| γ | 0.02 | N/m | 387.15 | Calculated Property |
| γ | 0.02 | N/m | 414.15 | Calculated Property |
| γ | 0.01 | N/m | 441.15 | Calculated Property |
Similar Compounds
![Ethanol, 2-[2-(2-butoxyethoxy)ethoxy]-.](data:image/png;base64,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)
![Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-.](data:image/png;base64,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)
![2-[2-(2-Pentoxyethoxy)ethoxy]ethanol.](data:image/png;base64,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)
Find more compounds similar to Ethanol, 2-butoxy-.
Mixtures
- n-Hexane + Ethanol, 2-butoxy-
- Ethanol, 2-butoxy- + Heptane
- Ethanol, 2-butoxy- + Methane, nitro-
- Ethanol, 2-butoxy- + 1-Hexanol
- Ethanol, 2-butoxy- + 1-Octanol
- Ethanol, 2-butoxy- + 1-Decanol
- Ethanol, 2-butoxy- + Benzyl alcohol
- Ethanol, 2-butoxy- + Glycine + Water
- 1-Propanol + Ethanol, 2-butoxy-
- Ethanol, 2-butoxy- + 2-Propanol
- Ethanol, 2-butoxy- + 1-Butanol
- Ethanol, 2-butoxy- + Decane + Water
- Ethanol, 2-butoxy- + LACTIC ACID, ETHYL ESTER
- Ethanol, 2-butoxy- + Octane + Water
- Ethanol, 2-butoxy- + Methyl Alcohol
- Ethanol, 2-butoxy- + Ethanol
- Ethanol, 2-butoxy- + Water
- Ethanol, 2-butoxy- + 2-Pyrrolidinone, 1-methyl-
- Ethanol, 2-butoxy- + 1-Butanol, 3-methyl-
- Ethanol, 2-butoxy- + Tetramethylammonium bromide + Water
Find more mixtures with Ethanol, 2-butoxy-.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- Densities, Viscosities, Sound Speeds, Refractive Indices, and Excess Properties of Binary Mixtures of Isoamyl Alcohol with Some Alkoxyethanols
- Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
- Thermodynamic and spectral investigations of binary liquid mixturesof 2-butoxy ethanol with alcohols at temperature range of 293.15-313.15 K
- Liquid liquid equilibria for the ternary system water + octane + 2-butyloxy-ethanol
- Phase behavior of glycol ether surfactant systems in the presence of brine and hydrocarbon: Experiment and modeling
- Solubility of disodium 4,4'-dinitrobibenzyl-2,2'-disulfonate in aqueous organic solutions and its effects on the oxidation reaction of DSD acid synthesis
- Thermodynamic properties and sPC-SAFT modeling of 2-ethoxyethanol, 2-propoxyethanol and 2-butoxyethanol from T = (293.15-413.15) K and pressure up to 30 MPa
- Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
- Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
- Thermodynamic and physicochemical properties of binary mixtures of nitromethane with {2-methoxyethanol + 2-butoxyethanol} systems at T = (293.15, 298.15, 303.15, 308.15, and 313.15) K
- Effect of hydrophilic additives on volumetric and viscosity properties of amino acids in aqueous solutions at T = (283.15 to 333.15) K
- Studies on intermolecular interactions in nitrobenzene + alkoxyethanol binary mixtures by relative permittivity measurements at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
- Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
- Group-contribution to limiting partial molar isentropic compressions of small amphiphile molecules in water. The temperature effect
- Solubility of disodium 4,4'-dinitrostilbene-2,2'-disulfonate and sodium 4-nitrotoluene-2-sulfonate in aqueous organic solutions and its application feasibility in oxidation stage of DSD acid synthesis
- FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
- Experimental study on the calorimetric data of 2-butoxyethanol with aliphatic alcohols (C1-C4) and correlation with the Wilson, NRTL and UNIQUAC models at T = 298 K
- Partial molar volumes of organic solutes in water. XXIX. Four 2-alkoxyethanols at temperatures T = (298 K to 573) K and pressures up to 30 MPa
- Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
- Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
- Densities of Diethylene Glycol, Monobutyl Ether, Diethylene Glycol Dibutyl Ether, and Ethylene Glycol Monobutyl Ether from (283.15 to 363.15) K at Pressures up to 60 MPa
- Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
- Partial Molar Volumes and Partial Molar Isentropic Compressions of Four 2-Alkoxyethanols at Infinite Dilution in Water at Temperatures T = 278 343 K and Atmospheric Pressure
- Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
- Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
- Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
- Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
- Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
- Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
- Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
- Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
- Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
- Conductance Studies of NaCl, KCl, NaBr, NaI, NaBPh4, Bu4NI, and NaClO4 in Water + 2-Butoxyethanol Mixtures at T = 298.15 K
- Thermal Conductivity of Aqueous Mixtures of 2-n-Butoxyethanol at Pressures up to 150 MPa
- Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
- Conductance Studies of Tetrabutylammonium Bromide, Sodium Bromide, and Sodium Tetraphenylborate in 2-Butoxyethanol (1) + Water (2) Mixtures at (298.15, 303.15, 308.15, and 313.15) K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Electrical Conductance of Some Tetraalkylammonium Bromide Salts in 2-Butoxyethanol (1) + Water (2) mixtures at (298.15, 303.15, 308.15, and 313.15) K
- Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
- Density, Viscosity, Refractive Index, and Ultrasonic Speed of Binary Mixtures of 1,3-Dioxolane with 2-Methoxyethanol, 2-Ethoxyethanol, 2-Butoxyethanol, 2-Propylamine, and Cyclohexylamine
- Density, Viscosity, and Refractive Index for Water + 2-Butoxyethanol and + 2-(2-Butoxyethoxy)ethanol at Various Temperatures
- Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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